ASPEN "12.1" DATETIME "08/23/2005 08:29:19:99" MACHINE "WIN32" SITEID "" USER "kibsen" ? SETUP SYS-OPTIONS ? ; ENG ; \ SYS-OPTIONS INTERPRET = NO \ ? SETUP UNITS-SET SET1 ? \ 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 GLOBAL ? \ IN-UNITS INSET = SET1 \ \ COMMENTS COMMENTS = ( ";" ";IN-UNITS MET TEMPERATURE=C" ) \ ? SETUP UNITS-SET SET2 ? \ 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 GLOBAL ? \ IN-UNITS OUTSET = SET2 \ \ COMMENTS COMMENTS = ( "; MASS-ENTROPY='KCAL/KG-K'" ) \ ? SETUP RUN-CONTROL ? ; SET1 ; \ PARAMETER MAX-TIME = 20000.0 <0> <0> MAX-ERRORS = 4000 MAX-FORT-ERR = 200 \ ? SETUP DIAGNOSTICS ? ; SET1 ; \ MSG-LEVEL SYS-LEVEL = 4 SIM-LEVEL = 4 PROP-LEVEL = 2 STREAM-LEVEL = 4 \ ? SETUP DIAGNOSTICS ? ; SET1 ; \ MAX-PRINT SIM-LIMIT = 1000 \ ? SETUP SIM-OPTIONS ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ SIM-OPTIONS PROP-DERIV = NUMERICAL \ ? SETUP MAIN ? ; SET1 ; \ COMMENTS COMMENTS = ( ";***************************************************************************" ";***************************************************************************" ";** NREL PROTECTED INFORMATION" ";***************************************************************************" ";***************************************************************************" ";" "; NREL Biomass to Ethanol Process" "; NREL Protected Information" "; Best Case Cofermentation (4_96a.INP)" "; Modified to include the NREL Biofuels Databank of Physical Properties" "; Authors: Vicky Putsche, Bob Wooley, Mark Ruth, Kelly Ibsen" "; Date: April 26, 1996" ";Changes" ";-------------------------------------------------------------------------" "; bw0401a_simp.inp Bob Wallace January 27, 2004" "; 1. Changed C6SUGAR to C6H12O6, from C6H10O5" "; 2. Change STOIC 10 in M202HI, add MIXED H2O -1 into reaction" "; 3. Did the same for reaction 1 in M202HI, Rx 1 in T310" "; 4. Subtracted one mole of H2O from rx 35 in F300F and rx 4 in F300CONT" "; 5. Added one mole H2O in F400 rx 2 and F401-4 rx 2, from 3.5947 to 4.5947" "; 6. Changed H2O from 5 to 6 in rx 18 of BURNER" "; 7. Changed QSTM_M from .0054217 to .0070039 after recalculation of latent" "; heat value" ";-------------------------------------------------------------------------" "; bw0302cs.inp Bob Wallace March 4, 2003" "; 1. Cleaned up all of the comments from I0302CS" ";-------------------------------------------------------------------------" "; I0302CS.inp KNI 10 FEb 2003 H301 change" "; 1. Changed H301 equipment scaling to QH301 stream, since no 590/591 T" "; available for calculating DT. Same concept as QRD501." "; 2. Added sensitivity variable QSTMH301 for Excel sheet." "; 3. Removed H301 DT, Q calculation from sensitivity block." ";--------------------------------------------------------------------------" "; I0302BS.inp KNI 8 Feb 2003 H201 fix" "; 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'Connel" "; 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" "; 9. Use QH301 to size H301, since don't have 590/591 streams for DT calc." ";10. Made QSTM_M negative since QRD502 is negative." ";11. Used I0302B values for ratios in WWT, BOILECON" ";12. Added design spec H201TEMP." ";--------------------------------------------------------------------------" "; I0302AS.inp KNI 8 Feb 2003 Incorporating relevant MR fixes in R0302B" "; 1. Added moles of 261 & 560 to BOILRAIR fortran block (supplementing 804 a" "; to combustor). Corrected F02 to FO2 in REQO2 calculation." "; 2. Changed CNNH4 in CODCALC1, CODCALC2, & CODEND from 1.143 to 1.557" "; to match NO2 production instead of N2 productioN." "; 3. Removed centrifuge, reactor and dryer number calculations and tabulate" "; stmts for them. Also removed ACET220A, CLVESSEL, SULF220A." "; 4. Removed ACET220A, CENTFLOW, CLVESSEL, SULF220A from aspen Excel sheet." "; 5. Changed multiplier for solslds moles in BOILRAIR to match R0302B." "; 6. Changed stream from H200MIX from 240A to 223 to match R0302B." "; 7. Modified fortran D502QCR eqns for REBFCT, CNDFCT to match R0302B." "; 8. Changed QCD501,QRD501,QCD502, QRD502 initial values to match R0302B.rep" "; 9. Modified D502OVHD ethanol/water spec in 511 from 0.925 to 0.926" "; (to match R0301C - stand alone dist.)" ";10. Modified D502 so that all the CO2 goes into stream 511 instead of 516" "; (to match R0301C result)" ";11. Modified temps in D502 to match R0103C results. Not enough steam now, s" ";12. Steam balance fixes:" "; -Added variable QMDMDH defined as QRD502 heat duty to BOILECON" "; -Removed QRD502 from low P HX mixer block QHXLOW" "; -Added calcs in BOILECON to add QRD502 load to med P plant load" "; -Changed 215 stream specs to match 216 (P=13 atm, T=268.8913 C)" "; -Moved STM215 variable to med P plant demand calc in BOILECON." "; -Changed UB on EVAPCONC (10 to 50)." ";13. Added initial estimates to 303A & 304A to prevent FERMDAP & FERMCSL" "; from losing properties of 311 & 311A" ";--------------------------------------------------------------------------" "; I0301CS.inp KNI 1/28/03" "; 1. Added HMF properties from BIODFMS3 changes to HMF in input language to" "; make them work, per Jechura." "; 2. Slight fixes to BOILECON ratios using I0301B. Added BOILECON sheet to" "; Excel spreadsheet to document variables in BOILECON." "; 3. Removed H301+, QH301EX, D-S SACCHEAT, steam streams 590/591." "; added QH301 to QHXLOW block to be included in BOILECON calcs for LP stm" "; 4. Made H205 area calculation variables more specific to avoid picking up" "; other values." "; 5. Corrected CWF calculation in fortran CW." "; 6. Adjusted WWT cost equation to match I0301B (adjusted intercept)." "; 7. Rechecked physical props against BIODFMS3 and R0302B.inp" ";--------------------------------------------------------------------------" "; I0301BS.inp KNI 1/15/03 Simplified model of 2002 design report model" "; 1. Added stream 256 temp to H200 area calculation." "; 2. Adjusted DHFORM of SOLSLDS to match I0301B, final fix of DHFORM for now" "; 3. Adjusted NOATOM of SOLSLDS to match I0301B, also BURNER coeffs for rxn." "; 4. Added Mixer H200MIX before H200 to better handle area calculation." "; 5. Changed WUSED in BOILECON fortran block based on I0301B results." "; 6. Removed ""Plant Electricty Use"" from Summary sheet in Excel. Not a true" "; value, since the boiler work is calculated in Aspen before reporting" "; the net work to Excel." "; 7. Changed ratios in BOILECON fortran block based on I0301B results." "; 8. Changed WWT ratios to match I0301B results." ";--------------------------------------------------------------------------" "; I0301AS.inp KNI 1/11/03 simplified model of 2002 design report model" "; Need to review WWT, BLR ratios when SOLSLDS phy. props is resolved:" "; WWT (I0203IP3 values)" "; WATERDEM, BOILECON, CW (I0203I values)" "; 2. Changed CH4 yield to 0.2289 (was 0.221) in WWT. 0.2289 is based on" "; USRAN4. 0.221 was from previous Merrick design." "; 3. Matched SOLSLDS DHFORM and NOATOM to Feedprop printout in I0203I.his" ";--------------------------------------------------------------------------" "; I0212AS.INP KNI 12/29/02 Simplified Model of 2002 design report model" "; 1. Changed pressure specs in blocks E501L, E502L, E503L to match streams" "; 526 (0.571 atm) and 528 (0.3042 atm) in report file of I0203IP3" "; (I0203IP3 is the BIODFMS3 version of I0203I - Solslds DHFORM issue)." "; 3. Removed DAP from S505 splits so that it does not recycle (should be" "; consumed in fermentation)." "; 4. Added rxn 36 to F300F to convert C6SUGAR to ORGANISM to add CISOLIDS" "; to evaporator feed - trying to get biomass production amount to match." "; 5. Changed split of SOLSLDS in S505 from 0.5 to 0.1." "; 7. Made minor fixes to S205SOL fortran block." "; 8. Updated ratio of 624/612 streams to calculate 624 in fortran WATERDEM." "; 9. Updated ratio of evap. water from CW tower in fortran CW." ";10. Updated ratios of QH602 and WWT power in fortran WWT." ";--------------------------------------------------------------------------" "; bw0211c.inp Bob Wallace 12/11/2002 USDA Model" "; Attempting to match up heat exchanger areas with design case" "; 1. Matched blocks H201+A, H201+B, and H201- to match design case" "; 2. Changed design spec on H201- to match the design case, T=95 and P=4" ";---------------------------------------------------------------------------" "; bw0211b.inp Bob Wallace 11/20/2002 USDA Model" "; 1. Replaced T302 with T301B and T302A with T301C in heat exchanger" "; FORTRAN block H302" "; 2. Stream 101 lines up with design model (report files)." ";--------------------------------------------------------------------------" "; bw0211a.inp Bob Wallace 11/8/2002 USDA model" "; 1. Changed the reflux ration in Area 500 from 7 to 3 to match I0203I" "; 2. Changed initail guesses of QCD501, QRD501, QCD502, & QRD502 to match" "; I0203I. This did not effect results, since guesses were just a start" "; point for the iterations." ";--------------------------------------------------------------------------" "; BW0208E.inp Bob Wallace 11/1/2002 USDA Model" "; 1. Raised the C6SUGAR conversion in T310 from cellulose to 0.052 from 0." "; 2. Raised the conversion of C6SUGAR to ethanol in F300F from .03 to .032" "; This gives us the same yield (gal/ton) and annual production (69.3MMGal/yr" "; as the I0203I model" ";--------------------------------------------------------------------------" ";I0208D.inp" "; 1. Changed MW of C6SGUAR from 180 to 162 in physical properties." "; This change was made to match the MW of glucolig in the I0203I model" "; so that the heat of QF300A would more closely match that of the" "; rigerous model. It had been negative in previous runs." "; 2. Changed all RSTOIC reactions containing C6SUGAR by adding a H2O to the" "; reaction to solubilize the C6SUGAR." ";--------------------------------------------------------------------------" "; I0208C.inp BW 23 August 02" "; 1. Updated BOILECON ratios using I0203I values." "; 2. Updated BFW calculation ratio (stream 821 & QBOILER) using I0203I.inp." ";--------------------------------------------------------------------------" "; I0208B.inp KNI 16 August 02" "; 1. Cleaned up physical properties by pasting PROPDATA-3 into this file." ";--------------------------------------------------------------------------" "; I0208A.inp KNI 11 August 02" "; 1. Changed solslds in stream 101 to match solslds + extractives + protein" "; flowrates calculated in I0203I Fortran block FEEDSTK = 7416.67 kg/hr." "; 2. Changed CISOLID flow rate to ((2000*1000)/24) - 7416.67) = 75916.66 kg/" "; 3. Changed mass fracs of CISOLID components in stream 101 to match adjuste" "; FEEDSTK in I0203I: variable TOT =.9104" "; CELLULOSE 0.410808" "; XYLAN 0.231437" "; C5SOLID 0.0320738" "; C6SOLID 0.0384446" "; LIGNIN 0.19760545" "; ACETATE 0.0321837" "; ASH 0.05744728" "; 4. Changed SOLSLDS property values for NOATOM and BURNER rxn #27" "; stoichiometry to match I0203I FEEDPROPS calcluations from history file." "; DHFORM is not changed to FEEDPROP calculated value, as I0203I is not" "; using it correctly yet - pulling DHFORM from in-house database." "; 5. Removed reflux ratio spec from D501 to match I0203I (J. Jechura tech" "; memo 2001)." "; 6. Added soluble lignin variable to calcs for stream 219." "; 7. Added If/Then statement to BOILECON to set BFW chems to 0 if no makeup" "; water (811) is needed." "; 8. Changed acid concentration in D-S ACIDCONC to 0.011 to match I0203I." "; 9. Changed M202HI temp to 190 C." ";10. Changed M202HI lignin to 5%." ";11. Changed inlet stream temps to match I0203I (most to 20 C)." ";12. Added stream 262 to S600 block (condensate from H205)." ";13. Added stream 104A to C103A sep block in flowsheet A100." ";14. Changed CONC1 in Fortran RECYCLE to 0.30 from 0.3091." ";15. Corrected LIGNIN VSPOLY first coeff. from 0.0133 to 0.1033" "; (typo on spreadsheet in Phys Props addendum report)." ";16. Changed temp of H200 from 40 to 50 C to match I0203I." ";17. Matched phys props up to BIODFMS3 which gives I0203I results." ";--------------------------------------------------------------------------" "; I0207K.inp KI 18 July 02" "; 1. Made changes KI and BWa found on 7/18/02." "; 2. Added list of PARAMETERS in use immediately before code starts" "; 3. Renamed SSFVES from PARAM 4 to PARAM 31" "; 4. Removed COMMON RXCON (previously, it had been commented out)" "; 5. Removed FRMSET & set the following params, renamed PUMPFLO to" "; PMPSSF and column name from PUMPFLOW to PUMPSSCF in sensitivity:" "; SSFDAY 32" "; SSFVOL 33" "; SSFWV 34" "; PMPSSF 35" "; 6. Removed CLSSET & set the following params" "; CLYLD 41" "; CLPROD 42" "; CLVES 43" "; CLVOL 44" "; CLWV 45" "; 7. Added params for Saccharification calcs to param list after comments" "; and to fortran SETVAR and MASSFLOW:" "; SACVES 36" "; SACDAY 37" "; SACVOL 38" "; SACWV 39" "; PMPSAC 40" "; 8. Added QF300A to block T310 in flowsheet section." "; 9. Added P-310 power calculation to MASSFLOW block, AP310 is variable" "; passed to Excel under column name VOLFM310. Based on P-300." ";10. Added work calculation for sacch. agitators A-310 to MASSFLOW." "; Based on A-300." ";11. Renamed WNET to PARAMETER 8 since PARAMETER 5 is P501GP." ";12. Commented out seed cellulase calculations in fortran ENZYME." ";13. Added calculation of volume of T310 (variables SAVT/VOLFS310) to MASSFL" ";14. Added power variable calcs for A-720, A-760, P-755, C-755." ";15. Combined Pnuemapress powers (WM205, WM505) with plant air 250 hp in WCM" ";--------------------------------------------------------------------------" "; Model bw0112k.inp Bob Wallace July 10, 2002 Usda Phase II" ";1. Added blocks M505COOL, S505FLSH in FLOWSHEET PNEUMOPRESS area and" "; BLOCK area" ";2. Added S505FLSH into SEQ12" ";3. Added QM505 to HEATCW-S and DEF-STREAMS HEAT" ";4. Changed vary statement in design spec CFUGE3S from 571 to 571B" ";5. Changed solid stream exiting S505 from 571 to 571B" ";6. Changed FORTRAN CFUGESLD statements from 571 to 571B" ";7. Added BLOCK M802MIX to FLOWSHEET and BLOCK areas" ";8. Changed M802 to M802MIX at the end of FORTRAN BOILRAIR" ";9. Added M802MIX in SEQ14" ";--------------------------------------------------------------------------" "; Model bw0112i.inp Bob Wallace July 2, 2002 Usda Phase II" "; Changes made to Saccharification and Fermentation area" "; Made changes from 2002 Design Report adding a separate" "; saccharification step" ";1. Removed QF301-6A from FLOWSHEET A900 and DEF-STREAMS HEAT" ";2. Added the following blocks to FLOWSHEET 300" "; H301, H301+, T310, H302, SACCHSPT, SEEDMIX, FERMMIX" ";3. Deleted the following blocks from FLOWSHEET 300" "; F301-6H, H301, SSFSPLT, F300H" ";4. Changed block H302 to match that of I0203I.inp" ";5. Replaced AREA 300 SSCF CBlocks with AREA 300 Saccharification and" "; cofermentation blocks from I0203I" ";6. Moved QH302 inlet stream from CHCWMIX to HEATCW-S" ";7. Removed QH301 from CHCWMIX" ";8. Commented out STREAM 316 and all of its components" ";9. Commented out FORTRAN BLOCK ENZ2S" ";10. Changed FORTRAN BLOCK ENZ2 to match that of I0203I for separate" "; saccharification and fermentation steps." ";11. Commented out 302, 302A lines from MASSFLOW sensitivity" ";12. Added STREAM 590" ";--------------------------------------------------------------------------" "; Model bw0112g.inp Bob Wallace June 27, 2002 USDA Phase II" ";" "; Pretreatment Separation area. Pneumopress changes" ";1. Added the following blocks" "; M205COOL, M205FLSH, H205, H244" ";2. Added the following streams to HEATCW-S, DEF-STREAMS HEAT" "; QH244, QH205, QM205" ";3. Added pneumopress FORTRAN blocks H205, M205COOL, S205FLSH, H205, H244" ";4. Deleted Stream 237, no longer need to send steam to overliming tank" ";5. Commented out design spec HT-T209, LP steam calculation