MM "12.1" FLAVOR "NO" VERSION "12.1" DATETIME "Wed Feb 22 11:01:53 2006" MACHINE "WIN-NT/VC" ; startlibrary version1 NumLibs = 1 Built-In NumCats = 9 Mixers/Splitters active Separators active Heat Exchangers active Columns active Reactors active Pressure Changers active Manipulators active Solids active User Models active endlibrary ; 175 >VERSION 0 C103A Sep Built-In SEP >VERSION 0 C103B FSplit Built-In FSPLIT >VERSION 0 C103C Mixer Built-In MIXER >VERSION 0 M104LOSS FSplit Built-In FSPLIT >VERSION 0 M104MIX Mixer Built-In MIXER >VERSION 0 MPOW1 Mixer Built-In MIXER >VERSION 0 A201 Mixer Built-In MIXER >VERSION 0 M202MIX Mixer Built-In MIXER >VERSION 0 M202LO Heater Built-In HEATER >VERSION 0 M202HI RStoic Built-In RSTOIC >VERSION 0 T203 Flash2 Built-In FLASH2 >VERSION 0 S205SPT FSplit Built-In FSPLIT >VERSION 0 S205A SSplit Built-In SSPLIT >VERSION 0 S205MIX Mixer Built-In MIXER >VERSION 0 S205B Sep Built-In SEP >VERSION 0 M205 Compr Built-In COMPR >VERSION 0 M205COOL Heater Built-In 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>VERSION 0 CHCWMIX Mixer Built-In MIXER >VERSION 0 H914 Heater Built-In HEATER >VERSION 0 T914 Mixer Built-In MIXER >VERSION 0 H910 Heater Built-In HEATER >VERSION 0 CIPCS Mixer Built-In MIXER >VERSION 0 MPOW10 Mixer Built-In MIXER >VERSION 0 AIRCMP Mixer Built-In MIXER >VERSION 0 MPOWTOT Mixer Built-In MIXER >VERSION 0 WKSEP Mixer Built-In MIXER ? SETUP MAIN ? \ TITLE TITLE = "BIOMASS TO ETHANOL PROCESS: TOTAL PLANT **NREL PROTECTED INFO**" \ \ SIMULATE INTERACTIVE = NO MOLEFLOW = NOMOLEFLOW MASSFLOW = MASSFLOW PROPERTIES = ( CP1 CP2 FRAC COMP1 COMP2 ) VISITED = 1 \ \ COMMENTS COMMENTS = ( ";***************************************************************************" ";***************************************************************************" ";** NREL PROTECTED INFORMATION" ";***************************************************************************" ";***************************************************************************" ";;" ) \ ? SETUP GLOBAL ? \ "IN-UNITS" INSET = SET1 OUTSET = SET2 \ \ "STREAM-CLASS" SCLASS = MIXCISLD \ \ COMMENTS COMMENTS = ( ";;" ) \ ? SETUP DIAGNOSTICS ? \ "MSG-LEVEL" SYS-LEVEL = 4 SIM-LEVEL = 4 PROP-LEVEL = 2 STREAM-LEVEL = 4 \ \ "MAX-PRINT" SIM-LIMIT = 1000 \ ? SETUP "SIM-OPTIONS" ? ; "SET1_MOLE" ; \ "SIM-OPTIONS" PROP-DERIV = NUMERICAL \ \ COMMENTS COMMENTS = ( ";;" ) \ ? SETUP "UNITS-SET" SET1 ? \ DESCRIPTION DESCRIPTION = "User-defined units set based on SI" \ \ MMLOCAL \ \ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 4 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \ ? SETUP "UNITS-SET" SET2 ? \ DESCRIPTION DESCRIPTION = "User-defined units set based on SI" \ \ MMLOCAL \ \ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 3 7 3 3 3 3 3 3 3 3 4 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 4 3 4 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \ ? SETUP "UNITS-SET" SET3 ? \ DESCRIPTION DESCRIPTION = "User-defined units set based on SI" \ \ MMLOCAL \ \ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 7 7 3 3 5 3 3 3 5 3 4 3 3 3 3 1 3 3 3 4 3 7 3 3 3 1 1 4 4 3 3 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3 3 3 3 3 3 4 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \ ? SETUP "UNITS-SET" SET4 ? \ DESCRIPTION DESCRIPTION = "User-defined units set based on SI" \ \ MMLOCAL \ \ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 4 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 1 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \ ? SETUP "UNITS-SET" SET5 ? \ DESCRIPTION DESCRIPTION = "User-defined units set based on SI" \ \ MMLOCAL \ \ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 5 3 4 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \ ? SETUP "UNITS-SET" SET6 ? \ DESCRIPTION DESCRIPTION = "User-defined units set based on SI" \ \ MMLOCAL \ \ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 3 7 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \ ? SETUP "SYS-OPTIONS" ? \ "SYS-OPTIONS" INTERPRET = NO \ ? SETUP "ACCOUNT-INFO" ? ? SETUP "RUN-CONTROL" ? \ PARAMETER MAX-TIME = 20000.0 <0> <0> MAX-ERRORS = 4000 MAX-FORT-ERR = 200 \ ? SETUP DESCRIPTION ? \ DESCRIP DESCRIP = ( "NREL Biomass to Ethanol Process " "NREL Protected Information " "Original Authors: Vicky Putsche, Bob Wooley, Mark Ruth, Kelly Ibsen" "Original Date: April 26, 1996 " " " " " "Changes " "-----------------------------------------------------------------------" "J0601A.inp; 17 Feb 2006: 2002 Design Report Target Case " "Changes necessary to run the same between versions 12.1 & 2004 when usin" " 1. Removed SEQ3. Interpretted differently in 12.1 vs. 2004. Neither " " interpretaiton completely correct when also considering the order " " for H507+ & H509. " " 2. At the direction of Aspen Tech Support, added the CONVERGENCE blocks" " C-1 & C-2. " " 3. Moved all of the CHANGE documentation from a set of comments to " " the DESCRIPTION block. " " *** NOT PICKED UP PROPERLY BY GUI - MUST BE ADDED SEPARATELY " " BEFORE STORING AS BKP OR APW FILE ***" " 4. Change the execution control on Calculator STORE from EXECUTE " " AFTER T507-8 to using READ-VARS & WRITE-VARS; STORE was being " " executed before all ofthe input streams were being determined in " " the simulaiton. " "-----------------------------------------------------------------------" "J0506A.GUI.inp; 7 Dec 2005: 2002 Design Report Target Case " "Changes necessary to run under the GUI. " " 1. Removed 'NPHASE=1 PHASE=S' from STREAM 227 statement. " " 2. Initialize work streams determined via CALCULATOR blocks to zero. " " 3. Add missing parameters in split fractions in SEP2 blocks D502, S505" " 4. Set zero pressure drops across heaters M205COOL & M505COOL. " " 5. Add missing parameters in split fractions in SEP2 block S505. Modify" " FORTRAN CFUGESLD to adjust the proper fractions no matter the " " component order. " " 6. Add missing parameters in split fractions in SEP2 block T507-8. " " Modify DESIGN-SPEC MS-BTM to adjust the H2O fractions accounting " " for the revised order in the component list. " " 7. Set DUTY=0.0 in reacidification tank T224. " " 8. Add TP keyword in FORTRAN NUTRB to properly apply the flash spec." " 9. Change EXECUTE statement in SET VAR from FEEDPROPS to FEEDPROP." "-----------------------------------------------------------------------" " J0506A.inp; 11 Aug 2005: 2002 Design Report Target Case " " Additional fixes to code. " " 1. Moved TDP calculation with the IF block in DEWPT. " " 2. Consolidate all steam heating into a single set of blocks (similar " " to what is done with cooling water). " " a. Create LP, HP, & XP steam streams to go to the steam heating " " manifold 890, 891, & 892). Add these streams into FORTRAN " " LPSTMD, HPSTMD, & XPSTMD. " " b. Add 890, 891, & 892 into a manifold (FLASH2 STMMAN) " " c. Remove the separate steam side HEATERs H501 & H506+. " " d. Add the heat demands QRD501 & QH506 in MIXER STMDMD to form " " QTSTM. " " e. Create a single HEATER STMHX to calculate heat available from " " the steam & match up to the process's steam heating demand. " " f. Added DESIGN-SPEC STDDMD to determine the amount of low pressure " " steam (890) needed to take of the steam heating demand from the " " manifold. " " g. Remove the separate steam side HEATERs H301+ & H502. Move heat " " duties to MIXER STMDMD. Remove steam streams 590 & 592. " " 3. Modified DHFORM values of sugars & oligomers to more closely match " " the accepted heats of combusion. " " a. Adjusted the heats of combustion in FEEDPROP from which the " " soluble solids value is backed out. " " b. Changed values in HHV values COMBHEAT as calculated from " " HHV_Vals.inp & HHV_Vals.xls. " " c. Changed values of HCOM to be used in COMBHET2 as calculated from" " HHV_Vals.inp & HHV_Vals.xls. " " d. Had to increase the temperature of 301A from 65�C -> 66�C so " " that the saccharification units still have a little cooling." " 4. Move the 1st stage of injection steam (215) back to low pressure. " " 5. Added reactor block conversions, SACDAY, & SSFDAY to the summary " " file via the SENSITIVITY MASSFLOW block. " " **** NOT YET DONE **** " " X. FERMCSL specified to execute after T310 but must be moved after " " SACCSPT. " " " "-----------------------------------------------------------------------" "J0403L.inp; 17 Mar 2004: 2002 Design Report Target Case " " 1. Changed the note for the E502 area calculation (used to say H502 " " area). " " 2. Added capability to model Overliming sugar loss & soluble CaSO4." " a. Add reactions for sugar losses to T224. Assume sugars go to TAR. " " Set all conversions to zero. " " b. Added a FORTRAN block (OLCONV) to an overall conversion of " " Ca(OH)2 to Gypsum (the remaining going to CaSO4 in MIXED stream." " The Fortran block reduces T224 conversion to gypsum to make this " " overall conversion (the combined conversions from T209 & T224). " " Set to 100%. " " c. Make fate of the CaSO4 reasonable in the simulation. Make the " " separation factors in Pneumapress (S205) & Lignin Separator " " (S505) like those of the other MIXED components. Convert CaSO4 " " in combustor (M803CMB) to Gypsum. " " 3. Reduced the heat loss in the lignin residue Pneumapress. Changed " " DCOOL2 from 40 to 70. " " 4. Increase exit temperature from H244 from 30 to 35 so that the " " approach to the cooling water side is 7�C (instead of 2�C). [Area " " of H244 goes from 2861 to 2002; area of H602 goes from 3128 to " " 3228]. " " 5. Modified the cost adjustment indices in the spreadsheet (sheet " " INDICES). " " a. Added the 2002 Chemical Engineering Magazine Capital Cost index." " b. Corrected the Inorganic Chemical Index values from the Chemical " " Engineering Handbook. " " c. Changed the Labor Index values to the new basis being reported " " on the US Department of Labor website. " " 6. Corrected the spreadsheet to update the costs to the desired year " " (sheet OPCOST). Use the year specified in DCFROR as year to which " " the operating costs are adjusted. " " 7. Change the outlet pressure condition of H501 to 4.0 atm instead of " " a pressure drop of 0 (to be consistent with all other steam sides " " of exchangers). " "-----------------------------------------------------------------------" "J0402B.inp; 11 Feb 2004: MR 2002 design -- Changes so it will run " "under Aspen Plus 12.1. " " 1. To allow Aspen Plus 12.1 to sequence & run properly, changed the " " sequence control for FORTRAN SETVAR from: " " WRITE-VARS SSFDAY SSFVOL SSFWV SACDAY SACVOL SACWV & " " CLYLD CLPROD CLVOL CLWV " " to: " " EXECUTE AFTER FEEDPROPS " " and the control on FORTRAN SETMAKUP from: " " EXECUTE BEFORE BLOCK T824AS " " to: " " READ-VARS FHPSTM FLPSTM FBLOW " " WRITE-VARS FMAKUP " " 2. DHFORM values for SOLSLDS, EXTRACT, & PROTEIN now being used " " properly (in 12.1 vs. 10.2). However, now the simulation is energy " " deficient, so some more steam must bypass the electric turbines. " " Converted 590 from LP steam to HP steam " " -- Removed 590 from LPSTMD & put it into HPSTMD " " -- Changed properties of 590 to match those of 216 " " -- Changed properties of H301+ from pressure drop of 0.0 to " " pressure of 4.0 atm " " -- 590 flow went from 8739 to 6917 " "-----------------------------------------------------------------------" "R0302B.inp; 6 Feb 2003: MR 2002 design -- New Base Case " " 1. Reduced 840 from 106 to 0.0000001 " " 2. Converted 592 from LP steam to HP steam " " -- Removed 592 from LPSTMD & put it into HPSTMD " " -- Changed properties of 592 to match those of 216 " " -- Changed properties of H502 from pressure drop of 0.0 to " " pressure of 4.0 atm " " -- 592 flow went from 7630 to 6917 " " -- QE501A2 went from 12.8749 to 13.2412 (needs to get to about " " 13.6886) " " 3. Converted 215 from LP steam to HP steam " " -- Removed 215 from LPSTMD & put it into HPSTMD " " -- Changed properties of 215 to match those of 592 " " -- 215 flow went from 11569 to 10697 " " -- QE501A2 went from 13.2412 to 13.6733 (needed) " " -- Excess energy in 816 = 158 kg/hr " " 4. Updated $s to 2001 from 2000 " " 5. Switched to most recent BIODFMS3 " " 6. Fixed DT calc for H301 in sensitivity " "-----------------------------------------------------------------------" "R0302A.inp; 3 Feb 2003: MR 2002 design -- FEEDPROP updates " " NO METHANE COST IS ADDED TO SPREADSHEET YET!!!!!! " " 1. Updated Access link " " 2. Updated Labor Index " " 3. Corrected area calc for H301 in sensitivity & cost data in Access" " (H301 went from 2024 ft^2 to 256 ft^2) " " 4. Updated MWs and heats of combustion in Energy Bal worksheet " " 5. Added HHVs for soluble solids, extractives, & protein to sensitivity" " for use in Energy Bal worksheet " " 6. Made Energy Bal worksheet use a lookup to get MWs and HHVs for " " soluble solids, extractives, & protein " " 7. Used READ-VARS & WRITE-VARS in FEEDPROP so that parameters can " " be sampled in the sensitivity " " 8. Corrected heat of vaporization of water in FEEDPROP (HVAP) " " 9. Converted heat of formation calc for SolSlds to use N2 as combustion" " product instead of NO2 " " 10. Made many clean up changes to FEEDPROP & developed .feedprop.xls " " spreadsheet " " 11. Reduced 814 from 161 to 106 " " 12. Used new MW and Heat of Combustion values in Energy Bal worksheet" "-----------------------------------------------------------------------" "J0301C.inp; 31 Jan 2003: MR 2002 design -- change to BIOFMS3 " " 1. Install BIODFMS3 as in-house pure component database. " " 2. Use INHSPCD LGNSOL-1 properties for LGNSOL. Modify COMPONENTS " " statement. Remove PROP-DATA statements for LGNSOL. " " 3. Use INHSPCD SOLSLD-1 properties for SOLSLDS, EXTRACT, & PROTEIN. " " Modify COMPONENTS statement. Remove PROP-DATA ATOMNO & NOATOM " " statements for SOLSLDS, EXTRACT, & PROTEIN (but keep the DHFORM " " statements). " " 4. Use INHSPCD HMF properties for HMF. Modify COMPONENTS statement. " " Remove MW from PROP-DATA DATA-1 statement. Add MUP & RGYR values " " to PROP-DATA DATA2. Keep the Henry's coefficients as given. Use " " new NRTL-1 coefficients. " " 5. Updated all HHV values in COMBHEAT to be consistent with values " " calculated by Aspen. Updated all mising LHV values in COMBHET2 to " " be consistent with values calculated by Aspen. (These HHV & LHV " " calculations were done using HHV_Values.inp.) " " 6. Removed references to the UNKNOWN in the CISOLID phase. " " 7. Change the ENZYL value from 0.0000001 to 0.00001 to eliminate " " errors in the 'removed' cellulase production area. " "-----------------------------------------------------------------------" "R0301J.inp; 29 Jan 2003: MR 2002 design -- clean up of Chilled Water " "system " " NO METHANE COST IS ADDED TO SPREADSHEET YET!!!!!! " " 1. Added DUPL block CHWDUP to duplicate chilled water load (added " " QCHWTOTA & QCHWTOTB with it) " " 2. Renamed 950 to 950A and 951 to 951A " " 3. Renamed CHWFLOW to CHWFLWCP " " 4. Added QCHWMX2 to total the requirements for chilled water heat " " removal in standard operation (with QCHWOP) " " 5. Added CHILOP, QCHWXS, 950, and 951 for heating allowance " " 6. Added CHWFLWOP to set flow of 950 " " 7. Modified EM-908 calc in MISCPOW to use QCHWOP for power calc for " " chiller " "-----------------------------------------------------------------------" "R0301I.inp; 28 Jan 2003: MR 2002 design report -- CSL, CNUTR, & WNUTR " "Properties " " NO METHANE COST IS ADDED TO SPREADSHEET YET!!!!!! " " 1. Modified CSL component statement to use glucose properties " " 2. Removed BPVALs (binary parameter values) using CSL " " 3. Modified stoichiometry of Zymo production to use new CSL MW and not" " produce O2 " " 4. Copied Glucose values for VB, MUP, RGYR to use for CSL " " 5. Modified CNUTR component statement to use glucose properties " " 6. Copied Glucose values for VB, MUP, RGYR to use for CNUTR " " 7. Modified WNUTR component statement to use glucose properties " " 8. Copied Glucose values for VB, MUP, RGYR to use for WNUTR " " 9. Removed BPVALs (binary parameter values) using CNUTR " " 10. No BPVALs with WNUTR existed so none had to be removed " " 11. Reduced 840 flow from 234 to 170 " " 12. Added initial estimates to 303A & 304A to prevent FERMDAP & FERMCSL" " from losing properties of 311 & 311A " " 13. Modified initial guesses for 804, 815A, 621, QBOILER, QH811, 812," " QH801, 102B, 211, 432A, 508, 441, 521, 514, 576, 524 " " 14. Added SEQ8 to reduce probs with steam cycle convergence " "-----------------------------------------------------------------------" " R0301H.inp; 22 Jan 2003: MR 2002 design report -- H201 fix " " NO METHANE COST IS ADDED TO SPREADSHEET YET!!!!!! " " 1. Removed H201+B, 222, QH201B " " 2. Removed temp spec from H201- " " 3. Renamed H201+A to H201+ " " 4. Modified H201+ specs to VFRAC=0.0 & PRES = 1.0 & to use Hayden-" " O'Connell " " 5. Set heat stream from H201+ to QH201A " " 5. Added QH201SPT to split QH201A into QH201 and QH201XTR " " 6. Renamed QH244 to QH244A " " 7. Added H244MIX to mix QH244A and QH201XTR into QH244 " " 8. Modified size calculation for H-244 " "-----------------------------------------------------------------------" " R0301F.inp; 22 Jan 2003: MR 2002 design report -- add methane " " 1. Adjusted 840 to 234 so that steam balance closes " " NO METHANE COST IS ADDED TO SPREADSHEET YET!!!!!! " "-----------------------------------------------------------------------" " R0301E.inp; 22 Jan 2003: MR 2002 design report -- get rid of comments" "***********************ERRORS*******************************************" " 1. Eliminated all 'top of the file' comments written before I0203I" " 2. Combined work stream defs into single paragraph " " 3. Removed initial values for work streams set by FORTRANs " " 4. Cleaned up comments throughout code " "-----------------------------------------------------------------------" " R0301D.inp; 21 Jan 2003: MR 2002 design report -- distillation update" "***********************ERRORS*******************************************" " 1. Modified D502QCR so that the heat calcs (QCD502 & QRD502) match " " R0301C " " 2. Modified D502OVHD ethanol/water spec in 511 from 0.925 to 0.926 " " (to match R0301C result) " " 3. Modified D502 so that all the CO2 goes into stream 511 instead of " " 516 (to match R0301C result) " " 4. Modified temps in D502 to match R0103C results " " (Reduced MESP from $1.0748 to $1.0733 but has errors) " "-----------------------------------------------------------------------" " R0301B.inp; 16 Jan 2003: MR 2002 design report -- more minor mods" " 1. Modified FLOW840 so that a biomass 840 stream matches 101 (it is " " currently commented out because biomass for combustion is not " " needed) " " 2. Modified Energy_Bal so that molecular weights of protien, soluble " " solids, and extractives are looked up from ASPEN worksheet " " 3. Added H200MIX to mix 221 & 256 into 223 (which is fed to H200) " " 4. Modified H200 area calc to use 223 instead of 221 & 256 " " (steps 3 & 4 reduced the MESP from $1.0750 to $1.0748) " "-----------------------------------------------------------------------" " I0301B.inp 15 Jan 2003: KI 2002 design report - SOLSLD DHFORM change" " 1. Changed DHFORM for SOLSLDS, EXTRACT, PROTEIN from 1.34e9 to 1.1018e9" " to match FEEDPROP output in history file. " " ** ASPEN IS NOT UPDATING THE SIMULATION WITH THE DHFORM CALCULATED IN" " FORTRAN FEEDPROP FOR SOLSLDS, EXTRACT, PROTEIN. IT USES THE PROP-" " DATA DHFORM VALUE. IF YOU CHANGE FEEDSTOCK COMPOSITION, UPDATE THE" " DHFORM VALUES IN PROP-DATA FROM THE HISTORY FILE FEEDPROP OUTPUT.**" " Enthalpy of stream 101 changed from -170.0809 for -174.3759 " " MMKcal/hr " " 2. Changed ATOMNO for SOLSLDS, EXTRACT, PROTEIN to match FEEDPROP " " output in history file. " " 3. Changed T608 and M803CMB coefficients to match FEEDPROP values also." " Aspen IS updating these values from the FEEDPROP fortran, so this is" " just to be consistent. " " 4. Added variable BIOSS to be written to history file. Coeff. for T608" " biomass production reaction. " " 5. Udpated BIODFMS3.inp to Solslds DHFORM, NOATOM calc'd in FEEDPROP." " 6. Added notes on top of input file, start of FEEDPROP and in FEEDPROP" " to remind users to update the DHFORM manually if feed comp. changes." " (I0301A & I0301B increase MESP from $1.0676 to $1.0750) " "-----------------------------------------------------------------------" "I0301A.inp 15 Jan 2003; KI 2002 design report - FEEDPROP/FEEDSTK " "changes " "A1. Put FEEDSTK write statements for stream 101 into FEEDPROP. " " Deleted FEEDSTK fortran block. " "B2. Added read variables to get lignin MW (WMLIG) from Aspen and " " (CLIG, HLIG and OLIG) formula coeffs (NOATOM). Removed hard coded " " formula coefficients for C,H,O in lignin. Aspen WMLIG is sl. " " different than one calc'd due to difference between Aspen and " " hard coded C,H,O MWs (154.91903 vs. 154.919586). " " 3. Added read variables to get acetate MW (ACEMW) from Aspen and (ACEC," " ACEH, ACEO) formula coeffs (NOATOM). Removed hard coded MW and " " coeffs. MW difference (60.05298 vs. 60.05256) " "C4. Added read variables to get cellulose MW (CELLMW) and NOATOM formula" " coeffs (CELLC, CELLH, CELLO). Removed hard coded MW and coeffs." " MW difference (hard vs. Aspen) is 162.1436 vs. 162.1424 " " 5. Added read variables to get xylan MW (XYLMW) and NOATOM formula" " coeffs (XYLC, XYLH, XYLO). Removed hard coded MW and coeffs. " " MW difference (hard vs. Aspen) is 132.117 vs. 132.11612 " " 6. Added read variables to get biomass MW (BIOMW). " " Removed hard coded MW and coeffs. " " MW difference (hard vs. Aspen) is 23.23747 vs. 23.2375688 " "D7. Added read variables to retrieve DHFORM for H2O, CO2, NO2, SO2 " " and also write it to the history file.DHFORM differences: " " Hard coded Aspen Delta " " H2O -288,043,000 -241,814,000 46,229,000 " " Which is correct? " " CO2 -393,776,000 -393,510,000 266,000 " " NO2 33180000 33180000 0 " " SO2 -296840000 -296840000 0 " " 8. Made hard coded element MWs equal to Aspen values in " " FEEDPROP. C and O were already correct: " " H 1.00794 " " N 14.00674 " " S 32.066 " " 9. Added write statements for NOATOM for Solslds, Extract, Protein to" " FEEDPROP in case they are used in the model (MW is also written)." "-----------------------------------------------------------------------" " R0301A.inp 3 Jan 2003; MR 2002 design report -- minor fixes " " 1. Fixed ARO in COMBHET2 (it was not being set previously) " " 2. Added 261 & 560 to O2CALC fortran block (they are now supplementing " " 804 with O2 into the combustor) " " 3. Changed feedstock definition from PROH20 to PROH2O to match variable" " in the rest of FEEDPROP " " (Changes 1-3 did not change MESP from $1.0667) " " 4. Changed T608 to react NH4ACET and produce NO2 instead of N2 " " 5. Changed CNNH4 in CODCALC1, CODCALC2, & CODEND from 1.143 to 1.557" " to match NO2 production instead of N2 production " " (Changes 4-5 did not change MESP from $1.0667) " " 6. Cleaned up Feedstock_Losses worksheet and added tracking of GlucOlig" " (also necessary in Aspen worksheet) to improve results' accuracy" " 7. Removed Area 400 from EQUIP " " 8. Added AIRCMP to SEQ11 to set WM904A to calculate after WM904 " " (Change 8 increased the MESP to $1.0676) " " 9. Removed the following variables from sensitivity: " " ACET220A, CENTFLOW, NUMRCENT, CLVESSEL, HIHV0101, INUMLAGT, NUMRREAC," " REACFLOW, PSEU0506, PSEU0511, QCWCAPIT, S221S256, SACCAGTR, SACVESSL," " SSCFAGTR, SSFVESSL " " 10. Removed the following variables from the Aspen worksheet: " " CCIS0401CELU, CCIS0420CELU, CMIX0220H2SO, CMIX0401ARAB, CMIX0401CELB," " CMIX0401GALO, CMIX0401GLUC, CMIX0401MANO, CMIX0401XYLO, CMIX0419H2O, " " CMIX0420ARAB, CMIX0420CELB, CMIX0420GALO, CMIX0420GLUC, CMIX0420MANO," " CMIX0420XYLO, CMIX0435H2O, CMIX0550H2O, CMIX301BARAB, CMIX301BGALO," " CMIX301BGLUC, CMIX301BMANO, CMIX301BXYLO, CMIX809AH2O, PRES0812, " " PRES0816, QH512, QTTOTAL, STRM0219, STRM0223, STRM0236, STRM0240," " STRM0243, STRM0244, STRM0246, STRM0310, STRM0311, STRM0415, STRM0416," " STRM0417, STRM0420, STRM0433, STRM0440, STRM0717, STRM0803, STRM0804," " STRM0816, STRM0851, STRM0906, STRM301B, STRM310A, STRM311A, STRM412A," " STRM613C, STRM619A, STRM804D, TEMP0812, TEMP0816, TEMP809A, VAP0812, " " VAP0816 " " 11. Fixed Aspen_Retrieval Subroutine: When there was no value for a " " requested temp, vapor frac, or density the 0 value and 'Missing" " Value' warning were put into the wrong row; therefore, overwriting" " a good value for a different variable. " " (Changes 9-11 did not change MESP from $1.0676) " "-----------------------------------------------------------------------" " bw0211a.inp November 20, 2002 Bob Wallace " " Fixes to design case in the heat exchanger areas " " 1. Added stream 256 and temp T256 into H200 since it combines with" " 221 before entering H200 " " 2. Replace T306 with T502 in H201 " "-----------------------------------------------------------------------" " I0203I.inp 20 March 2002; KNI 2002 design report final model " " 1. Changed temps of CSL, DAP and Cellulase 300 streams to 20 C. " " 2. BIOMASS define stmts from MIXED to CISOLID. " " 3. Remove negative sign from CO2 calc in FEEDPROP. " " 4. Added IF/ELSE stmt and negative sign to CEXTR calc to catch a " " negative COD and calculate a positive one from a neg. O2 coeff." " 5. Added CEXTR, CPRO, CSOLS to CODCALC1, 2, END as READ VARS. " " 6. Moved AERAIR after CODCALC2 in sequence. " " 7. Changed 219 calculation in fortran RECYCLE to calculate solids in " " T310 per M. Ruth discussion to control solids in sacch. tank for " " agitation. " " 8. Made changes to MASSFLOW block per B. Atherton's work on E balance." " 9. Overliming area changes per B. Hames, 3/22/02. " " Removed lignin ppt reaction from T-224; not likely at pH 9. " "10. Changed S-505 splits in block and fortran to send CSL, CNUTR, WNUTR" " to WWT, since they should be consumed by this point in process. All" " other solubles are treated as water. " "11. Updated 804 flow rate guess in stream statment - BRNAIR not " " converging. No help. Increased range for BNDLOW and BNDHI by " " changing 0.9 to 0.8 on BNDLOW and 1.0 to 1.2 on BNDHI. " "12. Updated QCD501, QRD501, QCD502, QRD502 inital values from stand " " alone distillation model run DM0203C.bkp. " "13. Removed several commented out lines to clean up code. " "14. Changed conversions in seed ferm F301F1-6 to match F300F but with 4%" " cell growth and added conversions for arabinose, mannose, galactose." "15. Changed zymo, glycerol, lactic, etc. conversions in F300F to match" " Yellow Poplar data reported in the 2002 design case (EPD0005 run)." "16. Added statements in MASSFLOW to print out the calculated molecular " " weights of the soluble solids, extract, & protein components. " " (JLJ 5/10/02) " "17. Added work streams for DAP and DAP/CSL mixing: " " WC755 DAP solids feeder copy of WC225 " " WP755 DAP unloading blower copy of WP223 " " WP760 CSL/DAP pump copy of WP720 " " WT760 CSL/DAP day tank agitator 0.5 hp/1000 gal " "18. Moved 531 to M803MIX so that O2 for burner is calculated right." " This will also fix BTU calculation (puts 531 into 803). " "19. Added stream 251 to block T914 to make PFDs look more balanced." " Still not completely balanced since minor components that would be" " coming from RW stream 905 are not calcd. for streams 574,906,941." "20. Changed WP211 calc to be based on FMP211 & FCP211 " "21. Added CH4101 & CH4840 definitions to COMBHEAT " "22. Removed TTL311, TTL31A, TTL303, & TTL304 from CNC2B calc in RECYCLE" "23. Changed HHVs of Soluble Solids, Proteins, & Extractives in COMBHEAT" " to be read as parameters 7, 8, & 9 from FEEDPROP " "24. Changed LHVs of Soluble Solids, Proteins, & Extractives in COMBHET2" " to be read as parameters 10, 11, & 12 from FEEDPROP " "BGA1. Modified hard coded heat of combustion values in COMBHET2 in order" " to match heat of combustion values calculated for the energy " " balance. See Fortran Block COMBHET2 with initials BGA for edits. " "BGA2. Fortran block COMBHET2 -> Added the vaporization energy instead of" " subtracting because all the heats of combustion are negative. " " Significantly changed LHV of feed to combustor. " "-----------------------------------------------------------------------" " *****PARAMETER VALUES IN USE***** " " 2 HLETOT " " 3 WATCON " " 4 BTU101 " " 5 P501GP " " 7 HCSOL " " 8 HCPRO " " 9 HCEXT " " 10 CMBSOL " " 11 CMBEXT " " 12 CMBPRO " " 13 CEXTR " " 14 CPRO " " 15 CSOLS " " 31 SSFVES " " 32 SSFDAY " " 33 SSFVOL " " 34 SSFWV " " 35 PMPSSF " " 36 SACVES " " 37 SACDAY " " 38 SACVOL " " 39 SACWV " " 40 PMPSAC " " " " 41 CLYLD " " 42 CLPROD " " 43 CLVES " " 44 CLVOL " " 45 CLWV " " " " 51 TOTWAT " " 52 WATPER " " 55 BNDLOW " ) \ \ COMMENTS COMMENTS = ( ";;" ";===========================================================================" "; Physical Property Data" ";===========================================================================" ";;" "; New Statements setting up the NREL Biofuels Database" ";;" ) \ ? DATABANKS ? \ DATABANKS FILE-SYM-NAM = ( INHSPCD PURE93 SOLIDS ASPENPCD ) \ ? COMPONENTS MAIN ? \ COMPONENTS CID = GLUCOSE ANAME = C6H12O6 OUTNAME = GLUCOSE DBNAME1 = "GLUCOSE" ANAME1 = "C6H12O6" / CID = CELLULOS ANAME = C6H10O5 OUTNAME = CELLULOS TYPE = SOLID DBNAME1 = "CELLULOS" ANAME1 = "C6H10O5" / CID = XYLOSE ANAME = C5H10O5 OUTNAME = XYLOSE DBNAME1 = "XYLOSE" ANAME1 = "C5H10O5" / CID = XYLAN ANAME = C5H8O4 OUTNAME = XYLAN TYPE = SOLID DBNAME1 = "XYLAN" ANAME1 = "C5H8O4" / CID = LIGNIN ANAME = CXHXOX-1 OUTNAME = LIGNIN TYPE = SOLID DBNAME1 = "LIGNIN-1" ANAME1 = "CXHXOX-1" / CID = CELLULAS ANAME = CHXNXOXSX-2 OUTNAME = CELLULAS TYPE = SOLID DBNAME1 = "CELLULAS" ANAME1 = "CHXNXOXSX-2" / CID = BIOMASS ANAME = CHXNXOXSX-1 OUTNAME = BIOMASS TYPE = SOLID DBNAME1 = "BIOMASS" ANAME1 = "CHXNXOXSX-1" / CID = ZYMO ANAME = CHXOXNX OUTNAME = ZYMO TYPE = SOLID DBNAME1 = "ZYMO" ANAME1 = "CHXOXNX" / CID = UNKNOWN ANAME = CXHOX OUTNAME = UNKNOWN DBNAME1 = "SOLUNKN" ANAME1 = "CXHOX" / CID = SOLSLDS ANAME = CXHXOXNXSX-1 OUTNAME = SOLSLDS DBNAME1 = "SOLSLD-1" ANAME1 = "CXHXOXNXSX-1" / CID = GYPSUM ANAME = CASO4-2H2O OUTNAME = GYPSUM TYPE = SOLID DBNAME1 = "GYPSUM" ANAME1 = "CASO4-2H2O" / CID = ACETATE ANAME = C2H4O2-N1 OUTNAME = ACETATE TYPE = SOLID DBNAME1 = "ACETATE" ANAME1 = "C2H4O2-N1" / CID = LGNSOL ANAME = CXHXOX-S1 OUTNAME = LGNSOL DBNAME1 = "LGNSOL-1" ANAME1 = "CXHXOX-S1" / CID = HMF ANAME = C6H6O3-1 OUTNAME = HMF DBNAME1 = "HMF" ANAME1 = "C6H6O3-1" / CID = ARABINOS ANAME = C5H10O5 OUTNAME = ARABINOS DBNAME1 = "XYLOSE" ANAME1 = "C5H10O5" / CID = GALACTOS ANAME = C6H12O6 OUTNAME = GALACTOS DBNAME1 = "GLUCOSE" ANAME1 = "C6H12O6" / CID = MANNOSE ANAME = C6H12O6 OUTNAME = MANNOSE DBNAME1 = "GLUCOSE" ANAME1 = "C6H12O6" / CID = ARABINAN ANAME = C5H8O4 OUTNAME = ARABINAN TYPE = SOLID DBNAME1 = "XYLAN" ANAME1 = "C5H8O4" / CID = MANNAN ANAME = C6H10O5 OUTNAME = MANNAN TYPE = SOLID DBNAME1 = "CELLULOS" ANAME1 = "C6H10O5" / CID = GALACTAN ANAME = C6H10O5 OUTNAME = GALACTAN TYPE = SOLID DBNAME1 = "CELLULOS" ANAME1 = "C6H10O5" / CID = GLUCOLIG ANAME = C6H12O6 OUTNAME = GLUCOLIG DBNAME1 = "GLUCOSE" ANAME1 = "C6H12O6" / CID = CELLOB ANAME = C6H12O6 OUTNAME = CELLOB DBNAME1 = "GLUCOSE" ANAME1 = "C6H12O6" / CID = XYLOLIG ANAME = C5H10O5 OUTNAME = XYLOLIG DBNAME1 = "XYLOSE" ANAME1 = "C5H10O5" / CID = TAR ANAME = C5H8O4 OUTNAME = TAR TYPE = SOLID DBNAME1 = "XYLAN" ANAME1 = "C5H8O4" / CID = MANOLIG ANAME = C6H12O6 OUTNAME = MANOLIG DBNAME1 = "GLUCOSE" ANAME1 = "C6H12O6" / CID = GALAOLIG ANAME = C6H12O6 OUTNAME = GALAOLIG DBNAME1 = "GLUCOSE" ANAME1 = "C6H12O6" / CID = ARABOLIG ANAME = C5H10O5 OUTNAME = ARABOLIG DBNAME1 = "XYLOSE" ANAME1 = "C5H10O5" / CID = ACETOLIG ANAME = C2H4O2-1 OUTNAME = ACETOLIG DBNAME1 = "ACETIC-ACID" ANAME1 = "C2H4O2-1" / CID = XYLITOL ANAME = CXHOX OUTNAME = XYLITOL DBNAME1 = "SOLUNKN" ANAME1 = "CXHOX" / CID = EXTRACT ANAME = CXHXOXNXSX-1 OUTNAME = EXTRACT DBNAME1 = "SOLSLD-1" ANAME1 = "CXHXOXNXSX-1" / CID = PROTEIN ANAME = CXHXOXNXSX-1 OUTNAME = PROTEIN DBNAME1 = "SOLSLD-1" ANAME1 = "CXHXOXNXSX-1" / CID = CASO4 ANAME = CASO4 OUTNAME = CASO4 TYPE = SOLID DBNAME1 = "CALCIUM-SULFATE" ANAME1 = "CASO4" / CID = CAH2O2 ANAME = "CA(OH)2" OUTNAME = CAH2O2 TYPE = SOLID DBNAME1 = "CALCIUM-HYDROXIDE" ANAME1 = "CA(OH)2" / CID = ASH ANAME = CAO OUTNAME = ASH TYPE = SOLID DBNAME1 = "CALCIUM-OXIDE" ANAME1 = "CAO" / CID = ETHANOL ANAME = C2H6O-2 OUTNAME = ETHANOL DBNAME1 = "ETHANOL" ANAME1 = "C2H6O-2" / CID = H2O ANAME = H2O OUTNAME = H2O DBNAME1 = "WATER" ANAME1 = "H2O" / CID = FURFURAL ANAME = C5H4O2 OUTNAME = FURFURAL DBNAME1 = "FURFURAL" ANAME1 = "C5H4O2" / CID = H2SO4 ANAME = H2SO4 OUTNAME = H2SO4 DBNAME1 = "SULFURIC-ACID" ANAME1 = "H2SO4" / CID = N2 ANAME = N2 OUTNAME = N2 DBNAME1 = "NITROGEN" ANAME1 = "N2" / CID = CO2 ANAME = CO2 OUTNAME = CO2 DBNAME1 = "CARBON-DIOXIDE" ANAME1 = "CO2" / CID = O2 ANAME = O2 OUTNAME = O2 DBNAME1 = "OXYGEN" ANAME1 = "O2" / CID = CH4 ANAME = CH4 OUTNAME = CH4 DBNAME1 = "METHANE" ANAME1 = "CH4" / CID = NO ANAME = NO OUTNAME = NO DBNAME1 = "NITRIC-OXIDE" ANAME1 = "NO" / CID = NO2 ANAME = NO2 OUTNAME = NO2 DBNAME1 = "NITROGEN-DIOXIDE" ANAME1 = "NO2" / CID = NH3 ANAME = H3N OUTNAME = NH3 DBNAME1 = "AMMONIA" ANAME1 = "H3N" / CID = LACID ANAME = C3H6O3-D1 OUTNAME = LACID DBNAME1 = "LACTIC-ACID" ANAME1 = "C3H6O3-D1" / CID = AACID ANAME = C2H4O2-1 OUTNAME = AACID DBNAME1 = "ACETIC-ACID" ANAME1 = "C2H4O2-1" / CID = NH4OH ANAME = H3N OUTNAME = NH4OH DBNAME1 = "AMMONIA" ANAME1 = "H3N" / CID = NH4SO4 ANAME = "(NH4)2SO4" OUTNAME = NH4SO4 DBNAME1 = "AMMONIUM-SULFATE" ANAME1 = "(NH4)2SO4" / CID = NH4ACET ANAME = "(NH4)2SO4" OUTNAME = NH4ACET DBNAME1 = "AMMONIUM-SULFATE" ANAME1 = "(NH4)2SO4" / CID = GLYCEROL ANAME = C3H8O3 OUTNAME = GLYCEROL DBNAME1 = "GLYCEROL" ANAME1 = "C3H8O3" / CID = SUCCACID ANAME = C4H6O4-2 OUTNAME = SUCCACID DBNAME1 = "SUCCINIC-ACID" ANAME1 = "C4H6O4-2" / CID = DAP ANAME = "(NH4)2HPO4" OUTNAME = DAP DBNAME1 = "DIAMMONIUM-PHOSPHATE" ANAME1 = "(NH4)2HPO4" / CID = PROPANE ANAME = C3H8 OUTNAME = PROPANE DBNAME1 = "PROPANE" ANAME1 = "C3H8" / CID = DENAT ANAME = C7H16-1 OUTNAME = DENAT DBNAME1 = "N-HEPTANE" ANAME1 = "C7H16-1" / CID = OIL ANAME = C18H34O2 OUTNAME = OIL DBNAME1 = "OLEIC-ACID" ANAME1 = "C18H34O2" / CID = CSL ANAME = C6H12O6 OUTNAME = CSL DBNAME1 = "GLUCOSE" ANAME1 = "C6H12O6" / CID = CNUTR ANAME = C6H12O6 OUTNAME = CNUTR DBNAME1 = "GLUCOSE" ANAME1 = "C6H12O6" / CID = WNUTR ANAME = C6H12O6 OUTNAME = WNUTR DBNAME1 = "GLUCOSE" ANAME1 = "C6H12O6" / CID = SO2 ANAME = O2S OUTNAME = SO2 DBNAME1 = "SULFUR-DIOXIDE" ANAME1 = "O2S" / CID = H2S ANAME = H2S OUTNAME = H2S DBNAME1 = "HYDROGEN-SULFIDE" ANAME1 = "H2S" / CID = C ANAME = C OUTNAME = C DBNAME1 = "CARBON-GRAPHITE" ANAME1 = "C" / CID = CO ANAME = CO OUTNAME = CO DBNAME1 = "CARBON-MONOXIDE" ANAME1 = "CO" \ \ COMMENTS COMMENTS = ( ";;" ";===========================================================================" "; Components" ";===========================================================================" ";;" "; In-house database components" "; In-house database aliases" "; Solids Database" "; Purecomps Database" "; DENAT IS GASOLINE FOR DENATURING" "; OIL IS CORN OIL FOR ANTIFOAM." "; CNUTR ARE CELLULASE NUTRIENTS (SALTS) AND WNUTR ARE" "; NUTRIENTS FOR WASTEWATER TREATMENT (I.E. TRIPLE" "; SUPER PO4 AND UREA)." ) \ ? COMPONENTS "HENRY-COMPS" HC ? \ "HENRY-COMPS" CID = ( O2 N2 CO2 CH4 ) \ \ COMMENTS COMMENTS = ( ";;" ) \ ? COMPONENTS "COMP-LIST" GLOBAL ? ? SOLVE ? ? FLOWSHEET A100 ? \ BLOCK BLKID = C103A BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 102 M0-1 107 M0-1 ) OUT = ( 104A M0-1 104D M0-1 ) \ \ BLOCK BLKID = C103B BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 104D M0-1 ) OUT = ( 104B M0-1 102A M0-1 ) \ \ BLOCK BLKID = C103C BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 104A M0-1 104B M0-1 ) OUT = ( 104 M0-1 ) \ \ BLOCK BLKID = M104LOSS BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 102A M0-1 ) OUT = ( 103 M0-1 102B M0-1 ) \ \ BLOCK BLKID = M104MIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 102B M0-1 101 M0-1 ) OUT = ( 105 M0-1 ) \ \ BLOCK BLKID = MPOW1 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WC101 W2-7 WC102 W2-7 WC104 W2-7 WC103 W2-7 WM103 W2-7 WM104 W2-7 WM105 W2-7 WM107 W2-7 WS101 W2-7 WS102 W2-7 WS103 W2-7 ) OUT = ( WMP1 W2-4 ) \ \ COMMENTS COMMENTS = ( ";;" ";----------------------------------------------------------------" "; FLOWSHEETS" ";---------------------------------------------------------------" ";;" ";THIS IS THE FLOWSHEET FOR FEED HANDLING." ) \ ? FLOWSHEET A200 ? \ BLOCK BLKID = A201 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 212 M0-1 211 M0-1 ) OUT = ( 214 M0-1 ) \ \ BLOCK BLKID = M202MIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 105 M0-1 214 M0-1 ) OUT = ( 214A M0-1 ) \ \ BLOCK BLKID = M202LO BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 214A M0-1 215 M0-1 ) OUT = ( 215A M0-1 QM202LO Q2-3 ) \ \ BLOCK BLKID = M202HI BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 215A M0-1 216 M0-1 ) OUT = ( 217 M0-1 QM202HI Q2-3 ) \ \ BLOCK BLKID = T203 BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 217 M0-1 ) OUT = ( 218 M0-1 220 M1-2 ) \ \ BLOCK BLKID = S205SPT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 219 M0-1 ) OUT = ( 252 M0-1 253 M0-1 ) \ \ BLOCK BLKID = S205A BLKTYPE = SSPLIT MDLTYPE = "SSplit" IN = ( 220 M0-1 ) OUT = ( 221 M0-1 225 M0-1 ) \ \ BLOCK BLKID = S205MIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 225 M0-1 252 M0-1 ) OUT = ( 254 M0-1 ) \ \ BLOCK BLKID = S205B BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 254 M0-1 ) OUT = ( 255A M0-1 256 M0-1 ) \ \ BLOCK BLKID = M205 BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 257 M0-1 ) OUT = ( 258 M0-1 WM205 W2-3 ) \ \ BLOCK BLKID = M205COOL BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 258 M0-1 ) OUT = ( 259 M0-1 QM205 Q2-3 ) \ \ BLOCK BLKID = S205FLSH BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 255A M0-1 259 M0-1 ) OUT = ( 260 M0-1 255 M1-2 ) \ \ BLOCK BLKID = H205 BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 260 M0-1 ) OUT = ( 261 M0-1 262 M1-2 QH205 Q3-4 ) \ \ BLOCK BLKID = H200MIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 221 M0-1 256 M0-1 ) OUT = ( 223 M0-1 ) \ \ BLOCK BLKID = H200 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 223 M0-1 ) OUT = ( 240 M0-1 QH200 Q2-3 ) \ \ BLOCK BLKID = T209 BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 240 M0-1 227 M0-1 ) OUT = ( 228 M0-1 ) \ \ BLOCK BLKID = T224 BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 233 M0-1 228 M0-1 ) OUT = ( 239 M0-1 ) \ \ BLOCK BLKID = S222 BLKTYPE = SSPLIT MDLTYPE = "SSplit" IN = ( 239 M0-1 ) OUT = ( 229 M0-1 230 M0-1 ) \ \ BLOCK BLKID = C202 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 255 M0-1 230 M0-1 253 M0-1 ) OUT = ( 250 M0-1 ) \ \ BLOCK BLKID = P224 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 250 M0-1 ) OUT = ( 232 M0-1 ) \ \ BLOCK BLKID = "H201+" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 218 M0-1 ) OUT = ( 520A M0-1 QH201A Q2-3 ) \ \ BLOCK BLKID = QH201SPT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( QH201A Q1-2 ) OUT = ( QH201 Q1-4 QH201XTR Q1-4 ) \ \ BLOCK BLKID = "H201-" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 502 M0-1 QH201 Q1-2 ) OUT = ( 501 M0-1 ) \ \ BLOCK BLKID = H244 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 520A M0-1 ) OUT = ( 520 M0-1 QH244A Q2-3 ) \ \ BLOCK BLKID = H244MIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QH244A Q1-4 QH201XTR Q1-4 ) OUT = ( QH244 Q1-3 ) \ \ BLOCK BLKID = MPOW2 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WM202 W2-7 WC202 W2-7 WC225 W2-7 WC201 W2-7 WS205 W2-7 WS221 W2-7 WS222 W2-7 ) OUT = ( WMP2 W2-4 ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS IS THE FLOWSHEET FOR THE PRETREATMENT AREA AND INCLUDES PRETREATMENT" ";AND DETOXIFICATION." ) \ ? FLOWSHEET A300 ? \ BLOCK BLKID = "H301-" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 301 M0-1 ) OUT = ( 301A M0-1 QH301 Q2-3 ) \ \ BLOCK BLKID = T310 BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 301A M0-1 312 M0-1 422 M0-1 ) OUT = ( 301B M0-1 QF300A Q2-3 ) \ \ BLOCK BLKID = H302 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 301B M0-1 ) OUT = ( 301C M0-1 QH302 Q2-3 ) \ \ BLOCK BLKID = SACCHSPT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 301C M0-1 ) OUT = ( 302 M0-1 303 M0-1 ) \ \ BLOCK BLKID = SEEDMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 303 M0-1 310 M0-1 310A M0-1 ) OUT = ( 303A M0-1 ) \ \ BLOCK BLKID = "F301-6F" BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 303A M0-1 ) OUT = ( 303B M0-1 "QF301-6B" Q2-3 ) \ \ BLOCK BLKID = "F301-6FL" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 303B M0-1 ) OUT = ( 304C M0-1 304 M1-2 ) \ \ BLOCK BLKID = FERMMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 302 M0-1 311 M0-1 311A M0-1 304 M0-1 ) OUT = ( 304A M0-1 ) \ \ BLOCK BLKID = CONTSPLT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 304A M0-1 ) OUT = ( 304F M0-1 304G M0-1 ) \ \ BLOCK BLKID = F300CONT BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 304G M0-1 ) OUT = ( 304H M0-1 QF300CNT Q2-3 ) \ \ BLOCK BLKID = F300F BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 304F M0-1 ) OUT = ( 304E M0-1 QF300B Q2-3 ) \ \ BLOCK BLKID = T306 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 306 M0-1 551 M0-1 ) OUT = ( 502 M0-1 ) \ \ BLOCK BLKID = F300FLSH BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 304E M0-1 304H M0-1 ) OUT = ( 308 M0-1 306 M1-2 ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS FLOWSHEET MODELS THE SACCHARIFICATION AND FERMENTATION PROCESS." "; BLOCK H301+ IN=590 QH301 OUT=591 QH301EX" ) \ ? FLOWSHEET A400 ? \ BLOCK BLKID = BTMSSPLT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 232 M0-1 ) OUT = ( 401 M0-1 301 M0-1 ) \ \ BLOCK BLKID = CLFDSPLT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 401 M0-1 ) OUT = ( 403 M0-1 410 M0-1 ) \ \ BLOCK BLKID = "F401-4MX" BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 403 M0-1 430 M0-1 ) OUT = ( 431 M0-1 ) \ \ BLOCK BLKID = "F401-4" BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 423 M0-1 431 M0-1 432 M0-1 434 M0-1 ) OUT = ( 432A M0-1 "QF401-4" Q2-3 ) \ \ BLOCK BLKID = "F401-4FL" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 432A M0-1 ) OUT = ( 435 M0-1 433 M1-2 ) \ \ BLOCK BLKID = H415 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 411 M0-1 ) OUT = ( 412 M0-1 QH415 Q2-3 ) \ \ BLOCK BLKID = T415 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 412 M0-1 410 M0-1 ) OUT = ( 412A M0-1 ) \ \ BLOCK BLKID = F400 BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 412A M0-1 433 M0-1 413 M0-1 436 M0-1 416 M0-1 417 M0-1 ) OUT = ( 417A M0-1 QF400 Q2-3 ) \ \ BLOCK BLKID = F400FL BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 417A M0-1 ) OUT = ( 419 M0-1 420 M1-2 ) \ \ BLOCK BLKID = CLSSPLIT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 420 M0-1 ) OUT = ( 421 M0-1 422 M0-1 ) \ \ BLOCK BLKID = T405 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 415 M0-1 414 M0-1 ) OUT = ( 416 M0-1 ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS FLOWSHEET MODELS THE CELLULASE PRODUCTION AREA." "; STREAM 421 SHOULD BE ZERO IN A SEP SACCH/FERM MODE" "; AND IS NOT ADDED TO ANY BLOCK IN AREA 300" ) \ ? FLOWSHEET A500 ? \ BLOCK BLKID = "H512-" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 501 M0-1 ) OUT = ( 506 M0-1 QH512 Q2-3 ) \ \ BLOCK BLKID = "H512+" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 518 M0-1 QH512 Q1-2 ) OUT = ( 518A M0-1 ) \ \ BLOCK BLKID = D501 BLKTYPE = RADFRAC MDLTYPE = "RadFrac" IN = ( 506 M0-1 ) OUT = ( 508 M0-1 510 M3-4 518 M2-3 QCD501 Q5-6 QRD501 Q6-7 ) \ \ BLOCK BLKID = D502 BLKTYPE = SEP2 MDLTYPE = "Sep2" IN = ( 510 M0-1 521 M0-1 ) OUT = ( 511 M0-1 516 M1-2 ) \ \ BLOCK BLKID = "H506-" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 511 M0-1 ) OUT = ( 511C M0-1 QH506 Q2-3 ) \ \ BLOCK BLKID = "T507-8" BLKTYPE = SEP2 MDLTYPE = "Sep2" IN = ( 511C M0-1 ) OUT = ( 515A M0-1 514 M1-2 ) \ \ BLOCK BLKID = H503 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 515A M0-1 ) OUT = ( 517 M0-1 QH503 Q2-3 ) \ \ BLOCK BLKID = "H507-" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 517 M0-1 QH507 Q1-2 ) OUT = ( 521 M0-1 ) \ \ BLOCK BLKID = "H507+" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 514 M0-1 ) OUT = ( 519 M0-1 QH507 Q2-3 ) \ \ BLOCK BLKID = H509 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 519 M0-1 ) OUT = ( 515 M0-1 QH509 Q2-3 ) \ \ BLOCK BLKID = RECTDUP BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( QCD502 Q1-2 ) OUT = ( QC502A Q1-2 QC502B Q1-2 ) \ \ BLOCK BLKID = E501LOSS BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( QC502A Q1-2 QE501A Q1-2 ) OUT = ( QE501L Q1-4 QE501B Q1-4 ) \ \ BLOCK BLKID = E501L BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 518A M0-1 QE501B Q1-2 ) OUT = ( 526 M0-1 525 M1-2 ) \ \ BLOCK BLKID = E502V BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 526 M0-1 ) OUT = ( 527 M0-1 QE502A Q2-3 ) \ \ BLOCK BLKID = E502LOSS BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( QE502A Q1-2 ) OUT = ( QE502L Q1-4 QE502B Q1-4 ) \ \ BLOCK BLKID = E502L BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 580 M0-1 QE502B Q1-2 ) OUT = ( 529 M0-1 528 M1-2 ) \ \ BLOCK BLKID = E503V BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 529 M0-1 ) OUT = ( 530 M0-1 QE503A Q2-3 ) \ \ BLOCK BLKID = E503LOSS BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( QE503A Q1-2 ) OUT = ( QE503L Q1-4 QE503B Q1-4 ) \ \ BLOCK BLKID = E503L BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 528 M0-1 QE503B Q1-2 ) OUT = ( 532 M0-1 531 M1-2 ) \ \ BLOCK BLKID = E501MIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 527 M0-1 530 M0-1 533 M0-1 ) OUT = ( 534A M0-1 ) \ \ BLOCK BLKID = E501WW BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 534A M0-1 852 M0-1 ) OUT = ( 534B M0-1 535 M0-1 ) \ \ BLOCK BLKID = E501SPT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 534B M0-1 ) OUT = ( 102 M0-1 211 M0-1 251 M0-1 ) \ \ BLOCK BLKID = H517 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 532 M0-1 ) OUT = ( 533 M0-1 QH517 Q2-3 ) \ \ BLOCK BLKID = VNTMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 508 M0-1 304C M0-1 308 M0-1 ) OUT = ( 523 M0-1 ) \ \ BLOCK BLKID = VNTSCRUB BLKTYPE = RADFRAC MDLTYPE = "RadFrac" IN = ( 523 M0-1 524 M0-1 ) OUT = ( 550 M0-1 551 M2-3 ) \ \ BLOCK BLKID = MPOW5 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WC501 W2-7 WS505 W2-7 ) OUT = ( WMP5 W2-4 ) \ \ BLOCK BLKID = DCOOL2 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 525 M0-1 ) OUT = ( 570 M0-1 QDCOOL2 Q2-3 ) \ \ BLOCK BLKID = S505 BLKTYPE = SEP2 MDLTYPE = "Sep2" IN = ( 570 M0-1 ) OUT = ( 572 M0-1 571B M1-2 ) \ \ BLOCK BLKID = T530 BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 572 M0-1 ) OUT = ( 573 M0-1 580 M0-1 ) \ \ BLOCK BLKID = M505 BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 557 M0-1 ) OUT = ( 558 M0-1 WM505 W2-3 ) \ \ BLOCK BLKID = M505COOL BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 558 M0-1 ) OUT = ( 559 M0-1 QM505 Q2-3 ) \ \ BLOCK BLKID = S505FLSH BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 571B M0-1 559 M0-1 ) OUT = ( 560 M0-1 571 M1-2 ) \ \ BLOCK BLKID = FWMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 516 M0-1 573 M0-1 574 M0-1 ) OUT = ( 576 M0-1 ) \ \ BLOCK BLKID = RWSPLT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 576 M0-1 ) OUT = ( 219 M0-1 430 M0-1 411 M0-1 ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS FLOWSHEET MODELS THE DISTILLATION/DEHYDRATION AREA." "; BLOCK H506+ IN=596 QH506 OUT=597 QH506EX ;" "; BLOCK H502 IN=592 QRD502 OUT=593 QH504EX ;" "; BLOCK H501 IN=594 QRD501 OUT=595 QRD501EX ;" "; ADDED SEPARATE MIXER AND SPLITTER SO WE CAN SEE TOTAL CONDENSATE" "; VENT SCRUBBER" "; Stream Definitions: 524 WATER, 550 VENT, 551 WASTE WATER" "; PNEUMAPRESS UNIT" ) \ ? FLOWSHEET A600 ? \ BLOCK BLKID = S600 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 262 M0-1 520 M0-1 821 M0-1 535 M0-1 944 M0-1 ) OUT = ( 612 M0-1 ) \ \ BLOCK BLKID = H602 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 612 M0-1 ) OUT = ( 613 M0-1 QH602 Q2-3 ) \ \ BLOCK BLKID = NUTMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 613 M0-1 630 M0-1 ) OUT = ( 632 M0-1 ) \ \ BLOCK BLKID = T606 BLKTYPE = USER MDLTYPE = "User" IN = ( 632 M0-1 ) OUT = ( 613C M0-1 ) \ \ BLOCK BLKID = T606FLSH BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 613C M0-1 ) OUT = ( 615 M0-1 618 M1-2 ) \ \ BLOCK BLKID = T608 BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 618 M0-1 626 M0-1 627 M0-1 ) OUT = ( 619A M0-1 ) \ \ BLOCK BLKID = T608FLSH BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 619A M0-1 ) OUT = ( 620 M0-1 621 M1-2 ) \ \ BLOCK BLKID = T610 BLKTYPE = SSPLIT MDLTYPE = "SSplit" IN = ( 621 M0-1 ) OUT = ( 625 M0-1 624 M0-1 ) \ \ BLOCK BLKID = S614 BLKTYPE = SSPLIT MDLTYPE = "SSplit" IN = ( 625 M0-1 631 M0-1 ) OUT = ( 627 M0-1 623 M0-1 ) \ \ BLOCK BLKID = MPOW6 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WC614 W2-7 WS614 W2-7 WM604 W2-7 WM612 W2-7 WS600 W2-7 WT610 W2-7 ) OUT = ( WMP6 W2-4 ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS SECTION MODELS THE WASTEWATER TREATMENT AREA." ) \ ? FLOWSHEET A700 ? \ BLOCK BLKID = DCOOLE BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 515 M0-1 ) OUT = ( 515E M0-1 ) \ \ BLOCK BLKID = PRODMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 515E M0-1 701 M0-1 ) OUT = ( 703 M0-1 ) \ \ BLOCK BLKID = TSTORE BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 710 M0-1 713 M0-1 717 M0-1 723 M0-1 735 M0-1 745 M0-1 750 M0-1 755 M0-1 ) OUT = ( 702 M0-1 ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS FLOWSHEET MODELS THE STORAGE AREA." ) \ ? FLOWSHEET A800 ? \ BLOCK BLKID = M803CMB BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 615 M0-1 803 M0-1 804B M0-1 840 M0-1 ) OUT = ( 804C M0-1 QM803 Q2-3 ) \ \ BLOCK BLKID = M801MIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 571A M0-1 623 M0-1 531 M0-1 ) OUT = ( 803 M0-1 ) \ \ BLOCK BLKID = M802MIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 804 M0-1 261 M0-1 560 M0-1 ) OUT = ( 804E M0-1 ) \ \ BLOCK BLKID = M802 BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 804E M0-1 ) OUT = ( 804A M0-1 WCOMBFAN W2-3 ) \ \ BLOCK BLKID = "H801-" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 804A M0-1 QH801 Q1-2 ) OUT = ( 804B M0-1 ) \ \ BLOCK BLKID = M801STM BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 853 M0-1 ) OUT = ( 854 M0-1 QM801 Q2-3 ) \ \ BLOCK BLKID = M801FLSH BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 571 M0-1 QM801 Q1-2 ) OUT = ( 851 M0-1 571A M1-2 ) \ \ BLOCK BLKID = M801CND BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 851 M0-1 ) OUT = ( 852 M0-1 QM801B Q2-3 ) \ \ BLOCK BLKID = "H801+" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 804D M0-1 ) OUT = ( 809A M0-1 QH801 Q2-3 ) \ \ BLOCK BLKID = M803HEAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 804C M0-1 QM803 Q1-2 ) OUT = ( 804D M0-1 QM803T Q2-3 ) \ \ BLOCK BLKID = M804 BLKTYPE = SSPLIT MDLTYPE = "SSplit" IN = ( 809A M0-1 ) OUT = ( 810 M0-1 809 M0-1 ) \ \ BLOCK BLKID = QCOMSPLT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( QM803T Q1-2 ) OUT = ( QCOMLOSS Q1-4 QBOILER Q1-4 ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS FLOWSHEET MODELS THE FUEL AND GAS SIDE OF THE BOILER." ) \ ? FLOWSHEET A810 ? \ BLOCK BLKID = P826AS BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 813 M0-1 ) OUT = ( 813A M0-1 WP826 W2-3 ) \ \ BLOCK BLKID = "H811+" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 813A M0-1 QH811B Q1-2 ) OUT = ( 813B M0-1 QH811 Q2-3 ) \ \ BLOCK BLKID = M803BD BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 813B M0-1 QBOILER Q1-2 ) OUT = ( 813C M0-1 821 M1-2 QSUPER Q3-4 ) \ \ BLOCK BLKID = M803SHTR BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 813C M0-1 QSUPER Q1-2 ) OUT = ( 812 M0-1 QM803EX Q2-3 ) \ \ BLOCK BLKID = M811XSPT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 812 M0-1 ) OUT = ( 812C M0-1 812D M0-1 ) \ \ BLOCK BLKID = M811HTRB BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 812C M0-1 ) OUT = ( 812A M0-1 WM811H W2-3 ) \ \ BLOCK BLKID = M811HSPT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 812A M0-1 ) OUT = ( 812B M0-1 814 M0-1 814A M0-1 ) \ \ BLOCK BLKID = M811ITRB BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 814A M0-1 ) OUT = ( 814B M0-1 WM811I W2-3 ) \ \ BLOCK BLKID = M811ISPT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 814B M0-1 ) OUT = ( 815A M0-1 815B M0-1 815 M0-1 ) \ \ BLOCK BLKID = M811LTRB BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 815B M0-1 ) OUT = ( 815C M0-1 WM811L W2-3 ) \ \ BLOCK BLKID = M811LSPT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 815C M0-1 ) OUT = ( 815D M0-1 860 M0-1 ) \ \ BLOCK BLKID = E501LB BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 860 M0-1 ) OUT = ( 861 M0-1 QE501A2 Q2-3 ) \ \ BLOCK BLKID = M811VLRB BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 815D M0-1 ) OUT = ( 815E M0-1 WM811VL W2-3 ) \ \ BLOCK BLKID = T824AS BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 816A M0-1 823 M0-1 824 M0-1 ) OUT = ( 811A M0-1 ) \ \ BLOCK BLKID = P824AS BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 811 M0-1 811A M0-1 ) OUT = ( 811B M0-1 WP824 W2-3 ) \ \ BLOCK BLKID = T826 BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 811B M0-1 815A M0-1 ) OUT = ( 812E M0-1 813 M1-2 QDEAER Q3-4 ) \ \ BLOCK BLKID = "H811-A" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 812B M0-1 QH811 Q1-2 ) OUT = ( 819 M0-1 QH811EX Q2-3 ) \ \ BLOCK BLKID = "H811-B" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 819 M0-1 ) OUT = ( 823 M0-1 QH811B Q2-3 ) \ \ BLOCK BLKID = M811CND BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 815E M0-1 ) OUT = ( 816 M0-1 QM811 Q2-3 ) \ \ BLOCK BLKID = P811AS BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 816 M0-1 ) OUT = ( 816A M0-1 WP811 W2-3 ) \ \ BLOCK BLKID = M811GEN BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( WM811L W2-3 WM811I W2-3 WM811H W2-3 WM811VL W2-3 ) OUT = ( WLOST W2-7 WTOTAL W2-7 ) \ \ BLOCK BLKID = MPOW8 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WM801 W2-7 WM804 W2-7 WM830 W2-7 WM832 W2-7 WM834 W2-7 ) OUT = ( WMP8 W2-4 ) \ \ BLOCK BLKID = STMMAN BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 890 M0-1 891 M0-1 892 M0-1 ) OUT = ( 895 M0-1 894 M1-2 ) \ \ BLOCK BLKID = STMHX BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 895 M0-1 QTSTM Q1-2 ) OUT = ( 896 M0-1 QTSTMXS Q2-3 ) \ \ BLOCK BLKID = STMDMD BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QRD501 Q1-4 QH506 Q1-4 QH301 Q1-4 QRD502 Q1-4 ) OUT = ( QTSTM Q1-3 ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS FLOWSHEET MODELS THE STEAM SIDE OF THE BOILER/TURBOGENERATOR." ) \ ? FLOWSHEET A900 ? \ BLOCK BLKID = SSCFCW BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QF300B Q1-4 QF300CNT Q1-4 ) OUT = ( QF300 Q1-3 ) \ \ BLOCK BLKID = CHCWDUP BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( QH914 Q1-2 ) OUT = ( QH914A Q1-2 QH914B Q1-2 QH914C Q1-2 ) \ \ BLOCK BLKID = SSCFSDCW BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QF301-6B" Q1-4 ) OUT = ( QF301 Q1-3 ) \ \ BLOCK BLKID = QH14BSP BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( QH914B Q1-2 ) OUT = ( QH14BCW Q1-4 QH14BCHW Q1-4 ) \ \ BLOCK BLKID = "HEATCW-S" BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QH602 Q1-4 QM811 Q1-4 QM205 Q1-4 QM401 Q1-4 QM505 Q1-4 QH503 Q1-4 QM801B Q1-4 QH509 Q1-4 QH517 Q1-4 QH200 Q1-4 QCD501 Q1-4 QH415 Q1-4 QH205 Q1-4 QH244 Q1-4 QF300A Q1-4 QH302 Q1-4 ) OUT = ( QTTOTAL Q1-3 ) \ \ BLOCK BLKID = QTDUP BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( QTTOTAL Q1-2 ) OUT = ( QTTOTA Q1-2 QTTOTB Q1-2 QTTOTC Q1-2 ) \ \ BLOCK BLKID = QCWMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QH914A Q1-4 QTTOTA Q1-4 QC502B Q1-4 ) OUT = ( QCWCAP Q1-3 ) \ \ BLOCK BLKID = CWATCAP BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 945 M0-1 QCWCAP Q1-2 ) OUT = ( 940 M0-1 QTTOTXS Q2-3 ) \ \ BLOCK BLKID = CWDUP BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( QH14BCW Q1-2 ) OUT = ( QH14CWA Q1-2 QH14CWB Q1-2 ) \ \ BLOCK BLKID = CWATOP BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 946 M0-1 QTTOTB Q1-2 QH14CWA Q1-2 ) OUT = ( 947 M0-1 QTTOTXB Q2-3 ) \ \ BLOCK BLKID = CWFLSH BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 948 M0-1 QTTOTC Q1-2 QH14CWB Q1-2 ) OUT = ( 949 M0-1 QCWFLXS Q2-3 ) \ \ BLOCK BLKID = CLTWR BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 941 M0-1 942 M0-1 944A M0-1 ) OUT = ( 941A M0-1 ) \ \ BLOCK BLKID = CHEMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 921 M0-1 922 M0-1 ) OUT = ( 923 M0-1 ) \ \ BLOCK BLKID = "HEATCHW-" BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QF401-4" Q1-4 QF400 Q1-4 ) OUT = ( QCHWTOT Q1-3 ) \ \ BLOCK BLKID = CHWDUP BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( QCHWTOT Q1-2 ) OUT = ( QCHWTOTA Q1-2 QCHWTOTB Q1-2 ) \ \ BLOCK BLKID = QCHWMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QCHWTOTA Q1-4 QH914C Q1-4 ) OUT = ( QCHWCAP Q1-3 ) \ \ BLOCK BLKID = CHILWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 950A M0-1 QCHWCAP Q1-2 ) OUT = ( 951A M0-1 QCHILXS Q2-3 ) \ \ BLOCK BLKID = QCHWMX2 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QCHWTOTB Q1-4 QH14BCHW Q1-4 ) OUT = ( QCHWOP Q1-3 ) \ \ BLOCK BLKID = CHILOP BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 950 M0-1 QCHWOP Q1-2 ) OUT = ( 951 M0-1 QCHWXS Q2-3 ) \ \ BLOCK BLKID = PMPWK BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WP101 W2-7 WP102 W2-7 WP103 W2-7 WP104 W2-7 WP105 W2-7 WP201 W2-7 WP224 W2-7 WP209 W2-7 WP222 W2-7 WP239 W2-7 WP205 W2-7 WP211 W2-7 WP213 W2-7 WP300 W2-7 WP301 W2-7 WP302 W2-7 WP306 W2-7 WP310 W2-7 WP400 W2-7 WP405 W2-7 WP420 W2-7 WP401 W2-7 WP501 W2-7 WP504 W2-7 WP514 W2-7 WP503 W2-7 WP505 W2-7 WP511 W2-7 WP512 W2-7 WP513 W2-7 WP515 W2-7 WP530 W2-7 WP611 W2-7 WP602 W2-7 WP606 W2-7 WP608 W2-7 WP610 W2-7 WP614 W2-7 WP616 W2-7 WP701 W2-7 WP703 W2-7 WP704 W2-7 WP706 W2-7 WP707 W2-7 WP708 W2-7 WP710 W2-7 WP720 W2-7 WP750 W2-7 WP760 W2-7 WP804 W2-7 WP828 W2-7 WP830 W2-7 WP824 W2-7 WP826 W2-7 WP811 W2-7 WP902 W2-7 WP912 W2-7 WP914 W2-7 ) OUT = ( WPTOTL W2-4 ) \ \ BLOCK BLKID = COMPWK BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WM401 W2-7 WCOMBFAN W2-7 ) OUT = ( WCMPTOT W2-4 ) \ \ BLOCK BLKID = ACOMP BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 440 M0-1 ) OUT = ( 441 M0-1 WM401 W2-3 ) \ \ BLOCK BLKID = AFLSH BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 441 M0-1 ) OUT = ( 443 M0-1 QM401 Q2-3 ) \ \ BLOCK BLKID = ASPLT BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 443 M0-1 ) OUT = ( 432 M0-1 413 M0-1 ) \ \ BLOCK BLKID = AGITAT BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WT224 W2-7 WT209 W2-7 WT232 W2-7 WT205 W2-7 WT300 W2-7 WT301 W2-7 WT304 W2-7 WT305 W2-7 WT306 W2-7 WT310 W2-7 WT400 W2-7 "WT402-3" W2-7 WT405 W2-7 WT530 W2-7 WT602 W2-7 WT606 W2-7 WT608 W2-7 WT720 W2-7 WT760 W2-7 ) OUT = ( WMIX W2-4 ) \ \ BLOCK BLKID = WKMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WPTOTL W2-7 WCMPTOT W2-7 WMIX W2-7 WTOTAL W2-7 WMISC W2-7 WM503 W2-7 WPLNTPOW W2-7 WP223 W2-7 WP755 W2-7 WC755 W2-7 ) OUT = ( WKNET W2-4 ) \ \ BLOCK BLKID = CHCWMIX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QF300 Q1-4 QF301 Q1-4 ) OUT = ( QWELL Q1-3 ) \ \ BLOCK BLKID = H914 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 903 M0-1 QWELL Q1-2 ) OUT = ( 904 M0-1 QH914 Q2-3 ) \ \ BLOCK BLKID = T914 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 624 M0-1 943 M0-1 251 M0-1 ) OUT = ( 905 M0-1 ) \ \ BLOCK BLKID = H910 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 906 M0-1 ) OUT = ( 909 M0-1 QH910 Q2-3 ) \ \ BLOCK BLKID = CIPCS BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 914 M0-1 ) OUT = ( 916 M0-1 ) \ \ BLOCK BLKID = MPOW10 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WM902 W2-7 WS904 W2-7 WM908 W2-7 ) OUT = ( WMP10 W2-4 ) \ \ BLOCK BLKID = AIRCMP BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WM205 W2-7 WM505 W2-7 WM904A W2-7 ) OUT = ( WM904 W2-4 ) \ \ BLOCK BLKID = MPOWTOT BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WMP1 W2-7 WMP2 W2-7 WMP5 W2-7 WMP6 W2-7 WMP8 W2-7 WMP10 W2-7 WM910 W2-7 WM904 W2-7 ) OUT = ( WMISC W2-4 ) \ \ BLOCK BLKID = WKSEP BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WKNET W2-7 WTOTAL2 W2-7 ) OUT = ( WPLANT W2-4 ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS FLOWSHEET MODELS THE MISCELLANEOUS UTILITIES" "; Heatcw-s Cooling Water Heat Load accumulator" "; HeatCHW- Chilled Water Heat Load accumulator" ";;" ) \ ? PROPERTIES MAIN ? \ GPROPERTIES GBASEOPSET = NRTL GOPSETNAME = NRTL GHEN = HC PARCON = -1 \ \ PROPERTIES SECID-LIST = A810 BASEOPSET = "STEAM-TA" OPSETNAME = SYSOP12 / SECID-LIST = A800 BASEOPSET = SYSOP0 OPSETNAME = SYSOP0 \ \ X-PROPS BOPSETNAME = "NRTL-HOC" \ \ COMMENTS COMMENTS = ( ";;" ";;" ) \ ? PROPERTIES "OPTION-SETS" NRTL ? \ PARAM BASE = NRTL \ \ MPROP MPROP-NAME = VLMX MROUTEID = VLMX49 \ \ SPROP SPROP-NAME = DHL SROUTEID = DHL09 \ \ COMMENTS COMMENTS = ( ";;" "; Uses Liguid heat capacity equation of DIPPR" ) \ ? PROPERTIES "OPTION-SETS" "NRTL-HOC" ? \ PARAM BASE = "NRTL-HOC" \ ? PROPERTIES "OPTION-SETS" SYSOP12 ? \ PARAM BASE = "STEAM-TA" \ ? PROPERTIES "MOLEC-STRUCT" AACID ? ? PROPERTIES "MOLEC-STRUCT" ACETATE ? ? PROPERTIES "MOLEC-STRUCT" ACETOLIG ? ? PROPERTIES "MOLEC-STRUCT" ARABINAN ? ? PROPERTIES "MOLEC-STRUCT" ARABINOS ? ? PROPERTIES "MOLEC-STRUCT" ARABOLIG ? ? PROPERTIES "MOLEC-STRUCT" ASH ? ? PROPERTIES "MOLEC-STRUCT" BIOMASS ? ? PROPERTIES "MOLEC-STRUCT" C ? ? PROPERTIES "MOLEC-STRUCT" CAH2O2 ? ? PROPERTIES "MOLEC-STRUCT" CASO4 ? ? PROPERTIES "MOLEC-STRUCT" CELLOB ? ? PROPERTIES "MOLEC-STRUCT" CELLULAS ? ? PROPERTIES "MOLEC-STRUCT" CELLULOS ? ? PROPERTIES "MOLEC-STRUCT" CH4 ? ? PROPERTIES "MOLEC-STRUCT" CNUTR ? ? PROPERTIES "MOLEC-STRUCT" CO ? ? PROPERTIES "MOLEC-STRUCT" CO2 ? ? PROPERTIES "MOLEC-STRUCT" CSL ? ? PROPERTIES "MOLEC-STRUCT" DAP ? ? PROPERTIES "MOLEC-STRUCT" DENAT ? ? PROPERTIES "MOLEC-STRUCT" ETHANOL ? ? PROPERTIES "MOLEC-STRUCT" EXTRACT ? ? PROPERTIES "MOLEC-STRUCT" FURFURAL ? ? PROPERTIES "MOLEC-STRUCT" GALACTAN ? ? PROPERTIES "MOLEC-STRUCT" GALACTOS ? ? PROPERTIES "MOLEC-STRUCT" GALAOLIG ? ? PROPERTIES "MOLEC-STRUCT" GLUCOLIG ? ? PROPERTIES "MOLEC-STRUCT" GLUCOSE ? ? PROPERTIES "MOLEC-STRUCT" GLYCEROL ? ? PROPERTIES "MOLEC-STRUCT" GYPSUM ? ? PROPERTIES "MOLEC-STRUCT" H2O ? ? PROPERTIES "MOLEC-STRUCT" H2S ? ? PROPERTIES "MOLEC-STRUCT" H2SO4 ? ? PROPERTIES "MOLEC-STRUCT" HMF ? ? PROPERTIES "MOLEC-STRUCT" LACID ? ? PROPERTIES "MOLEC-STRUCT" LGNSOL ? ? PROPERTIES "MOLEC-STRUCT" LIGNIN ? ? PROPERTIES "MOLEC-STRUCT" MANNAN ? ? PROPERTIES "MOLEC-STRUCT" MANNOSE ? ? PROPERTIES "MOLEC-STRUCT" MANOLIG ? ? PROPERTIES "MOLEC-STRUCT" N2 ? ? PROPERTIES "MOLEC-STRUCT" NH3 ? ? PROPERTIES "MOLEC-STRUCT" NH4ACET ? ? PROPERTIES "MOLEC-STRUCT" NH4OH ? ? PROPERTIES "MOLEC-STRUCT" NH4SO4 ? ? PROPERTIES "MOLEC-STRUCT" NO ? ? PROPERTIES "MOLEC-STRUCT" NO2 ? ? PROPERTIES "MOLEC-STRUCT" O2 ? ? PROPERTIES "MOLEC-STRUCT" OIL ? ? PROPERTIES "MOLEC-STRUCT" PROPANE ? ? PROPERTIES "MOLEC-STRUCT" PROTEIN ? ? PROPERTIES "MOLEC-STRUCT" SO2 ? ? PROPERTIES "MOLEC-STRUCT" SOLSLDS ? ? PROPERTIES "MOLEC-STRUCT" SUCCACID ? ? PROPERTIES "MOLEC-STRUCT" TAR ? ? PROPERTIES "MOLEC-STRUCT" UNKNOWN ? ? PROPERTIES "MOLEC-STRUCT" WNUTR ? ? PROPERTIES "MOLEC-STRUCT" XYLAN ? ? PROPERTIES "MOLEC-STRUCT" XYLITOL ? ? PROPERTIES "MOLEC-STRUCT" XYLOLIG ? ? PROPERTIES "MOLEC-STRUCT" XYLOSE ? ? PROPERTIES "MOLEC-STRUCT" ZYMO ? ? PROPERTIES PARAMETERS UNARY SCALAR DATA1 ? ; "SET1_MOLE" ; \ PROP-LIST PARAMNAME = MW SETNO = 1 UNITROW = 0 \ \ PVAL PARAMNAME2 = MW CID = NH4ACET UVALUE = 77.080 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = NH4OH UVALUE = 35.050 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = GLUCOLIG UVALUE = 162.14240 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = CELLOB UVALUE = 342.30010 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = XYLOLIG UVALUE = 132.116120 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = TAR UVALUE = 150.13140 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = MANOLIG UVALUE = 162.14240 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = GALAOLIG UVALUE = 162.14240 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = ARABOLIG UVALUE = 132.116120 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = XYLITOL UVALUE = 152.150 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? PROPERTIES PARAMETERS UNARY SCALAR DATA2 ? ; "SI_MOLE" ; \ PROP-LIST PARAMNAME = MUP SETNO = 1 UNITROW = 45 UNITLABEL = "(J*cum)**.5" / PARAMNAME = RGYR SETNO = 1 UNITROW = 17 UNITLABEL = meter \ \ PVAL PARAMNAME2 = MUP CID = GLUCOSE UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = XYLOSE UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = SOLSLDS UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = ARABINOS UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = GALACTOS UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = MANNOSE UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = UNKNOWN UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = GLUCOLIG UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = CELLOB UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = XYLOLIG UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = MANOLIG UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = GALAOLIG UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = ARABOLIG UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = ACETOLIG UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = XYLITOL UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = LGNSOL UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = EXTRACT UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = PROTEIN UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = CSL UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = CNUTR UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = WNUTR UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = MUP CID = HMF UVALUE = 5.849340E-25 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = GLUCOSE UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = XYLOSE UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = SOLSLDS UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = ARABINOS UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = GALACTOS UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = MANNOSE UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = UNKNOWN UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = GLUCOLIG UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = CELLOB UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = XYLOLIG UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = MANOLIG UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = GALAOLIG UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = ARABOLIG UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = ACETOLIG UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = XYLITOL UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = LGNSOL UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = EXTRACT UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = PROTEIN UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = CSL UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = CNUTR UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = WNUTR UVALUE = 6.150E-11 <0> <0> \ \ PVAL PARAMNAME2 = RGYR CID = HMF UVALUE = 6.150E-11 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" "; Use water's dipole moment and radius of gyration," "; these properties are important for the vapor fugacity" "; calculation in one block using Hayden & O'Connell." "; These particular components will not be in the vapor" "; phase so their values are unimportant." ) \ ? PROPERTIES PARAMETERS UNARY SCALAR DATA3 ? ; "SI_MOLE" ; \ PROP-LIST PARAMNAME = DHFORM SETNO = 1 UNITROW = 39 UNITLABEL = "J/kmol" \ \ PVAL PARAMNAME2 = DHFORM CID = SOLSLDS UVALUE = 1.10180E+09 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = EXTRACT UVALUE = 1.10180E+09 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = PROTEIN UVALUE = 1.10180E+09 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ";=======================================================================" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/" "; Soluble Solids, Extractives and Protein Info from feedstock analysis" ";***Change DHFORM for SOLSLDS,EXTRACT,PROTEIN WHEN FEED COMP. CHANGES***" "; Heat of Formation" ) \ ? PROPERTIES PARAMETERS UNARY SCALAR "PURE-1" ? ; "SET4_MOLE" ; \ PROP-LIST PARAMNAME = DHFORM SETNO = 1 UNITROW = 39 UNITLABEL = "J/kmol" \ \ PVAL PARAMNAME2 = DHFORM CID = GLUCOSE UVALUE = -1.2485360E+09 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = GALACTOS UVALUE = -1.2615360E+09 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = MANNOSE UVALUE = -1.2382370E+09 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = XYLOSE UVALUE = -1.0377950E+09 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = ARABINOS UVALUE = -1.0377950E+09 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = CELLOB UVALUE = -2.2120470E+09 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = GLUCOLIG UVALUE = -9.7395660E+08 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = GALAOLIG UVALUE = -9.7395660E+08 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = MANOLIG UVALUE = -9.7395660E+08 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = XYLOLIG UVALUE = -7.5921320E+08 <0> <0> \ \ PVAL PARAMNAME2 = DHFORM CID = ARABOLIG UVALUE = -7.5921320E+08 <0> <0> \ \ COMMENTS COMMENTS = ( ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/" ";;" ";=======================================================================" "; Heats of formation for sugars & oligomers to match accepted" "; heats of combusiton values." ";=======================================================================" ";;" ) \ ? PROPERTIES PARAMETERS UNARY SCALAR "PURE-2" ? ; "SET4_MOLE" ; \ PROP-LIST PARAMNAME = HCOM SETNO = 1 UNITROW = 39 UNITLABEL = "J/kmol" \ \ PVAL PARAMNAME2 = HCOM CID = GLUCOSE UVALUE = -2.562940E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = GALACTOS UVALUE = -2.549940E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = MANNOSE UVALUE = -2.573240E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = XYLOSE UVALUE = -2.134670E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = ARABINOS UVALUE = -2.134670E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = CELLOB UVALUE = -5.16960E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = GLUCOLIG UVALUE = -2.595710E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = GALAOLIG UVALUE = -2.595710E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = MANOLIG UVALUE = -2.595710E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = XYLOLIG UVALUE = -2.171440E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = ARABOLIG UVALUE = -2.171440E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = XYLITOL UVALUE = -2.300790E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = CELLULOS UVALUE = -2.593810E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = XYLAN UVALUE = -2.172420E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = LIGNIN UVALUE = -3.651710E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = ARABINAN UVALUE = -2.172420E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = MANNAN UVALUE = -2.593810E+09 <0> <0> \ \ PVAL PARAMNAME2 = HCOM CID = GALACTAN UVALUE = -2.593810E+09 <0> <0> \ ? PROPERTIES PARAMETERS UNARY SCALAR VB ? ; "SI_MOLE" ; \ PROP-LIST PARAMNAME = VB SETNO = 1 UNITROW = 43 UNITLABEL = "cum/kmol" \ \ PVAL PARAMNAME2 = VB CID = GLUCOSE UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = XYLOSE UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = SOLSLDS UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = ARABINOS UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = GALACTOS UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = MANNOSE UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = GLUCOLIG UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = CELLOB UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = XYLOLIG UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = MANOLIG UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = GALAOLIG UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = ARABOLIG UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = XYLITOL UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = LGNSOL UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = EXTRACT UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = PROTEIN UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = CSL UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = CNUTR UVALUE = .01850640 <0> <0> \ \ PVAL PARAMNAME2 = VB CID = WNUTR UVALUE = .01850640 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" "; Needed for tray sizing in RADFRAC" ) \ ? PROPERTIES PARAMETERS UNARY "T-DEPENDENT" "MULDIP-1" ? ; "SET3_MOLE" ; \ PROP-LIST PARAMNAME = MULDIP SETNO = 1 UNITROW = 26 UNITLABEL = cP TUNITROW = 22 TUNITLABEL = C NEL = 7 \ \ PVAL PARAMNAME2 = MULDIP CID = XYLOSE UNITROW2 = 26 UNITLABEL2 = cP TUNITROW2 = 22 TUNITLABEL2 = C NEL2 = 7 UVAL1 = -2267.40 <0> <0> UVAL2 = 138910.0 <0> <0> UVAL3 = 320.550 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 0.0 <0> <0> UVAL6 = 323.150 <0> <0> UVAL7 = 418.150 <0> <0> \ \ PVAL PARAMNAME2 = MULDIP CID = SOLSLDS UNITROW2 = 26 UNITLABEL2 = cP TUNITROW2 = 22 TUNITLABEL2 = C NEL2 = 7 UVAL1 = -2267.40 <0> <0> UVAL2 = 138910.0 <0> <0> UVAL3 = 320.550 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 0.0 <0> <0> UVAL6 = 323.0 <0> <0> UVAL7 = 418.0 <0> <0> \ \ PVAL PARAMNAME2 = MULDIP CID = ARABINOS UNITROW2 = 26 UNITLABEL2 = cP TUNITROW2 = 22 TUNITLABEL2 = C NEL2 = 7 UVAL1 = -2267.40 <0> <0> UVAL2 = 138900.0 <0> <0> UVAL3 = 320.0 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 0.0 <0> <0> UVAL6 = 323.0 <0> <0> UVAL7 = 418.0 <0> <0> \ \ PVAL PARAMNAME2 = MULDIP CID = XYLOLIG UNITROW2 = 26 UNITLABEL2 = cP TUNITROW2 = 22 TUNITLABEL2 = C NEL2 = 7 UVAL1 = -2267.40 <0> <0> UVAL2 = 138900.0 <0> <0> UVAL3 = 320.0 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 0.0 <0> <0> UVAL6 = 323.0 <0> <0> UVAL7 = 418.0 <0> <0> \ \ PVAL PARAMNAME2 = MULDIP CID = ARABOLIG UNITROW2 = 26 UNITLABEL2 = cP TUNITROW2 = 22 TUNITLABEL2 = C NEL2 = 7 UVAL1 = -2267.40 <0> <0> UVAL2 = 138900.0 <0> <0> UVAL3 = 320.0 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 0.0 <0> <0> UVAL6 = 323.0 <0> <0> UVAL7 = 418.0 <0> <0> \ \ PVAL PARAMNAME2 = MULDIP CID = XYLITOL UNITROW2 = 26 UNITLABEL2 = cP TUNITROW2 = 22 TUNITLABEL2 = C NEL2 = 7 UVAL1 = -2267.40 <0> <0> UVAL2 = 138900.0 <0> <0> UVAL3 = 320.0 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 0.0 <0> <0> UVAL6 = 323.0 <0> <0> UVAL7 = 418.0 <0> <0> \ \ PVAL PARAMNAME2 = MULDIP CID = LGNSOL UNITROW2 = 26 UNITLABEL2 = cP TUNITROW2 = 22 TUNITLABEL2 = C NEL2 = 7 UVAL1 = -2267.40 <0> <0> UVAL2 = 138910.0 <0> <0> UVAL3 = 320.550 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 0.0 <0> <0> UVAL6 = 323.150 <0> <0> UVAL7 = 418.150 <0> <0> \ \ PVAL PARAMNAME2 = MULDIP CID = EXTRACT UNITROW2 = 26 UNITLABEL2 = cP TUNITROW2 = 22 TUNITLABEL2 = C NEL2 = 7 UVAL1 = -2267.40 <0> <0> UVAL2 = 138910.0 <0> <0> UVAL3 = 320.550 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 0.0 <0> <0> UVAL6 = 323.0 <0> <0> UVAL7 = 418.0 <0> <0> \ \ PVAL PARAMNAME2 = MULDIP CID = PROTEIN UNITROW2 = 26 UNITLABEL2 = cP TUNITROW2 = 22 TUNITLABEL2 = C NEL2 = 7 UVAL1 = -2267.40 <0> <0> UVAL2 = 138910.0 <0> <0> UVAL3 = 320.550 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 0.0 <0> <0> UVAL6 = 323.0 <0> <0> UVAL7 = 418.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" "; Needed for Tray sizing in RADFRAC" ) \ ? PROPERTIES PARAMETERS BINARY SCALAR "HOCETA-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = HOCETA SETNO = 1 \ ? PROPERTIES PARAMETERS BINARY SCALAR "RKTKIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = RKTKIJ SETNO = 1 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "ANDKIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = ANDKIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F NEL = 2 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "ANDMIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = ANDMIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F NEL = 2 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "HENRY-1" ? ; "SET5_MOLE" ; \ PROP-LIST PARAMNAME = HENRY SETNO = 1 UNITROW = 20 UNITLABEL = bar TUNITROW = 22 TUNITLABEL = C NEL = 7 \ \ BPVAL PARAMNAME2 = HENRY CID1 = CH4 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -9.7921450 <0> <0> UVAL2 = 307.780 <0> <0> UVAL3 = 2.70770 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 10.0 <0> <0> UVAL6 = 30.0 <0> <0> / PARAMNAME2 = HENRY CID1 = CH4 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 212.57410 <0> <0> UVAL2 = -10429.0 <0> <0> UVAL3 = -29.2420 <0> <0> UVAL4 = -.0012910 <0> <0> UVAL5 = 2.310 <0> <0> UVAL6 = 55.0 <0> <0> / PARAMNAME2 = HENRY CID1 = CO2 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 89.583080 <0> <0> UVAL2 = -5018.80 <0> <0> UVAL3 = -11.8910 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 10.0 <0> <0> UVAL6 = 40.0 <0> <0> / PARAMNAME2 = HENRY CID1 = O2 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -30.297630 <0> <0> UVAL2 = 651.840 <0> <0> UVAL3 = 7.02120 <0> <0> UVAL4 = -.0149260 <0> <0> UVAL5 = -25.0 <0> <0> UVAL6 = 50.0 <0> <0> / PARAMNAME2 = HENRY CID1 = N2 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -1.9301950 <0> <0> UVAL2 = -22.0820 <0> <0> UVAL3 = 2.20610 <0> <0> UVAL4 = -.008830 <0> <0> UVAL5 = -60.0 <0> <0> UVAL6 = 50.0 <0> <0> / PARAMNAME2 = HENRY CID1 = CO2 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 181.18610 <0> <0> UVAL2 = -8982.0 <0> <0> UVAL3 = -25.8460 <0> <0> UVAL4 = .0121280 <0> <0> UVAL5 = .20000610 <0> <0> UVAL6 = 74.70 <0> <0> / PARAMNAME2 = HENRY CID1 = O2 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 216.59310 <0> <0> UVAL2 = -9622.0 <0> <0> UVAL3 = -31.1070 <0> <0> UVAL4 = .0121090 <0> <0> UVAL5 = .000006103520 <0> <0> UVAL6 = 90.0 <0> <0> / PARAMNAME2 = HENRY CID1 = N2 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -21.862430 <0> <0> UVAL2 = -2953.50 <0> <0> UVAL3 = 10.3960 <0> <0> UVAL4 = -.0540060 <0> <0> UVAL5 = .000006103520 <0> <0> UVAL6 = 72.50 <0> <0> / PARAMNAME2 = HENRY CID1 = N2 CID2 = FURFURAL UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -1.9433580 <0> <0> UVAL2 = -22.0820 <0> <0> UVAL3 = 2.20610 <0> <0> UVAL4 = -.008830 <0> <0> UVAL5 = 213.150 <0> <0> UVAL6 = 323.150 <0> <0> / PARAMNAME2 = HENRY CID1 = O2 CID2 = FURFURAL UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -30.310790 <0> <0> UVAL2 = 651.840 <0> <0> UVAL3 = 7.02120 <0> <0> UVAL4 = -.0149260 <0> <0> UVAL5 = 248.150 <0> <0> UVAL6 = 323.150 <0> <0> / PARAMNAME2 = HENRY CID1 = CH4 CID2 = FURFURAL UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -9.7921450 <0> <0> UVAL2 = 307.780 <0> <0> UVAL3 = 2.70770 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 10.0 <0> <0> UVAL6 = 30.0 <0> <0> / PARAMNAME2 = HENRY CID1 = CO2 CID2 = FURFURAL UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 89.583080 <0> <0> UVAL2 = -5018.80 <0> <0> UVAL3 = -11.8910 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 10.0 <0> <0> UVAL6 = 40.0 <0> <0> / PARAMNAME2 = HENRY CID1 = N2 CID2 = HMF UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -1.9433580 <0> <0> UVAL2 = -22.0820 <0> <0> UVAL3 = 2.20610 <0> <0> UVAL4 = -.008830 <0> <0> UVAL5 = 213.150 <0> <0> UVAL6 = 323.150 <0> <0> / PARAMNAME2 = HENRY CID1 = O2 CID2 = HMF UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -30.310790 <0> <0> UVAL2 = 651.840 <0> <0> UVAL3 = 7.02120 <0> <0> UVAL4 = -.0149260 <0> <0> UVAL5 = 248.150 <0> <0> UVAL6 = 323.150 <0> <0> / PARAMNAME2 = HENRY CID1 = CH4 CID2 = HMF UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -9.7921450 <0> <0> UVAL2 = 307.780 <0> <0> UVAL3 = 2.70770 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 10.0 <0> <0> UVAL6 = 30.0 <0> <0> / PARAMNAME2 = HENRY CID1 = CO2 CID2 = HMF UNITROW2 = 20 UNITLABEL2 = bar TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 89.583080 <0> <0> UVAL2 = -5018.80 <0> <0> UVAL3 = -11.8910 <0> <0> UVAL4 = 0.0 <0> <0> UVAL5 = 10.0 <0> <0> UVAL6 = 40.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";=======================================================================" "; Henry component parameters (Non-condensible <==> solvent)" "; New Parameters for N2 and O2 taken from version 9.2 to improve" "; the calculations involving these two components." ";=======================================================================" ";;" ";;" "; Using ethanol Henry's for FURFURAL & HMF" ";;" ) \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "MRKKIJ-1" ? ; "SET1_MOLE" ; \ PROP-LIST PARAMNAME = MRKKIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = C NEL = 3 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "NRTL-1" ? ; "SET3_MOLE" ; \ PROP-LIST PARAMNAME = NRTL SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = C NEL = 12 \ \ BPVAL PARAMNAME2 = NRTL CID1 = ETHANOL CID2 = H2O UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 0.0 <0> <0> UVAL2 = 0.0 <0> <0> UVAL3 = -55.16980 <0> <0> UVAL4 = 670.44420 <0> <0> UVAL5 = .30310 <0> <0> UVAL6 = 0.0 <0> <0> UVAL7 = 0.0 <0> <0> UVAL8 = 0.0 <0> <0> UVAL9 = 0.0 <0> <0> UVAL10 = 0.0 <0> <0> UVAL11 = 75.0 <0> <0> UVAL12 = 100.0 <0> <0> / PARAMNAME2 = NRTL CID1 = ETHANOL CID2 = FURFURAL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 0.0 <0> <0> UVAL2 = 0.0 <0> <0> UVAL3 = 139.60130 <0> <0> UVAL4 = 425.89810 <0> <0> UVAL5 = .30 <0> <0> UVAL6 = 0.0 <0> <0> UVAL7 = 0.0 <0> <0> UVAL8 = 0.0 <0> <0> UVAL9 = 0.0 <0> <0> UVAL10 = 0.0 <0> <0> UVAL11 = 75.0 <0> <0> UVAL12 = 135.0 <0> <0> / PARAMNAME2 = NRTL CID1 = H2O CID2 = FURFURAL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 0.0 <0> <0> UVAL2 = 0.0 <0> <0> UVAL3 = 1309.6940 <0> <0> UVAL4 = 219.89050 <0> <0> UVAL5 = .39580 <0> <0> UVAL6 = 0.0 <0> <0> UVAL7 = 0.0 <0> <0> UVAL8 = 0.0 <0> <0> UVAL9 = 0.0 <0> <0> UVAL10 = 0.0 <0> <0> UVAL11 = 95.0 <0> <0> UVAL12 = 140.0 <0> <0> / PARAMNAME2 = NRTL CID1 = ETHANOL CID2 = GLYCEROL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 0.0 <0> <0> UVAL2 = 0.0 <0> <0> UVAL3 = 384.16910 <0> <0> UVAL4 = 208.73190 <0> <0> UVAL5 = .61450 <0> <0> UVAL6 = 0.0 <0> <0> UVAL7 = 0.0 <0> <0> UVAL8 = 0.0 <0> <0> UVAL9 = 0.0 <0> <0> UVAL10 = 0.0 <0> <0> UVAL11 = 50.0 <0> <0> UVAL12 = 50.0 <0> <0> / PARAMNAME2 = NRTL CID1 = H2O CID2 = GLYCEROL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -1.25150 <0> <0> UVAL2 = -.73180 <0> <0> UVAL3 = 272.60750 <0> <0> UVAL4 = 170.91670 <0> <0> UVAL5 = .30 <0> <0> UVAL6 = 0.0 <0> <0> UVAL7 = 0.0 <0> <0> UVAL8 = 0.0 <0> <0> UVAL9 = 0.0 <0> <0> UVAL10 = 0.0 <0> <0> UVAL11 = 25.0 <0> <0> UVAL12 = 290.0 <0> <0> / PARAMNAME2 = NRTL CID1 = H2O CID2 = NH3 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = -6.26840 <0> <0> UVAL2 = 9.61210 <0> <0> UVAL3 = 1525.4540 <0> <0> UVAL4 = -3232.8160 <0> <0> UVAL5 = .30 <0> <0> UVAL6 = 0.0 <0> <0> UVAL7 = 0.0 <0> <0> UVAL8 = 0.0 <0> <0> UVAL9 = 0.0 <0> <0> UVAL10 = 0.0 <0> <0> UVAL11 = 10.0 <0> <0> UVAL12 = 91.50 <0> <0> / PARAMNAME2 = NRTL CID1 = ETHANOL CID2 = OIL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 0.0 <0> <0> UVAL2 = 0.0 <0> <0> UVAL3 = 490.98060 <0> <0> UVAL4 = -172.87780 <0> <0> UVAL5 = .29880 <0> <0> UVAL6 = 0.0 <0> <0> UVAL7 = 0.0 <0> <0> UVAL8 = 0.0 <0> <0> UVAL9 = 0.0 <0> <0> UVAL10 = 0.0 <0> <0> UVAL11 = 45.0 <0> <0> UVAL12 = 45.0 <0> <0> / PARAMNAME2 = NRTL CID1 = H2O CID2 = HMF UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = .3791796770 <0> <0> UVAL2 = -.9418711160 <0> <0> UVAL3 = 1788.4839660 <0> <0> UVAL4 = -288.70228150 <0> <0> UVAL5 = .2372956960 <0> <0> UVAL6 = 0.0 <0> <0> UVAL7 = 0.0 <0> <0> UVAL8 = 0.0 <0> <0> UVAL9 = 0.0 <0> <0> UVAL10 = 0.0 <0> <0> UVAL11 = 90.0 <0> <0> UVAL12 = 140.0 <0> <0> / PARAMNAME2 = NRTL CID1 = ETHANOL CID2 = HMF UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C UVAL1 = 0.0 <0> <0> UVAL2 = 0.0 <0> <0> UVAL3 = 405.27147860 <0> <0> UVAL4 = -218.05936270 <0> <0> UVAL5 = .30 <0> <0> UVAL6 = 0.0 <0> <0> UVAL7 = 0.0 <0> <0> UVAL8 = 0.0 <0> <0> UVAL9 = 0.0 <0> <0> UVAL10 = 0.0 <0> <0> UVAL11 = 75.0 <0> <0> UVAL12 = 135.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ";========================================================================" "; NRTL Binary Parameters generated by Aspen Plus Release 9.1-3" ";========================================================================" ";;" "; Added in W9806C 6/15/98 - ""Lit."" values from ASPEN 9.2" ";;" ) \ ? "PROP-SET" MAIN COMP1 ? ; "SET1_MOLE" ; \ P1 ID = MASSFLOW \ \ P2 SUBSTREAM = MIXED SYSPRES = YES \ ? "PROP-SET" MAIN COMP2 ? ; "SET1_MOLE" ; \ P1 ID = MASSFLOW \ \ P2 SUBSTREAM = CISOLID SYSPRES = YES \ ? "PROP-SET" MAIN CP1 ? ; "SET1_MOLE" ; \ P1 ID = CPMX \ \ P2 SUBSTREAM = MIXED SYSPRES = YES \ \ COMMENTS COMMENTS = ( ";;" ";Heat capacity" ) \ ? "PROP-SET" MAIN CP2 ? ; "SET1_MOLE" ; \ P1 ID = CPMX \ \ P2 SUBSTREAM = CISOLID SYSPRES = YES \ ? "PROP-SET" MAIN FRAC ? ; "SET1_MOLE" ; \ P1 ID = MOLEFLOW \ \ P2 SUBSTREAM = MIXED PHASE = ( L V ) SYSPRES = YES \ ? "PROP-SET" MAIN MASSFLW ? ; "SET1_MOLE" ; \ P1 ID = MASSFLMX UNITS = ( "kg/hr" ) \ \ P2 SUBSTREAM = ALL SYSPRES = YES \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 101 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 24582. <-80> <0> JUNK = 4 \ \ SUBSTREAM SSID = CISOLID TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 73458.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 8 \ \ MOLE-FLOW SSID1 = MIXED CID = SOLSLDS FLOW = 4342.0 <-80> <3> / SSID1 = MIXED CID = EXTRACT FLOW = 2167.0 <-80> <3> / SSID1 = MIXED CID = PROTEIN FLOW = 3367.0 <-80> <3> / SSID1 = MIXED CID = H2O FLOW = 14706.0 <-80> <3> / SSID1 = CISOLID CID = CELLULOS FLOW = .42030 <-3> <0> / SSID1 = CISOLID CID = XYLAN FLOW = .2260 <-3> <0> / SSID1 = CISOLID CID = LIGNIN FLOW = .20610 <-3> <0> / SSID1 = CISOLID CID = ACETATE FLOW = .02680 <-3> <0> / SSID1 = CISOLID CID = ARABINAN FLOW = .02870 <-3> <0> / SSID1 = CISOLID CID = MANNAN FLOW = .01510 <-3> <0> / SSID1 = CISOLID CID = GALACTAN FLOW = .01820 <-3> <0> / SSID1 = CISOLID CID = ASH FLOW = .05880 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";=======================================================================" "; Streams" ";=======================================================================" ";;" ";FEED STREAM calculated by FEEDPROP" ) \ ? STREAM MATERIAL 102B ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 73.92950 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 30587.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = .990 <-3> <0> / SSID1 = MIXED CID = AACID FLOW = .010 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" "; TEAR STREAM -- INITIAL GUESS" ) \ ? STREAM MATERIAL 107 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 5.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = WNUTR FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" "; POLYMER FOR CLARIFIER / BELT PRESS" "; CONTROLLED BY POLY1" ) \ ? STREAM MATERIAL 211 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 73.480 <22> <4> PRES = 3.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 99224.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 3 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = .99020 <-3> <0> / SSID1 = MIXED CID = FURFURAL FLOW = .00180 <-3> <0> / SSID1 = MIXED CID = AACID FLOW = .0080 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";RECYCLE WATER TO PRETREATMENT (A-201)" ";CONTROLLED BY RECYCLE" ) \ ? STREAM MATERIAL 212 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 3.40229820 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 500.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2SO4 FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";INLET ACID STREAM" ) \ ? STREAM MATERIAL 215 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 163.5110 <22> <4> PRES = 4.42290 <20> <3> BASIS = "MASS-FLOW" TOTAL = 19400. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 19400.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";MEDIUM PRESSURE STEAM TO M202LO IN PRETREATMENT" ";CONTROLLED BY DESIGN SPEC LPSTMFLO" ) \ ? STREAM MATERIAL 216 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 268.18930 <22> <4> PRES = 13.0 <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTFLOW = 42638.0 <-80> <3> NPHASE = 2 TOTAL = 42662. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 42662.0 <-80> <3> \ \ COMMENTS COMMENTS = ( "; SUBSTREAM MIXED PRES=13.0 TEMP=268.1893 &" "; MASS-FLOW=11600.0 NPHASE=2" "; MASS-FRAC H2O 1.0" ";;" ";HIGH PRESSURE STEAM TO RAISE PRETREATMENT REACTOR" ";TO REACTION TEMPERATURE" ";CONTROLLED BY DESIGN SPEC REACHEAT" ) \ ? STREAM MATERIAL 219 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 127700.0 <-80> <3> NPHASE = 1 PHASE = L TOTAL = 1. <-3> <0> JUNK = 3 \ \ SUBSTREAM SSID = CISOLID TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 327.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = .99090 <-3> <0> / SSID1 = MIXED CID = LACID FLOW = .00550 <-3> <0> / SSID1 = MIXED CID = AACID FLOW = .00360 <-3> <0> / SSID1 = CISOLID CID = LIGNIN FLOW = .330 <-3> <0> / SSID1 = CISOLID CID = CELLULAS FLOW = .330 <-3> <0> / SSID1 = CISOLID CID = ZYMO FLOW = .340 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";RECYCLE WATER TO BLOWDOWN TANK" ";CONTROLLED BY RECYCLE" ) \ ? STREAM MATERIAL 227 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 987.30 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ MOLE-FLOW SSID1 = CISOLID CID = CAH2O2 FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";LIME FOR OVERLIMING" ";Controlled by Fortran OLIME" ) \ ? STREAM MATERIAL 233 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 3.40229820 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 421.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2SO4 FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";H2SO4 FOR REACIDIFYING" ";Controlled by Fortran REACID" ) \ ? STREAM MATERIAL 257 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 25.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MOLE TOTFLOW = 2360.0 <-89> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = .790 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .210 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 303A ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 37.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 10000. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 10000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; initial value entered to prevent errors with FERMDAP & FERMCSL" ) \ ? STREAM MATERIAL 304A ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 37.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 100000. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 100000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; initial value entered to prevent errors with FERMDAP & FERMCSL" ) \ ? STREAM MATERIAL 310 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 500. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = DAP FLOW = 500.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 310A ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 850. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = CSL FLOW = 850.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 311 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 500. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = DAP FLOW = 500.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 311A ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 5116. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = CSL FLOW = 5116.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 312 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 9167. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 833. <-80> <0> JUNK = 1 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 9167.0 <-80> <3> / SSID1 = CISOLID CID = CELLULAS FLOW = 833.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Cellulase to saccharification T310" ) \ ? STREAM MATERIAL 411 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 22703.0 <-80> <3> NPHASE = 1 PHASE = L TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 58.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> / SSID1 = CISOLID CID = LIGNIN FLOW = .340 <-3> <0> / SSID1 = CISOLID CID = CELLULAS FLOW = .330 <-3> <0> / SSID1 = CISOLID CID = ZYMO FLOW = .330 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";RECYCLE WATER STREAM TO CELLULASE FERMENTORS" ";CONTROLLED BY RECYCLE" ) \ ? STREAM MATERIAL 414 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 463. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = CSL FLOW = 463.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";CSL FOR CELLULASE PRODUCTION" ";CONTROLLED BY FORTRAN CSL-ENZY" ) \ ? STREAM MATERIAL 415 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 200. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = CNUTR FLOW = 200.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";NUTRIENT STREAM FOR CELLULASE PRODUCTION" ";CONTROLLED BY FORTRAN CSL-ENZY" ) \ ? STREAM MATERIAL 417 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 238. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = OIL FLOW = 238.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";ANTI-FOAM STREAM FOR CALCULATING STORAGE TANK" ";CONTROLLED BY FORTRAN CSL-ENZY" ) \ ? STREAM MATERIAL 423 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 30.5 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = CSL FLOW = 30.50 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";CSL FOR CELLULASE SEED PRODUCTION" ";CONTROLLED BY FORTRAN CSL-ENZY" ) \ ? STREAM MATERIAL 430 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 2143.0 <-80> <3> NPHASE = 1 PHASE = L TOTAL = 1. <-3> <0> JUNK = 3 \ \ SUBSTREAM SSID = CISOLID TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 5.50 <-80> <3> TOTAL = 1.0000844 <-3> <0> JUNK = 4 \ \ MOLE-FLOW SSID1 = MIXED CID = XYLOSE FLOW = .00520 <-3> <0> / SSID1 = MIXED CID = SOLSLDS FLOW = .0110 <-3> <0> / SSID1 = MIXED CID = H2O FLOW = .98380 <-3> <0> / SSID1 = CISOLID CID = CELLULOS FLOW = .0150 <-3> <0> / SSID1 = CISOLID CID = LIGNIN FLOW = .070 <-3> <0> / SSID1 = CISOLID CID = BIOMASS FLOW = .00008440 <-3> <0> / SSID1 = CISOLID CID = GYPSUM FLOW = .9150 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";RECYCLE STREAM FOR CELLULASE SEED PRODUCTION" ";CONTROLLED BY RECYCLE" ) \ ? STREAM MATERIAL 432A ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = .150 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 3 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = .20 <-3> <0> / SSID1 = MIXED CID = N2 FLOW = .60 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .20 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";TEAR STREAM INITIAL GUESS" ) \ ? STREAM MATERIAL 434 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 16.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = NH3 FLOW = .50 <-3> <0> / SSID1 = MIXED CID = SO2 FLOW = .50 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 436 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 162.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = NH3 FLOW = .50 <-3> <0> / SSID1 = MIXED CID = SO2 FLOW = .50 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 440 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 126347.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = .790 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .210 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 441 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 152.60 <22> <4> PRES = 2.70 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = .0020 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = .790 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .210 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 501 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 30.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 380640.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 3 \ \ SUBSTREAM SSID = CISOLID TEMP = 30.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 31667.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ MOLE-FLOW SSID1 = MIXED CID = ETHANOL FLOW = .040 <-3> <0> / SSID1 = MIXED CID = H2O FLOW = .95870 <-3> <0> / SSID1 = MIXED CID = OIL FLOW = .00130 <-3> <0> / SSID1 = CISOLID CID = CELLULOS FLOW = .180 <-3> <0> / SSID1 = CISOLID CID = LIGNIN FLOW = .820 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 508 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 59.90 <22> <4> PRES = 1.860 <20> <3> BASIS = "MASS-FLOW" TOTAL = 491. <-80> <0> JUNK = 3 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = ETHANOL FLOW = 60.0 <-80> <3> / SSID1 = MIXED CID = H2O FLOW = 20.0 <-80> <3> / SSID1 = MIXED CID = CO2 FLOW = 411.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";TEAR STREAM INITIAL GUESS" ) \ ? STREAM MATERIAL 514 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 116.0 <22> <4> VFRAC = 1.0 <0> <0> BASIS = "MASS-FLOW" TOTAL = 24690. <-80> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = ETHANOL FLOW = 24568.0 <-80> <3> / SSID1 = MIXED CID = H2O FLOW = 122.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 521 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 70.0 <22> <4> PRES = 1.50 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 8381.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = ETHANOL FLOW = .70 <-3> <0> / SSID1 = MIXED CID = H2O FLOW = .30 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" "; Initial guess for recycle from Mole-sieve" ) \ ? STREAM MATERIAL 524 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 26.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 35747. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 35747.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Well water for vent scrubber" ) \ ? STREAM MATERIAL 557 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 25.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MOLE TOTFLOW = 205.831685 <-89> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = .790 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .210 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 574 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 211205. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 211205.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";FRESH MAKE-UP WATER ADDED TO RECYCLE WATER" ) \ ? STREAM MATERIAL 576 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 47.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 198670. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 198670.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";INITIAL GUESS" ) \ ? STREAM MATERIAL 621 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 21.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 88661.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TEMP = 21.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 60.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = .99860 <-3> <0> / SSID1 = MIXED CID = WNUTR FLOW = .00140 <-3> <0> / SSID1 = CISOLID CID = BIOMASS FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";STREAM 590" ";;THIS IS THE STEAM REQ'D TO HEAT THE HYDROLYZATE" ";;FOR SACCHARIFICATION IN H301." ";;CONTROLLED BY DESIGN-SPEC SACCHHEAT" ";; SUBSTREAM MIXED TEMP=163.5110 PRES=4.42290" "; SUBSTREAM MIXED PRES=13.0 TEMP=268.1893 NPHASE=2" "; MASS-FLOW H2O 7700." ";;" ";STREAM 592" ";;THIS IS THE STEAM REQ'D TO TRIM THE REBOILER" ";;FOR THE RECTIFICATION COLUMN" ";;CONTROLLED BY DESIGN-SPEC TRIM" ";; SUBSTREAM MIXED TEMP=163.5110 PRES=4.42290" ";; MASS-FLOW H2O 6303." "; SUBSTREAM MIXED PRES=13.0 TEMP=268.1893 &" "; MASS-FLOW=7000.0 NPHASE=2" "; MASS-FRAC H2O 1.0" ";;" ";STREAM 594" ";;THIS IS THE STEAM REQ'D TO RUN THE BEER COLUMN" ";;REBOILER." ";;CONTROLLED BY DESIGN-SPEC REBOIL" "; SUBSTREAM MIXED TEMP=163.5110 PRES=4.42290" "; MASS-FLOW H2O 50000." ";;" ";STREAM 596" ";;STEAM TO SUPERHEAT ETHANOL TO MOLE SIEVE" ";;CONTROLLED BY DESIGN SPEC SUPRHET" "; SUBSTREAM MIXED TEMP=163.5110 PRES=4.42290" "; MASS-FLOW H2O 298.1" ";;" ";INITIAL GUESS" ) \ ? STREAM MATERIAL 626 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 6944.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = .790 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .210 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";OXYGEN FOR AEROBIC TREATMENT" ";CONTROLLED BY FORTRAN AERAIR" ) \ ? STREAM MATERIAL 630 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 171. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = WNUTR FLOW = 171.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";WASTEWATER TREATMENT NUTRIENTS" ";CONTROLLED BY FORTRAN WWNUTR" ) \ ? STREAM MATERIAL 631 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 5.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = WNUTR FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" "; POLYMER FOR BELT PRESS" "; CONTROLLED BY WWNUTR2" ) \ ? STREAM MATERIAL 701 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 812.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = DENAT FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";DENATURANT FOR FINAL BLENDING" ";CONTROLLED BY FORTRAN STORE" ) \ ? STREAM MATERIAL 710 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 514.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2SO4 FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";H2SO4 STREAM FOR CALCULATING STORAGE TANK" ";CONTROLLED BY FORTRAN STORE" ) \ ? STREAM MATERIAL 713 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 6271.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";FIREWATER STREAM FOR CALCULATING STORAGE TANK" ) \ ? STREAM MATERIAL 717 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 17.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 229.60 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = NH3 FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";AMMONIA STREAM FOR CALCULATING STORAGE TANK" ";CONTROLLED BY FORTRAN STORE" ) \ ? STREAM MATERIAL 723 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 14.970 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = PROPANE FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";DIESEL FUEL STREAM FOR CALCULATING STORAGE TANK" ";CONTROLLED BY FORTRAN STORE" ) \ ? STREAM MATERIAL 735 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 1138.4 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = CSL FLOW = 1138.40 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";TOTAL CSL STREAM FOR CELLULASE & ETHANOL PRODUCTION" ";CONTROLLED BY FORTRAN CSL-ENZY" ) \ ? STREAM MATERIAL 745 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 1. <-80> <0> JUNK = 1 \ \ MOLE-FLOW SSID1 = CISOLID CID = CAH2O2 FLOW = 1.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";TOTAL LIME" ";CONTROLLED BY PHCONTR1" ) \ ? STREAM MATERIAL 750 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 9167. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 833. <-80> <0> JUNK = 1 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 9167.0 <-80> <3> / SSID1 = CISOLID CID = CELLULAS FLOW = 833.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Cellulase" ) \ ? STREAM MATERIAL 755 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 1000. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = DAP FLOW = 1000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Diammonium Phosphate (DAP), SSCF nutrient" ) \ ? STREAM MATERIAL 804 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 23.8888870 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 263000.0 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 3 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = .0130 <-3> <0> / SSID1 = MIXED CID = N2 FLOW = .75860 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .22840 <-3> <0> \ \ COMMENTS COMMENTS = ( ";INLET AIR STREAM TO THE COMBUSTION FAN (M802)" ";CONTROLLED BY DESIGN-SPEC COMBAIR" "; AIR COMPOSITION FROM FOSTER WHEELER IN REI 1998 SUBCONTRACT" ";Using the following molar composition of dry air (78.084% N2, 20.946% O2," ";0.033% CO2, & 0.934% Ar from CRC 63rd ed. p.F-171) and an air molecular" ";weight of 28.964 (CRC 63rd ed.) dry air is 23.14% O2 on a mass basis." ";Assuming that all non-oxygen components can be modeled as N2, dry air is" ";76.86% (mass) N2. Then assuming that water causes equal dissipation of" ";all components a stream that is 1.3% (mass) water is 22.84% O2 and" ";75.86% N2." ) \ ? STREAM MATERIAL 811 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 26.0 <22> <4> PRES = 3.40 <20> <3> BASIS = "MASS-FLOW" TOTAL = 73157.1 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 73157.10 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";BFW MAKE-UP" ) \ ? STREAM MATERIAL 812 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 510.0 <22> <4> PRES = 86.05770 <20> <3> BASIS = "MASS-FLOW" TOTAL = 187770. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 187770.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Tear stream initial guess" ) \ ? STREAM MATERIAL 814 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED PRES = 13.0 <20> <3> VFRAC = 1.0 <0> <0> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTFLOW = 85575.70 <-80> <3> NPHASE = 2 TOTAL = 85575.7 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 85575.70 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";HP (150 PSIG)PROCESS STEAM TO PRETREATMENT AND DISTILLATION" ";CONTROLLED BY FORTRAN BLOCK HPSTMD" ) \ ? STREAM MATERIAL 815 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 163.5110 <22> <4> PRES = 4.42290 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 55203.20 <-80> <3> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";LP (50 PSIG) PROCESS STEAM TO PRETREATMENT AND HEATERS" ";CONTROLLED BY FORTRAN BLOCK LPSTMD" ) \ ? STREAM MATERIAL 815A ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 163.5110 <22> <4> PRES = 4.42290 <20> <3> BASIS = "MASS-FLOW" TOTAL = 14694. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 14694.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";LP STEAM TO DEAERATOR" ";CONTROLLED BY DESIGN-SPEC DEAERHT" ) \ ? STREAM MATERIAL 821 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 321.0 <22> <4> PRES = 112.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 7219. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 7219.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";INITIAL GUESS" ) \ ? STREAM MATERIAL 824 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED PRES = 1.70 <20> <3> VFRAC = 0.0 <0> <0> BASIS = "MASS-FLOW" TOTAL = 109780. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 109780.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";CONDENSATE MAKE-UP" ) \ ? STREAM MATERIAL 840 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 25.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 1.E-007 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = CH4 FLOW = 1.0000E-07 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Auxillary fuel to supplement burner/boiler" ) \ ? STREAM MATERIAL 853 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 268.18950 <22> <4> PRES = 13.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 1.E-007 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0000E-07 <-80> <3> \ \ COMMENTS COMMENTS = ( "; For biomass use same definition as for stream 101" "; MASS-FLOW H2O 73530 / SOLSLDS 23375 / EXTRACT 13835 / PROTEIN 16835" "; SUBSTREAM CISOLID TEMP=20.0 PRES=1.0 MASS-FLOW=362625" "; MASS-FRAC CELLULOS 0.4285 / XYLAN 0.2361 /" "; ARABINAN 0.0255 / MANNAN 0.0018 /" "; GALACTAN 0.0139 / LIGNIN 0.2015 /" "; ACETATE 0.0225 / ASH 0.0701" ";;" ";HIGH PRESSURE STEAM FOR LIGNIN DRYER" ";PER ReTec QUOTE NEEDS TO BE AT LEAST 160 PSI SATURATED STEAM" ";CONTROLLED BY DESIGN SPEC LPSTMFLO" ) \ ? STREAM MATERIAL 890 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 163.5110 <22> <4> PRES = 4.42290 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 30000.0 <-80> <3> NPHASE = 2 TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";LOW PRESSURE STEAM TO THE UTILITY STEAM HEATING SYSTEM" "; Manually increased if LP steam not sufficient for heating" ) \ ? STREAM MATERIAL 891 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 268.18930 <22> <4> PRES = 13.0 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1.0000E-06 <-80> <3> NPHASE = 2 TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";MEDIUM PRESSURE STEAM TO THE UTILITY STEAM HEATING SYSTEM" "; Manually increased if LP steam not sufficient for heating" ) \ ? STREAM MATERIAL 892 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 510.0 <22> <4> PRES = 86.060 <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1.0000E-06 <-80> <3> NPHASE = 2 TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";;" ";HIGH PRESSURE STEAM TO THE UTILITY STEAM HEATING SYSTEM" "; Manually increased if LP steam not sufficient for heating" ) \ ? STREAM MATERIAL 903 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 13.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 100000. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 100000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";PROCESS MAKE-UP WATER DEMAND" ";CONTROLLED BY FORTRAN BLOCK WATERDEM" ) \ ? STREAM MATERIAL 906 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 63.04 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 63.040 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ";CIP/CS WATER" ) \ ? STREAM MATERIAL 914 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 63.04 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 63.040 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 921 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 3. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 3.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 922 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 4. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 4.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 941 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 30682. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 30682.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Place holder for Calculated Cooling Twr Make-up" ) \ ? STREAM MATERIAL 942 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 30682. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 30682.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Place holder for calculated Cooling Tower Windage" ) \ ? STREAM MATERIAL 943 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 26.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 30682. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 30682.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Place holder for Well water Mixed with treated water" ) \ ? STREAM MATERIAL 944 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 17820. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 17820.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Specified Cooling Tower Blowdown" ) \ ? STREAM MATERIAL 944A ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 30682. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 30682.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" "; Place Holder for calculated Cooling Tower Blowdown" "; Used as a comparison to the actual specified as 944" "; above." ) \ ? STREAM MATERIAL 945 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 4.08275780 <20> <3> BASIS = "MASS-FLOW" TOTAL = 100. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 100.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 946 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 4.08275780 <20> <3> BASIS = "MASS-FLOW" TOTAL = 100. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 100.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 948 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> BASIS = "MASS-FLOW" TOTAL = 100000. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 100000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 950 ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 4.0 <22> <4> PRES = 4.08275780 <20> <3> BASIS = "MASS-FLOW" TOTAL = 100. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 100.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM MATERIAL 950A ? ; "SET1_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 4.0 <22> <4> PRES = 4.08275780 <20> <3> BASIS = "MASS-FLOW" TOTAL = 3000000. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 3000000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM HEAT QBOILER ? ; "SET1_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 3.3409E+07 <13> <3> \ \ COMMENTS COMMENTS = ( ";;" "; TEAR -- INITIAL GUESS" ) \ ? STREAM HEAT QCD502 ? ; "SET1_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 5676418.49 <13> <3> \ \ COMMENTS COMMENTS = ( ";;" ";---------------------------------------------------------------------" "; HEAT STREAMS" ";-------------------------------------------------------------------" ";;" "; QCD502 and QRD502 are the condenser and reboiler duties to column" "; AS-502. They will be determined by the FORTRAN D502QCR." ";;" ) \ ? STREAM HEAT QE501A ? ; "SET1_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = .027777378 <13> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM HEAT QH14CWB ? ; "SET1_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 2306216.88 <13> <3> \ \ COMMENTS COMMENTS = ( ";;" "; TEAR -- INITIAL GUESS" ) \ ? STREAM HEAT QH602 ? ; "SET1_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 8555900.0 <13> <3> \ \ COMMENTS COMMENTS = ( ";;" "; TEAR -- INITIAL GUESS" ) \ ? STREAM HEAT QH801 ? ; "SET1_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 3328757.76 <13> <3> \ \ COMMENTS COMMENTS = ( ";;" "; TEAR -- INITIAL GUESS" ) \ ? STREAM HEAT QH811 ? ; "SET1_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = -181136.29 <13> <3> \ \ COMMENTS COMMENTS = ( ";;" "; TEAR -- INITIAL GUESS" ) \ ? STREAM HEAT QRD502 ? ; "SET1_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = -1.062E+06 <13> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? STREAM WORK WC101 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ \ COMMENTS COMMENTS = ( "; WS103 is tramp iron magnet power (S-103)" "; Set at 0.0 because power is unknown and assumed to be low (like R0008B)" "; Not modified by fortrans" ";;" "; Initialize work streams determined via CALCULATOR blocks." ) \ ? STREAM WORK WC102 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WC103 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WC104 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WC201 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WC202 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WC225 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WC501 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WC614 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WC755 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM103 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM104 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM105 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM107 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM202 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM503 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM604 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM612 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM801 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM804 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM830 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM832 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM834 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM902 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM904A ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM908 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WM910 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP101 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP102 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP103 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP104 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP105 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP201 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP205 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP209 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP211 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP213 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP222 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP223 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP224 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP239 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP300 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP301 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP302 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP306 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP310 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP400 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP401 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP405 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP420 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP501 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP503 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP504 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP505 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP511 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP512 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP513 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP514 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP515 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP530 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP602 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP606 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP608 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP610 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP611 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP614 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP616 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP701 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP703 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP704 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP706 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP707 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP708 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP710 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP720 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP750 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP755 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP760 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP804 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP828 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP830 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP902 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP912 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WP914 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WPLNTPOW ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WS101 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WS102 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WS103 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ \ COMMENTS COMMENTS = ( ";;" ";;" ) \ ? STREAM WORK WS205 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WS221 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WS222 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WS505 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WS600 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WS614 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WS904 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT205 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT209 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT224 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT232 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT300 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT301 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT304 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT305 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT306 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT310 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT400 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK "WT402-3" ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT405 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT530 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT602 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT606 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT608 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT610 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT720 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WT760 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? STREAM WORK WTOTAL2 ? ; "SET1_MOLE" ; \ INFO POWER = 0.0 <19> <3> \ ? BLOCK MIXER A201 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "INLINE SULFURIC ACID MIXER" \ \ PARAM PRES = 4.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER AGITAT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIXES THE AGITATOR POWER REQUIREMENTS" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER AIRCMP ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "TOTAL COMPRESSED AIR REQUIRED" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER C103C ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIXES POLYMER AND WATER FOR WASTE REMOVAL" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER C202 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIX CENTRIFUGE LIQUID STREAMS" \ \ PARAM PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER CHCWMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SSCF & SEED CHW/CW DEMAND MIXER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER CHEMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "BLOCK TO CALC CHEM'S FOR BOILER & COOLING TOWER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER CIPCS ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "CIP/CS SYSTEM TANKS AND PUMPS" \ \ COMMENTS COMMENTS = ( "; Controlled by fortran AIRREQ" ";;" ) \ ? BLOCK MIXER CLTWR ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "DUMMY BLOCK FOR COOLING TOWWER FLOWS" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER COMPWK ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "COMPRESSOR WORK DEMAND CALCULATOR" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER E501MIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIXES CONDENSATE FROM EVAPORATOR" \ \ PARAM PRES = 2.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER "F401-4MX" ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIXER FOR FEED AND WATER TO CELLULASE SEED FERMENTORS." \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER FERMMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIX CSL, DAP AND SEED WITH HYD. BEFORE FERM" \ \ COMMENTS COMMENTS = ( ";10% IS SAME VALUE IN SSFSPLT IN SSF MODEL" ";SOURCE NOT DOCUMENTED" ";;" ) \ ? BLOCK MIXER FWMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "TANK T-530 FOR MIXING FRESH H2O AND RECYCLE H2O" \ \ PARAM NPHASE = 1 PHASE = L \ \ COMMENTS COMMENTS = ( ";THE FRACTIONS LISTED ARE ASSUMPTIONS. THE ACTUAL VALUES ARE" ";DETERMINED BY THE FORTRAN BLOCK RECYCLE." ";;" ) \ ? BLOCK MIXER H200MIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIX 221 & 256 INTO 223 TO FEED INTO H200" \ \ COMMENTS COMMENTS = ( ";;" ";;" ";------------------------------------------------------------" ";;" "; PRETREATMENT BLOCKS - AREA 200" ";------------------------------------------------------------" ";;" ) \ ? BLOCK MIXER H244MIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "COOLING WATER HEAT STREAMS THAT ARE REQUIRED FOR H244" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER "HEATCHW-" ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "CHILLED WATER HEAT DEMAND MIXER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER "HEATCW-S" ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "COOLING WATER HEAT DEMAND MIXER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER M104MIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIXES INCOMING BIOMASS WITH RETAINED WASH WATER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER M202MIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "IMPREGNATOR - DESIGNED TO HEAT MIX TO 100 C" \ \ PARAM PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER M801MIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SLURRY MIXER" \ \ PARAM PRES = 1.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER M802MIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIX PNEUMAPRESS VENTS AND INCOMING AIR" \ \ COMMENTS COMMENTS = ( ";;" ";--------------------------------------------------------------" "; BOILER BLOCKS - AREA 800" ";-------------------------------------------------------------" ";;" ) \ ? BLOCK MIXER MPOW1 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "AREA 1000 MISCELLANEOUS WORK SUMMER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER MPOW2 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "AREA 2000 MISCELLANEOUS WORK SUMMER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER MPOW5 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "AREA 5000 MISCELLANEOUS WORK SUMMER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER MPOW6 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "AREA 6000 MISCELLANEOUS WORK SUMMER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER MPOW8 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "AREA 8000 MISCELLANEOUS WORK SUMMER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER MPOW10 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "AREA 10000 MISCELLANEOUS WORK SUMMER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER MPOWTOT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "TOTAL MISCELLANEOUS POWER SUMMER" \ \ COMMENTS COMMENTS = ( "; Does not include cellulase air requirement" ";;" ) \ ? BLOCK MIXER NUTMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "ADDS CHEMICALS AND NUTRIENTS TO ANAEROBIC DIGESTION" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER P224 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIX DETOXED SLURRY AND RECYCLE WATER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER PMPWK ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "PUMP WORK DEMAND CALCULATOR" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER PRODMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "ETHANOL AND DENATURANT MIXER" \ \ PARAM PRES = 1.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER QCHWMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "CHILLED WATER CAPITAL HEAT DEMAND MIXER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER QCHWMX2 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "CHILLED WATER OPERATING HEAT DEMAND MIXER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER QCWMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "CW CAPITAL HEAT DEMAND MIXER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER S205MIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIXES WASH-WATER WITH SINGLE-PRESSED SOLIDS" \ \ PARAM PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( "; THE MIXED FRACTION IS CALCULATED BY DESIGN-SPEC CT-S205A" ";;" ) \ ? BLOCK MIXER S600 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "TANK T-603 TO MIX PROCESS WASTEWATER AND OTHER WASTES" \ \ PARAM PRES = 2.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ";------------------------------------------------------------" "; DIGESTION (WASTE WATER TREATMENT) BLOCKS - AREA 600" ";----------------------------------------------------------" ";;" ) \ ? BLOCK MIXER SEEDMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIX CSL AND DAP WITH HYD BEFORE SEED FERM" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER SSCFCW ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SSCF COOLING WATER DEMAND MIXER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER SSCFSDCW ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SSCF SEED TRAIN HEAT MIXER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER STMDMD ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "HEAT DEMAND FROM STEAM" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER T306 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "BEER WELL" \ \ COMMENTS COMMENTS = ( ";3% Contamination" ";;" ) \ ? BLOCK MIXER T405 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "CELLULASE MEDIA PREP TANK" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER T415 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MIXER FOR FEED AND WATER TO CELLULASE PRODUCTION." \ \ COMMENTS COMMENTS = ( ";;" ";-----------------------------------------------------------" "; CELLULASE BLOCKS - AREA 400" ";----------------------------------------------------------" ";;" ) \ ? BLOCK MIXER T824AS ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "CONDENSATE SURGE DRUM MS-804" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER T914 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "DUMMY BLOCK TO CALCULATE TOTAL WATER DEMAND" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER TSTORE ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "GENERAL STORAGE TANK" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER VNTMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "VENT MIXER" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER WKMIX ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "OVERALL NET WORK CALCULATOR FOR THE PLANT" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK MIXER WKSEP ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "OVERALL NET WORK USED BY THE PLANT" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT ASPLT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "FERMENTATION AIR SPLITTER" \ \ PARAM SID = 432 / SID = 413 FRAC = .90 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = 432 / ORDER-STREAM = 413 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT BTMSSPLT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SPLIT CENTRIFUGE BOTTOMS BETWEEN CELLULASE FERM & ETOH FERM" \ \ PARAM SID = 401 FRAC = .0220 <0> <0> / SID = 301 \ \ STREAM-ORDER ORDER-STREAM = 401 / ORDER-STREAM = 301 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT C103B ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "RECYCLED MAKE-UP WATER AND LOSS WITH DIRT SPLITTER" \ \ PARAM SID = 104B FLOW-BASIS = MASS BASIS-FLOW = 1000.0 <-80> <3> / SID = 102A \ \ STREAM-ORDER ORDER-STREAM = 104B / ORDER-STREAM = 102A \ \ COMMENTS COMMENTS = ( ";;" "; Set by RECCOND" ) \ ? BLOCK FSPLIT CLFDSPLT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SPLIT BETWEEN SEED AND FERMENTORS." \ \ PARAM1 NPHASE1 = 1 PHASE1 = L \ \ PARAM SID = 403 FRAC = .050 <0> <0> / SID = 410 \ \ STREAM-ORDER ORDER-STREAM = 403 / ORDER-STREAM = 410 \ \ COMMENTS COMMENTS = ( ";Initial Guess: Calculated by ENZYME" ";;" ) \ ? BLOCK FSPLIT CLSSPLIT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SPLIT CELL. RCTR EFF. BTWN SEED FERM + ETOH FRM" \ \ PARAM SID = 421 FRAC = .20 <0> <0> / SID = 422 \ \ STREAM-ORDER ORDER-STREAM = 421 / ORDER-STREAM = 422 \ \ COMMENTS COMMENTS = ( ";The following fractionation and note were left by Vicki, I have ignored" ";her advice. MR 2 July 97" "; FRAC 403 .005" ";THE FRACTION SPECIFIED WAS SELECTED TO GET A 5% INOCULUM." ";CURRENTLY, IT IS NOT CHANGEABLE DUE TO CHANGING CONDITIONS." ";A CONTROL BLOCK SHOULD BE WRITTEN TO CHANGE THIS." ";;" ) \ ? BLOCK FSPLIT CONTSPLT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SPLIT TO CONTAMINATION REACTION" \ \ PARAM SID = 304F / SID = 304G FRAC = .030 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = 304F / ORDER-STREAM = 304G \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT E501LOSS ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "HEAT LOSS IN 1ST EFFECT" \ \ PARAM SID = QE501L FRAC = .020 <0> <0> / SID = QE501B \ \ STREAM-ORDER ORDER-STREAM = QE501L / ORDER-STREAM = QE501B \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT E501SPT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SPLITS CONDENSATE RECYCLE" \ \ PARAM1 PRES1 = 3.0 <20> <3> \ \ PARAM SID = 102 FLOW-BASIS = MASS BASIS-FLOW = 18000.0 <-80> <3> BASIS-KEYNO = 1 / SID = 211 FLOW-BASIS = MASS BASIS-FLOW = 2000.0 <-80> <3> BASIS-KEYNO = 1 / SID = 251 \ \ DEF-KEY DEF-KEYNO = 1 SUBSTREAM = MIXED COMPS = ( H2O ) \ \ STREAM-ORDER ORDER-STREAM = 102 / ORDER-STREAM = 211 / ORDER-STREAM = 251 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT E501WW ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SPECIFIES FLOW TO WASTEWATER TREATMENT" \ \ PARAM SID = 534B / SID = 535 FRAC = .10 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = 534B / ORDER-STREAM = 535 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT E502LOSS ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "HEAT LOSS IN 2ND EFFECT" \ \ PARAM SID = QE502L FRAC = .020 <0> <0> / SID = QE502B \ \ STREAM-ORDER ORDER-STREAM = QE502L / ORDER-STREAM = QE502B \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT E503LOSS ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "HEAT LOSS IN 3RD EFFECT" \ \ PARAM SID = QE503L FRAC = .020 <0> <0> / SID = QE503B \ \ STREAM-ORDER ORDER-STREAM = QE503L / ORDER-STREAM = QE503B \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT M104LOSS ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "MAKE-UP WATER AND EVAPORATION/WINDAGE LOSS SPLITTER" \ \ PARAM SID = 103 FLOW-BASIS = MASS BASIS-FLOW = 11300.0 <-80> <3> / SID = 102B \ \ STREAM-ORDER ORDER-STREAM = 103 / ORDER-STREAM = 102B \ \ COMMENTS COMMENTS = ( ";;" "; Set by RECCOND" ) \ ? BLOCK FSPLIT M811GEN ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "THIS BLOCK IS THE ELECTRICAL PART OF THE TURBOGENERATOR" \ \ PARAM SID = WLOST / SID = WTOTAL FRAC = .960 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = WLOST / ORDER-STREAM = WTOTAL \ \ COMMENTS COMMENTS = ( ";;" ";-------------------------------------------------------------" "; TURBOGENERATOR BLOCKS - AREA 810" ";-------------------------------------------------------------" ";;" ";THE GENERATOR EFFICIENCY WAS ESTIMATED AT 96%" ";EFFICIENCY LOSS IS FROM ABB (VENDOR) 1998 QUOTE IN" ";REI 1999 SUBCONTRACT REPORT" ) \ ? BLOCK FSPLIT M811HSPT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "HP (150 PSIG) STEAM SPLITTER" \ \ PARAM SID = 812B FRAC = .0770 <0> <0> / SID = 814 FLOW-BASIS = MASS BASIS-FLOW = 18758.0 <-80> <3> / SID = 814A \ \ STREAM-ORDER ORDER-STREAM = 812B / ORDER-STREAM = 814 / ORDER-STREAM = 814A \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT M811ISPT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "IP (50 PSIG) STEAM SPLITTER" \ \ PARAM SID = 815A FLOW-BASIS = MASS BASIS-FLOW = 14694.0 <-80> <3> / SID = 815B / SID = 815 FLOW-BASIS = MASS BASIS-FLOW = 70000.0 <-80> <3> \ \ STREAM-ORDER ORDER-STREAM = 815A / ORDER-STREAM = 815B / ORDER-STREAM = 815 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT M811LSPT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "LP (10 PSIG) STEAM SPLITTER" \ \ PARAM SID = 815D / SID = 860 FLOW-BASIS = MASS BASIS-FLOW = 27429.0 <-80> <3> \ \ STREAM-ORDER ORDER-STREAM = 815D / ORDER-STREAM = 860 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT M811XSPT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "XHP (86 ATM) STEAM SPLITTER" \ \ PARAM SID = 812C / SID = 812D FLOW-BASIS = MASS BASIS-FLOW = .10 <-80> <3> \ \ STREAM-ORDER ORDER-STREAM = 812C / ORDER-STREAM = 812D \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT QCOMSPLT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "ACCOUNT FOR 1% RADIANT LOSSES AND 1.5% UNACCOUNTED" \ \ PARAM SID = QCOMLOSS FRAC = .0260 <0> <0> / SID = QBOILER \ \ STREAM-ORDER ORDER-STREAM = QCOMLOSS / ORDER-STREAM = QBOILER \ \ COMMENTS COMMENTS = ( ";;" ";EFFICIENCY LOSS IS FROM FOSTER WHEELER (VENDOR) QUOTE IN" ";REI 1998 SUBCONTRACT" ) \ ? BLOCK FSPLIT QH14BSP ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SETS FRACTION OF YEAR THAT CHW IS REQ. FOR SSCF COOLING" \ \ PARAM SID = QH14BCW / SID = QH14BCHW FRAC = 1.0000E-08 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = QH14BCW / ORDER-STREAM = QH14BCHW \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT QH201SPT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "SPLITTER TO SET FRAC TO H201-" \ \ PARAM SID = QH201 FRAC = .950 <0> <0> / SID = QH201XTR \ \ STREAM-ORDER ORDER-STREAM = QH201 / ORDER-STREAM = QH201XTR \ \ COMMENTS COMMENTS = ( ";;" ";Split is controlled by D-Spec H201TEMP to reach temp spec for 501" ) \ ? BLOCK FSPLIT RWSPLT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "RECYCLE WATER SPLITTER" \ \ PARAM SID = 219 FRAC = .80 <0> <0> / SID = 430 FRAC = .0010 <0> <0> / SID = 411 \ \ STREAM-ORDER ORDER-STREAM = 219 / ORDER-STREAM = 430 / ORDER-STREAM = 411 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FSPLIT S205SPT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "RECYCLE WATER SPLITTER" \ \ PARAM SID = 252 FLOW-BASIS = MASS BASIS-FLOW = 125000.0 <-80> <3> / SID = 253 \ \ STREAM-ORDER ORDER-STREAM = 252 / ORDER-STREAM = 253 \ \ COMMENTS COMMENTS = ( ";;" "; Calculated in FORTRAN S205WASH" ) \ ? BLOCK FSPLIT SACCHSPT ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "FEED SPLITTER TO SEED TRAIN" \ \ PARAM SID = 302 / SID = 303 FRAC = .10 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = 302 / ORDER-STREAM = 303 \ \ COMMENTS COMMENTS = ( ";;" ";------------------------------------------------------------" "; SACCHARIFICATION AND CO-FERMENTATION BLOCKS - AREA 300" ";------------------------------------------------------------" ";;" ) \ ? BLOCK FSPLIT T530 ? ; "SET1_MOLE" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "RECYCLE WATER AND WWT LIQUID SEPARATOR" \ \ PARAM SID = 573 / SID = 580 FRAC = .750 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = 573 / ORDER-STREAM = 580 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK SEP C103A ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "CLARIFIER POLYMER REMOVAL" \ \ PARAM1 PRES1 = 1.0 <20> <3> \ \ PARAM PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = GLUCOSE FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = CELLULOS / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = XYLOSE FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = XYLAN / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = LIGNIN / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = CELLULAS / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = BIOMASS / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = ZYMO / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = UNKNOWN FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = SOLSLDS FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = GYPSUM / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = ACETATE / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = LGNSOL FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = HMF FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = ARABINOS FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = GALACTOS FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = MANNOSE FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = ARABINAN / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = MANNAN / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = GALACTAN / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = GLUCOLIG FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = CELLOB FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = XYLOLIG FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = TAR / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = MANOLIG FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = GALAOLIG FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = ARABOLIG FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = ACETOLIG FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = XYLITOL FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = EXTRACT FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = PROTEIN FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = CASO4 / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = CAH2O2 / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = ASH / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = H2O FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = FURFURAL FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = H2SO4 FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = N2 FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = CO2 FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = O2 FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = CH4 FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = NO FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = NO2 FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = NH3 FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = LACID FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = AACID FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = NH4OH / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = NH4SO4 / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = NH4ACET / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = GLYCEROL FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = SUCCACID FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = DAP / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = PROPANE / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = DENAT FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = OIL FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = CSL FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = CNUTR FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = WNUTR FRACS = 1.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = C / PARAM-STREAM = 104A SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = CELLULOS FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = XYLAN FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = LIGNIN FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = CELLULAS FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = BIOMASS FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = ZYMO FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = GYPSUM FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = ACETATE FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = ARABINAN FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = MANNAN FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = GALACTAN FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = TAR FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = CASO4 FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = CAH2O2 FRACS = 0.0 <0> <0> / PARAM-STREAM = 104A SUBSTREAM = CISOLID COMPS = ASH FRACS = 0.0 <0> <0> / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = GLUCOSE / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = CELLULOS / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = XYLOSE / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = XYLAN / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = LIGNIN / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = CELLULAS / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = BIOMASS / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = ZYMO / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = UNKNOWN / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = SOLSLDS / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = GYPSUM / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = ACETATE / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = LGNSOL / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = HMF / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = ARABINOS / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = GALACTOS / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = MANNOSE / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = ARABINAN / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = MANNAN / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = GALACTAN / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = GLUCOLIG / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = CELLOB / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = XYLOLIG / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = TAR / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = MANOLIG / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = GALAOLIG / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = ARABOLIG / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = ACETOLIG / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = XYLITOL / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = EXTRACT / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = PROTEIN / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = CASO4 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = CAH2O2 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = ASH / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = FURFURAL / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = H2SO4 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = NO / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = LACID / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = AACID / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = NH4OH / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = NH4SO4 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = NH4ACET / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = GLYCEROL / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = SUCCACID / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = DAP / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = PROPANE / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = DENAT / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = OIL / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = CSL / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = CNUTR / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = WNUTR / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = C / PARAM-STREAM = 104D SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = CELLULOS / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = XYLAN / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = LIGNIN / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = CELLULAS / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = BIOMASS / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = ZYMO / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = GYPSUM / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = ACETATE / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = ARABINAN / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = MANNAN / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = GALACTAN / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = TAR / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = CASO4 / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = CAH2O2 / PARAM-STREAM = 104D SUBSTREAM = CISOLID COMPS = ASH \ \ COMMENTS COMMENTS = ( ";;" ";;" ";------------------------------------------------------------" "; BLOCK SECTION" "; SOLIDS HANDLING BLOCKS - AREA 100" ";------------------------------------------------------------" ";;" ";ALL CNUTR & CSL SHOULD HAVE BEEN CONSUMED IN CELLULASE PRODUCTION &" ";SO ANY REMAINING SHOULD GO OFF TO WWT SO THAT THE RECYCLE WILL BE" ";CORRECT. DENAT AND WNUTR SHOULD NOT BE IN THIS STREAM, BUT IF THEY" ";ARE, THEY BEHAVE LIKE ANY LIQUID." ) \ ? BLOCK SEP S205B ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "POST-WASH SEPARATIONS FOR S205" \ \ PARAM1 PRES1 = 0.0 <20> <3> \ \ PARAM PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = GLUCOSE / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = CELLULOS / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = XYLOSE / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = XYLAN / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = LIGNIN / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = CELLULAS / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = BIOMASS / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = ZYMO / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = UNKNOWN / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = SOLSLDS / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = GYPSUM / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = ACETATE / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = LGNSOL / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = HMF / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = ARABINOS / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = GALACTOS / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = MANNOSE / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = ARABINAN / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = MANNAN / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = GALACTAN / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = GLUCOLIG / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = CELLOB / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = XYLOLIG / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = TAR / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = MANOLIG / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = GALAOLIG / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = ARABOLIG / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = ACETOLIG / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = XYLITOL / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = EXTRACT / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = PROTEIN / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = CASO4 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = CAH2O2 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = ASH / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = FURFURAL / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = H2SO4 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = NO / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = LACID / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = AACID / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = NH4OH / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = NH4SO4 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = NH4ACET / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = GLYCEROL / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = SUCCACID / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = DAP / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = PROPANE / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = DENAT / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = OIL / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = CSL / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = CNUTR / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = WNUTR / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = C / PARAM-STREAM = 255A SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = CELLULOS FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = XYLAN FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = LIGNIN FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = CELLULAS FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = BIOMASS FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = ZYMO FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = GYPSUM FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = ACETATE FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = ARABINAN FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = MANNAN FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = GALACTAN FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = TAR FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = CASO4 FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = CAH2O2 FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = ASH FRACS = 1.0 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = GLUCOSE FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CELLULOS / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = XYLOSE FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = XYLAN / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = LIGNIN / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CELLULAS / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = BIOMASS / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ZYMO / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = UNKNOWN FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = SOLSLDS FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = GYPSUM / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ACETATE / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = LGNSOL FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = HMF FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ARABINOS FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = GALACTOS FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = MANNOSE FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ARABINAN / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = MANNAN / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = GALACTAN / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = GLUCOLIG FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CELLOB FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = XYLOLIG FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = TAR / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = MANOLIG FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = GALAOLIG FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ARABOLIG FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ACETOLIG FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = XYLITOL FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = EXTRACT FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = PROTEIN FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CASO4 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CAH2O2 / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ASH / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ETHANOL FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = H2O FRACS = .750 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = FURFURAL FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = H2SO4 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = N2 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CO2 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = O2 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CH4 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = NO FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = NO2 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = NH3 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = LACID FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = AACID FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = NH4OH / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = NH4SO4 / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = NH4ACET / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = GLYCEROL FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = SUCCACID FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = DAP / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = PROPANE / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = DENAT FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = OIL FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CSL FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CNUTR FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = WNUTR FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = C / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = CELLULOS / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = XYLAN / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = LIGNIN / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = CELLULAS / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = BIOMASS / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = ZYMO / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = GYPSUM / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = ACETATE / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = ARABINAN / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = MANNAN / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = GALACTAN / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = TAR / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = CASO4 / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = CAH2O2 / PARAM-STREAM = 256 SUBSTREAM = CISOLID COMPS = ASH \ \ COMMENTS COMMENTS = ( ";;" ";THE FRACTIONAL SPLITS ARE BASED ON HARRIS 2000 SUBCONTRACT" ";PNEUMAPRESS TEST 9. 