for stream 237" ";6. Changed stream 255 to 255A into S205FLSH, out of S205B and in" "; BLOCK S205B, insoluble solids recovered by pneumopress." ";7. Changed stream 520 to 520A into H244, out of H201+B and in" "; sensitivity H201" ";8. Changed T520 to T520A in sensitivity H201" ";--------------------------------------------------------------------------" "; Model bw0112f3 Bob Wallace" "; Date: February 13, 2002" "; 1. Changed enzyme loading from 15% to 10%" "; 2. Changed SSF residence time (SSFDAY) from 7 to 3 days" "; 3. Changed hydrolysis temperature (F300H) from 30 C to 65 C" "; 4. Changed fermentation temperature (F300F) from 30 C to 41 C" "; 5. Changed chilled water fraction (QH14BSP) from 20% to 0% (.000000001)" "; 6. Changed contamination loss (CONTSPLT) from 7% to 3%" ";---------------------------------------------------------------------------" "; Model bw0112e1 Bob Wallace" "; Date: February 6,2002" "; Y Removed IX by removing sequence SEQ9" "; Y forts IXRGNFLW, PREACID -- Modified OLIME to read stream 240 not 236" "; N & 0'd costs of S-221, A-202, P-225&6, A-235" "; Y Removed STORE vars AMFLW1 (242) & AFLOW3 (235)" "; N& CHEMICAL var FLWIX3 (243)" "; Y PUMPS calcs & vars for P-225 & P-226, IX power calc." "; Y& WATERDEM var FLIX3" "; Y also removed blocks A202, S221A, S221B, & A235, and" "; Y streams 242, 243, 244, 245 (from E501SPT, too), 241, 246, 247" "; Y (from S600, too), 235, 236 (from T209, too - changed to 240)" "; Y3. Added stoichiometric flow to the liming factor in OLIME to neutralize" "; the acid in stream 240 (more now, since no IX to remove it)." "; Y4?. Made 230 the outlet of T224" "; Y5. Made 240 an inlet to T209" ";---------------------------------------------------------------------------" "; bw0112e.inp Bob Wallace" "; Jan 24, 2002" "; Changes to block m202hi" "; 1. Changed Xylan to tar(c5solids) yeild to .05" "; 2. Changed Changed lignin to soluble lignin yeild to .3 from .05" "; (with this change, the model had an error in the E501SPT block)" "; 3. Changed C6 solid conversion to C6 sugar conversion to.95" "; 4. Changed C6 solid conversion to HMF conversion to .05" "; 5. Changed C5 solid conversion to C5 sugar conversion to.95" "; 6. Changed C5 solid conversion to Furfural conversion to .05" "; 7. Changed Xylan to C5 Sugar conversion to .025 from .05" "; Changes to stream 101" "; 1. Changed mass flow to 73458 kg/hr" "; 2. changed cellulose mass frac to 0.4203" "; 3. changed xylan mass frac to 0.2260" "; 4. changed C5 solid mass frac to 0.0287" "; 5. changed C6 solid mass frac to 0.0333" "; 6. changed lignin mass frac to 0.2061" "; 7. changed acetate mass frac to 0.0268" "; 8. changed ash mass frac to 0.0588" "; Changed acid conc from .005 to .0035 in acidconc" ";---------------------------------------------------------------------------" "; bw0112c.inp Bob Wallace" "; 1. Changed temp to 150 C in m202hi" "; 2. Changed pressure of Stream 216 to 5.5 atm" ";---------------------------------------------------------------------------" "; Changes" "; BW0112b.inp Bob Wallace" "; January 22,2002" "; Block M202HI" "; 1. Changed xylan to xylose yeild to .9" "; 2. Changed xylan to furfural yeild to .025" "; 3. Changed xylan to oligomer(C5 sugar) yeild to .025" "; Block F300F" "; 4. Changed glucose to EtOH yeild to .95" "; 5. Changed glucose to DAP yeild to .017" "; 6. Changed glucose to Aacid yeild to .015" "; 7. changed glucose to lacid yeild to .015" "; 8. changed xylose to ethanol yeild to .9" ";----------------------------------------------------------------------" "; Changes" "; I0112A.inp; 12/17/01; KNI Trying to get H201 to run in GUI" "; 1. Removed T spec on H201- becuase enthalpy across H201+/H201- was" "; out of balance; not enough heat in QH201+QH201B to get to 95C." "; 7. Also moved QH201 to outlet of H201+A, and to inlet of H201-." ";----------------------------------------------------------------------" "; I0108B.inp; 8/10/01; KNI More GUI corrections" "; 1. Replaced prop-data stmts with ones from GUI." "; 2. Changed CO2 spec in D501 to match input file from GUI (I0108C)." "; 3. Removed SO2 from streams 434 and 436." "; 4. Added BLOCK-REPORT stmt with certain blocks to correct GUI problem" "; reading some blocks." "; 5. Changed P spec on E501L and E502L to match A0103A.rep, since no design" "; spec to change them anymore." ";----------------------------------------------------------------------" "; I0108A.inp; 8/3/01; KNI Making corrections to move into GUI running." "; 1. Added DAP to SEP blocks." "; 2. Commented out DEFINE statements in MASSFLOW that had variables starting" "; with ZZ." "; GUI didn't like P only spec so:" "; 3. Changed H201+A heat stream QH201 to an outlet. GUI didn't allow PV spec" "; with an inlet heat stream. Changed QH201 to an in in block H201-." "; 4. Made A235 PQ spec." "; 5. Made T-224 PQ spec." "; 6. Made H-201- a P only spec for the GUI rules." "; 7. Changed D501 CO2 spec from 0.845 to 0.83." "; 8. Cleaned up sensitivity block." "; 9. Got rid of LGNSOL prop stmts to see where GUI HS-2 is coming from." ";----------------------------------------------------------------------" "; I0107SB.inp; 7/4/01; KNI Simplified NREL model based on FY01 Benchmark mo" "; 1. Removed and combined components based on I0104D except lgnsol & DAP." "; 2. Changed databanks stmts to remove INHSPCD refs (in-house database)." "; 3. Used new (MR) DHFORM for SOLSLDS. NOATOM/ATOMNO was already the same." "; Added other properties from biodfms2 for SOLSLDS." "; 4. Used lgnsol properties from MR already in A0103A." "; 5. Removed property stmts for area 800." "; 6. Removed TEAR/TRACE stmts because GUI didn't like them last time." "; 7. Commented out TEAR2 and BRNAIR until I see what I need." "; 8. Changed SEQ10 because WWT blocks will be removed." "; 9. Commented out SEQ7 (boiler) and SEQ9 (power)." ";10. Changed SEQ13 because LOSS blocks and EV1SIZ and EV2SIZ will be removed" ";11. Removed convergence for EV1SIZ and EV2SIZ." ";12. Commented out WWT blocks to use J. Sheehan equation in fortran WWT." ";13. Commented out Boiler blocks to use R. Wooley fortran block." ";14. Added BTUTOT and BLRWTR blocks to sum feeds and BFW, respectively." ";15. Commented out turbogenerator blocks to use R. wooley fortran block." ";16. Leave at 2000 mTPD for now to compare results." ";17. Change CSL, Oil CNUTR, WNTUR to H2O, Cellulase, Zymo, Biomass to Organi" "; 10 CISOLID, 22 MIXED components for SEP blocks." ";18. No changes to params (yield, temp) yet." ";19. Adjusted M202 reactions/conversions. Left lignin solub. reaction in." ";20. Removed A202." ";21. Replaced F400 and F401-4 completely with I0004D code." ";22. Removed turbogenerator blocks and replaced M803CMB with block BURNER." ";23. Added lgnsol conversion to BURNER block." ";24. Removed all design specs that calc. steam flows." ";25. Removed design specs for WWT, Burner/Tgen, CW and CHW" ";26. Removed extra components from S-205 fortran block." ";27. Removed extractives and protein define stmts from fortran RECYCLE." ";28. Replaced CODCALC fortran blocks with fortran WWT from I0004D.inp." ";29. Replaced all Boiler fortran stmts with fortran BOILECON." ";30. Removed all turbogenerator fortran blocks." ";31. Added soluble lignin to fortran BOILRAIR." ";32. Replaced fortran CWDEM with CW in its entirety." ";33. Added TRTWW calculation to fortran WATERDEM." ";34. MAY NEED TO RECALC RATIOS IN BOILECON FROM NEWER CASE." ";35. NEED TO PICK THE CASE TO MODEL - 2010?" ";36. Made SSFVES parameter 8 (changed from 4, since 4 already used)." ";37. Need to add T-205 to agitator power calcs in spreadsheet." ";38. Need to add P-101,102,103,104,105,205, 211, 213, 750 to spreadsheet." ";39. Need to add misc power for area 100, M-202, S-205, S-530 to spsheet." ";40. Replaced tabulate section with I0004D except left in 2xx stmts." ";41. Changed C103C from SEP block to MIXER since polymer stream is water." ";----------------------------------------------------------------------" "; A0103A.inp; 28 MARCH 2001; Design Case for Process Design Update 2001" "; 1. Consolidated all air compressor requirements into two compressors" "; for the plant instead of 6 separate ones (4 for pneumapresses and" "; 2 for plant air). Kept this as M904 but created a new equipment" "; cost for it via ICARUS. Cellulase air compressor (M401) still" "; kept separate but since it's not currently used, it doesn't matter" "; 2. Relabeled WM904 as WM904A." "; 3. Added block AIRCMP (mixer block) to sum plant and instrument air" "; and pneumapress air requirements. Outflow stream is now WM904." "; Inlet flows are WM205, WM505, WM904A. Disconnect WM205 from" "; MPOW2, WM505 from MPOW5, and WM904A from MPOW10." "; 4. Define new work stream WM904." "; 5. Connected stream WM904 to inlet of MPOWTOT." "; 6. Eliminate M-205 and M-505 compressors from equipment list in" "; excel." ";----------------------------------------------------------------------" ";===========================================================================" "; Total Plant File" ";===========================================================================" ";" ) \ \ TITLE TITLE = "BIOMASS TO ETHANOL PROCESS: TOTAL PLANT **NREL PROTECTED INFO**" \ \ COMMENTS COMMENTS = ( ";" ";===========================================================================" "; Physical Property Data" ";===========================================================================" ";" "; New Statements setting up the NREL Biofuels Database" ";" ) \ ? REPORT REPORT ? ; SET1 ; \ COMMENTS COMMENTS = ( ";STREAM-REPORT WIDE MOLEFLOW NOZEROFLOW NOCOMP-ATTR NOSUBS-ATTR" ";" "; 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" ) \ \ SECTIONS PROPERTIES = PROPERTIES \ ? %M FLOWSHEET A100 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";----------------------------------------------------------------" "; FLOWSHEETS" ";---------------------------------------------------------------" ";" ";THIS IS THE FLOWSHEET FOR FEED HANDLING." ) \ \ BLOCK BLKID = C103A IN = (102 X 107 X) OUT = (104D X) \ \ BLOCK BLKID = C103B IN = (104D X) OUT = (104B X 102A X) \ \ BLOCK BLKID = C103C IN = (104B X) OUT = (104 X) \ \ BLOCK BLKID = M104LOSS IN = (102A X) OUT = (103 X 102B X) \ \ BLOCK BLKID = M104MIX IN = (102B X 101 X) OUT = (105 X) \ ? %M FLOWSHEET A200 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";THIS IS THE FLOWSHEET FOR THE PRETREATMENT AREA AND INCLUDES PRETREATMENT" ";AND DETOXIFICATION." ) \ \ BLOCK BLKID = A201 IN = (212 X 211 X) OUT = (214 X) \ \ BLOCK BLKID = M202MIX IN = (105 X 214 X) OUT = (214A X) \ \ BLOCK BLKID = M202LO IN = (214A X 215 X) OUT = (215A X QM202LO X) \ \ BLOCK BLKID = M202HI IN = (215A X 216 X) OUT = (217 X QM202HI X) \ \ BLOCK BLKID = T203 IN = (217 X) OUT = (218 X 220 X) \ \ BLOCK BLKID = S205SPT IN = (219 X) OUT = (252 X 253 X) \ \ BLOCK BLKID = S205A IN = (220 X) OUT = (221 X 225 X) \ \ BLOCK BLKID = S205MIX IN = (225 X 252 X) OUT = (254 X) \ \ BLOCK BLKID = S205B IN = (254 X) OUT = (255A X 256 X) \ \ BLOCK BLKID = M205 IN = (257 X) OUT = (258 X WM205 X) \ \ BLOCK BLKID = M205COOL IN = (258 X) OUT = (259 X QM205 X) \ \ BLOCK BLKID = S205FLSH IN = (255A X 259 X) OUT = (260 X 255 X) \ \ BLOCK BLKID = H205 IN = (260 X) OUT = (261 X 262 X QH205 X) \ \ BLOCK BLKID = H200MIX IN = (221 X 256 X) OUT = (223 X) \ \ BLOCK BLKID = H200 IN = (223 X) OUT = (240 X QH200 X) \ \ BLOCK BLKID = T209 IN = (227 X 240 X) OUT = (228 X) \ \ BLOCK BLKID = T224 IN = (233 X 228 X) OUT = (239 X) \ \ BLOCK BLKID = S222 IN = (239 X) OUT = (229 X 230 X) \ \ BLOCK BLKID = C202 IN = (255 X 230 X 253 X) OUT = (250 X) \ \ BLOCK BLKID = P224 IN = (250 X) OUT = (232 X) \ \ BLOCK BLKID = "H201+" IN = (218 X) OUT = (520A X QH201A X) \ \ BLOCK BLKID = QH201SPT IN = (QH201A X) OUT = (QH201 X QH201XTR X) \ \ BLOCK BLKID = H201- IN = (502 X QH201 X) OUT = (501 X) \ \ BLOCK BLKID = H244MIX IN = (QH201XTR X QH244A X) OUT = (QH244 X) \ \ BLOCK BLKID = H244 IN = (520A X) OUT = (520 X QH244A X) \ ? %M FLOWSHEET A300 ? ; SET1 ; \ COMMENTS COMMENTS = ( "; BLOCK MPOW2 IN=WM202 WC202 WC225 WC201 WS205 WS221 WS222 OUT=WMP2" ";" ";THIS FLOWSHEET MODELS THE SSCF PROCESS." ) \ \ BLOCK BLKID = H301- IN = (301 X) OUT = (301A X QH301 X) \ \ BLOCK BLKID = T310 IN = (301A X 312 X 422 X) OUT = (301B X QF300A X) \ \ BLOCK BLKID = H302 IN = (301B X) OUT = (301C X QH302 X) \ \ BLOCK BLKID = SACCHSPT IN = (301C X) OUT = (302 X 303 X) \ \ BLOCK BLKID = SEEDMIX IN = (303 X 310 X 310A X) OUT = (303A X) \ \ BLOCK BLKID = F301-6F IN = (303A X) OUT = (303B X QF301-6B X) \ \ BLOCK BLKID = F301-6FL IN = (303B X) OUT = (304C X 304 X) \ \ BLOCK BLKID = FERMMIX IN = (302 X 311 X 311A X 304 X) OUT = (304A X) \ \ BLOCK BLKID = CONTSPLT IN = (304A X) OUT = (304F X 304G X) \ \ BLOCK BLKID = F300CONT IN = (304G X) OUT = (304H X QF300CNT X) \ \ BLOCK BLKID = F300F IN = (304F X) OUT = (304E X QF300B X) \ \ BLOCK BLKID = T306 IN = (306 X 551 X) OUT = (502 X) \ \ BLOCK BLKID = F300FLSH IN = (304E X 304H X) OUT = (308 X 306 X) \ ? %M FLOWSHEET A400 ? ; SET1 ; \ 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" ) \ \ BLOCK BLKID = BTMSSPLT IN = (232 X) OUT = (401 X 301 X) \ \ BLOCK BLKID = CLFDSPLT IN = (401 X) OUT = (403 X 410 X) \ \ BLOCK BLKID = F401-4MX IN = (403 X 430 X) OUT = (431 X) \ \ BLOCK BLKID = F401-4 IN = (423 X 431 X 432 X 434 X) OUT = (432A X QF401-4 X) \ \ BLOCK BLKID = F401-4FL IN = (432A X) OUT = (435 X 433 X) \ \ BLOCK BLKID = H415 IN = (411 X) OUT = (412 X QH415 X) \ \ BLOCK BLKID = T415 IN = (412 X 410 X) OUT = (412A X) \ \ BLOCK BLKID = F400 IN = (412A X 433 X 413 X 436 X 416 X 417 X) OUT = (417A X QF400 X) \ \ BLOCK BLKID = F400FL IN = (417A X) OUT = (419 X 420 X) \ \ BLOCK BLKID = CLSSPLIT IN = (420 X) OUT = (421 X 422 X) \ \ BLOCK BLKID = T405 IN = (415 X 414 X) OUT = (416 X) \ ? %M FLOWSHEET A500 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";THIS FLOWSHEET MODELS THE DISTILLATION/DEHYDRATION AREA." "; ADDED SEPARATE MIXER AND SPLITTER SO WE CAN SEE TOTAL CONDENSATE" "; VENT SCRUBBER" "; PNEUMAPRESS UNIT" ) \ \ BLOCK BLKID = H512- IN = (501 X) OUT = (506 X QH512 X) \ \ BLOCK BLKID = "H512+" IN = (518 X QH512 X) OUT = (518A X) \ \ BLOCK BLKID = D501 IN = (506 X) OUT = (508 X 510 X 518 X QCD501 X QRD501 X) \ \ BLOCK BLKID = D502 IN = (510 X 521 X) OUT = (511 X 516 X) \ \ BLOCK BLKID = H506- IN = (511 X) OUT = (511C X QH506 X) \ \ BLOCK BLKID = T507-8 IN = (511C X) OUT = (515A X 514 X) \ \ BLOCK BLKID = H503 IN = (515A X) OUT = (517 X QH503 X) \ \ BLOCK BLKID = H507- IN = (517 X QH507 X) OUT = (521 X) \ \ BLOCK BLKID = "H507+" IN = (514 X) OUT = (519 X QH507 X) \ \ BLOCK BLKID = H509 IN = (519 X) OUT = (515 X QH509 X) \ \ BLOCK BLKID = RECTDUP IN = (QCD502 X) OUT = (QC502A X QC502B X) \ \ BLOCK BLKID = STMDUP IN = (QE501A X) OUT = (QE501A1 X QE501A2 X) \ \ BLOCK BLKID = E501L IN = (518A X QC502A X QE501A1 X) OUT = (526 X 525 X) \ \ BLOCK BLKID = E502V IN = (526 X) OUT = (527 X QE502A X) \ \ BLOCK BLKID = E502L IN = (580 X QE502A X) OUT = (529 X 528 X) \ \ BLOCK BLKID = E503V IN = (529 X) OUT = (530 X QE503A X) \ \ BLOCK BLKID = E503L IN = (528 X QE503A X) OUT = (532 X 531 X) \ \ BLOCK BLKID = E501MIX IN = (527 X 530 X 533 X) OUT = (534A X) \ \ BLOCK BLKID = E501WW IN = (534A X) OUT = (534B X 535 X) \ \ BLOCK BLKID = E501SPT IN = (534B X) OUT = (102 X 211 X 251 X) \ \ BLOCK BLKID = H517 IN = (532 X) OUT = (533 X QH517 X) \ \ BLOCK BLKID = VNTMIX IN = (508 X 304C X 308 X) OUT = (523 X) \ \ BLOCK BLKID = VNTSCRUB IN = (523 X 524 X) OUT = (550 X 551 X) \ \ BLOCK BLKID = DCOOL2 IN = (525 X) OUT = (570 X QDCOOL2 X) \ \ BLOCK BLKID = S505 IN = (570 X) OUT = (572 X 571B X) \ \ BLOCK BLKID = T530 IN = (572 X) OUT = (573 X 580 X) \ \ BLOCK BLKID = M505 IN = (557 X) OUT = (558 X WM505 X) \ \ BLOCK BLKID = M505COOL IN = (558 X) OUT = (559 X QM505 X) \ \ BLOCK BLKID = S505FLSH IN = (571B X 559 X) OUT = (560 X 571 X) \ \ BLOCK BLKID = FWMIX IN = (516 X 573 X 574 X) OUT = (576 X) \ \ BLOCK BLKID = RWSPLT IN = (576 X) OUT = (219 X 430 X 411 X) \ ? %M FLOWSHEET A600 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";THIS SECTION MODELS THE WASTEWATER TREATMENT AREA." ) \ \ BLOCK BLKID = S600 IN = (262 X 520 X 821 X 535 X 944 X) OUT = (612 X) \ \ BLOCK BLKID = NUTMIX IN = (631 X 630 X) OUT = (632 X) \ ? %M FLOWSHEET A700 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";THIS FLOWSHEET MODELS THE STORAGE AREA." ) \ \ BLOCK BLKID = DCOOLE IN = (515 X) OUT = (515E X) \ \ BLOCK BLKID = PRODMIX IN = (515E X 701 X) OUT = (703 X) \ \ BLOCK BLKID = TSTORE IN = (710 X 713 X 717 X 723 X 735 X 745 X 750 X 755 X) OUT = (702 X) \ ? %M FLOWSHEET A800 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";THIS FLOWSHEET MODELS THE FUEL AND GAS SIDE OF THE BOILER." ) \ \ BLOCK BLKID = BTUTOT IN = (571 X 531 X 615 X) OUT = (803 X) \ \ BLOCK BLKID = BLRWTR IN = (811 X 921 X) OUT = (811A X) \ \ BLOCK BLKID = BURNER IN = (804A X 803 X) OUT = (804C X QM803 X) \ \ BLOCK BLKID = M802 IN = (804E X) OUT = (804A X WCOMBFAN X) \ \ BLOCK BLKID = M802MIX IN = (804 X 261 X 560 X) OUT = (804E X) \ ? %M FLOWSHEET A900 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";THIS FLOWSHEET MODELS THE MISCELLANEOUS UTILITIES" "; Heatcw-s Cooling Water Heat Load accumulator" "; HeatCHW- Chilled Water Heat Load accumulator" ";" ) \ \ BLOCK BLKID = SSCFCW IN = (QF300B X QF300CNT X) OUT = (QF300 X) \ \ BLOCK BLKID = SSCFSDCW IN = (QF301-6B X) OUT = (QF301 X) \ \ BLOCK BLKID = CHCWDUP IN = (QH914 X) OUT = (QH914A X QH914B X QH914C X) \ \ BLOCK BLKID = QH14BSP IN = (QH914B X) OUT = (QH14BCW X QH14BCHW X) \ \ BLOCK BLKID = HEATCW-S IN = (QH602 X QM811 X QM205 X QM401 X QM505 X QH503 X QH509 X QH517 X QH200 X QCD501 X QH415 X QH205 X QH244 X QF300A X QH302 X) OUT = (QCW X) \ \ BLOCK BLKID = QCWMIX IN = (QH914A X QCW X QC502B X) OUT = (QCWTOT X) \ \ BLOCK BLKID = CWMAKUP IN = (941A X 922 X) OUT = (941 X) \ \ BLOCK BLKID = HEATCHW- IN = (QF401-4 X QF400 X) OUT = (QCHW X) \ \ BLOCK BLKID = QCHWMIX IN = (QCHW X QH914C X) OUT = (QCHWTOT X) \ \ BLOCK BLKID = ACOMP IN = (440 X) OUT = (441 X WM401 X) \ \ BLOCK BLKID = AFLSH IN = (441 X) OUT = (443 X QM401 X) \ \ BLOCK BLKID = ASPLT IN = (443 X) OUT = (432 X 413 X) \ \ BLOCK BLKID = CHCWMIX IN = (QF300 X QF301 X) OUT = (QWELL X) \ \ BLOCK BLKID = H914 IN = (903 X QWELL X) OUT = (904 X QH914 X) \ \ BLOCK BLKID = T914 IN = (624 X 943 X 251 X) OUT = (905 X) \ \ BLOCK BLKID = H910 IN = (906 X) OUT = (909 X QH910 X) \ \ BLOCK BLKID = CIPCS IN = (914 X) OUT = (916 X) \ \ BLOCK BLKID = QHXMED IN = (QRD502I X) OUT = (QRD502 X) \ \ BLOCK BLKID = QSTMVLO IN = (QE501A2 X) OUT = (QVLOW X) \ \ BLOCK BLKID = QHXLOW IN = (QH301 X QRD501 X QH506 X) OUT = (QHXLOW X) \ ? COMPONENTS MAIN ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";===========================================================================" "; Components" ";===========================================================================" ";" "; Biomass components" "; Aliases components" "; Solids Database" "; Purecomps Database" ) \ \ COMPONENTS CID = GLUCOSE / CID = CELLULOS / CID = XYLOSE / CID = XYLAN / CID = LIGNIN / CID = ACETATE / CID = ORGANISM / CID = SOLSLDS / CID = GYPSUM / CID = LGNSOL / CID = HMF / CID = C5SUGAR / CID = C6SUGAR / CID = C5SOLID / CID = C6SOLID / CID = CAH2O2 ANAME = "CA(OH)2" OUTNAME = CAH2O2 / CID = ASH ANAME = "CAO" OUTNAME = ASH / CID = ETHANOL ANAME = "C2H6O-2" OUTNAME = ETHANOL / CID = H2O ANAME = "H2O" OUTNAME = H2O / CID = FURFURAL ANAME = "C5H4O2" OUTNAME = FURFURAL / CID = H2SO4 ANAME = "H2SO4" OUTNAME = H2SO4 / CID = N2 ANAME = "N2" OUTNAME = N2 / CID = CO2 ANAME = "CO2" OUTNAME = CO2 / CID = O2 ANAME = "O2" OUTNAME = O2 / CID = NH3 ANAME = "H3N" OUTNAME = NH3 / CID = LACID ANAME = "C3H6O3-D1" OUTNAME = LACID / CID = AACID ANAME = "C2H4O2-1" OUTNAME = AACID / CID = NH4SO4 ANAME = "(NH4)2SO4" OUTNAME = NH4SO4 / CID = NH4ACET ANAME = "(NH4)2SO4" OUTNAME = NH4ACET / CID = CH4 ANAME = "CH4" OUTNAME = CH4 / CID = NO2 ANAME = "NO2" OUTNAME = NO2 / CID = SO2 ANAME = "O2S" OUTNAME = SO2 / CID = DAP ANAME = "(NH4)2HPO4" OUTNAME = DAP \ ? COMPONENTS HENRY-COMPS HC ? \ HENRY-COMPS CID = (O2 N2 CO2 CH4) \ \ COMMENTS COMMENTS = ( ";" ) \ ? %M PROPERTIES OPTION-SETS NRTL ? \ PARAM BASE = NRTL \ \ MPROP MPROP-NAME = VLMX MROUTEID = VLMX49 \ \ SPROP SPROP-NAME = DHL SROUTEID = DHL09 \ \ COMMENTS COMMENTS = ( ";" "; Uses the Modified Rackett for Density" "; Uses Liguid heat capacity equation of DIPPR" ) \ ? %M PROPERTIES MAIN ? \ GPROPERTIES GOPSETNAME = NRTL GHEN = HC \ \ X-PROPS BOPSETNAME = NRTL-HOC \ \ COMMENTS COMMENTS = ( ";" "; End of HMF Data" ";======================================================================" ) \ ? %M DATABANKS ? \ DATABANKS FILE-SYM-NAM = ( PURE93 SOLIDS ASPENPCD BINARY ) \ \ COMMENTS COMMENTS = ( ";PROP-SOURCES INHSPCD / PURE93 / SOLIDS" ) \ ? PROPERTIES PROP-DATA PARAMS DATA1 ? ; SI ; \ PROP-LIST PARAMNAME = TC \ \ PVAL PARAMNAME2 = TC CID = GLUCOSE VALUE = 1011.10 <0> <0> \ \ PROP-LIST PARAMNAME = PC \ \ PVAL PARAMNAME2 = PC CID = GLUCOSE VALUE = 6200000.0 <0> <0> \ \ PROP-LIST PARAMNAME = VC \ \ PVAL PARAMNAME2 = VC CID = GLUCOSE VALUE = .41650 <0> <0> \ \ PROP-LIST PARAMNAME = TB \ \ PVAL PARAMNAME2 = TB CID = GLUCOSE VALUE = 825.40 <0> <0> \ \ PROP-LIST PARAMNAME = OMEGA \ \ PVAL PARAMNAME2 = OMEGA CID = GLUCOSE VALUE = 2.56740 <0> <0> \ \ PROP-LIST PARAMNAME = DHFORM \ \ PVAL PARAMNAME2 = DHFORM CID = GLUCOSE VALUE = -1.2569030E+09 <0> <0> \ \ PROP-LIST PARAMNAME = DGFORM \ \ PVAL PARAMNAME2 = DGFORM CID = GLUCOSE VALUE = -9.09330E+08 <0> <0> \ \ PROP-LIST PARAMNAME = RKTZRA \ \ PVAL PARAMNAME2 = RKTZRA CID = GLUCOSE VALUE = .358520 <0> <0> \ \ PROP-LIST PARAMNAME = COMPHL \ \ PVAL PARAMNAME2 = COMPHL CID = GLUCOSE VALUE = 1.0 <0> <0> \ \ PROP-LIST PARAMNAME = TC \ \ PVAL PARAMNAME2 = TC CID = XYLOSE VALUE = 890.420 <0> <0> \ \ PROP-LIST PARAMNAME = PC \ \ PVAL PARAMNAME2 = PC CID = XYLOSE VALUE = 6577700.0 <0> <0> \ \ PROP-LIST PARAMNAME = VC \ \ PVAL PARAMNAME2 = VC CID = XYLOSE VALUE = .34250 <0> <0> \ \ PROP-LIST PARAMNAME = TB \ \ PVAL PARAMNAME2 = TB CID = XYLOSE VALUE = 715.010 <0> <0> \ \ PROP-LIST PARAMNAME = OMEGA \ \ PVAL PARAMNAME2 = OMEGA CID = XYLOSE VALUE = 2.30420 <0> <0> \ \ PROP-LIST PARAMNAME = DHFORM \ \ PVAL PARAMNAME2 = DHFORM CID = XYLOSE VALUE = -1.0400020E+09 <0> <0> \ \ PROP-LIST PARAMNAME = RKTZRA \ \ PVAL PARAMNAME2 = RKTZRA CID = XYLOSE VALUE = .299360 <0> <0> \ \ PROP-LIST PARAMNAME = COMPHL \ \ PVAL PARAMNAME2 = COMPHL CID = XYLOSE VALUE = 1.0 <0> <0> \ \ PROP-LIST PARAMNAME = DHSFRM \ \ PVAL PARAMNAME2 = DHSFRM CID = CELLULOS VALUE = -9.763620E+08 <0> <0> \ \ PROP-LIST PARAMNAME = DHSFRM \ \ PVAL PARAMNAME2 = DHSFRM CID = XYLAN VALUE = -7.624160E+08 <0> <0> \ \ PROP-LIST PARAMNAME = DHSFRM \ \ PVAL PARAMNAME2 = DHSFRM CID = LIGNIN VALUE = -1.964050E+09 <0> <0> \ \ PROP-LIST PARAMNAME = DHSFRM \ \ PVAL PARAMNAME2 = DHSFRM CID = ACETATE VALUE = -4.563280E+08 <0> <0> \ \ PROP-LIST PARAMNAME = DHSFRM \ \ PVAL PARAMNAME2 = DHSFRM CID = ORGANISM VALUE = -1.3050E+08 <0> <0> \ \ PROP-LIST PARAMNAME = TC \ \ PVAL PARAMNAME2 = TC CID = SOLSLDS VALUE = 1011.10 <0> <0> \ \ PROP-LIST PARAMNAME = PC \ \ PVAL PARAMNAME2 = PC CID = SOLSLDS VALUE = 6200000.0 <0> <0> \ \ PROP-LIST PARAMNAME = VC \ \ PVAL PARAMNAME2 = VC CID = SOLSLDS VALUE = .41650 <0> <0> \ \ PROP-LIST PARAMNAME = TB \ \ PVAL PARAMNAME2 = TB CID = SOLSLDS VALUE = 825.40 <0> <0> \ \ PROP-LIST PARAMNAME = OMEGA \ \ PVAL PARAMNAME2 = OMEGA CID = SOLSLDS VALUE = 2.56740 <0> <0> \ \ PROP-LIST PARAMNAME = DHFORM \ \ PVAL PARAMNAME2 = DHFORM CID = SOLSLDS VALUE = 1.0896690E+09 <0> <0> \ \ PROP-LIST PARAMNAME = RKTZRA \ \ PVAL PARAMNAME2 = RKTZRA CID = SOLSLDS VALUE = .099080 <0> <0> \ \ PROP-LIST PARAMNAME = COMPHL \ \ PVAL PARAMNAME2 = COMPHL CID = SOLSLDS VALUE = 1.0 <0> <0> \ \ PROP-LIST PARAMNAME = DHSFRM \ \ PVAL PARAMNAME2 = DHSFRM CID = GYPSUM VALUE = -2.0226280E+09 <0> <0> \ \ PROP-LIST PARAMNAME = DGSFRM \ \ PVAL PARAMNAME2 = DGSFRM CID = GYPSUM VALUE = -1.7971970E+09 <0> <0> \ \ PROP-LIST PARAMNAME = TC \ \ PVAL PARAMNAME2 = TC CID = LGNSOL VALUE = 1011.10 <0> <0> \ \ PROP-LIST PARAMNAME = PC \ \ PVAL PARAMNAME2 = PC CID = LGNSOL VALUE = 6200000.0 <0> <0> \ \ PROP-LIST PARAMNAME = VC \ \ PVAL PARAMNAME2 = VC CID = LGNSOL VALUE = .41650 <0> <0> \ \ PROP-LIST PARAMNAME = TB \ \ PVAL PARAMNAME2 = TB CID = LGNSOL VALUE = 825.40 <0> <0> \ \ PROP-LIST PARAMNAME = OMEGA \ \ PVAL PARAMNAME2 = OMEGA CID = LGNSOL VALUE = 2.56740 <0> <0> \ \ PROP-LIST PARAMNAME = DHFORM \ \ PVAL PARAMNAME2 = DHFORM CID = LGNSOL VALUE = -1.964050E+09 <0> <0> \ \ PROP-LIST PARAMNAME = RKTZRA \ \ PVAL PARAMNAME2 = RKTZRA CID = LGNSOL VALUE = .358520 <0> <0> \ \ PROP-LIST PARAMNAME = COMPHL \ \ PVAL PARAMNAME2 = COMPHL CID = LGNSOL VALUE = 1.0 <0> <0> \ \ PROP-LIST PARAMNAME = TC \ \ PVAL PARAMNAME2 = TC CID = C6SUGAR VALUE = 1011.10 <0> <0> \ \ PROP-LIST PARAMNAME = PC \ \ PVAL PARAMNAME2 = PC CID = C6SUGAR VALUE = 6200000.0 <0> <0> \ \ PROP-LIST PARAMNAME = VC \ \ PVAL PARAMNAME2 = VC CID = C6SUGAR VALUE = .41650 <0> <0> \ \ PROP-LIST PARAMNAME = TB \ \ PVAL PARAMNAME2 = TB CID = C6SUGAR VALUE = 825.40 <0> <0> \ \ PROP-LIST PARAMNAME = OMEGA \ \ PVAL PARAMNAME2 = OMEGA CID = C6SUGAR VALUE = 2.56740 <0> <0> \ \ PROP-LIST PARAMNAME = DHFORM \ \ PVAL PARAMNAME2 = DHFORM CID = C6SUGAR VALUE = -1.2569030E+09 <0> <0> \ \ PROP-LIST PARAMNAME = DGFORM \ \ PVAL PARAMNAME2 = DGFORM CID = C6SUGAR VALUE = -9.09330E+08 <0> <0> \ \ PROP-LIST PARAMNAME = RKTZRA \ \ PVAL PARAMNAME2 = RKTZRA CID = C6SUGAR VALUE = .358520 <0> <0> \ \ PROP-LIST PARAMNAME = COMPHL \ \ PVAL PARAMNAME2 = COMPHL CID = C6SUGAR VALUE = 1.0 <0> <0> \ \ PROP-LIST PARAMNAME = TC \ \ PVAL PARAMNAME2 = TC CID = C5SUGAR VALUE = 890.420 <0> <0> \ \ PROP-LIST PARAMNAME = PC \ \ PVAL PARAMNAME2 = PC CID = C5SUGAR VALUE = 6577700.0 <0> <0> \ \ PROP-LIST PARAMNAME = VC \ \ PVAL PARAMNAME2 = VC CID = C5SUGAR VALUE = .34250 <0> <0> \ \ PROP-LIST PARAMNAME = TB \ \ PVAL PARAMNAME2 = TB CID = C5SUGAR VALUE = 715.010 <0> <0> \ \ PROP-LIST PARAMNAME = OMEGA \ \ PVAL PARAMNAME2 = OMEGA CID = C5SUGAR VALUE = 2.30420 <0> <0> \ \ PROP-LIST PARAMNAME = DHFORM \ \ PVAL PARAMNAME2 = DHFORM CID = C5SUGAR VALUE = -1.0400020E+09 <0> <0> \ \ PROP-LIST PARAMNAME = RKTZRA \ \ PVAL PARAMNAME2 = RKTZRA CID = C5SUGAR VALUE = .299360 <0> <0> \ \ PROP-LIST PARAMNAME = COMPHL \ \ PVAL PARAMNAME2 = COMPHL CID = C5SUGAR VALUE = 1.0 <0> <0> \ \ PROP-LIST PARAMNAME = DHSFRM \ \ PVAL PARAMNAME2 = DHSFRM CID = C6SOLID VALUE = -9.763620E+08 <0> <0> \ \ PROP-LIST PARAMNAME = DHSFRM \ \ PVAL PARAMNAME2 = DHSFRM CID = C5SOLID VALUE = -7.624160E+08 <0> <0> \ \ PROP-LIST PARAMNAME = RKTZRA \ \ PVAL PARAMNAME2 = RKTZRA CID = ETHANOL VALUE = .2485070 <0> <0> \ \ PROP-LIST PARAMNAME = TB \ \ PVAL PARAMNAME2 = TB CID = HMF VALUE = 532.70 <0> <0> \ \ PROP-LIST PARAMNAME = TC \ \ PVAL PARAMNAME2 = TC CID = HMF VALUE = 731.0120 <0> <0> \ \ PROP-LIST PARAMNAME = PC \ \ PVAL PARAMNAME2 = PC CID = HMF VALUE = 5235810.0 <0> <0> \ \ PROP-LIST PARAMNAME = VC \ \ PVAL PARAMNAME2 = VC CID = HMF VALUE = .34250 <0> <0> \ \ PROP-LIST PARAMNAME = DHFORM \ \ PVAL PARAMNAME2 = DHFORM CID = HMF VALUE = -3.238090E+08 <0> <0> \ \ PROP-LIST PARAMNAME = DGFORM \ \ PVAL PARAMNAME2 = DGFORM CID = HMF VALUE = -2.3790E+08 <0> <0> \ \ PROP-LIST PARAMNAME = OMEGA \ \ PVAL PARAMNAME2 = OMEGA CID = HMF VALUE = .993646710 <0> <0> \ \ PROP-LIST PARAMNAME = RKTZRA \ \ PVAL PARAMNAME2 = RKTZRA CID = HMF VALUE = .1981779740 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA2 ? ; SI ; \ PROP-LIST PARAMNAME = CPIG \ \ PVAL PARAMNAME2 = CPIG CID = GLUCOSE VAL1 = 207000.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 250.0 <0> <0> VAL8 = 1000.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> VAL11 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA3 ? ; SI ; \ PROP-LIST PARAMNAME = PLXANT \ \ PVAL PARAMNAME2 = PLXANT CID = GLUCOSE VAL1 = 1182.20 <0> <0> VAL2 = -84682.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = .15640 <0> <0> VAL5 = -175.850 <0> <0> VAL6 = -.0000237770 <0> <0> VAL7 = 2.0 <0> <0> VAL8 = 573.150 <0> <0> VAL9 = 993.150 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA4 ? ; SI ; \ PROP-LIST PARAMNAME = DHVLWT \ \ PVAL PARAMNAME2 = DHVLWT CID = GLUCOSE VAL1 = 502000.0 <0> <0> VAL2 = 298.0 <0> <0> VAL3 = .380 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 200.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA5 ? ; SI ; \ PROP-LIST PARAMNAME = CPLDIP \ \ PVAL PARAMNAME2 = CPLDIP CID = GLUCOSE VAL1 = 207431.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 250.0 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA6 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = GLUCOSE VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA7 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = GLUCOSE VAL1 = 6.0 <0> <0> VAL2 = 12.0 <0> <0> VAL3 = 6.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA8 ? ; SI ; \ PROP-LIST PARAMNAME = THRSWT \ \ PVAL PARAMNAME2 = THRSWT CID = GLUCOSE VAL1 = 0.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 100.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA9 ? ; SI ; \ PROP-LIST PARAMNAME = PLXANT \ \ PVAL PARAMNAME2 = PLXANT CID = XYLOSE VAL1 = 481.330 <0> <0> VAL2 = -46623.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = .0210070 <0> <0> VAL5 = -64.3310 <0> <0> VAL6 = .00000622430 <0> <0> VAL7 = 2.0 <0> <0> VAL8 = 573.150 <0> <0> VAL9 = 873.150 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA10 ? ; SI ; \ PROP-LIST PARAMNAME = DHVLWT \ \ PVAL PARAMNAME2 = DHVLWT CID = XYLOSE VAL1 = 4186800.0 <0> <0> VAL2 = 298.0 <0> <0> VAL3 = .380 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 200.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA11 ? ; SI ; \ PROP-LIST PARAMNAME = CPIG \ \ PVAL PARAMNAME2 = CPIG CID = XYLOSE VAL1 = 170000.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 250.0 <0> <0> VAL8 = 1000.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> VAL11 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA12 ? ; SI ; \ PROP-LIST PARAMNAME = CPLDIP \ \ PVAL PARAMNAME2 = CPLDIP CID = XYLOSE VAL1 = 172857.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 250.0 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA13 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = XYLOSE VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA14 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = XYLOSE VAL1 = 5.0 <0> <0> VAL2 = 10.0 <0> <0> VAL3 = 5.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA15 ? ; SI ; \ PROP-LIST PARAMNAME = THRSWT \ \ PVAL PARAMNAME2 = THRSWT CID = XYLOSE VAL1 = 0.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 100.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA16 ? ; SI ; \ PROP-LIST PARAMNAME = CPSPO1 \ \ PVAL PARAMNAME2 = CPSPO1 CID = CELLULOS VAL1 = -11704.0 <0> <0> VAL2 = 672.070 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 298.150 <0> <0> VAL8 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA17 ? ; SI ; \ PROP-LIST PARAMNAME = VSPOLY \ \ PVAL PARAMNAME2 = VSPOLY CID = CELLULOS VAL1 = .1060 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 298.150 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA18 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = CELLULOS VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA19 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = CELLULOS VAL1 = 6.0 <0> <0> VAL2 = 10.0 <0> <0> VAL3 = 5.