93.3% OF THE TOTAL INLET SOLUBLES ARE" ";RECOVERED TO FILTRATE. 99.5% OF INSOLUBLE SOLIDS ARE RECOVERED" ";TO CAKE" ";ACCORDING TO HARRIS MEETING 17 Jan 01 99.5% OF INSOLUBLE SOLIDS" ";ARE RECOVERED BY THE PNEUMAPRESS" ) \ ? BLOCK SEP2 D502 ? ; "SET1_MOLE" ; ; ICON2 ; \ PARAM PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = GLUCOSE / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = CELLULOS / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = XYLOSE / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = XYLAN / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = LIGNIN / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = CELLULAS / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = BIOMASS / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = ZYMO / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = UNKNOWN / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = SOLSLDS / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = GYPSUM / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = ACETATE / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = LGNSOL / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = HMF / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = ARABINOS / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = GALACTOS / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = MANNOSE / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = ARABINAN / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = MANNAN / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = GALACTAN / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = GLUCOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = CELLOB / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = XYLOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = TAR / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = MANOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = GALAOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = ARABOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = ACETOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = XYLITOL / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = EXTRACT / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = PROTEIN / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = CASO4 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = CAH2O2 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = ASH / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = ETHANOL MFFRAC = .8260 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = H2O / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = FURFURAL / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = H2SO4 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = N2 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = CO2 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = O2 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = CH4 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = NO / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = NO2 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = NH3 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = LACID / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = AACID / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = NH4OH / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = NH4SO4 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = NH4ACET / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = GLYCEROL / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = SUCCACID / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = DAP / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = PROPANE / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = DENAT / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = OIL / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = CSL / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = CNUTR / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = WNUTR / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = SO2 / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = H2S / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = C / PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = CO / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = GLUCOSE FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CELLULOS FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = XYLOSE FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = XYLAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = LIGNIN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CELLULAS FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = BIOMASS FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = ZYMO FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = UNKNOWN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = SOLSLDS FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = GYPSUM FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = ACETATE FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = LGNSOL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = HMF FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = ARABINOS FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = GALACTOS FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = MANNOSE FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = ARABINAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = MANNAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = GALACTAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = GLUCOLIG FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CELLOB FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = XYLOLIG FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = TAR FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = MANOLIG FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = GALAOLIG FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = ARABOLIG FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = ACETOLIG FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = XYLITOL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = EXTRACT FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = PROTEIN FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CASO4 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CAH2O2 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = ASH FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = ETHANOL MFFRAC = .00020 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = H2O / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = FURFURAL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = H2SO4 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = N2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CO2 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = O2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CH4 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = NO FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = NO2 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = NH3 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = LACID FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = AACID FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = NH4OH FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = NH4SO4 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = NH4ACET FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = GLYCEROL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = SUCCACID FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = DAP FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = PROPANE FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = DENAT FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = OIL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CSL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CNUTR FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = WNUTR FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = SO2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = H2S FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = C FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CO FRACS = 0.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = CELLULOS / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = XYLAN / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = LIGNIN / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = CELLULAS / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = BIOMASS / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = ZYMO / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = GYPSUM / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = ACETATE / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = ARABINAN / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = MANNAN / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = GALACTAN / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = TAR / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = CASO4 / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = CAH2O2 / PARAM-SUBS = CISOLID PARAM-STREAM = 511 COMPS = ASH / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = CELLULOS FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = XYLAN FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = LIGNIN FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = CELLULAS FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = BIOMASS FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = ZYMO FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = GYPSUM FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = ACETATE FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = ARABINAN FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = MANNAN FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = GALACTAN FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = TAR FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = CASO4 FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = CAH2O2 FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = ASH FRACS = 1.0 <0> <0> \ \ FLASH-SPECS FLASH-STREAM = 511 TEMP = 92.4110 <22> <4> VFRAC = 1.0 <0> <0> \ \ FLASH-SPECS FLASH-STREAM = 516 TEMP = 121.0490 <22> <4> VFRAC = 0.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" "; Overhead - 511" "; Bottoms 516" ) \ ? BLOCK SEP2 S505 ? ; "SET1_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "BEER BOTTOMS PNEUMAPRESS" \ \ PARAM1 PRES1 = 3.20 <20> <3> \ \ PARAM PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = GLUCOSE / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = CELLULOS / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = XYLOSE / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = XYLAN / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = LIGNIN / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = CELLULAS / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = BIOMASS / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = ZYMO / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = UNKNOWN / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = SOLSLDS / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = GYPSUM / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = ACETATE / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = LGNSOL / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = HMF / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = ARABINOS / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = GALACTOS / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = MANNOSE / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = ARABINAN / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = MANNAN / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = GALACTAN / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = GLUCOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = CELLOB / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = XYLOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = TAR / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = MANOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = GALAOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = ARABOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = ACETOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = XYLITOL / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = EXTRACT / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = PROTEIN / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = CASO4 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = CAH2O2 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = ASH / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = ETHANOL / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = H2O / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = FURFURAL / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = H2SO4 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = N2 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = CO2 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = O2 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = CH4 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = NO / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = NO2 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = NH3 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = LACID / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = AACID / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = NH4OH / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = NH4SO4 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = NH4ACET / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = GLYCEROL / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = SUCCACID / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = DAP / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = PROPANE / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = DENAT / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = OIL / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = CSL / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = CNUTR / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = WNUTR / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = SO2 / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = H2S / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = C / PARAM-SUBS = MIXED PARAM-STREAM = 572 COMPS = CO / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = GLUCOSE FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CELLULOS FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = XYLOSE FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = XYLAN FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = LIGNIN FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CELLULAS FRACS = .50 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = BIOMASS FRACS = .50 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ZYMO FRACS = .50 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = UNKNOWN FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = SOLSLDS FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = GYPSUM FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ACETATE FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = LGNSOL FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = HMF FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ARABINOS FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = GALACTOS FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = MANNOSE FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ARABINAN FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = MANNAN FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = GALACTAN FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = GLUCOLIG FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CELLOB FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = XYLOLIG FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = TAR FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = MANOLIG FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = GALAOLIG FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ARABOLIG FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ACETOLIG FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = XYLITOL FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = EXTRACT FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = PROTEIN FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CASO4 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CAH2O2 FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ASH FRACS = .980 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ETHANOL FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = H2O FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = FURFURAL FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = H2SO4 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = N2 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CO2 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = O2 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CH4 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = NO FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = NO2 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = NH3 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = LACID FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = AACID FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = NH4OH FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = NH4SO4 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = NH4ACET FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = GLYCEROL FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = SUCCACID FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = DAP FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = PROPANE FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = DENAT FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = OIL FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CSL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CNUTR FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = WNUTR FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = SO2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = H2S FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = C FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CO FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = CELLULOS / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = XYLAN / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = LIGNIN / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = CELLULAS / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = BIOMASS / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = ZYMO / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = GYPSUM / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = ACETATE / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = ARABINAN / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = MANNAN / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = GALACTAN / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = TAR / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = CASO4 / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = CAH2O2 / PARAM-SUBS = CISOLID PARAM-STREAM = 572 COMPS = ASH / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = CELLULOS FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = XYLAN FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = LIGNIN FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = CELLULAS FRACS = .50 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = BIOMASS FRACS = .50 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = ZYMO FRACS = .50 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = GYPSUM FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = ACETATE FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = ARABINAN FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = MANNAN FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = GALACTAN FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = TAR FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = CASO4 FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = CAH2O2 FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = ASH FRACS = .980 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" "; Formerly centrifuges" ";THE FRACTIONAL SPLITS ARE BASED ON THE PDU VENDOR TESTS" ";THAT SHOWED AN OUTLET SOLIDS CONCENTRATION OF" ";30% AND 98% RECOVERY OF INSOLUBLE SOLIDS FOR CENTRIFUGES." ";SOLUBLE COMPONENTS ARE SPLIT SO THAT THE LIQUID FRACTION OF" ";EACH STREAM HAS THE SAME COMPOSITION." ";KI 3/22/02:" ";ALL WNUTR, CNUTR & CSL SHOULD HAVE BEEN CONSUMED &" ";SO ANY REMAINING SHOULD GO OFF TO WWT SO THAT THE RECYCLE WILL BE" ";CORRECT." ) \ ? BLOCK SEP2 "T507-8" ? ; "SET1_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "MOLE SIEVE" \ \ PARAM PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = GLUCOSE / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = CELLULOS / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = XYLOSE / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = XYLAN / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = LIGNIN / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = CELLULAS / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = BIOMASS / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = ZYMO / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = UNKNOWN / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = SOLSLDS / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = GYPSUM / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = ACETATE / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = LGNSOL / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = HMF / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = ARABINOS / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = GALACTOS / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = MANNOSE / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = ARABINAN / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = MANNAN / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = GALACTAN / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = GLUCOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = CELLOB / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = XYLOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = TAR / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = MANOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = GALAOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = ARABOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = ACETOLIG / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = XYLITOL / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = EXTRACT / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = PROTEIN / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = CASO4 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = CAH2O2 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = ASH / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = ETHANOL FRACS = .150 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = H2O / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = FURFURAL / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = H2SO4 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = N2 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = CO2 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = O2 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = CH4 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = NO / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = NO2 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = NH3 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = LACID / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = AACID / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = NH4OH / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = NH4SO4 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = NH4ACET / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = GLYCEROL / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = SUCCACID / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = DAP / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = PROPANE / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = DENAT / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = OIL / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = CSL / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = CNUTR / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = WNUTR / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = SO2 / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = H2S / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = C / PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = CO / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = GLUCOSE FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CELLULOS FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = XYLOSE FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = XYLAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = LIGNIN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CELLULAS FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = BIOMASS FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = ZYMO FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = UNKNOWN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = SOLSLDS FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = GYPSUM FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = ACETATE FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = LGNSOL FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = HMF FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = ARABINOS FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = GALACTOS FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = MANNOSE FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = ARABINAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = MANNAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = GALACTAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = GLUCOLIG FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CELLOB FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = XYLOLIG FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = TAR FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = MANOLIG FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = GALAOLIG FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = ARABOLIG FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = ACETOLIG FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = XYLITOL FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = EXTRACT FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = PROTEIN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CASO4 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CAH2O2 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = ASH FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = ETHANOL / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = H2O FRACS = .0050 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = FURFURAL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = H2SO4 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = N2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CO2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = O2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CH4 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = NO FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = NO2 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = NH3 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = LACID FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = AACID FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = NH4OH FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = NH4SO4 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = NH4ACET FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = GLYCEROL FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = SUCCACID FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = DAP FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = PROPANE FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = DENAT FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = OIL FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CSL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CNUTR FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = WNUTR FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = SO2 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = H2S FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = C FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CO FRACS = 0.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = CELLULOS / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = XYLAN / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = LIGNIN / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = CELLULAS / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = BIOMASS / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = ZYMO / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = GYPSUM / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = ACETATE / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = ARABINAN / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = MANNAN / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = GALACTAN / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = TAR / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = CASO4 / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = CAH2O2 / PARAM-SUBS = CISOLID PARAM-STREAM = 515A COMPS = ASH / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = CELLULOS FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = XYLAN FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = LIGNIN FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = CELLULAS FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = BIOMASS FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = ZYMO FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = GYPSUM FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = ACETATE FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = ARABINAN FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = MANNAN FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = GALACTAN FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = TAR FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = CASO4 FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = CAH2O2 FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = ASH FRACS = 1.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ";BLOCK H506+ HEATER" "; DESCRIPTION ""Steam side of EtOH Superheater before Mole Sieve""" "; PARAM PRES=0.0 VFRAC=0.0" ";;" "; AS PER THE DELTA-T SIMULATION" "; Overheads" "; Bottoms" ) \ ? BLOCK HEATER AFLSH ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "PRESSURE REDUCER FOR FERMENTATION AIR" \ \ PARAM TEMP = 40.0 <22> <4> PRES = 1.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER CHILOP ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "CHILLED WATER OPERATING REQUIREMENT CALC" \ \ PARAM PRES = 0.0 <20> <3> DELT = 4.0 <31> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER CHILWAT ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "CHILLED WATER CAPITAL REQUIREMENT CALC" \ \ PARAM PRES = 0.0 <20> <3> DELT = 4.0 <31> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER CWATCAP ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "COOLING WATER REQUIREMENT CALC FOR CAPITAL COST" \ \ PARAM PRES = 0.0 <20> <3> DELT = 9.0 <31> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER CWATOP ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "COOLING WATER REQUIREMENT CALC FOR OPERATING COST" \ \ PARAM PRES = 0.0 <20> <3> DELT = 9.0 <31> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER CWFLSH ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "COOLING TOWER FLASH CALC" \ \ PARAM TEMP = 28.0 <22> <4> VFRAC = 1.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER DCOOL2 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "DUMMY COOLER / AMBIENT COOLING IN S505" \ \ PARAM TEMP = 70.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER DCOOLE ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "DUMMY COOLER TO SET ETHANOL DENSITY" \ \ PARAM TEMP = 20.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ";-----------------------------------------------------------" "; STORAGE BLOCKS - AREA 700" ";-----------------------------------------------------------" ";;" ) \ ? BLOCK HEATER E501LB ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "AUXILIARY STEAM CONDENSOR" \ \ PARAM PRES = 0.0 <20> <3> VFRAC = 0.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER E502V ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "2ND EFFECT CONDENSER" \ \ PARAM VFRAC = 0.0 <0> <0> DELT = 0.0 <31> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER E503V ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "3RD EFFECT CONDENSER" \ \ PARAM VFRAC = 0.0 <0> <0> DELT = 0.0 <31> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER H200 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "HYDROLYSATE SLURRY COOLER" \ \ PARAM TEMP = 50.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H201+" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "FEED CROSS EXCHANGER (HOT SIDE)" \ \ PARAM PRES = 1.0 <20> <3> VFRAC = 0.0 <0> <0> \ \ PROPERTIES OPSETNAME = "NRTL-HOC" \ \ COMMENTS COMMENTS = ( ";;" ";;" ";-------------------------------------------------------------" "; DISTILLATION BLOCKS - AREA 500" ";-------------------------------------------------------------" ";;" ) \ ? BLOCK HEATER "H201-" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "FEED CROSS EXCHANGER (COLD SIDE)" \ \ PARAM PRES = 4.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ";Temp is specified by D-Spec H201TEMP" ) \ ? BLOCK HEATER H244 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "COOL BLOWDOWN VAPOR PRIOR TO WWT" \ \ PARAM TEMP = 35.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H301-" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "HYDROLYSATE SLURRY HEATER FOR SACCH." \ \ PARAM TEMP = 67.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER H302 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "SACCHARIFIED SLURRY COOLER BEFORE FERMENTATION" \ \ PARAM TEMP = 41.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER H415 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "COOLER FOR CELLULASE PRODUCTION FERMENTOR WATER" \ \ PARAM TEMP = 40.0 <22> <4> PRES = 1.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER H503 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "COOL DOWN SEPARATED WATER & REGEN LOSSES" \ \ PARAM TEMP = 35.0 <22> <4> PRES = .136091928 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ";;" ) \ ? BLOCK HEATER "H506-" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "PROCESS SIDE OF ETOH SUPERHEATER BEFORE MOLE SIEVE" \ \ PARAM TEMP = 116.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H507+" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "PROD/REGEN RECYCLE INTERCHANGER, REGEN SIDE" \ \ PARAM TEMP = 91.70 <22> <4> PRES = 1.440 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H507-" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "PROD/REGEN RECYCLE INTERCHANGER, PROD SIDE" \ \ PARAM PRES = 1.53103419 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER H509 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "PRODUCT ETHANOL CONDENSER AND COOLER AFTER MOLE SIEVE" \ \ PARAM TEMP = 38.0 <22> <4> PRES = 1.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H512+" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "BEED COL BTMS/FEED INTERCHANGER, BTMS SIDE" \ \ PARAM PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H512-" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "BEER COLUMN BTMS/FEED INTERCHANGER, FEED SIDE" \ \ PARAM TEMP = 100.0 <22> <4> PRES = 4.76321748 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER H517 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "FINAL CONDENSER ON EVAPORATOR" \ \ PARAM VFRAC = 0.0 <0> <0> DELT = 0.0 <31> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER H602 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "COOLER TO BRING WASTEWATER TO ANAEROBIC TEMP" \ \ PARAM TEMP = 35.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H801+" ? ; "SET1_MOLE" ; ; HEATER ; \ PARAM TEMP = 157.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H801-" ? ; "SET1_MOLE" ; ; HEATER ; \ PARAM PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H811+" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "BOILER ECONOMIZER" \ \ PARAM TEMP = 176.666666 <22> <4> PRES = -.680 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H811-A" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "BFW HEATER-SENSIBLE" \ \ PARAM PRES = -.680 <20> <3> VFRAC = 1.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER "H811-B" ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "BFW HEATER-LATENT" \ \ PARAM PRES = 0.0 <20> <3> VFRAC = 0.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER H910 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "WATER STERILIZER" \ \ PARAM TEMP = 121.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER H914 ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "WELL WATER COOLER FOR SSCF BROTH" \ \ PARAM TEMP = 26.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER M202LO ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "HEATER TO GET FLUIDS TO RXN TEMP" \ \ PARAM TEMP = 100.0 <22> <4> PRES = 39.260 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER M205COOL ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "COOLER FOR COMPRESSED PNEUMAPRESS AIR" \ \ PARAM TEMP = 40.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER M505COOL ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "COOLER FOR COMPRESSED PNEUMAMPRESS AIR" \ \ PARAM TEMP = 40.0 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER M801CND ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "DRYER OFFGAS CONDENSER" \ \ PARAM TEMP = 50.0 <22> <4> PRES = 1.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER M801STM ? ; "SET1_MOLE" ; ; HEATER ; \ PARAM TEMP = 120.0 <22> <4> VFRAC = 0.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER M803HEAT ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "GAS SIDE OF STEAM BOILER" \ \ PARAM TEMP = 278.30 <22> <4> PRES = 0.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER M803SHTR ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "BOILER SUPERHEATER" \ \ PARAM TEMP = 510.000002 <22> <4> PRES = 86.0577306 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER M811CND ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "STEAM SYSTEM CONDENSOR" \ \ PARAM PRES = 0.0 <20> <3> VFRAC = 0.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK HEATER STMHX ? ; "SET1_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "MANIFOLD STEAM FOR HEATING" \ \ PARAM PRES = 4.0 <20> <3> VFRAC = 0.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 E501L ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "1ST EFFECT LIQUID SIDE" \ \ PARAM PRES = .3840 <20> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ PROPERTIES OPSETNAME = "NRTL-HOC" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 E502L ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "2ND EFFECT LIQUID SIDE" \ \ PARAM PRES = .2890 <20> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ PROPERTIES OPSETNAME = "NRTL-HOC" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 E503L ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "3RD EFFECT LIQUID SIDE" \ \ PARAM PRES = .2110 <20> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ PROPERTIES OPSETNAME = "NRTL-HOC" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 F300FLSH ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "DUMMY BLOCK TO RELEASE GASES FROM FERM" \ \ PARAM PRES = 1.0 <20> <3> DUTY = 0.0 <13> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 "F301-6FL" ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "SEED CO2 VENT" \ \ PARAM PRES = 1.0 <20> <3> DUTY = 0.0 <13> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 F400FL ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "CELLULASE PRODUCTION DUMMY FOR FLASH CALC." \ \ PARAM PRES = 0.0 <20> <3> DUTY = 0.0 <13> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 "F401-4FL" ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "CELLULASE SEED DUMMY FOR FLASH CALC." \ \ PARAM PRES = 1.0 <20> <3> DUTY = 0.0 <13> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 H205 ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "CONDENSER ON PNEUMAPRESS VENT" \ \ PARAM TEMP = 38.0 <22> <4> PRES = 0.0 <20> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 M801FLSH ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "CAKE DRYER PRIOR TO BOILER" \ \ PARAM PRES = 1.0 <20> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ PROPERTIES OPSETNAME = "NRTL-HOC" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 M803BD ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "STEAM SIDE OF THE FLUIDIZED BED BOILER" \ \ PARAM PRES = 96.2646252 <20> <3> VFRAC = .970 <0> <0> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 S205FLSH ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "AIR-SOLID CONTACT IN PNEUMAPRESS" \ \ PARAM PRES = 0.0 <20> <3> DUTY = 0.0 <13> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 S505FLSH ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "AIR-SOLIDS CONTACT IN PNEUMAPRESS" \ \ PARAM PRES = 0.0 <20> <3> DUTY = 0.0 <13> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 STMMAN ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "STEAM MANIFOLD" \ \ PARAM PRES = 4.42290 <20> <3> DUTY = 0.0 <13> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 T203 ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "PREHYDROLYSIS BLOWDOWN TANK" \ \ PARAM PRES = 1.0 <20> <3> DUTY = 0.0 <13> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ PROPERTIES OPSETNAME = "NRTL-HOC" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 T606FLSH ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "FLASH FOR ANAEROBIC DIGESTION" \ \ PARAM PRES = 1.0 <20> <3> DUTY = 0.0 <13> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 T608FLSH ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "FLASH FOR AEROBIC TREATMENT" \ \ PARAM PRES = 0.0 <20> <3> DUTY = 0.0 <13> <3> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK FLASH2 T826 ? ; "SET1_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "BOILER WATER DEAERATOR" \ \ PARAM PRES = -.10 <20> <3> VFRAC = 0.0 <0> <0> \ \ FRAC SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK RADFRAC D501 ? ; "ENG_MOLE" ; ; FRACT1 ; \ PARAM NSTAGE = 16 ALGORITHM = NONIDEAL MAXOL = 100 SOLID-BAL = STAGE OPT-PRES = "DP-COL" OPT-PRES-TOP = "DP-COND" CONV-METH = NONIDEAL NSTAGEMAX = 17 \ \ "COL-CONFIG" CONDENSER = "PARTIAL-V" \ \ FEEDS FEED-SID = 506 FEED-STAGE = 2 \ \ PRODUCTS PROD-STREAM = 508 PROD-STAGE = 1 PROD-PHASE = V / PROD-STREAM = 510 PROD-STAGE = 3 PROD-PHASE = V FLOW-BASIS = MASS PROD-FLOW = 105000.0 <-80> <2> / PROD-STREAM = 518 PROD-STAGE = 16 PROD-PHASE = L \ \ H-PRODUCTS H-PROD-SID = QCD501 H-PROD-STAGE = 1 / H-PROD-SID = QRD501 H-PROD-STAGE = 16 \ \ "P-SPEC2" PRES1 = 27.40 <20> <2> \ \ "COL-SPECS" DP-COL = 3.0 <75> <2> RDV-BASIS = MOLE BASIS-RDV = 1.0 <-1> <0> D-BASIS = MASS BASIS-D = 1050.0 <-80> <2> RR-BASIS = MOLE BASIS-RR = 3.0 <-1> <0> DP-COND = .50 <75> <2> \ \ T-EST TEMP-STAGE = 1 TEMP-EST = 140.0 <22> <2> / TEMP-STAGE = 2 TEMP-EST = 235.0 <22> <2> / TEMP-STAGE = 5 TEMP-EST = 239.0 <22> <2> / TEMP-STAGE = 7 TEMP-EST = 243.0 <22> <2> / TEMP-STAGE = 9 TEMP-EST = 246.0 <22> <2> / TEMP-STAGE = 11 TEMP-EST = 248.0 <22> <2> / TEMP-STAGE = 13 TEMP-EST = 252.0 <22> <2> \ \ SPEC SPEC-NO = 1 SPEC-TYPE = TEMP VALUE = 140.0 <0> <0> SCALE = 1.0 <0> <0> SPEC-STAGE = 1 \ \ SPEC SPEC-NO = 2 SPEC-TYPE = "MASS-FRAC" VALUE = .00050 <0> <0> SPEC-STAGE = 16 SPEC-COMPS = ( ETHANOL ) OPT-SPC-STR = INTERNAL \ \ VARY VARY-NO = 1 VARTYPE = VPROD LB = 60000.0 <0> <0> UB = 120000.0 <0> <0> VARY-STAGE = 3 \ \ VARY VARY-NO = 2 VARTYPE = D LB = 800.0 <0> <0> UB = 1100.0 <0> <0> \ \ TRAY-SIZE TS-SECNO = 1 TS-STAGE1 = 2 TS-STAGE2 = 15 TS-TRAYTYPE = SIEVE \ \ "KLL-VECS" \ \ "SIZE-DATA" COND = YES REB = YES \ \ "TRSZ-VECS" \ \ "PCKSR-VECS" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK RADFRAC VNTSCRUB ? ; "SET1_MOLE" ; ; FRACT1 ; \ PARAM NSTAGE = 4 VIEW-PRES = PROFILE NSTAGEMAX = 5 \ \ "COL-CONFIG" CONDENSER = NONE REBOILER = NONE \ \ FEEDS FEED-SID = 523 FEED-STAGE = 4 FEED-CONVEN = "ON-STAGE" FEED-CONVE2 = "ON-STAGE" / FEED-SID = 524 FEED-STAGE = 1 \ \ PRODUCTS PROD-STREAM = 550 PROD-STAGE = 1 PROD-PHASE = V / PROD-STREAM = 551 PROD-STAGE = 4 PROD-PHASE = L \ \ P-SPEC PRES-STAGE = 1 STAGE-PRES = .90 <20> <3> \ \ "P-SPEC2" PRES1 = .90 <20> <3> \ \ "COL-SPECS" RDV-BASIS = MOLE BASIS-RDV = 1.0 <-1> <0> \ \ "KLL-VECS" \ \ "TRSZ-VECS" \ \ "PCKSR-VECS" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK RSTOIC F300CONT ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "FERMENTORS CONTAMINATION BLOCK" \ \ PARAM TEMP = 41.0 <22> <4> PRES = 1.0 <20> <3> SERIES = NO \ \ STOIC REACNO = 1 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 3 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 4 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 5 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = 1.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" "; ALL FERMENTABLE SUGARS ARE CONVERTED TO LACTIC ACID IN THIS BLOCK" "; THE FRACTION OF SUGAR LOST TO CONTAMINATION IS SET IN CONTSPLT" ) \ ? BLOCK RSTOIC F300F ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "FERMENTORS FERMENTATION BLOCK" \ \ PARAM TEMP = 41.0 <22> <4> PRES = 1.0 <20> <3> SERIES = NO \ \ STOIC REACNO = 7 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = CSL STOIC-SSID = MIXED COEF = -.046960 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = DAP STOIC-SSID = MIXED COEF = -.0180 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 16 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = CSL STOIC-SSID = MIXED COEF = -.039130 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = DAP STOIC-SSID = MIXED COEF = -.0150 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 19 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 19 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 20 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 20 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 21 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 22 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 26 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 27 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 27 STOIC-CID = CSL STOIC-SSID = MIXED COEF = -.039130 <0> <0> \ \ STOIC REACNO = 27 STOIC-CID = DAP STOIC-SSID = MIXED COEF = -.0150 <0> <0> \ \ STOIC REACNO = 28 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 28 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 29 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 29 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 30 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 31 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 35 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 36 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 36 STOIC-CID = CSL STOIC-SSID = MIXED COEF = -.046960 <0> <0> \ \ STOIC REACNO = 36 STOIC-CID = DAP STOIC-SSID = MIXED COEF = -.0180 <0> <0> \ \ STOIC REACNO = 37 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 37 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 38 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 38 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 39 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 40 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 44 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 45 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 45 STOIC-CID = CSL STOIC-SSID = MIXED COEF = -.046960 <0> <0> \ \ STOIC REACNO = 45 STOIC-CID = DAP STOIC-SSID = MIXED COEF = -.0180 <0> <0> \ \ STOIC REACNO = 46 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 46 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 47 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 47 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 48 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 49 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = ZYMO STOIC-SSID1 = CISOLID COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.40 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = GLYCEROL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = SUCCACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = ZYMO STOIC-SSID1 = CISOLID COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 18 STOIC-CID1 = GLYCEROL STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 18 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 2.50 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = XYLITOL STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = .50 <0> <0> \ \ STOIC1 REACNO1 = 20 STOIC-CID1 = SUCCACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 20 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 2.50 <0> <0> \ \ STOIC1 REACNO1 = 21 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 22 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 26 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 26 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 27 STOIC-CID1 = ZYMO STOIC-SSID1 = CISOLID COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 27 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 28 STOIC-CID1 = GLYCEROL STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 28 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 2.50 <0> <0> \ \ STOIC1 REACNO1 = 29 STOIC-CID1 = SUCCACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 29 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 2.50 <0> <0> \ \ STOIC1 REACNO1 = 30 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 31 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 35 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 35 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 36 STOIC-CID1 = ZYMO STOIC-SSID1 = CISOLID COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 36 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.40 <0> <0> \ \ STOIC1 REACNO1 = 37 STOIC-CID1 = GLYCEROL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 37 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 38 STOIC-CID1 = SUCCACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 38 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 39 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 40 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 44 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 44 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 45 STOIC-CID1 = ZYMO STOIC-SSID1 = CISOLID COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 45 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.40 <0> <0> \ \ STOIC1 REACNO1 = 46 STOIC-CID1 = GLYCEROL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 46 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 47 STOIC-CID1 = SUCCACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 47 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 48 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 49 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ CONVEX EXT-REACNO = 7 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .950 <0> <0> \ \ CONVEX EXT-REACNO = 8 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .020 <0> <0> \ \ CONVEX EXT-REACNO = 9 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0040 <0> <0> \ \ CONVEX EXT-REACNO = 10 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0060 <0> <0> \ \ CONVEX EXT-REACNO = 11 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0150 <0> <0> \ \ CONVEX EXT-REACNO = 12 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0020 <0> <0> \ \ CONVEX EXT-REACNO = 16 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .850 <0> <0> \ \ CONVEX EXT-REACNO = 17 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0190 <0> <0> \ \ CONVEX EXT-REACNO = 18 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0030 <0> <0> \ \ CONVEX EXT-REACNO = 19 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0460 <0> <0> \ \ CONVEX EXT-REACNO = 20 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0090 <0> <0> \ \ CONVEX EXT-REACNO = 21 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0140 <0> <0> \ \ CONVEX EXT-REACNO = 22 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0020 <0> <0> \ \ CONVEX EXT-REACNO = 26 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .850 <0> <0> \ \ CONVEX EXT-REACNO = 27 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .0190 <0> <0> \ \ CONVEX EXT-REACNO = 28 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .0030 <0> <0> \ \ CONVEX EXT-REACNO = 29 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .0150 <0> <0> \ \ CONVEX EXT-REACNO = 30 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .0140 <0> <0> \ \ CONVEX EXT-REACNO = 31 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .0020 <0> <0> \ \ CONVEX EXT-REACNO = 35 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .850 <0> <0> \ \ CONVEX EXT-REACNO = 36 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .0190 <0> <0> \ \ CONVEX EXT-REACNO = 37 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .0030 <0> <0> \ \ CONVEX EXT-REACNO = 38 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .0150 <0> <0> \ \ CONVEX EXT-REACNO = 39 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .0140 <0> <0> \ \ CONVEX EXT-REACNO = 40 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .0020 <0> <0> \ \ CONVEX EXT-REACNO = 44 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .850 <0> <0> \ \ CONVEX EXT-REACNO = 45 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .0190 <0> <0> \ \ CONVEX EXT-REACNO = 46 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .0030 <0> <0> \ \ CONVEX EXT-REACNO = 47 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .0150 <0> <0> \ \ CONVEX EXT-REACNO = 48 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .0140 <0> <0> \ \ CONVEX EXT-REACNO = 49 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .0020 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" "; THE FERMENTATION REACTIONS ARE CALCULATED IN THIS BLOCK" ";;" ) \ ? BLOCK RSTOIC "F301-6F" ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "SSCF SEED FERMENTORS FERMENTATION" \ \ PARAM TEMP = 41.0 <22> <4> PRES = 1.0 <20> <3> SERIES = NO \ \ STOIC REACNO = 7 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = CSL STOIC-SSID = MIXED COEF = -.046960 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = DAP STOIC-SSID = MIXED COEF = -.0180 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 16 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = CSL STOIC-SSID = MIXED COEF = -.039130 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = DAP STOIC-SSID = MIXED COEF = -.0150 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 19 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 19 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 20 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 20 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 21 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 22 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 26 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 27 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 27 STOIC-CID = CSL STOIC-SSID = MIXED COEF = -.039130 <0> <0> \ \ STOIC REACNO = 27 STOIC-CID = DAP STOIC-SSID = MIXED COEF = -.0150 <0> <0> \ \ STOIC REACNO = 28 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 28 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 29 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 29 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 30 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 31 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 35 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 36 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 36 STOIC-CID = CSL STOIC-SSID = MIXED COEF = -.046960 <0> <0> \ \ STOIC REACNO = 36 STOIC-CID = DAP STOIC-SSID = MIXED COEF = -.0180 <0> <0> \ \ STOIC REACNO = 37 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 37 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 38 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 38 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 39 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 40 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 44 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 45 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 45 STOIC-CID = CSL STOIC-SSID = MIXED COEF = -.046960 <0> <0> \ \ STOIC REACNO = 45 STOIC-CID = DAP STOIC-SSID = MIXED COEF = -.0180 <0> <0> \ \ STOIC REACNO = 46 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 46 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 47 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 47 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 48 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 49 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = ZYMO STOIC-SSID1 = CISOLID COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.40 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = GLYCEROL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = SUCCACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = ZYMO STOIC-SSID1 = CISOLID COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 18 STOIC-CID1 = GLYCEROL STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 18 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 2.50 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = XYLITOL STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = .50 <0> <0> \ \ STOIC1 REACNO1 = 20 STOIC-CID1 = SUCCACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 20 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 2.50 <0> <0> \ \ STOIC1 REACNO1 = 21 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 22 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 26 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 26 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 27 STOIC-CID1 = ZYMO STOIC-SSID1 = CISOLID COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 27 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 28 STOIC-CID1 = GLYCEROL STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 28 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 2.50 <0> <0> \ \ STOIC1 REACNO1 = 29 STOIC-CID1 = SUCCACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 29 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 2.50 <0> <0> \ \ STOIC1 REACNO1 = 30 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 31 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 35 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 35 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 36 STOIC-CID1 = ZYMO STOIC-SSID1 = CISOLID COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 36 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.40 <0> <0> \ \ STOIC1 REACNO1 = 37 STOIC-CID1 = GLYCEROL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 37 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 38 STOIC-CID1 = SUCCACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 38 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 39 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 40 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 44 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 44 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 45 STOIC-CID1 = ZYMO STOIC-SSID1 = CISOLID COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 45 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.40 <0> <0> \ \ STOIC1 REACNO1 = 46 STOIC-CID1 = GLYCEROL STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 46 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 47 STOIC-CID1 = SUCCACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 47 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 48 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 49 STOIC-CID1 = LACID STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ CONVEX EXT-REACNO = 7 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .90 <0> <0> \ \ CONVEX EXT-REACNO = 8 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .040 <0> <0> \ \ CONVEX EXT-REACNO = 9 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0040 <0> <0> \ \ CONVEX EXT-REACNO = 10 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0060 <0> <0> \ \ CONVEX EXT-REACNO = 11 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0150 <0> <0> \ \ CONVEX EXT-REACNO = 12 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0020 <0> <0> \ \ CONVEX EXT-REACNO = 16 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .80 <0> <0> \ \ CONVEX EXT-REACNO = 17 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .040 <0> <0> \ \ CONVEX EXT-REACNO = 18 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0030 <0> <0> \ \ CONVEX EXT-REACNO = 19 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0460 <0> <0> \ \ CONVEX EXT-REACNO = 20 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0090 <0> <0> \ \ CONVEX EXT-REACNO = 21 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0140 <0> <0> \ \ CONVEX EXT-REACNO = 22 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0020 <0> <0> \ \ CONVEX EXT-REACNO = 26 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .80 <0> <0> \ \ CONVEX EXT-REACNO = 27 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .040 <0> <0> \ \ CONVEX EXT-REACNO = 28 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .0030 <0> <0> \ \ CONVEX EXT-REACNO = 29 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .0150 <0> <0> \ \ CONVEX EXT-REACNO = 30 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .0140 <0> <0> \ \ CONVEX EXT-REACNO = 31 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .0020 <0> <0> \ \ CONVEX EXT-REACNO = 35 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .80 <0> <0> \ \ CONVEX EXT-REACNO = 36 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .040 <0> <0> \ \ CONVEX EXT-REACNO = 37 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .0030 <0> <0> \ \ CONVEX EXT-REACNO = 38 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .0150 <0> <0> \ \ CONVEX EXT-REACNO = 39 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .0140 <0> <0> \ \ CONVEX EXT-REACNO = 40 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .0020 <0> <0> \ \ CONVEX EXT-REACNO = 44 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .80 <0> <0> \ \ CONVEX EXT-REACNO = 45 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .040 <0> <0> \ \ CONVEX EXT-REACNO = 46 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .0030 <0> <0> \ \ CONVEX EXT-REACNO = 47 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .0150 <0> <0> \ \ CONVEX EXT-REACNO = 48 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .0140 <0> <0> \ \ CONVEX EXT-REACNO = 49 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .0020 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" "; THE SEED FERMENTATION REACTIONS ARE CALCULATED IN THIS BLOCK" ";;" "; THE CONVERSTIONS TO ETHANOL ARE BASED ON EPD0005 RUN" "; MODIFIED SO THAT 4% OF MONOMERIC SUGARS ARE CONVERTED" "; TO CELL MASS AND ALL SUGARS ARE CONSUMED." ";;" ) \ ? BLOCK RSTOIC F400 ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "CELLULASE FERMENTOR" \ \ PARAM TEMP = 28.0 <22> <4> PRES = 1.66032150 <20> <3> \ \ STOIC REACNO = 1 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -7.452170 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -7.452170 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -7.452170 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.452170 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.452170 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -8.458620 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.024140 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -8.458620 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.024140 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -8.458620 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.024140 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.458620 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.024140 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.458620 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.024140 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -2.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -8.458620 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.024140 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = MANNAN STOIC-SSID = CISOLID COEF = -2.0 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -8.458620 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.024140 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = GALACTAN STOIC-SSID = CISOLID COEF = -2.0 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -8.458620 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.024140 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 9.934780 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 7.652170 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 9.934780 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 7.652170 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 9.934780 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 7.652170 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 7.934780 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.652170 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 7.934780 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.652170 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 10.79310 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 8.551720 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = CELLULAS STOIC-SSID1 = CISOLID COEF1 = 3.448280 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 10.79310 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 8.551720 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = CELLULAS STOIC-SSID1 = CISOLID COEF1 = 3.448280 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 10.79310 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 8.551720 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = CELLULAS STOIC-SSID1 = CISOLID COEF1 = 3.448280 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 8.79310 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.551720 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = CELLULAS STOIC-SSID1 = CISOLID COEF1 = 3.448280 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 8.79310 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.551720 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = CELLULAS STOIC-SSID1 = CISOLID COEF1 = 3.448280 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 8.79310 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 8.551720 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = CELLULAS STOIC-SSID1 = CISOLID COEF1 = 3.448280 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 8.79310 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 8.551720 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = CELLULAS STOIC-SSID1 = CISOLID COEF1 = 3.448280 <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 8.79310 <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 8.551720 <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = CELLULAS STOIC-SSID1 = CISOLID COEF1 = 3.448280 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .470 <0> <0> \ \ CONVEX EXT-REACNO = 4 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .470 <0> <0> \ \ CONVEX EXT-REACNO = 3 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .470 <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .470 <0> <0> \ \ CONVEX EXT-REACNO = 5 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .470 <0> <0> \ \ CONVEX EXT-REACNO = 6 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .530 <0> <0> \ \ CONVEX EXT-REACNO = 7 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .530 <0> <0> \ \ CONVEX EXT-REACNO = 8 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .530 <0> <0> \ \ CONVEX EXT-REACNO = 9 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .530 <0> <0> \ \ CONVEX EXT-REACNO = 10 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .530 <0> <0> \ \ CONVEX EXT-REACNO = 11 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 12 KEY-SSID = CISOLID KEY-CID = MANNAN CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 13 KEY-SSID = CISOLID KEY-CID = GALACTAN CONV = 1.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" "; SO2 and NH3 addition through stream 436 are set by FORTRAN" "; Block NUTRA. If the conversions are changed, FORTRAN must also" "; be modified." ";CONVERSIONS ARE BASED ON THE 1990 BASE CASE." ) \ ? BLOCK RSTOIC "F401-4" ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "CELLULASE SEED FERMENTOR" \ \ PARAM TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> \ \ STOIC REACNO = 1 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -7.452170 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -7.452170 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -7.452170 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.452170 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.452170 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -2.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -7.452170 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = MANNAN STOIC-SSID = CISOLID COEF = -2.0 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -7.452170 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = GALACTAN STOIC-SSID = CISOLID COEF = -2.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -7.452170 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -.015220 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 9.934780 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 7.652170 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 9.934780 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 7.652170 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 9.934780 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 7.652170 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 7.934780 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.652170 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 7.934780 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.652170 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 7.934780 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 7.652170 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 7.934780 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 7.652170 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 7.934780 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 7.652170 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.347830 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 3 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 4 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 5 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 6 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 7 KEY-SSID = CISOLID KEY-CID = MANNAN CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 8 KEY-SSID = CISOLID KEY-CID = GALACTAN CONV = 1.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" "; SO2 and NH3 addition through stream 434 is set by FORTRAN" "; block NUTRB. If conversions are changed, the FORTRAN must" "; also be modified." "; CONVERSIONS ARE BASED ON THE 1990 BASE CASE." ) \ ? BLOCK RSTOIC M202HI ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "PREHYDROLYSIS (SUNDS) REACTOR" \ \ PARAM TEMP = 190.0 <22> <4> VFRAC = 0.0 <0> <0> SERIES = NO \ \ STOIC REACNO = 1 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -2.