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA20 ? ; SI ; \ PROP-LIST PARAMNAME = CPSPO1 \ \ PVAL PARAMNAME2 = CPSPO1 CID = XYLAN VAL1 = -9536.30 <0> <0> VAL2 = 547.620 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 298.150 <0> <0> VAL8 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA21 ? ; SI ; \ PROP-LIST PARAMNAME = VSPOLY \ \ PVAL PARAMNAME2 = VSPOLY CID = XYLAN VAL1 = .08640 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 298.150 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA22 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = XYLAN VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA23 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = XYLAN VAL1 = 5.0 <0> <0> VAL2 = 8.0 <0> <0> VAL3 = 4.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA24 ? ; SI ; \ PROP-LIST PARAMNAME = THRSWT \ \ PVAL PARAMNAME2 = THRSWT CID = XYLAN VAL1 = 0.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA25 ? ; SI ; \ PROP-LIST PARAMNAME = CPSPO1 \ \ PVAL PARAMNAME2 = CPSPO1 CID = LIGNIN VAL1 = 39752.80 <0> <0> VAL2 = 498.8470 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 298.150 <0> <0> VAL8 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA26 ? ; SI ; \ PROP-LIST PARAMNAME = VSPOLY \ \ PVAL PARAMNAME2 = VSPOLY CID = LIGNIN VAL1 = .10330 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 298.150 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA27 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = LIGNIN VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA28 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = LIGNIN VAL1 = 10.0 <0> <0> VAL2 = 13.90 <0> <0> VAL3 = 1.30 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA29 ? ; SI ; \ PROP-LIST PARAMNAME = CPSPO1 \ \ PVAL PARAMNAME2 = CPSPO1 CID = ACETATE VAL1 = -4335.0 <0> <0> VAL2 = 248.90 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 298.150 <0> <0> VAL8 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA30 ? ; SI ; \ PROP-LIST PARAMNAME = VSPOLY \ \ PVAL PARAMNAME2 = VSPOLY CID = ACETATE VAL1 = .039250 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 298.150 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA31 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = ACETATE VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA32 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = ACETATE VAL1 = 2.0 <0> <0> VAL2 = 4.0 <0> <0> VAL3 = 2.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA33 ? ; SI ; \ PROP-LIST PARAMNAME = CPSPO1 \ \ PVAL PARAMNAME2 = CPSPO1 CID = ORGANISM VAL1 = 38409.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 298.150 <0> <0> VAL8 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA34 ? ; SI ; \ PROP-LIST PARAMNAME = VSPOLY \ \ PVAL PARAMNAME2 = VSPOLY CID = ORGANISM VAL1 = .01640 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 298.150 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA35 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = ORGANISM VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 7.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA36 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = ORGANISM VAL1 = 1.0 <0> <0> VAL2 = 1.80 <0> <0> VAL3 = .50 <0> <0> VAL4 = .20 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA37 ? ; SI ; \ PROP-LIST PARAMNAME = CPIG \ \ PVAL PARAMNAME2 = CPIG CID = SOLSLDS VAL1 = 16900.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 250.0 <0> <0> VAL8 = 1000.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> VAL11 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA38 ? ; SI ; \ PROP-LIST PARAMNAME = PLXANT \ \ PVAL PARAMNAME2 = PLXANT CID = SOLSLDS VAL1 = 1182.20 <0> <0> VAL2 = -84682.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = .15640 <0> <0> VAL5 = -175.850 <0> <0> VAL6 = -.0000237770 <0> <0> VAL7 = 2.0 <0> <0> VAL8 = 573.150 <0> <0> VAL9 = 993.150 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA39 ? ; SI ; \ PROP-LIST PARAMNAME = DHVLWT \ \ PVAL PARAMNAME2 = DHVLWT CID = SOLSLDS VAL1 = 4186800.0 <0> <0> VAL2 = 298.0 <0> <0> VAL3 = .380 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 200.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA40 ? ; SI ; \ PROP-LIST PARAMNAME = CPLDIP \ \ PVAL PARAMNAME2 = CPLDIP CID = SOLSLDS VAL1 = 19094.80 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 250.0 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA41 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = SOLSLDS VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 7.0 <0> <0> VAL5 = 16.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA42 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = SOLSLDS VAL1 = 1.0 <0> <0> VAL2 = .10970 <0> <0> VAL3 = 5.05940 <0> <0> VAL4 = .36620 <0> <0> VAL5 = .002780 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA43 ? ; SI ; \ PROP-LIST PARAMNAME = THRSWT \ \ PVAL PARAMNAME2 = THRSWT CID = SOLSLDS VAL1 = 0.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 100.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA44 ? ; SI ; \ PROP-LIST PARAMNAME = CPSPO1 \ \ PVAL PARAMNAME2 = CPSPO1 CID = GYPSUM VAL1 = 72182.0 <0> <0> VAL2 = 97.3430 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = -1.37330E+08 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 298.0 <0> <0> VAL8 = 1400.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA45 ? ; SI ; \ PROP-LIST PARAMNAME = VSPOLY \ \ PVAL PARAMNAME2 = VSPOLY CID = GYPSUM VAL1 = .074690 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 298.150 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA46 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = GYPSUM VAL1 = 20.0 <0> <0> VAL2 = 16.0 <0> <0> VAL3 = 1.0 <0> <0> VAL4 = 8.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA47 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = GYPSUM VAL1 = 1.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 4.0 <0> <0> VAL4 = 6.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA48 ? ; SI ; \ PROP-LIST PARAMNAME = CPIG \ \ PVAL PARAMNAME2 = CPIG CID = LGNSOL VAL1 = 207000.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 250.0 <0> <0> VAL8 = 1000.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> VAL11 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA49 ? ; SI ; \ PROP-LIST PARAMNAME = PLXANT \ \ PVAL PARAMNAME2 = PLXANT CID = LGNSOL VAL1 = 1182.20 <0> <0> VAL2 = -84682.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = .15640 <0> <0> VAL5 = -175.850 <0> <0> VAL6 = -.0000237770 <0> <0> VAL7 = 2.0 <0> <0> VAL8 = 573.150 <0> <0> VAL9 = 993.150 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA50 ? ; SI ; \ PROP-LIST PARAMNAME = DHVLWT \ \ PVAL PARAMNAME2 = DHVLWT CID = LGNSOL VAL1 = 4186800.0 <0> <0> VAL2 = 298.0 <0> <0> VAL3 = .380 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 200.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA51 ? ; SI ; \ PROP-LIST PARAMNAME = CPLDIP \ \ PVAL PARAMNAME2 = CPLDIP CID = LGNSOL VAL1 = 207431.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 250.0 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA52 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = LGNSOL VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA53 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = LGNSOL VAL1 = 10.0 <0> <0> VAL2 = 13.90 <0> <0> VAL3 = 1.30 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA54 ? ; SI ; \ PROP-LIST PARAMNAME = THRSWT \ \ PVAL PARAMNAME2 = THRSWT CID = LGNSOL VAL1 = 0.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 100.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA55 ? ; SI ; \ PROP-LIST PARAMNAME = CPIG \ \ PVAL PARAMNAME2 = CPIG CID = C6SUGAR VAL1 = 207000.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 250.0 <0> <0> VAL8 = 1000.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> VAL11 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA56 ? ; SI ; \ PROP-LIST PARAMNAME = PLXANT \ \ PVAL PARAMNAME2 = PLXANT CID = C6SUGAR VAL1 = 1182.20 <0> <0> VAL2 = -84682.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = .15640 <0> <0> VAL5 = -175.850 <0> <0> VAL6 = -.0000237770 <0> <0> VAL7 = 2.0 <0> <0> VAL8 = 573.150 <0> <0> VAL9 = 993.150 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA57 ? ; SI ; \ PROP-LIST PARAMNAME = DHVLWT \ \ PVAL PARAMNAME2 = DHVLWT CID = C6SUGAR VAL1 = 502000.0 <0> <0> VAL2 = 298.0 <0> <0> VAL3 = .380 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 200.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA58 ? ; SI ; \ PROP-LIST PARAMNAME = CPLDIP \ \ PVAL PARAMNAME2 = CPLDIP CID = C6SUGAR VAL1 = 207431.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 250.0 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA59 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = C6SUGAR VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA60 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = C6SUGAR VAL1 = 6.0 <0> <0> VAL2 = 12.0 <0> <0> VAL3 = 6.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA61 ? ; SI ; \ PROP-LIST PARAMNAME = THRSWT \ \ PVAL PARAMNAME2 = THRSWT CID = C6SUGAR VAL1 = 0.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 100.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA62 ? ; SI ; \ PROP-LIST PARAMNAME = PLXANT \ \ PVAL PARAMNAME2 = PLXANT CID = C5SUGAR VAL1 = 481.330 <0> <0> VAL2 = -46623.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = .0210070 <0> <0> VAL5 = -64.3310 <0> <0> VAL6 = .00000622430 <0> <0> VAL7 = 2.0 <0> <0> VAL8 = 573.150 <0> <0> VAL9 = 873.150 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA63 ? ; SI ; \ PROP-LIST PARAMNAME = DHVLWT \ \ PVAL PARAMNAME2 = DHVLWT CID = C5SUGAR VAL1 = 4186800.0 <0> <0> VAL2 = 298.0 <0> <0> VAL3 = .380 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 200.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA64 ? ; SI ; \ PROP-LIST PARAMNAME = CPIG \ \ PVAL PARAMNAME2 = CPIG CID = C5SUGAR VAL1 = 170000.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 250.0 <0> <0> VAL8 = 1000.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> VAL11 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA65 ? ; SI ; \ PROP-LIST PARAMNAME = CPLDIP \ \ PVAL PARAMNAME2 = CPLDIP CID = C5SUGAR VAL1 = 172857.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 250.0 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA66 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = C5SUGAR VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA67 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = C5SUGAR VAL1 = 5.0 <0> <0> VAL2 = 10.0 <0> <0> VAL3 = 5.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA68 ? ; SI ; \ PROP-LIST PARAMNAME = THRSWT \ \ PVAL PARAMNAME2 = THRSWT CID = C5SUGAR VAL1 = 0.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 100.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA69 ? ; SI ; \ PROP-LIST PARAMNAME = CPSPO1 \ \ PVAL PARAMNAME2 = CPSPO1 CID = C6SOLID VAL1 = -11704.0 <0> <0> VAL2 = 672.070 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 298.150 <0> <0> VAL8 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA70 ? ; SI ; \ PROP-LIST PARAMNAME = VSPOLY \ \ PVAL PARAMNAME2 = VSPOLY CID = C6SOLID VAL1 = .1060 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 298.150 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA71 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = C6SOLID VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA72 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = C6SOLID VAL1 = 6.0 <0> <0> VAL2 = 10.0 <0> <0> VAL3 = 5.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA73 ? ; SI ; \ PROP-LIST PARAMNAME = CPSPO1 \ \ PVAL PARAMNAME2 = CPSPO1 CID = C5SOLID VAL1 = -9536.30 <0> <0> VAL2 = 547.620 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 298.150 <0> <0> VAL8 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA74 ? ; SI ; \ PROP-LIST PARAMNAME = VSPOLY \ \ PVAL PARAMNAME2 = VSPOLY CID = C5SOLID VAL1 = .08640 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 298.150 <0> <0> VAL7 = 1000.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA75 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = C5SOLID VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA76 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = C5SOLID VAL1 = 5.0 <0> <0> VAL2 = 8.0 <0> <0> VAL3 = 4.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA77 ? ; SI ; \ PROP-LIST PARAMNAME = THRSWT \ \ PVAL PARAMNAME2 = THRSWT CID = C5SOLID VAL1 = 0.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA78 ? ; SI ; \ PROP-LIST PARAMNAME = MRKZRA \ \ PVAL PARAMNAME2 = MRKZRA CID = ETHANOL VAL1 = .2572820 <0> <0> VAL2 = -.000009299520 <0> <0> VAL3 = -5.828140E-08 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA79 ? ; SI ; \ PROP-LIST PARAMNAME = THRSWT \ \ PVAL PARAMNAME2 = THRSWT CID = ETHANOL VAL1 = 100.0 <0> <0> VAL2 = 0.0 <0> <0> VAL3 = 101.0 <0> <0> VAL4 = 106.0 <0> <0> VAL5 = 100.0 <0> <0> VAL6 = 100.0 <0> <0> VAL7 = 107.0 <0> <0> VAL8 = 104.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA80 ? ; SI ; \ PROP-LIST PARAMNAME = ATOMNO \ \ PVAL PARAMNAME2 = ATOMNO CID = HMF VAL1 = 6.0 <0> <0> VAL2 = 1.0 <0> <0> VAL3 = 8.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA81 ? ; SI ; \ PROP-LIST PARAMNAME = NOATOM \ \ PVAL PARAMNAME2 = NOATOM CID = HMF VAL1 = 6.0 <0> <0> VAL2 = 6.0 <0> <0> VAL3 = 3.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 0.0 <0> <0> VAL8 = 0.0 <0> <0> VAL9 = 0.0 <0> <0> VAL10 = 0.0 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA82 ? ; SI ; \ PROP-LIST PARAMNAME = CPIG \ \ PVAL PARAMNAME2 = CPIG CID = HMF VAL1 = -23327.10 <0> <0> VAL2 = 706.4310 <0> <0> VAL3 = -.6115380 <0> <0> VAL4 = .0002043910 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 0.0 <0> <0> VAL7 = 280.0 <0> <0> VAL8 = 1100.0 <0> <0> VAL9 = 36029.20 <0> <0> VAL10 = 20.27330 <0> <0> VAL11 = 1.50 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA83 ? ; SI ; \ PROP-LIST PARAMNAME = DHVLWT \ \ PVAL PARAMNAME2 = DHVLWT CID = HMF VAL1 = 83770000.0 <0> <0> VAL2 = 383.150 <0> <0> VAL3 = .380 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 273.150 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA84 ? ; SI ; \ PROP-LIST PARAMNAME = PLXANT \ \ PVAL PARAMNAME2 = PLXANT CID = HMF VAL1 = 126.396590 <0> <0> VAL2 = -15309.6390 <0> <0> VAL3 = 0.