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = XYLAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = XYLAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = XYLAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = XYLAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = MANNAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = MANNAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = MANNAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = GALACTAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = GALACTAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 14 STOIC-CID = GALACTAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = ARABINAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 16 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 16 STOIC-CID = ARABINAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = ARABINAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = ARABINAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 19 STOIC-CID = ACETATE STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 20 STOIC-CID = ACETATE STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 21 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 21 STOIC-CID = FURFURAL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 22 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 22 STOIC-CID = HMF STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 23 STOIC-CID = LIGNIN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = GLUCOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CELLOB STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = GLUCOSE STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = HMF STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = XYLOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = XYLOSE STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = FURFURAL STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = TAR STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = MANOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = MANNOSE STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = HMF STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = GALAOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = GALACTOS STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 14 STOIC-CID1 = HMF STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 14 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 15 STOIC-CID1 = ARABOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = ARABINOS STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = FURFURAL STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 18 STOIC-CID1 = TAR STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = ACETOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 20 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 21 STOIC-CID1 = TAR STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 22 STOIC-CID1 = TAR STOIC-SSID1 = CISOLID COEF1 = 1.20 <0> <0> \ \ STOIC1 REACNO1 = 23 STOIC-CID1 = LGNSOL STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .0070 <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .0070 <0> <0> \ \ CONVEX EXT-REACNO = 3 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .070 <0> <0> \ \ CONVEX EXT-REACNO = 4 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 5 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = .0250 <0> <0> \ \ CONVEX EXT-REACNO = 6 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = .90 <0> <0> \ \ CONVEX EXT-REACNO = 7 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = .050 <0> <0> \ \ CONVEX EXT-REACNO = 8 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 9 KEY-SSID = CISOLID KEY-CID = MANNAN CONV = .0250 <0> <0> \ \ CONVEX EXT-REACNO = 10 KEY-SSID = CISOLID KEY-CID = MANNAN CONV = .90 <0> <0> \ \ CONVEX EXT-REACNO = 11 KEY-SSID = CISOLID KEY-CID = MANNAN CONV = .050 <0> <0> \ \ CONVEX EXT-REACNO = 12 KEY-SSID = CISOLID KEY-CID = GALACTAN CONV = .0250 <0> <0> \ \ CONVEX EXT-REACNO = 13 KEY-SSID = CISOLID KEY-CID = GALACTAN CONV = .90 <0> <0> \ \ CONVEX EXT-REACNO = 14 KEY-SSID = CISOLID KEY-CID = GALACTAN CONV = .050 <0> <0> \ \ CONVEX EXT-REACNO = 15 KEY-SSID = CISOLID KEY-CID = ARABINAN CONV = .0250 <0> <0> \ \ CONVEX EXT-REACNO = 16 KEY-SSID = CISOLID KEY-CID = ARABINAN CONV = .90 <0> <0> \ \ CONVEX EXT-REACNO = 17 KEY-SSID = CISOLID KEY-CID = ARABINAN CONV = .050 <0> <0> \ \ CONVEX EXT-REACNO = 18 KEY-SSID = CISOLID KEY-CID = ARABINAN CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 19 KEY-SSID = CISOLID KEY-CID = ACETATE CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 20 KEY-SSID = CISOLID KEY-CID = ACETATE CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 21 KEY-SSID = MIXED KEY-CID = FURFURAL CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 22 KEY-SSID = MIXED KEY-CID = HMF CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 23 KEY-SSID = CISOLID KEY-CID = LIGNIN CONV = .050 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ";;" ) \ ? BLOCK RSTOIC M803CMB ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "FLUID BED BOILER COMBUSTOR" \ \ PARAM TEMP = 870.0 <22> <4> PRES = -.03402298 <20> <3> NPHASE = 1 SERIES = YES \ \ STOIC REACNO = 1 STOIC-CID = CH4 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = XYLAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = ARABINAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = MANNAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = LIGNIN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -12.8250 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = ACETATE STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = GALACTAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = GLUCOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = CELLOB STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -12.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = HMF STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = XYLOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 14 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 14 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = FURFURAL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 16 STOIC-CID = TAR STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 16 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = MANOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 19 STOIC-CID = GALAOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 19 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 20 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 20 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 21 STOIC-CID = ARABOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 21 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 22 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 22 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 23 STOIC-CID = ACETOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 23 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 24 STOIC-CID = AACID STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 24 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 25 STOIC-CID = LACID STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 25 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 26 STOIC-CID = CELLULAS STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 26 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.24450 <0> <0> \ \ STOIC REACNO = 27 STOIC-CID = SOLSLDS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 28 STOIC-CID = ETHANOL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 28 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 29 STOIC-CID = ZYMO STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 29 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.20 <0> <0> \ \ STOIC REACNO = 30 STOIC-CID = GLYCEROL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 30 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.50 <0> <0> \ \ STOIC REACNO = 31 STOIC-CID = SUCCACID STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 31 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.50 <0> <0> \ \ STOIC REACNO = 32 STOIC-CID = XYLITOL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 32 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.50 <0> <0> \ \ STOIC REACNO = 33 STOIC-CID = BIOMASS STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 33 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.21850 <0> <0> \ \ STOIC REACNO = 105 STOIC-CID = SO2 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 105 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -.50 <0> <0> \ \ STOIC REACNO = 105 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 66 STOIC-CID = H2S STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 66 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.50 <0> <0> \ \ STOIC REACNO = 67 STOIC-CID = N2 STOIC-SSID = MIXED COEF = -.50 <0> <0> \ \ STOIC REACNO = 67 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 99 STOIC-CID = H2SO4 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 100 STOIC-CID = NH4SO4 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 100 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 34 STOIC-CID = OIL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 34 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -25.50 <0> <0> \ \ STOIC REACNO = 35 STOIC-CID = NH4ACET STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 35 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -2.750 <0> <0> \ \ STOIC REACNO = 36 STOIC-CID = EXTRACT STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 37 STOIC-CID = PROTEIN STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 40 STOIC-CID = CO2 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 45 STOIC-CID = LGNSOL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 45 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -12.8250 <0> <0> \ \ STOIC REACNO = 101 STOIC-CID = CASO4 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 101 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 6.950 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 10.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 12.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 11.0 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 14 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 14 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 15 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 15 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 18 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 18 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 20 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 20 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 21 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 21 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 22 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 22 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 23 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 23 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 24 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 24 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 25 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 25 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 26 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = .7850 <0> <0> \ \ STOIC1 REACNO1 = 26 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 26 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = .1450 <0> <0> \ \ STOIC1 REACNO1 = 26 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = .0070 <0> <0> \ \ STOIC1 REACNO1 = 27 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.49950 <0> <0> \ \ STOIC1 REACNO1 = 27 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = .054870 <0> <0> \ \ STOIC1 REACNO1 = 27 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 27 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = .183120 <0> <0> \ \ STOIC1 REACNO1 = 27 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = .002780 <0> <0> \ \ STOIC1 REACNO1 = 28 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 28 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 29 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = .90 <0> <0> \ \ STOIC1 REACNO1 = 29 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 29 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = .10 <0> <0> \ \ STOIC1 REACNO1 = 30 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 30 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 31 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 31 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 32 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 32 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 33 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = .820 <0> <0> \ \ STOIC1 REACNO1 = 33 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 33 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = .1150 <0> <0> \ \ STOIC1 REACNO1 = 33 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = .00350 <0> <0> \ \ STOIC1 REACNO1 = 105 STOIC-CID1 = H2SO4 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 66 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 66 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 67 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 99 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 99 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 99 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = .50 <0> <0> \ \ STOIC1 REACNO1 = 100 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 100 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 100 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 34 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 18.0 <0> <0> \ \ STOIC1 REACNO1 = 34 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 17.0 <0> <0> \ \ STOIC1 REACNO1 = 35 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 35 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.50 <0> <0> \ \ STOIC1 REACNO1 = 35 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = .50 <0> <0> \ \ STOIC1 REACNO1 = 36 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.49950 <0> <0> \ \ STOIC1 REACNO1 = 36 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = .054870 <0> <0> \ \ STOIC1 REACNO1 = 36 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 36 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = .183120 <0> <0> \ \ STOIC1 REACNO1 = 36 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = .002780 <0> <0> \ \ STOIC1 REACNO1 = 37 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.49950 <0> <0> \ \ STOIC1 REACNO1 = 37 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = .054870 <0> <0> \ \ STOIC1 REACNO1 = 37 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 37 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = .183120 <0> <0> \ \ STOIC1 REACNO1 = 37 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = .002780 <0> <0> \ \ STOIC1 REACNO1 = 40 STOIC-CID1 = CO STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 40 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = .50 <0> <0> \ \ STOIC1 REACNO1 = 45 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 6.950 <0> <0> \ \ STOIC1 REACNO1 = 45 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 10.0 <0> <0> \ \ STOIC1 REACNO1 = 101 STOIC-CID1 = GYPSUM STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = CH4 CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 3 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 4 KEY-SSID = CISOLID KEY-CID = ARABINAN CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 5 KEY-SSID = CISOLID KEY-CID = MANNAN CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 6 KEY-SSID = CISOLID KEY-CID = LIGNIN CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 8 KEY-SSID = CISOLID KEY-CID = ACETATE CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 7 KEY-SSID = CISOLID KEY-CID = GALACTAN CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 9 KEY-SSID = MIXED KEY-CID = GLUCOLIG CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 10 KEY-SSID = MIXED KEY-CID = CELLOB CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 11 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 12 KEY-SSID = MIXED KEY-CID = HMF CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 13 KEY-SSID = MIXED KEY-CID = XYLOLIG CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 14 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 15 KEY-SSID = MIXED KEY-CID = FURFURAL CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 16 KEY-SSID = CISOLID KEY-CID = TAR CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 17 KEY-SSID = MIXED KEY-CID = MANOLIG CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 18 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 19 KEY-SSID = MIXED KEY-CID = GALAOLIG CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 20 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 21 KEY-SSID = MIXED KEY-CID = ARABOLIG CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 22 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 23 KEY-SSID = MIXED KEY-CID = ACETOLIG CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 24 KEY-SSID = MIXED KEY-CID = AACID CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 25 KEY-SSID = MIXED KEY-CID = LACID CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 26 KEY-SSID = CISOLID KEY-CID = CELLULAS CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 27 KEY-SSID = MIXED KEY-CID = SOLSLDS CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 28 KEY-SSID = MIXED KEY-CID = ETHANOL CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 29 KEY-SSID = CISOLID KEY-CID = ZYMO CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 30 KEY-SSID = MIXED KEY-CID = GLYCEROL CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 31 KEY-SSID = MIXED KEY-CID = SUCCACID CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 32 KEY-SSID = MIXED KEY-CID = XYLITOL CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 33 KEY-SSID = CISOLID KEY-CID = BIOMASS CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 105 KEY-SSID = MIXED KEY-CID = SO2 CONV = .010 <0> <0> \ \ CONVEX EXT-REACNO = 66 KEY-SSID = MIXED KEY-CID = H2S CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 67 EXTENT = .0010 <11> <3> OPT-EXT-CONV = EXTENT \ \ CONVEX EXT-REACNO = 99 KEY-SSID = MIXED KEY-CID = H2SO4 CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 100 KEY-SSID = MIXED KEY-CID = NH4SO4 CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 34 KEY-SSID = MIXED KEY-CID = OIL CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 35 KEY-SSID = MIXED KEY-CID = NH4ACET CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 36 KEY-SSID = MIXED KEY-CID = EXTRACT CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 37 KEY-SSID = MIXED KEY-CID = PROTEIN CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 40 EXTENT = .00010 <11> <3> OPT-EXT-CONV = EXTENT \ \ CONVEX EXT-REACNO = 45 KEY-SSID = MIXED KEY-CID = LGNSOL CONV = .990 <0> <0> \ \ CONVEX EXT-REACNO = 101 KEY-SSID = MIXED KEY-CID = CASO4 CONV = 1.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK RSTOIC T209 ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "OVERLIMING TANK T-209" \ \ PARAM TEMP = 50.0 <22> <4> PRES = 0.0 <20> <3> NPHASE = 1 PHASE = L \ \ STOIC REACNO = 1 STOIC-CID = H2SO4 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = CAH2O2 STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = GYPSUM STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = H2SO4 CONV = 1.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK RSTOIC T224 ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "REACIDIFICATION TANK" \ \ PARAM PRES = 0.0 <20> <3> DUTY = 0.0 <13> <3> \ \ STOIC REACNO = 1 STOIC-CID = H2SO4 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = CAH2O2 STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = H2SO4 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CAH2O2 STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 14 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = CELLOB STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = GYPSUM STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CASO4 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = TAR STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = TAR STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = TAR STOIC-SSID1 = CISOLID COEF1 = 1.20 <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = TAR STOIC-SSID1 = CISOLID COEF1 = 1.20 <0> <0> \ \ STOIC1 REACNO1 = 14 STOIC-CID1 = TAR STOIC-SSID1 = CISOLID COEF1 = 1.20 <0> <0> \ \ STOIC1 REACNO1 = 15 STOIC-CID1 = TAR STOIC-SSID1 = CISOLID COEF1 = 2.40 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = CISOLID KEY-CID = CAH2O2 CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = CISOLID KEY-CID = CAH2O2 CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 10 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 11 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 12 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 13 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 14 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 15 KEY-SSID = MIXED KEY-CID = CELLOB CONV = 0.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK RSTOIC T310 ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "SSCF FERMENTORS HYDROLYSIS BLOCK" \ \ PARAM TEMP = 65.0 <22> <4> PRES = 1.0 <20> <3> SERIES = NO \ \ STOIC REACNO = 1 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -2.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = GLUCOLIG STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = GLUCOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = CELLOB STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = XYLAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 14 STOIC-CID = XYLAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 14 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = XYLOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 23 STOIC-CID = ARABINAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 24 STOIC-CID = ARABINAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 24 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 25 STOIC-CID = ARABOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 25 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 32 STOIC-CID = GALACTAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 33 STOIC-CID = GALACTAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 33 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 34 STOIC-CID = GALAOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 34 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 41 STOIC-CID = MANNAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 42 STOIC-CID = MANNAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 42 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 43 STOIC-CID = MANOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 43 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = GLUCOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CELLOB STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = GLUCOSE STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = CELLOB STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = GLUCOSE STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = GLUCOSE STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = XYLOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 14 STOIC-CID1 = XYLOSE STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 15 STOIC-CID1 = XYLOSE STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 23 STOIC-CID1 = ARABOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 24 STOIC-CID1 = ARABINOS STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 25 STOIC-CID1 = ARABINOS STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 32 STOIC-CID1 = GALAOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 33 STOIC-CID1 = GALACTOS STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 34 STOIC-CID1 = GALACTOS STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 41 STOIC-CID1 = MANOLIG STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 42 STOIC-CID1 = MANNOSE STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 43 STOIC-CID1 = MANNOSE STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .040 <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .0120 <0> <0> \ \ CONVEX EXT-REACNO = 3 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .90 <0> <0> \ \ CONVEX EXT-REACNO = 4 KEY-SSID = MIXED KEY-CID = GLUCOLIG CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 5 KEY-SSID = MIXED KEY-CID = GLUCOLIG CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 6 KEY-SSID = MIXED KEY-CID = CELLOB CONV = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 13 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 14 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 15 KEY-SSID = MIXED KEY-CID = XYLOLIG CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 23 KEY-SSID = CISOLID KEY-CID = ARABINAN CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 24 KEY-SSID = CISOLID KEY-CID = ARABINAN CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 25 KEY-SSID = MIXED KEY-CID = ARABOLIG CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 32 KEY-SSID = CISOLID KEY-CID = GALACTAN CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 33 KEY-SSID = CISOLID KEY-CID = GALACTAN CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 34 KEY-SSID = MIXED KEY-CID = GALAOLIG CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 41 KEY-SSID = CISOLID KEY-CID = MANNAN CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 42 KEY-SSID = CISOLID KEY-CID = MANNAN CONV = 0.0 <0> <0> \ \ CONVEX EXT-REACNO = 43 KEY-SSID = MIXED KEY-CID = MANOLIG CONV = 0.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ";BLOCK H301+ HEATER" "; DESCRIPTION ""STEAM SIDE OF HYDROLYSATE SLURRY HEATER""" "; PARAM PRES=4.0 VFRAC=0.0" ";;" "; THE HYDROLYSIS REACTIONS ARE CALCULATED IN THIS BLOCK." ";;" "; THE CONVERSTIONS TO ETHANOL ARE BASED ON PD 23 #3 MODIFIED" "; SO THAT 4% OF MONOMERIC SUGARS ARE CONVERTED TO CELL MASS" ";;" ) \ ? BLOCK RSTOIC T608 ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "AEROBIC DIGESTOR" \ \ PARAM TEMP = 21.10 <22> <4> PRES = 1.0 <20> <3> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = GLUCOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -12.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CELLOB STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = HMF STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = XYLOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = FURFURAL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = MANOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = GALAOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = ARABOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = ACETOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 16 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -2.0 <0> <0> \ \ STOIC REACNO = 16 STOIC-CID = AACID STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = LACID STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -.50 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = UNKNOWN STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 19 STOIC-CID = SOLSLDS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 20 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 20 STOIC-CID = ETHANOL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 21 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.50 <0> <0> \ \ STOIC REACNO = 21 STOIC-CID = GLYCEROL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 22 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.50 <0> <0> \ \ STOIC REACNO = 22 STOIC-CID = SUCCACID STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 23 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.50 <0> <0> \ \ STOIC REACNO = 23 STOIC-CID = XYLITOL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 24 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.750 <0> <0> \ \ STOIC REACNO = 24 STOIC-CID = NH4ACET STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 25 STOIC-CID = GLUCOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 26 STOIC-CID = MANNOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 27 STOIC-CID = GALACTOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 28 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 29 STOIC-CID = ARABINOS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 30 STOIC-CID = XYLITOL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 31 STOIC-CID = SOLSLDS STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 32 STOIC-CID = UNKNOWN STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 33 STOIC-CID = GLUCOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 34 STOIC-CID = GALAOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 35 STOIC-CID = MANOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 36 STOIC-CID = XYLOLIG STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 37 STOIC-CID = CELLOB STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 38 STOIC-CID = FURFURAL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 39 STOIC-CID = HMF STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 40 STOIC-CID = AACID STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 41 STOIC-CID = LACID STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 42 STOIC-CID = SUCCACID STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 43 STOIC-CID = GLYCEROL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 44 STOIC-CID = OIL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 45 STOIC-CID = ETHANOL STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 46 STOIC-CID = NH4ACET STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 47 STOIC-CID = EXTRACT STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 48 STOIC-CID = PROTEIN STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 49 STOIC-CID = EXTRACT STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 50 STOIC-CID = PROTEIN STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 11.0 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 12.0 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 15 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 15 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 18 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = .50 <0> <0> \ \ STOIC1 REACNO1 = 18 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = .50 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.13330 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = .054870 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = .36620 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = .002780 <0> <0> \ \ STOIC1 REACNO1 = 20 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 20 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 21 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 21 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 22 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.0 <0> <0> \ \ STOIC1 REACNO1 = 22 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 23 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 23 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 24 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.50 <0> <0> \ \ STOIC1 REACNO1 = 24 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 24 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 25 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 7.75281869 <0> <0> \ \ STOIC1 REACNO1 = 26 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 7.75281869 <0> <0> \ \ STOIC1 REACNO1 = 27 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 7.75281869 <0> <0> \ \ STOIC1 REACNO1 = 28 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 6.46062489 <0> <0> \ \ STOIC1 REACNO1 = 29 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 6.46062489 <0> <0> \ \ STOIC1 REACNO1 = 30 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 6.54746538 <0> <0> \ \ STOIC1 REACNO1 = 31 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.22970 <0> <0> \ \ STOIC1 REACNO1 = 32 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = .646071090 <0> <0> \ \ STOIC1 REACNO1 = 33 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 6.9775970 <0> <0> \ \ STOIC1 REACNO1 = 34 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 6.9775970 <0> <0> \ \ STOIC1 REACNO1 = 35 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 6.9775970 <0> <0> \ \ STOIC1 REACNO1 = 36 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 5.6854540 <0> <0> \ \ STOIC1 REACNO1 = 37 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 14.7304610 <0> <0> \ \ STOIC1 REACNO1 = 38 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.1349230 <0> <0> \ \ STOIC1 REACNO1 = 39 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 5.42695580 <0> <0> \ \ STOIC1 REACNO1 = 40 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 2.5842880 <0> <0> \ \ STOIC1 REACNO1 = 41 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 3.8764310 <0> <0> \ \ STOIC1 REACNO1 = 42 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 5.0818240 <0> <0> \ \ STOIC1 REACNO1 = 43 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 3.9631820 <0> <0> \ \ STOIC1 REACNO1 = 44 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 12.1555420 <0> <0> \ \ STOIC1 REACNO1 = 45 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 1.9825240 <0> <0> \ \ STOIC1 REACNO1 = 46 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 3.3171350 <0> <0> \ \ STOIC1 REACNO1 = 47 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.13330 <0> <0> \ \ STOIC1 REACNO1 = 47 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = .054870 <0> <0> \ \ STOIC1 REACNO1 = 47 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 47 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = .36620 <0> <0> \ \ STOIC1 REACNO1 = 47 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = .002780 <0> <0> \ \ STOIC1 REACNO1 = 48 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1.13330 <0> <0> \ \ STOIC1 REACNO1 = 48 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = .054870 <0> <0> \ \ STOIC1 REACNO1 = 48 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 48 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = .36620 <0> <0> \ \ STOIC1 REACNO1 = 48 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = .002780 <0> <0> \ \ STOIC1 REACNO1 = 49 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.22970 <0> <0> \ \ STOIC1 REACNO1 = 50 STOIC-CID1 = BIOMASS STOIC-SSID1 = CISOLID COEF1 = 4.22970 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = GLUCOLIG CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = MIXED KEY-CID = CELLOB CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 3 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 4 KEY-SSID = MIXED KEY-CID = HMF CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 5 KEY-SSID = MIXED KEY-CID = XYLOLIG CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 6 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 7 KEY-SSID = MIXED KEY-CID = FURFURAL CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 8 KEY-SSID = MIXED KEY-CID = MANOLIG CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 9 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 10 KEY-SSID = MIXED KEY-CID = GALAOLIG CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 11 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 12 KEY-SSID = MIXED KEY-CID = ARABOLIG CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 13 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 15 KEY-SSID = MIXED KEY-CID = ACETOLIG CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 16 KEY-SSID = MIXED KEY-CID = AACID CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 17 KEY-SSID = MIXED KEY-CID = LACID CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 18 KEY-SSID = MIXED KEY-CID = UNKNOWN CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 19 KEY-SSID = MIXED KEY-CID = SOLSLDS CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 20 KEY-SSID = MIXED KEY-CID = ETHANOL CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 21 KEY-SSID = MIXED KEY-CID = GLYCEROL CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 22 KEY-SSID = MIXED KEY-CID = SUCCACID CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 23 KEY-SSID = MIXED KEY-CID = XYLITOL CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 24 KEY-SSID = MIXED KEY-CID = NH4ACET CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 25 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 26 KEY-SSID = MIXED KEY-CID = MANNOSE CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 27 KEY-SSID = MIXED KEY-CID = GALACTOS CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 28 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 29 KEY-SSID = MIXED KEY-CID = ARABINOS CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 30 KEY-SSID = MIXED KEY-CID = XYLITOL CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 31 KEY-SSID = MIXED KEY-CID = SOLSLDS CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 32 KEY-SSID = MIXED KEY-CID = UNKNOWN CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 33 KEY-SSID = MIXED KEY-CID = GLUCOLIG CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 34 KEY-SSID = MIXED KEY-CID = GALAOLIG CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 35 KEY-SSID = MIXED KEY-CID = MANOLIG CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 36 KEY-SSID = MIXED KEY-CID = XYLOLIG CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 37 KEY-SSID = MIXED KEY-CID = CELLOB CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 38 KEY-SSID = MIXED KEY-CID = FURFURAL CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 39 KEY-SSID = MIXED KEY-CID = HMF CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 40 KEY-SSID = MIXED KEY-CID = AACID CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 41 KEY-SSID = MIXED KEY-CID = LACID CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 42 KEY-SSID = MIXED KEY-CID = SUCCACID CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 43 KEY-SSID = MIXED KEY-CID = GLYCEROL CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 44 KEY-SSID = MIXED KEY-CID = OIL CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 45 KEY-SSID = MIXED KEY-CID = ETHANOL CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 46 KEY-SSID = MIXED KEY-CID = NH4ACET CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 47 KEY-SSID = MIXED KEY-CID = EXTRACT CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 48 KEY-SSID = MIXED KEY-CID = PROTEIN CONV = .60 <0> <0> \ \ CONVEX EXT-REACNO = 49 KEY-SSID = MIXED KEY-CID = EXTRACT CONV = .30 <0> <0> \ \ CONVEX EXT-REACNO = 50 KEY-SSID = MIXED KEY-CID = PROTEIN CONV = .30 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ";;" ";;" ) \ ? BLOCK PUMP P811AS ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "CONDENSATE PUMP" \ \ PARAM PRES = 4.20 <20> <3> OPT-SPEC = PRES \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK PUMP P824AS ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "CONDENSATE MAKE-UP PUMP" \ \ PARAM PRES = 3.4020 <20> <3> OPT-SPEC = PRES \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK PUMP P826AS ? ; "SET1_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "BOILER FEED WATER PUMP" \ \ PARAM PRES = 98.3060042 <20> <3> OPT-SPEC = PRES \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK COMPR ACOMP ? ; "SET1_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "AIR COMPRESSOR FOR FERMENTATIONS" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = PRES PRES = 3.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK COMPR M205 ? ; "SET1_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "AIR COMPRESSOR FOR PNEUMAPRESS SYSTEM" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = DELP DELP = 8.50574550 <75> <3> SEFF = .720 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK COMPR M505 ? ; "SET1_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "AIR COMPRESSOR FOR POST-D PNEUMAPRESS SYSTEM" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = DELP DELP = 8.50574550 <75> <3> SEFF = .720 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK COMPR M802 ? ; "SET1_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "COMBUSTION FAN" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = PRES PRES = 1.01388490 <20> <3> SEFF = .750 <0> <0> NPHASE = 2 SB-MAXIT = 100 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK COMPR M811HTRB ? ; "SET1_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "HIGH PRESSURE PART OF THE STEAM TURBINE" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = PRES PRES = 13.0 <20> <3> SEFF = .850 <0> <0> MEFF = .980 <0> <0> NPHASE = 2 \ \ COMMENTS COMMENTS = ( ";;" ";EFFICIENCIES ARE FROM ABB (VENDOR) QUOTE IN" ";REI 1998 SUBCONTRACT" ) \ ? BLOCK COMPR M811ITRB ? ; "SET1_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "MEDIUM PRESSURE PART OF THE STEAM TURBINE" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = PRES PRES = 4.42298770 <20> <3> SEFF = .850 <0> <0> MEFF = .980 <0> <0> NPHASE = 2 SB-MAXIT = 100 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK COMPR M811LTRB ? ; "SET1_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "VACUUM PART OF THE STEAM TURBINE" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = PRES PRES = 1.68073531 <20> <3> SEFF = .850 <0> <0> MEFF = .980 <0> <0> NPHASE = 2 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK COMPR M811VLRB ? ; "SET1_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "VACUUM PART OF THE STEAM TURBINE" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = PRES PRES = .100027567 <20> <3> SEFF = .850 <0> <0> MEFF = .980 <0> <0> NPHASE = 2 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK DUPL CHCWDUP ? ; "SET1_MOLE" ; ; HEAT ; \ DESCRIPTION DESCRIPTION = "DUPLICATES QH914 FOR CHW AND CW CAPITAL & OP COSTING" \ \ COMMENTS COMMENTS = ( ";;" ";------------------------------------------------------------" "; UTILITY BLOCKS - AREA 900" ";------------------------------------------------------------" ";;" ) \ ? BLOCK DUPL CHWDUP ? ; "SET1_MOLE" ; ; HEAT ; \ DESCRIPTION DESCRIPTION = "DUPLICATES QCHWTOT FOR CHW CAPITAL & OP COSTING" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK DUPL CWDUP ? ; "SET1_MOLE" ; ; HEAT ; \ DESCRIPTION DESCRIPTION = "DUPLICATES QH14BCW FOR CW CAPACITY AND EVAPORATION" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK DUPL QTDUP ? ; "SET1_MOLE" ; ; HEAT ; \ DESCRIPTION DESCRIPTION = "DUPLICATES QTTOTAL FOR CW CAPITAL & OP COSTING" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK DUPL RECTDUP ? ; "SET1_MOLE" ; ; HEAT ; \ DESCRIPTION DESCRIPTION = "DUPLICATES QCD502 FOR EVAPORATOR AND CW CAPITAL" \ \ COMMENTS COMMENTS = ( ";;" ";BLOCK H502 HEATER" "; DESCRIPTION ""D502 REBOILER - STEAM DEMAND""" "; PARAM PRES=4.0 VFRAC=0.0" ";;" ";BLOCK H501 HEATER" "; DESCRIPTION ""D501 REBOILER - STEAM DEMAND""" "; PARAM PRES=4.0 VFRAC=0.0" ";;" ) \ ? BLOCK USER T606 ? ; "SET1_MOLE" ; ; SMALL ; \ DESCRIPTION DESCRIPTION = "ANAEROBIC DIGESTER" \ \ SUBROUTINE USRMODEL = USRAN4 \ \ PARAM NREAL = 5 \ \ REAL RVALUE-LIST = ( .90 <0> <0> 1.0 <0> <0> .030 <0> <0> .750 <0> <0> 1.0 <0> <0> ) \ \ FLASH-SPECS FLASH-STREAM = 613C KODE = TP TEMP = 34.9999982 <22> <4> PRES = 1.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK SSPLIT M804 ? ; "SET1_MOLE" ; ; CYCLONE ; \ DESCRIPTION DESCRIPTION = "BAGHOUSE FOR THE BOILER" \ \ PARAM SID = 810 SUBSTREAM = MIXED FRAC = 1.0 <0> <0> / SID = 810 SUBSTREAM = CISOLID / SID = 809 SUBSTREAM = MIXED / SID = 809 SUBSTREAM = CISOLID FRAC = .9880 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ";EFFICIENCY LOSS IS BASED ON HAMON-COTTRELL (VENDOR) QUOTE IN" ";REI 1998 SUBCONTRACT" ) \ ? BLOCK SSPLIT S205A ? ; "SET1_MOLE" ; ; CYCLONE ; \ DESCRIPTION DESCRIPTION = "PRE-WASH SEPARATIONS FOR S-202" \ \ PARAM1 PRES = 0.0 <20> <3> \ \ PARAM SID = 221 SUBSTREAM = MIXED / SID = 221 SUBSTREAM = CISOLID / SID = 225 SUBSTREAM = MIXED FRAC = .1450 <0> <0> / SID = 225 SUBSTREAM = CISOLID FRAC = .9950 <0> <0> \ \ PROPERTIES OPSETNAME = "NRTL-HOC" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK SSPLIT S222 ? ; "SET1_MOLE" ; ; CYCLONE ; \ DESCRIPTION DESCRIPTION = "GYPSUM REMOVAL S/L SEP" \ \ PARAM SID = 229 SUBSTREAM = MIXED FRAC = .0040 <0> <0> / SID = 229 SUBSTREAM = CISOLID FRAC = .9950 <0> <0> / SID = 230 SUBSTREAM = MIXED / SID = 230 SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK SSPLIT S614 ? ; "SET1_MOLE" ; ; CYCLONE ; \ DESCRIPTION DESCRIPTION = "DEWATERING BELT FILTER PRESS" \ \ PARAM SID = 627 SUBSTREAM = MIXED / SID = 627 SUBSTREAM = CISOLID / SID = 623 SUBSTREAM = MIXED FRAC = .10 <0> <0> / SID = 623 SUBSTREAM = CISOLID FRAC = 1.0 <0> <0> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? BLOCK SSPLIT T610 ? ; "SET1_MOLE" ; ; CYCLONE ; \ DESCRIPTION DESCRIPTION = "CLARIFIER" \ \ PARAM SID = 625 SUBSTREAM = MIXED FRAC = .10 <0> <0> / SID = 625 SUBSTREAM = CISOLID FRAC = 1.0 <0> <0> / SID = 624 SUBSTREAM = MIXED / SID = 624 SUBSTREAM = CISOLID \ \ COMMENTS COMMENTS = ( ";;" ) \ ? "DESIGN-SPEC" ACIDCONC ? ; "SET1_MOLE" ; \ DEFINE FVN = ACIDFL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 217 FVN-SUBS = MIXED FVN-COMPONEN = H2SO4 \ \ DEFINE FVN = WATFLW FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 217 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ FORTRAN FORTRAN-EXEC = ( "F ACDCNC = ACIDFL/(WATFLW+ACIDFL)" ) \ \ SPEC EXPR1 = "ACDCNC" EXPR2 = "0.011" \ \ "TOL-SPEC" TOL = "0.00001" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 212 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "100" UPPER = "10000" \ \ COMMENTS COMMENTS = ( ";;" ";-----------------------------------------------------------------------" "; DESIGN SPECIFICATIONS" "; PRETREATMENT DESIGN-SPECS" ";------------------------------------------------------------------------" ";;" ";CONTROLS THE ACID CONCENTRATION OF STREAM 217" ) \ ? "DESIGN-SPEC" CFUGE3S ? ; "SET1_MOLE" ; \ DEFINE FVN = SOLIDS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 571 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = TMIXED FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 571 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FH2O FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 571 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ FORTRAN FORTRAN-EXEC = ( "F RATIO = FH2O / (SOLIDS + TMIXED)" "F WRITE(NHSTRY,101)RATIO" "F 101 FORMAT(' CFUGE 3 DESIGN SPEC',/,' FRACTION MOISTURE',G12.5)" ) \ \ SPEC EXPR1 = "RATIO" EXPR2 = "0.45" \ \ "TOL-SPEC" TOL = "0.01" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = S505 VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 571B VARYID3 = H2O \ \ LIMITS LOWER = "0.000001" UPPER = "0.40" \ \ COMMENTS COMMENTS = ( ";;" "; Varies the split of water and most of the mixed components" "; to reach a specified solids fraction in 571. Works with" "; fortran block CFUGESLD to vary not only water but several" "; components" ";;" ) \ ? "DESIGN-SPEC" CHWFLWCP ? ; "SET1_MOLE" ; \ DEFINE FVN = QCHW FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QCHILXS \ \ SPEC EXPR1 = "QCHW" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "50" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 950A VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "1E4" UPPER = "8E6" \ \ COMMENTS COMMENTS = ( ";;" ";----------------------------------------------------------------" "; UTILITY DESIGN-SPECS" ";-----------------------------------------------------------------" ";;" ";CALCULATES THE AMOUNT OF CHILLED WATER REQUIRED TO" ";HANDLE THE LOAD FOR THE PLANT (capital)." ) \ ? "DESIGN-SPEC" CHWFLWOP ? ; "SET1_MOLE" ; \ DEFINE FVN = QCHWOP FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QCHWXS \ \ SPEC EXPR1 = "QCHWOP" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "0.0001" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 950 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "0.0000001" UPPER = "1000" \ \ COMMENTS COMMENTS = ( ";;" ";CALCULATES THE AMOUNT OF CHILLED WATER REQUIRED TO" ";HANDLE THE LOAD FOR THE PLANT (operating)." ) \ ? "DESIGN-SPEC" COMBAIR ? ; "SET1_MOLE" ; \ DEFINE FVN = O2IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 804E FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = O2OUT FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 804C FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = BNDLOW FVN-VARTYPE = PARAMETER FVN-PARAMNO = 55 \ \ DEFINE FVN = BNDHIH FVN-VARTYPE = PARAMETER FVN-PARAMNO = 56 \ \ SPEC EXPR1 = "O2IN" EXPR2 = "6.0 * O2OUT" \ \ "TOL-SPEC" TOL = "0.01" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 804 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "BNDLOW" UPPER = "BNDHIH" \ \ COMMENTS COMMENTS = ( ";;" ";----------------------------------------------------------------" "; BOILER DESIGN-SPECS" ";---------------------------------------------------------------" ";;" ";CONTROLS THE COMBUSTION AIR FOR A 20% EXCESS" ) \ ? "DESIGN-SPEC" "CT-S205A" ? ; "SET1_MOLE" ; \ DEFINE FVN = SOL225 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 225 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WAT225 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 225 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ SPEC EXPR1 = "SOL225/(SOL225+WAT225)" EXPR2 = "0.548" \ \ "TOL-SPEC" TOL = "0.001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = S205A VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 225 \ \ LIMITS LOWER = "0.01" UPPER = "1.0" \ \ COMMENTS COMMENTS = ( ";;" "; The spec of 0.548 is from Pneumapress Test #9" "; under the Harris 2000 subcontract" ) \ ? "DESIGN-SPEC" "CT-S205B" ? ; "SET1_MOLE" ; \ DEFINE FVN = SOLID FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 255 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = OTHER FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 255 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ SPEC EXPR1 = "SOLID/(OTHER+SOLID)" EXPR2 = "0.548" \ \ "TOL-SPEC" TOL = "0.001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = S205B VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 256 VARYID3 = H2O \ \ LIMITS LOWER = "0.70" UPPER = "0.999" \ \ COMMENTS COMMENTS = ( ";;" "; The spec of 0.548 is from Pneumapress Test #9" "; under the Harris 2000 subcontract" ) \ ? "DESIGN-SPEC" "CT-S222" ? ; "SET1_MOLE" ; \ DEFINE FVN = SOL229 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 229 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WAT229 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 229 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ SPEC EXPR1 = "SOL229/(SOL229+WAT229)" EXPR2 = "0.8" \ \ "TOL-SPEC" TOL = "0.001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = S222 VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 229 \ \ LIMITS LOWER = "0.0" UPPER = "1.0" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? "DESIGN-SPEC" "CT-S614" ? ; "SET1_MOLE" ; \ DEFINE FVN = SOL623 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 623 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WAT623 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 623 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ SPEC EXPR1 = "SOL623/(SOL623+WAT623)" EXPR2 = "0.3" \ \ "TOL-SPEC" TOL = "0.001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = S614 VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 623 \ \ LIMITS LOWER = "0.0" UPPER = "1.0" \ \ COMMENTS COMMENTS = ( ";;" "; The spec of 0.30 is just a guess -- MR 24 Apr 97" ) \ ? "DESIGN-SPEC" "CT-T610" ? ; "SET1_MOLE" ; \ DEFINE FVN = SOL625 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 625 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WAT625 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 625 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ SPEC EXPR1 = "SOL625/(SOL625+WAT625)" EXPR2 = "0.05" \ \ "TOL-SPEC" TOL = "0.001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = T610 VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 625 \ \ LIMITS LOWER = "0.0" UPPER = "1.0" \ \ COMMENTS COMMENTS = ( ";;" ";---------------------------------------------------------------" "; DESIGN SPECS" "; DIGESTER (AREA 6000)" ";---------------------------------------------------------------" ";;" "; The spec of 0.05 is just a guess -- MR 24 Apr 97" ) \ ? "DESIGN-SPEC" CWFLOWA ? ; "SET1_MOLE" ; \ DEFINE FVN = QTOT FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QTTOTXS \ \ SPEC EXPR1 = "QTOT" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "100" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 945 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "300000" UPPER = "30000000" \ \ COMMENTS COMMENTS = ( ";;" ";CONTROLS THE COOLING WATER FLOW TO MEET THE DEMAND OF THE" ";PLANT." ) \ ? "DESIGN-SPEC" CWFLOWB ? ; "SET1_MOLE" ; \ DEFINE FVN = QTOT FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QTTOTXB \ \ SPEC EXPR1 = "QTOT" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "100" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 946 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "300000" UPPER = "30000000" \ \ COMMENTS COMMENTS = ( ";;" ";CONTROLS THE COOLING WATER FLOW TO MEET THE DEMAND OF THE" ";PLANT (OPERATING COST CALC)." ) \ ? "DESIGN-SPEC" CWFLOWC ? ; "SET1_MOLE" ; \ DEFINE FVN = QTOT FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QCWFLXS \ \ SPEC EXPR1 = "QTOT" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "100" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 948 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "10000" UPPER = "30000000" \ \ COMMENTS COMMENTS = ( ";;" ";CONTROLS THE COOLING WATER FLOW TO MEET THE DEMAND OF THE" ";PLANT (EVAPORATION CALC)." ) \ ? "DESIGN-SPEC" D502BTMS ? ; "SET1_MOLE" ; \ DEFINE FVN = BTMETH FVN-VARTYPE = "MASS-FRAC" FVN-STREAM = 516 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ SPEC EXPR1 = "BTMETH" EXPR2 = ".0005" \ \ "TOL-SPEC" TOL = ".00001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = D502 VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 516 VARYID3 = ETHANOL \ \ LIMITS LOWER = ".0001" UPPER = ".1" \ \ COMMENTS COMMENTS = ( ";;" "; Adjust mole-frac specification in D502 SEP2 to meet a specified" "; MASS-FRAC" ) \ ? "DESIGN-SPEC" D502OVHD ? ; "SET1_MOLE" ; \ DEFINE FVN = OVETOH FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 511 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = OVH2O FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 511 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ SPEC EXPR1 = "OVETOH/(OVETOH+OVH2O)" EXPR2 = ".926028472" \ \ "TOL-SPEC" TOL = ".0001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = D502 VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 511 VARYID3 = ETHANOL \ \ LIMITS LOWER = ".75" UPPER = ".999" \ \ COMMENTS COMMENTS = ( "; Adjust mole-frac specification in D502 SEP2 to meet a specified" "; MASS-FRAC" ) \ ? "DESIGN-SPEC" DEAERHT ? ; "SET1_MOLE" ; \ DEFINE FVN = QDEAER FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QDEAER \ \ SPEC EXPR1 = "QDEAER" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "100" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = M811ISPT VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = 815A \ \ LIMITS LOWER = "10000" UPPER = "90000" \ \ COMMENTS COMMENTS = ( ";;" ";---------------------------------------------------------------------" "; STEAM CYCLE DESIGN-SPECS" ";--------------------------------------------------------------------" ";;" ";CONTROLS THE AMOUNT OF MED PRESSURE STEAM" ";TO THE DEAERATOR." ) \ ? "DESIGN-SPEC" ECONSTM ? ; "SET1_MOLE" ; \ DEFINE FVN = QECON FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH811EX \ \ SPEC EXPR1 = "QECON" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "100" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = M811HSPT VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = 812B \ \ LIMITS LOWER = ".0005" UPPER = "0.5" \ \ COMMENTS COMMENTS = ( ";;" ";CONTROLS THE AMOUNT OF HIGH PRESSURE STEAM TO THE" ";ECONOMIZER." ) \ ? "DESIGN-SPEC" EV1SIZ ? ; "SET1_MOLE" ; \ DEFINE FVN = Q0 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QC502A \ \ DEFINE FVN = Q0B FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QE501A \ \ DEFINE FVN = Q1 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QE502A \ \ DEFINE FVN = Q2 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QE503A \ \ DEFINE FVN = T0 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 511 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 526 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 529 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T3 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 532 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ FORTRAN FORTRAN-EXEC = ( "F U1 = 135.0" "F U2 = 170.0" "F QF1=(Q0+Q0B)/((T0-T1)*U1)" "F QF2=Q1/((T1-T2)*0.5*U2)" "F QF3=Q2/((T2-T3)*U2)" "F QSET=(QF1+QF2+QF3)/3" "F WRITE(NHSTRY,'(""EV1SIZ"")')" "F WRITE(NHSTRY,'('' QF1 = '',G12.5)')QF1" "F WRITE(NHSTRY,'('' QF2 = '',G12.5)')QF2" "F WRITE(NHSTRY,'('' QF3 = '',G12.5)')QF3" "F WRITE(NHSTRY,'('' QSET = '',G12.5)')QSET" ) \ \ SPEC EXPR1 = "QF2" EXPR2 = "QSET" \ \ "TOL-SPEC" TOL = "1" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = E501L VARYVARIABLE = PRES VARYSENTENCE = PARAM \ \ LIMITS LOWER = "0.5" UPPER = "0.65" \ \ COMMENTS COMMENTS = ( ";;" ";DESIGN-SPEC TRIM" ";;THIS SPEC DETERMINES THE AMOUNT OF 50 PSIG STEAM" ";;REQUIRED TO TRIM THE RECTIFICATION COLUMN." ";;" "; DEFINE QTRMO INFO-VAR INFO=HEAT VARIABLE=DUTY STREAM=QH504EX" "; SPEC QTRMO TO 0" "; TOL-SPEC 10" "; VARY STREAM-VAR STREAM=592 SUBSTREAM=MIXED VARIABLE=MASS-FLOW" "; LIMITS 1 100000" ";;" ";DESIGN-SPEC REBOIL" ";;THIS SPEC DETERMINES THE AMOUNT OF 150 PSIG STEAM" ";;REQ'D FOR THE BEER COLUMN REBOILER." ";;" "; DEFINE QREBO INFO-VAR INFO=HEAT VARIABLE=DUTY STREAM=QRD501EX" "; SPEC QREBO TO 0" "; TOL-SPEC 10" "; VARY STREAM-VAR STREAM=594 SUBSTREAM=MIXED VARIABLE=MASS-FLOW" "; LIMITS 10000 200000" ";;" ";DESIGN-SPEC SUPRHET" ";;THIS SPEC DETERMINES THE AMOUNT OF 50 PSIG STEAM" ";;REQ'D TO SUPERHEAT THE ETHANOL INTO THE MOLECULAR SIEVE" ";;" "; DEFINE QSUPE INFO-VAR INFO=HEAT VARIABLE=DUTY STREAM=QH506EX" "; SPEC QSUPE TO 0" "; TOL-SPEC 10" "; VARY STREAM-VAR STREAM=596 SUBSTREAM=MIXED VARIABLE=MASS-FLOW" "; LIMITS 10 20000" ";;" ";CALCULATES THE PRESSURE FOR E501L TO MAKE THE HEAT-TRANSFER" ";TO ALL EFFECTS THE SAME" "; The heat transfer coefficient for the 1st stage is 135 Btu / ft^2 F" "; The heat transfer coefficient for the 2nd and 3rd stages is 170" "; There are 2 1st & 3rd stages and 1 2nd stage" "; Changes to the stages and heat transfer coefficients need to be made to" "; EV2SIZ as well. MR 21 May 98" ) \ ? "DESIGN-SPEC" EV2SIZ ? ; "SET1_MOLE" ; \ DEFINE FVN = Q0 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QC502A \ \ DEFINE FVN = Q0B FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QE501A \ \ DEFINE FVN = Q1 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QE502A \ \ DEFINE FVN = Q2 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QE503A \ \ DEFINE FVN = T0 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 511 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 526 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 529 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T3 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 532 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ FORTRAN FORTRAN-EXEC = ( "F U1 = 135.0" "F U2 = 170.0" "F QF1=(Q0+Q0B)/((T0-T1)*U1)" "F QF2=Q1/((T1-T2)*0.5*U2)" "F QF3=Q2/((T2-T3)*U2)" "F QSET=(QF1+QF2+QF3)/3" "F WRITE(NHSTRY,'(""EV2SIZ"")')" "F WRITE(NHSTRY,'('' QF1 = '',G12.5)')QF1" "F WRITE(NHSTRY,'('' QF2 = '',G12.5)')QF2" "F WRITE(NHSTRY,'('' QF3 = '',G12.5)')QF3" "F WRITE(NHSTRY,'('' QSET = '',G12.5)')QSET" ) \ \ SPEC EXPR1 = "QF3" EXPR2 = "QSET" \ \ "TOL-SPEC" TOL = "1" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = E502L VARYVARIABLE = PRES VARYSENTENCE = PARAM \ \ LIMITS LOWER = "0.25" UPPER = "0.35" \ \ COMMENTS COMMENTS = ( ";;" ";CALCULATES THE PRESSURE FOR E502L TO MAKE THE HEAT-TRANSFER" ";TO ALL EFFECTS THE SAME" "; The heat transfer coefficient for the 1st stage is 135 Btu / ft^2 F" "; The heat transfer coefficient for the 2nd and 3rd stages is 170" "; There are 2 1st & 3rd stages and 1 2nd stage" "; Changes to the stages and heat transfer coefficients need to be made to" "; EV1SIZ as well. MR 21 May 98" ) \ ? "DESIGN-SPEC" EVAPCONC ? ; "SET6_MOLE" ; \ DEFINE FVN = SOL531 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLW531 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WAT531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ SPEC EXPR1 = "WAT531/(SOL531+FLW531)" EXPR2 = "0.6" \ \ "TOL-SPEC" TOL = "0.001" \ \ VARY VARY-VARTYPE = "HEAT-DUTY" VARYSTREAM = QE501A \ \ LIMITS LOWER = "0.0" UPPER = "50.0" \ \ COMMENTS COMMENTS = ( ";;" "; SETS FLOW OF QE501A to set moisture concentration in 531" ) \ ? "DESIGN-SPEC" H201TEMP ? ; "SET1_MOLE" ; \ DEFINE FVN = T501 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 501 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ SPEC EXPR1 = "T501" EXPR2 = "95.0" \ \ "TOL-SPEC" TOL = "0.01" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = QH201SPT VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = QH201 \ \ LIMITS LOWER = "0.5" UPPER = "1.0" \ \ COMMENTS COMMENTS = ( ";;" ";CONTROLS THE TEMPERATURE OF 501 (LEAVING H201-)" ";If this spec is in error due to hitting the upper bound, not enough heat" ";is available in 218 to make the desired temp increase in 502. The error" ";is not a problem because 502 will just be warmed as much as possible with" ";the heat available." ) \ ? "DESIGN-SPEC" LPSTMFLO ? ; "SET1_MOLE" ; \ DEFINE FVN = THTR FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QM202LO \ \ SPEC EXPR1 = "THTR" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "10.0" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 215 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "100" UPPER = "500000" \ \ COMMENTS COMMENTS = ( ";;" ";CONTROLS THE AMOUNT OF LP STEAM TO PRETREATMENT TO" ";ACHIEVE 100 C." ) \ ? "DESIGN-SPEC" "MS-BTM" ? ; "SET1_MOLE" ; \ DEFINE FVN = WT514 FVN-VARTYPE = "MASS-FRAC" FVN-STREAM = 514 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ SPEC EXPR1 = "WT514" EXPR2 = "0.005" \ \ "TOL-SPEC" TOL = "0.0001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = "T507-8" VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 514 VARYID3 = H2O \ \ LIMITS LOWER = "0.001" UPPER = "0.3" \ \ COMMENTS COMMENTS = ( ";;" "; Specification of 0.005 mass fraction H2O in product ethanol" ) \ ? "DESIGN-SPEC" "MS-OVHD" ? ; "SET1_MOLE" ; \ DEFINE FVN = ET515A FVN-VARTYPE = "MASS-FRAC" FVN-STREAM = 515A FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ SPEC EXPR1 = "ET515A" EXPR2 = "0.722" \ \ "TOL-SPEC" TOL = "0.001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = "T507-8" VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 515A VARYID3 = ETHANOL \ \ LIMITS LOWER = "0.05" UPPER = "0.5" \ \ COMMENTS COMMENTS = ( ";;" "; Specification of 0.7 mass frac ethanol in recycle to Rectification" ) \ ? "DESIGN-SPEC" REACHEAT ? ; "SET1_MOLE" ; \ DEFINE FVN = QRXNXS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QM202HI \ \ SPEC EXPR1 = "QRXNXS" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "5" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 216 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "200" UPPER = "100000" \ \ COMMENTS COMMENTS = ( ";;" ";CALCULATES THE AMOUNT OF HP STEAM REQUIRED TO OBTAIN" ";THE CORRECT RXN TEMPERATURE IN PRETREATMENT." ) \ ? "DESIGN-SPEC" SCRBFLOW ? ; "SET1_MOLE" ; \ DEFINE FVN = FRCETO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 550 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ SPEC EXPR1 = "FRCETO" EXPR2 = "4.316" \ \ "TOL-SPEC" TOL = "0.0001" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 524 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "5000" UPPER = "40000" \ \ COMMENTS COMMENTS = ( ";;" ";---------------------------------------------------------------" "; SACCHARIFICATION AND FERMENTATION DESIGN-SPECS" ";---------------------------------------------------------------" ";;" ";DESIGN-SPEC SACCHHEAT" ";;THIS SPEC DETERMINES THE AMOUNT OF 50 PSIG STEAM" ";;REQ'D TO HEAT THE HYDROLZYATE SLURRY TO 65C FOR SACCHARIFICATION" ";;" "; DEFINE QSACCH INFO-VAR INFO=HEAT VARIABLE=DUTY STREAM=QH301EX" "; SPEC QSACCH TO 0" "; TOL-SPEC 10" "; VARY STREAM-VAR STREAM=590 SUBSTREAM=MIXED VARIABLE=MASS-FLOW" "; LIMITS 10 20000" ";;" ";---------------------------------------------------------------" "; DISTILLAION DESIGN-SPECS" ";---------------------------------------------------------------" ";;" "; 40 ton/yr ethanol loss = 4.316kg/hr (8406 hr/yr)" "; changed from 8400 hr/yr to 8406 by AA, 2/20/01" ) \ ? "DESIGN-SPEC" SETSTEAM ? ; "SET1_MOLE" ; \ DEFINE FVN = QSUPXS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QM803EX \ \ SPEC EXPR1 = "QSUPXS" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "100" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 824 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "1.0E4" UPPER = "3.5E5" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? "DESIGN-SPEC" STDDMD ? ; "SET1_MOLE" ; \ DEFINE FVN = QXCS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QTSTMXS \ \ SPEC EXPR1 = "QXCS" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "10" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 890 VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "1000" UPPER = "100000" \ \ COMMENTS COMMENTS = ( ";;" ";This spec determines the amount of LP steam req'd by the process" ";;" ) \ ? "DESIGN-SPEC" VLPSTM ? ; "SET1_MOLE" ; \ DEFINE FVN = QEVAP1 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QE501A \ \ DEFINE FVN = QEVAP2 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QE501A2 \ \ SPEC EXPR1 = "QEVAP2" EXPR2 = "QEVAP1" \ \ "TOL-SPEC" TOL = "0.1" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = M811LSPT VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = 860 \ \ LIMITS LOWER = "0" UPPER = "500000" \ \ COMMENTS COMMENTS = ( ";;" ";CONTROLS THE AMOUNT OF VERY LOW PRESSURE STEAM" ";TO THE EVAPORATOR." ) \ ? "EO-CONV-OPTI" ? \ DMO-PARAMS MODE = DEFAULT \ \ DMO-PARAMS MODE = SIMULATION \ \ DMO-PARAMS MODE = "PARAMETER-ESTIMATION" \ \ DMO-PARAMS MODE = RECONCILIATION \ \ DMO-PARAMS MODE = OPTIMIZATION \ \ LSSQP-PARAMS MODE-L = DEFAULT \ \ LSSQP-PARAMS MODE-L = SIMULATION \ \ LSSQP-PARAMS MODE-L = "PARAMETER-ESTIMATION" \ \ LSSQP-PARAMS MODE-L = RECONCILIATION \ \ LSSQP-PARAMS MODE-L = OPTIMIZATION \ \ NSOLVE-PARAM NSOLVE-MODE = DEFAULT \ \ NSOLVE-PARAM NSOLVE-MODE = SIMULATION \ \ NSOLVE-PARAM NSOLVE-MODE = "PARAMETER-ESTIMATION" \ ? CALCULATOR AERAIR ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F COMMON/ WWLOD2/ COD2, BOD2, CODDY2, BODDY2, BODHP" ) \ \ DEFINE FVN = AIR FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 626 FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C THE AIR REQUIREMENT IS 50% ABOVE THEORETICAL (J. RUOCCO)" "C" "F XO2 = 2.5*COD2" "F AIR=XO2/0.21" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = T608 \ \ COMMENTS COMMENTS = ( ";------------------------------------------------------" "; DIGESTOR FORTRAN BLOCKS - AREA 6000" ";------------------------------------------------------" ";;" ) \ ? CALCULATOR AIRREQ ? ; "SET1_MOLE" ; \ DEFINE FVN = CLYLD FVN-VARTYPE = PARAMETER FVN-PARAMNO = 41 \ \ DEFINE FVN = CLPROD FVN-VARTYPE = PARAMETER FVN-PARAMNO = 42 \ \ DEFINE FVN = CLVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 43 \ \ DEFINE FVN = CLVOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 44 \ \ DEFINE FVN = CLWV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 45 \ \ DEFINE FVN = STDEN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 413 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = ARFDEN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 432 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = SDIN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 431 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SDDEN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 431 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = CL412A FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 412A FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XY412A FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 412A FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = AIRIN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 440 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = F1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = ASPLT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 413 \ \ FORTRAN FORTRAN-EXEC = ( "C WORKING VOLUME (WV1)=90%" "C AIR REQUIRED IN PRODUCTION FERMENTORS (AIR1) = 0.577 VVM" "C 0.577 VVM = OTR OF 75 MMOL/L HR & 20% DO" "F AIR1=0.577" "C V1 IS THE VOLUME (IN LITERS) OF THE PRODUCTION FERMS" "C IT IS CALCULATED FROM THE FLOW RATES, YIELD, AND PRODUCTIVITY" "C 2*CLVOL IS ADDED FOR THE 2 FERMS NOT IN USE." "F V1=((CL412A+XY412A)*1000*CLYLD/CLPROD)/CLWV" "F DV1=STDEN*(V1*60*AIR1)" "C CLVES IS THE NUMBER OF PRODUCTION VESSELS AND IS CALCULATED HERE" "F CLVES=V1/CLVOL + 3." "C" "C RESIDENCE TIME IN SEED FERMENTORS=3.5 DAYS" "C TOTAL TURNAROUND TIME (T2)=4.0 DAYS" "F T2=72.0" "C VOLUME (WV2)=90%" "F WV2=0.8" "C AIR REQUIRED IN SEED FERMENTORS = 0.577 VVM" "C 0.577 VVM = OTR OF 75 MMOL/L HR & 20% DO FOR PRODUCTION FERMS" "C MAY BE SLIGHTLY HIGHER FOR SEEDS" "F AIR2=0.577" "C NUMBER OF SEED TRAINS (SEED) = 2" "F SEED=2" "C VOLUMETRIC FLOWRATE OF SUBSTRATE INTO THE SEED FERMENTORS IS VFL2" "F VFL2=SDIN/SDDEN" "F DV2=ARFDEN*(VFL2*T2*60*AIR2*SEED)/WV2" "C" "F F1=DV1/(DV1+DV2)" "C CALCULATE TOTAL AIR IN""D:\GJK\ENZ998\G9809G.HIS""" "F AIRIN=DV1 + DV2" "C" "F WRITE(NHSTRY,80)STDEN,V1,DV1,DV2,ARFDEN,SDIN," "F 1 SDDEN,AIRIN,F1,CLVES" "F 80 FORMAT('AIRREQ RESULTS',/," "F 2 'STDEN ',G12.5,/," "F 3 'V1 ',G12.5,/," "F 4 'DV1 ',G12.5,/," "F 5 'DV2 ',G12.5,/," "F 6 'ARFDEN ',G12.5,/," "F 7 'SDIN ',G12.5,/," "F 8 'SDDEN ',G12.5,/," "F 9 'AIRIN ',G12.5,/," "F 1 'F1 ',G12.5,/," "F 2 'CLVES ',G12.5)" ) \ \ "READ-VARS" READ-VAR = ( STDEN ARFDEN SDIN SDDEN CL412A XY412A CLYLD CLPROD CLVOL CLWV ) \ \ "WRITE-VARS" WRITE-VAR = ( AIRIN F1 CLVES ) \ \ COMMENTS COMMENTS = ( ";;" ";F COMMON /CLSSET/ CLYLD, CLPROD, CLVES, CLVOL, CLWV" ";;" ";CONTROLS THE AMOUNT OF AIR NEEDED IN CELLULASE" ";PRODUCTION AND SEED FERMENTORS" ";;" "; CLYLD IS THE CELLULASE YIELD (FPU/G CELLULOSE + G XYLOSE)" "; AND IS ENTERED IN SETVAR" "; CLPROD IS THE CELLULASE PRODUCTION PRODUCTIVITY (FPU/L HR)" "; AND IS ENTERED IN SETVAR" "; IS ENTERED IN SETVAR (CLWV)" ) \ ? CALCULATOR CFUGESLD ? ; "SET1_MOLE" ; \ DEFINE FVN = F1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = H2O \ \ DEFINE FVN = F2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = ETHANOL \ \ DEFINE FVN = F3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = FURFURAL \ \ DEFINE FVN = F4 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = HMF \ \ DEFINE FVN = F5 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = H2SO4 \ \ DEFINE FVN = F6 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = N2 \ \ DEFINE FVN = F7 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CO2 \ \ DEFINE FVN = F8 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = O2 \ \ DEFINE FVN = F9 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CH4 \ \ DEFINE FVN = F10 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = NO \ \ DEFINE FVN = F11 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = NO2 \ \ DEFINE FVN = F12 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = NH3 \ \ DEFINE FVN = F13 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = SOLSLDS \ \ DEFINE FVN = F14 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = GLUCOSE \ \ DEFINE FVN = F15 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = XYLOSE \ \ DEFINE FVN = F16 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = GALACTOS \ \ DEFINE FVN = F17 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = MANNOSE \ \ DEFINE FVN = F18 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = ARABINOS \ \ DEFINE FVN = F19 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = UNKNOWN \ \ DEFINE FVN = F20 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = AACID \ \ DEFINE FVN = F21 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = LACID \ \ DEFINE FVN = F22 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CNUTR \ \ DEFINE FVN = F23 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = WNUTR \ \ DEFINE FVN = F24 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CSL \ \ DEFINE FVN = F25 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = OIL \ \ DEFINE FVN = F26 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = DENAT \ \ DEFINE FVN = F27 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = GLUCOLIG \ \ DEFINE FVN = F28 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CELLOB \ \ DEFINE FVN = F29 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = XYLOLIG \ \ DEFINE FVN = F30 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = MANOLIG \ \ DEFINE FVN = F31 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = GALAOLIG \ \ DEFINE FVN = F32 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = ARABOLIG \ \ DEFINE FVN = F33 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = ACETOLIG \ \ DEFINE FVN = F34 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = GLYCEROL \ \ DEFINE FVN = F35 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = SUCCACID \ \ DEFINE FVN = F36 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = XYLITOL \ \ DEFINE FVN = F37 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = LGNSOL \ \ DEFINE FVN = F38 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = EXTRACT \ \ DEFINE FVN = F39 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = PROTEIN \ \ DEFINE FVN = F40 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CASO4 \ \ DEFINE FVN = F41 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = DAP \ \ DEFINE FVN = F42 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CELLULOS \ \ DEFINE FVN = F43 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = XYLAN \ \ DEFINE FVN = F44 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = ARABINAN \ \ DEFINE FVN = F45 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = MANNAN \ \ DEFINE FVN = F46 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = GALACTAN \ \ DEFINE FVN = F47 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = LIGNIN \ \ DEFINE FVN = F48 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = BIOMASS \ \ DEFINE FVN = F49 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CELLULAS \ \ DEFINE FVN = F50 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = ZYMO \ \ DEFINE FVN = F51 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CAH2O2 \ \ DEFINE FVN = F52 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = GYPSUM \ \ DEFINE FVN = F53 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = TAR \ \ DEFINE FVN = F54 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = ACETATE \ \ DEFINE FVN = F55 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = ASH \ \ DEFINE FVN = F56 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = NH4OH \ \ DEFINE FVN = F57 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = NH4SO4 \ \ DEFINE FVN = F58 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = NH4ACET \ \ DEFINE FVN = F59 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = PROPANE \ \ DEFINE FVN = F60 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = SO2 \ \ DEFINE FVN = F61 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = H2S \ \ DEFINE FVN = F62 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = C \ \ DEFINE FVN = F63 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S505 FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CO \ \ FORTRAN FORTRAN-EXEC = ( "F IF (F2 .LT.0.5) F2 = F1" "F IF (F3 .LT.0.5) F3 = F1" "F IF (F4 .LT.0.5) F4 = F1" "F IF (F5 .LT.0.5) F5 = F1" "F IF (F6 .LT.0.5) F6 = F1" "F IF (F7 .LT.0.5) F7 = F1" "F IF (F8 .LT.0.5) F8 = F1" "F IF (F9 .LT.0.5) F9 = F1" "F IF (F10.LT.0.5) F10 = F1" "F IF (F11.LT.0.5) F11 = F1" "F IF (F12.LT.0.5) F12 = F1" "F IF (F13.LT.0.5) F13 = F1" "F IF (F14.LT.0.5) F14 = F1" "F IF (F15.LT.0.5) F15 = F1" "F IF (F16.LT.0.5) F16 = F1" "F IF (F17.LT.0.5) F17 = F1" "F IF (F18.LT.0.5) F18 = F1" "F IF (F19.LT.0.5) F19 = F1" "F IF (F20.LT.0.5) F20 = F1" "F IF (F21.LT.0.5) F21 = F1" "F IF (F22.LT.0.5) F22 = F1" "F IF (F23.LT.0.5) F23 = F1" "F IF (F24.LT.0.5) F24 = F1" "F IF (F25.LT.0.5) F25 = F1" "F IF (F26.LT.0.5) F26 = F1" "F IF (F27.LT.0.5) F27 = F1" "F IF (F28.LT.0.5) F28 = F1" "F IF (F29.LT.0.5) F29 = F1" "F IF (F30.LT.0.5) F30 = F1" "F IF (F31.LT.0.5) F31 = F1" "F IF (F32.LT.0.5) F32 = F1" "F IF (F33.LT.0.5) F33 = F1" "F IF (F34.LT.0.5) F34 = F1" "F IF (F35.LT.0.5) F35 = F1" "F IF (F36.LT.0.5) F36 = F1" "F IF (F37.LT.0.5) F37 = F1" "F IF (F38.LT.0.5) F38 = F1" "F IF (F39.LT.0.5) F39 = F1" "F IF (F40.LT.0.5) F40 = F1" "F IF (F41.LT.0.5) F41 = F1" "F IF (F42.LT.0.5) F42 = F1" "F IF (F43.LT.0.5) F43 = F1" "F IF (F44.LT.0.5) F44 = F1" "F IF (F45.LT.0.5) F45 = F1" "F IF (F46.LT.0.5) F46 = F1" "F IF (F47.LT.0.5) F47 = F1" "F IF (F48.LT.0.5) F48 = F1" "F IF (F49.LT.0.5) F49 = F1" "F IF (F50.LT.0.5) F50 = F1" "F IF (F51.LT.0.5) F51 = F1" "F IF (F52.LT.0.5) F52 = F1" "F IF (F53.LT.0.5) F53 = F1" "F IF (F54.LT.0.5) F54 = F1" "F IF (F55.LT.0.5) F55 = F1" "F IF (F56.LT.0.5) F56 = F1" "F IF (F57.LT.0.5) F57 = F1" "F IF (F58.LT.0.5) F58 = F1" "F IF (F59.LT.0.5) F59 = F1" "F IF (F60.LT.0.5) F60 = F1" "F IF (F61.LT.0.5) F61 = F1" "F IF (F62.LT.0.5) F62 = F1" "F IF (F63.LT.0.5) F63 = F1" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = S505 \ \ COMMENTS COMMENTS = ( ";;" "; This FORTRAN Block works with the design-spec CFUGE3S to make" "; vary the splits of all of the following components the same" "; as water (F1). Water split is being varied by CFUGE3S. CSL Split" "; is not controlled by this block." ";;" ) \ ? CALCULATOR CHEMICAL ? ; "SET1_MOLE" ; \ DEFINE FVN = BFLOW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 811 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLXTRA FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 251 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = BFC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 921 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CWF FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 947 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CWC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 922 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "F BFCREQ=7.E-6" "C BFCREQ IS THE BFW CHEMICAL REQ IN LB/LB BFW" "C" "F CWCREQ=2.E-7" "C CWCREQ IS THE COOLING TOWER CHEMICAL REQ" "C IN LB/LB COOLING WATER FLOW" "C" "C CHECK TO SEE IF THERE IS MORE CLEAN RECYCLE WATER THAN 811 MAKEUP:" "F IF (BFLOW.GT.FLXTRA) THEN" "F BFC=BFCREQ*(BFLOW - FLXTRA)" "F ELSE" "F BFC=1.0" "F END IF" "F CWC=CWCREQ*CWF" "C" ) \ \ "READ-VARS" READ-VAR = ( BFLOW CWF FLXTRA ) \ \ "WRITE-VARS" WRITE-VAR = ( BFC CWC ) \ \ COMMENTS COMMENTS = ( "; EXECUTE AFTER T507-8" ";;" ";;" ";CALCULATE BFW & COOLING TOWER CHEMICALS." ";VALUES ARE SCALED FROM THE SPREADSHEET VALUES." ";;" ";ASSUME BFW CHEMICALS ARE NEEDED FOR THE WATER FED TO IX" ";DEFINE RATIOS OF CHEMICALS" ";;" "; Requirement from Radian Report. Back-calculated from cases." ) \ ? CALCULATOR CODCALC1 ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "C CALCULATES THE INCOMMING COD" "F COMMON/ WWLOAD/ CODTOT, BODTOT, CODDAY, BODDAY" ) \ \ DEFINE FVN = CEXTR FVN-VARTYPE = PARAMETER FVN-PARAMNO = 13 \ \ DEFINE FVN = CPRO FVN-VARTYPE = PARAMETER FVN-PARAMNO = 14 \ \ DEFINE FVN = CSOLS FVN-VARTYPE = PARAMETER FVN-PARAMNO = 15 \ \ DEFINE FVN = GLUC FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = UNKN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = SOLS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = ARAB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = GALA FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = XMANS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GLUO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CELB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XYLG FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = XMANO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GALO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = ACEO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = XYLL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = ETOH FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FURF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XHMF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = CH4 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = XLACI FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = AACI FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = GLYC FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUCC FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = DENA FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = XOIL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = XNNH4 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = SLLGN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXTCT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PROTN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = TOTANA FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 632 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = ANROHP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT606 \ \ FORTRAN FORTRAN-EXEC = ( "C" "C SET THE COD FOR COMPONENTS (KG O2/KG COMPONENT)" "C THE COD VALUES ARE THE THEORETICAL O2 REQUIRED FOR COMBUSTION, BUT" "C ONLY FOR SOLUBLE COMPONENTS. INSOLUBLE COMPONENTS ARE ASSUMED TO" "C BE NON-REACTIVE AND ARE NOT CONTAINED IN THE CALCULATION." "C EXTRACTIVE, SOLSOLIDS AND PROTEIN VALUES ARE READ IN BY PARAMETERS" "C 13, 14, 15." "C" "C SOLUBLE C-CONTAINING COMPOUNDS" "F CGLUC = 1.07" "F CXYLO = 1.07" "F CUNKN = 1.07" "F CETOH = 2.09" "F CARAB = 1.07" "F CGALA = 1.07" "F CMANS = 1.07" "F CGLUO = 1.07" "F CCELB = 1.07" "F CXYLG = 1.07" "F CMANO = 1.07" "F CGALO = 1.07" "F CARAO = 1.07" "F CXYLL = 1.22" "F CFURF = 1.67" "F CHMF = 1.52" "F CCH4 = 4.0" "F CLACI = 1.07" "F CAACI = 1.07" "F CGLYC = 1.22" "F CSUCC = 0.95" "F CDENA = 3.52" "F COIL = 2.89" "F CACEO = 1.07" "F CNNH4 = 1.557" "F CSLGN = 1.6000" "C" "C" "C CALCULATE HOURLY COD LOADINGS (KG/HR)" "C" "F CODTOT = GLUC*CGLUC + XYLO*CXYLO + UNKN*CUNKN + SOLS*CSOLS +" "F 1 GALA*CGALA + XMANS*CMANS + ARAB*CARAB + GLUO*CGLUO +" "F 2 CELB*CCELB + XYLG*CXYLG + XMANO*CMANO + GALO*CGALO +" "F 3 ARAO*CARAO + XYLL*CXYLL + ETOH*CETOH + FURF*CFURF +" "F 4 XHMF*CHMF + CH4*CCH4 + XLACI*CLACI + AACI*CAACI +" "F 5 GLYC*CGLYC + SUCC*CSUCC + DENA*CDENA + XOIL*COIL +" "F 6 ACEO*CACEO + CNNH4*XNNH4 + SLLGN*CSLGN + EXTCT*CEXTR +" "F 7 PROTN*CPRO" "C" "C" "C CALCULATE HOURLY BOD LOADINGS (KG/HR)" "C" "F BODCOD = 0.70" "C BODCOD IS THE BOD/COD RATIO AND WAS PROVIDED BY J. RUOCCO 7/29/98" "C THIS VALUE IS WITHIN THE RANGE (0.45-0.78) PROVIDED IN PERRY'S" "C 7TH EDITION, PG. 25-62." "C" "F BODTOT= BODCOD*CODTOT" "C" "C" "C CALCULATE DAILY BOD AND COD LOADINGS (LB/DAY)" "C" "F CODDAY = CODTOT*2.205*24." "F BODDAY = BODTOT*2.205*24." "C" "C 2.205 IS LB/KG AND 24 HR/DAY TO CONVERT KG/HR TO LB/DAY" "C" "C WRITE ANSWERS TO THE HISTORY FILE" "C" "F WRITE(NHSTRY,*)'CODTOT, BODTOT= ',CODTOT, BODTOT" "F WRITE(NHSTRY,*)'CODDAY, BODDAY= ',CODDAY, BODDAY" "C" "C" "C ANEROBIC SPACE VELOCITY RUCCO, G/L/D" "C" "F ANLOAD = 12.0" "F ANCONC = (CODTOT*1000.)/TOTANA" "F ANRT = (ANCONC*24.0)/ANLOAD" "C CALCULATE ANEROBIC VOLUME IN GALLONS" "F ANVOL1 = (TOTANA*ANRT)/3.7854" "C ASSUME HP 0.05 HP / 1000 GAL" "F ANRHP = 0.05 * ANVOL1 / 1000." "C CONVERT TO KW" "F ANROHP = ANRHP * 0.7457" "F WRITE(NHSTRY,*)'ANVOL1=',ANVOL1,' ANRHP=',ANRHP" "C" ) \ \ "READ-VARS" READ-VAR = ( GLUC TOTANA CEXTR CPRO CSOLS ) \ \ "WRITE-VARS" WRITE-VAR = ( ANROHP ) \ \ COMMENTS COMMENTS = ( "; EXECUTE BEFORE E501MIX" ";;" ";;" ";;" ) \ ? CALCULATOR CODCALC2 ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "C CALCULATES COD AFTER ANEROBIC AND BEFORE AEROBIC" "F COMMON/ WWLOD2/ COD2, BOD2, CODDY2, BODDY2, BODHP" ) \ \ DEFINE FVN = CEXTR FVN-VARTYPE = PARAMETER FVN-PARAMNO = 13 \ \ DEFINE FVN = CPRO FVN-VARTYPE = PARAMETER FVN-PARAMNO = 14 \ \ DEFINE FVN = CSOLS FVN-VARTYPE = PARAMETER FVN-PARAMNO = 15 \ \ DEFINE FVN = GLUC FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = UNKN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = SOLS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = ARAB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = GALA FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = XMANS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GLUO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CELB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XYLG FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = XMANO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GALO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = ACEO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = XYLL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = ETOH FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FURF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XHMF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = CH4 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = XLACI FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = AACI FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = GLYC FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUCC FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = DENA FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = XOIL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = XNNH4 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = SLLGN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXTCT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PROTN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = AEROHP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT608 \ \ FORTRAN FORTRAN-EXEC = ( "C" "C SET THE COD FOR COMPONENTS (KG O2/KG COMPONENT)" "C THE COD VALUES ARE THE THEORETICAL O2 REQUIRED FOR COMBUSTION, BUT" "C ONLY FOR SOLUBLE COMPONENTS. INSOLUBLE COMPONENTS ARE ASSUMED TO" "C BE NON-REACTIVE AND ARE NOT CONTAINED IN THE CALCULATION." "C EXTRACTIVE, SOLSOLIDS AND PROTEIN VALUES ARE READ IN BY PARAMETERS" "C 13, 14, 15." "C" "C SOLUBLE C-CONTAINING COMPOUNDS" "F CGLUC = 1.07" "F CXYLO = 1.07" "F CUNKN = 1.07" "F CETOH = 2.09" "F CARAB = 1.07" "F CGALA = 1.07" "F CMANS = 1.07" "F CGLUO = 1.07" "F CCELB = 1.07" "F CXYLG = 1.07" "F CMANO = 1.07" "F CGALO = 1.07" "F CARAO = 1.07" "F CXYLL = 1.22" "F CFURF = 1.67" "F CHMF = 1.52" "F CCH4 = 4.0" "F CLACI = 1.07" "F CAACI = 1.07" "F CGLYC = 1.22" "F CSUCC = 0.95" "F CDENA = 3.52" "F COIL = 2.89" "F CACEO = 1.07" "F CNNH4 = 1.557" "F CSLGN = 1.6000" "C" "C CALCULATE HOURLY COD LOADINGS (KG/HR)" "C" "F COD2 = GLUC*CGLUC + XYLO*CXYLO + UNKN*CUNKN + SOLS*CSOLS +" "F 1 GALA*CGALA + XMANS*CMANS + ARAB*CARAB + GLUO*CGLUO +" "F 2 CELB*CCELB + XYLG*CXYLG + XMANO*CMANO + GALO*CGALO +" "F 3 ARAO*CARAO + XYLL*CXYLL + ETOH*CETOH + FURF*CFURF +" "F 4 XHMF*CHMF + CH4*CCH4 + XLACI*CLACI + AACI*CAACI +" "F 5 GLYC*CGLYC + SUCC*CSUCC + DENA*CDENA + XOIL*COIL +" "F 6 ACEO*CACEO + CNNH4*XNNH4 + SLLGN*CSLGN + EXTCT*CEXTR +" "F 7 PROTN*CPRO" "C" "C" "C CALCULATE HOURLY BOD LOADINGS (KG/HR)" "C" "F BODCOD = 0.70" "C BODCOD IS THE BOD/COD RATIO AND WAS PROVIDED BY J. RUOCCO 7/29/98" "C THIS VALUE IS WITHIN THE RANGE (0.45-0.78) PROVIDED IN PERRY'S" "C 7TH EDITION, PG. 25-62." "C" "F BOD2 = BODCOD*COD2" "C" "C" "C CALCULATE DAILY BOD AND COD LOADINGS (LB/DAY)" "C" "F CODDY2 = COD2*2.205*24." "F BODDY2 = BOD2*2.205*24." "C" "C 2.205 IS LB/KG AND 24 HR/DAY TO CONVERT KG/HR TO LB/DAY" "C" "C WRITE ANSWERS TO THE HISTORY FILE" "C" "F WRITE(NHSTRY,*)'COD2, BOD2= ',COD2, BOD2" "F WRITE(NHSTRY,*)'CODDY2, BODDY2= ',CODDY2, BODDY2" "C" "C PER THE MEREICK QUOTE FROM GOBLE SAMPSON, CALCULATE THE HP" "C NECESSARY FOR AEROBIC AERATION (11/23/98)" "C" "C CALCULATE THE O2, LB PER DAY, 2 LB O2 PER LB BOD" "C" "F BOD2O2 = BODDY2 * 2." "C" "C CALCULATE HP PER GOBLE SAMPSON QUOTE" "C" "F BODHP = BOD2O2 / (0.616 * 64.8)" "C" "F AEROHP = BODHP * 0.7457" "F WRITE(NHSTRY,*)'AEROHP=',AEROHP,' BODHP=',BODHP" ) \ \ "READ-VARS" READ-VAR = ( GLUC CEXTR CPRO CSOLS ) \ \ "WRITE-VARS" WRITE-VAR = ( AEROHP ) \ ? CALCULATOR CODEND ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "C CALCULATES THE FINAL COD LEVEL IN THE WASTE WATER" "F COMMON/ WWLOD3/ COD3, BOD3, CODDY3, BODDY3" ) \ \ DEFINE FVN = CEXTR FVN-VARTYPE = PARAMETER FVN-PARAMNO = 13 \ \ DEFINE FVN = CPRO FVN-VARTYPE = PARAMETER FVN-PARAMNO = 14 \ \ DEFINE FVN = CSOLS FVN-VARTYPE = PARAMETER FVN-PARAMNO = 15 \ \ DEFINE FVN = GLUC FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = UNKN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = SOLS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = ARAB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = GALA FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = XMANS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GLUO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CELB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XYLG FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = XMANO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GALO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = ACEO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = XYLL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = ETOH FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FURF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XHMF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = CH4 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = XLACI FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = AACI FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = GLYC FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUCC FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = DENA FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = XOIL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = XNNH4 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = SLLGN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXTCT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PROTN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ FORTRAN FORTRAN-EXEC = ( "C" "C SET THE COD FOR COMPONENTS (KG O2/KG COMPONENT)" "C THE COD VALUES ARE THE THEORETICAL O2 REQUIRED FOR COMBUSTION, BUT" "C ONLY FOR SOLUBLE COMPONENTS. INSOLUBLE COMPONENTS ARE ASSUMED TO" "C BE NON-REACTIVE AND ARE NOT CONTAINED IN THE CALCULATION." "C EXTRACTIVE, SOLSOLIDS AND PROTEIN VALUES ARE READ IN BY PARAMETERS" "C 13, 14, 15." "C" "C SOLUBLE C-CONTAINING COMPOUNDS" "F CGLUC = 1.07" "F CXYLO = 1.07" "F CUNKN = 1.07" "F CETOH = 2.09" "F CARAB = 1.07" "F CGALA = 1.07" "F CMANS = 1.07" "F CGLUO = 1.07" "F CCELB = 1.07" "F CXYLG = 1.07" "F CMANO = 1.07" "F CGALO = 1.07" "F CARAO = 1.07" "F CXYLL = 1.22" "F CFURF = 1.67" "F CHMF = 1.52" "F CCH4 = 4.0" "F CLACI = 1.07" "F CAACI = 1.07" "F CGLYC = 1.22" "F CSUCC = 0.95" "F CDENA = 3.52" "F COIL = 2.89" "F CACEO = 1.07" "F CNNH4 = 1.557" "F CSLGN = 1.6000" "C" "C" "C CALCULATE HOURLY COD LOADINGS (KG/HR)" "C" "F COD3 = GLUC*CGLUC + XYLO*CXYLO + UNKN*CUNKN + SOLS*CSOLS +" "F 1 GALA*CGALA + XMANS*CMANS + ARAB*CARAB + GLUO*CGLUO +" "F 2 CELB*CCELB + XYLG*CXYLG + XMANO*CMANO + GALO*CGALO +" "F 3 ARAO*CARAO + XYLL*CXYLL + ETOH*CETOH + FURF*CFURF +" "F 4 XHMF*CHMF + CH4*CCH4 + XLACI*CLACI + AACI*CAACI +" "F 5 GLYC*CGLYC + SUCC*CSUCC + DENA*CDENA + XOIL*COIL +" "F 6 ACEO*CACEO + CNNH4*XNNH4 + SLLGN*CSLGN + EXTCT*CEXTR +" "F 7 PROTN*CPRO" "C" "C" "C CALCULATE HOURLY BOD LOADINGS (KG/HR)" "C" "F BODCOD = 0.70" "C BODCOD IS THE BOD/COD RATIO AND WAS PROVIDED BY J. RUOCCO 7/29/98" "C THIS VALUE IS WITHIN THE RANGE (0.45-0.78) PROVIDED IN PERRY'S" "C 7TH EDITION, PG. 25-62." "C" "F BOD3 = BODCOD*COD3" "C" "C" "C CALCULATE DAILY BOD AND COD LOADINGS (LB/DAY)" "C" "F CODDY3 = COD3*2.205*24." "F BODDY3 = BOD3*2.205*24." "C" "C 2.205 IS LB/KG AND 24 HR/DAY TO CONVERT KG/HR TO LB/DAY" "C" "C WRITE ANSWERS TO THE HISTORY FILE" "C" "F WRITE(NHSTRY,*)'COD3, BOD3= ',COD3, BOD3" "F WRITE(NHSTRY,*)'CODDY3, BODDY3= ',CODDY3, BODDY3" "C" ) \ \ "READ-VARS" READ-VAR = ( GLUC CEXTR CPRO CSOLS ) \ ? CALCULATOR COMBHEAT ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F COMMON / HEATIN / BTUTOT" ) \ \ DEFINE FVN = BTU101 FVN-VARTYPE = PARAMETER FVN-PARAMNO = 4 \ \ DEFINE FVN = CH4101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = SOL101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = CEL101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XYN101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = ARN101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = ARABINAN \ \ DEFINE FVN = XNN101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = GAN101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = XLG101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = LIGNIN \ \ DEFINE FVN = ACE101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = ACETATE \ \ DEFINE FVN = GLO101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CLB101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XNO101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GAO101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARO101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = XYO101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = TAR101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = TAR \ \ DEFINE FVN = ACO101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = FUR101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = XLL101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = GLU101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYL101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = XNS101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GAL101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = ARA101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = AA101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = XLA101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = CLS101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = CELLULAS \ \ DEFINE FVN = ETO101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = ZYM101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = ZYMO \ \ DEFINE FVN = GLY101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUC101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = BIO101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = BIOMASS \ \ DEFINE FVN = C101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = C \ \ DEFINE FVN = UNK101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = X2S101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = ACN101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = COI101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = DEN101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = XSL101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXT101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PRO101 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = CH4615 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = X2S615 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = FUR615 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF615 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = AA615 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = CH4840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = SOL840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = CEL840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XYN840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = ARN840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = ARABINAN \ \ DEFINE FVN = XNN840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = GAN840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = XLG840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = LIGNIN \ \ DEFINE FVN = ACE840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = ACETATE \ \ DEFINE FVN = GLO840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CLB840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XNO840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GAO840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARO840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = XYO840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = TAR840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = TAR \ \ DEFINE FVN = ACO840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = FUR840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = XLL840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = GLU840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYL840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = XNS840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GAL840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = ARA840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = AA840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = XLA840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = CLS840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = CELLULAS \ \ DEFINE FVN = ETO840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = ZYM840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = ZYMO \ \ DEFINE FVN = GLY840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUC840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = BIO840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = BIOMASS \ \ DEFINE FVN = C840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = C \ \ DEFINE FVN = UNK840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = X2S840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = ACN840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = COI840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = DEN840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = XSL840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXT840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PRO840 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = SOL803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = CEL803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XYN803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = ARN803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ARABINAN \ \ DEFINE FVN = XNN803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = GAN803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = XLG803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = LIGNIN \ \ DEFINE FVN = ACE803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ACETATE \ \ DEFINE FVN = GLO803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CLB803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XNO803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GAO803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARO803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = XYO803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = TAR803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = TAR \ \ DEFINE FVN = ACO803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = FUR803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = XLL803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = GLU803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYL803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = XNS803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GAL803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = ARA803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = AA803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = XLA803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = CLS803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = CELLULAS \ \ DEFINE FVN = ETO803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = ZYM803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ZYMO \ \ DEFINE FVN = GLY803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUC803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = BIO803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = BIOMASS \ \ DEFINE FVN = C803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = C \ \ DEFINE FVN = UNK803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = X2S803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = ACN803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = COI803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = DEN803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = XSL803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXT803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PRO803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = SOL531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = CEL531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XYN531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = ARN531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = ARABINAN \ \ DEFINE FVN = XNN531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = GAN531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = XLG531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = LIGNIN \ \ DEFINE FVN = ACE531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = ACETATE \ \ DEFINE FVN = GLO531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CLB531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XNO531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GAO531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARO531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = XYO531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = TAR531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = TAR \ \ DEFINE FVN = ACO531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = FUR531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = XLL531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = GLU531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYL531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = XNS531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GAL531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = ARA531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = AA531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = XLA531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = CLS531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = CELLULAS \ \ DEFINE FVN = ETO531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = ZYM531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = ZYMO \ \ DEFINE FVN = GLY531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUC531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = BIO531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = BIOMASS \ \ DEFINE FVN = C531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-COMPONEN = C \ \ DEFINE FVN = UNK531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = X2S531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = ACN531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = COI531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = DEN531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = XSL531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXT531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PRO531 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = HCSOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 7 \ \ DEFINE FVN = HCPRO FVN-VARTYPE = PARAMETER FVN-PARAMNO = 8 \ \ DEFINE FVN = HCEXT FVN-VARTYPE = PARAMETER FVN-PARAMNO = 9 \ \ FORTRAN FORTRAN-EXEC = ( "C SET THE HEAT OF COMBUSTION (HHVS) FOR EACH COMPONENT" "C THE HEAT OF COMBUSTIONS ARE IN BTU/KG" "C THE VARIABLES ARE HCXXX WITH THE 3 X'S CORRESPONDING" "C TO A 3 LETTER CODE FOR EACH COMPONENT USED IN THE DEFINE STATEMENTS" "C" "C SOLUBLE SOLIDS, PROTEIN, AND EXTRACTIVES FROM FEEDPROP" "F HCAAC = 14239.0" "F HCACE = 14237.4" "F HCACN = 7094.6" "F HCACO = 14239.0" "F HCARA = 14861.4" "F HCARN = 16844.0" "F HCARO = 16837.0" "F HCBIO = 21686.3" "F HCC = 81005.1" "F HCCEL = 16444.5" "F HCCH4 = 52603.4" "F HCCLB = 15650.6" "F HCCLS = 22613.1" "F HCCOI = 37552.8" "F HCDEN = 45552.0" "F HCETH = 28115.9" "F HCFUR = 23072.9" "F HCGAL = 14800.1" "F HCGAN = 16444.5" "F HCGAO = 16455.6" "F HCGLO = 16455.6" "F HCGLU = 14868.5" "F HCGLY = 17008.0" "F HCSLG = 24181.3" "F HCSUC = 12080.8" "F HCTAR = 16626.4" "F HCUNK = 13662.6" "F HCX2S = 15626.4" "F HCXLA = 14253.6" "F HCXLG = 24206.9" "F HCXLL = 15972.4" "F HCXMF = 21068.8" "F HCXNN = 16444.5" "F HCXNO = 16455.6" "F HCXNS = 14922.7" "F HCXYL = 14861.4" "F HCXYN = 16844.0" "F HCXYO = 16837.0" "F HCZYM = 20018.7" "C" "C CALCULATE THE BTU/HR OF STREAM 615, ANAEROBIC OFF-GAS" "C" "F BTU615 = CH4615*HCCH4 + X2S615*HCX2S + FUR615*HCFUR +" "F 1 XMF615*HCXMF + AA615*HCAAC" "F WRITE(NHSTRY,*)'HHV OF 615 (BTU/HR) -- BTU615= ',BTU615" "C" "C CALCULATE THE BTU/HR OF STREAM 101, BIOMASS FEED" "C" "F BTU101 = CH4101*HCCH4 +" "F 1 SOL101*HCSOL + CEL101*HCCEL + XYN101*HCXYN +" "F 2 ARN101*HCARN + XNN101*HCXNN + GAN101*HCGAN +" "F 3 XLG101*HCXLG + ACE101*HCACE +" "F 4 GLO101*HCGLO + CLB101*HCCLB + XNO101*HCXNO +" "F 5 GAO101*HCGAO + ARO101*HCARO + XYO101*HCXYO +" "F 6 TAR101*HCTAR + ACO101*HCACO + FUR101*HCFUR +" "F 7 XMF101*HCXMF + XLL101*HCXLL + GLU101*HCGLU +" "F 8 XYL101*HCXYL + XNS101*HCXNS + GAL101*HCGAL +" "F 9 ARA101*HCARA + AA101*HCAAC + XLA101*HCXLA +" "F * CLS101*HCCLS + ETO101*HCETH + ZYM101*HCZYM +" "F 1 GLY101*HCGLY + SUC101*HCSUC + BIO101*HCBIO +" "F 2 C101*HCC + UNK101*HCUNK + X2S101*HCX2S +" "F 3 ACN101*HCACN + COI101*HCCOI + DEN101*HCDEN +" "F 4 XSL101*HCSLG + EXT101*HCEXT + PRO101*HCPRO" "F WRITE(NHSTRY,*)'HHV OF 101 (BTU/HR) -- BTU101= ',BTU101" "C" "C CALCULATE THE BTU/HR OF STREAM 840, EITHER NATURAL GAS OR BIOMASS SUPPLEMENT" "C" "F BTU840 = CH4840*HCCH4 +" "F 1 SOL840*HCSOL + CEL840*HCCEL + XYN840*HCXYN +" "F 2 ARN840*HCARN + XNN840*HCXNN + GAN840*HCGAN +" "F 3 XLG840*HCXLG + ACE840*HCACE +" "F 4 GLO840*HCGLO + CLB840*HCCLB + XNO840*HCXNO +" "F 5 GAO840*HCGAO + ARO840*HCARO + XYO840*HCXYO +" "F 6 TAR840*HCTAR + ACO840*HCACO + FUR840*HCFUR +" "F 7 XMF840*HCXMF + XLL840*HCXLL + GLU840*HCGLU +" "F 8 XYL840*HCXYL + XNS840*HCXNS + GAL840*HCGAL +" "F 9 ARA840*HCARA + AA840*HCAAC + XLA840*HCXLA +" "F * CLS840*HCCLS + ETO840*HCETH + ZYM840*HCZYM +" "F 1 GLY840*HCGLY + SUC840*HCSUC + BIO840*HCBIO +" "F 2 C840*HCC + UNK840*HCUNK + X2S840*HCX2S +" "F 3 ACN840*HCACN + COI840*HCCOI + DEN840*HCDEN +" "F 4 XSL840*HCSLG + EXT840*HCEXT + PRO840*HCPRO" "F WRITE(NHSTRY,*)'HHV OF 840 (BTU/HR) -- BTU840= ',BTU840" "C" "C CALCULATE THE BTU/HR OF STREAM 803, SOLIDS" "C" "F BTU803 = SOL803*HCSOL + CEL803*HCCEL + XYN803*HCXYN +" "F 1 ARN803*HCARN + XNN803*HCXNN + GAN803*HCGAN +" "F 2 XLG803*HCXLG + ACE803*HCACE +" "F 3 GLO803*HCGLO + CLB803*HCCLB + XNO803*HCXNO +" "F 4 GAO803*HCGAO + ARO803*HCARO + XYO803*HCXYO +" "F 5 TAR803*HCTAR + ACO803*HCACO + FUR803*HCFUR +" "F 6 XMF803*HCXMF + XLL803*HCXLL + GLU803*HCGLU +" "F 7 XYL803*HCXYL + XNS803*HCXNS + GAL803*HCGAL +" "F 8 ARA803*HCARA + AA803*HCAAC + XLA803*HCXLA +" "F 9 CLS803*HCCLS + ETO803*HCETH + ZYM803*HCZYM +" "F * GLY803*HCGLY + SUC803*HCSUC + BIO803*HCBIO +" "F 1 C803*HCC + UNK803*HCUNK + X2S803*HCX2S +" "F 2 ACN803*HCACN + COI803*HCCOI + DEN803*HCDEN +" "F 3 XSL803*HCSLG + EXT803*HCEXT + PRO803*HCPRO" "F WRITE(NHSTRY,*)'HHV OF 803 (BTU/HR) -- BTU803= ',BTU803" "C" "C CALCULATE THE BTU/HR OF STREAM 531, SYRUP" "C" "F BTU531 = SOL531*HCSOL + CEL531*HCCEL + XYN531*HCXYN +" "F 1 ARN531*HCARN + XNN531*HCXNN + GAN531*HCGAN +" "F 2 XLG531*HCXLG + ACE531*HCACE +" "F 3 GLO531*HCGLO + CLB531*HCCLB + XNO531*HCXNO +" "F 4 GAO531*HCGAO + ARO531*HCARO + XYO531*HCXYO +" "F 5 TAR531*HCTAR + ACO531*HCACO + FUR531*HCFUR +" "F 6 XMF531*HCXMF + XLL531*HCXLL + GLU531*HCGLU +" "F 7 XYL531*HCXYL + XNS531*HCXNS + GAL531*HCGAL +" "F 8 ARA531*HCARA + AA531*HCAAC + XLA531*HCXLA +" "F 9 CLS531*HCCLS + ETO531*HCETH + ZYM531*HCZYM +" "F * GLY531*HCGLY + SUC531*HCSUC + BIO531*HCBIO +" "F 1 C531*HCC + UNK531*HCUNK + X2S531*HCX2S +" "F 2 ACN531*HCACN + COI531*HCCOI + DEN531*HCDEN +" "F 3 XSL531*HCSLG + EXT531*HCEXT + PRO531*HCPRO" "F WRITE(NHSTRY,*)'HHV OF 531 (BTU/HR) -- BTU531= ',BTU531" "C CALCULATE THE TOTAL HEAT INTO THE BOILER (MM BTU/HR)" "C" "F BTUTOT = (BTU615+BTU840+BTU803)/1E6" "C" "C CALCULATE % OF HEAT INPUT FOR EACH STREAM" "C" "F FRC615 = BTU615/(BTUTOT*1E6)" "F FRC840 = BTU840/(BTUTOT*1E6)" "F FRC803 = BTU803/(BTUTOT*1E6)" "F FRC531 = BTU531/(BTUTOT*1E6)" "C" "C WRITE RESULTS TO THE HISTORY FILE" "C" "F WRITE(NHSTRY,*)'TOTAL FEED TO BURNER'" "F WRITE(NHSTRY,*)'BTUTOT (HHV) (MM BTU/HR)= ',BTUTOT" "F WRITE(NHSTRY,*)'FRC615,FRC840= ',FRC615,FRC840" "F WRITE(NHSTRY,*)'FRC803= ',FRC803" "F WRITE(NHSTRY,*)'FRC531= ',FRC531" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = M803CMB \ \ COMMENTS COMMENTS = ( ";;" ";;" ";;" "; Needed for the HHV of the inlet biomass feed." ";;" "; JLJ 1/31/03. All values calculated from heats of formation (see HHV_Vals.i" ) \ ? CALCULATOR COMBHET2 ? ; "SET1_MOLE" ; \ DEFINE FVN = HLETOT FVN-VARTYPE = PARAMETER FVN-PARAMNO = 2 \ \ DEFINE FVN = WATCON FVN-VARTYPE = PARAMETER FVN-PARAMNO = 3 \ \ DEFINE FVN = WMLGLU FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = GLUCOSE FVN-ID2 = 1 \ \ DEFINE FVN = CMBGLU FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = GLUCOSE FVN-ID2 = 1 \ \ DEFINE FVN = WMLXYL FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = XYLOSE FVN-ID2 = 1 \ \ DEFINE FVN = CMBXYL FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = XYLOSE FVN-ID2 = 1 \ \ DEFINE FVN = WMLSOL FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = SOLSLDS FVN-ID2 = 1 \ \ DEFINE FVN = CMBSOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 10 \ \ DEFINE FVN = WMLARA FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = ARABINOS FVN-ID2 = 1 \ \ DEFINE FVN = CMBARA FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = ARABINOS FVN-ID2 = 1 \ \ DEFINE FVN = WMLGAL FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = GALACTOS FVN-ID2 = 1 \ \ DEFINE FVN = CMBGAL FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = GALACTOS FVN-ID2 = 1 \ \ DEFINE FVN = WMLXNS FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = MANNOSE FVN-ID2 = 1 \ \ DEFINE FVN = CMBXNS FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = MANNOSE FVN-ID2 = 1 \ \ DEFINE FVN = WMLGLO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = GLUCOLIG FVN-ID2 = 1 \ \ DEFINE FVN = CMBGLO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = GLUCOLIG FVN-ID2 = 1 \ \ DEFINE FVN = WMLCLB FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = CELLOB FVN-ID2 = 1 \ \ DEFINE FVN = CMBCLB FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = CELLOB FVN-ID2 = 1 \ \ DEFINE FVN = WMLXYO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = XYLOLIG FVN-ID2 = 1 \ \ DEFINE FVN = CMBXYO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = XYLOLIG FVN-ID2 = 1 \ \ DEFINE FVN = WMLXNO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = MANOLIG FVN-ID2 = 1 \ \ DEFINE FVN = CMBXNO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = MANOLIG FVN-ID2 = 1 \ \ DEFINE FVN = WMLGAO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = GALAOLIG FVN-ID2 = 1 \ \ DEFINE FVN = CMBGAO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = GALAOLIG FVN-ID2 = 1 \ \ DEFINE FVN = WMLARO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = ARABOLIG FVN-ID2 = 1 \ \ DEFINE FVN = CMBARO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = ARABOLIG FVN-ID2 = 1 \ \ DEFINE FVN = WMLXLL FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = XYLITOL FVN-ID2 = 1 \ \ DEFINE FVN = CMBXLL FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = XYLITOL FVN-ID2 = 1 \ \ DEFINE FVN = WMLETH FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = ETHANOL FVN-ID2 = 1 \ \ DEFINE FVN = CMBETH FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = ETHANOL FVN-ID2 = 1 \ \ DEFINE FVN = WMLFUR FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = FURFURAL FVN-ID2 = 1 \ \ DEFINE FVN = WMLXMF FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = HMF FVN-ID2 = 1 \ \ DEFINE FVN = WMLCH4 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = CH4 FVN-ID2 = 1 \ \ DEFINE FVN = CMBCH4 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = CH4 FVN-ID2 = 1 \ \ DEFINE FVN = WMLXLA FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = LACID FVN-ID2 = 1 \ \ DEFINE FVN = CMBXLA FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = LACID FVN-ID2 = 1 \ \ DEFINE FVN = WMLAAC FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = AACID FVN-ID2 = 1 \ \ DEFINE FVN = CMBAAC FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = AACID FVN-ID2 = 1 \ \ DEFINE FVN = WMLACN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = NH4ACET FVN-ID2 = 1 \ \ DEFINE FVN = CMBACN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = NH4ACET FVN-ID2 = 1 \ \ DEFINE FVN = WMLGLY FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = GLYCEROL FVN-ID2 = 1 \ \ DEFINE FVN = CMBGLY FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = GLYCEROL FVN-ID2 = 1 \ \ DEFINE FVN = WMLSUC FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = SUCCACID FVN-ID2 = 1 \ \ DEFINE FVN = CMBSUC FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = SUCCACID FVN-ID2 = 1 \ \ DEFINE FVN = WMLCOI FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = OIL FVN-ID2 = 1 \ \ DEFINE FVN = CMBCOI FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = OIL FVN-ID2 = 1 \ \ DEFINE FVN = WMLACO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = ACETOLIG FVN-ID2 = 1 \ \ DEFINE FVN = CMBACO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = ACETOLIG FVN-ID2 = 1 \ \ DEFINE FVN = WMLUNK FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = UNKNOWN FVN-ID2 = 1 \ \ DEFINE FVN = WMLX2S FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = H2S FVN-ID2 = 1 \ \ DEFINE FVN = CMBX2S FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = H2S FVN-ID2 = 1 \ \ DEFINE FVN = WMLDEN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = DENAT FVN-ID2 = 1 \ \ DEFINE FVN = CMBDEN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = DENAT FVN-ID2 = 1 \ \ DEFINE FVN = WMLCEL FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = CELLULOS FVN-ID2 = 1 \ \ DEFINE FVN = CMBCEL FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = CELLULOS FVN-ID2 = 1 \ \ DEFINE FVN = WMLXYN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = XYLAN FVN-ID2 = 1 \ \ DEFINE FVN = CMBXYN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = XYLAN FVN-ID2 = 1 \ \ DEFINE FVN = WMLXLG FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = LIGNIN FVN-ID2 = 1 \ \ DEFINE FVN = CMBXLG FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = LIGNIN FVN-ID2 = 1 \ \ DEFINE FVN = WMLCLS FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = CELLULAS FVN-ID2 = 1 \ \ DEFINE FVN = WMLBIO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = BIOMASS FVN-ID2 = 1 \ \ DEFINE FVN = WMLZYM FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = ZYMO FVN-ID2 = 1 \ \ DEFINE FVN = WMLARN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = ARABINAN FVN-ID2 = 1 \ \ DEFINE FVN = CMBARN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = ARABINAN FVN-ID2 = 1 \ \ DEFINE FVN = WMLXNN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = MANNAN FVN-ID2 = 1 \ \ DEFINE FVN = CMBXNN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = MANNAN FVN-ID2 = 1 \ \ DEFINE FVN = WMLGAN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = GALACTAN FVN-ID2 = 1 \ \ DEFINE FVN = CMBGAN FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = HCOM FVN-ID1 = GALACTAN FVN-ID2 = 1 \ \ DEFINE FVN = WMLTAR FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = TAR FVN-ID2 = 1 \ \ DEFINE FVN = WMLACE FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = ACETATE FVN-ID2 = 1 \ \ DEFINE FVN = WMLC FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = C FVN-ID2 = 1 \ \ DEFINE FVN = WMLSLG FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = LIGNIN FVN-ID2 = 1 \ \ DEFINE FVN = WMLEXT FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = EXTRACT FVN-ID2 = 1 \ \ DEFINE FVN = CMBEXT FVN-VARTYPE = PARAMETER FVN-PARAMNO = 11 \ \ DEFINE FVN = WMLPRO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = PROTEIN FVN-ID2 = 1 \ \ DEFINE FVN = CMBPRO FVN-VARTYPE = PARAMETER FVN-PARAMNO = 12 \ \ DEFINE FVN = WMLH2O FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = H2O FVN-ID2 = 1 \ \ DEFINE FVN = ETH615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FUR615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = CH4615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = AAC615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = X2S615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = WAT615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = FLW615 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WAT803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = GLU803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = SOL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = ARA803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = GAL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = XNS803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GLO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CLB803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XYO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = XNO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GAO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = XLL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = ETH803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FUR803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = CH4803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = XLA803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = AAC803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = ACN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = GLY803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUC803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = COI803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = ACO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = UNK803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = X2S803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = DEN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = SLG803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXT803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PRO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = CEL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XYN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = XLG803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = LIGNIN \ \ DEFINE FVN = CLS803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULAS \ \ DEFINE FVN = BIO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = BIOMASS \ \ DEFINE FVN = ZYM803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ZYMO \ \ DEFINE FVN = ARN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ARABINAN \ \ DEFINE FVN = XNN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = GAN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = TAR803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = TAR \ \ DEFINE FVN = ACE803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ACETATE \ \ DEFINE FVN = C803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = C \ \ DEFINE FVN = FLW83M FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLW83C FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WAT840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = GLU840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = SOL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = ARA840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = GAL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = XNS840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GLO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CLB840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XYO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = XNO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GAO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = XLL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = ETH840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FUR840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = CH4840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = XLA840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = AAC840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = ACN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = GLY840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUC840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = COI840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = ACO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = UNK840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = X2S840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = DEN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = SLG840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXT840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PRO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = CEL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XYN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = XLG840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = LIGNIN \ \ DEFINE FVN = CLS840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULAS \ \ DEFINE FVN = BIO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = BIOMASS \ \ DEFINE FVN = ZYM840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = ZYMO \ \ DEFINE FVN = ARN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = ARABINAN \ \ DEFINE FVN = XNN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = GAN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = TAR840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = TAR \ \ DEFINE FVN = ACE840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = ACETATE \ \ DEFINE FVN = C840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = C \ \ DEFINE FVN = FL840M FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FL840C FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WT615B FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = WT803B FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = WT840B FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ FORTRAN FORTRAN-EXEC = ( "C SAMPLES MOLECULAR WEIGHTS AND LOWER HEATING VALUES (J/KMOL) FOR EACH" "C COMPONENT : EACH COMPONENT GETS A 3 LETTER CODE" "C GLUCOSE = GLU" "C XYLOSE = XYL" "C SOLUBLE SOLIDS = SOL" "C ARABINOSE = ARA" "C GALACTOSE = GAL" "C MANNOSE = XNS" "C GLUCOLIG = GLO" "C CELLOBIOSE = CLB" "C XYLOLIG = XYO" "C MANOLIG = XNO" "C GALAOLIG = GAO" "C ARABOLIG = ARO" "C XYLITOL = XLL" "C ETHANOL = ETH" "C FURFURAL = FUR" "F CMBFUR = -2.25134E+09" "C HMF = XMF" "F CMBXMF = -2.67171E+09" "C CH4 = CH4" "C LACTIC ACID = XLA" "C ACETIC ACID = AAC" "C NH4ACET = ACN" "C GLYCEROL = GLY" "C SUCCINIC ACID = SUC" "C OIL = COI" "C ACETOLIG = ACO" "C UNKNOWN = UNK" "F CMBUNK = -1.94478E+08" "C H2S = X2S" "C DENATURANT = DEN" "C CELLULOSE = CEL" "C XYLAN = XYN" "C LIGNIN = XLG" "C CELLULASE = CLS" "F CMBCLS = -5.10475E+08" "C BIOMASS = BIO" "F CMBBIO = -4.95710E+08" "C ZYMO = ZYM" "F CMBZYM = -4.80650E+08" "C ARABINAN = ARN" "C MANNAN = XNN" "C GALACTAN = GAN" "C TAR = TAR" "F CMBTAR = -2.41424E+09" "C ACETATE = ACE" "F CMBACE = -8.14332E+08" "C C = C" "F CMBC = -1.02652E+09" "C SOLUBLE LIGNIN = SLG" "F CMBSLG = -3.64752E+09" "C EXTRACTIVES = EXT" "C PROTEIN = PRO" "C THE HEAT OF VAPORIZATION OF WATER IS 2442.5 KJ/KG AT 25C" "C THE MOLECULAR WEIGHT OF WATER IS 18.01528 1ST STUDENT EDITION" "C VAPWAT IS THE HEAT OF VAPORIZATION OF WATER IN J/KMOL" "F VAPWAT = 2442.5 * 1000 * 18.01528" "C THE FOLLOWING ARE TEST WRITE STATEMENTS THAT SHOW THE VALUES" "C THE LOWER HEATING VALUE OF METHANE IS 802620000 J/KMOL" "C THE LOWER HEATING VALUE OF ETHANOL IS 1235000000 J/KMOL" "F WRITE(NHSTRY,*)'MW CH4=',WMLCH4" "F WRITE(NHSTRY,*)'HEAT OF COMB CH4 (J/KMOL)=',CMBCH4" "F WRITE(NHSTRY,*)'MW ETHANOL=',WMLETH" "F WRITE(NHSTRY,*)'HEAT OF COMB ETHANOL=',CMBETH" "C MORE TESTS" "F WRITE(NHSTRY,*)'MW GLU=',WMLGLU" "F WRITE(NHSTRY,*)'HEAT OF COMB GLU=',CMBGLU" "F WRITE(NHSTRY,*)'MW XYL=',WMLXYL" "F WRITE(NHSTRY,*)'HEAT OF COMB XYL=',CMBXYL" "F WRITE(NHSTRY,*)'MW SOL=',WMLSOL" "F WRITE(NHSTRY,*)'HEAT OF COMB SOL=',CMBSOL" "F WRITE(NHSTRY,*)'MW ARA=',WMLARA" "F WRITE(NHSTRY,*)'HEAT OF COMB ARA=',CMBARA" "F WRITE(NHSTRY,*)'MW GAL=',WMLGAL" "F WRITE(NHSTRY,*)'HEAT OF COMB GAL=',CMBGAL" "F WRITE(NHSTRY,*)'MW XNS=',WMLXNS" "F WRITE(NHSTRY,*)'HEAT OF COMB XNS=',CMBXNS" "F WRITE(NHSTRY,*)'MW GLO=',WMLGLO" "F WRITE(NHSTRY,*)'HEAT OF COMB GLO=',CMBGLO" "F WRITE(NHSTRY,*)'MW CLB=',WMLCLB" "F WRITE(NHSTRY,*)'HEAT OF COMB CLB=',CMBCLB" "F WRITE(NHSTRY,*)'MW XYO=',WMLXYO" "F WRITE(NHSTRY,*)'HEAT OF COMB XYO=',CMBXYO" "F WRITE(NHSTRY,*)'MW XNO=',WMLXNO" "F WRITE(NHSTRY,*)'HEAT OF COMB XNO=',CMBXNO" "F WRITE(NHSTRY,*)'MW GAO=',WMLGAO" "F WRITE(NHSTRY,*)'HEAT OF COMB GAO=',CMBGAO" "F WRITE(NHSTRY,*)'MW ARO=',WMLARO" "F WRITE(NHSTRY,*)'HEAT OF COMB ARO=',CMBARO" "F WRITE(NHSTRY,*)'MW XLL=',WMLXLL" "F WRITE(NHSTRY,*)'HEAT OF COMB XLL=',CMBXLL" "F WRITE(NHSTRY,*)'MW FUR=',WMLFUR" "F WRITE(NHSTRY,*)'HEAT OF COMB FUR=',CMBFUR" "F WRITE(NHSTRY,*)'MW XMF=',WMLXMF" "F WRITE(NHSTRY,*)'HEAT OF COMB XMF=',CMBXMF" "F WRITE(NHSTRY,*)'MW XLA=',WMLXLA" "F WRITE(NHSTRY,*)'HEAT OF COMB XLA=',CMBXLA" "F WRITE(NHSTRY,*)'MW AAC=',WMLAAC" "F WRITE(NHSTRY,*)'HEAT OF COMB AAC=',CMBAAC" "F WRITE(NHSTRY,*)'MW GLY=',WMLGLY" "F WRITE(NHSTRY,*)'HEAT OF COMB GLY=',CMBGLY" "F WRITE(NHSTRY,*)'MW SUC=',WMLSUC" "F WRITE(NHSTRY,*)'HEAT OF COMB SUC=',CMBSUC" "F WRITE(NHSTRY,*)'MW COI=',WMLCOI" "F WRITE(NHSTRY,*)'HEAT OF COMB COI=',CMBCOI" "F WRITE(NHSTRY,*)'MW ACO=',WMLACO" "F WRITE(NHSTRY,*)'HEAT OF COMB ACO=',CMBACO" "F WRITE(NHSTRY,*)'MW UNK=',WMLUNK" "F WRITE(NHSTRY,*)'HEAT OF COMB UNK=',CMBUNK" "F WRITE(NHSTRY,*)'MW X2S=',WMLX2S" "F WRITE(NHSTRY,*)'HEAT OF COMB X2S=',CMBX2S" "F WRITE(NHSTRY,*)'MW DEN=',WMLDEN" "F WRITE(NHSTRY,*)'HEAT OF COMB DEN=',CMBDEN" "F WRITE(NHSTRY,*)'MW CEL=',WMLCEL" "F WRITE(NHSTRY,*)'HEAT OF COMB CEL=',CMBCEL" "F WRITE(NHSTRY,*)'MW XYN=',WMLXYN" "F WRITE(NHSTRY,*)'HEAT OF COMB XYN=',CMBXYN" "F WRITE(NHSTRY,*)'MW XLG=',WMLXLG" "F WRITE(NHSTRY,*)'HEAT OF COMB XLG=',CMBXLG" "F WRITE(NHSTRY,*)'MW CLS=',WMLCLS" "F WRITE(NHSTRY,*)'HEAT OF COMB CLS=',CMBCLS" "F WRITE(NHSTRY,*)'MW BIO=',WMLBIO" "F WRITE(NHSTRY,*)'HEAT OF COMB BIO=',CMBBIO" "F WRITE(NHSTRY,*)'MW ZYM=',WMLZYM" "F WRITE(NHSTRY,*)'HEAT OF COMB ZYM=',CMBZYM" "F WRITE(NHSTRY,*)'MW ARN=',WMLARN" "F WRITE(NHSTRY,*)'HEAT OF COMB ARN=',CMBARN" "F WRITE(NHSTRY,*)'MW XNN=',WMLXNN" "F WRITE(NHSTRY,*)'HEAT OF COMB XNN=',CMBXNN" "F WRITE(NHSTRY,*)'MW GAN=',WMLGAN" "F WRITE(NHSTRY,*)'HEAT OF COMB GAN=',CMBGAN" "F WRITE(NHSTRY,*)'MW TAR=',WMLTAR" "F WRITE(NHSTRY,*)'HEAT OF COMB TAR=',CMBTAR" "F WRITE(NHSTRY,*)'MW ACE=',WMLACE" "F WRITE(NHSTRY,*)'HEAT OF COMB ACE=',CMBACE" "F WRITE(NHSTRY,*)'MW C=',WMLC" "F WRITE(NHSTRY,*)'HEAT OF COMB C=',CMBC" "F WRITE(NHSTRY,*)'MW SOLUBLE LIGNIN=',WMLSLG" "F WRITE(NHSTRY,*)'HEAT OF COMB SOLUBLE LIGNIN=',CMBSLG" "F WRITE(NHSTRY,*)'MW EXTRACTIVES=',WMLEXT" "F WRITE(NHSTRY,*)'HEAT OF COMB EXTRACTIVES=',CMBEXT" "F WRITE(NHSTRY,*)'MW PROTEIN=',WMLPRO" "F WRITE(NHSTRY,*)'HEAT OF COMB PROTEIN=',CMBPRO" "F WRITE(NHSTRY,*)'MW H2O=',WMLH2O" "C FOLLOWING IS THE CALULATION OF LHV FOR STREAM 615" "C VLW615 CALCULATES THE LOWER HEATING VALUE IN J/HR" "C WATER ENTERING THE BURNER IS NOT INCLUDED IN THIS CALCULATION," "C BECAUSE IT IS ALREADY A VAPOR" "F VLW615 = ETH615 * CMBETH + FUR615 * CMBFUR" "F 1 + XMF615 * CMBXMF + CH4615 * CMBCH4" "F 2 + AAC615 * CMBAAC + X2S615 * CMBX2S" "C HLV615 CALCULATES THE LOWER HEATING VALUE IN J/KG" "F HLV615 = VLW615 / FLW615" "C HLE615 CALCULATES THE LOWER HEATING VALUE IN BTU/LB" "C CONVERSION FACTORS 9.478E-4 BTU/J & 2.20462 LB/KG" "F HLE615 = HLV615 * 9.478E-4 / 2.20462" "F WRITE(NHSTRY,*)'LHV OF 615 (J/HR)=',VLW615" "F WRITE(NHSTRY,*)'LHV OF 615 (J/KG)=',HLV615" "F WRITE(NHSTRY,*)'LHV OF 615 (BTU/LB)=',HLE615" "C FOLLOWING IS THE CALCULATION OF LHV FOR STREAM 803" "C VLW803 CALCULATES THE LOWER HEATING VALUE IN J/HR" "F VLW803 = GLU803 * CMBGLU + XYL803 * CMBXYL" "F 1 + SOL803 * CMBSOL + ARA803 * CMBARA" "F 2 + GAL803 * CMBGAL + XNS803 * CMBXNS" "F 3 + GLO803 * CMBGLO + CLB803 * CMBCLB" "F 4 + XYO803 * CMBXYO + XNO803 * CMBXNO" "F 5 + GAO803 * CMBGAO + ARO803 * CMBARO" "F 6 + XLL803 * CMBXLL + ETH803 * CMBETH" "F 7 + FUR803 * CMBFUR + XMF803 * CMBXMF" "F 8 + CH4803 * CMBCH4 + XLA803 * CMBXLA" "F 9 + AAC803 * CMBAAC + ACN803 * CMBACN" "F 1 + GLY803 * CMBGLY + SUC803 * CMBSUC" "F 2 + COI803 * CMBCOI + ACO803 * CMBACO" "F 3 + UNK803 * CMBUNK + X2S803 * CMBX2S" "F 4 + DEN803 * CMBDEN + SLG803 * CMBSLG" "F 5 + EXT803 * CMBEXT + PRO803 * CMBPRO" "F 6 + CEL803 * CMBCEL" "F 5 + XYN803 * CMBXYN + XLG803 * CMBXLG" "F 6 + CLS803 * CMBCLS + BIO803 * CMBBIO" "F 7 + ZYM803 * CMBZYM + ARN803 * CMBARN" "F 8 + XNN803 * CMBXNN + GAN803 * CMBGAN" "F 9 + TAR803 * CMBTAR + ACE803 * CMBACE" "F 1 + C803 * CMBC" "F 9 + WAT803 * VAPWAT" "C HLV803 CALCULATES THE LOWER HEATING VALUE IN J/KG" "F HLV803 = VLW803 / (FLW83M + FLW83C)" "C HLE803 CALCULATES THE LOWER HEATING VALUE IN BTU/LB" "C CONVERSION FACTORS 9.478E-4 BTU/J & 2.20462 LB/KG" "F HLE803 = HLV803 * 9.478E-4 / 2.20462" "F WRITE(NHSTRY,*)'LHV OF 803 (J/HR)=',VLW803" "F WRITE(NHSTRY,*)'LHV OF 803 (J/KG)=',HLV803" "F WRITE(NHSTRY,*)'LHV OF 803 (BTU/LB)=',HLE803" "C FOLLOWING IS THE CALCULATION OF LHV FOR STREAM 840" "C VLW840 CALCULATES THE LOWER HEATING VALUE IN J/HR" "F VLW840 = GLU840 * CMBGLU + XYL840 * CMBXYL" "F 1 + SOL840 * CMBSOL + ARA840 * CMBARA" "F 2 + GAL840 * CMBGAL + XNS840 * CMBXNS" "F 3 + GLO840 * CMBGLO + CLB840 * CMBCLB" "F 4 + XYO840 * CMBXYO + XNO840 * CMBXNO" "F 5 + GAO840 * CMBGAO + ARO840 * CMBARO" "F 6 + XLL840 * CMBXLL + ETH840 * CMBETH" "F 7 + FUR840 * CMBFUR + XMF840 * CMBXMF" "F 8 + CH4840 * CMBCH4 + XLA840 * CMBXLA" "F 9 + AAC840 * CMBAAC + ACN840 * CMBACN" "F 1 + GLY840 * CMBGLY + SUC840 * CMBSUC" "F 2 + COI840 * CMBCOI + ACO840 * CMBACO" "F 3 + UNK840 * CMBUNK + X2S840 * CMBX2S" "F 4 + DEN840 * CMBDEN + SLG840 * CMBSLG" "F 5 + EXT840 * CMBEXT + PRO840 * CMBPRO" "F 6 + CEL840 * CMBCEL" "F 5 + XYN840 * CMBXYN + XLG840 * CMBXLG" "F 6 + CLS840 * CMBCLS + BIO840 * CMBBIO" "F 7 + ZYM840 * CMBZYM + ARN840 * CMBARN" "F 8 + XNN840 * CMBXNN + GAN840 * CMBGAN" "F 9 + TAR840 * CMBTAR + ACE840 * CMBACE" "F 1 + C840 * CMBC" "F 9 + WAT840 * VAPWAT" "C HLV840 CALCULATES THE LOWER HEATING VALUE IN J/KG" "F FLW840 = FL840M + FL840C" "F HLV840 = VLW840 / FLW840" "C HLE840 CALCULATES THE LOWER HEATING VALUE IN BTU/LB" "C CONVERSION FACTORS 9.478E-4 BTU/J & 2.20462 LB/KG" "F HLE840 = HLV840 * 9.478E-4 / 2.20462" "F WRITE(NHSTRY,*)'LHV OF 840 (J/HR)=',VLW840" "F WRITE(NHSTRY,*)'LHV OF 840 (J/KG)=',HLV840" "F WRITE(NHSTRY,*)'LHV OF 840 (BTU/LB)=',HLE840" "F VLWTOT = VLW615 + VLW803 + VLW840" "F HLVTOT = VLWTOT / (FLW615 + FLW83M + FLW83C + FLW840)" "C HLETOT CALCULATES THE LOWER HEATING VALUE IN BTU/LB" "C CONVERSION FACTORS 9.478E-4 BTU/J & 2.20462 LB/KG" "F HLETOT = HLVTOT * 9.478E-4 / 2.20462" "F WRITE(NHSTRY,*)'TOTAL LHV (J/HR)=',VLWTOT" "F WRITE(NHSTRY,*)'TOTAL LHV (J/KG)=',HLVTOT" "F WRITE(NHSTRY,*)'TOTAL LHV (BTU/LB)=',HLETOT" "C WATCON IS THE WATER CONCENTRATION IN THE BOILER FEEDSTREAMS" "F WATCON = (WT615B + WT803B + WT840B) /" "F 1 (FLW615 + FLW83M + FLW83C + FLW840)" "F WRITE(NHSTRY,*)'WATER CONCENTRATION IN FEEDS TO BURNER=',WATCON" ) \ \ "READ-VARS" READ-VAR = ( WMLGLU CMBGLU WMLXYL WMLSOL WMLARA WMLGAL WMLXNS WMLGLO WMLCLB WMLXYO WMLXNO WMLGAO WMLARO WMLXLL WMLETH CMBETH WMLFUR WMLXMF WMLCH4 CMBCH4 WMLXLA CMBXLA WMLAAC CMBAAC WMLACN CMBACN WMLGLY CMBGLY WMLSUC CMBSUC WMLCOI CMBCOI WMLACO WMLUNK WMLX2S CMBX2S WMLDEN CMBDEN WMLCEL WMLXYN WMLXLG WMLCLS WMLBIO WMLZYM WMLARN WMLXNN WMLGAN WMLTAR WMLACE WMLC ETH615 FUR615 XMF615 CH4615 AAC615 X2S615 WAT615 FLW615 GLU803 XYL803 SOL803 ARA803 GAL803 XNS803 GLO803 CLB803 XYO803 XNO803 GAO803 ARO803 XLL803 ETH803 FUR803 XMF803 CH4803 XLA803 AAC803 ACN803 GLY803 SUC803 COI803 ACO803 UNK803 X2S803 DEN803 CEL803 XYN803 XLG803 CLS803 BIO803 ZYM803 ARN803 XNN803 GAN803 TAR803 ACE803 C803 FLW83M FLW83C CH4840 WT615B WT803B CMBSOL ) \ \ "WRITE-VARS" WRITE-VAR = ( HLETOT WATCON ) \ \ COMMENTS COMMENTS = ( ";;" "; Mark Ruth 2 Nov 98" "; To replace COMBHEAT" ";;" "; (JLJ 1/31/03) Missing values calculated using HHV_Values.inp" ";;" "; LHV calculated by FEEDPROP" "; DEFINE CMBFUR UNARY-PARAM VARIABLE=HCOM ID1=FURFURAL ID2=1" "; Unary-Param incorrect, so it is input" "; DEFINE CMBXMF UNARY-PARAM VARIABLE=HCOM ID1=HMF ID2=1" "; Unary-Param incorrect, so it is input" "; DEFINE CMBUNK UNARY-PARAM VARIABLE=HCOM ID1=UNKNOWN ID2=1" "; Unary-Param was not available, so it is input" "; DEFINE CMBCLS UNARY-PARAM VARIABLE=HCOM ID1=CELLULAS ID2=1" "; Unary-Param was not available, so it is input" "; DEFINE CMBBIO UNARY-PARAM VARIABLE=HCOM ID1=BIOMASS ID2=1" "; Unary-Param was not available, so it is input" "; DEFINE CMBZYM UNARY-PARAM VARIABLE=HCOM ID1=ZYMO ID2=1" "; Unary-Param was not available, so it is input" "; DEFINE CMBTAR UNARY-PARAM VARIABLE=HCOM ID1=TAR ID2=1" "; Unary-Param incorrect, so it is input" "; DEFINE CMBACE UNARY-PARAM VARIABLE=HCOM ID1=ACETATE ID2=1" "; Unary-Param incorrect, so it is input" "; DEFINE CMBC UNARY-PARAM VARIABLE=HCOM ID1=C ID2=1" "; BGA, 6/18/02, Unary-Param was incorrect, so it is input" "; DEFINE CMBSLG UNARY-PARAM VARIABLE=HCOM ID1=LIGNIN ID2=1" "; Unary-Param was not available, so it is input" "; LHV calculated by FEEDPROP" "; LHV calculated by FEEDPROP" "; Water for MW calculation purposes" ";;" ";;" ";;" "; the following line could be used to include water if desired" "; BGA EDIT, 6/18/02, CHANGED TO + BECAUSE HEATS OF COMB WERE MODELED AS NEG." "; F 9 + WAT615 * VAPWAT" ";;" ";;" "; BGA EDIT, 6/18/02, CHANGED TO + BECAUSE HEATS OF COMB WERE MODELED AS NEG." ";;" ";;" ";;" "; BGA EDIT, 6/18/02, CHANGED TO + BECAUSE HEATS OF COMB WERE MODELED AS NEG." ";;" ";;" "; VLWTOT calculates the sum of the lower heating values of the 3 streams" "; HVLTOT calculates the lower heating value in J/kg" ";;" ";;" ) \ ? CALCULATOR "CSL-ENZY" ? ; "SET1_MOLE" ; \ DEFINE FVN = CF FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 412A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CFS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CND FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 436 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 431 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SND FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 434 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FSCLS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 310A FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = FCLS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 311A FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = CFD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 412A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = CFSD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = CODD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 417 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = CNDD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 436 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = CLSP FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 414 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CLSS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 423 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CLNUTR FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 415 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = TTLCSL FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 417 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C" "F CLD = 0.01" "C CLD IS THE DEMAND FOR CSL IN CELLULASE PRODUCTION IN KG/KG" "F CLSP = CLD * (CF + CFS + CND)" "C" "F CLSD = 0.01" "C CLSD IS THE DEMAND FOR CSL IN CELLULASE SEED PRODUCTION IN KG/KG" "F CLSS = CLSD * (SD + SND)" "C" "C CN IS THE CELLULASE NUTRIENT DEMAND IN LB/LB TOTAL STREAM" "C THIS VALUE IS FROM THE BASE CASE & SHOULD BE UPDATED WITH" "C NEW DATA. 0.0043 = 4.3 G/L FROM THE 1991 BASE CASE (1.4 G/L" "C AMMONIUM SULFATE, 2.0 G/L POTASSIUM PHOSPHATE, 0.3 G/L MAGNESIUM" "C SULFATE*7H2O, 0.4 G/L CALCIUM CHLORIDE*2H2O, & 0.2 G/L TWEEN 80." "C" "F CN = 0.0043" "F CLNUTR = CN * (CF + CFS + CND)" "C CALCULATE THE TOTAL CSL USED" "F TTLCSL = CLSS + CLSP + FSCLS + FCLS" "C" "F COD=0.001" "C COD IS THE CORN OIL DEMAND IN L/L (ANTIFOAM)" "C" "F CO = COD * (CF/CFD + CFS/CFSD + CND/CNDD) * CODD" "C" ) \ \ "READ-VARS" READ-VAR = ( CF CFS CND SD SND FSCLS FCLS CFD CFSD CODD CNDD ) \ \ "WRITE-VARS" WRITE-VAR = ( CLSP CLSS CLNUTR TTLCSL CO ) \ \ COMMENTS COMMENTS = ( ";-------------------------------------------------------" "; STORAGE FORTRAN BLOCKS - AREA 7000" ";------------------------------------------------------" ";;" "; This FORTRAN block calculates the CSL requirements of" "; the Cellulase Production and Seed Fermentation" "; Streams 414 and 423" "; Also calculates the ""Other Nutrients"" demand, Stream 415" "; Finally the total CLS requirements are calculated and" "; the flow of 735 set" ";;" "; INPUT FLOWS" "; INPUT DENSITIES" "; OUTPUTS" ) \ ? CALCULATOR CWDEM ? ; "SET1_MOLE" ; \ DEFINE FVN = CWTOT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 946 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CWEVAP FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 949 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CWBL1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 944 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CWBL2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 944A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CWMKUP FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 941 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CWWNDG FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 942 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C WINDAGE IS ASSUMED TO BE 0.1% OF THE TOTAL FLOW TO THE TOWER (946)" "C BLOWDOWN IS ASSUMED TO BE EQUAL TO THE EVAP LOSS + WINDAGE WITH" "C 90% BEING RECOVERED TO THE TOWER (10% LOSS NEEDING MAKEUP)" "C" "F CWWNDG = 0.001 * CWTOT" "F CWBL2 = 0.1 * (CWWNDG + CWEVAP)" "F CWBL1 = CWBL2" "F CWMKUP = CWBL2 + CWWNDG + CWEVAP" "C" ) \ \ "READ-VARS" READ-VAR = ( CWEVAP CWTOT ) \ \ "WRITE-VARS" WRITE-VAR = ( CWBL2 CWMKUP CWWNDG CWBL1 ) \ \ COMMENTS COMMENTS = ( "; EXECUTE BEFORE T914" ";;" ";;" ";THIS BLOCK CALCULATES THE TOTAL WELL WATER DEMAND FOR THE" ";ENTIRE PROCESS." ";PWMU IS PROCESS H2O MAKE-UP. CTL IS COOLING TOWER LOSSES." ";STLOSS ARE LOSSES FROM THE STEAM SYSTEM, INCLUDING DIRECT" ";STEAM INJECTION & BOILER BLOWDOWN. CIPCS ARE LOSSES FROM" "; THE CIP/CS SYSTEM. CW IS THE COOLING TOWER STREAM." "; Read Variable - total flow to Cooling tower" "; Read Variable - Evaporative Loss" "; Read Variable - Specified Value of Blowdown" "; Calculated value of Blowdown" "; Total Cooling Tower Make-up" ";;" ) \ ? CALCULATOR D502QCR ? ; "SET1_MOLE" ; \ DEFINE FVN = FD502 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 510 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = Q502R FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QRD502 \ \ DEFINE FVN = Q502C FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QCD502 \ \ FORTRAN FORTRAN-EXEC = ( "F WRITE(NHSTRY,'('' FORTRAN D502QCR RESULTS'')')" "F WRITE(NHSTRY,'('' D502 COLUMN FEED = '',G12.5)')FD502" "F REBFCT = 3.9439 / 6.2404E4" "F CNDFCT = 21.0407 / 6.2404E4" "F QR = FD502 * REBFCT" "F QC = FD502 * CNDFCT" "F Q502R = QR * (-1E6/3.599948)" "F Q502C = QC * ( 1E6/3.599948)" "F WRITE(NHSTRY,'('' D502 REBOILER = '',G12.5,'' MMKCAL/HR'')')QR" "F WRITE(NHSTRY,'('' D502 REBOILER = '',G12.5,'' CAL/S'')')Q502R" "F WRITE(NHSTRY,'('' D502 CONDENSER = '',G12.5,'' MMKCAL/HR'')')QC" "F WRITE(NHSTRY,'('' D502 CONDENSER = '',G12.5,'' CAL/S'')')Q502C" ) \ \ "READ-VARS" READ-VAR = ( FD502 ) \ \ "WRITE-VARS" WRITE-VAR = ( Q502R Q502C ) \ \ COMMENTS COMMENTS = ( ";;" "; Heat in MMkcal/hr divided by flow of 510 in kg/hr from R0301C" ) \ ? CALCULATOR DENATURE ? ; "SET1_MOLE" ; \ DEFINE FVN = PDENS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 515E FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = PROD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 515E FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = GDENS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 701 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = GGAS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 701 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "F DPERC = 4.75" "C" "C CALCULATE THE FLOWRATE OF DENATURANT INTO THE SYSTEM." "C" "F GGAS = DPERC / 100 * (PROD / PDENS) * GDENS" "C" ) \ \ "READ-VARS" READ-VAR = ( PDENS PROD GDENS ) \ \ "WRITE-VARS" WRITE-VAR = ( GGAS ) \ \ COMMENTS COMMENTS = ( ";THIS BLOCK CALCULATES THE AMOUNT OF DENATURANT REQUIRED." ";IT ALSO CALCULATES THE SIZE OF THE GASOLINE (DENATURANT)" ";TANK." "; INPUTS" "; OUTPUT" ";;" ";SPECIFY THE DENATURANT ADDITION (PART DENAT / 100 PARTS ETHANOL FUEL)" ";4.75 PER MARK RUTH MEMO 3 NOVEMBER 1999" ";;" ) \ ? CALCULATOR DEWPT ? ; "SET1_MOLE" ; \ DEFINE FVN = ACIDFR FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = 804D FVN-SUBS = MIXED FVN-COMPONEN = H2SO4 \ \ DEFINE FVN = H2OFR FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = 804D FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = PRES FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 804D FVN-SUBS = MIXED FVN-VARIABLE = PRES \ \ DEFINE FVN = TOUT FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "H801+" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM \ \ FORTRAN FORTRAN-EXEC = ( "C" "C THE ACID DEW POINT OF THE FLUE GAS IS CALCULATED" "C FROM THE FOLLOWING EQUATION THAT WAS TAKEN FROM" "C HYDROCARBON PROCESSING, FEBRUARY 1993, GANAPATHY, V." "C ""COMPUTE DEW POINT OF GASES""." "C" "C THE MOLE FRACTIONS OF H2O AND H2SO4 ARE ASSUMED" "C TO BE EQUIVALENT TO THEIR PARTIAL PRESSURES" "C" "F HGPRES = PRES*760.0" "C HGPRES IS THE PRESSURE IN MM HG" "C IF THE ACID GAS CONCENTRATION IS VERY LOW, SET AN UPPER LIMIT TO THE" "C VALUE CALCULATED." "F IF (ACIDFR .LT. 1E-12) THEN" "F TDP = 433" "F ELSE" "F TDPINV = (2.276E-3)-2.943E-5*LOG(H2OFR*HGPRES) -" "F 1 8.58E-5*LOG(ACIDFR*HGPRES) +" "F 2 6.2E-6*LOG(H2OFR*HGPRES)*LOG(ACIDFR*HGPRES)" "F TDP = 1.0/TDPINV" "F END IF" "C" "C" "C WRITE THE ANSWERS TO THE HISTORY FILE." "C" "F WRITE(NHSTRY,*)'THE ACID DEW POINT IS= ',TDP, 'K'" "F WRITE(NHSTRY,*)'PRES,H2OFR,ACIDFR= ',PRES,H2OFR,ACIDFR" "F TDPC = TDP - 273.2" "F TEXIT = TDPC + 34.7" "C" "C THE AIR PREHEATER EXIT TEMPERATURE SHOULD HAVE A 50-75 F" "C SAFETY FACTOR. THE AVERAGE IS 62.5 F (34.7 C)" "C" "C CHECK TO SEE IF TEXIT IS BELOW AIR PREHEATER EXIT" "C TEMPERATURE. IF IT IS, THEN LEAVE THE AIR PREHEATER TEMPERATURE" "C IF NOT, THEN SET THE AIR PREHEATER TEMPERATURE EQUAL TO THE" "C TEXIT" "C" "F IF (TEXIT .GT. 149.) THEN" "F TOUT = TEXIT" "F ELSE" "F TOUT=149." "F END IF" ) \ \ "READ-VARS" READ-VAR = ( ACIDFR H2OFR PRES ) \ \ "WRITE-VARS" WRITE-VAR = ( TOUT ) \ \ COMMENTS COMMENTS = ( ";;" ";;" ";;" ) \ ? CALCULATOR EFFCY ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F COMMON / HEATIN / BTUTOT" "F COMMON / EFFCYS /HTRATE, BLREFF" ) \ \ DEFINE FVN = WKOUT FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WTOTAL \ \ DEFINE FVN = QSTEAM FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QBOILER \ \ FORTRAN FORTRAN-EXEC = ( "C CALCULATE THE HEAT RATE(BTU/KWH)" "C" "F HTRATE = (BTUTOT*1.E6)/(-WKOUT)" "F WRITE(NHSTRY,*)'HTRATE,BTUTOT,WKOUT= ',HTRATE,BTUTOT,WKOUT" "C" "C CALCULATE THE BOILER EFFICIENCY" "C" "F BLRBTU = QSTEAM*3600.*3.968E-3" "C BLRBTU IS THE HEAT FROM THE BOILER IN BTU/HR" "C AND IS CONVERTED FROM CAL/S" "C 3600 S/H AND 3.968E-3 BTU/CAL" "C" "F BLREFF = BLRBTU/(BTUTOT*1.E6)" "F WRITE(NHSTRY,*)'BLREFF,BLRBTU,BTUTOT= ',BLREFF,BLRBTU,BTUTOT" ) \ \ "READ-VARS" READ-VAR = ( WKOUT QSTEAM ) \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CALCULATOR ENZ2 ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "C MADE CHANGES (*) FOR A SEPARATE SACCHARIFICATION AND FERMENTATION MODE" "C KI, 3/10/02" "C *CELLULASE IS CALCULATED FOR WHOLE STREAM ENTERING AREA 300, STR. 301A" ) \ \ DEFINE FVN = CL301A FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 301A FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XM312 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CI312 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 312 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C ELOAD IS ENZYME LOADING (FPU / G CELLULOSE)" "F ELOAD = 12.0" "C ECONC IS ENZYME CONCENTRATION (50 FPU/ML IS APPROX CURRENT IOGEN CONC" "F ECONC = 50.0" "C ERAT IS ENZYME RATIO (SOLID ENZYME TO WATER)" "F ERAT = CI312 / (CI312 + XM312)" "C EREQ IS ENZYME REQUIRED (FPU / HR)" "F EREQ = ELOAD * 1000 * (CL301A)" "C DENS IS THE ASSUMED DENSITY OF THE ENZYME (1.000 USED BECAUSE WE ARE ONLY" "C MODELING ENZYME PROTEIN AND WATER; NO CELL MASS OR PRESERVATIVE) (G/ML)" "F DENS = 1.0" "C EREQM IS THE ENZYME REQUIRED (KG / HR)" "F EREQM = EREQ / ECONC * DENS / 1000" "F CI312 = ERAT * EREQM" "F XM312 = (1-ERAT) * EREQM" ) \ \ "READ-VARS" READ-VAR = ( CL301A ) \ \ "WRITE-VARS" WRITE-VAR = ( XM312 CI312 ) \ \ COMMENTS COMMENTS = ( "; DEFINE CL304 MASS-FLOW STREAM=304 SUBSTREAM=CISOLID &" "; COMPONENT=CELLULOS" ) \ ? CALCULATOR ENZYME ? ; "SET1_MOLE" ; \ DEFINE FVN = CELL1T FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 302 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = CELS1T FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = F1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = BTMSSPLT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 401 \ \ DEFINE FVN = CSDSPT FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = CLFDSPLT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 403 \ \ DEFINE FVN = CLIN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XIN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = CLSSPT FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = CLSSPLIT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 421 \ \ DEFINE FVN = CLYLD FVN-VARTYPE = PARAMETER FVN-PARAMNO = 41 \ \ FORTRAN FORTRAN-EXEC = ( "C" "C MADE CHANGES (*) FOR A SEPARATE SACCHARIFICATION AND FERMENTATION MODE" "C KI, 3/10/02" "C" "C *REMOVED SSFSPLT TERMS FROM CELLULOSE CALC, SINCE IN A NO SSF MODE," "C ONLY ONE STREAM IS GOING TO SACCHARIFICATION AND BLOCK SSFSPLT" "C DOESN'T EXIST." "C" "C CELL1 IS THE CELLULOSE FLOW RATE IN THE PRIMARY FEED TO SSCF." "C IT COULD BE DIRECTLY MEASURED, BUT THAT CAUSES SEVERE ERRORS FOR THE" "C FIRST FEW ITERATIONS, SO IT IS BEING CALCULATED." "C" "F CELL1=CLIN*(1-F1)" "C" "C *NO CELLULASE TO SEED NEEDED IN SEPARATE SACCH/FERM MODE." "C ENZYME LOADING ENZYL (FPU/G CELLULOSE IN PRIMARY FEED) TO SACCHARIFICATION" "C" "F ENZYL=0.00001" "C" "C *NO CELLULASE TO SEED NEEDED IN SEPARATE SACCH/FERM MODE." "C CELLULASE DEMAND BY SACCHARIFICATION" "C" "F EZDMD = CELL1 * ENZYL" "C" "C *NO CELLULASE TO SEED NEEDED IN SEPARATE SACCH/FERM MODE." "C CELLULASE DEMAND BY SSCF SEED" "C" "F EZDMDS = 0.0" "C" "C SUBSTRATE NEEDED BY CELLULASE REACTOR TO PRODUCE CELLULASE" "C" "F SUBDMD = (EZDMD + EZDMDS) / CLYLD" "C" "C TOTAL SUBSTRATE IS THE SUM OF CELLULASE RXT DEMAND + SEED" "C" "F TOTDMD = SUBDMD / (1-CSDSPT)" "C + ( CSDC + CSDX)" "C" "C SPLIT OF HYDROLYZATE TO CELLULASE REACTORS," "C CLIN + XIN TOTAL AMOUNT OF SUBSTRATE LEAVING PREHYDROLYSIS" "C" "F F1 = TOTDMD / ( CLIN + XIN )" "C" "C *LEAVE SPLIT BLOCK IN, BUT 421 WILL BE ZERO" "C SPLIT OF CELLULASE BROTH TO SSCF SEED AND PRODUCTION REACTORS" "C" "F CLSSPT = EZDMDS / (EZDMD + EZDMDS)" "C" "F WRITE(NHSTRY,101)CELL1,CELL1T,CELLS1,CELS1T,F1,CSDSPT,CLIN," "F 1 XIN,ENZYL" "F 101 FORMAT(' ENZYME FORTRAN BLOCK RESULTS',/," "F 1 ' FLOWS',/," "F 2 ' CELL1 ',G12.5,/," "F 3 ' CELL1T ',G12.5,/," "F 3 ' CELLS1 ',G12.5,/," "F 4 ' CELS1T ',G12.5,/," "F 4 ' F1 ',G12.5,/," "F 5 ' CSDSPT ',G12.5,/," "F 1 ' CLIN ',G12.5,/," "F 3 ' XIN ',G12.5,/," "F 5 ' ENZYL ',G12.5)" "F WRITE(NHSTRY,102)ENZYLS,CLYLD,EZDMD,EZDMDS,SUBDMD,TOTDMD,CLSSPT" "F 102 FORMAT(' ENZYME FORTRAN BLOCK RESULTS',/," "F 1 ' FLOWS',/," "F 2 ' ENZYLS ',G12.5,/," "F 3 ' ENY ',G12.5,/," "F 4 ' EZDMD ',G12.5,/," "F 5 ' EZDMDS ',G12.5,/," "F 1 ' SUBDMD ',G12.5,/," "F 3 ' TOTDMD ',G12.5,/," "F 5 ' CLSSPT ',G12.5)" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = BTMSSPLT \ \ COMMENTS COMMENTS = ( ";;" ";;" ";FORTRAN ENZ2S" "; Removed whole block, because seed hydrolysis is not used in sep sacch/ferm" "; KI, 3/10/02" "; DEFINE CL303C MASS-FLOW STREAM=303C SUBSTREAM=CISOLID &" "; COMPONENT=CELLULOS" "; DEFINE XM316 STREAM-VAR STREAM=316 SUBSTREAM=MIXED &" "; VARIABLE=MASS-FLOW" "; DEFINE CI316 STREAM-VAR STREAM=316 SUBSTREAM=CISOLID &" "; VARIABLE=MASS-FLOW" ";;" ";C ELOAD IS ENZYME LOADING (FPU / G CELLULOSE)" ";F ELOADS = 15.0" ";C ECONC IS ENZYME CONCENTRATION (50 FPU/ML IS APPROX CURRENT IOGEN CONC" ";F ECONCS = 50.0" ";C ERAT IS ENZYME RATIO (SOLID ENZYME TO WATER)" ";F ERATS = CI316 / (CI316 + XM316)" ";C EREQ IS ENZYME REQUIRED (FPU / HR)" ";F EREQS = ELOADS * 1000 * (CL303C)" ";C DENS IS THE ASSUMED DENSITY OF THE ENZYME (1.000 USED BECAUSE WE ARE ON" ";C MODELING ENZYME PROTEIN AND WATER; NO CELL MASS OR PRESERVATIVE) (G/ML)" ";F DENS = 1.0" ";C EREQM IS THE ENZYME REQUIRED (KG / HR)" ";F EREQMS = EREQS / ECONCS * DENS / 1000" ";F CI316 = ERATS * EREQMS" ";F XM316 = (1-ERATS) * EREQMS" "; READ-VARS CL303C" "; WRITE-VARS XM316 CI316" ";;" ";-------------------------------------------------------" "; CELLULASE FORTRAN BLOCKS - AREA 400" ";------------------------------------------------------" ";;" ";THIS BLOCK CALCULTES THE SPLIT IN BLOCK BTMSSPLT SO THAT" ";SSCF GETS THE CORRECT ENZYME LOADING." ";;" ";DEFINE ALL VARIABLES" "; CELL1T & CELS1T are sampled only to be printed to verify calculation" "; & convergence accuracy" ";;" ";;" ";FORTRAN STATEMENTS" ";c CELLS1 is the cellulose flow rate in the primary feed to SSCF seed." ";c It could be directly measured, but that causes severe errors for the" ";c first few iterations, so it is being calculated." ";c" ";F CELLS1=CLIN*(1-F1)*SSFSPT" ";c" ";c Enzyme loading ENZYLS (FPU/g Cellulose in primary feed) to SSCF seed" ";c" ";F ENZYLS=0.0000001" ";c" ";CELLS1 * ENZYLS" ";;" "; READ-VARS CELL1T CELS1T CSDSPT CLIN XIN CLYLD" "; WRITE-VARS F1 CLSSPT" ) \ ? CALCULATOR FEEDPROP ? ; "SET1_MOLE" ; \ DEFINE FVN = HCSOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 7 \ \ DEFINE FVN = HCPRO FVN-VARTYPE = PARAMETER FVN-PARAMNO = 8 \ \ DEFINE FVN = HCEXT FVN-VARTYPE = PARAMETER FVN-PARAMNO = 9 \ \ DEFINE FVN = CMBSOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 10 \ \ DEFINE FVN = CMBEXT FVN-VARTYPE = PARAMETER FVN-PARAMNO = 11 \ \ DEFINE FVN = CMBPRO FVN-VARTYPE = PARAMETER FVN-PARAMNO = 12 \ \ DEFINE FVN = CEXTR FVN-VARTYPE = PARAMETER FVN-PARAMNO = 13 \ \ DEFINE FVN = CPRO FVN-VARTYPE = PARAMETER FVN-PARAMNO = 14 \ \ DEFINE FVN = CSOLS FVN-VARTYPE = PARAMETER FVN-PARAMNO = 15 \ \ DEFINE FVN = WMLIG FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = LIGNIN FVN-ID2 = 1 \ \ DEFINE FVN = CLIG FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = LIGNIN FVN-ID2 = 1 FVN-ELEM = 1 \ \ DEFINE FVN = HLIG FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = LIGNIN FVN-ID2 = 1 FVN-ELEM = 2 \ \ DEFINE FVN = OLIG FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = LIGNIN FVN-ID2 = 1 FVN-ELEM = 3 \ \ DEFINE FVN = ACEMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = ACETATE FVN-ID2 = 1 \ \ DEFINE FVN = ACEC FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = ACETATE FVN-ID2 = 1 FVN-ELEM = 1 \ \ DEFINE FVN = ACEH FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = ACETATE FVN-ID2 = 1 FVN-ELEM = 2 \ \ DEFINE FVN = ACEO FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = ACETATE FVN-ID2 = 1 FVN-ELEM = 3 \ \ DEFINE FVN = CELLMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = CELLULOS FVN-ID2 = 1 \ \ DEFINE FVN = CELLC FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = CELLULOS FVN-ID2 = 1 FVN-ELEM = 1 \ \ DEFINE FVN = CELLH FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = CELLULOS FVN-ID2 = 1 FVN-ELEM = 2 \ \ DEFINE FVN = CELLO FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = CELLULOS FVN-ID2 = 1 FVN-ELEM = 3 \ \ DEFINE FVN = XYLMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = XYLAN FVN-ID2 = 1 \ \ DEFINE FVN = XYLC FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = XYLAN FVN-ID2 = 1 FVN-ELEM = 1 \ \ DEFINE FVN = XYLH FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = XYLAN FVN-ID2 = 1 FVN-ELEM = 2 \ \ DEFINE FVN = XYLO FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = XYLAN FVN-ID2 = 1 FVN-ELEM = 3 \ \ DEFINE FVN = BIOMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = BIOMASS FVN-ID2 = 1 \ \ DEFINE FVN = HFH2O FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = DHFORM FVN-ID1 = H2O FVN-ID2 = 1 \ \ DEFINE FVN = HFCO2 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = DHFORM FVN-ID1 = CO2 FVN-ID2 = 1 \ \ DEFINE FVN = HFNO2 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = DHFORM FVN-ID1 = NO2 FVN-ID2 = 1 \ \ DEFINE FVN = HFSO2 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = DHFORM FVN-ID1 = SO2 FVN-ID2 = 1 \ \ DEFINE FVN = HFN2 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = DHFORM FVN-ID1 = N2 FVN-ID2 = 1 \ \ DEFINE FVN = HFO2 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = DHFORM FVN-ID1 = O2 FVN-ID2 = 1 \ \ DEFINE FVN = HFSS FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = DHFORM FVN-ID1 = SOLSLDS FVN-ID2 = 1 \ \ DEFINE FVN = HFEXT FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = DHFORM FVN-ID1 = EXTRACT FVN-ID2 = 1 \ \ DEFINE FVN = HFPRO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = DHFORM FVN-ID1 = PROTEIN FVN-ID2 = 1 \ \ DEFINE FVN = SOLMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = SOLSLDS FVN-ID2 = 1 \ \ DEFINE FVN = EXTMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = EXTRACT FVN-ID2 = 1 \ \ DEFINE FVN = PROMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = PROTEIN FVN-ID2 = 1 \ \ DEFINE FVN = SSC FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = SOLSLDS FVN-ID2 = 1 FVN-ELEM = 1 \ \ DEFINE FVN = SSH FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = SOLSLDS FVN-ID2 = 1 FVN-ELEM = 2 \ \ DEFINE FVN = SSO FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = SOLSLDS FVN-ID2 = 1 FVN-ELEM = 3 \ \ DEFINE FVN = SSN FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = SOLSLDS FVN-ID2 = 1 FVN-ELEM = 4 \ \ DEFINE FVN = SSS FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = SOLSLDS FVN-ID2 = 1 FVN-ELEM = 5 \ \ DEFINE FVN = EXTC FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = EXTRACT FVN-ID2 = 1 FVN-ELEM = 1 \ \ DEFINE FVN = EXTH FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = EXTRACT FVN-ID2 = 1 FVN-ELEM = 2 \ \ DEFINE FVN = EXTO FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = EXTRACT FVN-ID2 = 1 FVN-ELEM = 3 \ \ DEFINE FVN = EXTN FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = EXTRACT FVN-ID2 = 1 FVN-ELEM = 4 \ \ DEFINE FVN = EXTS FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = EXTRACT FVN-ID2 = 1 FVN-ELEM = 5 \ \ DEFINE FVN = PROC FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = PROTEIN FVN-ID2 = 1 FVN-ELEM = 1 \ \ DEFINE FVN = PROH FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = PROTEIN FVN-ID2 = 1 FVN-ELEM = 2 \ \ DEFINE FVN = PROO FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = PROTEIN FVN-ID2 = 1 FVN-ELEM = 3 \ \ DEFINE FVN = PRON FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = PROTEIN FVN-ID2 = 1 FVN-ELEM = 4 \ \ DEFINE FVN = PROS FVN-VARTYPE = "UNARY-COR-EL" FVN-VARIABLE = NOATOM FVN-ID1 = PROTEIN FVN-ID2 = 1 FVN-ELEM = 5 \ \ DEFINE FVN = SSH2O FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 27 FVN-ID2 = H2O FVN-ID3 = MIXED \ \ DEFINE FVN = EXTH2O FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 36 FVN-ID2 = H2O FVN-ID3 = MIXED \ \ DEFINE FVN = PROH2O FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 37 FVN-ID2 = H2O FVN-ID3 = MIXED \ \ DEFINE FVN = SSCO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 27 FVN-ID2 = CO2 FVN-ID3 = MIXED \ \ DEFINE FVN = EXTCO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 36 FVN-ID2 = CO2 FVN-ID3 = MIXED \ \ DEFINE FVN = PROCO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 37 FVN-ID2 = CO2 FVN-ID3 = MIXED \ \ DEFINE FVN = SSN2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 27 FVN-ID2 = N2 FVN-ID3 = MIXED \ \ DEFINE FVN = EXTN2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 36 FVN-ID2 = N2 FVN-ID3 = MIXED \ \ DEFINE FVN = PRON2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 37 FVN-ID2 = N2 FVN-ID3 = MIXED \ \ DEFINE FVN = SSSO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 27 FVN-ID2 = SO2 FVN-ID3 = MIXED \ \ DEFINE FVN = EXTSO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 