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = -13.7334440 <0> <0> VAL6 = 3.81230E-18 <0> <0> VAL7 = 6.0 <0> <0> VAL8 = 373.150 <0> <0> VAL9 = 731.0117970 <0> <0> \ ? PROPERTIES PROP-DATA CORRS DATA85 ? ; SI ; \ PROP-LIST PARAMNAME = MULAND \ \ PVAL PARAMNAME2 = MULAND CID = HMF VAL1 = 208.780 <0> <0> VAL2 = -14965.80 <0> <0> VAL3 = -30.02090 <0> <0> VAL4 = 532.70 <0> <0> VAL5 = 723.7020 <0> <0> \ \ COMMENTS COMMENTS = ( ";IN-HOUSE-DATA PCD=YES" ";" ";======================================================================" "; ADDED PROP-DATA FROM IN-HOUSE DATABASE (PROPDATA-3.INP)" ";" ";" ";" ";" ";" ";" ";" "; COMPHL required to envoke CPLDIP" ";" ";" ";" ";" "; End of Glucose Data" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/" "; Xylose" ";" ";" ";" ";" ";" ";" ";" "; COMPHL required to envoke CPLDIP" ";" ";" ";" ";" ";" "; End of Xylose Data" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\" "; Cellulose" "; (Solid)" ";" ";" ";" ";" ";" ";" "; End of Cellulose Data" ";" ";\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\" "; Xylan" "; (Solid)" ";" ";" ";" ";" ";" ";" ";" "; End of Xylan Data" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\" "; Lignin" "; (Solid)" "; Formula of Lignin C10 H13.9 O1.3" ";" ";" ";" ";" ";" ";" "; End of Lignin Data" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\" "; Acetate" "; (Solid)" "; Formula of Acetate C2H4O2" ";" ";" ";" ";" ";" ";" "; End of Acetate Data" ";" ";\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/" "; Organism (Based on Zymo component, represents Zymo, Cellulase, Biomass)" "; (Solid)" "; Formula of Zymo C H1.8 O0.5 N0.2" ";" ";" ";" ";" ";" ";" "; End of Organism Data" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/" "; Solslds (Represents soluble solids including protein and extractives)" "; (Considered a Mixed Component - Dissolved Solid)" "; Actual Formula:" ";" ";" ";" ";" ";" ";" ";" "; COMPHL required to envoke CPLDIP" ";" ";" ";" "; End of Solslds Data" ";" ";\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/" "; Gypsum" "; Solid" "; Formula of Gypsum CaSO4-2H2O" ";" ";" ";" ";" ";" ";" "; End of Gypsum Data" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\" "; Soluble Lignin" "; Using Formula of Lignin-1" ";" ";" ";" ";" ";" ";" ";" "; COMPHL required to envoke CPLDIP" ";" ";" ";" ";" "; End of Lgnsol Data" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\" "; C6sugar (Copy of Glucose, represents Cellobiose, Mannose, Galactose," "; and C6 oligomers)" ";" ";" ";" ";" ";" ";" "; COMPHL required to envoke CPLDIP" ";" ";" ";" ";" "; End of C6sugar Data" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/" "; C5sugar (Copy of Xylose, represents Arabinose, Xylitol, C5 oligomers)" ";" ";" ";" ";" ";" ";" ";" "; COMPHL required to envoke CPLDIP" ";" ";" ";" ";" ";" "; End of C5sugar Data" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\" "; C6solid (Copy of Cellulose, represents Mannan and Galactan)" "; (Solid)" ";" ";" ";" ";" ";" ";" "; End of C6solid Data" ";" ";\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\" "; C5solid (Copy of Xylan, represents Arabinan and Tar)" "; (Solid)" ";" ";" ";" ";" ";" ";" ";" "; End of C5solid Data" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\" "; Ethanol" "; Selected properties for Ethanol - replace/augment Aspen databanks" ";" ";" ";" ";" ";/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\/\" "; HMF" "; Estimates made from chemical structure." ";" ";" ";" ";" ";" ";" ";" ";" ) \ ? %M PROPERTIES PROP-DATA PARAMS VB ? ; SI ; \ PROP-LIST PARAMNAME = VB \ \ PVAL PARAMNAME2 = VB CID = GLUCOSE VALUE = .01850640 <0> <0> \ \ PROP-LIST PARAMNAME = VB \ \ PVAL PARAMNAME2 = VB CID = XYLOSE VALUE = .01850640 <0> <0> \ \ PROP-LIST PARAMNAME = VB \ \ PVAL PARAMNAME2 = VB CID = SOLSLDS VALUE = .01850640 <0> <0> \ \ PROP-LIST PARAMNAME = VB \ \ PVAL PARAMNAME2 = VB CID = C5SUGAR VALUE = .01850640 <0> <0> \ \ PROP-LIST PARAMNAME = VB \ \ PVAL PARAMNAME2 = VB CID = C6SUGAR VALUE = .01850640 <0> <0> \ \ PROP-LIST PARAMNAME = VB \ \ PVAL PARAMNAME2 = VB CID = LGNSOL VALUE = .01850640 <0> <0> \ \ COMMENTS COMMENTS = ( ";" "; Needed for tray sizing in RADFRAC" ) \ ? SETUP UNITS-SET SET3 ? \ 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) \ ? %M PROPERTIES PROP-DATA CORRS MULDIP ? ; SET3 ; \ PROP-LIST PARAMNAME = MULDIP \ \ PVAL PARAMNAME2 = MULDIP CID = GLUCOSE VAL1 = -2267.40 <0> <0> VAL2 = 138900.0 <0> <0> VAL3 = 320.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 323.0 <0> <0> VAL7 = 418.0 <0> <0> / PARAMNAME2 = MULDIP CID = XYLOSE VAL1 = -2267.40 <0> <0> VAL2 = 138910.0 <0> <0> VAL3 = 320.550 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 323.150 <0> <0> VAL7 = 418.150 <0> <0> / PARAMNAME2 = MULDIP CID = SOLSLDS VAL1 = -2267.40 <0> <0> VAL2 = 138910.0 <0> <0> VAL3 = 320.550 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 323.0 <0> <0> VAL7 = 418.0 <0> <0> / PARAMNAME2 = MULDIP CID = C5SUGAR VAL1 = -2267.40 <0> <0> VAL2 = 138900.0 <0> <0> VAL3 = 320.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 323.0 <0> <0> VAL7 = 418.0 <0> <0> / PARAMNAME2 = MULDIP CID = C6SUGAR VAL1 = -2267.40 <0> <0> VAL2 = 138900.0 <0> <0> VAL3 = 320.0 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 323.0 <0> <0> VAL7 = 418.0 <0> <0> / PARAMNAME2 = MULDIP CID = LGNSOL VAL1 = -2267.40 <0> <0> VAL2 = 138910.0 <0> <0> VAL3 = 320.550 <0> <0> VAL4 = 0.0 <0> <0> VAL5 = 0.0 <0> <0> VAL6 = 323.150 <0> <0> VAL7 = 418.150 <0> <0> \ \ COMMENTS COMMENTS = ( ";" "; Needed for Tray sizing in RADFRAC" ) \ ? %M PROPERTIES PROP-DATA PARAMS MW-1 ? ; SET1 ; \ PROP-LIST PARAMNAME = MW \ \ PVAL PARAMNAME2 = MW CID = NH4ACET VALUE = 77.080 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? %M PROPERTIES PROP-DATA PARAMS MUP-1 ? ; SI ; \ PROP-LIST PARAMNAME = MUP \ \ PVAL PARAMNAME2 = MUP CID = GLUCOSE VALUE = 5.849340E-25 <0> <0> \ \ PROP-LIST PARAMNAME = RGYR \ \ PVAL PARAMNAME2 = RGYR CID = GLUCOSE VALUE = 6.150E-11 <0> <0> \ \ PROP-LIST PARAMNAME = MUP \ \ PVAL PARAMNAME2 = MUP CID = XYLOSE VALUE = 5.849340E-25 <0> <0> \ \ PROP-LIST PARAMNAME = RGYR \ \ PVAL PARAMNAME2 = RGYR CID = XYLOSE VALUE = 6.150E-11 <0> <0> \ \ PROP-LIST PARAMNAME = MUP \ \ PVAL PARAMNAME2 = MUP CID = SOLSLDS VALUE = 5.849340E-25 <0> <0> \ \ PROP-LIST PARAMNAME = RGYR \ \ PVAL PARAMNAME2 = RGYR CID = SOLSLDS VALUE = 6.150E-11 <0> <0> \ \ PROP-LIST PARAMNAME = MUP \ \ PVAL PARAMNAME2 = MUP CID = C5SUGAR VALUE = 5.849340E-25 <0> <0> \ \ PROP-LIST PARAMNAME = RGYR \ \ PVAL PARAMNAME2 = RGYR CID = C5SUGAR VALUE = 6.150E-11 <0> <0> \ \ PROP-LIST PARAMNAME = MUP \ \ PVAL PARAMNAME2 = MUP CID = C6SUGAR VALUE = 5.849340E-25 <0> <0> \ \ PROP-LIST PARAMNAME = RGYR \ \ PVAL PARAMNAME2 = RGYR CID = C6SUGAR VALUE = 6.150E-11 <0> <0> \ \ PROP-LIST PARAMNAME = MUP \ \ PVAL PARAMNAME2 = MUP CID = LGNSOL VALUE = 5.849340E-25 <0> <0> \ \ PROP-LIST PARAMNAME = RGYR \ \ PVAL PARAMNAME2 = RGYR CID = LGNSOL VALUE = 6.150E-11 <0> <0> \ \ PROP-LIST PARAMNAME = MUP \ \ PVAL PARAMNAME2 = MUP CID = HMF VALUE = 5.849340E-25 <0> <0> \ \ PROP-LIST PARAMNAME = RGYR \ \ PVAL PARAMNAME2 = RGYR CID = HMF VALUE = 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." ) \ ? SETUP UNITS-SET SET4 ? \ 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) \ ? %M PROPERTIES PROP-DATA BI-CORRS HENRY-1 ? ; SET4 ; \ PROP-LIST PARAMNAME = HENRY \ \ BPVAL PARAMNAME2 = HENRY CID1 = CH4 CID2 = ETHANOL 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 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 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 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 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 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 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 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 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 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 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 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 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 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 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 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" ";" ) \ ? %M PROPERTIES PROP-DATA BI-CORRS NRTL-1 ? ; SET3 ; \ PROP-LIST PARAMNAME = NRTL \ \ BPVAL PARAMNAME2 = NRTL CID1 = ETHANOL CID2 = H2O 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 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 = ETHANOL CID2 = HMF 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> / PARAMNAME2 = NRTL CID1 = H2O CID2 = FURFURAL 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 = H2O CID2 = HMF 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 = H2O CID2 = NH3 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> \ \ 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" ";" ) \ ? REPORT PROPERTY-REP ? ; SET1 ; \ OPTIONS PARAMS = PARAMS \ ? SETUP GLOBAL ? \ STREAM-CLASS SCLASS = MIXCISLD \ ? HEATSTREAMS QH200 QM202LO QM202HI QF301-6B QF301 QH301 QH302 QF300B QF300CNT QF300 QF300A QH910 QH914 QWELL QH14BCW QH14BCHW QH415 QM401 QF400 QF401-4 QH201 QH201A QH201XTR QH506 QH507 QCD501 QH503 QH517 QH509 QC502A QC502B QRD501 QRD502I QRD502 QCD502 QE501A QE502A QE503A QE501A1 QE501A2 QH602 QM205 QH205 QH244 QH244A QH914A QH914B QH914C QDCOOL2 QH512 QCW QCHW QCWTOT QCHWTOT QM803 QM811 QHXLOW QVLOW QM505 ? \ COMMENTS COMMENTS = ( ";" ) \ ? WORKSTREAMS WM205 WM401 WM505 WCOMBFAN ? \ COMMENTS COMMENTS = ( ";" ";----------------------------------------------------------------------" "; WORK STREAMS" ";----------------------------------------------------------------------" ";" ) \ ? STREAM MATERIAL 101 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 14705.670 <-80> <3> / SSID1 = MIXED CID = SOLSLDS FLOW = 7416.0 <-80> <3> \ \ SUBSTREAM SSID = CISOLID TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 75917.660 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = CISOLID CID = CELLULOS FLOW = .41080 <-3> <0> / SSID1 = CISOLID CID = XYLAN FLOW = .23140 <-3> <0> / SSID1 = CISOLID CID = C5SOLID FLOW = .03210 <-3> <0> / SSID1 = CISOLID CID = C6SOLID FLOW = .03840 <-3> <0> / SSID1 = CISOLID CID = LIGNIN FLOW = .19760 <-3> <0> / SSID1 = CISOLID CID = ACETATE FLOW = .03220 <-3> <0> / SSID1 = CISOLID CID = ASH FLOW = .05740 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ";=======================================================================" "; Streams" ";=======================================================================" ";" ";FEED STREAM" "; Basis 2000 dry metric tonnes/day" "; Total flow 2,000,000 Kg/day" "; 83,333 Kg/hr" ";" ";Corn stover is assumed to have 15% moisture" ";SOLSLDS are soluble solids, extractives and protein combined" ) \ ? STREAM MATERIAL 102B ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 73.92950 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 30587.0 <-80> <3> BASIS = MASS-FRAC \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 5.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" "; POLYMER FOR CLARIFIER / BELT PRESS" "; CONTROLLED BY POLY1" ) \ ? STREAM MATERIAL 211 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 73.480 <22> <4> PRES = 3.0 <20> <3> FLOWBASE = MASS TOTFLOW = 99224.0 <-80> <3> BASIS = MASS-FRAC \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 3.40229820 <20> <3> FLOWBASE = MASS TOTFLOW = 500.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = H2SO4 FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ";INLET ACID STREAM" ) \ ? STREAM MATERIAL 215 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 268.18930 <22> <4> PRES = 13.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 12000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";MEDIUM PRESSURE STEAM TO M202LO IN PRETREATMENT" ";CONTROLLED BY DESIGN SPEC LPSTMFLO" ) \ ? STREAM MATERIAL 216 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 268.18930 <22> <4> PRES = 13.0 <20> <3> FLOWBASE = MASS TOTFLOW = 42638.0 <-80> <3> NPHASE = 2 BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 42662.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";MEDIUM PRESSURE STEAM TO RAISE PRETREATMENT REACTOR" ";TO REACTION TEMPERATURE" ";CONTROLLED BY DESIGN SPEC REACHEAT" ) \ ? STREAM MATERIAL 219 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 127700.0 <-80> <3> NPHASE = 1 PHASE = L BASIS = MASS-FRAC \ \ 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> \ \ SUBSTREAM SSID = CISOLID TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 327.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = CISOLID CID = ORGANISM FLOW = .670 <-3> <0> / SSID1 = CISOLID CID = LIGNIN FLOW = .330 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ";RECYCLE WATER TO BLOWDOWN TANK" ";CONTROLLED BY RECYCLE" ) \ ? STREAM MATERIAL 227 ? ; SET1 ; \ SUBSTREAM SSID = CISOLID TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 987.30 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = CISOLID CID = CAH2O2 FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ";LIME FOR OVERLIMING" ";Controlled by Fortran OLIME" ) \ ? STREAM MATERIAL 233 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 3.40229820 <20> <3> FLOWBASE = MASS TOTFLOW = 421.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = H2SO4 FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ";H2SO4 FOR REACIDIFYING" ";Controlled by Fortran REACID" ) \ ? STREAM MATERIAL 257 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 25.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MOLE TOTFLOW = 2360.0 <-89> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = .790 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .210 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 303A ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 37.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 37.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = DAP FLOW = 500.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 311 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = DAP FLOW = 500.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 310A ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 850.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 311A ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 5116.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 312 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 9167.0 <-80> <3> \ \ SUBSTREAM SSID = CISOLID TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = CISOLID CID = ORGANISM FLOW = 833.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; Cellulase" ) \ ? STREAM MATERIAL 411 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 22703.0 <-80> <3> NPHASE = 1 PHASE = L BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 58.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = CISOLID CID = LIGNIN FLOW = .340 <-3> <0> / SSID1 = CISOLID CID = ORGANISM FLOW = .660 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ";RECYCLE WATER STREAM TO CELLULASE FERMENTORS" ";CONTROLLED BY RECYCLE" ) \ ? STREAM MATERIAL 414 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 463.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";CSL FOR CELLULASE PRODUCTION" ";CONTROLLED BY FORTRAN CSL-ENZY" ) \ ? STREAM MATERIAL 415 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 200.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";NUTRIENT STREAM FOR CELLULASE PRODUCTION" ";CONTROLLED BY FORTRAN CSL-ENZY" ) \ ? STREAM MATERIAL 417 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 238.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";ANTI-FOAM STREAM FOR CALCULATING STORAGE TANK" ";CONTROLLED BY FORTRAN CSL-ENZY" ) \ ? STREAM MATERIAL 423 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 30.50 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";CSL FOR CELLULASE SEED PRODUCTION" ";CONTROLLED BY FORTRAN CSL-ENZY" ) \ ? STREAM MATERIAL 430 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 2143.0 <-80> <3> NPHASE = 1 PHASE = L BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = .98380 <-3> <0> / SSID1 = MIXED CID = XYLOSE FLOW = .00520 <-3> <0> / SSID1 = MIXED CID = SOLSLDS FLOW = .0110 <-3> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 100.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 5.50 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = CISOLID CID = CELLULOS FLOW = .0150 <-3> <0> / SSID1 = CISOLID CID = LIGNIN FLOW = .070 <-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 ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = .150 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = .60 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .20 <-3> <0> / SSID1 = MIXED CID = H2O FLOW = .20 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ";TEAR STREAM INITIAL GUESS" ) \ ? STREAM MATERIAL 434 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 16.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = NH3 FLOW = .50 <-3> <0> / SSID1 = MIXED CID = SO2 FLOW = .50 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 436 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 162.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = NH3 FLOW = .50 <-3> <0> / SSID1 = MIXED CID = SO2 FLOW = .50 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 440 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 126347.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = .790 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .210 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 441 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 152.60 <22> <4> PRES = 2.70 <20> <3> FLOWBASE = MASS TOTFLOW = .0020 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = .790 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .210 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 501 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 30.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 380640.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = ETHANOL FLOW = .040 <-3> <0> / SSID1 = MIXED CID = H2O FLOW = .960 <-3> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 30.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 31667.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = CISOLID CID = CELLULOS FLOW = .180 <-3> <0> / SSID1 = CISOLID CID = LIGNIN FLOW = .820 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 508 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 59.90 <22> <4> PRES = 1.860 <20> <3> BASIS = MASS-FLOW \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 116.0 <22> <4> VFRAC = 1.0 <0> <0> BASIS = MASS-FLOW \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 70.0 <22> <4> PRES = 1.50 <20> <3> FLOWBASE = MASS TOTFLOW = 8381.0 <-80> <3> BASIS = MASS-FRAC \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 26.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 35747.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; Well water for vent scrubber" ) \ ? STREAM MATERIAL 557 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 25.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MOLE TOTFLOW = 205.831685 <-89> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = .790 <-3> <0> / SSID1 = MIXED CID = O2 FLOW = .210 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 574 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 47.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 198670.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";iNITIAL GUESS" ) \ ? STREAM MATERIAL 615 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 35.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = CH4 FLOW = 1200.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";WWT methane to burner/boiler" ) \ ? STREAM MATERIAL 624 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 21.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 17000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; TREATED WW FROM WWT; CALCULATED IN FORTRAN WATERDEM" ) \ ? STREAM MATERIAL 630 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 171.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";WASTEWATER TREATMENT NUTRIENTS" ";CONTROLLED BY FORTRAN WWNUTR" ) \ ? STREAM MATERIAL 631 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 5.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" "; POLYMER FOR BELT PRESS" "; CONTROLLED BY WWNUTR2" ) \ ? STREAM MATERIAL 701 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 812.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ";DENATURANT FOR FINAL BLENDING" ";CONTROLLED BY FORTRAN STORE" ) \ ? STREAM MATERIAL 710 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 514.0 <-80> <3> BASIS = MASS-FRAC \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 6271.0 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ";FIREWATER STREAM FOR CALCULATING STORAGE TANK" ) \ ? STREAM MATERIAL 717 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 17.0 <20> <3> FLOWBASE = MASS TOTFLOW = 229.60 <-80> <3> BASIS = MASS-FRAC \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 14.970 <-80> <3> BASIS = MASS-FRAC \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1.0 <-3> <0> \ \ COMMENTS COMMENTS = ( ";" ";PROPANE FUEL STREAM FOR CALCULATING STORAGE TANK" ";CONTROLLED BY FORTRAN STORE" ) \ ? STREAM MATERIAL 735 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1138.40 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";TOTAL CSL STREAM FOR CELLULASE & ETHANOL PRODUCTION" ";CONTROLLED BY FORTRAN CSL-ENZY" ) \ ? STREAM MATERIAL 745 ? ; SET1 ; \ SUBSTREAM SSID = CISOLID TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = CISOLID CID = CAH2O2 FLOW = 1.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";TOTAL LIME" ";CONTROLLED BY PHCONTR1" ) \ ? STREAM MATERIAL 750 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 9167.0 <-80> <3> \ \ SUBSTREAM SSID = CISOLID TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = CISOLID CID = ORGANISM FLOW = 833.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; Cellulase" ) \ ? STREAM MATERIAL 755 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = DAP FLOW = 1000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; Diammonium Phosphate (DAP), SSCF nutrient" ) \ ? STREAM MATERIAL 804 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 23.8888870 <22> <4> PRES = 1.0 <20> <3> FLOWBASE = MASS TOTFLOW = 263000.0 <-80> <3> BASIS = MASS-FRAC \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 26.0 <22> <4> PRES = 3.40 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 73157.10 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";BFW MAKE-UP" ) \ ? STREAM MATERIAL 821 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 321.0 <22> <4> PRES = 112.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 7219.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";INITIAL GUESS" ) \ ? STREAM MATERIAL 903 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 13.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ 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 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 63.040 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ";CIP/CS WATER" ) \ ? STREAM MATERIAL 914 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 63.040 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 921 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 3.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 922 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 20.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 4.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM MATERIAL 944 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 17820.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; Specified Cooling Tower Blowdown" "; CALCULATED IN FORTRAN CW" ) \ ? STREAM MATERIAL 941A ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 30682.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; Place holder for Calculated Cooling Twr Make-up" ) \ ? STREAM MATERIAL 943 ? ; SET1 ; \ SUBSTREAM SSID = MIXED TEMP = 26.0 <22> <4> PRES = 1.0 <20> <3> BASIS = MASS-FLOW \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 30682.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; Place holder for Well water Mixed with treated water" ) \ ? STREAM HEAT QCD501 ? ; SET1 ; \ INFO DUTY = 103026.298 <13> <3> \ \ COMMENTS COMMENTS = ( ";" ";---------------------------------------------------------------------" "; HEAT STREAMS" ";-------------------------------------------------------------------" ";" "; QCD502 and QRD502I are the condenser and reboiler duties to column" "; AS-502. They will be determined by the FORTRAN block D502QCR" ";" ) \ ? STREAM HEAT QRD501 ? ; SET1 ; \ INFO DUTY = -9.350E+06 <13> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM HEAT QCD502 ? ; SET1 ; \ INFO DUTY = 5827166.32 <13> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM HEAT QRD502I ? ; SET1 ; \ INFO DUTY = -1.092E+06 <13> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM HEAT QH602 ? ; SET1 ; \ INFO DUTY = 637944.0 <13> <3> \ \ COMMENTS COMMENTS = ( ";" "; TEAR -- INITIAL VALUE FROM I0302B, CALCULATED IN WWT" ) \ ? STREAM HEAT QE501A ? ; SET1 ; \ INFO DUTY = .027777378 <13> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM HEAT QM811 ? ; SET1 ; \ INFO DUTY = 0.0 <13> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM WORK WM205 ? ; SET1 ; \ INFO POWER = 0.0 <19> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM WORK WM401 ? ; SET1 ; \ INFO POWER = 0.0 <19> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM WORK WM505 ? ; SET1 ; \ INFO POWER = 0.0 <19> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? STREAM WORK WCOMBFAN ? ; SET1 ; \ INFO POWER = 0.0 <19> <3> \ \ COMMENTS COMMENTS = ( ";" ) \ ? PROP-SET MAIN MASSFLW ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ P1 ID = MASSFLMX UNITS = ( "KG/HR" ) \ \ P2 SUBSTREAM = ALL \ ? REPORT BLOCK-REPORT ? ; SET1 ; \ COMMENTS COMMENTS = ( "; NODESCRIPTION" ";" "; NODESCRIPTION Eliminates the Convergence Summary, but also gets rid of th" "; flowsheet connectivity" ";" ) \ \ OPTIONS INPUT = NOINPUT TOTBAL = NOTOTBAL INCL-BLOCKS = (D501 D502) \ ? BLOCK MIXER C103A ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";------------------------------------------------------------" "; BLOCK SECTION" "; SOLIDS HANDLING BLOCKS - AREA 1000" ";------------------------------------------------------------" ";" ) \ ? BLOCK FSPLIT C103B ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "RECYCLED MAKE-UP WATER AND LOSS WITH DIRT SPLITTER" \ \ PARAM SID = 104B FLOW-BASIS = MASS BASIS-FLOW = 1000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; Set by RECCOND" ) \ ? BLOCK MIXER C103C ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "MIXES POLYMER AND WATER FOR WASTE REMOVAL" \ ? BLOCK FSPLIT M104LOSS ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "MAKE-UP WATER AND EVAPORATION/WINDAGE LOSS SPLITTER" \ \ PARAM SID = 103 FLOW-BASIS = MASS BASIS-FLOW = 11300.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; Set by RECCOND" ) \ ? BLOCK MIXER M104MIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "MIXES INCOMING BIOMASS WITH RETAINED WASH WATER" \ ? BLOCK MIXER A201 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";------------------------------------------------------------" ";" "; PRETREATMENT BLOCKS - AREA 2000" ";------------------------------------------------------------" ";" ) \ \ DESCRIPTION DESCRIPTION = "INLINE SULFURIC ACID MIXER" \ \ PARAM PRES = 4.0 <20> <3> \ ? BLOCK MIXER M202MIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "IMPREGNATOR - DESIGNED TO HEAT MIX TO 100 C" \ \ PARAM PRES = 0.0 <20> <3> \ ? BLOCK HEATER M202LO ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "HEATER TO GET FLUIDS TO RXN TEMP" \ \ PARAM TEMP = 100.0 <22> <4> PRES = 39.260 <20> <3> \ ? BLOCK FLASH2 T203 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "PREHYDROLYSIS BLOWDOWN TANK" \ \ PROPERTIES OPSETNAME = NRTL-HOC \ \ PARAM PRES = 1.0 <20> <3> DUTY = 0.0 <13> <3> \ ? BLOCK MIXER H200MIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "MIX 2 STREAMS BEFORE COOLER" \ \ PARAM PRES = 0.0 <20> <3> \ ? BLOCK HEATER H200 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "HYDROLYSATE SLURRY COOLER" \ \ PARAM TEMP = 50.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK MIXER C202 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "MIX CENTRIFUGE LIQUID STREAMS" \ \ PARAM PRES = 0.0 <20> <3> \ ? BLOCK MIXER P224 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "MIX DETOXED SLURRY AND RECYCLE WATER" \ ? BLOCK FSPLIT S205SPT ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "RECYCLE WATER SPLITTER" \ \ PARAM SID = 252 FLOW-BASIS = MASS BASIS-FLOW = 125000.0 <-80> <3> \ \ COMMENTS COMMENTS = ( ";" "; Calculated in FORTRAN S205WASH" ) \ ? BLOCK HEATER H244 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "COOL BLOWDOWN VAPOR PRIOR TO WWT" \ \ PARAM TEMP = 30.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK MIXER H244MIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "COOLING WATER HEAT STREAMS THAT ARE REQUIRED FOR H244" \ ? BLOCK SSPLIT S205A ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "PRE-WASH SEPARATIONS FOR S-202" \ \ PROPERTIES OPSETNAME = NRTL-HOC \ \ PARAM1 PRES = 1.0 <20> <3> \ \ PARAM SID = 225 SUBSTREAM = MIXED FRAC = .1450 <0> <0> / SID = 225 SUBSTREAM = CISOLID FRAC = .9950 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? BLOCK MIXER S205MIX ? ; SET1 ; \ COMMENTS COMMENTS = ( "; THE MIXED FRACTION IS CALCULATED BY DESIGN-SPEC CT-S205A" ";" ) \ \ DESCRIPTION DESCRIPTION = "MIXES WASH-WATER WITH SINGLE-PRESSED SOLIDS" \ \ PARAM PRES = 0.0 <20> <3> \ ? BLOCK SEP S205B ? ; SET1 ; \ 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" ) \ \ DESCRIPTION DESCRIPTION = "POST-WASH SEPARATIONS FOR S205" \ \ PARAM PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = H2O FRACS = .750 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ETHANOL FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = FURFURAL FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = HMF 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 = NO2 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = NH3 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = SOLSLDS FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = GLUCOSE FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = XYLOSE FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = C5SUGAR FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = NH4SO4 FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = NH4ACET FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = C6SUGAR FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = AACID FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = LACID FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = LGNSOL FRACS = .90 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CELLULOS FRACS = 0.0 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = XYLAN FRACS = 0.0 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = C5SOLID FRACS = 0.0 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = C6SOLID FRACS = 0.0 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = LIGNIN FRACS = 0.0 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ORGANISM FRACS = 0.0 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = CAH2O2 FRACS = 0.0 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = GYPSUM FRACS = 0.0 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ACETATE FRACS = 0.0 <0> <0> / PARAM-STREAM = 256 SUBSTREAM = MIXED COMPS = ASH FRACS = 0.0 <0> <0> / 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 = C5SOLID FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = C6SOLID FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = LIGNIN FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = ORGANISM FRACS = 1.0 <0> <0> / PARAM-STREAM = 255A SUBSTREAM = CISOLID COMPS = CAH2O2 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 = ASH FRACS = 1.0 <0> <0> \ \ PARAM1 PRES1 = 0.0 <20> <3> \ ? BLOCK COMPR M205 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "AIR COMPRESSOR FOR PNEUMAPRESS SYSTEM" \ \ PARAM TYPE = ISENTROPIC SEFF = .720 <0> <0> DELP = 8.50574550 <75> <3> \ ? BLOCK HEATER M205COOL ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "COOLER FOR COMPRESSED PNEUMAPRESS AIR" \ \ PARAM TEMP = 40.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK FLASH2 S205FLSH ? ; SET1 ; \ COMMENTS COMMENTS = ( "; PARAM TEMP=40.0" ";" ) \ \ DESCRIPTION DESCRIPTION = "AIR-SOLID CONTACT IN PNEUMAPRESS" \ \ PARAM PRES = 0.0 <20> <3> DUTY = 0.0 <13> <3> \ ? BLOCK FLASH2 H205 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "CONDENSER ON PNEUMAPRESS VENT" \ \ PARAM TEMP = 38.