36 FVN-ID2 = SO2 FVN-ID3 = MIXED \ \ DEFINE FVN = PROSO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 37 FVN-ID2 = SO2 FVN-ID3 = MIXED \ \ DEFINE FVN = SSO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 27 FVN-ID2 = O2 FVN-ID3 = MIXED \ \ DEFINE FVN = EXTO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 36 FVN-ID2 = O2 FVN-ID3 = MIXED \ \ DEFINE FVN = PROO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 37 FVN-ID2 = O2 FVN-ID3 = MIXED \ \ DEFINE FVN = TSSO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 19 FVN-ID2 = O2 FVN-ID3 = MIXED \ \ DEFINE FVN = TEXTO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 47 FVN-ID2 = O2 FVN-ID3 = MIXED \ \ DEFINE FVN = TPROO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 48 FVN-ID2 = O2 FVN-ID3 = MIXED \ \ DEFINE FVN = TSSH2O FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 19 FVN-ID2 = H2O FVN-ID3 = MIXED \ \ DEFINE FVN = TEXH2O FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 47 FVN-ID2 = H2O FVN-ID3 = MIXED \ \ DEFINE FVN = TPRH2O FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 48 FVN-ID2 = H2O FVN-ID3 = MIXED \ \ DEFINE FVN = TSSCO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 19 FVN-ID2 = CO2 FVN-ID3 = MIXED \ \ DEFINE FVN = TEXCO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 47 FVN-ID2 = CO2 FVN-ID3 = MIXED \ \ DEFINE FVN = TPRCO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 48 FVN-ID2 = CO2 FVN-ID3 = MIXED \ \ DEFINE FVN = TSSNO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 19 FVN-ID2 = NO2 FVN-ID3 = MIXED \ \ DEFINE FVN = TEXNO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 47 FVN-ID2 = NO2 FVN-ID3 = MIXED \ \ DEFINE FVN = TPRNO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 48 FVN-ID2 = NO2 FVN-ID3 = MIXED \ \ DEFINE FVN = TSSSO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 19 FVN-ID2 = SO2 FVN-ID3 = MIXED \ \ DEFINE FVN = TEXSO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 47 FVN-ID2 = SO2 FVN-ID3 = MIXED \ \ DEFINE FVN = TPRSO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 48 FVN-ID2 = SO2 FVN-ID3 = MIXED \ \ DEFINE FVN = BIOSS FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 31 FVN-ID2 = BIOMASS FVN-ID3 = CISOLID \ \ DEFINE FVN = BIOEXT FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 49 FVN-ID2 = BIOMASS FVN-ID3 = CISOLID \ \ DEFINE FVN = BIOPRO FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T608 FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 50 FVN-ID2 = BIOMASS FVN-ID3 = CISOLID \ \ DEFINE FVN = WMO2 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = O2 FVN-ID2 = 1 \ \ DEFINE FVN = WMCO2 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = CO2 FVN-ID2 = 1 \ \ DEFINE FVN = WMH2O FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = H2O FVN-ID2 = 1 \ \ DEFINE FVN = WMN2 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = N2 FVN-ID2 = 1 \ \ DEFINE FVN = WMSO2 FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = SO2 FVN-ID2 = 1 \ \ DEFINE FVN = EXTFLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = CELLF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XYLF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = GALF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = ARBF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = ARABINAN \ \ DEFINE FVN = FMAN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = FLIG FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = LIGNIN \ \ DEFINE FVN = ASHF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = ASH \ \ DEFINE FVN = ACETF FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = ACETATE \ \ DEFINE FVN = PROFLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = SSFLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = H2OFLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = CIFLO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "F DFEXT = 0.0468" "F DFCELL = 0.374" "F DFXYL = 0.2107" "F DFGAL = 0.0194" "F DFARAB = 0.0292" "F DFMAN = 0.0156" "F DFLIG = 0.1799" "F DFASH = 0.0523" "F DFACE = 0.0293" "F DFPRO = 0.031" "F DFSS = 0.0112" "F WET = 0.15" "F RATE = 2000.0" "F CFRAC = 0.4452" "F HFRAC = 0.0574" "F OFRAC = 0.4242" "F FRACN = 0.0046" "F SFRAC = 0.00008" "F AFRAC = 0.0686" "F HHVFS = 7503.0" "F HHVL = 10980.1" "F HHVA = 6458.0" "F HHVC = 7459.1" "F HHVX = 7640.4" "F HVAP = 43870063." "F WRITE (NHSTRY,*) 'LIGNIN ATOMIC NUMBERS AND MW:'" "F WRITE (NHSTRY,*) 'C,H,O,MW LIGNIN:',CLIG, HLIG, OLIG, WMLIG" "F WRITE (NHSTRY,*) 'ACETATE ATOMIC NUMBERS AND MW:'" "F WRITE (NHSTRY,*) 'C,H,O,MW ACETATE:',ACEC, ACEH, ACEO, ACEMW" "F WRITE (NHSTRY,*) 'CELLULOSE ATOMIC NUMBERS AND MW:'" "F WRITE (NHSTRY,*) 'C,H,O,MW CELLULOSE:',CELLC, CELLH, CELLO, CELLMW" "F WRITE (NHSTRY,*) 'XYLAN ATOMIC NUMBERS AND MW:'" "F WRITE (NHSTRY,*) 'C,H,O,MW XYLAN:',XYLC, XYLH, XYLO, XYLMW" "F WRITE (NHSTRY,*) 'BIOMASS MW:'" "F WRITE (NHSTRY,*) 'MW BIOMASS:',BIOMW" "F WRITE (NHSTRY,*) ' '" "F OMW = WMO2 / 2." "F CMW = WMCO2 - WMO2" "F HMW = (WMH2O - OMW) / 2" "F WMN = WMN2 / 2." "F SMW = WMSO2 - WMO2" "F WRITE(NHSTRY,*)'ATOMIC WEIGHTS:'" "F WRITE(NHSTRY,*)' CMW: CARBON= ',CMW" "F WRITE(NHSTRY,*)' HMW: HYDROGEN= ',HMW" "F WRITE(NHSTRY,*)' OMW: OXYGEN= ',OMW" "F WRITE(NHSTRY,*)' WMN: NITROGEN= ',WMN" "F WRITE(NHSTRY,*)' SMW: SULFUR= ',SMW" "F WRITE(NHSTRY,*)' '" "F WRITE (NHSTRY,*) 'COMBUSTION PRODUCTS DHFORM (J/KMOL):'" "F WRITE (NHSTRY,*) ' HFH2O=',HFH2O" "F WRITE (NHSTRY,*) ' HFCO2=',HFCO2" "F WRITE (NHSTRY,*) ' HFNO2=',HFNO2" "F WRITE (NHSTRY,*) ' HFSO2=',HFSO2" "F WRITE (NHSTRY,*) ' HFN2=',HFN2" "F WRITE (NHSTRY,*) ' '" "F C6 = DFGAL + DFMAN + DFCELL" "F C5 = DFXYL + DFARAB" "F SOLS = DFPRO + DFSS + DFEXT" "F AFHHV = HHVFS/(1-AFRAC)" "F WRITE (NHSTRY,*) 'AFHHV: ASH FREE HHV (BTU/LB)',AFHHV" "F WRITE (NHSTRY,*) ' '" "F AFEC = (CFRAC/CMW)/(1-AFRAC)" "F AFEH = (HFRAC/HMW)/(1-AFRAC)" "F AFEO = (OFRAC/OMW)/(1-AFRAC)" "F AFEN = (FRACN/WMN)/(1-AFRAC)" "F AFES = (SFRAC/SMW)/(1-AFRAC)" "F WRITE(NHSTRY,*)'ULTIMATE ANAL ASH FREE BASIS:'" "F WRITE(NHSTRY,*)' AFEC: MOLES ASH FREE CARBON= ',AFEC" "F WRITE(NHSTRY,*)' AFEH: MOLES ASH FREE HYDROGEN= ',AFEH" "F WRITE(NHSTRY,*)' AFEO: MOLES ASH FREE OXYGEN= ',AFEO" "F WRITE(NHSTRY,*)' AFEN: MOLES ASH FREE NITROGEN= ',AFEN" "F WRITE(NHSTRY,*)' AFES: MOLES ASH FREE SULFUR= ',AFES" "F WRITE(NHSTRY,*)' '" "F WAFC = C6/(1-DFASH)" "F WAFX = C5/(1-DFASH)" "F WAFL = DFLIG/(1-DFASH)" "F WAFA = DFACE/(1-DFASH)" "F WAFS = SOLS/(1-DFASH)" "F AFCC = WAFC/CELLMW" "F AFCX = WAFX/XYLMW" "F AFCL = WAFL/WMLIG" "F AFCA = WAFA/ACEMW" "F EAFC = AFEC - AFCC*CELLC-AFCX*XYLC-AFCL*CLIG-AFCA*ACEC" "F EAFH = AFEH - AFCC*CELLH-AFCX*XYLH-AFCL*HLIG-AFCA*ACEH" "F EAFO = AFEO - AFCC*CELLO-AFCX*XYLO-AFCL*OLIG-AFCA*ACEO" "F EAFN = AFEN" "F EAFS = AFES" "F WRITE(NHSTRY,*)'MOLES OF ELEMENTS FOR SOLUBLE SOLIDS:'" "F WRITE(NHSTRY,*)' EAFC: CARBON= ',EAFC" "F WRITE(NHSTRY,*)' EAFH: HYDROGEN= ',EAFH" "F WRITE(NHSTRY,*)' EAFO: OXYGEN= ',EAFO" "F WRITE(NHSTRY,*)' EAFN: NITROGEN= ',EAFN" "F WRITE(NHSTRY,*)' EAFS: SULFUR= ',EAFS" "F WRITE(NHSTRY,*)' '" "F SSC = EAFC/EAFC" "F SSH = EAFH/EAFC" "F SSO = EAFO/EAFC" "F SSN = EAFN/EAFC" "F SSS = EAFS/EAFC" "F WRITE (NHSTRY,*) 'NUMBER OF ATOMS IN SOLUBLE SOLIDS:'" "F WRITE(NHSTRY,*)' SSC: CARBON= ',SSC" "F WRITE(NHSTRY,*)' SSH: HYDROGEN= ',SSH" "F WRITE(NHSTRY,*)' SSO: OXYGEN= ',SSO" "F WRITE(NHSTRY,*)' SSN: NITROGEN= ',SSN" "F WRITE(NHSTRY,*)' SSS: SULFUR= ',SSS" "F WRITE(NHSTRY,*)' '" "F EXTC = SSC" "F PROC = SSC" "F EXTH = SSH" "F PROH = SSH" "F EXTO = SSO" "F PROO = SSO" "F EXTN = SSN" "F PRON = SSN" "F EXTS = SSS" "F PROS = SSS" "F SOLMW = SSC*CMW + SSH*HMW + SSO*OMW + SSN*WMN + SSS*SMW" "F EXTMW = SOLMW" "F PROMW = SOLMW" "F WRITE (NHSTRY,*) 'MOLECULAR WEIGHTS:'" "F WRITE(NHSTRY,*)' SOLMW: SOLUBLE SOLIDS= ',SOLMW" "F WRITE(NHSTRY,*)' PROMW: PROTEIN= ',PROMW" "F WRITE(NHSTRY,*)' EXTMW: EXTRACTIVES= ',EXTMW" "F WRITE(NHSTRY,*)' '" "F SSH2O = SSH/2.0" "F EXTH2O = SSH2O" "F PROH2O = SSH2O" "F SSCO2 = SSC" "F EXTCO2 = SSCO2" "F PROCO2 = SSCO2" "F SSN2 = SSN/2.0" "F EXTN2 = SSN2" "F PRON2 = SSN2" "F SSSO2 = SSS" "F EXTSO2 = SSS" "F PROSO2 = SSS" "F SSO2 = (SSO - SSH2O - SSCO2*2.0 - SSSO2*2.0)/2.0" "F EXTO2 = SSO2" "F PROO2 = SSO2" "F WRITE (NHSTRY,*) 'SOLSLDS COMBUSTION STOICHIOMETRY - M803CMB'" "F WRITE (NHSTRY,*) ' SSO2: OXYGEN= ', SSO2" "F WRITE (NHSTRY,*) ' SSCO2: CARBON DIOXIDE= ', SSCO2" "F WRITE (NHSTRY,*) ' SSH2O: WATER= ', SSH2O" "F WRITE (NHSTRY,*) ' SSN2: NITROGEN= ', SSN2" "F WRITE (NHSTRY,*) ' SSSO2: SULFUR DIOXIDE= ', SSSO2" "F WRITE(NHSTRY,*)' '" "F HCSOL=AFHHV-(C6*HHVC+C5*HHVX+DFLIG*HHVL+DFACE*HHVA)/(1-DFASH)" "F HCSOL = HCSOL/(SOLS/(1-DFASH))*2.20462" "F HCPRO = HCSOL" "F HCEXT = HCSOL" "F WRITE(NHSTRY,*)'HIGHER HEATING VALUE '" "F WRITE(NHSTRY,*)' HCSOL: SOLUBLE SOLIDS= ',HCSOL" "F TSSH2O = SSH/2.0" "F TEXH2O = TSSH2O" "F TPRH2O = TSSH2O" "F TSSCO2 = SSC" "F TEXCO2 = TSSCO2" "F TPRCO2 = TSSCO2" "F TSSNO2 = SSN" "F TEXNO2 = TSSNO2" "F TPRNO2 = TSSNO2" "F TSSSO2 = SSS" "F TEXSO2 = TSSSO2" "F TPRSO2 = TSSSO2" "F TSSO2 = (SSO-SSC*2.0-SSH/2.0-SSN*2.0-SSS*2.0)/2.0" "F TEXTO2 = TSSO2" "F TPROO2 = TSSO2" "F WRITE (NHSTRY,*) 'SOLSLDS AEROBIC DIGESTION STOICHIOMETRY--T608'" "F WRITE (NHSTRY,*) ' TSSO2: OXYGEN= ', TSSO2" "F WRITE (NHSTRY,*) ' TSSCO2: CARBON DIOXIDE= ', TSSCO2" "F WRITE (NHSTRY,*) ' TSSH2O: WATER= ', TSSH2O" "F WRITE (NHSTRY,*) ' TSSNO2: NITROGEN DIOXIDE= ', TSSNO2" "F WRITE (NHSTRY,*) ' TSSSO2: SULFUR DIOXIDE= ', TSSSO2" "F BIOSS = SOLMW/BIOMW" "F BIOEXT = BIOSS" "F BIOPRO = BIOSS" "F WRITE (NHSTRY,*) ' BIOSS: BIOMASS RXNS 31, 49, 50= ', BIOSS" "F WRITE(NHSTRY,*)' '" "F HFSS=-(-HCSOL*SOLMW*1055.1)" "F HFSS=HFSS-(-(HFCO2*SSCO2+HFH2O*SSH2O+HFN2*SSN2+HFSO2*SSSO2))" "F HFEXT = HFSS" "F HFPRO = HFSS" "F WRITE (NHSTRY,*) 'SOLSLDS HEAT OF FORMATION'" "F WRITE(NHSTRY,*)' HFSS: LIQUID WATER DHFORM (J/KMOL)= ',HFSS" "F HFV = HFSS - SSH2O*HVAP" "F WRITE(NHSTRY,*)' HFV: VAPOR WATER (J/KMOL)= ',HFV" "F CMBSOL = (HFCO2*SSCO2+HFH2O*SSH2O+HFSO2*SSSO2+HFN2*SSN2)-HFV" "F CMBEXT = CMBSOL" "F CMBPRO = CMBSOL" "F WRITE (NHSTRY,*) 'SOLSLDS LOWER HEATING VALUE'" "F WRITE(NHSTRY,*)' CMBSOL (J/KMOL)= ',CMBSOL" "F WRITE(NHSTRY,*)' '" "F IF (TSSO2.LT.0) THEN" "F CEXTR = -(TSSO2*OMW*2.0)/SOLMW" "F ELSE" "F CEXTR=0.0" "F END IF" "C" "F CPRO = CEXTR" "F CSOLS = CEXTR" "F WRITE(NHSTRY,*)'COD FOR AEROBIC DIGESTION'" "F WRITE(NHSTRY,*)'CSOLS: SOLUBLE SOLIDS (G/G)= ',CSOLS" "F WRITE(NHSTRY,*)' '" "F H2OFLO = RATE * (1000.0/24.0) * (WET/(1-WET))" "F SSFLO = RATE * (1000.0/24.0) * DFSS" "F EXTFLO = RATE * (1000.0/24.0) * DFEXT" "F PROFLO = RATE * (1000.0/24.0) * DFPRO" "F WRITE(NHSTRY,*)'STREAM 101 CALCULATIONS'" "F WRITE(NHSTRY,*)'H2OFLO: WATER FLOW (KG/HR)= ', H2OFLO" "F WRITE(NHSTRY,*)'SSFLO: SOLUBLE SOLIDS FLOW (KG/HR)= ', SSFLO" "F WRITE(NHSTRY,*)'EXTFLO: EXTRACTIVES FLOW (KG/HR) =', EXTFLO" "F WRITE(NHSTRY,*)'PROFLO: PROTEIN FLOW (KG/HR) =', PROFLO" "F WRITE(NHSTRY,*)' '" "F CIFLO = RATE*(1000.0/24.0) - (SSFLO+EXTFLO+PROFLO)" "F WRITE(NHSTRY,*)'CIFLO: CISOLIDS FLOW (KG/HR) =', CIFLO" "F TOT = DFCELL+DFXYL+DFGAL+DFARAB+DFMAN+DFLIG+DFASH+DFACE" "F CELLF = (DFCELL / TOT) * CIFLO" "F WRITE(NHSTRY,*)'CELLF: CELLULOSE FLOW (KG/HR)= ',CELLF" "F XYLF = (DFXYL / TOT) * CIFLO" "F WRITE(NHSTRY,*)'XYLF: XYLAN FLOW (KG/HR)= ',XYLF" "F ARBF = (DFARAB / TOT) * CIFLO" "F WRITE(NHSTRY,*)'ARBF: ARABINAN FLOW (KG/HR)= ',ARBF" "F FMAN = (DFMAN / TOT) * CIFLO" "F WRITE(NHSTRY,*)'FMAN: MANNAN FLOW (KG/HR)= ',FMAN" "F GALF = (DFGAL / TOT) * CIFLO" "F WRITE(NHSTRY,*)'GALF: GALACTAN FLOW (KG/HR)= ',GALF" "F FLIG = (DFLIG / TOT) * CIFLO" "F WRITE(NHSTRY,*)'FLIG: LIGNIN FLOW (KG/HR)= ',FLIG" "F ACETF = (DFACE / TOT) * CIFLO" "F WRITE(NHSTRY,*)'ACETF: ACETATE FLOW (KG/HR)= ',ACETF" "F ASHF = (DFASH / TOT) * CIFLO" "F WRITE(NHSTRY,*)'ASHF: ASH FLOW (KG/HR)= ',ASHF" "F WRITE(NHSTRY,*)' '" ) \ \ "READ-VARS" READ-VAR = ( WMLIG CLIG HLIG OLIG ACEMW ACEC ACEH ACEO CELLMW CELLC CELLH CELLO XYLMW XYLC XYLH XYLO BIOMW HFH2O HFCO2 HFNO2 HFSO2 ) \ \ "WRITE-VARS" WRITE-VAR = ( HCSOL HCPRO HCEXT CMBSOL CMBEXT CMBPRO CEXTR CPRO CSOLS HFSS HFEXT HFPRO SOLMW EXTMW PROMW SSC EXTC PROC SSH2O EXTH2O PROH2O SSCO2 SSN2 SSSO2 SSO2 TSSO2 TSSH2O TSSCO2 TSSNO2 TSSSO2 BIOSS EXTFLO CELLF XYLF GALF ARBF FMAN FLIG ASHF ACETF PROFLO SSFLO H2OFLO CIFLO ) \ \ COMMENTS COMMENTS = ( ";;" ";----------------------------------------------------" "; FEED HANDLING FORTRAN BLOCKS - AREA 100" ";----------------------------------------------------" ";;" ";;" ";THIS BLOCK CALCULATES:" "; 1. Feed stream (101) component flow rates given the plant feedrate," "; mass fractions (dry basis) and feed moisture." ";NOTE: DHFORM IS NOT BEING WRITTEN OUT OF THIS BLOCK YET. YOU MUST CHANGE" "; IT BY HAND (USING THE PRINT STMTS FOR THIS BLOCK IN THE HISTORY FILE)" "; IN THE PROP-DATA STMTS ABOVE IF YOU CHANGE THE FEED COMPOSITION." "; KNI 1/15/03" "; 2. DHFORM, NOATOM and MW of SOLSLDS, EXTRACT, PROTEIN components given" "; the feedstock ultimate analysis, Higher heating value, composition." "; 3. Reaction coeffs. for SOLSLDS, EXTRACT, PROTEIN for T608 and M803CMB" "; 4. Parameters for fortran blocks COMBHEAT, COMBHET2, CODCALC1," "; CODCALC2, CODEND." ";----------------------------------------------------------------" ";Parameters calculated and passed to other fortran blocks" "; Higher heating value parameters for SOLSLDS, EXTRACT and PROTEIN" "; These values are passed to COMBHEAT" "; Lower heating value parameters for SOLSLDS, EXTRACT and PROTEIN" "; These values are passed to COMBHET2" "; COD values in (kg O2/kg component)" "; These values are passed to CODCALC1, CODCALC2, AND CODEND" ";----------------------------------------------------------------" "; Read Variables used to calculate solslds DHFORM, NOATOMS" "; MW and Formula Coefficients of Lignin" "; MW and Formula Coefficients of Acetate" "; MW and Formula Coefficients of Cellulose" "; MW and Formula Coefficients of Xylan" "; MW of Biomass" "; DHFORM for combustion products H2O, CO2, NO2, SO2" ";----------------------------------------------------------------" "; Write Variables" "; Heat of Formation for SOLSLDS, EXTRACT and PROTEIN" "; Molecular weight of SOLSLDS, EXTRACT and PROTEIN" "; Number of Atoms of SOLSLDS, EXTRACT and PROTEIN" "; Might not be necessary, since MW is written, but not sure (KI)" "; Coefficient for water in block M803CMB for sol solids" "; Coefficient for CO2 in block M803CMb for sol solids" "; Coefficient for N2 in block M803CMB for sol solids" "; Coefficient for SO2 in block M803CMB for sol solids" "; Coefficients for O2 in block M803CMB for sol solids" "; Coefficients for O2 in block T608 for sol solids" "; Coefficients for H2O in block T608 for sol solids" "; Coefficients for CO2 in block T608 for sol solids" "; Coefficients for NO2 in block T608 for sol solids" "; Coefficients for SO2 in block T608 for sol solids" "; Coefficients for biomass in block T608 for sol solids" ";;" "; Internal variables - Values entered by the user:" "; DFEXT - Dry Mass Fraction of Extractives" "; DFCELL- Dry Mass Fraction of Cellulose" "; DFXYL - Dry Mass Fraction of Xylan" "; DFGAL - Dry Mass Fraction of Galactan" "; DFARAB- Dry Mass Fraction of Arabinan" "; DFMAN - Dry Mass Fraction of Mannan" "; DFLIG - Dry Mass Fraction of Lignin" "; DFASH - Dry Mass Fraction of Ash" "; DFACE - Dry Mass Fraction of Acetate" "; DFPRO - Dry Mass Fraction of Protein" "; DFSS - Dry Mass Fraction of Soluble Solids" "; WET - Percent Moisture in Feedstock" "; RATE - Plant feedrate" "; CFRAC - Carbon weight fraction" "; HFRAC - Hydrogen weight fraction" "; OFRAC - Oxygen weight fraction" "; FRACN - Nitrogen weight fraction" "; SFRAC - Sulfur weight fraction" "; AFRAC - Ash weight fraction" "; HHVFS - Higher heating value for the feedstock (BTU/LB)" "; HHVC - Higher heating value of cellulose" "; HHVX - Higher heating value of xylan" "; HHVL - Higher heating value of lignin" "; HHVA - Higher heating value of acetate" "; Element MWs checked against Aspen values:" "; CMW - Molecular weight of carbon" "; HMW - Molecular weight of hydrogen" "; OMW - Molecular weight of oxygen" "; NMW - Molecular weight of nitrogen" "; SMW - Molecular weight of sulfur" "; Read variables - brought in from in-house or Aspen phys props databases:" "; CLIG - Number of carbon atoms in lignin" "; HLIG - Number of hydrogen atoms in lignin" "; OLIG - Number of oxygen atoms in lignin" "; WMLIG - Molecular weight of lignin" "; ACEC - Number of carbon atoms in acetate" "; ACEH - Number of hydrogen atoms in acetate" "; ACEO - Number of oxygen atoms in acetate" "; ACEMW - Molecular weight of acetate" "; CELLC - Number of carbon atoms in cellulose" "; CELLH - Number of hydrogen atoms in cellulose" "; CELLO - Number of oxygen atoms in cellulose" "; CELLMW - Molecular weight of cellulose" "; XYLC - Number of carbon atoms in xylan" "; XYLH - Number of hydrogen atoms in xylan" "; XYLO - Number of oxygen atoms in xylan" "; XYLMW - Molecular weight of xylan" "; BIOMW - Molecular weight of biomass" "; HFCO2 - Heat of formation of CO2 (J/kmol)" "; HFH2O - Heat of formation of H2O (J/kmol)" "; HFSO2 - Heat of formation of SO2 (J/kmol)" "; HFNO2 - Heat of formation of NO2 (J/kmol)" "; Variables still to be read in if possible (hard-coded now):" "; HVAP - Water heat of vaporization (J/kmol) at 25C" "; Calculated variables:" "; C6 - Total dry weight fraction of all carbon six compounds" "; C5 - Total dry weight fraction of all carbon five compounds" "; SOLS - Total dry weight fraction of all soluble compounds" "; AFHHV - Ash free higher heating value for the feedstock" "; AFEC - Ash free carbon moles from the element analysis" "; AFEH - Ash free hydrogen moles from the element analysis" "; AFEO - Ash free oxygen moles from the element analysis" "; AFEN - Ash free nitrogen moles from the element analysis" "; AFES - Ash free sulfur moles from the element analysis" "; AFCC - Ash free cellulose moles from the component analysis" "; AFCX - Ash free xylan moles from the component analysis" "; AFCL - Ash free lignin moles from the component analysis" "; AFCA - Ash free acetate moles from the component analysis" "; AFCS - Ash free solubles moles from the component analysis" "; WAFC - Ash free weight fraction of C6 sugars" "; WAFX - Ash free weight fraction of C5 sugars" "; WAFL - Ash free weight fraction of lignin" "; WAFA - Ash free weight fraction of acetate" "; WAFS - Ash free weight fraction of soluble solids" "; SOLMW - Molecular weight of soluble solids" "; EAFC - Excess ash free carbon" "; EAFH - Excess ash free hydrogen" "; EAFO - Excess ash free oxygen" "; EAFN - Excess ash free nitrogen" "; EAFS - Excess ash free sulfur" "; HCSOL - Higher heating value for soluble solids" "; SSCO2 - CO2 combustion coefficient" "; SSH2O - H2O combustion coefficient" "; SSN2 - N2 combustion coefficient" "; SSSO2 - SO2 combustion coefficient" "; SSO2 - O2 combustion coefficient" "; HFV - Heat of formation for vapor water product" ";NOTE: DHFORM IS NOT BEING WRITTEN OUT OF THIS BLOCK YET DUE TO UNKNOWN ASPE" "; PROBLEMS WHEN TRYING IT. YOU MUST CHANGEIT BY HAND" "; (USING THE PRINT STATEMENTS FOR THIS BLOCK IN THE HISTORY FILE)" "; IN THE PROP-DATA STATEMETS ABOVE IF YOU CHANGE THE FEED COMPOSITION." "; KNI 1/15/03" ";Internal Variables - Feed comp. and other values entered by user" "; REMEMBER THE ABOVE NOTE REGARDING FEED COMPOSITION" ";Internal variables and constants that should not change" "; Water heat of vaporization at 25C" "; Atomic Weights calculated from sampled molecular weights" "; C6 - Total dry weight fraction of all carbon six compounds" "; C5 - Total dry weight fraction of all carbon five compounds" "; SOLS - Total dry weight fraction of all soluble compounds" "; Calculation of the soluble solids empirical formula" "; The calculation below is wrong but is not used anywhere" "; therefore I commented it out MR 4 Feb 03" ";F AFCS = 1-AFCC-AFCX-AFCL-AFCA" "; Calculation of" "; Reaction stoichiometry for block M803CMB" "; Calculates higher heating value for the soluble solids (btu/kg)" "; T608 stoichiometry calculations" "; Calculation of BIOMASS coefficients for T608 rxns 31, 49, 50" "; Heat of formation calculations for liquid water product (J/kmol)" "; Heat of formation calculations for vapor water product (J/kmol)" "; Calculates lower heating value for the soluble solids (J/kmol)" "; Calculation of COD values" "; If TSSO2 is positive, COD contribution from CEXTR, etc. should be 0." "; If TSSO2 is negative, COD contribution from CEXTR, etc. should be +." ";--------------------------------------------------------" "; Calculation of stream 101 component and substream flow rates:" "; Calculation of Mixed Substream Flowrates (kg/Hr)" "; Calculation of CISOLID Substream Flowrate (kg/Hr)" ";Calculation of CISOLID Substream Component Mass Fractions" "; Write the component flow rates to stream 101:" "; WRITE Variable - Mass Flow of Extractives" "; WRITE Variable - Mass Flow of Cellulose" "; WRITE Variable - Mass Flow of Xylan" "; WRITE Variable - Mass Flow of Galactan" "; WRITE Variable - Mass Flow of Arabinan" "; WRITE Variable - Mass Flow of Mannan" "; WRITE Variable - Mass Flow of Lignin" "; WRITE Variable - Mass Flow of Ash" "; WRITE Variable - Mass Flow of Acetate" "; WRITE Variable - Mass Flow of Protein" "; WRITE Variable - Mass Flow of Soluble Solids" "; WRITE Variable - Mass Flow of Water" "; WRITE Variable - Mass Flow of the CISOLID substream in kg/Hr" "; EXECUTE AFTER SETVAR" ) \ ? CALCULATOR FERMCSL ? ; "SET1_MOLE" ; \ DEFINE FVN = FL303A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 303A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FS303A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 303A FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FL304A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FS304A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304A FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FL310A FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 310A FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = FL311A FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 311A FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ FORTRAN FORTRAN-EXEC = ( "F CSLSD=0.005" "F CSLPRD=0.0025" "F FL310A=CSLSD*(FL303A+FS303A)" "F FL311A=CSLPRD*(FL304A+FS304A)" ) \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = BLOCK BLK-ID = T310 \ \ COMMENTS COMMENTS = ( ";;" ";----------------------------------------------------------------------" "; SSCF FORTRAN BLOCKS - AREA 300" ";----------------------------------------------------------------------" ";;" "; THIS FORTRAN BLOCK SETS THE CSL FLOWS TO SSCF PRODUCTION AND SEED" ";;" "; INPUTS" "; OUTPUTS" "; CSLSD IS THE CSL CONCENTRATION IN THE SEED FERMS (MASS/MASS)" "; CSLPRD IS THE CSL CONCENTRATION IN THE PRODUCTION FERMS (MASS/MASS)" ) \ ? CALCULATOR FERMDAP ? ; "SET1_MOLE" ; \ DEFINE FVN = FM303A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 303A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FC303A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 303A FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = DM303A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 303A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = DC303A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 303A FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FM304A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FC304A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304A FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = DM304A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = DC304A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304A FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FL310 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 310 FVN-SUBS = MIXED FVN-COMPONEN = DAP \ \ DEFINE FVN = FL311 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 311 FVN-SUBS = MIXED FVN-COMPONEN = DAP \ \ FORTRAN FORTRAN-EXEC = ( "F DAPSD=0.67" "F DAPPRD=0.33" "F VLFLW1 = (FM303A/DM303A + FC303A/DC303A)" "F VLFLW2 = (FM304A/DM304A + FC304A/DC304A)" "F FL310=(DAPSD/1000)*VLFLW1" "F FL311=(DAPPRD/1000)*VLFLW2" "F WRITE(NHSTRY,*)'FLOW OF 303A MIXED IS ',FM303A,' KG/HR'" "F WRITE(NHSTRY,*)'FLOW OF 303A CISOLID IS ',FC303A,' KG/HR'" "F WRITE(NHSTRY,*)'FLOW OF 304A MIXED IS ',FM304A,' KG/HR'" "F WRITE(NHSTRY,*)'FLOW OF 304A CISOLID IS ',FC304A,' KG/HR'" "F WRITE(NHSTRY,*)'DENSITY OF 303A MIXED IS ',DM303A,' G/CM3'" "F WRITE(NHSTRY,*)'DENSITY OF 303A CISOLID IS ',DC303A,' G/CM3'" "F WRITE(NHSTRY,*)'DENSITY OF 304A MIXED IS ',DM304A,' G/CM3'" "F WRITE(NHSTRY,*)'DENSITY OF 304A CISOLID IS ',DC304A,' G/CM3'" "F WRITE(NHSTRY,*)'VLFLW1 = ',VLFLW1,' L/HR'" "F WRITE(NHSTRY,*)'VLFLW2 = ',VLFLW2,' L/HR'" "F WRITE(NHSTRY,*)'FL310 = ',FL310,' KG/HR'" "F WRITE(NHSTRY,*)'FL311 = ',FL311,' KG/HR'" ) \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = CALCULATOR BLK-ID = FERMCSL \ \ COMMENTS COMMENTS = ( "; READ-VARS FL303A FS303A FL304A FS304A" "; WRITE-VARS FL310A FL311A" ";;" "; THIS FORTRAN BLOCK SETS THE DAP FLOWS TO SSCF PRODUCTION AND SEED" ";;" "; INPUTS" "; OUTPUTS" "; DAPSD IS THE DAP CONCENTRATION IN THE SEED FERMS (MASS/VOLUME)" "; DAPPRD IS THE DAP CONC. IN THE PRODUCTION FERMS (MASS/VOLUME)" "; DAP nutrient addition rate set at 0.33 g/L; AA 02/16/01" "; VOLFLW1 is the volumetric flow of 303A (L/hr)" "; VOLFLW2 is the volumetric flow of 304A (L/hr)" ";;" "; READ-VARS FM303A FC303A FM304A FC304A &" "; DM303A DC303A DM304A DC304A" "; WRITE-VARS FL310 FL311" ) \ ? CALCULATOR FRWD501 ? ; "ENG_MOLE" ; \ DEFINE FVN = D501D FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = D501 FVN-VARIABLE = "MASS-D" FVN-SENTENCE = "COL-SPECS" \ \ DEFINE FVN = FEEDC FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 506 FVN-SUBS = MIXED FVN-COMPONEN = CO2 \ \ DEFINE FVN = D501DL FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = D501 FVN-VARIABLE = LB FVN-SENTENCE = VARY FVN-ID1 = 2 \ \ DEFINE FVN = D501DH FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = D501 FVN-VARIABLE = UB FVN-SENTENCE = VARY FVN-ID1 = 2 \ \ DEFINE FVN = D501V FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = D501 FVN-VARIABLE = "MASS-FLOW" FVN-SENTENCE = PRODUCTS FVN-ID1 = 510 \ \ DEFINE FVN = FEEDE FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 506 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = D501VL FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = D501 FVN-VARIABLE = LB FVN-SENTENCE = VARY FVN-ID1 = 1 \ \ DEFINE FVN = D501VU FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = D501 FVN-VARIABLE = UB FVN-SENTENCE = VARY FVN-ID1 = 1 \ \ FORTRAN FORTRAN-EXEC = ( "C ASSUME 2/3 OF CO2 GOES OVERHEAD" "C OVERHEAD SPEC IS 0.8391 MASS FRACTION CO2" "F CO2SPC = 0.8391" "F WRITE(NTERM, 102) D501D, D501DL, D501DH, D501V, D501VL, D501VU" "F 102 FORMAT(' D501D ',G12.5,/," "F 1 ' D501DL ',G12.5,/," "F 2 ' D501DH ',G12.5,/," "F 3 ' D501V ',G12.5,/," "F 4 ' D501VL ',G12.5,/," "F 5 ' D501VU ',G12.5,/)" "C" "C SET INITIAL GUESSES FOR DISTILLATIE FLOW" "C" "F D501D = (FEEDC ) / CO2SPC" "C 7936.5 IS A UNITS CONVERSION" "F D501DL = 0.8 * D501D / 7936.5" "F D501DH = 1.2 * D501D / 7936.5" "F WRITE(NTERM, 101) D501D, D501DL, D501DH, FEEDC" "F 101 FORMAT(' D501D ',G12.5,/," "F 1 ' D501DL ',G12.5,/," "F 2 ' D501DH ',G12.5,/," "F 3 ' FEEDC ',G12.5,/)" "C" "C SET INITIAL GUESSES FOR VAPOR PRODUCT FLOW" "C" "C ASSUME ALL ETHANOL IS IN PRODUCT AND THAT" "C IT IS 42% BY WEIGHT" "C" "F ETHSPC = 0.42" "F D501V = FEEDE / ETHSPC" "F D501VL = D501V * 0.80 / 7936.5" "F D501VU = D501V * 1.40 / 7936.5" "F WRITE(NTERM,103) D501V, D501VL, D501VU, FEEDE" "F 103 FORMAT(' D501V ',G12.5,/," "F 1 ' D501VL ',G12.5,/," "F 2 ' D501VU ',G12.5,/," "F 3 ' FEEDE ',G12.5)" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = D501 \ \ COMMENTS COMMENTS = ( ";;" ";--------------------------------------------------------" "; DISTILLATION FORTRAN BLOCKS - AREA 5000" ";-------------------------------------------------------" ";;" "; Feed forward control for 501 column. Estimates the distillate" "; flow and specification bounds for 501" ";;" ) \ ? CALCULATOR HPSTMD ? ; "SET1_MOLE" ; \ DEFINE FVN = STMHP FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M811HSPT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 814 \ \ DEFINE FVN = REB FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 216 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = F853 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 853 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = HPSTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 891 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C REB IS THE STEAM REQUIRED FOR PRETREATMENT" "F STMHP = REB + F853 + HPSTM" ) \ \ "READ-VARS" READ-VAR = ( REB F853 HPSTM ) \ \ "WRITE-VARS" WRITE-VAR = ( STMHP ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS BLOCK CALCULATES THE TOTAL HP STEAM DEMAND." ";;" "; DEFINE PTSTM STREAM-VAR STREAM=215 SUBSTREAM=MIXED &" "; VARIABLE=MASS-FLOW" ";;" ";;" ) \ ? CALCULATOR LPSTMD ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "C F COMMON /RXSPEC/ TEMPIN, CONCIN, TIME" "C THIS BLOCK CALCULATES THE TOTAL LP STEAM DEMAND." ) \ \ DEFINE FVN = STMDEM FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M811ISPT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 815 \ \ DEFINE FVN = PTSTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 215 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = LPSTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 890 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "F STMDEM = PTSTM + LPSTM" "F WRITE(NHSTRY,20) PTSTM, LPSTM" "F 20 FORMAT(' LP RESULTS',/," "F 6 ' LPSTM = ',G12.5)" ) \ \ "READ-VARS" READ-VAR = ( PTSTM LPSTM ) \ \ "WRITE-VARS" WRITE-VAR = ( STMDEM ) \ \ COMMENTS COMMENTS = ( "; EXECUTE BEFORE M811HSPT" ";;" ";;" ) \ ? CALCULATOR MISCPOW ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "C PH=PREHYDROLYSIS SCREW FEEDER / IMPREGNATOR / REACTOR (M-202)" ) \ \ DEFINE FVN = ST101 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 101 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = WPH FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM202 \ \ DEFINE FVN = STV220 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = STC220 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WFL FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC201 \ \ DEFINE FVN = WHF FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS205 \ \ DEFINE FVN = ST255 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 255 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = WCK FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC202 \ \ DEFINE FVN = ST239 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 239 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = GYPREM FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS222 \ \ DEFINE FVN = ULOAD FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP223 \ \ DEFINE FVN = STC227 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 227 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WFL2 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC225 \ \ DEFINE FVN = ETHDEN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 515 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = ETHFLO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 515 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = PWR FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM503 \ \ DEFINE FVN = STC570 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 570 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WCF FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS505 \ \ DEFINE FVN = STV5 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 571 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = STC5 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 571 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WS1 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC501 \ \ DEFINE FVN = SV614 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 623 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SC614 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 623 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WS2 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC614 \ \ DEFINE FVN = ST618 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 618 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = WS3 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS614 \ \ DEFINE FVN = ST613 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 613 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = WM604 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM604 \ \ DEFINE FVN = ST625 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 625 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = WM612 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM612 \ \ DEFINE FVN = ST612 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 612 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = WS600 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS600 \ \ DEFINE FVN = ST621 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 621 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = WT610 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT610 \ \ DEFINE FVN = UNLDAP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP755 \ \ DEFINE FVN = STC755 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 755 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WFD2 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC755 \ \ DEFINE FVN = WEM801 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM801 \ \ DEFINE FVN = STV6 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 851 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WEM804 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM804 \ \ DEFINE FVN = WEM830 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM830 \ \ DEFINE FVN = WEM832 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM832 \ \ DEFINE FVN = WEM834 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM834 \ \ DEFINE FVN = PCWCAP FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QCWCAP \ \ DEFINE FVN = WCT FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM902 \ \ DEFINE FVN = FM946 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 941A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RM946 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 941A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WEM104 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM904A \ \ DEFINE FVN = WES104 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS904 \ \ DEFINE FVN = QREF FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QCHWOP \ \ DEFINE FVN = WEM108 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM908 \ \ DEFINE FVN = WCIP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM910 \ \ DEFINE FVN = FM914 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 914 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "F PH = 7.138E-3" "F WPH = PH * ST101" "F WRITE(NHSTRY,*)'STRM 101: ',ST101,' WM202: ',WPH" "C FL=FLASH TANK SCREW CONVEYOR (C-201)" "F FL=1.643E-4" "F WFL=FL*(STV220+STC220)" "C HF=HYDROLYSATE PNEUMAPRESS (S-205)" "C POWER BASED ON THE SOLIDS FLOW OF STREAM 220" "C" "F HF = 2.0E-3" "F WHF = HF * STC220" "C CK=HYDROLYSATE WASHED SOLIDS BELT CONVEYOR (C-202)" "C" "F CK = 3.06E-4" "F WCK = CK * ST255" "F WRITE(NHSTRY,*)'STRM 255: ',ST255,' WC202: ',WCK" "C GYPREM = GYPSUM FILTER(S-222)" "C 25 HP / 167280 KG/HR = 1.495E-4HP/KG/HR = 1.114E-4 KW/KG/HR" "F GYPREM = 1.114E-4 * ST239" "F WRITE(NHSTRY,*)'STRM 239: ',ST239,' WC222: ',GYPREM" "C ULOAD=LIME UNLOADER BLOWER" "F UL1=0.012" "F ULOAD=UL1*(STC227)" "C FL=LIME SOLIDS AIR LOCK (C-225)" "F FL2=3.523E-4" "F WFL2=FL2*(STC227)" "C SVE=MOLE SIEVE SYSTEM (T-507-8)" "F GALFLO = (ETHFLO / ETHDEN / 3.7854)" "F WRITE(NHSTRY,*)'GALFLO,ETHFLO,ETHDEN= ',GALFLO,ETHFLO,ETHDEN" "C .0204 KW/GAL/HR" "F PWR = GALFLO * 0.0204" "F WRITE(NHSTRY,*)'PWR= ',PWR" "C CF=PNEUMAPRESS (S-505)" "C" "C 180 HP * (.7457 KW/HP) / 26601 KG/HR" "C" "F CF = 180. * 0.7457 / 26601." "F WCF = CF * STC570" "C S1=SLUDGE SCREWS (C-501A/B)" "C 85 HP / 99199 KG/HR" "F S1 = (85./99199.) * (STV5 + STC5)" "C CONVERT TO KW" "F WS1 = S1 * 0.7457" "C" "C S2=DIGESTION CELL MASS SCREWS (C-614)" "C 7.5 HP / 978 KG/HR" "F S2 = (7.5/978.) * (SV614 + SC614)" "C CONVERT TO KW" "F WS2 = S2 * 0.7457" "C" "C S3=FINISHING BELT FILTER PRESS (S-614)" "C" "C 30 HP * .7457 KW/HP / 185782 KG/HR" "C" "F S3 = 30. * 0.7457 / 185782." "F WS3 = S3 * ST618" "C ANEROBIC NUTRIENT FEED SYSTEM (M-604)" "C ASSUME A TOTAL OF 10 HP PER 175,000 KG/HR FROM 613" "C" "F REQ = 10. *.7457 / 175000." "F WM604 = ST613 * REQ" "C POLYMER ADDITION FOR ANEROBIC SLUDGE FILTER (M-612)" "C ASSUME A TOTAL OF 5 HP PER 5369 KG/HR FROM 625" "C" "F REQ = 5. *.7457 / 5369." "F WM612 = ST625 * REQ" "C MECHANICAL CLEANERS FOR BAR SCREENS (S-600)" "C ASSUME A TOTAL OF 1 HP PER 174500 KG/HR FROM 612" "C" "F REQ = 1. *.7457 / 174500." "F WS600 = ST612 * REQ" "C CLARIFIER MIXER (T-610)" "C ASSUME A TOTAL OF 5 HP PER 174500 KG/HR FROM 621" "C" "F REQ = 5. *.7457 / 174500." "F WT610 = ST621 * REQ" "C UNLDAP=DAP UNLOADER BLOWER (P-755)" "F UL2=0.012" "F UNLDAP=UL2*(STC755)" "C FD=DAP SOLIDS AIR LOCK (C-755)" "F FD2=3.523E-4" "F WFD2=FD2*(STC755)" "C POWER FOR DRYER BASED ON RETEC QUOTE" "C 30 HP / 8910 LB/HR (EVAPORATED) = 0.00742 HP/ (KG DRY/HR)" "F EM801=0.00742 *.7457" "F WEM801=EM801 * STV6" "C EM804=COMBUSTION GAS BAGHOUSE (M-804)" "C 176 KW POWER REQUIREMENT FROM QUOTE IN REI 1999 REPORT" "F EM804=176.0" "F WEM804=EM804" "C" "C EM830=HYDRAZINE ADDITION PACKAGE (M-830)" "C 10 KW POWER REQUIREMENT IS JUST A GUESS (=13 HP)" "F EM830=10.0" "F WEM830=EM830" "C" "C EM832=AMMONIA ADDITION PACKAGE (M-832)" "C 10 KW POWER REQUIREMENT IS JUST A GUESS (=13 HP)" "F EM832=10.0" "F WEM832=EM832" "C" "C EM834=PHOSPHATE ADDITION PACKAGE (M-834)" "C 10 KW POWER REQUIREMENT IS JUST A GUESS (=13 HP)" "F EM834=10.0" "F WEM834=EM834" "C" "C CT=COOLING TOWER PACKAGE (M-902)" "C 5 243 HP FANS ARE REQUIRED FOR 41,100,000 CAL/SEC COOLING" "C 2.204E-5 KW / CAL/SEC = (5 * 243 HP) / 41,100,000 CAL/SEC" "F CT=2.204E-5" "C PUMPING IS ALSO REQUIRED" "C EPM IS THE PUMP EFFICIENCIES" "C EEL IS THE MOTOR EFFICIENCIES" "F EPM = 0.60" "F EEL = 0.95" "F DP946 = 44.3" "F AP946 =(FM946/3600.)/(RM946*1000.)" "F WP946 =(AP946 * (DP946*6894.8) / (EPM*EEL) ) / 1000." "F WCT=CT*PCWCAP+WP946" "C EM904=PLANT AND INSTRUMENT AIR COMPRESSOR (M-904)" "C 93.2 KW = 125 HP & 2 IN USE" "F EM904=93.2*2" "F WEM104=EM904" "C" "C ES904=INSTRUMENT AIR DRYER (S-904)" "C 12 KW RATIOED FROM DELTA T" "F ES904=12" "F WES104=ES904*ST101/159948.0" "C EM908=CHILLED WATER SYSTEM CALCULATION (M-908A/S)" "C 5.327E-4 KW / CAL/SEC = 1200 HP / 2000 TONS REFRIGERATION" "F EM908=5.327E-4" "F WEM108=EM908*QREF" "C" "C" "F WRITE(NHSTRY,60)QREF,QSSF,CHWSPT,EM908,WEM108" "F 60 FORMAT('MISC RESULTS',/," "F 1 'QREF=',G12.5,/," "F 2 'QSSF=',G12.5,/," "F 4 'CHWSPT=',G12.5,/," "F 6 'EM908=',G12.5,/," "F 7 'WEM108=',G12.5)" "C EM910=CIP SYSTEM CALCULATION (M-910)" "C I ENTERED THE REQUIRED POWER FROM DELTA-T AND ALLOWED IT TO BE RATIOED TO" "C THE FLOW OF 914" "C PUMPING IS REQUIRED" "C EPM IS THE PUMP EFFICIENCIES" "C EEL IS THE MOTOR EFFICIENCIES" "F DPPMP1 = 125.0" "F APPMP1 = 600.0 / 60 * 3.785 / 1000" "F WPPMP1 =(APPMP1 * (DPPMP1*6894.8) / (EPM*EEL) ) / 1000." "F DPPMP2 = 60.0" "F APPMP2 = 2000.0 / 60 * 3.785 / 1000" "F WPPMP2 =(APPMP2 * (DPPMP2*6894.8) / (EPM*EEL) ) / 1000." "F DPPMP3 = 60.0" "F APPMP3 = 600.0 / 60 * 3.785 / 1000" "F WPPMP3 =(APPMP3 * (DPPMP3*6894.8) / (EPM*EEL) ) / 1000." "C 1 HP / 1000 GAL MR ESTIMATE" "C 50000 GAL DELTA T" "F WPAG1 = 1 * 50000/1000 * 0.7457" "C 0.5 HP / 1000 GAL MR ESTIMATE" "C 50000 GAL DELTA T" "F WPAG2 = 0.5 * 50000/1000 * 0.7457" "C 25 KW MR ESTIMATE" "F WPCN1 = 25" "C TOTAL POWER IS RATIOED TO FLOW OF 914 (63 WAS DESIGN FLOW)" "F WCIP = (WPPMP1+WPPMP2+WPPMP3+WPAG1+WPAG2+WPCN1)*FM914/63.0" "C" ) \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = CALCULATOR BLK-ID = POWER \ \ COMMENTS COMMENTS = ( "; EXECUTE BEFORE PMPWK" ";;" ";THIS BLOCK CALCULATES THE POWER REQUIREMENTS FOR" ";ALL OF THE SOLIDS HANDLING AND OTHER MISCELLANEOUS" ";EQUIPMENT EXCEPT AREA 100 (CALCULATED IN POW101)" ";;" ";;" ";DEFINE THE POWER REQUIREMENTS ( KW / (KG/HR) )" ";UNLESS OTHERWISE NOTED, THE POWER REQUIREMENTS WERE CALCULATED" ";FROM THE 1990 BASE CASE." ";THEY ARE SIMPLY RATIOS OF THE POWER REQUIRED AND THE FLOWRATE" ";THROUGH THE EQUIPMENT ITEM." ";;" "; AREA 200" ";;" "; DELTA-T/SUNDS:" "; Power Requirement 0.85 * 1363 hp (motor sizes) = 1158 hp = 863 kW" "; for total feed of 159948 kg/hr in Stream 101" "; 863 / 159948 = 5.396E-3" ";;" "; HARRIS/ANCO-EAGLIN:" "; Power Requirement 0.85 * 1801 hp (motor sizes) = 1531 hp = 1142 kW" "; for total feed of 159948 kg/hr in Stream 101" "; 1142 / 159948 = 7.138E-3" ";;" ";;" "; Power Req. 1.643E-4 kW/ kg/hr == 50 hp/ 250 ton/hr" ";;" ";;" "; Power Required from Harris design (60 hp for 3 machines at 75% power)" "; equals 135 hp / Flow from R0101C (see equip design" "; sheet)" "; Power Required 135 hp / 50299 kg/hr CISOLIDS flow = 2.68E-3 hp/kg/hr" "; = 2.00E-3 kW/kg/hr" ";;" "; Power Required from Harris design (50 hp at 75% power)" "; equals 37.5 hp / Flow from R0101C (see equip design" "; sheet)" "; 37.5 hp/91633 kg/hr = 28.0 KW/91633 Kg/hr" "; = 3.06E-4 kW/kg/hr" ";;" ";;" ";;" ";;" "; Average Power 8.6 hp / 548 kg/hr" ";;" "; Power Req. 6.4 kW / 548 kg/hr = 0.012 kW / kg/hr" ";;" ";;" "; 3.523E-4 kW/ kg/hr =1.5 hp/7000 lb/hr from Icarus 20 Oct 98" ";;" "; AREA 500" ";THE POWER REQUIREMENTS ARE SIMPLE RATIOS FROM A" ";COST QUOTE." ";;" "; was formerly centrifuges so that's why it's CF" ";;" "; AREA 600" ";;" ";;" ";;" ";;" ";;" "; AREA 700" ";;" "; COPY OF WP223 POWER CALCULATION" "; Average Power 8.6 hp / 548 kg/hr" ";;" "; Power Req. 6.4 kW / 548 kg/hr = 0.012 kW / kg/hr" ";;" ";;" ";;" "; COPY OF WC225 POWER CALCULATION" "; 3.523E-4 kW/ kg/hr =1.5 hp/7000 lb/hr from Icarus 20 Oct 98" ";;" "; AREA 800" ";;" ";;" "; AREA 900" "; 44.3 psi=100 ft head" "; First pump 600 gpm & 125 psi from Delta-T" "; Second pump 2000 gpm & 60 psi from Delta-T" "; Third pump 600 gpm from Delta-T & 60 psi MR estimate" "; Agitator in Sterizilation Tank" "; Agitator in Cleaning Chemical Tank" "; Centrifugal Separator" ) \ ? CALCULATOR MOISTURE ? ; "SET1_MOLE" ; \ DEFINE FVN = W803 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = X803 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = C803 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = W615 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = X615 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = C615 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 615 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = TOTWAT FVN-VARTYPE = PARAMETER FVN-PARAMNO = 51 \ \ DEFINE FVN = WATPER FVN-VARTYPE = PARAMETER FVN-PARAMNO = 52 \ \ FORTRAN FORTRAN-EXEC = ( "F TOTWAT = W803 + W615" "F TOTFLO = X803 + X615 + C803 + C615" "F WATPER = TOTWAT/TOTFLO*100." "F WRITE(NHSTRY,*)'WATPER = ',WATPER" ) \ \ "READ-VARS" READ-VAR = ( W803 X803 C803 W615 X615 C615 ) \ \ "WRITE-VARS" WRITE-VAR = ( TOTWAT WATPER ) \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CALCULATOR NUTRA ? ; "SET1_MOLE" ; \ DEFINE FVN = GLUCA FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 412A FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = GLUCB FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = ANNOA FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 412A FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = ANNOB FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GALAA FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 412A FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = GALAB FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = XYLOA FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 412A FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = XYLOB FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = ARABA FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 412A FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = ARABB FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = CELLA FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 412A FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = CELLB FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 433 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = ANNNA FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 412A FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = ANNNB FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 433 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = GLTNA FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 412A FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = GLTNB FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 433 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = ASO2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 436 FVN-SUBS = MIXED FVN-COMPONEN = SO2 \ \ DEFINE FVN = ANH3 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 436 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ DEFINE FVN = XNH3 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 412A FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ DEFINE FVN = YNH3 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ FORTRAN FORTRAN-EXEC = ( "F GLUCOS = GLUCA + GLUCB" "F ANNOSE = ANNOA + ANNOB" "F GALAOS = GALAA + GALAB" "F XYLOSE = XYLOA + XYLOB" "F ARABOS = ARABA + ARABB" "F CELLOS = CELLA + CELLB" "F ANNAN = ANNNA + ANNNB" "F GLTAN = GLTNA + GLTNB" "F SO2X = .47*(GLUCOS + ANNOSE + GALAOS + XYLOSE + ARABOS)*0.01522/2." "F SO2Y = .53*(GLUCOS + ANNOSE + GALAOS + XYLOSE + ARABOS)*0.02414/2." "F SO2Z = (CELLOS+ANNAN+GLTAN) * 0.02414/2." "F ASO2 = SO2X + SO2Y + SO2Z" "F ANH3 = ((GLUCOS + ANNOSE + GALAOS + XYLOSE + ARABOS + CELLOS" "F 1 + ANNAN + GLTAN) * 1./2.) - XNH3 - YNH3" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = F400 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CALCULATOR NUTRB ? ; "SET1_MOLE" ; \ DEFINE FVN = GLUC FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 431 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = ANNO FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 431 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GALA FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 431 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = XYLO FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 431 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = ZNH3 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 431 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ DEFINE FVN = ZSO2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 431 FVN-SUBS = MIXED FVN-COMPONEN = SO2 \ \ DEFINE FVN = ARAB FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 431 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = CELL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 431 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = ANNA FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 431 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = GALT FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 431 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = BSO2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 434 FVN-SUBS = MIXED FVN-COMPONEN = SO2 \ \ DEFINE FVN = BNH3 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 434 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ FORTRAN FORTRAN-EXEC = ( "F BSO2 = (GLUC+ANNO+GALA+XYLO+ARAB+CELL+ANNA+GALT) * 0.01522/2." "F 1 - ZSO2" "F BNH3 = (GLUC+ANNO+GALA+XYLO+ARAB+CELL+ANNA+GALT) * 1./2." "F 1 - ZNH3" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = "F401-4" \ \ FLASH-SPECS FLASH-STREAM = 434 KODE = TP TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CALCULATOR O2CALC ? ; "SET1_MOLE" ; \ DEFINE FVN = CH4615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = X2S615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = FUR615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = AA615 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 615 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = CH4840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = SOL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = CEL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XYN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = ARN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = ARABINAN \ \ DEFINE FVN = XNN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = GAN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = XLG840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = LIGNIN \ \ DEFINE FVN = ACE840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = ACETATE \ \ DEFINE FVN = GLO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CLB840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XNO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GAO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = XYO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = TAR840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = TAR \ \ DEFINE FVN = ACO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = FUR840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = XLL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = GLU840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = XNS840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GAL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = ARA840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = AA840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = XLA840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = CLS840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = CELLULAS \ \ DEFINE FVN = ETO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = ZYM840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = ZYMO \ \ DEFINE FVN = GLY840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUC840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = BIO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = BIOMASS \ \ DEFINE FVN = C840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = CISOLID FVN-COMPONEN = C \ \ DEFINE FVN = UNK840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = X2S840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = ACN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = COI840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = DEN840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = XSL840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXT840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PRO840 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 840 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = SOL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = CEL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = XYN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = ARN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ARABINAN \ \ DEFINE FVN = XNN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = MANNAN \ \ DEFINE FVN = GAN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = GALACTAN \ \ DEFINE FVN = XLG803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = LIGNIN \ \ DEFINE FVN = ACE803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ACETATE \ \ DEFINE FVN = GLO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CLB803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = XNO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = GAO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = ARO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = XYO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = TAR803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = TAR \ \ DEFINE FVN = ACO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = FUR803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XMF803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = XLL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = GLU803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = XNS803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = GAL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = ARA803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = AA803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = XLA803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = CLS803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = CELLULAS \ \ DEFINE FVN = ETO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = ZYM803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ZYMO \ \ DEFINE FVN = GLY803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = SUC803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = BIO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = BIOMASS \ \ DEFINE FVN = C803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = C \ \ DEFINE FVN = UNK803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = X2S803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ DEFINE FVN = ACN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = COI803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = DEN803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = XSL803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EXT803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PRO803 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = FRACO2 FVN-VARTYPE = "MASS-FRAC" FVN-STREAM = 804 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = OXY261 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 261 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = OXY560 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 560 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = BNDLOW FVN-VARTYPE = PARAMETER FVN-PARAMNO = 55 \ \ DEFINE FVN = BNDHIH FVN-VARTYPE = PARAMETER FVN-PARAMNO = 56 \ \ FORTRAN FORTRAN-EXEC = ( "C SET THE MOLES OF OXYGEN REQUIRED TO COMBUST 1 MOLE OF EACH COMPONENT" "C THE VARIABLES ARE ROXXX WITH THE 3 X'S CORRESPONDING" "C TO A 3 LETTER CODE FOR EACH COMPONENT USED IN THE DEFINE STATEMENTS" "C" "F ROCH4 = 2.0" "F ROX2S = 1.5" "F ROFUR = 5.0" "F ROXMF = 6.0" "F ROAA = 2.0" "F ROSOL = 1.4995" "F ROCEL = 6.0" "F ROXYN = 5.0" "F ROARN = 5.0" "F ROXNN = 6.0" "F ROGAN = 6.0" "F ROXLG = 12.825" "F ROACE = 2.0" "F ROGLO = 6.0" "F ROCLB = 12.0" "F ROXNO = 6.0" "F ROGAO = 6.0" "F ROARO = 5.0" "F ROXYO = 5.0" "F ROTAR = 5.0" "F ROACO = 2.0" "F ROXLL = 5.5" "F ROGLU = 6.0" "F ROXYL = 5.0" "F ROXNS = 6.0" "F ROGAL = 6.0" "F ROARA = 5.0" "F ROXLA = 3.0" "F ROCLS = 1.2445" "F ROETO = 3.0" "F ROZYM = 1.2" "F ROGLY = 3.5" "F ROSUC = 3.5" "F ROBIO = 1.2185" "F ROACN = 2.75" "F ROCOI = 25.5" "F ROXLGS = 12.825" "F ROEXT = 1.4995" "F ROPRO = 1.4995" "F ROC = 1.0" "F RODEN = 11.0" "C UNKNOWN COMPONENT IS CURRENTLY NOT BEING USED SO ROEXS=0.0" "C & ROUNK=0.0 MR 14 NOV 00" "F ROEXS = 0.0" "F ROUNK = 0.0" "C" "C CALCULATE THE O2 REQUIREMENT TO COMBUST STREAM 615, ANAEROBIC OFF-GAS" "C" "F RO615 = CH4615*ROCH4 + X2S615*ROX2S + FUR615*ROFUR +" "F 1 XMF615*RO615 + AA615*RO615" "F WRITE(NHSTRY,*)'REQUIRED OXYGEN FOR 615 (MOLE/HR)= ',RO615" "C" "C CALCULATE THE O2 REQUIREMENT TO COMBUST OF STREAM 840, SUPPLEMENT TO BOILER" "C" "F RO840 = CH4840*ROCH4 +" "F 1 SOL840*ROSOL + CEL840*ROCEL + XYN840*ROXYN +" "F 2 ARN840*ROARN + XNN840*ROXNN + GAN840*ROGAN +" "F 3 XLG840*ROXLG + ACE840*ROACE +" "F 4 GLO840*ROGLO + CLB840*ROCLB + XNO840*ROXNO +" "F 5 GAO840*ROGAO + ARO840*ROARO + XYO840*ROXYO +" "F 6 TAR840*ROTAR + ACO840*ROACO + FUR840*ROFUR +" "F 7 XMF840*ROXMF + XLL840*ROXLL + GLU840*ROGLU +" "F 8 XYL840*ROXYL + XNS840*ROXNS + GAL840*ROGAL +" "F 9 ARA840*ROARA + AA840*ROAA + XLA840*ROXLA +" "F * CLS840*ROCLS + ETO840*ROETO + ZYM840*ROZYM +" "F 1 GLY840*ROGLY + SUC840*ROSUC + BIO840*ROBIO +" "F 2 C840*ROC + UNK840*ROUNK + X2S840*ROX2S +" "F 3 ACN840*ROACN + COI840*ROCOI + DEN840*RODEN +" "F 4 XSL840*ROXLGS + EXT840*ROEXT + PRO840*ROPRO" "F WRITE(NHSTRY,*)'REQUIRED OXYGEN FOR 840 (MOLE/HR)= ',RO840" "C" "C CALCULATE THE BTU/HR OF STREAM 803:S505 SOLIDS,DIGESTOR SOLIDS,SYRUP" "C" "F RO803 = SOL803*ROSOL + CEL803*ROCEL + XYN803*ROXYN +" "F 1 ARN803*ROARN + XNN803*ROXNN + GAN803*ROGAN +" "F 2 XLG803*ROXLG + ACE803*ROACE +" "F 3 GLO803*ROGLO + CLB803*ROCLB + XNO803*ROXNO +" "F 4 GAO803*ROGAO + ARO803*ROARO + XYO803*ROXYO +" "F 5 TAR803*ROTAR + ACO803*ROACO + FUR803*ROFUR +" "F 6 XMF803*ROXMF + XLL803*ROXLL + GLU803*ROGLU +" "F 7 XYL803*ROXYL + XNS803*ROXNS + GAL803*ROGAL +" "F 8 ARA803*ROARA + AA803*ROAA + XLA803*ROXLA +" "F 9 CLS803*ROCLS + ETO803*ROETO + ZYM803*ROZYM +" "F * GLY803*ROGLY + SUC803*ROSUC + BIO803*ROBIO +" "F 1 C803*ROC + UNK803*ROUNK + X2S803*ROX2S +" "F 2 ACN803*ROACN + COI803*ROCOI + DEN803*RODEN +" "F 3 XSL803*ROXLGS + EXT803*ROEXT + PRO803*ROPRO" "F WRITE(NHSTRY,*)'REQUIRED OXYGEN FOR 803 (MOLE/HR)= ',RO803" "C" "C CALCULATE THE TOTAL OXYGEN REQUIREMENT OF THE BOILER (MOLE/HR)" "C" "F ROTMOL = (RO615+RO840+RO803)" "C" "C CALCULATE THE TOTAL OXYGEN REQUIREMENT OF THE BOILER + EXCESS (KG/HR)" "C - THAT PROVIDED BY STREAMS 261 & 560" "F ROTMAS = ROTMOL * 32 * 1.2" "F ROTMAS = ROTMAS - OXY261 - OXY560" "C" "C WRITE RESULTS TO THE HISTORY FILE" "C" "F WRITE(NHSTRY,*)'REQUIRED OXYGEN MOLE FLOW (NO EXCESS)= ',ROTMOL" "F WRITE(NHSTRY,*)'REQUIRED OXYGEN MASS FLOW= ',ROTMAS" "C" "C SET UPPER AND LOWER BOUNDS FOR COMBAIR" "C" "F BNDLOW = ROTMAS * 0.8 / FRACO2" "F BNDHIH = ROTMAS * 1.2 / FRACO2" "C" ) \ \ "READ-VARS" READ-VAR = ( AA615 CH4840 XLG803 FRACO2 OXY261 OXY560 ) \ \ "WRITE-VARS" WRITE-VAR = ( BNDLOW BNDHIH ) \ \ COMMENTS COMMENTS = ( "; EXECUTE AFTER T914" ";-------------------------------------------------------------" "; BURNER FORTRAN BLOCKS - AREA 800" ";------------------------------------------------------------" ";;" "; ROSOL, ROEXT, & ROPRO should be modified by FEEDPROP or sampled from M803C" "; which is set by FEEDPROP to get the proper values but I have not made t" "; change yet." ) \ ? CALCULATOR OLCONV ? ; "SET1_MOLE" ; \ DEFINE FVN = CONV1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T224 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 1 \ \ DEFINE FVN = CONV2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T224 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 2 \ \ DEFINE FVN = CA227 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 227 FVN-SUBS = CISOLID FVN-COMPONEN = CAH2O2 \ \ DEFINE FVN = CA228 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 228 FVN-SUBS = CISOLID FVN-COMPONEN = CAH2O2 \ \ FORTRAN FORTRAN-EXEC = ( "F TARGET = 1.0" "F CAOUT = (1. - TARGET)*CA227" "F CONV1 = 1. - CAOUT / CA228" "F IF (CONV1 .LT. 0.) CONV1 = 0." "F IF (CONV1 .GT. 1.) CONV1 = 1." "F CONV2 = 1. - CONV1" "F WRITE (NHSTRY,*) ' T224 CA(OH)2 CONVERSIONS: ', CONV1, CONV2" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = T224 \ \ COMMENTS COMMENTS = ( ";;" ";;" "; TARGET is the desired overall conversion of Ca(OH)2 to Gypsum." ) \ ? CALCULATOR OLIME ? ; "SET1_MOLE" ; \ DEFINE FVN = FL240 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 240 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FL227 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 227 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FA240 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 240 FVN-SUBS = MIXED FVN-COMPONEN = H2SO4 \ \ FORTRAN FORTRAN-EXEC = ( "F WM227=74.09" "F FACTOR = 0.01/3" "F FL227 = FACTOR * FL240 + FA240 * WM227" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = T209 \ \ COMMENTS COMMENTS = ( ";;" "; FACTOR = THE LIME ADDITION FACTOR (g CaOH / g Hydrolysate Liquor)" "; FACTOR = 0.003 was experimentally determined by MN, MA, & TKH on" "; P961008SD, P961010SD, and P961014SD, respectively." "; Reduced by factor of 3 due to increased flow with S/L wasH before IX" ) \ ? CALCULATOR PLANTPOW ? ; "SET1_MOLE" ; \ DEFINE FVN = POWREQ FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WPLNTPOW \ \ FORTRAN FORTRAN-EXEC = ( "C 1000 KW REQUIREMENT IS A GUESS (MR 12 FEB 1998)" "F POWREQ=1000" ) \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = CALCULATOR BLK-ID = MISCPOW \ \ COMMENTS COMMENTS = ( ";;" ";;" ) \ ? CALCULATOR PLNTELEC ? ; "SET1_MOLE" ; \ DEFINE FVN = WTOT FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WTOTAL \ \ DEFINE FVN = WTOT2 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WTOTAL2 \ \ FORTRAN FORTRAN-EXEC = ( "F WTOT2 = -WTOT" ) \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = BLOCK BLK-ID = M811GEN \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CALCULATOR POLLUTE ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F COMMON / HEATIN / BTUTOT" ) \ \ DEFINE FVN = FINNOX FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = EXTENT FVN-SENTENCE = EXTENT FVN-ID1 = 67 \ \ DEFINE FVN = WTNOX FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = NO2 FVN-ID2 = 1 \ \ DEFINE FVN = WTCO FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = CO FVN-ID2 = 1 \ \ DEFINE FVN = FINCO FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M803CMB FVN-VARIABLE = EXTENT FVN-SENTENCE = EXTENT FVN-ID1 = 40 \ \ FORTRAN FORTRAN-EXEC = ( "C SET THE EXPECTED NOX GENERATION RATE, GENNOX (LB/MMBTU)" "C" "F GENNOX = 0.20" "C 0.2 ASSUMES NO NOX CONTROL IN THE BURNER; FROM FOSTER WHEELER" "C FROM REI SUBCONTRACT, 1999" "C" "F FINNOX = GENNOX/2.205*BTUTOT/WTNOX" "F WRITE(NHSTRY,*)'FINNOX= ',FINNOX" "C SET THE EXPECTED CO GENERATION RATE, GENCO (LB/MMBTU)" "C" "F GENCO = 0.20" "C THIS VALUE WAS OBTAINED FROM THE FWEC QUOTE IN THE REI FINAL" "C REPORT 1999" "C" "F FINCO = GENCO/2.205*BTUTOT/WTCO" "C" "F WRITE(NHSTRY,*)'FINCO = ',FINCO" "F WRITE(NHSTRY,*)'WTCO =',WTCO" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = M803CMB \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CALCULATOR POLY1 ? ; "SET1_MOLE" ; \ DEFINE FVN = POLY FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 107 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDSL FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C" "C POLREQ IS THE POLYMER REQUIREMENT (PPM) AS FUNCTION OF FEED TO CLARIFIER." "C THE FEED TO CLARIFIER IS 5000 GPM PER HARRIS 2000 SUBCONTRACT REPORT" "C SO CLARFD IS SET AT 5000 GPM * 3.785 L/GAL * 1 KG/L * 60 MIN/HR (SO IT" "C IS IN UNITS KG/HR AND IS RATIOED OFF OF STREAM 101 -- 98040 KG/HR TOTAL" "C IN HARRIS SUBCONTRACT)." "F POLREQ = 25.0" "F CLARFD = 5000.0 * 3.785 * 1.0 * 60.0 * ((FEEDMX+FEEDSL)/98040.0)" "C" "F POLY = POLREQ * CLARFD / 1000000.0" "C" ) \ \ "READ-VARS" READ-VAR = ( FEEDMX FEEDSL ) \ \ "WRITE-VARS" WRITE-VAR = ( POLY ) \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CALCULATOR POW101 ? ; "SET1_MOLE" ; \ DEFINE FVN = STV1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = STC1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WWC101 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC101 \ \ DEFINE FVN = WWC102 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC102 \ \ DEFINE FVN = WWC104 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC104 \ \ DEFINE FVN = WWC103 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC103 \ \ DEFINE FVN = WWM104 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM104 \ \ DEFINE FVN = WWM105 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM105 \ \ DEFINE FVN = WWM107 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM107 \ \ DEFINE FVN = WWP101 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP101 \ \ DEFINE FVN = WWP102 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP102 \ \ DEFINE FVN = WWP103 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP103 \ \ DEFINE FVN = WWP104 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP104 \ \ DEFINE FVN = WWP105 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP105 \ \ DEFINE FVN = WWS101 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS101 \ \ DEFINE FVN = WWS102 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS102 \ \ FORTRAN FORTRAN-EXEC = ( "F TOTFLO1 = STV1 + STC1" "F PWRRAT=0.75" "F PMPREQ=0.5" "F FLORAT = 98039." "F PC101 = 74.57" "F WWC101 = PC101 * PWRRAT * TOTFLO1/FLORAT" "F PC102 = 14.91" "F WWC102 = PC102 * PWRRAT * TOTFLO1/FLORAT" "F PC104 = 14.91" "F WWC104 = PC104 * PWRRAT * TOTFLO1/FLORAT" "F PC103 = 3.73" "F WWC103 = PC103 * PWRRAT * TOTFLO1/FLORAT" "F PM104 = 111.86" "F WWM104 = PM104 * PWRRAT * TOTFLO1/FLORAT" "F PM105 = 1491.4" "F WWM105 = PM105 * PWRRAT * TOTFLO1/FLORAT" "F PM107 = 25.0 / PWRRAT" "F WWM107 = PM107 * PWRRAT * TOTFLO1/FLORAT" "F EPM = 0.67" "F EEL = 0.95" "F DP101 = 21.68" "F AP101 = 0.1578 * PMPREQ" "C TWO UNITS" "F EP101 = 2.0" "F WWP101 = EP101 * (AP101 * (DP101*6894.8) / (EPM*EEL) ) / 1000." "F DP102 = 21.68" "F AP102 = 0.3155 * PMPREQ" "C TWO UNITS" "F EP102 = 2.0" "F WWP102 = EP102 * (AP102 * (DP102*6894.8) / (EPM*EEL) ) / 1000." "F EPM103 = 0.169" "F DP103 = 21.68" "F AP103 = 0.00631 * PMPREQ" "C ONE UNIT" "F EP103 = 1.0" "F WWP103 = EP103 * (AP103 * (DP103*6894.8) / (EPM103*EEL) ) / 1000." "F DP104 = 21.68" "F AP104 = 0.3155 * PMPREQ" "C ONE UNIT" "F EP104 = 1.0" "F WWP104 = EP104 * (AP104 * (DP104*6894.8) / (EPM*EEL) ) / 1000." "C EPM105 IS THE PUMP EFFICIENCIES (SET AT 33.7% TO GET 3 HP DESIGN LIKE REPORT)" "F EPM105=0.337" "C EEL IS THE MOTOR EFFICIENCIES" "F DP105 = 17.34" "F AP105 = 0.00631 * PMPREQ" "C ONE UNIT" "F EP105 = 1.0" "F WWP105 = EP105 * (AP105 * (DP105*6894.8) / (EPM105*EEL) ) / 1000." "F PS101 = 7.457" "F WWS101 = PS101 * PWRRAT * TOTFLO1/FLORAT" "F PS102 = 5.59" "F WWS102 = PS102 * PWRRAT * TOTFLO1/FLORAT" ) \ \ "READ-VARS" READ-VAR = ( STV1 STC1 ) \ \ "WRITE-VARS" WRITE-VAR = ( WWC101 WWC102 WWC104 WWC103 WWM104 WWM105 WWM107 WWP101 WWP102 WWP103 WWP104 WWP105 WWS101 WWS102 ) \ \ COMMENTS COMMENTS = ( ";;" ";--------------------------------------------------------" "; UTILITY FORTRAN BLOCKS - AREA 900" ";-------------------------------------------------------" ";;" "; Calculates Power requirements for equipment in Area 100 from Harris" "; Subcontract Information" "; Power requirements are ratioed from 101's flow-rate" "; Harris stated that power requirements are 75% of connected power" "; and reported connected power for equipment so PWRRAT=0.75" "; Subcontract ACO-9-29067-01" "; Report 99-10600/13 page 4" "; Harris stated that 2500 gpm per line is the necessary water flow and" "; designed the pumps for 5000 gpm so I set PMPREQ to 0.5" "; Harris' design was for 2000 bone dry metric tonnes / day at 15% moisture" "; That is equivalent to 2594 short tons as recieved material / day" "; Also equivalent to 98039 kg as received material / hr" "; Subcontract ACO-9-29067-01" "; Report 99-10600/13 page 2" "; Bale Transport Conveyors (C-101)" "; 2 motors at 50 hp each = 100 hp = 74.57 kW for standard size facility" "; (159948 kg/hr in 101)" ";;" "; Bale Unwrapping Conveyors (C-102)" "; 2 motors at 10 hp each = 20 hp = 14.91 kW for standard size facility" "; (159948 kg/hr in 101)" ";;" "; Shredder Feed Conveyor (C-104)" "; 4 motors at 5 hp each = 20 hp = 14.91 kW for standard size facility" "; (159948 kg/hr in 101)" ";;" "; Belt Press Discharge Conveyor (C-105)" "; 1 motors at 5 hp each = 5 hp = 3.73 kW for standard size facility" "; (159948 kg/hr in 101)" ";;" "; Wash Tables (M-104)" "; 2 motors at 75 hp each = 150 hp = 111.86 kW for standard size facility" "; (159948 kg/hr in 101)" ";;" "; Wash Tables (M-105)" "; 4 motors at 500 hp each = 2000 hp = 1491.4 kW for standard size facility" "; (159948 kg/hr in 101)" ";;" "; Polymer Feed System (M-107)" "; Minimal Power required so 25 kW for standard size facility" "; (159948 kg/hr in 101)" ";;" "; Wash Table Pump (P-101)" "; The listed pump design is 2500 gpm (0.1578 m^3/s) at 50 ft (21.68 psi) (Ap" ";C EPM is the pump efficiencies (set at 67% to get 100hp design like report" ";C EEL is the motor efficiencies" ";;" "; Wash Water Pump (P-102)" "; The listed pump design is 5000 gpm (0.3155 m^3/s) at 50 ft (21.68 psi) (Ap" ";C EPM is the pump efficiencies (set at 67% to get 100hp design like report" ";C EEL is the motor efficiencies" ";;" "; Clarifier Underflow Feed Pump (P-103)" "; The listed pump design is 100 gpm (0.00631 m^3/s) at 50 ft (21.68 psi) (Ap" "; EPM103 is the pump efficiencies (set at 16.9% to get 7.5hp design like re" "; EEL is the motor efficiencies" ";;" "; Clarified Water Pump (P-104)" "; The listed pump design is 5000 gpm (0.3155 m^3/s) at 50 ft (21.68 psi) (Ap" ";C EPM is the pump efficiencies (set at 67% to get 100hp design like report" ";C EEL is the motor efficiencies" ";;" "; Belt Press Sump Pump (P-105)" "; The listed pump design is 100 gpm (0.00631 m^3/s) at 40 ft (17.34 psi) (Ap" ";;" "; Clarifier Thickener (S-101)" "; 1 motors at 10 hp each = 10 hp = 7.457 kW for standard size facility" "; (159948 kg/hr in 101)" ";;" "; Belt Filter (S-102)" "; 1 units at 7.5 hp each = 7.5 hp = 5.59 kW for standard size facility" "; (159948 kg/hr in 101)" ) \ ? CALCULATOR POWER ? ; "SET1_MOLE" ; \ DEFINE FVN = CLVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 43 \ \ DEFINE FVN = CLVOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 44 \ \ DEFINE FVN = OL FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 228 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = OLD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 228 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = OLS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 228 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = OLDS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 228 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = OLMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT209 \ \ DEFINE FVN = XNT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 239 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = XNTD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 239 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = XNTS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 239 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = XNTDS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 239 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = XNTMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT224 \ \ DEFINE FVN = HMT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = HMTD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = HMTS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = HMTDS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = HMTMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT205 \ \ DEFINE FVN = SLT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 250 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SLTD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 250 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = SLTS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 250 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SLTDS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 250 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = SLTMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT232 \ \ DEFINE FVN = SD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SDD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = SDS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SDSD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = SDMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT305 \ \ DEFINE FVN = SDMXP2 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT304 \ \ DEFINE FVN = ZMMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT301 \ \ DEFINE FVN = SA FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301B FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SAD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301B FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = SAS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301B FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SASD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301B FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = SAMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT310 \ \ DEFINE FVN = SACVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 36 \ \ DEFINE FVN = SACDAY FVN-VARTYPE = PARAMETER FVN-PARAMNO = 37 \ \ DEFINE FVN = SACVOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 38 \ \ DEFINE FVN = SACWV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 39 \ \ DEFINE FVN = SAR FVN-VARTYPE = PARAMETER FVN-PARAMNO = 20 \ \ DEFINE FVN = SM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SMD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = SMS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SMSD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = SMMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT300 \ \ DEFINE FVN = SSFVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 31 \ \ DEFINE FVN = SSFDAY FVN-VARTYPE = PARAMETER FVN-PARAMNO = 32 \ \ DEFINE FVN = SSFVOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 33 \ \ DEFINE FVN = SSFWV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 34 \ \ DEFINE FVN = SMR FVN-VARTYPE = PARAMETER FVN-PARAMNO = 21 \ \ DEFINE FVN = BW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 502 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = BWD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 502 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = BWS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 502 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = BWSD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 502 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = BWMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT306 \ \ DEFINE FVN = CSD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CSDD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = CSDS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 433 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CSDSD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 433 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = CSMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "WT402-3" \ \ DEFINE FVN = CLMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT400 \ \ DEFINE FVN = PM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 416 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = PMD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 416 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = PMS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 416 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = PMSD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 416 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = PMMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT405 \ \ DEFINE FVN = AB FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 612 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = ABD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 612 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = ABS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 612 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = ABSD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 612 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = EQMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT602 \ \ DEFINE FVN = RW2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 572 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RWD2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 572 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = RWS2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 572 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RWSD2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 572 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = RWMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT530 \ \ DEFINE FVN = CSLT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CSLTD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = CSLTS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CSLTDS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = CSLMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT720 \ \ DEFINE FVN = DAPT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = DAPTD FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = DAPTS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = DAPTDS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = DAPMXP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT760 \ \ FORTRAN FORTRAN-EXEC = ( "C" "C POWER REQUIREMENTS FOR EACH STREAM ARE IN KW/L (**P)" "C" "C THESE POWER REQUIREMENTS WAS OBTAINED FROM THE" "C 1990 BASE CASE. EXCEPTIONS INCLUDE THOSE FOR" "C WASTEWATER TREATMENT WHICH WERE OBTAINED FROM" "C THE 1995 CHEM SYSTEMS STUDY AND THE CH2MHILL" "C REPORT. THEY ARE LISTED IN KW/L. 3.94E-4 KW/L=2 HP/1000 GAL." "C" "C" "C THE RESIDENCE TIME FOR EACH VESSEL IS IN HOURS (**R)" "C" "C THE RESIDENCE TIMES (H) WERE TAKEN FROM THE 1990 BASE" "C CASE EXCEPT FOR THOSE FOR WASTEWATER TREATMENT" "C WHICH WERE TAKEN FROM THE 1995 CHEM SYSTEMS STUDY AND" "C FROM THE CH2MHILL REPORT." "C" "C" "C THE POWER FOR EACH VESSEL IS CALCULATED IN KW (**MXP)" "C" "F OLV=OL/OLD+OLS/OLDS" "C 9.85E-5 KW/L=0.5 HP/1000 GAL" "F OLP=9.85E-5" "C 1 HR. RESIDENCE TIME FROM DELTA T" "F OLR=1" "F OLMXP=OLV*OLR*OLP" "F XNTV=XNT/XNTD+XNTS/XNTDS" "F XNTP=9.85E-5" "F XNTR=4" "F XNTMXP=XNTV*XNTR*XNTP" "F HMTV=HMT/HMTD+HMTS/HMTDS" "F HMTP=2.96E-4" "F HMTR=0.25" "F HMTMXP=HMTV*HMTR*HMTP" "F SLTV=SLT/SLTD+SLTS/SLTDS" "F SLTP=2.96E-4" "F SLTR=0.25" "F SLTMXP=SLTV*SLTR*SLTP" "F SDV = (SD/SDD + SDS/SDSD)" "F SDV = SDV * 0.1" "F SDP = 1.97E-5" "F SDR = 24." "F SDNU = 2." "F SDMXP = SDNU * SDV * SDR * SDP" "C THEN A-304" "C SDN2 IS THE VOLUME RATIO OF F-304 TO F-305" "F SDN2 = 0.1" "C SDP2 IS THE MIXING POWER FOR A-304 (5.91E-5=0.3 HP/1000 GAL)" "F SDP2 = 5.91E-5" "F SDMXP2 = SDP2 * (SDNU * SDV * SDR) * SDN2" "F ZMINC=1.2" "F ZMP=1.97E-5" "F ZMR=24" "F ZMMXP=(SDV*ZMR) * ZMINC * ZMP" "F SAV = SA/SAD + SAS/SASD" "F SAP = 2.9549E-5" "F SAR = SACDAY * 24" "F SAMXP = SAV * SAR * SAP" "F SACVES = SAV * SAR / SACVOL / SACWV" "F SMV = SM/SMD + SMS/SMSD" "F SMP = 2.9549E-5" "F SMR = SSFDAY * 24" "F SMMXP = SMV * SMR * SMP" "F SSFVES = SMV * SMR / SSFVOL / SSFWV" "F BWV = BW/BWD + BWS/BWSD" "F BWP = 5.91E-5" "F BWR = 4" "F BWMXP = BWV * BWR * BWP" "C FIRST CALCULATE FOR A-403" "F CSV=CSD/CSDD+CSDS/CSDSD" "F CSP=1.972E-3" "F CSR=24" "F CSNU=3" "F CSMXP=CSNU*CSV*CSR*CSP" "C THEN FOR A-402" "C CSR3 IS THE VOLUME RATIO OF F-402 TO F-403" "F CSR3=0.05" "C CSP3 IS THE POWER REQUIREMENT FOR A-402 (5.20E-3 KW/L=26.4HP/1000 GAL)" "F CSP3=5.2E-3" "F CSMXP=CSMXP + CSNU*CSV*CSR*CSR3*CSP3" "C CLV IS THE VOLUME (IN LITERS) OF THE CELLULASE PRODUCTION FERMS" "C IT IS CALCULATED FROM VARIABLES CALCULATED IN AIRREQ" "F CLV=(CLVES-3)*CLVOL" "C 4.48E-4 KW/L= 2.2727 HP/1000 GAL = 600 HP / 264000 GAL" "C (FROM LIGHTNIN QUOTE -- ON FULL VOLUME BASIS)" "F CLP=4.48E-4" "F CLMXP=CLV*CLP" "F PMV=PM/PMD+PMS/PMSD" "C 0.2 HP/1000 GAL = 39.40E-6 KW/L" "F PMP=39.4E-6" "C RESIDENCE TIME 36 HR" "F PMR=36" "F PMMXP=PMV*PMP*PMR" "F WRITE(NHSTRY,*)'PMV=',PMV,'PMR=',PMR,'PMMXP=',PMMXP" "F EQV=AB/ABD" "C 0.1 HP/1000 GAL = 19.70E-6 KW/L" "F EQP=19.7E-6" "C RESIDENCE TIME 7.2 HR" "F EQR=7.2" "F EQMXP=EQV*EQP*EQR" "F WRITE(NHSTRY,*)'EQV=',EQV,'EQR=',EQR,'EQMXP=',EQMXP" "F RWV=RW2/RWD2+RWS2/RWSD2" "C POWER FROM VENDOR QUOTE 0.4 HP/1000 GAL, 78.8 KW/L" "F RWP=78.8E-6" "C RESIDENCE TIME 20 MINUTES, 0.333 HOURS" "F RWR=0.3333" "F RWMXP=RWV*RWP*RWR" "F CSLTV=CSLT/CSLTD+CSLTS/CSLTDS" "F CSLTP=1.97E-5" "F CSLTR=120" "F CSLMXP=CSLTV*CSLTR*CSLTP" "F DAPTV=DAPT/DAPTD+DAPTS/DAPTDS" "F DAPTP=9.85E-5" "F DAPTR=28" "F DAPMXP=DAPTV*DAPTR*DAPTP" "F WRITE(NHSTRY,'('' **** WKMIX RESULTS ****'')')" "F WRITE(NHSTRY,'('' SMMXP '',G12.5)')SMMXP" "F WRITE(NHSTRY,'('' SDMXP '',G12.5)')SDMXP" "F WRITE(NHSTRY,'('' SMV '',G12.5)')SMV" "F WRITE(NHSTRY,'('' SDV '',G12.5)')SDV" "F WRITE(NHSTRY,'('' SM '',G12.5)')SM" "F WRITE(NHSTRY,'('' SMD '',G12.5)')SMD" "F WRITE(NHSTRY,'('' SD '',G12.5)')SD" "F WRITE(NHSTRY,'('' SDD '',G12.5)')SDD" ) \ \ "READ-VARS" READ-VAR = ( OL OLD OLS OLDS XNT XNTD XNTS XNTDS HMT HMTD HMTS HMTDS SLT SLTD SLTS SLTDS SD SDD SDS SDSD SA SAD SAS SASD SM SMD SMS SMSD CSD CSDD CSDS CSDSD AB ABD ABS ABSD PM PMD PMS PMSD RW2 RWD2 RWS2 RWSD2 CSLT CSLTD CSLTS CSLTDS DAPT DAPTD DAPTS DAPTDS SSFDAY SSFVOL SSFWV CLVES CLVOL ) \ \ "WRITE-VARS" WRITE-VAR = ( SSFVES SACVES OLMXP XNTMXP HMTMXP SLTMXP SDMXP ZMMXP SAMXP SMMXP CSMXP CLMXP EQMXP PMMXP RWMXP CSLMXP DAPMXP SAR SMR ) \ \ COMMENTS COMMENTS = ( ";;" ";;" ";THIS BLOCK CALCULATES THE AGITATION REQUIREMENT FOR MIXERS" "; AND FERMENTORS. THE FOLLOWING SYMBOLISM IS USED IN THIS" ";BLOCK." "; Unless Otherwise Stated" ";OL - OVERLIMING TANK AGITATOR (A-209)" ";XNT - REACIDIFICATION TANK AGITATOR (A-224)" "; 0.5 hp/1000 gal = 9.85E-5 kW/L" "; Residence Time 4 hours" ";HMT - HYDROLYSATE MIX TANK AGITATOR (A-205)" "; 2.96E-4 kW/L=1.5 hp/1000 gal" ";SLT - SLURRYING TANK AGITATOR (A-232)" "; 2.96E-4 kW/L=1.5 hp/1000 gal" ";;" ";;" ";SD - ZYMOMONAS SEED FERMENTOR AGITATORS (A-303-305A/B&306A-F)" "; Calculate the volumetric flow to F-305 (306)" "; Calculate the volume as 10% (inoculum level)" "; 0.1 HP/1000 GAL = 1.97e-5 KW/L" "; One batch turns around each 24 hrs. So this is the effective residence ti" "; SDNU is the number of Zymo Seed trains on line at any one time" "; Calculate Power" "; Calculate Power" ";;" ";ZM - ZYMOMONAS HOLD TANK AGITATORS (A-301)" ";;" "; ZMINC=VOLUME RATIO OF SEED HOLD TO LARGEST SEED TANK" ";;" ";;" "; 0.1 HP/1000 GAL = 1.97E-5 KW/L" ";;" ";;" "; 24 hr Residence time, Same as F-305 (Largest Seed)" ";;" ";;" "; SDV (calculated earlier), volumetric flow to F-305" "; SDV*ZMR = volume of F-305" ";;" ";;" ";SA - SACCHARIFICATION TANK AGITATORS (A-310)" "; Use hp requirements of SSCF fermentors; the requirements may be higher" "; and the ferms lower when separate sacch. and fermentation" "; Calculate Volumetric Flow Rate" "; 0.15 HP/1000 GAL = 2.9549e-5 KW/L" "; SACDAY is the Sacch. residence time in days." "; Calculate the number of Sacch. tanks required for costing" ";;" ";SM - FERMENTOR AGITATORS (A-300)" "; Calculate Volumetric Flow Rate" "; 0.15 HP/1000 GAL = 2.9549e-5 KW/L" "; SSFDAY is the SSCF residence time in days." "; Calculate the number of SSCF vessels required for costing" ";;" ";BW - BEER WELL" "; Calculate Volumetric Flow" "; 0.3 HP/1000 GAL = 5.91e-5 KW/L" "; BWR is the Beer Well Residence time in hrs" ";;" ";CS - CELLULASE SEED FERMENTOR AGITATORS (A-402-3A/B)" "; 10.2 HP/1000 GAL = 1.972E-3" "; CSNU is the number of cellulase seed trains use" ";CL - CELLULASE FERMENTOR AGITATORS (A-400A-L)" ";PM - MEDIA PREP TANK AGITATOR (T-405)" ";EQ - EQUALIZATION BASIN AGITATOR (A-602)" ";RW - RECYCLE WATER TANK AGITATOR (A-530)" ";CSL - CSL STORAGE TANK AGITATOR (A-720)" "; 0.1 hp/1000 gal = 1.97E-5 kW/L (based on A-301)" "; Residence Time 120 hours (guess by AA 02/22/01)" "; (because T720 has a 120 hr residence time)" ";;" ";DAP - CSL/DAP DAY TANK AGITATOR (A-760)" "; 0.5 hp/1000 gal = 9.85E-5 kW/L (based on ?)" "; Residence Time is about 28 hours" "; CSL flow rate is 372 gph (1300 kg/hr) and T-760 is 10,000 gal" "; =>10,000/372 = 28 hours" ";;" ";;" ) \ ? CALCULATOR PUMPS ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "C EACH DIFFERENTIAL PRESURE (DP) TERM IS THE PUMP HEAD AND IS IN PSI" "C IN THE WP EQUATIONS DP IS CONVERTED TO N/M^2" "C" "C FLOWS (FMS & FCS) ARE RETRIEVED IN KG/HR & CONVERTED TO KG/S" "C DENSITIES (RMS & RCS) ARE RETRIEVED IN KG/L & CONVERTED TO KG/M^3" "C POWER IS CALCULATED IN KW (N M/S, J/S)" "C" "C CONVERT PSI * 6894.8 = N/M^2" "C CONVERT KG/HR * 1/3600 = KG/S" "C CONVERT KG/L * 1000 = KG/M^3" "C CONVERT W /1000 = KW" ) \ \ DEFINE FVN = FMP201 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 710 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP201 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 710 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP201 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 710 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP201 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 710 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP201 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP201 \ \ DEFINE FVN = STC220 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WP205 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP205 \ \ DEFINE FVN = FMP209 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 228 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP209 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 228 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP209 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 228 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP209 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 228 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = AWP209 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP209 \ \ DEFINE FVN = FMP222 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 230 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP222 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 230 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP222 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 230 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP222 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 230 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP222 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP222 \ \ DEFINE FVN = FMP211 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FCP211 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 221 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WP211 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP211 \ \ DEFINE FVN = F256 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 256 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = WP213 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP213 \ \ DEFINE FVN = FMP224 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP224 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP224 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 232 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP224 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 232 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP224 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP224 \ \ DEFINE FVN = FMP239 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 239 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP239 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 239 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP239 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 239 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP239 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 239 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP239 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP239 \ \ DEFINE FVN = FMP310 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301B FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP310 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301B FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP310 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301B FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP310 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301B FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP310 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP310 \ \ DEFINE FVN = QSAC FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QF300A \ \ DEFINE FVN = SACVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 36 \ \ DEFINE FVN = PMPSAC FVN-VARTYPE = PARAMETER FVN-PARAMNO = 40 \ \ DEFINE FVN = FMP300 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP300 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP300 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP300 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 306 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP300 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP300 \ \ DEFINE FVN = QREM FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QF300 \ \ DEFINE FVN = SSFVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 31 \ \ DEFINE FVN = PMPSSF FVN-VARTYPE = PARAMETER FVN-PARAMNO = 35 \ \ DEFINE FVN = FMP301 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP301 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP301 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP301 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP301 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP301 \ \ DEFINE FVN = WP302 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP302 \ \ DEFINE FVN = FMP306 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 502 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP306 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 502 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP306 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 502 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP306 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 502 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP306 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP306 \ \ DEFINE FVN = FMP400 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 420 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP400 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 420 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP400 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 420 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP400 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 420 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP400 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP400 \ \ DEFINE FVN = FMP401 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP401 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 433 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP401 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 433 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP401 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 433 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP401 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP401 \ \ DEFINE FVN = FMP405 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 416 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP405 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 416 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP405 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 416 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP405 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 416 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP405 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP405 \ \ DEFINE FVN = FMP420 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 417 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP420 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 417 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP420 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 417 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP420 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 417 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP420 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP420 \ \ DEFINE FVN = FMP501 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 518 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP501 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 518 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP501 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 518 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP501 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 518 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = QREB FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QRD501 \ \ DEFINE FVN = WP501 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP501 \ \ DEFINE FVN = P501GP FVN-VARTYPE = PARAMETER FVN-PARAMNO = 5 \ \ DEFINE FVN = WP503 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP503 \ \ DEFINE FVN = FMP504 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 516 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP504 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 516 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP504 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 516 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP504 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 516 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP504 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP504 \ \ DEFINE FVN = WP505 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP505 \ \ DEFINE FVN = FMP511 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 525 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP511 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 525 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP511 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 525 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP511 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 525 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP511 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP511 \ \ DEFINE FVN = FMP512 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 528 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP512 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 528 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP512 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 528 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP512 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 528 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP512 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP512 \ \ DEFINE FVN = FMP513 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP513 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 531 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP513 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP513 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 531 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP513 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP513 \ \ DEFINE FVN = FMP514 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 534A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP514 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 534A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP514 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 534A FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP514 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 534A FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP514 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP514 \ \ DEFINE FVN = FMP515 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 551 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP515 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 551 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP515 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 551 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP515 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 551 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP515 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP515 \ \ DEFINE FVN = FMP530 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 572 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP530 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 572 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP530 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 572 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP530 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 572 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP530 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP530 \ \ DEFINE FVN = FMP602 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP602 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP602 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 613 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP602 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 613 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP602 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP602 \ \ DEFINE FVN = FMP606 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP606 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP606 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 618 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP606 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 618 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP606 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP606 \ \ DEFINE FVN = FMP610 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 625 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP610 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 625 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP610 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 625 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP610 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 625 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP608 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP608 \ \ DEFINE FVN = WP610 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP610 \ \ DEFINE FVN = FMP611 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 621 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP611 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 621 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP611 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 621 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP611 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 621 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP611 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP611 \ \ DEFINE FVN = FMP614 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 627 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP614 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 627 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP614 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 627 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP614 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 627 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP614 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP614 \ \ DEFINE FVN = FMP616 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP616 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP616 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 624 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP616 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 624 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP616 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP616 \ \ DEFINE FVN = FMP701 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 515 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP701 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 515 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP701 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 515 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP701 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 515 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP701 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP701 \ \ DEFINE FVN = FMP703 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 710 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP703 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 710 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP703 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 710 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP703 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 710 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP703 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP703 \ \ DEFINE FVN = FMP706 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 717 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP706 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 717 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP706 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 717 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP706 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 717 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP706 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP706 \ \ DEFINE FVN = FMP707 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 417 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP707 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 417 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP707 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 417 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP707 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 417 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP707 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP707 \ \ DEFINE FVN = FMP708 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 723 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP708 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 723 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP708 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 723 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP708 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 723 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP708 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP708 \ \ DEFINE FVN = FMP710 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 701 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP710 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 701 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP710 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 701 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP710 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 701 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP710 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP710 \ \ DEFINE FVN = FMP720 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP720 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP720 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP720 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP720 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP720 \ \ DEFINE FVN = FMP750 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 750 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP750 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 750 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP750 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 750 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP750 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 750 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP750 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP750 \ \ DEFINE FVN = FMP760 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP760 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP760 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP760 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 735 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP760 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP760 \ \ DEFINE FVN = FMP804 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 824 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP804 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 824 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP804 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 824 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RCP804 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 824 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP804 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP804 \ \ DEFINE FVN = FMP828 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 821 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP828 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 821 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FCP828 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 821 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WP828 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP828 \ \ DEFINE FVN = RCP828 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 821 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FMP830 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 813 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RMP830 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 813 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP830 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP830 \ \ DEFINE FVN = FM902 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 940 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RM902 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 940 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FC902 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 940 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RC902 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 940 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP902 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP902 \ \ DEFINE FVN = FM912 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 904 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RM912 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 904 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FC912 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 904 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RC912 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 904 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP912 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP912 \ \ DEFINE FVN = FM914 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 905 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RM914 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 905 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FC914 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 905 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RC914 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 905 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WP914 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP914 \ \ FORTRAN FORTRAN-EXEC = ( "C EPM IS THE PUMP EFFICIENCIES" "C EEL IS THE MOTOR EFFICIENCIES" "F EPM = 0.60" "F EEL = 0.95" "C 250 FT. HEAD OF SULFURIC ACID (DENS. 1.8)= 191.1 PSI" "F DP201 =191.1" "F AP201 =(FMP201/3600.)/(RMP201*1000.)+(FCP201/3600.)/(RCP201*1000.)" "F WP201 =(AP201 * (DP201*6894.8) / (EPM*EEL) ) / 1000." "C POWER BASED ON THE SOLIDS FLOW OF STREAM 220" "C" "F HF = 3.33E-3" "F WP205 = HF * STC220" "C 150 FT. HEAD = 65 PSI" "F DP209 = 65.0" "F AP209 =(FMP209/3600.)/(RMP209*1000.)+(FCP209/3600.)/(RCP209*1000.)" "F AWP209 =(AP209 * (DP209*6894.8) / (EPM*EEL) ) / 1000." "C 150 FT. HEAD = 65 PSI" "F DP222 = 65.0" "F AP222 =(FMP222/3600.)/(RMP222*1000.)+(FCP222/3600.)/(RCP222*1000.)" "F WP222 =(AP222 * (DP222*6894.8) / (EPM*EEL) ) / 1000." "C POWER BASED ON THE TOTAL FLOW OF 221" "C" "F HP211 = 1.03E-4" "F WP211 = HP211 * (FMP211 + FCP211)" "C POWER BASED ON THE TOTAL FLOW OF 256" "C" "F HP213 = 1.70E-3" "F WP213 = HP213 * F256" "C P-224 IS A ROTARY LOBE PUMP, SO THE POWER REQ. IS NOT CALCULATED" "C LIKE A CENTRIFUGAL PUMP. IT HAS AN INPUT OF 1.231E-2 KW/ L/MIN" "C (50 HP/800 GPM)" "F PP224=1.231E-2" "F AP224 =(FMP224/60.)/(RMP224)+(FCP224/60.)/(RCP224)" "F WP224 =AP224 * PP224" "C 100 FT HEAD = 43.4" "F DP239 = 43.4" "F AP239 =(FMP239/3600.)/(RMP239*1000.)+(FCP239/3600.)/(RCP239*1000.)" "F WP239 =(AP239 * (DP239*6894.8) / (EPM*EEL) ) / 1000." "F DELTAT = 2.0" "F CPMIX = 1.0" "F CPCI = 1.0" "F FRCMIX = FMP310/(FMP310+FCP310)" "F FRCCI = 1-FRCMIX" "C PMPSAC IS FIRST CALCULATED IN G/SEC" "F PMPSAC = QSAC / (DELTAT * (FRCMIX * CPMIX + FRCCI * CPCI))" "F WRITE(NHSTRY,*)' PMPSAC1: ',PMPSAC" "F FRWFLW = (FMP310 + FCP310) / 3." "F RECFLW = (PMPSAC*3600/1000) / SACVES" "F PMPSAC = ( RECFLW + FRWFLW ) * SACVES" "F DP310 = 60.0" "F AP310 =(PMPSAC*FRCMIX/3600.)/(RMP310*1000.)" "F AP310 =AP310+(FCP310*(1-FRCMIX)/3600.)/(RCP310*1000.)" "F WP310 =(AP310 * (DP310*6894.8) / (EPM*EEL) ) / 1000." "F WRITE(NHSTRY,*)' QSAC: ',QSAC" "F WRITE(NHSTRY,*)' SACVES: ',SACVES" "F WRITE(NHSTRY,*)' FMP310: ',FMP310" "F WRITE(NHSTRY,*)' RMP310: ',RMP310" "F WRITE(NHSTRY,*)' FCP310: ',FCP310" "F WRITE(NHSTRY,*)' RCP310: ',RCP310" "F WRITE(NHSTRY,*)' WP310: ',WP310" "F WRITE(NHSTRY,*)' PMPSAC: ',PMPSAC" "F WRITE(NHSTRY,*)' FRWFLW: ',FRWFLW" "F WRITE(NHSTRY,*)' RECFLW: ',RECFLW" "F DELTAT = 2.0" "F CPMIX = 1.0" "F CPCI = 1.0" "F FRCMIX = FMP300/(FMP300+FCP300)" "F FRCCI = 1-FRCMIX" "C PMPSSF IS FIRST CALCULATED IN G/SEC" "F PMPSSF = QREM / (DELTAT * (FRCMIX * CPMIX + FRCCI * CPCI))" "F WRITE(NHSTRY,*)' PMPSSF1: ',PMPSSF" "F FRWFLW = (FMP300 + FCP300) / 3." "F RECFLW = (PMPSSF*3600/1000) / SSFVES" "F PMPSSF = ( RECFLW + FRWFLW ) * SSFVES" "F DP300 = 60.0" "F AP300 =(PMPSSF*FRCMIX/3600.)/(RMP300*1000.)" "F AP300 =AP300+(FCP300*(1-FRCMIX)/3600.)/(RCP300*1000.)" "F WP300 =(AP300 * (DP300*6894.8) / (EPM*EEL) ) / 1000." "F WRITE(NHSTRY,*)' QREM: ',QREM" "F WRITE(NHSTRY,*)' SSFVES: ',SSFVES" "F WRITE(NHSTRY,*)' FMP300: ',FMP300" "F WRITE(NHSTRY,*)' RMP300: ',RMP300" "F WRITE(NHSTRY,*)' FCP300: ',FCP300" "F WRITE(NHSTRY,*)' RCP300: ',RCP300" "F WRITE(NHSTRY,*)' WP300: ',WP300" "F WRITE(NHSTRY,*)' PMPSSF: ',PMPSSF" "F WRITE(NHSTRY,*)' FRWFLW: ',FRWFLW" "F WRITE(NHSTRY,*)' RECFLW: ',RECFLW" "C P-301 & P-302 ARE ROTARY LOBE PUMPS, SO THE POWER REQ. NOT CALCULATED" "C LIKE A CENTRIFUGAL PUMP. IT HAS AN INPUT OF 2.462E-2 KW/ L/MIN" "C (100 HP/800 GPM)" "C P-302 IS A LARGER PUMP, BUT DOESN'T RUN ALL OF THE TIME. ON THE" "C AVERAGE IT IS THE SAME AS P-301" "F PP301 = 2.462E-2" "F AP301 = (FMP301/60.)/(RMP301)+(FCP301/60.)/(RCP301)" "F WP301 = AP301 * PP301" "F WP302 = WP301" "F DP306 = 73.7" "F AP306 =(FMP306/3600.)/(RMP306*1000.)+(FCP306/3600.)/(RCP306*1000.)" "F WP306 =(AP306 * (DP306*6894.8) / (EPM*EEL) ) / 1000." "F DP400 = 43.3" "F AP400 =(FMP400/3600.)/(RMP400*1000.)+(FCP400/3600.)/(RCP400*1000.)" "F WP400 =(AP400 * (DP400*6894.8) / (EPM*EEL) ) / 1000." "C P-401 IS A ROTARY LOBE PUMP, SO THE POWER REQ. IS NOT CALCULATED" "C LIKE A CENTRIFUGAL PUMP. IT HAS AN INPUT OF 1.77E-2 KW/ L/MIN" "C (6.5 HP/72.5 GPM PER DELTA T)" "F PP401 = 1.77E-2" "F AP401 =(FMP401/60.)/(RMP401)+(FCP401/60.)/(RCP401)" "F WP401 =AP401 * PP401" "F DP405 = 44.3" "F AP405 =(FMP405/3600.)/(RMP405*1000.)+(FCP405/3600.)/(RCP405*1000.)" "F WP405 =(AP405 * (DP405*6894.8) / (EPM*EEL) ) / 1000." "C 33 PSI = 75 FT. HEAD" "F DP420 = 33" "F AP420 =(FMP420/3600.)/(RMP420*1000.)+(FCP420/3600.)/(RCP420*1000.)" "F WP420 =(AP420 * (DP420*6894.8) / (EPM*EEL) ) / 1000." "C" "C PUMP FLOW = RECIRC FLOW + BOTTOMS FLOW" "C BOTTOMS FLOW = STREAM 518" "C RECIRC FLOW(GPM)=QRD501(BTU/HR)/1.21E8(BTU/HR)*3827 GPM(FROM DELTA-T)" "C" "C FLOW OF 518 IN M^3/S" "F AP501 =(FMP501/3600.)/(RMP501*1000.)+(FCP501/3600.)/(RCP501*1000.)" "C FLOW OF 518 IN GPM" "F GP501 = AP501 * 15850.45" "C QRD501 IN BTU/HR" "F QBTU = -(QREB * 14.2869)" "C RECIRC FLOW IN GPM" "F GPMREC = (QBTU / 1.21E8) * 3827." "C RECIRC FLOW IN M^3/S" "F APREC = GPMREC / 15850.45" "F WRITE(NHSTRY,*)' AP501 = ',AP501,' GP501 = ',GP501,' QBTU = ',QBTU" "F WRITE(NHSTRY,*)' GPMREC = ',GPMREC,' APREC = ',APREC" "C TOTAL FLOW" "F AP501 = AP501 + APREC" "F P501GP = AP501 * 15850.45" "C 67.5 PSI=150 FT HEAD" "F DP501 = 67.5" "F WP501 =(AP501 * (DP501*6894.8) / (EPM*EEL) ) / 1000." "F WRITE(NHSTRY,*)' AP501 = ',AP501,' WP501 = ',WP501" "F WRITE(NHSTRY,*)' P501GP = ',P501GP" "C 60.7 PSI = 140 FT HEAD" "F DP503 = 60.7" "C ASSUME FLOW IS 2500 KG/HR & DENSITY IS 1KG/L" "F AP503 =(2500/3600.)/(1.*1000.)" "F WP503 =(AP503 * (DP503*6894.8) / (EPM*EEL) ) / 1000." "C 66 PSI = 155 FT. HEAD" "F DP504 = 66." "F AP504 =(FMP504/3600.)/(RMP504*1000.)+(FCP504/3600.)/(RCP504*1000.)" "F WP504 =(AP504 * (DP504*6894.8) / (EPM*EEL) ) / 1000." "F WRITE(NHSTRY,71)AP504,WP504" "F 71 FORMAT('MISC RESULTS',/," "F 1 'AP504=',G12.5,/," "F 2 'WP504=',G12.5)" "C 47.5 PSI = 109.5 FT. HEAD" "F DP505 = 47.5" "C ASSUME FLOW IS 80000 KG/HR AND DENSITY IS 1KG/L" "F AP505 =(80000/3600.)/(1*1000.)" "F WP505 =(AP505 * (DP505*6894.8) / (EPM*EEL) ) / 1000." "C 47.7 PSI = 110 FT. HEAD" "F DP511 = 47.7" "F AP511 =(FMP511/3600.)/(RMP511*1000.)+(FCP511/3600.)/(RCP511*1000.)" "C RECIRCULATION RATIO = 3" "F AP511 = AP511 * (3. + 1.)" "F WRITE(NHSTRY,*)' AP511 = ',AP511" "F WP511 =(AP511 * (DP511*6894.8) / (EPM*EEL) ) / 1000." "C 47.7 PSI = 110 FT. HEAD" "F DP512 = 47.7" "F AP512 =(FMP512/3600.)/(RMP512*1000.)+(FCP512/3600.)/(RCP512*1000.)" "C RECIRCULATION RATIO = 1.9" "F AP512 = AP512 * (1.9 + 1.)" "F WRITE(NHSTRY,*)' AP512 = ',AP512" "F WP512 =(AP512 * (DP512*6894.8) / (EPM*EEL) ) / 1000." "C 47.7 PSI = 110 FT. HEAD" "F DP513 = 47.7" "F AP513 =(FMP513/3600.)/(RMP513*1000.)+(FCP513/3600.)/(RCP513*1000.)" "C RECIRCULATION RATIO = 3" "F AP513 = AP513 * (3. + 1.)" "F WRITE(NHSTRY,*)' AP513 = ',AP513" "F WP513 =(AP513 * (DP513*6894.8) / (EPM*EEL) ) / 1000." "C 47.7 PSI = 110 FT. HEAD" "F DP514 = 47.7" "F AP514 =(FMP514/3600.)/(RMP514*1000.)+(FCP514/3600.)/(RCP514*1000.)" "F WP514 =(AP514 * (DP514*6894.8) / (EPM*EEL) ) / 1000." "C 47.7 PSI = 110 FT. HEAD" "F DP515 = 47.7" "F AP515 =(FMP515/3600.)/(RMP515*1000.)+(FCP515/3600.)/(RCP515*1000.)" "F WP515 =(AP515 * (DP515*6894.8) / (EPM*EEL) ) / 1000." "C 68 PSI = 150 FT HEAD" "F DP530 = 68." "F AP530 =(FMP530/3600.)/(RMP530*1000.)+(FCP530/3600.)/(RCP530*1000.)" "F WP530 =((AP530) * (DP530*6894.8) / (EPM*EEL) ) / 1000." "C 68 PSI = 150 FT. HEAD" "F DP602 = 68." "F AP602 =(FMP602/3600.)/(RMP602*1000.)+(FCP602/3600.)/(RCP602*1000.)" "F WP602 =(AP602 * (DP602*6894.8) / (EPM*EEL) ) / 1000." "C 68 PSI = 150 FT HEAD" "F DP606 = 68." "F AP606 =(FMP606/3600.)/(RMP606*1000.)+(FCP606/3600.)/(RCP606*1000.)" "F WP606 =(AP606 * (DP606*6894.8) / (EPM*EEL) ) / 1000." "C FAC608 IS THE RECYCLE RATIO ON STREAM 625" "F FAC608 = 1." "C 68 PSI = 150 FT. HEAD" "F DP608 = 68." "F AP608 =(FMP610/3600.)/(RMP610*1000.)+(FCP610/3600.)/(RCP610*1000.)" "F WP608 =(FAC608 * AP608 * (DP608*6894.8) / (EPM*EEL) ) / 1000." "C 40 PSI = 92 FT. HEAD" "F DP610 = 40." "F AP610 =(FMP610/3600.)/(RMP610*1000.)+(FCP610/3600.)/(RCP610*1000.)" "F WP610 =(AP610 * (DP610*6894.8) / (EPM*EEL) ) / 1000." "F DP611 = 68.0" "F AP611 =(FMP611/3600.)/(RMP611*1000.)+(FCP611/3600.)/(RCP611*1000.)" "F WP611 =(AP611 * (DP611*6894.8) / (EPM*EEL) ) / 1000." "F WRITE(NHSTRY,*)'AP611=',AP611,'WP611=',WP611" "F DP614 = 68.0" "F AP614 =(FMP614/3600.)/(RMP614*1000.)+(FCP614/3600.)/(RCP614*1000.)" "F WP614 =(AP614 * (DP614*6894.8) / (EPM*EEL) ) / 1000." "F DP616 = 68." "F AP616 =(FMP616/3600.)/(RMP616*1000.)+(FCP616/3600.)/(RCP616*1000.)" "F WP616 =(AP616 * (DP616*6894.8) / (EPM*EEL) ) / 1000." "C 49 PSI = 112 FT HEAD" "F DP701 = 49." "F AP701 =(FMP701/3600.)/(RMP701*1000.)+(FCP701/3600.)/(RCP701*1000.)" "F WP701 =(AP701 * (DP701*6894.8) / (EPM*EEL) ) / 1000." "C 65. PSI = 150 FT HEAD" "F DP703 = 65." "F AP703 =(FMP703/3600.)/(RMP703*1000.)+(FCP703/3600.)/(RCP703*1000.)" "F WP703 =(AP703 * (DP703*6894.8) / (EPM*EEL) ) / 1000." "C 10 PSI = 22 FT HEAD" "F DP706 = 10." "F AP706 =(FMP706/3600.)/(RMP706*1000.)+(FCP706/3600.)/(RCP706*1000.)" "F WP706 =(AP706 * (DP706*6894.8) / (EPM*EEL) ) / 1000." "C 39 PSI = 90 FT HEAD" "F DP707 = 39." "F AP707 =(FMP707/3600.)/(RMP707*1000.)+(FCP707/3600.)/(RCP707*1000.)" "F WP707 =(AP707 * (DP707*6894.8) / (EPM*EEL) ) / 1000." "C 51.6 PSI = 119 FT HEAD" "F DP708 = 0.0" "F AP708 =(FMP708/3600.)/(RMP708*1000.)+(FCP708/3600.)/(RCP708*1000.)" "F WP708 =(AP708 * (DP708*6894.8) / (EPM*EEL) ) / 1000." "C 86.7 PSI = 200 FT HEAD" "F DP710 = 86.7" "F AP710 =(FMP710/3600.)/(RMP710*1000.)+(FCP710/3600.)/(RCP710*1000.)" "F WP710 =(AP710 * (DP710*6894.8) / (EPM*EEL) ) / 1000." "C 65 PSI = 150 FT HEAD" "F DP720 = 65." "F AP720 =(FMP720/3600.)/(RMP720*1000.)+(FCP720/3600.)/(RCP720*1000.)" "F WP720 =(AP720 * (DP720*6894.8) / (EPM*EEL) ) / 1000." "C 21.7 PSI = 50 FT HEAD" "F DP750 = 21.7" "F AP750 =(FMP750/3600.)/(RMP750*1000.)+(FCP750/3600.)/(RCP750*1000.)" "F WP750 =(AP750 * (DP750*6894.8) / (EPM*EEL) ) / 1000." "C 65 PSI = 150 FT HEAD" "F DP760 = 65." "F AP760 =(FMP760/3600.)/(RMP760*1000.)+(FCP760/3600.)/(RCP760*1000.)" "F WP760 =(AP760 * (DP760*6894.8) / (EPM*EEL) ) / 1000." "C 65 PSI = 150 FT HEAD" "F DP804 = 65." "F AP804 =(FMP804/3600.)/(RMP804*1000.)+(FCP804/3600.)/(RCP804*1000.)" "F WP804 =(AP804 * (DP804*6894.8) / (EPM*EEL) ) / 1000." "C 65 PSI = 150 FT HEAD" "F DP828 = 65" "F AP828 =(FMP828/3600.)/(RMP828*1000.)+(FCP828/3600.)/(RCP828*1000.)" "F WP828 =(AP828 * (DP828*6894.8) / (EPM*EEL) ) / 1000." "C FR830 IS THE RATIO OF HYDRAZINE FLOW TO STREAM 813 (0.001 IS A GUESS)" "F FR830=0.001" "C 33 PSI = 75 FT HEAD" "F DP830 = 33." "F AP830 =(FR830*FMP830/3600.)/(RMP830*1000.)" "F WP830 =(AP830 * (DP830*6894.8) / (EPM*EEL) ) / 1000." "C 30 PSI = 70 FT HEAD" "F DP902 = 30." "F AP902=(FM902/3600.)/(RM902*1000.)" "F & +(FC902/3600.)/(RC902*1000.)" "F WP902=(AP902 * (DP902*6894.8) / (EPM*EEL) ) / 1000." "C 33 PSI = 75 FT HEAD" "F DP912 = 33." "F AP912=(FM912/3600.)/(RM912*1000.)" "F & +(FC912/3600.)/(RC912*1000.)" "F WP912=(AP912 * (DP912*6894.8) / (EPM*EEL) ) / 1000." "C 65 PSI = 150 FT HEAD" "F DP914 = 65." "F AP914=(FM914/3600.)/(RM914*1000.)" "F & +(FC914/3600.)/(RC914*1000.)" "F WP914=(AP914 * (DP914*6894.8) / (EPM*EEL) ) / 1000." ) \ \ "READ-VARS" READ-VAR = ( SSFVES QREB FMP201 RMP201 FCP201 RCP201 STC220 F256 FMP209 RMP209 FCP209 RCP209 FMP222 RMP222 FCP222 RCP222 FMP224 RMP224 FCP224 RCP224 FMP211 FCP211 FMP239 RMP239 FCP239 RCP239 FMP310 RMP310 FCP310 RCP310 FMP300 RMP300 FCP300 RCP300 FMP301 RMP301 FCP301 RCP301 FMP400 RMP400 FCP400 RCP400 FMP405 RMP405 FCP405 RCP405 FMP420 RMP420 FCP420 RCP420 FMP501 RMP501 FCP501 RCP501 FMP504 RMP504 FCP504 RCP504 FMP511 RMP511 FCP511 RCP511 FMP512 RMP512 FCP512 RCP512 FMP513 RMP513 FCP513 RCP513 FMP514 RMP514 FCP514 RCP514 FMP515 RMP515 FCP515 RCP515 FMP530 RMP530 FCP530 RCP530 FMP602 RMP602 FCP602 RCP602 FMP606 RMP606 FCP606 RCP606 FMP610 RMP610 FCP610 RCP610 FMP614 RMP614 FCP614 RCP614 FMP616 RMP616 FCP616 RCP616 FMP701 RMP701 FCP701 RCP701 FMP703 RMP703 FCP703 RCP703 FMP706 RMP706 FCP706 RCP706 FMP707 RMP707 FCP707 RCP707 FMP708 RMP708 FCP708 RCP708 FMP710 RMP710 FCP710 RCP710 FMP720 RMP720 FCP720 RCP720 FMP750 RMP750 FCP750 RCP750 FMP760 RMP760 FCP760 RCP760 FMP804 RMP804 FCP804 RCP804 FMP828 RMP828 FCP828 RCP828 FMP830 RMP830 FM902 RM902 FC902 RC902 FM912 RM912 FC912 RC912 FM914 RM914 FC914 RC914 ) \ \ "WRITE-VARS" WRITE-VAR = ( WP201 WP205 AWP209 WP211 WP222 WP224 WP239 WP213 WP300 WP301 WP302 WP306 WP310 WP400 WP405 WP420 WP501 WP503 WP504 WP505 WP511 WP512 WP513 WP514 WP515 WP530 WP602 WP606 WP608 WP610 WP614 WP616 WP701 WP703 WP706 WP707 WP708 WP710 WP720 WP750 WP760 WP804 WP828 WP830 WP902 WP912 WP914 P501GP PMPSSF PMPSAC ) \ \ COMMENTS COMMENTS = ( "; EXECUTE BEFORE PUMPS" ";;" ";;" "; Calculates the electrical work required by each pump not specifically" "; simulated." ";;" "; P-201 Sulfuric Acid Pump" "; P-205 Pneumapress Feed Pumps" ";;" "; Power Required from Harris design (300 hp at 75% power)" "; equals 225 hp / Flow from R0101C (see equip design" "; sheet)" "; Power Required 225 hp / 50299 kg/hr CISOLIDS flow = 4.47E-3 hp/kg/hr" "; = 3.33E-3 kW/kg/hr" ";;" "; P-209 Overlimed Hydrolysate Pump" "; P-222 Overlimed Hydrolysate Liquor Pump" "; P-211 Concentrated Filtrate Pumps" ";;" "; Power Required from Harris design (25 hp at 75% power)" "; equals 18.8 hp / Flow from R0101C (see equip design" "; sheet)" "; Power Required 18.8 hp / 136350 kg/hr CISOLIDS flow = 1.38E-4 hp/kg/hr" "; = 1.03E-4 kW/kg/hr" ";;" "; P-213 Wash Filtrate Pump #2" ";;" "; Power Required from Harris design (400 hp at 75% power)" "; equals 300.0 hp / Flow from R0101C (see equip design" "; sheet)" "; Power Required 300.0 hp / 131530 kg/hr CISOLIDS flow = 2.28E-3 hp/kg/hr" "; = 1.70E-3 kW/kg/hr" ";;" "; P-224 Fermentation Feed Pump" "; P-239 Reacidified Liquor Pump" "; P-310 Saccharified Slurry Transfer Pump" "; Using same parameters as fermentation (SSF) transfer pump" ";;" "; Calculate the pump-around flow to cool Saccharified Slurry" "; DELTAT=temperature decrease of slurry in heat exchanger" "; CPMIX=heat capacity of mixed stream (cal / g C)" "; CPCI=heat capacity of CI solid stream (cal /g C)" "; FRCMIX =mixed fraction of 301B" "; FRCCI = CI solids fraction of 301B" "; PMPSAC = Pumparound flow rate for Saccharification (same as SSCF)" "; SACVES = Number of Sacch. tanks from common block" "; RECFKW = Individual Pump Recirculation Flow" "; FRDFLW = Individual pump forward flow" ";;" "; Three parallel trains (approximately)" "; Calculate the forward flow through each train" "; Individual Pump Recirculation Flow (divided by total number of pumps)" "; Total Pump Flow" "; 138.6 FT. HEAD = 60 PSI" "; P-300 SSCF Transfer Pump" ";;" "; Calculate the pump-around flow to cool SSCF broth" "; DELTAT=temperature decrease of broth in heat exchanger" "; CPMIX=heat capacity of mixed stream (cal / g C)" "; CPCI=heat capacity of CI solid stream (cal /g C)" "; FRCMIX =mixed fraction of 306" "; FRCCI = CI solids fraction of 306" "; PMPSSF = Pumparound flow rate for SSCF" "; SSFVES = Number of SSF vessels from common block" "; RECFKW = Individual Pump Recirculation Flow" "; FRDFLW = Individual pump forward flow" ";;" "; Three parallel trains (approximately)" "; Calculate the forward flow through each train" "; Individual Pump Recirculation Flow (divided by total number of pumps)" "; Total Pump Flow" "; 138.6 FT. HEAD = 60 PSI" "; P-301 SSCF Seed Transfer Pump" "; P-306 Beer Transfer Pump" "; 170 FT = 73.7 PSI" ";;" "; P-400 Cellulase Transfer Pump" "; 43.3 psi=100.0 ft head" "; P-401 Cellulase Seed Transfer Pump" ";;" "; P-405 Media Pump" "; 44.3 psi=100 ft head" "; P-420 Antifoam Pump" "; P-501 Beer Column Bottoms Pump" "; P-503 Beer Column Reflux Pump" "; DEFINE FP503B STREAM-VAR STRM=PS506 SUBSTREAM=CISOLID VAR=MASS-FLOW" "; DEFINE RP503B STREAM-VAR STRM=PS506 SUBSTREAM=CISOLID VAR=MASS-DENSITY" "; P-504 Rectification Column Bottoms Pump" "; P-505 Rectification Column Reflux Pump" "; DEFINE FMP505 STREAM-VAR STRM=PS511 SUBSTREAM=MIXED VAR=MASS-FLOW" "; DEFINE RMP505 STREAM-VAR STRM=PS511 SUBSTREAM=MIXED VAR=MASS-DENSITY" "; P-511 1st Effect Pump" "; P-512 2ND Effect Pump" "; P-513 3RD Effect Pump" "; P-514 CONDENSATE Pump" "; P-515 Scrubber Bottoms Pump" "; P-530 Recycle Water Pump" "; P-602 Anaerobic Digester Feed Pump" "; P-606 Aerobic Digester Feed Pump" "; P-608 Return Activated Sludge pump" "; P-610 Waste Activated Sludge Pump" "; P-611 Clarifier feed Pump" "; P-614 Filtrate/Wash Recycle Pump" "; P-616 Potable Water Pump" "; 68 psi = 150 ft. head" "; P-701 Ethanol Product Pump" "; P-703 Sulfuric Acid Pump" ";; P-704 Firewater Pump -- Commented out, because it does not run regularly" "; DEFINE FMP704 STREAM-VAR STRM=713 SUBSTREAM=MIXED VAR=MASS-FLOW" "; DEFINE RMP704 STREAM-VAR STRM=713 SUBSTREAM=MIXED VAR=MASS-DENSITY" "; DEFINE FCP704 STREAM-VAR STRM=713 SUBSTREAM=CISOLID VAR=MASS-FLOW" "; DEFINE RCP704 STREAM-VAR STRM=713 SUBSTREAM=CISOLID VAR=MASS-DENSITY" "; DEFINE WP704 INFO-VAR STRM=WP704 INFO=WORK VAR=POWER" ";c 36 psi = 82 ft head" ";F DP704 = 36." ";F AP704 =(FMP704/3600.)/(RMP704*1000.)+(FCP704/3600.)/(RCP704*1000.)" ";F WP704 =(AP704 * (DP704*6894.8) / (EPM*EEL) ) / 1000." "; P-706 Ammonia Pump" "; P-707 Antifoam Pump" "; P-708 Diesel Pump (no longer needed because it's a propane tank now)" ";F DP708 = 51.6" "; P-710 Gasoline Pump" "; P-720 CSL Pump" "; P-750 Cellulase Enzyme Pump" "; P-760 CSL/DAP Pump" "; P-804 Condensate Pump" "; P-828 Blowdown Pump" "; P-830 Hydrazine addition - flow set as 0.001 of 813" "; P-902 Cooling Water Pump" "; P-912 Makeup Water Pump" "; P-914 Process Water Circulating Pump" ) \ ? CALCULATOR RADUACC ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F COMMON / HEATIN / BTUTOT" ) \ \ DEFINE FVN = QTOT FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QM803T \ \ DEFINE FVN = HTLOSS FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = QCOMSPLT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = QCOMLOSS \ \ FORTRAN FORTRAN-EXEC = ( "C" "F UNACC = 0.003" "F RADI = 0.003" "F XMM = 0.01" "C UNACC ARE THE UNACCOUNTED LOSSES" "C RADI ARE THE RADIANT LOSSES" "C XMM IS THE MANUFACTURER'S MARGIN" "C ALL ARE %S OF TOTAL HEAT TO THE BOILER" "C AND ARE BASED ON THE FWEC QUOTE 10/26/98" "C" "F TLOSS = (UNACC + RADI + XMM)*(BTUTOT*1E6)" "C" "C CALCULATE THE HEAT FROM THE BOILER BEFORE THESE LOSSES" "C IN BTU/HR" "C" "F QOUT = QTOT*3600.*3.968E-3" "C 3600 S/H AND 3.968E-3 BTU/CAL" "C" "F HTLOSS = TLOSS/QOUT" "C" "F WRITE(NHSTRY,*)'HTLOSS= ',HTLOSS" ) \ \ "READ-VARS" READ-VAR = ( QTOT ) \ \ "WRITE-VARS" WRITE-VAR = ( HTLOSS ) \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CALCULATOR REACID ? ; "SET1_MOLE" ; \ DEFINE FVN = CA228 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 228 FVN-SUBS = CISOLID FVN-COMPONEN = CAH2O2 \ \ DEFINE FVN = HS228 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 228 FVN-SUBS = MIXED FVN-COMPONEN = H2SO4 \ \ DEFINE FVN = FL233 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 233 FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "F FL233=CA228-HS228" "F IF (FL233.LT.0) FL233=0" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = T224 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CALCULATOR RECCOND ? ; "SET1_MOLE" ; \ DEFINE FVN = FDV1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 105 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CI1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 214A FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SSL1 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 214A FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = EXT1 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 214A FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PRO1 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 214A FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = STV1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 215 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = STV2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 216 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = ACV1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 212 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FDV2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FDS2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SSL2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = EXT2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = PRO2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = AV1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = E501SPT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 211 \ \ DEFINE FVN = DRTSEP FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = C103B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 104B \ \ DEFINE FVN = EVPSEP FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M104LOSS FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 103 \ \ DEFINE FVN = WAT102 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = E501SPT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 102 \ \ FORTRAN FORTRAN-EXEC = ( "C" "C WSHCNC: SOLIDS CONCENTRATION AFTER WASHING (IN 105)" "C 65% FROM HARRIS SUB (ACO-9-29067-01) REPORT 99-10600/13 P 4 GIVES" "C RANGE OF 0.6-0.7" "F WSHCNC = 0.65" "F CVW = (FDS2 + SSL2 + EXT2 + PRO2) / WSHCNC" "C" "C DRT: FRACTION OF INCOMING FEEDSTOCK THAT IS DIRT" "C WE DO NOT MODEL/TRACK THE DIRT; HOWEVER, WATER IS LOST WITH DIRT" "C SEPARATION AND DISPOSAL" "C 1% SEEMS REASONABLE IN THE NEAR TERM (D. TEMPLETON & J. FARMER 6 NOV 00)" "C DRTCNC: FRACTION DIRT IN DIRT DISPOSAL STREAM (REMAINDER IS WATER)" "C 50% FROM HARRIS ESTIMATION (J. LUKAS EMAIL 16 OCT 00)" "F DRT = 0.01" "F DRTCNC = 0.5" "F DRTSEP = DRT * (FDV2 + FDS2) * ((1.-DRTCNC)/DRTCNC)" "C" "C WATFLO: TOTAL WATER FLOW FOR WASHING INCLUDES RECYCLE" "C 5000 GPM (1,140,000 KG/HR) FOR STANDARD SIZE FACILITY (2000 DRY" "C METRIC TONNE / DAY @ 15% MOISTURE = 98040 KG/HR)" "C EVPLOS: EVAPORATION AND WINDAGE LOSS AS FRACTION OF TOTAL WATER FLOW" "C 1% FROM HARRIS ESTIMATION (J. LUKAS EMAIL 16 OCT 00)" "F WATFLO = 1140000 * (FDV2 + FDS2)/98040" "F EVPLOS = 0.01" "F EVPSEP = EVPLOS * WATFLO" "C" "C WAT102: RECYCLE WATER FLOW (102)" "F WAT102 = (CVW - FDV2 - FDS2) + DRTSEP + EVPSEP" "C" "C CONC1: SOLIDS CONCENTRATION IN REACTOR, STREAMS 215A + 216" "C" "F CONC1 = 0.30" "F CV1 = ((1.-CONC1)/CONC1) * (CI1 + SSL1 + EXT1 + PRO1)" "C" "C AV1 RECYCLE WATER FLOW (STREAM 211)" "C" "F AV1 = CV1 - STV1 - STV2 - ACV1 - ( FDV1 - SSL1 - EXT1 - PRO1 )" "C" "F CNC1A = CI1 / (CV1 + CI1 + STV1)" "F CNC1 = CI1 / (CV1 + CI1 + STV1 + STV2)" ) \ \ "READ-VARS" READ-VAR = ( CI1 STV1 STV2 ACV1 FDV2 FDS2 SSL2 FDV1 ) \ \ "WRITE-VARS" WRITE-VAR = ( DRTSEP EVPSEP WAT102 AV1 ) \ \ COMMENTS COMMENTS = ( ";;" ";;" "; DEFINE VARIABLES FOR RECYCLE WATER STREAM #1. THIS STREAM" "; CONTROLS THE SOLIDS CONCENTRATION IN THE IMPREGNATOR." ";;" ) \ ? CALCULATOR RECYCLE ? ; "SET1_MOLE" ; \ DEFINE FVN = FWAT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 574 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RWAT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 573 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RWT3 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 516 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RV2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RI2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 219 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RGLU FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = RXYE FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = RSSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = RARS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = RGAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = RMAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = RCSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = RCNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = RWNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = RGLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = RCLB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = RXYO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = RMAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = RGAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = RARO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = RACO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = RLGS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = REXT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = RPRO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = HF1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = HS1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 232 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = HGLU FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = HXYE FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = HSSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = HARS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = HGAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = HMAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = HCSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = HCNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = HWNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = HGLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = HCLB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = HXYO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = HMAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = HGAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = HARO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = HACO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = HLGS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = HEXT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = HPRO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = CFF1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CFS1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 401 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CFGLU FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = CFXYE FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = CFSSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = CFARS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = CFGAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = CFMAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = CFCSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = CFCNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = CFWNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = CFGLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CFCLB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = CFXYO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = CFMAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = CFGAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = CFARO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = CFACO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = CFLGS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = CFEXT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = CFPRO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = CPF1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CPS1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 422 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CPGLU FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = CPXYE FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = CPSSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = CPARS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = CPGAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = CPMAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = CPCSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = CPCNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = CPWNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = CPGLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = CPCLB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = CPXYO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = CPMAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = CPGAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = CPARO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = CPACO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = CPLGS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = CPEXT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = CPPRO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = DPF1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 311 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = DPS1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 311 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = DPDAP FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 311 FVN-SUBS = MIXED FVN-COMPONEN = DAP \ \ DEFINE FVN = CLF1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 311A FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CLS1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 311A FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CLCSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 311A FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = EZF1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = EZS1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 312 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = EZGLU FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = EZXYE FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = EZSSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = EZARS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = EZGAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = EZMAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = EZCSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = EZCNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = EZWNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = EZGLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = EZCLB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = EZXYO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = EZMAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = EZGAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = EZARO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = EZACO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = EZLGS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = EZEXT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = EZPRO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = SFF1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SFS1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 303 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SFGLU FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = SFXYE FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = SFSSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = SFARS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = SFGAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = SFMAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = SFCSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = SFCNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = SFWNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = SFGLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = SFCLB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = SFXYO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = SFMAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = SFGAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = SFARO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = SFACO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = SFLGS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = SFEXT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = SFPRO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = SPF1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SPS1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 304 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SPGLU FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = SPXYE FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = SPSSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = SPARS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = SPGAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = SPMAS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = SPCSL FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = SPCNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = SPWNT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = SPGLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = SPCLB FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = SPXYO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = SPMAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = SPGAO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = SPARO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = SPACO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = SPLGS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = SPEXT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = SPPRO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = CV3 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 403 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CI3 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 403 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RI3 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 430 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = ST3X FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 403 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = ST3C FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 403 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = R3X FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 430 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = R3C FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 430 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = CV4 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 410 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CI4 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 410 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = RI4 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 411 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = ST4C FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 410 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = R4C FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 411 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = F2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = RWSPLT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 219 \ \ DEFINE FVN = F3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = RWSPLT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 430 \ \ DEFINE FVN = HP1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = HPS1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C CSLCONC IS THE SOLIDS CONCENTRATION OF CSL" "F CSLCONC=0.5" "C AV2: RECYCLE WATER FLOW (STREAM 219)" "C CONC2: TOTAL SOLIDS CONC GOING TO FERMENTATION (STREAM 232)" "C (INCLUDES SUGARS + SOLSLDS)" "C SLDXXX: TOTAL SOLIDS IN STREAM" "C TTLXXX: TOTAL FLOW IN STREAM" "C CNC219: TOTAL SOLIDS CONC IN STREAM 219" "C OTHSLD: TOTAL OTHER SOLIDS" "C OTHTTL: TOTAL OTHER FLOW" "C" "C CONC2 IS THE DESIRED SACCHARIFIACTION EFFECTIVE SOLIDS CONCENTRATION" "F CONC2 = 0.2" "C OLG CALCS ARE THE OLIGOMER FLOWS IN EACH STREAM" "C SLD CALCS ARE THE TOTAL SOLIDS IN EACH STREAM" "F OLG232 = HGLO + HCLB + HXYO + HMAO + HGAO + HARO + HACO" "F SLD232 = HS1 + HGLU + HXYE + HSSL + HARS + HGAS + HMAS +" "F 1 (HCSL*CSLCONC) + HCNT + HWNT + HLGS + HEXT + HPRO +" "F 2 OLG232" "F OLG219 = RGLO + RCLB + RXYO + RMAO + RGAO + RARO + RACO" "F SLD219 = RI2 + RGLU + RXYE + RSSL + RARS + RGAS + RMAS +" "F 1 (RCSL*CSLCONC) + RCNT + RWNT + RLGS + REXT + RPRO +" "F 2 OLG219" "F OLG401 = CFGLO + CFCLB + CFXYO + CFMAO + CFGAO + CFARO + CFACO" "F SLD401 = CFS1 + CFGLU + CFXYE + CFSSL + CFARS + CFGAS + CFMAS +" "F 1 (CFCSL*CSLCONC) + CFCNT + CFWNT + CFLGS + CFEXT + CFPRO +" "F 2 OLG401" "F OLG422 = CPGLO + CPCLB + CPXYO + CPMAO + CPGAO + CPARO + CPACO" "F SLD422 = CPS1 + CPGLU + CPXYE + CPSSL + CPARS + CPGAS + CPMAS +" "F 1 (CPCSL*CSLCONC) + CPCNT + CPWNT + CPLGS + CPEXT + CPPRO +" "F 2 OLG422" "C" "F OLG312 = EZGLO + EZCLB + EZXYO + EZMAO + EZGAO + EZARO + EZACO" "F SLD312 = EZS1 + EZGLU + EZXYE + EZSSL + EZARS + EZGAS + EZMAS +" "F 1 (EZCSL*CSLCONC) + EZCNT + EZWNT + EZLGS + EZEXT + EZPRO +" "F 2 OLG312" "C" "C TTL CALC ARE THE TOTAL FLOWS OF EACH STREAM" "F TTL232 = HF1 + HS1" "F TTL219 = RV2 + RI2" "F TTL401 = CFF1 + CFS1" "F TTL422 = CPF1 + CPS1" "F TTL312 = EZF1 + EZS1" "F CNC219 = SLD219 / TTL219" "F OTHSLD = SLD232 + SLD312 + SLD422 - SLD219 - SLD401" "F OTHTTL = TTL232 + TTL312 + TTL422 - TTL219 - TTL401" "F CAL219 = ((CONC2 * OTHTTL) - OTHSLD) / (CNC219 - CONC2)" "C" "C AV2: RECYCLE WATER TO HYDROLYZATE PNEUMAPRESS" "F AV2 = CAL219 - RI2" "C" "C" "C CONC3: CELLULOSE + XYLOSE CONCENTRATION IN STREAM 431" "C AV3: RECYCLE FLOW STREAM 430" "C" "F CONC3 = 0.04" "F AV3 = ((ST3X + ST3C + R3X + R3C) / CONC3)" "F 1 - (CI3 + CV3 + RI3)" "C" "C CONC4: CELLULOSE + XYLOSE IN STREAM 412A" "C AV4: RECYCLE FLOW STREAM 430" "C" "F CONC4 = 0.04" "F AV4 = ((ST4C + R4C) / CONC4) -(CI4 + CV4 + RI4)" "C" "C RECALC CONCENTRATIONS AND WRITE TO THE HISTORY FILE" "C" "F CNC2 = (SLD232 - SLD401 + SLD422) / (TTL232 - TTL401 + TTL422)" "F CNC2B = (RI2 - CFS1 + CPS1 + DPS1 + CLS1 - SFS1 + SPS1)" "F 1 / (TTL232 - TTL401 + TTL422 )" "F CNC3 = (ST3X + ST3C + R3X + R3C)" "F 1 / (CI3 + CV3 + RI3 + AV3)" "F CNC4 = (ST4C + R4C) / (CI4 + CV4 + RI4 + AV4)" "C" "F WRITE(NHSTRY,101)CNC2,CNC3,CNC4,CNC2B" "F 101 FORMAT(' RECYCLE FORTRAN BLOCK RESULTS',/," "F 1 ' SPECIFIED CONCENTRATIONS',/," "F 3 ' SSCF EFFECTIVE SOLIDS CONC: ',G12.5,/," "F 4 ' CELLULASE SEED FEED CELLULOSE+XYLOSE (431): ',G12.5,/," "F 5 ' CELLULASE FERM CELLULOSE CONC (412A): ',G12.5,/,/," "F 7 ' SSCF INSOLUBLE SOLIDS CONC: ',G12.5)" "C" "F WRITE(NHSTRY,151)OTHTTL,OTHSLD,CNC219,CONC2,CAL219" "F 151 FORMAT(' RECYCLE FORTRAN BLOCK RESULTS',/," "F 3 ' OTHTTL: ',G12.5,/," "F 4 ' OTHSLD: ',G12.5,/," "F 5 ' CNC219: ',G12.5,/," "F 6 ' CONC2: ',G12.5,/," "F 7 ' CAL219: ',G12.5)" "C" "C CALCULATE SPLITS FOR BLOCK RWSPLT" "C" "F F2=AV2/(AV2+AV3+AV4)" "F F3=AV3/(AV2+AV3+AV4)" "F F4=1-F2-F3" "C" "C CALCULATE MAKE-UP WATER, STREAM 574" "C" "F RWTAV = RWAT + RWT3" "F FWAT= AV2 + RI2 + AV3 + RI3 + AV4 + RI4 - RWTAV" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = FWMIX \ \ COMMENTS COMMENTS = ( ";;" "; BLOCK TO CALCULATE THE AMOUNT OF RECYCLE NEEDED AND INCOMING" "; FRESH WATER" ";;" "; DEFINE VARIABLES FOR FRESH WATER AND PROCESS RECYCLE WATER" ";;" "; DEFINE VARIABLES FOR RECYCLE WATER STREAM #2 (Stream. 