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK SSPLIT S222 ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "GYPSUM REMOVAL S/L SEP" \ \ PARAM SID = 229 SUBSTREAM = MIXED FRAC = .0040 <0> <0> / SID = 229 SUBSTREAM = CISOLID FRAC = .9950 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? BLOCK RSTOIC T224 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ 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> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = GYPSUM STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = CISOLID KEY-CID = CAH2O2 CONV = 1.0 <0> <0> \ ? BLOCK RSTOIC M202HI ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ 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 = 1 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <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 = 5 STOIC-CID = H2O STOIC-SSID = MIXED 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 = XYLAN STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = C6SOLID STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = C6SOLID 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 = C5SOLID STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = C5SOLID 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 = -2.0 <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 = -2.0 <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 = C6SUGAR 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 = C5SUGAR 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 = C5SOLID STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = C6SUGAR 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 = 16 STOIC-CID1 = C5SUGAR 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 = 20 STOIC-CID1 = AACID STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 21 STOIC-CID1 = C5SOLID STOIC-SSID1 = CISOLID COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 22 STOIC-CID1 = C5SOLID STOIC-SSID1 = CISOLID COEF1 = 1.22730 <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 = .0140 <0> <0> / EXT-REACNO = 3 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .070 <0> <0> / EXT-REACNO = 4 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = 0.0 <0> <0> / EXT-REACNO = 5 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = .0250 <0> <0> / EXT-REACNO = 6 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = .90 <0> <0> / EXT-REACNO = 7 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = .050 <0> <0> / EXT-REACNO = 8 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = 0.0 <0> <0> / EXT-REACNO = 10 KEY-SSID = CISOLID KEY-CID = C6SOLID CONV = .9250 <0> <0> / EXT-REACNO = 11 KEY-SSID = CISOLID KEY-CID = C6SOLID CONV = .050 <0> <0> / EXT-REACNO = 16 KEY-SSID = CISOLID KEY-CID = C5SOLID CONV = .9250 <0> <0> / EXT-REACNO = 17 KEY-SSID = CISOLID KEY-CID = C5SOLID CONV = .050 <0> <0> / EXT-REACNO = 20 KEY-SSID = CISOLID KEY-CID = ACETATE CONV = 1.0 <0> <0> / EXT-REACNO = 21 KEY-SSID = MIXED KEY-CID = FURFURAL CONV = 1.0 <0> <0> / EXT-REACNO = 22 KEY-SSID = MIXED KEY-CID = HMF CONV = 1.0 <0> <0> / EXT-REACNO = 23 KEY-SSID = CISOLID KEY-CID = LIGNIN CONV = .050 <0> <0> \ ? BLOCK RSTOIC T209 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ 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> \ ? BLOCK FSPLIT SACCHSPT ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "FEED SPLITTER TO SEED TRAIN" \ \ PARAM SID = 303 FRAC = .10 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ";------------------------------------------------------------" "; SACCHARIFICATION AND CO-FERMENTATION BLOCKS - AREA 300" ";------------------------------------------------------------" ";" ) \ ? BLOCK MIXER FERMMIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";10% IS SAME VALUE IN SSFSPLT IN SSF MODEL" ";SOURCE NOT DOCUMENTED" ";" ) \ \ DESCRIPTION DESCRIPTION = "MIX CSL, DAP AND SEED WITH HYD. BEFORE FERM" \ ? BLOCK FSPLIT CONTSPLT ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "SPLIT TO CONTAMINATION REACTION" \ \ PARAM SID = 304G FRAC = .030 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? BLOCK MIXER T306 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";3% Contamination" ";" ) \ \ DESCRIPTION DESCRIPTION = "BEER WELL" \ ? BLOCK FLASH2 F300FLSH ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "DUMMY BLOCK TO RELEASE GASES FROM FERM" \ \ PARAM PRES = 1.0 <20> <3> DUTY = 0.0 <13> <3> \ ? BLOCK HEATER H301- ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "HYDROLYSATE SLURRY HEATER FOR SACCH." \ \ PARAM TEMP = 65.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK RSTOIC T310 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; THE HYDROLYSIS REACTIONS ARE CALCULATED IN THIS BLOCK." "; THE REACTIONS NEEDED FOR FERMENTATION HAVE BEEN COMMENTED OUT." ";" "; THE CONVERSTIONpS TO ETHANOL ARE BASED ON PD 23 #3 MODIFIED" "; SO THAT 4% OF MONOMERIC SUGARS ARE CONVERTED TO CELL MASS" ";" ) \ \ 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 = 1 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> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = C6SUGAR STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = GLUCOSE STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .0520 <0> <0> / EXT-REACNO = 3 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .910 <0> <0> \ ? BLOCK RSTOIC F300F ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; THE FERMENTATION REACTIONS ARE CALCULATED IN THIS BLOCK" "; THE HYDROLYSIS REACTIONS HAVE BEEN COMMENTED OUT" ";" ) \ \ 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 = DAP STOIC-SSID = MIXED COEF = -.0180 <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 = DAP STOIC-SSID = MIXED COEF = -.0150 <0> <0> \ \ STOIC REACNO = 19 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <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 = C5SUGAR STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 35 STOIC-CID = C6SUGAR 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 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1.40 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = .30 <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 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1.1650 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = .250 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = C5SUGAR STOIC-SSID1 = MIXED COEF1 = 1.0 <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 = 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> \ \ CONVEX EXT-REACNO = 7 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .950 <0> <0> / EXT-REACNO = 8 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0170 <0> <0> / EXT-REACNO = 11 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0150 <0> <0> / EXT-REACNO = 12 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0150 <0> <0> / EXT-REACNO = 16 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .850 <0> <0> / EXT-REACNO = 17 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0190 <0> <0> / EXT-REACNO = 19 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0460 <0> <0> / EXT-REACNO = 21 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0230 <0> <0> / EXT-REACNO = 22 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .0020 <0> <0> / EXT-REACNO = 26 KEY-SSID = MIXED KEY-CID = C5SUGAR CONV = .80 <0> <0> / EXT-REACNO = 35 KEY-SSID = MIXED KEY-CID = C6SUGAR CONV = .3250 <0> <0> \ ? BLOCK RSTOIC F300CONT ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; ALL FERMENTABLE SUGARS ARE CONVERTED TO LACTIC ACID IN THIS BLOCK" "; THE FRACTION OF SUGAR LOST TO CONTAMINATION IS SET IN CONTSPLT" ) \ \ 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 = C5SUGAR STOIC-SSID = MIXED COEF = -3.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = C6SUGAR 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> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = 1.0 <0> <0> / EXT-REACNO = 2 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = 1.0 <0> <0> / EXT-REACNO = 3 KEY-SSID = MIXED KEY-CID = C5SUGAR CONV = .340 <0> <0> / EXT-REACNO = 4 KEY-SSID = MIXED KEY-CID = C6SUGAR CONV = .430 <0> <0> \ ? BLOCK HEATER H302 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "SACCHARIFIED SLURRY COOLER BEFORE FERMENTATION" \ \ PARAM TEMP = 41.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK MIXER SEEDMIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "MIX CSL AND DAP WITH HYD BEFORE SEED FERM" \ ? BLOCK RSTOIC F301-6F ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; THE FERMENTATION REACTIONS ARE CALCULATED IN THIS BLOCK" "; THE HYDROLYSIS REACTIONS HAVE BEEN COMMENTED OUT" ";" "; THE CONVERSTIONS TO ETHANOL ARE BASED ON PD 23 #3 MODIFIED" "; SO THAT 4% OF MONOMERIC SUGARS ARE CONVERTED TO CELL MASS" ";" ) \ \ 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 = DAP STOIC-SSID = MIXED COEF = -.0180 <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 = DAP STOIC-SSID = MIXED COEF = -.0150 <0> <0> \ \ STOIC REACNO = 19 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <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> \ \ 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 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1.40 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = .30 <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 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1.1350 <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = .250 <0> <0> \ \ STOIC1 REACNO1 = 19 STOIC-CID1 = C5SUGAR STOIC-SSID1 = MIXED COEF1 = 1.0 <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> \ \ CONVEX EXT-REACNO = 7 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .850 <0> <0> / EXT-REACNO = 8 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .040 <0> <0> / EXT-REACNO = 11 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0220 <0> <0> / EXT-REACNO = 12 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .0230 <0> <0> / EXT-REACNO = 16 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .80 <0> <0> / EXT-REACNO = 17 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .030 <0> <0> / EXT-REACNO = 19 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .020 <0> <0> / EXT-REACNO = 21 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .010 <0> <0> / EXT-REACNO = 22 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = 0.0 <0> <0> \ ? BLOCK FLASH2 F301-6FL ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "SEED CO2 VENT" \ \ PARAM PRES = 1.0 <20> <3> DUTY = 0.0 <13> <3> \ ? BLOCK MIXER T415 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";-----------------------------------------------------------" "; CELLULASE BLOCKS - AREA 4000" ";----------------------------------------------------------" ";" ) \ \ DESCRIPTION DESCRIPTION = "MIXER FOR FEED AND WATER TO CELLULASE PRODUCTION." \ ? BLOCK MIXER F401-4MX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "MIXER FOR FEED AND WATER TO CELLULASE SEED FERMENTORS." \ ? BLOCK MIXER T405 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "CELLULASE MEDIA PREP TANK" \ ? BLOCK FSPLIT BTMSSPLT ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "SPLIT CENTRIFUGE BOTTOMS BETWEEN CELLULASE FERMENTATION & SSF" \ \ PARAM SID = 401 FRAC = .0220 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? BLOCK FSPLIT CLFDSPLT ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "SPLIT BETWEEN SEED AND FERMENTORS." \ \ PARAM1 NPHASE1 = 1 PHASE1 = L \ \ PARAM SID = 403 FRAC = .050 <0> <0> \ \ COMMENTS COMMENTS = ( ";THE FRACTION SPECIFIED IS A GUESS BASED ON THE 1990 BASE CASE. THE" ";ACTUAL SPLIT IS CALCULATED BY THE FORTRAN BLOCK ENZYME DEPENDING ON" ";THE LOADING REQUIRED IN SSCF." ";" ) \ ? BLOCK FSPLIT CLSSPLIT ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "SPLIT CELL. RCTR EFF. BTWN SSF SD FERM + SSF FRM" \ \ PARAM SID = 421 FRAC = .20 <0> <0> \ \ 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 HEATER H415 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "COOLER FOR CELLULASE PRODUCTION FERMENTOR WATER" \ \ PARAM TEMP = 40.0 <22> <4> PRES = 1.0 <20> <3> \ ? BLOCK FLASH2 F401-4FL ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "CELLULASE SEED DUMMY FOR FLASH CALC." \ \ PARAM PRES = 1.0 <20> <3> DUTY = 0.0 <13> <3> \ ? BLOCK FLASH2 F400FL ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "CELLULASE PRODUCTION DUMMY FOR FLASH CALC." \ \ PARAM PRES = 0.0 <20> <3> DUTY = 0.0 <13> <3> \ ? BLOCK RSTOIC F400 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; NH3 addition through stream 436 are set by FORTRAN" "; Block NUTR400. If the conversions are changed, FORTRAN must also" "; be modified." ";CONVERSIONS ARE BASED ON THE 1990 BASE CASE." ) \ \ 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 = -1.0 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.46840 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.54080 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = C6SUGAR STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.46840 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.54080 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.60960 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.79740 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = C5SUGAR STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.60960 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.79740 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.54160 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.15670 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.54160 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.15670 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = C6SOLID STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.65790 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.59470 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 2.34210 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.65790 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.59470 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 2.34210 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.95180 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.1670 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 3.04820 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.95180 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.1670 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 3.04820 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.29210 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.37530 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 2.70790 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.29210 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.37530 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 2.70790 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = 1.0 <0> <0> / EXT-REACNO = 2 KEY-SSID = MIXED KEY-CID = C6SUGAR CONV = .6150 <0> <0> / EXT-REACNO = 3 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = 1.0 <0> <0> / EXT-REACNO = 4 KEY-SSID = MIXED KEY-CID = C5SUGAR CONV = .390 <0> <0> / EXT-REACNO = 5 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = 1.0 <0> <0> / EXT-REACNO = 6 KEY-SSID = CISOLID KEY-CID = C6SOLID CONV = 1.0 <0> <0> \ ? BLOCK RSTOIC F401-4 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; NH3 addition through stream 434 is set by FORTRAN" "; block NUTR4S. If conversions are changed, the FORTRAN must" "; also be modified." ";" "; CONVERSIONS ARE BASED ON THE 1990 BASE CASE." ) \ \ 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 = -1.0 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.46840 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.54080 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = C6SUGAR STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.46840 <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.54080 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = XYLOSE STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.60960 <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.79740 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = C5SUGAR STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.60960 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.79740 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.54160 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.15670 