219). THIS" "; STREAM CONTROLS THE SOLIDS CONCENTRATION to fermentation" ";;" ";;" "; DEFINE THE COMPONENTS OF STREAM 232 (Diluted Hydrolysate)" ";;" ";;" "; DEFINE THE COMPONENTS OF STREAM 401 (Feed to Cellulase Production)" ";;" ";;" "; DEFINE THE COMPONENTS OF STREAM 422 (Cellulase to Ethanol Production)" ";;" ";;" "; DEFINE THE COMPONENTS OF 311 (DAP to Ethanol Production)" "; Changed to DAP by AA 02/21/01" "; Since DAP is only component, do not need to break it out like" "; other streams." ";;" ";;" "; DEFINE THE COMPONENTS OF 311A (CSL to Ethanol Production)" ";;" "; DEFINE THE COMPONENTS OF 312 (Enzyme to Ethanol Production)" ";;" ";;" "; DEFINE THE COMPONENTS OF 303 (Feed to Ferm Seed)" ";;" ";;" "; DEFINE THE COMPONENTS OF 304 (Seed to Production)" ";;" "; DEFINE VARIABLES FOR RECYCLE WATER STREAM #3. THIS STREAM" "; CONTROLS THE XYLOSE AND CELLULOSE CONCENTRATIONS IN 431." "; CURRENTLY, THIS IS SET TO 1%." ";;" ";;" "; DEFINE VARIABLES FOR RECYCLE WATER STREAM #4. THIS STREAM" "; CONTROLS THE CELLULOSE CONCENTRATION IN 412A." "; CURRENTLY, THIS IS SET TO 4%." ";;" ";;" "; DEFINE SPLIT VARIABLES IN THE RECYCLE WATER SPLITTER." ";;" ";;" "; DEFINE THE COMPONENTS OF STREAM 220 (Out of Pre Hydrolysis" ";;" ";;" ";FORTRAN STATEMENTS" ) \ ? CALCULATOR S205SOL ? ; "SET1_MOLE" ; \ DEFINE FVN = FS2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = ETHANOL \ \ DEFINE FVN = ETH220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = ETH221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = ETH254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = ETH252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FS3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = FURFURAL \ \ DEFINE FVN = FRF220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = FRF221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = FRF254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = FRF252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = FS4 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = HMF \ \ DEFINE FVN = HMF220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = HMF221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = HMF254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = HMF252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = FS5 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = H2SO4 \ \ DEFINE FVN = H2S220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = H2SO4 \ \ DEFINE FVN = H2S221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = H2SO4 \ \ DEFINE FVN = H2S254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = H2SO4 \ \ DEFINE FVN = H2S252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = H2SO4 \ \ DEFINE FVN = FS6 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = N2 \ \ DEFINE FVN = GN2220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = N2 \ \ DEFINE FVN = GN2221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = N2 \ \ DEFINE FVN = GN2254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = N2 \ \ DEFINE FVN = GN2252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = N2 \ \ DEFINE FVN = FS7 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = CO2 \ \ DEFINE FVN = CO2220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = CO2 \ \ DEFINE FVN = CO2221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = CO2 \ \ DEFINE FVN = CO2254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = CO2 \ \ DEFINE FVN = CO2252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = CO2 \ \ DEFINE FVN = FS8 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = O2 \ \ DEFINE FVN = O2G220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = O2G221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = O2G254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = O2G252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = FS9 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = CH4 \ \ DEFINE FVN = CH4220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = CH4221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = CH4254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = CH4252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = CH4 \ \ DEFINE FVN = FS10 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = NO \ \ DEFINE FVN = GNO220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = NO \ \ DEFINE FVN = GNO221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = NO \ \ DEFINE FVN = GNO254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = NO \ \ DEFINE FVN = GNO252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = NO \ \ DEFINE FVN = FS11 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = NO2 \ \ DEFINE FVN = XNO220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = NO2 \ \ DEFINE FVN = XNO221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = NO2 \ \ DEFINE FVN = XNO254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = NO2 \ \ DEFINE FVN = XNO252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = NO2 \ \ DEFINE FVN = FS12 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = NH3 \ \ DEFINE FVN = XNH220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ DEFINE FVN = XNH221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ DEFINE FVN = XNH254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ DEFINE FVN = XNH252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ DEFINE FVN = FS13 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = SOLSLDS \ \ DEFINE FVN = SOL220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = SOL221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = SOL254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = SOL252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = FS14 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = GLUCOSE \ \ DEFINE FVN = GLU220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = GLU221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = GLU254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = GLU252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = FS15 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = XYLOSE \ \ DEFINE FVN = XYL220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = XYL221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = XYL254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = XYL252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = FS16 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = GALACTOS \ \ DEFINE FVN = GAL220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = GAL221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = GAL254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = GAL252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = GALACTOS \ \ DEFINE FVN = FS17 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = MANNOSE \ \ DEFINE FVN = XMN220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = XMN221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = XMN254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = XMN252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = MANNOSE \ \ DEFINE FVN = FS18 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = ARABINOS \ \ DEFINE FVN = ARA220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = ARA221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = ARA254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = ARA252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = ARABINOS \ \ DEFINE FVN = FS19 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = UNKNOWN \ \ DEFINE FVN = UNK220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = UNK221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = UNK254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = UNK252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = UNKNOWN \ \ DEFINE FVN = FS20 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = AACID \ \ DEFINE FVN = AAC220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = AAC221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = AAC254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = AAC252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = FS21 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = LACID \ \ DEFINE FVN = LAC220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = LAC221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = LAC254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = LAC252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = FS22 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = CNUTR \ \ DEFINE FVN = CNU220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = CNU221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = CNU254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = CNU252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = CNUTR \ \ DEFINE FVN = FS23 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = WNUTR \ \ DEFINE FVN = WNU220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = WNU221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = WNU254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = WNU252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = WNUTR \ \ DEFINE FVN = FS24 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = CSL \ \ DEFINE FVN = CSL220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = CSL221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = CSL254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = CSL252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = CSL \ \ DEFINE FVN = FS25 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = OIL \ \ DEFINE FVN = OIL220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = OIL221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = OIL254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = OIL252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = OIL \ \ DEFINE FVN = FS26 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = DENAT \ \ DEFINE FVN = DEN220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = DEN221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = DEN254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = DEN252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = DENAT \ \ DEFINE FVN = FS27 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = GLUCOLIG \ \ DEFINE FVN = GLG220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = GLG221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = GLG254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = GLG252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOLIG \ \ DEFINE FVN = FS28 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = CELLOB \ \ DEFINE FVN = CLB220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = CLB221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = CLB254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = CLB252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = CELLOB \ \ DEFINE FVN = FS29 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = XYLOLIG \ \ DEFINE FVN = XLG220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = XLG221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = XLG254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = XLG252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = XYLOLIG \ \ DEFINE FVN = FS30 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = MANOLIG \ \ DEFINE FVN = ZLG220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = ZLG221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = ZLG254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = ZLG252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = MANOLIG \ \ DEFINE FVN = FS31 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = GALAOLIG \ \ DEFINE FVN = GGG220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = GGG221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = GGG254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = GGG252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = GALAOLIG \ \ DEFINE FVN = FS32 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = ARABOLIG \ \ DEFINE FVN = ARG220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = ARG221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = ARG254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = ARG252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = ARABOLIG \ \ DEFINE FVN = FS33 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = ACETOLIG \ \ DEFINE FVN = ACG220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = ACG221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = ACG254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = ACG252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = ACETOLIG \ \ DEFINE FVN = FS34 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = GLYCEROL \ \ DEFINE FVN = GLY220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = GLY221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = GLY254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = GLY252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = GLYCEROL \ \ DEFINE FVN = FS35 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = SUCCACID \ \ DEFINE FVN = SUC220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = SUC221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = SUC254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = SUC252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = SUCCACID \ \ DEFINE FVN = FS36 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = XYLITOL \ \ DEFINE FVN = XYT220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = XYT221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = XYT254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = XYT252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = XYLITOL \ \ DEFINE FVN = FS37 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = LGNSOL \ \ DEFINE FVN = SLG220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = SLG221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = SLG254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = SLG252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = FS38 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = EXTRACT \ \ DEFINE FVN = EXT220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = EXT221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = EXT254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = EXT252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = EXTRACT \ \ DEFINE FVN = FS39 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205B FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = PROTEIN \ \ DEFINE FVN = PRO220 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = PRO221 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = PRO254 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ DEFINE FVN = PRO252 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = PROTEIN \ \ FORTRAN FORTRAN-EXEC = ( "F RECOV=0.933" "F IF (ETH254.GT.0) THEN" "F FS2 = ((RECOV * ETH220) - ETH221 + ETH252) / ETH254" "F ELSE" "F FS2 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'ETHANOL RECOVERY IN S205B= ',FS2" "F IF (FRF254.GT.0) THEN" "F FS3 = ((RECOV * FRF220) - FRF221 + FRF252) / FRF254" "F ELSE" "F FS3 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'FURFURAL RECOVERY IN S205B= ',FS3" "F IF (HMF254.GT.0) THEN" "F FS4 = ((RECOV * HMF220) - HMF221 + HMF252) / HMF254" "F ELSE" "F FS4 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'HMF RECOVERY IN S205B= ',FS4" "F IF (H2S254.GT.0) THEN" "F FS5 = ((RECOV * H2S220) - H2S221 + H2S252) / H2S254" "F ELSE" "F FS5 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'H2SO4 RECOVERY IN S205B= ',FS5" "F IF (GN2254.GT.0) THEN" "F FS6 = ((RECOV * GN2220) - GN2221 + GN2252) / GN2254" "F ELSE" "F FS6 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'N2 RECOVERY IN S205B= ',FS6" "F IF (CO2254.GT.0) THEN" "F FS7 = ((RECOV * CO2220) - CO2221 + CO2252) / CO2254" "F ELSE" "F FS7 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'CO2 RECOVERY IN S205B= ',FS7" "F IF (O2G254.GT.0) THEN" "F FS8 = ((RECOV * O2G220) - O2G221 + O2G252) / O2G254" "F ELSE" "F FS8 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'O2 RECOVERY IN S205B= ',FS8" "F IF (CH4254.GT.0) THEN" "F FS9 = ((RECOV * CH4220) - CH4221 + CH4252) / CH4254" "F ELSE" "F FS9 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'CH4 RECOVERY IN S205B= ',FS9" "F IF (GNO254.GT.0) THEN" "F FS10 = ((RECOV * GNO220) - GNO221 + GNO252) / GNO254" "F ELSE" "F FS10 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'NO RECOVERY IN S205B= ',FS10" "F IF (XNO254.GT.0) THEN" "F FS11 = ((RECOV * XNO220) - XNO221 + XNO252) / XNO254" "F ELSE" "F FS11 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'NO2 RECOVERY IN S205B= ',FS11" "F IF (XNH254.GT.0) THEN" "F FS12 = ((RECOV * XNH220) - XNH221 + XNH252) / XNH254" "F ELSE" "F FS12 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'NH3 RECOVERY IN S205B= ',FS12" "F IF (SOL254.GT.0) THEN" "F FS13 = ((RECOV * SOL220) - SOL221 + SOL252) / SOL254" "F ELSE" "F FS13 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'SOLSLDS RECOVERY IN S205B= ',FS13" "F IF (GLU254.GT.0) THEN" "F FS14 = ((RECOV * GLU220) - GLU221 + GLU252) / GLU254" "F ELSE" "F FS14 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'GLUCOSE RECOVERY IN S205B= ',FS14" "F IF (XYL254.GT.0) THEN" "F FS15 = ((RECOV * XYL220) - XYL221 + XYL252) / XYL254" "F ELSE" "F FS15 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'XYLOSE RECOVERY IN S205B= ',FS15" "F IF (GAL254.GT.0) THEN" "F FS16 = ((RECOV * GAL220) - GAL221 + GAL252) / GAL254" "F ELSE" "F FS16 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'GALACTOSE RECOVERY IN S205B= ',FS16" "F IF (XMN254.GT.0) THEN" "F FS17 = ((RECOV * XMN220) - XMN221 + XMN252) / XMN254" "F ELSE" "F FS17 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'MANNOSE RECOVERY IN S205B= ',FS17" "F IF (ARA254.GT.0) THEN" "F FS18 = ((RECOV * ARA220) - ARA221 + ARA252) / ARA254" "F ELSE" "F FS18 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'ARABINOSE RECOVERY IN S205B= ',FS18" "F IF (UNK254.GT.0) THEN" "F FS19 = ((RECOV * UNK220) - UNK221 + UNK252) / UNK254" "F ELSE" "F FS19 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'UNKNOWN RECOVERY IN S205B= ',FS19" "F IF (AAC254.GT.0) THEN" "F FS20 = ((RECOV * AAC220) - AAC221 + AAC252) / AAC254" "F ELSE" "F FS20 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'AACID RECOVERY IN S205B= ',FS20" "F IF (LAC254.GT.0) THEN" "F FS21 = ((RECOV * LAC220) - LAC221 + LAC252) / LAC254" "F ELSE" "F FS21 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'LACID RECOVERY IN S205B= ',FS21" "F IF (CNU254.GT.0) THEN" "F FS22 = ((RECOV * CNU220) - CNU221 + CNU252) / CNU254" "F ELSE" "F FS22 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'CNUTR RECOVERY IN S205B= ',FS22" "F IF (WNU254.GT.0) THEN" "F FS23 = ((RECOV * WNU220) - WNU221 + WNU252) / WNU254" "F ELSE" "F FS23 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'WNUTR RECOVERY IN S205B= ',FS23" "F IF (CSL254.GT.0) THEN" "F FS24 = ((RECOV * CSL220) - CSL221 + CSL252) / CSL254" "F ELSE" "F FS24 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'CSL RECOVERY IN S205B= ',FS24" "F IF (OIL254.GT.0) THEN" "F FS25 = ((RECOV * OIL220) - OIL221 + OIL252) / OIL254" "F ELSE" "F FS25 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'OIL RECOVERY IN S205B= ',FS25" "F IF (DEN254.GT.0) THEN" "F FS26 = ((RECOV * DEN220) - DEN221 + DEN252) / DEN254" "F ELSE" "F FS26 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'DENAT RECOVERY IN S205B= ',FS26" "F IF (GLG254.GT.0) THEN" "F FS27 = ((RECOV * GLG220) - GLG221 + GLG252) / GLG254" "F ELSE" "F FS27 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'GLUCOLIG RECOVERY IN S205B= ',FS27" "F IF (CLB254.GT.0) THEN" "F FS28 = ((RECOV * CLB220) - CLB221 + CLB252) / CLB254" "F ELSE" "F FS28 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'CELLOB RECOVERY IN S205B= ',FS28" "F IF (XLG254.GT.0) THEN" "F FS29 = ((RECOV * XLG220) - XLG221 + XLG252) / XLG254" "F ELSE" "F FS29 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'XYLOLIG RECOVERY IN S205B= ',FS29" "F IF (ZLG254.GT.0) THEN" "F FS30 = ((RECOV * ZLG220) - ZLG221 + ZLG252) / ZLG254" "F ELSE" "F FS30 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'MANOLIG RECOVERY IN S205B= ',FS30" "F IF (GGG254.GT.0) THEN" "F FS31 = ((RECOV * GGG220) - GGG221 + GGG252) / GGG254" "F ELSE" "F FS31 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'GALAOLIG RECOVERY IN S205B= ',FS31" "F IF (ARG254.GT.0) THEN" "F FS32 = ((RECOV * ARG220) - ARG221 + ARG252) / ARG254" "F ELSE" "F FS32 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'ARABOLIG RECOVERY IN S205B= ',FS32" "F IF (ACG254.GT.0) THEN" "F FS33 = ((RECOV * ACG220) - ACG221 + ACG252) / ACG254" "F ELSE" "F FS33 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'ACETOLIG RECOVERY IN S205B= ',FS33" "F IF (GLY254.GT.0) THEN" "F FS34 = ((RECOV * GLY220) - GLY221 + GLY252) / GLY254" "F ELSE" "F FS34 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'GLYCEROL RECOVERY IN S205B= ',FS34" "F IF (SUC254.GT.0) THEN" "F FS35 = ((RECOV * SUC220) - SUC221 + SUC252) / SUC254" "F ELSE" "F FS35 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'SUCCACID RECOVERY IN S205B= ',FS35" "F IF (XYT254.GT.0) THEN" "F FS36 = ((RECOV * XYT220) - XYT221 + XYT252) / XYT254" "F ELSE" "F FS36 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'XYLITOL RECOVERY IN S205B= ',FS36" "F IF (SLG254.GT.0) THEN" "F FS37 = ((RECOV * SLG220) - SLG221 + SLG252) / SLG254" "F ELSE" "F FS37 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'LGNSOL RECOVERY IN S205B= ',FS37" "F IF (EXT254.GT.0) THEN" "F FS38 = ((RECOV * EXT220) - EXT221 + EXT252) / EXT254" "F ELSE" "F FS38 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'EXTRACT RECOVERY IN S205B= ',FS38" "F IF (PRO254.GT.0) THEN" "F FS39 = ((RECOV * PRO220) - PRO221 + PRO252) / PRO254" "F ELSE" "F FS39 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'PROTEIN RECOVERY IN S205B= ',FS39" ) \ \ "READ-VARS" READ-VAR = ( ETH220 ETH221 ETH254 ETH252 XYL220 XYL221 XYL254 XYL252 ) \ \ "WRITE-VARS" WRITE-VAR = ( FS2 FS3 FS4 FS5 FS6 FS7 FS8 FS9 FS10 FS11 FS12 FS13 FS14 FS15 FS16 FS17 FS18 FS19 FS20 FS21 FS22 FS23 FS24 FS25 FS26 FS27 FS28 FS29 FS30 FS31 FS32 FS33 FS34 FS35 FS36 FS37 FS38 FS39 ) \ \ COMMENTS COMMENTS = ( ";;" "; DEFINE FS1 BLOCK-VAR BLOCK=S205B SENTENCE=FRAC &" "; VARIABLE=FRACS ID1=MIXED ID2=256 ELEMENT=1" "; Water set by CT-S205B to get proper insol solids" "; Calculate the recovery" "; The mean solubles removal efficiency is 93.3% according to" "; Pneumapress P100 Test (#9) (Under Harris 2000 Subcontract)" "; That removal includes both concentrated recovery stream (221) &" "; dilute recovery stream (256). This Fort. Block calculates the" "; recovery in the dilute stream to hit the desired overall recovery" "; for xylose and sets all solubles to same recovery" ) \ ? CALCULATOR S205WASH ? ; "SET1_MOLE" ; \ DEFINE FVN = SOL220 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WAT220 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WSH252 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = S205SPT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 252 \ \ DEFINE FVN = AIRRQ FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 257 FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "F WASHR2 = 0.58" "F WSH252 = WASHR2 * (SOL220 + WAT220)" "C" "F AIRFLW = 2 * 1180.0" "F AIRP = 0.0" "F AIRT = 25.0" "F AIRNUM = ((AIRP+14.6096)*100000.0/14.5038*AIRFLW/35.3147)" "F AIRDEN = (8.314 * (AIRT + 273.15))" "F AIRRQ = (AIRNUM/AIRDEN) / 1000.0 * 60.0" "F WRITE(NHSTRY,*)'AIRNUM IN 257= ',AIRNUM" "F WRITE(NHSTRY,*)'AIRDEN IN 257= ',AIRDEN" "F WRITE(NHSTRY,*)'MOLEFLOW IN 257= ',AIRRQ" ) \ \ "READ-VARS" READ-VAR = ( SOL220 WAT220 ) \ \ "WRITE-VARS" WRITE-VAR = ( WSH252 AIRRQ ) \ \ COMMENTS COMMENTS = ( ";;" ";----------------------------------------------------" "; PRETREATMENT FORTRAN BLOCKS - AREA 200" ";----------------------------------------------------" ";;" ";;" "; calculation of air requirement" "; airflw = required flow in CFM (given per pneumapress unit as 1180 scfm" "; as shown by air compressor sizing for process 100 -- Harris Repor" "; appendix D page 3)" "; airp = pressure of airflw (psig)" "; airt = temperature of airflw (C)" "; conversion of AIRRQ to kmol/hr" ) \ ? CALCULATOR SETMAKUP ? ; "SET1_MOLE" ; \ DEFINE FVN = FMAKUP FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 811 FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" \ \ DEFINE FVN = FBLOW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 821 FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" \ \ DEFINE FVN = FHPSTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 216 FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" \ \ DEFINE FVN = FLPSTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 215 FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "F FMAKUP = FHPSTM + FLPSTM + FBLOW" ) \ \ "READ-VARS" READ-VAR = ( FHPSTM FLPSTM FBLOW ) \ \ "WRITE-VARS" WRITE-VAR = ( FMAKUP ) \ \ COMMENTS COMMENTS = ( ";;" ";THIS BLOCK CALCULATES THE LOSSES IN THE STEAM CYCLE DUE TO" ";DIRECT STEAM INJECTION AND BOILER BLOWDOWN. STEAM DEMANDS" ";TO HEAT EXCHANGERS ARE NOT INCLUDED BECAUSE THESE FLOWS" ";SHOULD RETURN." ";;" "; EXECUTE BEFORE BLOCK T824AS" ) \ ? CALCULATOR SETVAR ? ; "SET1_MOLE" ; \ DEFINE FVN = SSFVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 31 \ \ DEFINE FVN = SSFDAY FVN-VARTYPE = PARAMETER FVN-PARAMNO = 32 \ \ DEFINE FVN = SSFVOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 33 \ \ DEFINE FVN = SSFWV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 34 \ \ DEFINE FVN = PMPSSF FVN-VARTYPE = PARAMETER FVN-PARAMNO = 35 \ \ DEFINE FVN = SACVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 36 \ \ DEFINE FVN = SACDAY FVN-VARTYPE = PARAMETER FVN-PARAMNO = 37 \ \ DEFINE FVN = SACVOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 38 \ \ DEFINE FVN = SACWV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 39 \ \ DEFINE FVN = PMPSAC FVN-VARTYPE = PARAMETER FVN-PARAMNO = 40 \ \ DEFINE FVN = CLYLD FVN-VARTYPE = PARAMETER FVN-PARAMNO = 41 \ \ DEFINE FVN = CLPROD FVN-VARTYPE = PARAMETER FVN-PARAMNO = 42 \ \ DEFINE FVN = CLVOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 44 \ \ DEFINE FVN = CLWV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 45 \ \ DEFINE FVN = TEMP FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 101 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ FORTRAN FORTRAN-EXEC = ( "C FERMENTATION PARAMETERS" "C SSFDAY IS THE SSCF RESIDENCE TIME IN DAYS" "F SSFDAY=1.5" "C SSFVOL IS THE VOLUME PER FERMENTER OF THE SSCF VESSELS IN LITERS" "F SSFVOL=1000000*3.785" "C SSFWV IS THE WORKING VOLUME TO TOTAL VOL RATIO OF THE SSCF VESSELS" "F SSFWV=0.95" "C SACCHARIFICATION PARAMETERS" "C SACDAY IS THE SACCHARIFICATION RESIDENCE TIME IN DAYS" "F SACDAY=1.5" "C SACVOL IS THE VOLUME PER TANK OF THE SACCH. VESSELS IN LITERS" "F SACVOL=1000000*3.785" "C SACWV IS THE WORKING VOLUME TO TOTAL VOL RATIO OF THE SACCH. VESSELS" "F SACWV=0.95" "C CELLULASE PRODUCTION PARAMETERS" "C CLYLD IS THE CELLULASE YIELD (FPU/G CELLULOSE + XYLOSE)" "F CLYLD=200" "C CLPROD IS THE CELLULASE PRODUCTIVITY (FPU/L HR)" "F CLPROD=75" "C CLVOL IS THE VOLUME PER CELLULASE REACTOR (L)" "F CLVOL=264000*3.785" "C CLWV IS THE WORKING VOLUME TO TOTAL VOL RATIO OF THE CELL. VSLS." "F CLWV=0.8" "C" ) \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = CALCULATOR BLK-ID = FEEDPROP \ \ COMMENTS COMMENTS = ( ";;" ";-------------------------------------------------------" "; *FORTRAN BLOCKS*" "; Common Block Holder" ";-------------------------------------------------------" "; Inputs are entered here to be used throughout the model" ";;" ";;" ";;" ";;" ";;" ";;" "; WRITE-VARS SSFDAY SSFVOL SSFWV SACDAY SACVOL SACWV &" "; CLYLD CLPROD CLVOL CLWV" ) \ ? CALCULATOR STORE ? ; "SET1_MOLE" ; \ DEFINE FVN = PRFLOW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 515 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = AFLOW1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 212 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = AFLOW2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 233 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = AMFLW2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 434 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ DEFINE FVN = AMFLW3 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 436 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ DEFINE FVN = APFLW1 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 310 FVN-SUBS = MIXED FVN-COMPONEN = DAP \ \ DEFINE FVN = APFLW2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 311 FVN-SUBS = MIXED FVN-COMPONEN = DAP \ \ DEFINE FVN = ALFLW2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 227 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = F312M FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 312 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = F312S FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 312 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = TAFLOW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 710 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FWFLOW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 713 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = TAMFLW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 717 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = DFLOW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 723 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = TLFLOW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 745 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = F750M FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 750 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = F750S FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 750 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = TAPFLW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 755 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "F TAFLOW = AFLOW1 + AFLOW2" "F TLFLOW = ALFLW2" "C CALCULATE THE FIREWATER TANK (T704) VARIABLES" "C" "C THE FIREWATER FLOWRATE IS SCALED FROM THE ORIGINAL BASE CASE" "C ETHANOL PRODUCT FLOWRATE (PROD)" "C" "F PROD = 21769." "F FWFLOW = 8007 * PRFLOW / PROD" "C" "C CALCULATE THE AMMONIA STORAGE SYSTEM" "C" "C DNH3 IS THE AMMONIA REQ PER ETHANOL PRODUCED (LB/LB)" "F TAMFLW = AMFLW2 + AMFLW3" "C" "C CALCULATE THE DIESEL FUEL TANK. IT WILL BE SIMILAR TO THAT FOR" "C THE FIREWATER TANK AND WILL BE SCALED OFF OF THE PRODUCT FLOWRATE." "C" "F BCDF = 519.7" "C BCDF IS THE BASE CASE DIESEL FLOWRATE IN KG/HR" "C" "C BCPF IS THE BASE CASE PROPANE FLOWRATE IN KG/HR" "C A 33 LB PROPANE TANK WILL LAST 8 HOURS ACCORDING TO QUOTE FROM" "C HARRIS GROUP" "C THEREFORE, 33 LB / 8 HR = 4.125 LB/HR FOR A SINGLE FORKLIFT" "C 8 FORK LIFTS REQUIRED FOR BASE CASE" "C 4.125 LB/HR * 8 = 33 LB/HR / 2.205 = 14.97 KG/HR" "C" "F BCPF = 14.97" "F PROD2 = 18285." "C PROD2 SET AT 18285 FOR MODEL A0102Q." "F DFLOW = BCPF * PRFLOW / PROD2" "C" "C CALCULATE CELLASE FLOW TO WHOLE FACILITY" "F F750M = F312M" "F F750S = F312S" "C" "C CALCULATE DAP FLOW TO WHOLE FACILITY" "F TAPFLW = APFLW1 + APFLW2" "C" ) \ \ "READ-VARS" READ-VAR = ( AFLOW1 AFLOW2 ALFLW2 PRFLOW AMFLW2 AMFLW3 F312M F312S APFLW1 APFLW2 ) \ \ "WRITE-VARS" WRITE-VAR = ( TAFLOW TLFLOW FWFLOW TAMFLW DFLOW F750M F750S TAPFLW ) \ \ COMMENTS COMMENTS = ( "; EXECUTE AFTER T507-8" ";;" ";;" "; Sums up various Tank Farm Flows and Sets others, like" "; Diesel, & Fire Water as ratios of Ethanol Product" ";;" "; INPUTS" ";;" "; DAP is SSCF nutrient, Phosphorus source likely." "; Enzyme required" "; OUTPUTS" "; Acid Flows" ";;" "; Lime Flows" ";;" "; + F316M" "; + F316S" ) \ ? CALCULATOR WATERDEM ? ; "SET1_MOLE" ; \ DEFINE FVN = PWMU FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 574 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = STLOSS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 811 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = EXTRA FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 251 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WELLMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 943 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = WATI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 903 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = TRTWW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 624 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = SCRBWT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 524 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CWMKUP FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 941 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = CIPCS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 906 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "F CIPCS=145" "C" "F WATI = PWMU + STLOSS + CIPCS + CWMKUP - TRTWW + SCRBWT" "F 1 - EXTRA" "F WELLMX = WATI - STLOSS - SCRBWT" "C" ) \ \ "READ-VARS" READ-VAR = ( PWMU STLOSS TRTWW SCRBWT EXTRA CWMKUP ) \ \ "WRITE-VARS" WRITE-VAR = ( WATI WELLMX CIPCS ) \ \ COMMENTS COMMENTS = ( "; EXECUTE BEFORE ACOMP" ";;" ";;" ";THIS BLOCK CALCULATES THE TOTAL WELL WATER DEMAND FOR THE" ";ENTIRE PROCESS." ";PWMU IS PROCESS H2O MAKE-UP. CTL IS COOLING TOWER LOSSES." ";STLOSS ARE LOSSES FROM THE STEAM SYSTEM, INCLUDING DIRECT" ";STEAM INJECTION & BOILER BLOWDOWN. CIPCS ARE LOSSES FROM" "; THE CIP/CS SYSTEM. CW IS THE COOLING TOWER STREAM." "; Include water to IX" "; Read Variable - Additional Stream to reduce flow of 535 to Digestor" "; Write variable - amount of well water mixed with treated water" ";;" ";CIP/CS LOSS IS SET AT 320 LB/HR BY THE BASE CASE." ";;" ";F write(nhstry,50)CWEVAP,CWWNDG,CWBL2,CWBL1,CIPCS,SCRBWT,PWMU," ";F 1 STLOSS,TRTWW,WELLMX,WATI,CWTOT" ";F 50 format(' WATER RESULTS',/," ";F 9 ' CWEVAP(Cooling Tower Evap, Calc) = ',g12.5,/," ";F 1 ' CWWNDG(Cooling Tower Windage) = ',g12.5,/," ";F 6 ' CWBL2(Cooling Tower Blowdown, Calc Here) = ',g12.5,/," ";F 6 ' CWBL1(Cooling Tower Blowdown, Specified) = ',g12.5,/," ";F 2 ' CIPCS(CIP/CS Loses - Fixed) = ',g12.5,/," ";F 4 ' SCRBWT(Scrubber water demand) = ',g12.5,/," ";F 3 ' PWMU(Main make-up water #574) = ',g12.5,/," ";F 4 ' STLOSS(Steam Losses #811) = ',g12.5,/," ";F 7 ' TRTWW(Treated WW) = ',g12.5,/," ";f 8 ' WELLMX(Well water mixed with treated) = ',g12.5,/," ";F 5 ' WATI(Total #903) = ',g12.5,/," ";f 6 ' cwtot = ',g12.5)" ";;" ) \ ? CALCULATOR WWNUTR1 ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F COMMON/ WWLOAD/ CODTOT, BODTOT, CODDAY, BODDAY" ) \ \ DEFINE FVN = WWTNUT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 630 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C" "F WWTFAC = 3.675E-2" "C" "C THE AMOUNT OF PHOSPHORIC ACID, UREA, MICRONUTRIENTS AND CAUSTIC" "C" "F WWTNUT = WWTFAC*CODTOT" "C" ) \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = CALCULATOR BLK-ID = CODCALC1 \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CALCULATOR WWNUTR2 ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F COMMON/ WWLOD2/ COD2, BOD2, CODDY2, BODDY2, BODHP" ) \ \ DEFINE FVN = WWTNUT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 631 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C" "F WWTFAC = 1.701E-3" "C" "C WWTFAC IS THE AMOUNT OF POLYMER ADDED LB/LB COD TO THE AEROBIC" "C SYSTEM. IT IS THE AVERAGE VALUE PROVIDED BY J. RUOCCO FOR THE" "C 3 SYSTEM DESIGNS (ENZYME, COUNTERCURRENT AND SOFTWOOD)" "C POLYMER IS MODELLED AS THE COMPONENT WNUTR" "C" "F WWTNUT = WWTFAC*COD2" "C" ) \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = CALCULATOR BLK-ID = CODCALC2 \ ? CALCULATOR XPSTMD ? ; "SET1_MOLE" ; \ DEFINE FVN = STMXP FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M811XSPT FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 812D \ \ DEFINE FVN = XPSTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 892 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C REB IS THE STEAM REQUIRED FOR PRETREATMENT" "F STMXP = XPSTM" ) \ \ "READ-VARS" READ-VAR = ( XPSTM ) \ \ "WRITE-VARS" WRITE-VAR = ( STMXP ) \ \ COMMENTS COMMENTS = ( ";;" ";-------------------------------------------------------------" "; STEAM CYCLE FORTRAN BLOCKS - AREA 8100" ";------------------------------------------------------------" ";;" ";THIS BLOCK CALCULATES THE TOTAL XHP STEAM DEMAND." ";;" ";;" ";;" ) \ ? SENSITIVITY MASSFLOW ? ; "SET1_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F COMMON /WWLOAD/ CODTOT, BODTOT, CODDAY, BODDAY" "F COMMON /WWLOD2/ COD2, BOD2, CODDY2, BODDY2, BODHP" ) \ \ PARAM BASE-CASE = NO \ \ DEFINE FVN = HLETOT FVN-VARTYPE = PARAMETER FVN-PARAMNO = 2 \ \ DEFINE FVN = WATCON FVN-VARTYPE = PARAMETER FVN-PARAMNO = 3 \ \ DEFINE FVN = BTU101 FVN-VARTYPE = PARAMETER FVN-PARAMNO = 4 \ \ DEFINE FVN = P501GP FVN-VARTYPE = PARAMETER FVN-PARAMNO = 5 \ \ DEFINE FVN = SSFVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 31 \ \ DEFINE FVN = SACVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 36 \ \ DEFINE FVN = SAR FVN-VARTYPE = PARAMETER FVN-PARAMNO = 20 \ \ DEFINE FVN = SMR FVN-VARTYPE = PARAMETER FVN-PARAMNO = 21 \ \ DEFINE FVN = DD501 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = D501 FVN-VARIABLE = "TS-DIAM" FVN-SENTENCE = "TSIZE-RESULT" FVN-ID1 = 1 \ \ DEFINE FVN = QF300A FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QF300A \ \ DEFINE FVN = QF0300 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QF300 \ \ DEFINE FVN = QF0400 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QF400 \ \ DEFINE FVN = S510 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 510 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = S521 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 521 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = S851 FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 851 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = PTRR01 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 1 \ \ DEFINE FVN = PTRR02 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 2 \ \ DEFINE FVN = PTRR03 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 3 \ \ DEFINE FVN = PTRR04 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 4 \ \ DEFINE FVN = PTRR05 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 5 \ \ DEFINE FVN = PTRR06 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 6 \ \ DEFINE FVN = PTRR07 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 7 \ \ DEFINE FVN = PTRR08 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 8 \ \ DEFINE FVN = PTRR09 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 9 \ \ DEFINE FVN = PTRR10 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 10 \ \ DEFINE FVN = PTRR11 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 11 \ \ DEFINE FVN = PTRR12 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 12 \ \ DEFINE FVN = PTRR13 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 13 \ \ DEFINE FVN = PTRR14 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 14 \ \ DEFINE FVN = PTRR15 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 15 \ \ DEFINE FVN = PTRR16 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 16 \ \ DEFINE FVN = PTRR17 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 17 \ \ DEFINE FVN = PTRR18 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 18 \ \ DEFINE FVN = PTRR19 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 19 \ \ DEFINE FVN = PTRR20 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 20 \ \ DEFINE FVN = PTRR21 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 21 \ \ DEFINE FVN = PTRR22 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 22 \ \ DEFINE FVN = PTRR23 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = M202HI FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 23 \ \ DEFINE FVN = SACR01 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 1 \ \ DEFINE FVN = SACR02 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 2 \ \ DEFINE FVN = SACR03 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 3 \ \ DEFINE FVN = SACR04 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 4 \ \ DEFINE FVN = SACR05 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 5 \ \ DEFINE FVN = SACR06 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 6 \ \ DEFINE FVN = SACR13 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 13 \ \ DEFINE FVN = SACR14 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 14 \ \ DEFINE FVN = SACR15 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 15 \ \ DEFINE FVN = SACR23 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 23 \ \ DEFINE FVN = SACR24 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 24 \ \ DEFINE FVN = SACR25 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 25 \ \ DEFINE FVN = SACR32 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 32 \ \ DEFINE FVN = SACR33 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 33 \ \ DEFINE FVN = SACR34 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 34 \ \ DEFINE FVN = SACR41 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 41 \ \ DEFINE FVN = SACR42 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 42 \ \ DEFINE FVN = SACR43 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T310 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 43 \ \ DEFINE FVN = FRMR07 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 7 \ \ DEFINE FVN = FRMR08 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 8 \ \ DEFINE FVN = FRMR09 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 9 \ \ DEFINE FVN = FRMR10 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 10 \ \ DEFINE FVN = FRMR11 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 11 \ \ DEFINE FVN = FRMR12 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 12 \ \ DEFINE FVN = FRMR16 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 16 \ \ DEFINE FVN = FRMR17 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 17 \ \ DEFINE FVN = FRMR18 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 18 \ \ DEFINE FVN = FRMR19 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 19 \ \ DEFINE FVN = FRMR20 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 20 \ \ DEFINE FVN = FRMR21 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 21 \ \ DEFINE FVN = FRMR22 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 22 \ \ DEFINE FVN = FRMR26 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 26 \ \ DEFINE FVN = FRMR27 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 27 \ \ DEFINE FVN = FRMR28 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 28 \ \ DEFINE FVN = FRMR29 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 29 \ \ DEFINE FVN = FRMR30 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 30 \ \ DEFINE FVN = FRMR31 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 31 \ \ DEFINE FVN = FRMR35 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 35 \ \ DEFINE FVN = FRMR36 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 36 \ \ DEFINE FVN = FRMR37 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 37 \ \ DEFINE FVN = FRMR38 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 38 \ \ DEFINE FVN = FRMR39 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 39 \ \ DEFINE FVN = FRMR40 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 40 \ \ DEFINE FVN = FRMR44 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 44 \ \ DEFINE FVN = FRMR45 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 45 \ \ DEFINE FVN = FRMR46 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 46 \ \ DEFINE FVN = FRMR47 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 47 \ \ DEFINE FVN = FRMR48 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 48 \ \ DEFINE FVN = FRMR49 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = F300F FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 49 \ \ DEFINE FVN = OSLR01 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T224 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 1 \ \ DEFINE FVN = OSLR02 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T224 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 2 \ \ DEFINE FVN = OSLR10 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T224 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 10 \ \ DEFINE FVN = OSLR11 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T224 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 11 \ \ DEFINE FVN = OSLR12 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T224 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 12 \ \ DEFINE FVN = OSLR13 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T224 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 13 \ \ DEFINE FVN = OSLR14 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T224 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 14 \ \ DEFINE FVN = OSLR15 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = T224 FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 15 \ \ DEFINE FVN = WP101 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP101 \ \ DEFINE FVN = WP102 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP102 \ \ DEFINE FVN = WP103 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP103 \ \ DEFINE FVN = WP104 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP104 \ \ DEFINE FVN = WP105 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP105 \ \ DEFINE FVN = WC101 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC101 \ \ DEFINE FVN = WC102 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC102 \ \ DEFINE FVN = WC104 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC104 \ \ DEFINE FVN = WC103 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC103 \ \ DEFINE FVN = WM104 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM104 \ \ DEFINE FVN = WM105 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM105 \ \ DEFINE FVN = WM107 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM107 \ \ DEFINE FVN = WS101 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS101 \ \ DEFINE FVN = WS102 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS102 \ \ DEFINE FVN = WC201 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC201 \ \ DEFINE FVN = WM202 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM202 \ \ DEFINE FVN = WP201 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP201 \ \ DEFINE FVN = WC202 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC202 \ \ DEFINE FVN = WM205 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM205 \ \ DEFINE FVN = WP205 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP205 \ \ DEFINE FVN = WP211 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP211 \ \ DEFINE FVN = WP213 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP213 \ \ DEFINE FVN = WP224 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP224 \ \ DEFINE FVN = WS205 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS205 \ \ DEFINE FVN = WS221 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS221 \ \ DEFINE FVN = WT205 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT205 \ \ DEFINE FVN = WT232 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT232 \ \ DEFINE FVN = WC225 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC225 \ \ DEFINE FVN = WP209 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP209 \ \ DEFINE FVN = WP222 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP222 \ \ DEFINE FVN = WP223 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP223 \ \ DEFINE FVN = WP239 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP239 \ \ DEFINE FVN = WS222 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS222 \ \ DEFINE FVN = WT209 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT209 \ \ DEFINE FVN = WT224 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT224 \ \ DEFINE FVN = WP301 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP301 \ \ DEFINE FVN = WP302 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP302 \ \ DEFINE FVN = WT301 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT301 \ \ DEFINE FVN = WT304 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT304 \ \ DEFINE FVN = WT305 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT305 \ \ DEFINE FVN = WP300 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP300 \ \ DEFINE FVN = WP306 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP306 \ \ DEFINE FVN = WP310 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP310 \ \ DEFINE FVN = WT300 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT300 \ \ DEFINE FVN = WT306 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT306 \ \ DEFINE FVN = WT310 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT310 \ \ DEFINE FVN = WP401 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP401 \ \ DEFINE FVN = WT402 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "WT402-3" \ \ DEFINE FVN = WM401 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM401 \ \ DEFINE FVN = WP400 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP400 \ \ DEFINE FVN = WP405 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP405 \ \ DEFINE FVN = WP420 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP420 \ \ DEFINE FVN = WT400 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT400 \ \ DEFINE FVN = WT405 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT405 \ \ DEFINE FVN = WC501 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC501 \ \ DEFINE FVN = WM505 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM505 \ \ DEFINE FVN = WP501 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP501 \ \ DEFINE FVN = WP503 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP503 \ \ DEFINE FVN = WP504 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP504 \ \ DEFINE FVN = WP505 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP505 \ \ DEFINE FVN = WP515 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP515 \ \ DEFINE FVN = WM503 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM503 \ \ DEFINE FVN = WP511 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP511 \ \ DEFINE FVN = WP512 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP512 \ \ DEFINE FVN = WP513 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP513 \ \ DEFINE FVN = WP514 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP514 \ \ DEFINE FVN = WP530 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP530 \ \ DEFINE FVN = WS505 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS505 \ \ DEFINE FVN = WT530 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT530 \ \ DEFINE FVN = WM604 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM604 \ \ DEFINE FVN = WP602 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP602 \ \ DEFINE FVN = WP606 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP606 \ \ DEFINE FVN = WS600 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS600 \ \ DEFINE FVN = WT602 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT602 \ \ DEFINE FVN = WT606 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT606 \ \ DEFINE FVN = WC614 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC614 \ \ DEFINE FVN = WM612 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM612 \ \ DEFINE FVN = WP608 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP608 \ \ DEFINE FVN = WP610 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP610 \ \ DEFINE FVN = WP611 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP611 \ \ DEFINE FVN = WP614 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP614 \ \ DEFINE FVN = WP616 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP616 \ \ DEFINE FVN = WS614 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS614 \ \ DEFINE FVN = WT608 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT608 \ \ DEFINE FVN = WT610 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT610 \ \ DEFINE FVN = WC755 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WC755 \ \ DEFINE FVN = WP701 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP701 \ \ DEFINE FVN = WP703 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP703 \ \ DEFINE FVN = WP704 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP704 \ \ DEFINE FVN = WP706 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP706 \ \ DEFINE FVN = WP707 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP707 \ \ DEFINE FVN = WP708 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP708 \ \ DEFINE FVN = WP710 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP710 \ \ DEFINE FVN = WP720 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP720 \ \ DEFINE FVN = WP750 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP750 \ \ DEFINE FVN = WP755 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP755 \ \ DEFINE FVN = WP760 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP760 \ \ DEFINE FVN = WT720 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT720 \ \ DEFINE FVN = WT760 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WT760 \ \ DEFINE FVN = WM801 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM801 \ \ DEFINE FVN = WM804 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM804 \ \ DEFINE FVN = WCOMB FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WCOMBFAN \ \ DEFINE FVN = WP811 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP811 \ \ DEFINE FVN = WP804 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP804 \ \ DEFINE FVN = WP824 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP824 \ \ DEFINE FVN = WP826 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP826 \ \ DEFINE FVN = WP828 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP828 \ \ DEFINE FVN = WP830 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP830 \ \ DEFINE FVN = WM830 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM830 \ \ DEFINE FVN = WM832 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM832 \ \ DEFINE FVN = WM834 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM834 \ \ DEFINE FVN = WPLNT FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WPLNTPOW \ \ DEFINE FVN = WM902 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM902 \ \ DEFINE FVN = WM904A FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM904A \ \ DEFINE FVN = WM908 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM908 \ \ DEFINE FVN = WS904 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WS904 \ \ DEFINE FVN = WP912 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP912 \ \ DEFINE FVN = WP914 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP914 \ \ DEFINE FVN = WP902 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WP902 \ \ DEFINE FVN = WM910 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WM910 \ \ DEFINE FVN = T895 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 895 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T896 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 896 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T501 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 501 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T506 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 506 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T518 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 518 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T518A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 518A FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QHX512 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH512 \ \ DEFINE FVN = T223 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 223 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T240 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 240 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T945 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 945 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T940 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 940 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QHX200 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH200 \ \ DEFINE FVN = T218 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 218 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T520A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 520A FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T502 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 502 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QH201 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH201 \ \ DEFINE FVN = T260 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 260 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T262 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 262 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QHX205 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH205 \ \ DEFINE FVN = T520 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 520 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QHX244 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH244A \ \ DEFINE FVN = QHX201 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH201XTR \ \ DEFINE FVN = T301 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T301A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301A FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QHX301 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH301 \ \ DEFINE FVN = T301B FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301B FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T301C FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 301C FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QHX302 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH302 \ \ DEFINE FVN = T526 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 526 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T528 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 528 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QEX502 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QE502A \ \ DEFINE FVN = T612 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 612 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T613 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 613 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QHX602 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH602 \ \ DEFINE FVN = T812B FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 812B FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T823 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 823 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T813A FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 813A FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = T813B FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 813B FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QHX811 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH811 \ \ DEFINE FVN = T819 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 819 FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = QHX81B FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = QH811B \ \ DEFINE FVN = TOTANA FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 632 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = TOTAER FVN-VARTYPE = "STREAM-PROP" FVN-STREAM = 618 FVN-PROPSET = MASSFLW \ \ DEFINE FVN = D618 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = SOLMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = SOLSLDS FVN-ID2 = 1 \ \ DEFINE FVN = EXTMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = EXTRACT FVN-ID2 = 1 \ \ DEFINE FVN = PROMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = PROTEIN FVN-ID2 = 1 \ \ DEFINE FVN = HCSOL FVN-VARTYPE = PARAMETER FVN-PARAMNO = 7 \ \ DEFINE FVN = HCPRO FVN-VARTYPE = PARAMETER FVN-PARAMNO = 8 \ \ DEFINE FVN = HCEXT FVN-VARTYPE = PARAMETER FVN-PARAMNO = 9 \ \ FORTRAN FORTRAN-EXEC = ( "F SACDAY = SAR / 24." "F SSFDAY = SMR / 24." "F C100 = WC101+WC102+WC104+WC103" "F M100 = WM104+WM105+WM107+WP101+WP102+WP103+WP104+WP105" "F S100 = WS101+WS102" "F WA100= C100+M100+S100" "F C200 = WC201+WM202+WP201+WC202+WM205+WP205+WP211+WP213" "F 1 +WP224" "F M200 = WS205+WS221+WT205+WT232+WC225+WP209+WP222+WP223" "F 2 +WP239" "F S200 = WS222+WT209+WT224" "F WA200=C200+M200+S200" "F C300 = WP301+WP302+WT301+WT304+WT305" "F M300 = WP300+WP306+WP310" "F S300 = WT300+WT306+WT310" "F WA300=C300+M300+S300" "F C400 = WP401+WT402+WM401" "F M400 = WP400+WP405+WP420" "F S400 = WT400+WT405" "F WA400=C400+M400+S400" "F C500 = WC501+WM505+WP501+WP503+WP504+WP505+WP530+WS505+WT530" "F M500 = WP515+WM503+WP511+WP512" "F S500 = WP513+WP514" "F WA500=C500+M500+S500" "F C600 = WM604+WP602+WP606" "F M600 = WS600+WT602+WT606+WC614+WM612+WP608+WP610" "F S600 = WP611+WP614+WP616+WS614+WT608+WT610" "F WA600= C600+M600+S600" "F C700 = WP701+WP703+WP704+WT720+WT760" "F M700 = WP706+WP707+WP708+WP755+WP760" "F S700 = WP710+WP720+WP750+WC755" "F WA700= C700+M700+S700" "F C800 = WM801+WM804+WCOMB+WP811+WPLNT" "F M800 = WP804+WP824+WP826+WP828+WP830+WM830" "F S800 = WM834+WM832" "F WA800= C800+M800+S800" "F C900 = WM902+WM904A+WM908" "F M900 = WS904+WP912" "F S900 = WP914+WP902+WM910" "F WA900= C900+M900+S900" "F DT512=((T501-T518A)-(T506-T518))/DLOG((T501-T518A)/(T506-T518))" "F DT512 = DABS(DT512 * 1.8)" "F U512 = 200." "C CONVERT FROM CAL/S TO BTU/HR" "F Q512 = QHX512 * 14.2869" "C AREA IN SQUARE FEET" "F A512 = DABS(Q512) / (U512 * DT512)" "F DT=((T223-T940)-(T240-T945))" "F 1 /DLOG((T223-T940)/(T240-T945))" "F DT = DABS(DT * 1.8)" "F U = 250." "C CONVERT FROM CAL/S TO BTU/HR" "F Q = QHX200 * 14.2869" "C AREA IN SQUARE FEET" "F A200 = DABS(Q) / (U * DT)" "F WRITE(NHSTRY,101)DT,Q,A200" "F 101 FORMAT(' HX CALC RESULTS',/," "F 1 ' DT = ',G12.5,/," "F 2 ' Q = ',G12.5,/," "F 3 ' A200 = ',G12.5)" "F DT1=((T218-T501)-(T520A-T502))/DLOG((T218-T501)/(T520A-T502))" "F DT1 = DABS(DT1 * 1.8)" "F U = 150." "C CONVERT FROM CAL/S TO BTU/HR" "F Q1 = QH201 * 14.2869" "C AREA IN SQUARE FEET" "F A201 = DABS(Q1) / (U * DT1)" "F WRITE(NHSTRY,102)DT1,Q1,A201" "F 102 FORMAT(' HX CALC RESULTS',/," "F 1 ' DT1 = ',G12.5,/," "F 2 ' Q1 = ',G12.5,/," "F 5 ' A201 = ',G12.5)" "F DT205=((T260-T940)-(T262-T945))/DLOG((T260-T940)/(T262-T945))" "F DT205 = DABS(DT205 * 1.8)" "F U205 = 250." "C CONVERT FROM CAL/S TO BTU/HR" "F Q205 = QHX205 * 14.2869" "C AREA IN SQUARE FEET" "F A205 = DABS(Q205) / (U205 * DT205)" "F WRITE(NHSTRY,101)DT205,Q205,A205" "F 120 FORMAT(' HX CALC RESULTS',/," "F 1 ' DT205 = ',G12.5,/," "F 2 ' Q205 = ',G12.5,/," "F 3 ' A205 = ',G12.5)" "C LATENT HEAT FIRST" "F DTLAT=((T520A-T940)-(T520A-T945))/DLOG((T520A-T940)/(T520A-T945))" "F DTLAT = DABS(DTLAT * 1.8)" "F ULAT = 150." "C CONVERT FROM CAL/S TO BTU/HR" "F QLAT = QHX201 * 14.2869" "C AREA IN SQUARE FEET" "F ALAT = DABS(QLAT) / (ULAT * DTLAT)" "C" "C SENSIBLE HEAT NEXT" "F DTSNS=((T520A-T940)-(T520-T945))/DLOG((T520A-T940)/(T520-T945))" "F DTSNS = DABS(DTSNS * 1.8)" "F USNS = 150." "C CONVERT FROM CAL/S TO BTU/HR" "F QSNS = QHX244 * 14.2869" "C AREA IN SQUARE FEET" "F ASNS = DABS(QSNS) / (USNS * DTSNS)" "C SUM THE TWO AREAS" "F A244 = ALAT + ASNS" "F WRITE(NHSTRY,112)DTSNS,QSNS,ALAT,ASNS,A244" "F 112 FORMAT(' H-244 CALC RESULTS',/," "F 1 ' DTSNS = ',G12.5,/," "F 2 ' QSNS = ',G12.5,/," "F 3 ' ALAT = ',G12.5,/," "F 4 ' ASNS = ',G12.5,/," "F 5 ' A244 = ',G12.5)" "F DT=((T301-T896)-(T301A-T895))/DLOG((T301-T896)/(T301A-T895))" "F DT = DABS(DT * 1.8)" "F U = 400." "C CONVERT FROM CAL/S TO BTU/HR" "F Q = QHX301 * 14.2869" "C AREA IN SQUARE FEET" "F A301 = DABS(Q) / (U * DT)" "F WRITE(NHSTRY,103)DT,Q,A301" "F 103 FORMAT(' HX CALC RESULTS',/," "F 1 ' DT = ',G12.5,/," "F 2 ' Q = ',G12.5,/," "F 3 ' A301 = ',G12.5)" "F DT=((T301B-T940)-(T301C-T945))/DLOG((T301B-T940)/(T301C-T945))" "F DT = DABS(DT * 1.8)" "F U = 300." "C CONVERT FROM CAL/S TO BTU/HR" "F Q = QHX302 * 14.2869" "C AREA IN SQUARE FEET" "F A302 = DABS(Q) / (U * DT)" "F WRITE(NHSTRY,104)DT,Q,A302" "F 104 FORMAT(' HX CALC RESULTS',/," "F 1 ' DT = ',G12.5,/," "F 2 ' Q = ',G12.5,/," "F 3 ' A302 = ',G12.5)" "F DT = T526-T528" "F DT = DABS(DT * 1.8)" "F U = 170." "C CONVERT FROM CAL/S TO BTU/HR" "F Q = QEX502 * 14.2869" "C AREA IN SQUARE FEET" "F AE502 = DABS(Q) / (U * DT)" "F WRITE(NHSTRY,105)DT,Q,AE502" "F 105 FORMAT(' HX CALC RESULTS',/," "F 1 ' DT = ',G12.5,/," "F 2 ' Q = ',G12.5,/," "F 3 ' AE502 = ',G12.5)" "C" "F DI501 = DD501 * DD501" "F DT=((T612-T940)-(T613-T945))/DLOG((T612-T940)/(T613-T945))" "F DT = DABS(DT * 1.8)" "F U = 115." "C CONVERT FROM CAL/S TO BTU/HR" "F Q = QHX602 * 14.2869" "C AREA IN SQUARE FEET" "F A602 = DABS(Q) / (U * DT)" "F WRITE(NHSTRY,106)DT,Q,A602" "F 106 FORMAT(' HX CALC RESULTS',/," "F 1 ' DT = ',G12.5,/," "F 2 ' Q = ',G12.5,/," "F 3 ' A602 = ',G12.5)" "F DT1=((T812B-T813B)-(T819-T813A))/DLOG((T812B-T813B)/(T819-T813A))" "F DT1 = DABS(DT1 * 1.8)" "F U = 700." "C CONVERT FROM CAL/S TO BTU/HR" "F Q1 = QHX811 * 14.2869" "F DT2=T813B-T813A" "F DT2 = DABS(DT1 * 1.8)" "F U = 700." "C CONVERT FROM CAL/S TO BTU/HR" "F Q2 = QHX81B * 14.2869" "C AREA IN SQUARE FEET" "F A811A = DABS(Q1) / (U * DT1)" "F A811B = DABS(Q2) / (U * DT2)" "F A811 = A811A + A811B" "F WRITE(NHSTRY,110)DT1,Q1,DT2,Q2,A811" "F 110 FORMAT(' HX H-811 CALC RESULTS',/," "F 1 ' DT1 = ',G12.5,/," "F 2 ' Q1 = ',G12.5,/," "F 3 ' DT2 = ',G12.5,/," "F 4 ' Q2 = ',G12.5,/," "F 5 ' A811 = ',G12.5)" "C" "F ANLOAD = 12.0" "F AELOAD = 0.55" "C" "C ANLOAD AND AELOAD ARE THE SPACE LOADINGS IN G/L/D FOR THE ANAEROBIC" "C AND AEROBIC SYSTEMS, RESPECTIVELY" "C BOTH VALUES WERE PROVIDED BY J. RUOCCO" "C" "F ANCONC = (CODTOT*1000.)/TOTANA" "F AECONC = (COD2*1000.)/TOTAER" "C" "C ANCONC AND AECONC ARE THE COD CONCENTRATIONS (G/L)" "C THESE CALCULATIONS ASSUME THAT THE STREAMS HAVE THE SAME DENSITY" "C AS FOR WATER (1 KG/L)." "C" "F ANRT = (ANCONC*24.0)/ANLOAD" "F AERT = (AECONC*24.0)/AELOAD" "C" "C ANRT AND AERT ARE THE RESIDENCE TIME (H) FOR THE ANAEROBIC AND" "C AEROBIC SYSTEMS, RESPECTIVELY" "C" "F ANVOL1 = (TOTANA*ANRT)/3.7854" "F AEVOL1 = (TOTAER*AERT)/3.7854" "C" "C ANVOL AND AEVOL ARE THE VOLUMES (GAL) OF THE ANAEROBIC AND AEROBIC" "C SYSTEMS, RESPECTIVELY." "C THIS CALCULATION ASSUMES THAT THE STREAMS HAVE THE SAME DENSITY AS" "C WATER (1 KG/L)." "C" "C CALCULATE THE NUMBER OF ANEROBIC VESSELS, ASSUMING THAT THE VESSELS" "C ARE LIMITED TO 962,651 GAL." "C" "F INMANR = INT (ANVOL1 / 962651.) + 1" "F ANVOL = ANVOL1 / INMANR" "C" "C SECOND METHOD OF CALCULATING AEROBIC VOLUME, 16.3 DAY RESIDENCE TIME" "C STREAM 618 IS THE INLET VOLUME IN KG/HR" "C" "F AEVOL = TOTAER *2.2 * 24. * 16.3 / (8.33 * D618)" "F" "F WRITE(NHSTRY,108)TOTAER,D618,AEVOL" "F 108 FORMAT(' TOTAL FLOW TO AEROBIC: ',G12.5,' KG/HR',/," "F 1 ' DENSITY OF STREAM 618: ',G12.5,' G/CC',/," "F 2 ' AEROBIC VOLUME, 15 DAY RES: ',G12.5,' GAL')" "C" "F WRITE(NHSTRY,107)ANVOL1, INMANR, ANVOL, AEVOL1" "F 107 FORMAT(' TOTAL ANEROBIC VOLUME: ',G12.5,' GAL',/," "F 1 ' NUMBER OF ANEROBIC TANKS: ',I4,/," "F 2 ' VOLUME OF EACH ANEROBIC TANK: ',G12.5,' GAL',/," "F 3 ' TOTAL AEROBIC VOLUME (RUCCO): ',G12.5,' GAL')" "C" "F S51021 = S510 + S521" "C HEAT DUTY TO EACH SACCH. COOLER" "F ISAC = SACVES" "F ISAC = ISAC + 1" "F ISACAG = 2 * ISAC" "F QH300A = QF300A / ISAC" "C HEAT DUTY TO EACH FERM COOLER" "F ISSF = SSFVES" "F ISSF = ISSF + 1" "F ISSFAG = 2 * ISSF" "F QEH300 = QF0300 / ISSF" "F HCSOLC = HCSOL*0.251996 / 1000000. * SOLMW" "F HCPROC = HCPRO*0.251996 / 1000000. * SOLMW" "F HCEXTC = HCEXT*0.251996 / 1000000. * SOLMW" ) \ \ TABULATE COLNO = 1 EXPR = "BODHP" LINE1 = "AEROBCHP" \ \ TABULATE COLNO = 2 EXPR = "COD2" LINE1 = "AEROBCOD" \ \ TABULATE COLNO = 3 EXPR = "AEVOL" LINE1 = "AEROBVOL" \ \ TABULATE COLNO = 4 EXPR = "ANVOL" LINE1 = "ANEROVOL" \ \ TABULATE COLNO = 5 EXPR = "A200" LINE1 = "AREA0200" \ \ TABULATE COLNO = 6 EXPR = "A201" LINE1 = "AREA0201" \ \ TABULATE COLNO = 7 EXPR = "A205" LINE1 = "AREA0205" \ \ TABULATE COLNO = 8 EXPR = "A244" LINE1 = "AREA0244" \ \ TABULATE COLNO = 9 EXPR = "A301" LINE1 = "AREA0301" \ \ TABULATE COLNO = 10 EXPR = "A302" LINE1 = "AREA0302" \ \ TABULATE COLNO = 11 EXPR = "AE502" LINE1 = "AREA0502" \ \ TABULATE COLNO = 12 EXPR = "A512" LINE1 = "AREA0512" \ \ TABULATE COLNO = 13 EXPR = "A602" LINE1 = "AREA0602" \ \ TABULATE COLNO = 14 EXPR = "A811" LINE1 = "AREA0811" \ \ TABULATE COLNO = 15 EXPR = "HLETOT" LINE1 = "BURNLOHV" \ \ TABULATE COLNO = 16 EXPR = "DI501" LINE1 = "DIAMD501" \ \ TABULATE COLNO = 17 EXPR = "INMANR" LINE1 = "INUMANER" \ \ TABULATE COLNO = 18 EXPR = "ISAC" LINE1 = "INUMSACC" \ \ TABULATE COLNO = 19 EXPR = "ISACAG" LINE1 = "INUMSACA" \ \ TABULATE COLNO = 20 EXPR = "ISSF" LINE1 = "INUMSSCF" \ \ TABULATE COLNO = 21 EXPR = "ISSFAG" LINE1 = "INUMSSFA" \ \ TABULATE COLNO = 22 EXPR = "P501GP" LINE1 = "P501FLOW" \ \ TABULATE COLNO = 23 EXPR = "QH300A" LINE1 = "QHX310EA" \ \ TABULATE COLNO = 24 EXPR = "QEH300" LINE1 = "QHX300EA" \ \ TABULATE COLNO = 25 EXPR = "S51021" LINE1 = "S510S521" \ \ TABULATE COLNO = 26 EXPR = "WATCON" LINE1 = "WATRCONC" \ \ TABULATE COLNO = 27 EXPR = "WA100" LINE1 = "WORKA100" \ \ TABULATE COLNO = 28 EXPR = "WA200" LINE1 = "WORKA200" \ \ TABULATE COLNO = 29 EXPR = "WA300" LINE1 = "WORKA300" \ \ TABULATE COLNO = 30 EXPR = "WA400" LINE1 = "WORKA400" \ \ TABULATE COLNO = 31 EXPR = "WA500" LINE1 = "WORKA500" \ \ TABULATE COLNO = 32 EXPR = "WA600" LINE1 = "WORKA600" \ \ TABULATE COLNO = 33 EXPR = "WA700" LINE1 = "WORKA700" \ \ TABULATE COLNO = 34 EXPR = "WA900" LINE1 = "WORKA900" \ \ TABULATE COLNO = 35 EXPR = "WA800" LINE1 = "WORKA800" \ \ TABULATE COLNO = 36 EXPR = "PTRR01" LINE1 = "PRETRX01" \ \ TABULATE COLNO = 37 EXPR = "PTRR02" LINE1 = "PRETRX02" \ \ TABULATE COLNO = 38 EXPR = "PTRR03" LINE1 = "PRETRX03" \ \ TABULATE COLNO = 39 EXPR = "PTRR04" LINE1 = "PRETRX04" \ \ TABULATE COLNO = 40 EXPR = "PTRR05" LINE1 = "PRETRX05" \ \ TABULATE COLNO = 41 EXPR = "PTRR06" LINE1 = "PRETRX06" \ \ TABULATE COLNO = 42 EXPR = "PTRR07" LINE1 = "PRETRX07" \ \ TABULATE COLNO = 43 EXPR = "PTRR08" LINE1 = "PRETRX08" \ \ TABULATE COLNO = 44 EXPR = "PTRR09" LINE1 = "PRETRX09" \ \ TABULATE COLNO = 45 EXPR = "PTRR10" LINE1 = "PRETRX10" \ \ TABULATE COLNO = 46 EXPR = "PTRR11" LINE1 = "PRETRX11" \ \ TABULATE COLNO = 47 EXPR = "PTRR12" LINE1 = "PRETRX12" \ \ TABULATE COLNO = 48 EXPR = "PTRR13" LINE1 = "PRETRX13" \ \ TABULATE COLNO = 49 EXPR = "PTRR14" LINE1 = "PRETRX14" \ \ TABULATE COLNO = 50 EXPR = "PTRR15" LINE1 = "PRETRX15" \ \ TABULATE COLNO = 51 EXPR = "PTRR16" LINE1 = "PRETRX16" \ \ TABULATE COLNO = 52 EXPR = "PTRR17" LINE1 = "PRETRX17" \ \ TABULATE COLNO = 53 EXPR = "PTRR18" LINE1 = "PRETRX18" \ \ TABULATE COLNO = 54 EXPR = "PTRR19" LINE1 = "PRETRX19" \ \ TABULATE COLNO = 55 EXPR = "PTRR20" LINE1 = "PRETRX20" \ \ TABULATE COLNO = 56 EXPR = "PTRR21" LINE1 = "PRETRX21" \ \ TABULATE COLNO = 57 EXPR = "PTRR22" LINE1 = "PRETRX22" \ \ TABULATE COLNO = 58 EXPR = "PTRR23" LINE1 = "PRETRX23" \ \ TABULATE COLNO = 59 EXPR = "SACR01" LINE1 = "SACHRX01" \ \ TABULATE COLNO = 60 EXPR = "SACR02" LINE1 = "SACHRX02" \ \ TABULATE COLNO = 61 EXPR = "SACR03" LINE1 = "SACHRX03" \ \ TABULATE COLNO = 62 EXPR = "SACR04" LINE1 = "SACHRX04" \ \ TABULATE COLNO = 63 EXPR = "SACR05" LINE1 = "SACHRX05" \ \ TABULATE COLNO = 64 EXPR = "SACR06" LINE1 = "SACHRX06" \ \ TABULATE COLNO = 65 EXPR = "SACR13" LINE1 = "SACHRX13" \ \ TABULATE COLNO = 66 EXPR = "SACR14" LINE1 = "SACHRX14" \ \ TABULATE COLNO = 67 EXPR = "SACR15" LINE1 = "SACHRX15" \ \ TABULATE COLNO = 68 EXPR = "SACR23" LINE1 = "SACHRX23" \ \ TABULATE COLNO = 69 EXPR = "SACR24" LINE1 = "SACHRX24" \ \ TABULATE COLNO = 70 EXPR = "SACR25" LINE1 = "SACHRX25" \ \ TABULATE COLNO = 71 EXPR = "SACR32" LINE1 = "SACHRX32" \ \ TABULATE COLNO = 72 EXPR = "SACR33" LINE1 = "SACHRX33" \ \ TABULATE COLNO = 73 EXPR = "SACR34" LINE1 = "SACHRX34" \ \ TABULATE COLNO = 74 EXPR = "SACR41" LINE1 = "SACHRX41" \ \ TABULATE COLNO = 75 EXPR = "SACR42" LINE1 = "SACHRX42" \ \ TABULATE COLNO = 76 EXPR = "SACR43" LINE1 = "SACHRX43" \ \ TABULATE COLNO = 77 EXPR = "FRMR07" LINE1 = "FERMRX07" \ \ TABULATE COLNO = 78 EXPR = "FRMR08" LINE1 = "FERMRX08" \ \ TABULATE COLNO = 79 EXPR = "FRMR09" LINE1 = "FERMRX09" \ \ TABULATE COLNO = 80 EXPR = "FRMR10" LINE1 = "FERMRX10" \ \ TABULATE COLNO = 81 EXPR = "FRMR11" LINE1 = "FERMRX11" \ \ TABULATE COLNO = 82 EXPR = "FRMR12" LINE1 = "FERMRX12" \ \ TABULATE COLNO = 83 EXPR = "FRMR16" LINE1 = "FERMRX16" \ \ TABULATE COLNO = 84 EXPR = "FRMR17" LINE1 = "FERMRX17" \ \ TABULATE COLNO = 85 EXPR = "FRMR18" LINE1 = "FERMRX18" \ \ TABULATE COLNO = 86 EXPR = "FRMR19" LINE1 = "FERMRX19" \ \ TABULATE COLNO = 87 EXPR = "FRMR20" LINE1 = "FERMRX20" \ \ TABULATE COLNO = 88 EXPR = "FRMR21" LINE1 = "FERMRX21" \ \ TABULATE COLNO = 89 EXPR = "FRMR22" LINE1 = "FERMRX22" \ \ TABULATE COLNO = 90 EXPR = "FRMR26" LINE1 = "FERMRX26" \ \ TABULATE COLNO = 91 EXPR = "FRMR27" LINE1 = "FERMRX27" \ \ TABULATE COLNO = 92 EXPR = "FRMR28" LINE1 = "FERMRX28" \ \ TABULATE COLNO = 93 EXPR = "FRMR29" LINE1 = "FERMRX29" \ \ TABULATE COLNO = 94 EXPR = "FRMR30" LINE1 = "FERMRX30" \ \ TABULATE COLNO = 95 EXPR = "FRMR31" LINE1 = "FERMRX31" \ \ TABULATE COLNO = 96 EXPR = "FRMR35" LINE1 = "FERMRX35" \ \ TABULATE COLNO = 97 EXPR = "FRMR36" LINE1 = "FERMRX36" \ \ TABULATE COLNO = 98 EXPR = "FRMR37" LINE1 = "FERMRX37" \ \ TABULATE COLNO = 99 EXPR = "FRMR38" LINE1 = "FERMRX38" \ \ TABULATE COLNO = 100 EXPR = "FRMR39" LINE1 = "FERMRX39" \ \ TABULATE COLNO = 101 EXPR = "FRMR40" LINE1 = "FERMRX40" \ \ TABULATE COLNO = 102 EXPR = "FRMR44" LINE1 = "FERMRX44" \ \ TABULATE COLNO = 103 EXPR = "FRMR45" LINE1 = "FERMRX45" \ \ TABULATE COLNO = 104 EXPR = "FRMR46" LINE1 = "FERMRX46" \ \ TABULATE COLNO = 105 EXPR = "FRMR47" LINE1 = "FERMRX47" \ \ TABULATE COLNO = 106 EXPR = "FRMR48" LINE1 = "FERMRX48" \ \ TABULATE COLNO = 107 EXPR = "FRMR49" LINE1 = "FERMRX49" \ \ TABULATE COLNO = 108 EXPR = "SACDAY" LINE1 = "SACHDAYS" \ \ TABULATE COLNO = 109 EXPR = "SSFDAY" LINE1 = "FERMDAYS" \ \ TABULATE COLNO = 110 EXPR = "OSLR01" LINE1 = "OLSLRX01" \ \ TABULATE COLNO = 111 EXPR = "OSLR02" LINE1 = "OLSLRX02" \ \ TABULATE COLNO = 112 EXPR = "OSLR10" LINE1 = "OLSLRX10" \ \ TABULATE COLNO = 113 EXPR = "OSLR11" LINE1 = "OLSLRX11" \ \ TABULATE COLNO = 114 EXPR = "OSLR12" LINE1 = "OLSLRX12" \ \ TABULATE COLNO = 115 EXPR = "OSLR13" LINE1 = "OLSLRX13" \ \ TABULATE COLNO = 116 EXPR = "OSLR14" LINE1 = "OLSLRX14" \ \ TABULATE COLNO = 117 EXPR = "OSLR15" LINE1 = "OLSLRX15" \ \ TABULATE COLNO = 118 EXPR = "SOLMW" LINE1 = "MOWTSOLS" \ \ TABULATE COLNO = 119 EXPR = "EXTMW" LINE1 = "MOWTEXTR" \ \ TABULATE COLNO = 120 EXPR = "PROMW" LINE1 = "MOWTPROT" \ \ TABULATE COLNO = 121 EXPR = "HCSOLC" LINE1 = "HHHVSOLS" \ \ TABULATE COLNO = 122 EXPR = "HCPROC" LINE1 = "HHHVEXTR" \ \ TABULATE COLNO = 123 EXPR = "HCEXTC" LINE1 = "HHHVPROT" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 101 VARYSUBS = MIXED VARYVARIABLE = TEMP LIST = ( 20.0 <0> <0> ) VARYLINE1 = "101 TEMP" OPT-LIST = OLIST \ \ COMMENTS COMMENTS = ( ";;" ";FORTRAN FLOW840" ";; This Fortran block scales the flow of 840 flows from" ";; a specified overall flowrate (variable FL840)." ";; The definition of the biomass fractions is picked up from the" ";; original Stream 101 definition (calculated by FEEDPROP)." ";;" ";; Read the component flow rates from stream 101:" ";; READ Variable - Mass Flow of Extractives" "; DEFINE EXTFLO MASS-FLOW STREAM=101 SUBSTREAM=MIXED &" "; COMPONENT=EXTRACT" ";; READ Variable - Mass Flow of Cellulose" "; DEFINE CELLF MASS-FLOW STREAM=101 SUBSTREAM=CISOLID &" "; COMPONENT=CELLULOS" ";; READ Variable - Mass Flow of Xylan" "; DEFINE XYLF MASS-FLOW STREAM=101 SUBSTREAM=CISOLID &" "; COMPONENT=XYLAN" ";; READ Variable - Mass Flow of Galactan" "; DEFINE GALF MASS-FLOW STREAM=101 SUBSTREAM=CISOLID &" "; COMPONENT=GALACTAN" ";; READ Variable - Mass Flow of Arabinan" "; DEFINE ARBF MASS-FLOW STREAM=101 SUBSTREAM=CISOLID &" "; COMPONENT=ARABINAN" ";; READ Variable - Mass Flow of Mannan" "; DEFINE FMAN MASS-FLOW STREAM=101 SUBSTREAM=CISOLID &" "; COMPONENT=MANNAN" ";; READ Variable - Mass Flow of Lignin" "; DEFINE FLIG MASS-FLOW STREAM=101 SUBSTREAM=CISOLID &" "; COMPONENT=LIGNIN" ";; READ Variable - Mass Flow of Ash" "; DEFINE ASHF MASS-FLOW STREAM=101 SUBSTREAM=CISOLID &" "; COMPONENT=ASH" ";; READ Variable - Mass Flow of Acetate" "; DEFINE ACETF MASS-FLOW STREAM=101 SUBSTREAM=CISOLID &" "; COMPONENT=ACETATE" ";; READ Variable - Mass Flow of Protein" "; DEFINE PROFLO MASS-FLOW STREAM=101 SUBSTREAM=MIXED &" "; COMPONENT=PROTEIN" ";; READ Variable - Mass Flow of Soluble Solids" "; DEFINE SSFLO MASS-FLOW STREAM=101 SUBSTREAM=MIXED &" "; COMPONENT=SOLSLDS" ";; READ Variable - Mass Flow of Water" "; DEFINE H2OFLO MASS-FLOW STREAM=101 SUBSTREAM=MIXED &" "; COMPONENT=H2O" ";; READ Variable - Mass Flow of the CISOLID substream in kg/Hr" "; DEFINE CIFLO STREAM-VAR STREAM=101 SUBSTREAM=CISOLID &" "; VARIABLE = MASS-FLOW" ";; READ Variable - Mass Flow of the MIXED substream in kg/Hr" "; DEFINE FLOMIX STREAM-VAR STREAM=101 SUBSTREAM=MIXED &" "; VARIABLE = MASS-FLOW" ";;" ";; Write the component flow rates to stream 840:" ";; WRITE Variable - Mass Flow of Extractives" "; DEFINE EXT840 MASS-FLOW STREAM=840 SUBSTREAM=MIXED &" "; COMPONENT=EXTRACT" ";; WRITE Variable - Mass Flow of Cellulose" "; DEFINE CEL840 MASS-FLOW STREAM=840 SUBSTREAM=CISOLID &" "; COMPONENT=CELLULOS" ";; WRITE Variable - Mass Flow of Xylan" "; DEFINE XYL840 MASS-FLOW STREAM=840 SUBSTREAM=CISOLID &" "; COMPONENT=XYLAN" ";; WRITE Variable - Mass Flow of Galactan" "; DEFINE GAL840 MASS-FLOW STREAM=840 SUBSTREAM=CISOLID &" "; COMPONENT=GALACTAN" ";; WRITE Variable - Mass Flow of Arabinan" "; DEFINE ARB840 MASS-FLOW STREAM=840 SUBSTREAM=CISOLID &" "; COMPONENT=ARABINAN" ";; WRITE Variable - Mass Flow of Mannan" "; DEFINE FMN840 MASS-FLOW STREAM=840 SUBSTREAM=CISOLID &" "; COMPONENT=MANNAN" ";; WRITE Variable - Mass Flow of Lignin" "; DEFINE FLG840 MASS-FLOW STREAM=840 SUBSTREAM=CISOLID &" "; COMPONENT=LIGNIN" ";; WRITE Variable - Mass Flow of Ash" "; DEFINE ASH840 MASS-FLOW STREAM=840 SUBSTREAM=CISOLID &" "; COMPONENT=ASH" ";; WRITE Variable - Mass Flow of Acetate" "; DEFINE ACT840 MASS-FLOW STREAM=840 SUBSTREAM=CISOLID &" "; COMPONENT=ACETATE" ";; WRITE Variable - Mass Flow of Protein" "; DEFINE PRO840 MASS-FLOW STREAM=840 SUBSTREAM=MIXED &" "; COMPONENT=PROTEIN" ";; WRITE Variable - Mass Flow of Soluble Solids" "; DEFINE SS840 MASS-FLOW STREAM=840 SUBSTREAM=MIXED &" "; COMPONENT=SOLSLDS" ";; WRITE Variable - Mass Flow of Water" "; DEFINE H2O840 MASS-FLOW STREAM=840 SUBSTREAM=MIXED &" "; COMPONENT=H2O" ";;" ";c FL840 is the total desired flow of 840" ";c (Input by user here)" ";F FL840=100" ";;" ";; FLO101 is the total flow of 101 & ratio is the ratio between 840 & 101" ";F FLO101 = CIFLO + FLOMIX" ";F RATIO = FL840 / FLO101" ";;" ";F EXT840 = RATIO * EXTFLO" ";F CEL840 = RATIO * CELLF" ";F XYL840 = RATIO * XYLF" ";F GAL840 = RATIO * GALF" ";F ARB840 = RATIO * ARBF" ";F FMN840 = RATIO * FMAN" ";F FLG840 = RATIO * FLIG" ";F ASH840 = RATIO * ASHF" ";F ACT840 = RATIO * ACETF" ";F PRO840 = RATIO * PROFLO" ";F SS840 = RATIO * SSFLO" ";F H2O840 = RATIO * H2OFLO" ";;" "; EXECUTE BEFORE M803CMB" ";; Not Using READ & WRITE-VARS because it locates fortran block at beginning" ";; READ-VARS EXTFLO CELLF XYLF GALF ARBF FMAN FLIG ASHF ACETF PROFLO &" ";; SSFLO H2OFLO CIFLO FLOMIX" ";; WRITE-VARS EXT840 CEL840 XYL840 GAL840 ARB840 FMN840 FLG840 ASH840 &" ";; ACT840 PRO840 SS840 H2O840" ";;" ";;" "; Reactor block extents of conversion" "; AREA 100 WORK STREAMS" ";Calculates the work for area 100" "; AREA 200 WORK STREAMS" ";Calculates the work for area 200" ";Hot Wash Blowdown Pump +WP228" "; AREA 300 WORK STREAMS" ";Calculates the work for area 300" "; AREA 400 WORK STREAMS" ";Calculates the work for area 400" "; AREA 500 WORK STREAMS" ";Calculates the work for area 500" "; AREA 600 WORK STREAMS" ";Calculates the work for area 600" "; AREA 700 WORK STREAMS" ";Calculates the work for area 700" "; AREA 800 WORK STREAMS" ";Calculates the work for area 800" "; AREA 900 WORK STREAMS" ";Calculates the work for area 900" ";;" "; **** HEAT EXCHANGERS ****" ";;" "; Temperatures in steam manifold." "; H512 AREA" ";;" ";;" "; H200 AREA" ";;" "; H201 AREA" ";;" ";;" ";;" ";;" "; H205 AREA" ";PneumaPress vent condenser" ";;" ";;" ";;" "; H244 AREA" ";;" "; H301 AREA" ";HYDROLYZATE HEATER PRIOR TO SACCHARIFICATION" "; U of 400 from Perry's 6th edition, table 10-10 (Typical Overall Heat" "; transfer coefficients in tubular heat exchangers -- page 10-44)." "; Assumed steam on shell side. Water on tube side gives a U of" "; 400-1000. Used 400 due to solids in water." "; DEFINE T590 STREAM-VAR STREAM=590 SUBSTREAM=MIXED VARIABLE=TEMP" "; DEFINE T591 STREAM-VAR STREAM=591 SUBSTREAM=MIXED VARIABLE=TEMP" ";F DT=((T301-T591)-(T301A-T590))/DLOG((T301-T591)/(T301A-T590))" ";;HYDROLYZATE COOLER PRIOR TO SACCHARIFICATION" ";; Use this section if hydrolysate must be cooled prior to saccharification." "; DEFINE T301 STREAM-VAR STREAM=301 SUBSTREAM=MIXED VARIABLE=TEMP" "; DEFINE T301A STREAM-VAR STREAM=301A SUBSTREAM=MIXED VARIABLE=TEMP" ";; DEFINE T590 STREAM-VAR STREAM=590 SUBSTREAM=MIXED VARIABLE=TEMP" ";; DEFINE T591 STREAM-VAR STREAM=591 SUBSTREAM=MIXED VARIABLE=TEMP" "; DEFINE QHX301 INFO-VAR INFO=HEAT VARIABLE=DUTY STREAM=QH301" ";F DT=((T301-T940)-(T301A-T945))/DLOG((T301-T940)/(T301A-T945))" ";F DT = DABS(DT * 1.8)" ";F U = 300." ";C Convert from cal/s to BTU/hr" ";F Q = QHX301 * 14.2869" ";C Area in square feet" ";F A301 = DABS(Q) / (U * DT)" ";F WRITE(NHSTRY,103)DT,Q,A301" ";F 103 FORMAT(' HX Calc Results',/," ";F 1 ' DT = ',g12.5,/," ";F 2 ' Q = ',g12.5,/," ";F 3 ' A301 = ',g12.5)" ";H302 AREA" ";SACCHARIFIED SLURRY COOLER AFTER SACCHARIFICATION" ";;" "; H502 AREA" ";;" "; Use Diameter of 501 squared for scaling" ";;" ";;" "; H811 AREA" ";;" ";;" ";F DT2=((T819-T813B)-(T823-T813A))/DLOG((T819-T813B)/(T823-T813A))" ";;" ";;" ";;" "; WWT Volume Calculations" "; THIS CODE CALCULATES THE SIZE OF THE ANAEROBIC DIGESTOR" "; AND THE AEROBIC SYSTEM." ";;" ";;" "; **** Other Calculated Variables to be Tabulated ****" ";;" ";;" ";;" ";;" ";;" "; Write Variable - Molecular weight & higher heating values" "; of SOLSLDS, EXTRACT and PROTEIN" "; Used in Energy Balance worksheet" ) \ ? "CONV-OPTIONS" ? \ PARAM CHECKSEQ = NO \ \ WEGSTEIN WEG-MAXIT = 100 WEG-QMAX = .50 <0> <0> \ \ SECANT BRACKET = YES \ \ COMMENTS COMMENTS = ( ";;" ) \ ? TEAR ? \ TEAR SID = 576 / SID = 514 / SID = 521 \ \ COMMENTS COMMENTS = ( ";;" ";-------------------------------------------------------------------" "; RECYCLE/SEQUENCING" ";-------------------------------------------------------------------" ";;" ) \ ? CONVERGENCE WEGSTEIN "C-1" ? \ TEAR SID = 813B \ ? CONVERGENCE WEGSTEIN "C-2" ? \ TEAR SID = QH14CWB \ ? CONVERGENCE SECANT CFUGE3SC ? \ SPEC SPECID = CFUGE3S \ \ COMMENTS COMMENTS = ( ";;" ) \ ? CONVERGENCE SECANT EV1SZ ? \ SPEC SPECID = EV1SIZ \ ? CONVERGENCE SECANT EV2SZ ? \ SPEC SPECID = EV2SIZ \ ? CONVERGENCE SECANT EVAPCNCC ? \ SPEC SPECID = EVAPCONC \ ? CONVERGENCE BROYDEN BRNAIR ? \ TEAR SID = QH801 \ \ SPEC SPECID = COMBAIR \ ? CONVERGENCE BROYDEN TEAR2 ? \ TEAR SID = 621 / SID = QBOILER / SID = QH811 / SID = 812 \ \ TEAR-VAR FOR-BLOCK = CWDEM VAR-NAME = CWBL1 \ \ PARAM MAXIT = 500 \ ? SEQUENCE SEQ7 ? \ SEQUENCE BLOCK-TYPE = CALCULATOR BLOCK-ID = LPSTMD / BLOCK-TYPE = BLOCK BLOCK-ID = M811ISPT \ \ COMMENTS COMMENTS = ( ";;" ";SEQUENCE SEQ3 T507-8 STORE PRODMIX TSTORE" ) \ ? SEQUENCE SEQ8 ? \ SEQUENCE BLOCK-TYPE = BLOCK BLOCK-ID = M811LSPT / BLOCK-TYPE = BLOCK BLOCK-ID = E501LB \ ? SEQUENCE SEQ10 ? \ SEQUENCE BLOCK-TYPE = BLOCK BLOCK-ID = S600 / BLOCK-TYPE = BLOCK BLOCK-ID = H602 / BLOCK-TYPE = BLOCK BLOCK-ID = NUTMIX / BLOCK-TYPE = CALCULATOR BLOCK-ID = CODCALC1 / BLOCK-TYPE = BLOCK BLOCK-ID = T606 / BLOCK-TYPE = BLOCK BLOCK-ID = T606FLSH / BLOCK-TYPE = CALCULATOR BLOCK-ID = CODCALC2 / BLOCK-TYPE = CALCULATOR BLOCK-ID = AERAIR / BLOCK-TYPE = BLOCK BLOCK-ID = T608 / BLOCK-TYPE = CALCULATOR BLOCK-ID = CODEND \ ? SEQUENCE SEQ11 ? \ SEQUENCE BLOCK-TYPE = CALCULATOR BLOCK-ID = POWER / BLOCK-TYPE = CALCULATOR BLOCK-ID = MISCPOW / BLOCK-TYPE = BLOCK BLOCK-ID = AIRCMP / BLOCK-TYPE = BLOCK BLOCK-ID = MPOW1 / BLOCK-TYPE = BLOCK BLOCK-ID = MPOW2 / BLOCK-TYPE = BLOCK BLOCK-ID = MPOW5 / BLOCK-TYPE = BLOCK BLOCK-ID = MPOW6 / BLOCK-TYPE = BLOCK BLOCK-ID = MPOW8 / BLOCK-TYPE = BLOCK BLOCK-ID = MPOW10 \ ? SEQUENCE SEQ12 ? \ SEQUENCE RETURN = BEGIN BLOCK-TYPE = CONVERGENCE BLOCK-ID = CFUGE3SC / BLOCK-TYPE = CALCULATOR BLOCK-ID = CFUGESLD / BLOCK-TYPE = BLOCK BLOCK-ID = S505 / BLOCK-TYPE = BLOCK BLOCK-ID = S505FLSH / RETURN = RETURNTO BLOCK-TYPE = CONVERGENCE BLOCK-ID = CFUGE3SC \ ? SEQUENCE SEQ13 ? \ SEQUENCE RETURN = BEGIN BLOCK-TYPE = CONVERGENCE BLOCK-ID = EVAPCNCC / BLOCK-TYPE = BLOCK BLOCK-ID = E501LOSS / RETURN = BEGIN BLOCK-TYPE = CONVERGENCE BLOCK-ID = EV1SZ / BLOCK-TYPE = BLOCK BLOCK-ID = E501L / BLOCK-TYPE = BLOCK BLOCK-ID = E502V / BLOCK-TYPE = BLOCK BLOCK-ID = E502LOSS / BLOCK-TYPE = BLOCK BLOCK-ID = DCOOL2 / BLOCK-TYPE = SEQUENCE BLOCK-ID = SEQ12 / BLOCK-TYPE = BLOCK BLOCK-ID = T530 / RETURN = BEGIN BLOCK-TYPE = CONVERGENCE BLOCK-ID = EV2SZ / BLOCK-TYPE = BLOCK BLOCK-ID = E502L / BLOCK-TYPE = BLOCK BLOCK-ID = E503V / BLOCK-TYPE = BLOCK BLOCK-ID = E503LOSS / BLOCK-TYPE = BLOCK BLOCK-ID = E503L / RETURN = RETURNTO BLOCK-TYPE = CONVERGENCE BLOCK-ID = EV2SZ / RETURN = RETURNTO BLOCK-TYPE = CONVERGENCE BLOCK-ID = EV1SZ / RETURN = RETURNTO BLOCK-TYPE = CONVERGENCE BLOCK-ID = EVAPCNCC \ ? REPORT "BLOCK-REPORT" ? \ OPTIONS TOTBAL = NOTOTBAL INPUT = NOINPUT INCL-BLOCKS = ( M811ISPT D501 D502 M811HTRB M811ITRB M811LTRB M811VLRB F400 "F401-4" AFLSH ) \ \ COMMENTS COMMENTS = ( "; NODESCRIPTION" ";;" "; NODESCRIPTION Eliminates the Convergence Summary, but also gets rid of th" "; flowsheet connectivity" ";;" ) \ ? REPORT "STREAM-REPOR" ? \ OPTIONS MOLEFLOW = NOMOLEFLOW MASSFLOW = MASSFLOW PROPERTIES = ( CP1 CP2 FRAC COMP1 COMP2 ) \ \ COMMENTS COMMENTS = ( ";;" "; Use EXCL-STREAMS = or INCL-STREAMS = to reduce the number of blocks report" "; With Ion Exchange need to eliminate 10 streams from the report" "; EXCL-STREAMS = 905 909 &" "; 922 923" ) \ ? REPORT "FLOWSHEET-RE" ? \ OPTIONS TOTBAL = NOTOTBAL CONVERGENCE = NOCONVERGENC COMPBAL = NOCOMPBAL FORTRAN = NOFORTRAN DESIGN-SPEC = "NODESIGN-SPE" \ \ COMMENTS COMMENTS = ( ";;" ) \ ? REPORT "PROPERTY-REP" ? \ OPTIONS PARAMS = PARAMS \ \ COMMENTS COMMENTS = ( ";REPORT NOPROPERTIES" ) \ GRAPHICS_BACKUP PFS V 5.00 $CONFIG paramdata ENRTL-RK paramdata VLE-IG paramdata VLE-RK paramdata VLE-HOC paramdata LLE-LIT paramdata LLE-ASPEN paramdata VLE-LIT paramdata BINARY paramdata EOS-LIT paramdata HENRY paramdata SRK-ASPEN purebank PURE12 purebank AQUEOUS purebank SOLIDS purebank INORGANIC regdbank 1 ftn_check 1 autoblockid 1 autostreamid 1 showblockid 1 showstreamid 1 autoplacement 1 grid 2 gridresolution 0.100000 scale 0 streamprefix blockprefix B labelscale 1.000000 qwformat %.0f tempformat %.0f presformat %.0f flowformat %.0f strmqwformat %.0f vflowformat %.0f mflowformat %.0f vfracformat %.2f pseudobatch 0 partial 1 animation 1 runanyway 0 tooldrawvisible 0 browserheight 9705 browserwidth 14115 browsertreewidth 2895 polyplusenabled 1 dynaplusenabled 1 bfracenabled 1 rtfenabled 1 pinchenabled 0 linklimit 500 material_color 0 material_style 983041 material_width 1 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