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = CELLULOS STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = NH3 STOIC-SSID = MIXED COEF = -.54160 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -3.15670 <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = C6SOLID STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.65790 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.59470 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 2.34210 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.65790 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.59470 <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 2.34210 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.95180 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.1670 <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 3.04820 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.95180 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.1670 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 3.04820 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.29210 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.37530 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 2.70790 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 3.29210 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.37530 <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = ORGANISM STOIC-SSID1 = CISOLID COEF1 = 2.70790 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = 1.0 <0> <0> / EXT-REACNO = 2 KEY-SSID = MIXED KEY-CID = C6SUGAR CONV = .590 <0> <0> / EXT-REACNO = 3 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = 1.0 <0> <0> / EXT-REACNO = 4 KEY-SSID = MIXED KEY-CID = C5SUGAR CONV = .350 <0> <0> / EXT-REACNO = 5 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = 1.0 <0> <0> / EXT-REACNO = 6 KEY-SSID = CISOLID KEY-CID = C6SOLID CONV = 1.0 <0> <0> \ ? BLOCK HEATER "H201+" ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";" ";-------------------------------------------------------------" "; DISTILLATION BLOCKS - AREA 5000" ";-------------------------------------------------------------" ";" ) \ \ DESCRIPTION DESCRIPTION = "FEED CROSS EXCHANGER (HOT SIDE)" \ \ PROPERTIES OPSETNAME = NRTL-HOC \ \ PARAM PRES = 1.0 <20> <3> VFRAC = 0.0 <0> <0> \ ? BLOCK FSPLIT QH201SPT ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "SPLITTER TO SET FRAC TO H201-" \ \ PARAM SID = QH201 FRAC = .950 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ";Split is controlled by D-Spec H201TEMP to reach temp spec for 501" ) \ ? BLOCK HEATER H201- ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";Temp is specified by D-Spec H201TEMP" ) \ \ DESCRIPTION DESCRIPTION = "FEED CROSS EXCHANGER (COLD SIDE)" \ \ PARAM PRES = 4.0 <20> <3> \ ? BLOCK HEATER H512- ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "BEER COLUMN BTMS/FEED INTERCHANGER, FEED SIDE" \ \ PARAM TEMP = 100.0 <22> <4> PRES = 4.76321748 <20> <3> \ ? BLOCK HEATER "H512+" ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "BEED COL BTMS/FEED INTERCHANGER, BTMS SIDE" \ \ PARAM PRES = 0.0 <20> <3> \ ? BLOCK RADFRAC D501 ? ; ENG ; \ COMMENTS COMMENTS = ( ";" ) \ \ PARAM NSTAGE = 16 MAXOL = 100 ALGORITHM = NONIDEAL SOLID-BAL = STAGE \ \ COL-SPECS RDV-BASIS = MOLE BASIS-RDV = 1.0 <-1> <0> RR-BASIS = MOLE BASIS-RR = 3.0 <-1> <0> DP-COL = 3.0 <75> <2> D-BASIS = MASS BASIS-D = 1050.0 <-80> <2> DP-COND = .50 <75> <2> \ \ FEEDS FEED-SID = 506 FEED-STAGE = 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> \ \ P-SPEC2 PRES1 = 27.40 <20> <2> \ \ SPEC SPEC-NO = 1 SPEC-TYPE = TEMP VALUE = 140.0 <0> <0> SCALE = 1.0 <0> <0> SPEC-STAGE = 1 / SPEC-NO = 2 SPEC-TYPE = MASS-FRAC VALUE = .00050 <0> <0> SPEC-STAGE = 16 SPEC-COMPS = (ETHANOL) \ \ PRODUCTS PROD-STREAM = 518 PROD-STAGE = 16 PROD-PHASE = L / PROD-STREAM = 508 PROD-STAGE = 1 PROD-PHASE = V / PROD-STREAM = 510 PROD-STAGE = 3 PROD-PHASE = V PROD-FLOW = 105000.0 <-80> <2> FLOW-BASIS = MASS \ \ H-PRODUCTS H-PROD-SID = QCD501 H-PROD-STAGE = 1 / H-PROD-SID = QRD501 H-PROD-STAGE = 16 \ \ TRAY-SIZE TS-SECNO = 1 TS-STAGE1 = 2 TS-STAGE2 = 15 TS-TRAYTYPE = SIEVE \ \ SIZE-DATA COND = YES REB = YES \ \ VARY VARY-NO = 2 VARTYPE = VPROD LB = 60000.0 <0> <0> UB = 120000.0 <0> <0> VARY-STAGE = 3 / VARY-NO = 3 VARTYPE = D LB = 800.0 <0> <0> UB = 1100.0 <0> <0> \ ? BLOCK SEP2 D502 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; Overhead - 511" ";" "; Bottoms 516" ";" ) \ \ FLASH-SPECS FLASH-STREAM = 511 TEMP = 92.4110 <22> <4> VFRAC = 1.0 <0> <0> / FLASH-STREAM = 516 TEMP = 121.0490 <22> <4> VFRAC = 0.0 <0> <0> \ \ PARAM PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = GLUCOSE FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = XYLOSE FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = SOLSLDS FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = C5SUGAR FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = C6SUGAR 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 = 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 = O2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = SO2 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 = FURFURAL 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 = 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 = LGNSOL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = CH4 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = NH4SO4 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = NH4ACET FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = NO2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = DAP 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 = XYLAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = C5SOLID FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = C6SOLID 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 = ORGANISM 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 = 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 = ASH FRACS = 0.0 <0> <0> / 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 = ORGANISM 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 = ASH FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = C5SOLID FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 516 COMPS = C6SOLID 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 = ACETATE FRACS = 1.0 <0> <0> \ \ PARAM PARAM-SUBS = MIXED PARAM-STREAM = 511 COMPS = ETHANOL MFFRAC = .8260 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 516 COMPS = ETHANOL MFFRAC = .00020 <0> <0> \ ? BLOCK HEATER H506- ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "PROCESS SIDE OF ETOH SUPERHEATER BEFORE MOLE SIEVE" \ \ PARAM TEMP = 116.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK SEP2 T507-8 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; Overheads" "; Bottoms" ) \ \ DESCRIPTION DESCRIPTION = "MOLE SIEVE" \ \ PARAM PARAM-SUBS = MIXED PARAM-STREAM = 515A COMPS = ETHANOL FRACS = .150 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = H2O FRACS = .0050 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = GLUCOSE 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 = AACID 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 = FURFURAL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = HMF 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 = C5SUGAR FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = C6SUGAR 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 = N2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = NH3 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = SO2 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 = NO2 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = SOLSLDS FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CH4 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = NH4SO4 FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = NH4ACET FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = LGNSOL FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = DAP FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = CELLULOS FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = XYLAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = C5SOLID FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 514 COMPS = C6SOLID 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 = ORGANISM 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 = 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 = ASH FRACS = 0.0 <0> <0> / 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 = ORGANISM 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 = ASH FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = C5SOLID FRACS = 1.0 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 514 COMPS = C6SOLID 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 = ACETATE FRACS = 1.0 <0> <0> \ ? BLOCK HEATER H503 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "COOL DOWN SEPARATED WATER & REGEN LOSSES" \ \ PARAM TEMP = 35.0 <22> <4> PRES = .136091928 <20> <3> \ ? BLOCK HEATER H507- ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "PROD/REGEN RECYCLE INTERCHANGER, PROD SIDE" \ \ PARAM PRES = 1.53103419 <20> <3> \ ? BLOCK HEATER "H507+" ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "PROD/REGEN RECYCLE INTERCHANGER, REGEN SIDE" \ \ PARAM TEMP = 91.70 <22> <4> PRES = 1.440 <20> <3> \ ? BLOCK HEATER H509 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "PRODUCT ETHANOL CONDENSER AND COOLER AFTER MOLE SIEVE" \ \ PARAM TEMP = 38.0 <22> <4> PRES = 1.0 <20> <3> \ ? BLOCK DUPL RECTDUP ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "DUPLICATES QCD502 FOR EVAPORATOR AND CW CAPITAL" \ ? BLOCK DUPL STMDUP ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "DUPLICATES QE501A FOR EVAPS AND STEAM TOTALIZER" \ ? BLOCK MIXER E501MIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "MIXES CONDENSATE FROM EVAPORATOR" \ \ PARAM PRES = 2.0 <20> <3> \ ? BLOCK FSPLIT E501WW ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "SPECIFIES FLOW TO WASTEWATER TREATMENT" \ \ PARAM SID = 535 FRAC = .10 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? BLOCK FSPLIT E501SPT ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "SPLITS CONDENSATE RECYCLE" \ \ PARAM1 PRES1 = 3.0 <20> <3> \ \ DEF-KEY DEF-KEYNO = 1 SUBSTREAM = MIXED COMPS = (H2O) \ \ 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 \ \ COMMENTS COMMENTS = ( ";" ) \ ? BLOCK HEATER E502V ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "2ND EFFECT CONDENSER" \ \ PARAM VFRAC = 0.0 <0> <0> DELT = 0.0 <31> <3> \ ? BLOCK HEATER E503V ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "3RD EFFECT CONDENSER" \ \ PARAM VFRAC = 0.0 <0> <0> DELT = 0.0 <31> <3> \ ? BLOCK HEATER H517 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "FINAL CONDENSER ON EVAPORATOR" \ \ PARAM VFRAC = 0.0 <0> <0> DELT = 0.0 <31> <3> \ ? BLOCK FLASH2 E501L ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "1ST EFFECT LIQUID SIDE" \ \ PROPERTIES OPSETNAME = NRTL-HOC \ \ PARAM PRES = .57070 <20> <3> \ ? BLOCK FLASH2 E502L ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "2ND EFFECT LIQUID SIDE" \ \ PROPERTIES OPSETNAME = NRTL-HOC \ \ PARAM PRES = .30410 <20> <3> \ ? BLOCK FLASH2 E503L ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "3RD EFFECT LIQUID SIDE" \ \ PROPERTIES OPSETNAME = NRTL-HOC \ \ PARAM PRES = .2110 <20> <3> \ ? BLOCK MIXER VNTMIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "VENT MIXER" \ ? BLOCK RADFRAC VNTSCRUB ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ PARAM NSTAGE = 4 \ \ COL-SPECS RDV-BASIS = MOLE BASIS-RDV = 1.0 <-1> <0> Q1 = 0.0 <13> <3> QN = 0.0 <13> <3> \ \ FEEDS FEED-SID = 524 FEED-STAGE = 1 / FEED-SID = 523 FEED-STAGE = 4 FEED-CONVEN = ON-STAGE \ \ P-SPEC PRES-STAGE = 1 STAGE-PRES = .90 <20> <3> \ \ PRODUCTS PROD-STREAM = 550 PROD-STAGE = 1 PROD-PHASE = V / PROD-STREAM = 551 PROD-STAGE = 4 PROD-PHASE = L \ ? BLOCK HEATER DCOOL2 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "DUMMY COOLER / AMBIENT COOLING IN S505" \ \ PARAM TEMP = 40.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK FSPLIT T530 ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "RECYCLE WATER AND WWT LIQUID SEPARATOR" \ \ PARAM SID = 580 FRAC = .750 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? BLOCK SEP2 S505 ? ; SET1 ; \ 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." ";" ";ALL CNUTR & CSL & DAP SHOULD HAVE BEEN CONSUMED" ";SO ANY REMAINING SHOULD GO OFF WITH SOLIDS 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." ) \ \ DESCRIPTION DESCRIPTION = "BEER BOTTOMS PNEUMAPRESS" \ \ PARAM PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = H2O FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ETHANOL FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = FURFURAL FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = HMF 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 = NH3 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = SOLSLDS FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = GLUCOSE FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = XYLOSE FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = C6SUGAR FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = NO2 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = C5SUGAR FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = AACID FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = LACID FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = LGNSOL FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = NH4SO4 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = NH4ACET FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = SO2 FRACS = .10 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = DAP FRACS = 1.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CELLULOS FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = XYLAN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = C5SOLID FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = C6SOLID FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = LIGNIN FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ORGANISM FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = CAH2O2 FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = GYPSUM FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ACETATE FRACS = 0.0 <0> <0> / PARAM-SUBS = MIXED PARAM-STREAM = 571B COMPS = ASH FRACS = 0.0 <0> <0> / 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 = C5SOLID FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = C6SOLID FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = LIGNIN FRACS = .980 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = ORGANISM FRACS = .50 <0> <0> / PARAM-SUBS = CISOLID PARAM-STREAM = 571B COMPS = CAH2O2 FRACS = .980 <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 = ASH FRACS = .980 <0> <0> \ \ PARAM1 PRES1 = 3.20 <20> <3> \ ? BLOCK COMPR M505 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "AIR COMPRESSOR FOR POST-D PNEUMAPRESS SYSTEM" \ \ PARAM TYPE = ISENTROPIC SEFF = .720 <0> <0> DELP = 8.50574550 <75> <3> \ ? BLOCK HEATER M505COOL ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "COOLER FOR COMPRESSED PNEUMAMPRESS AIR" \ \ PARAM TEMP = 40.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK FLASH2 S505FLSH ? ; SET1 ; \ COMMENTS COMMENTS = ( "; PARAM TEMP=40.0" ";" ) \ \ DESCRIPTION DESCRIPTION = "AIR-SOLIDS CONTACT IN PNEUMAPRESS" \ \ PARAM PRES = 0.0 <20> <3> DUTY = 0.0 <13> <3> \ ? BLOCK FSPLIT RWSPLT ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "RECYCLE WATER SPLITTER" \ \ PARAM SID = 219 FRAC = .80 <0> <0> / SID = 430 FRAC = .0010 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? BLOCK MIXER FWMIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";THE FRACTIONS LISTED ARE ASSUMPTIONS. THE ACTUAL VALUES ARE" ";DETERMINED BY THE FORTRAN BLOCK RECYCLE." ";" ) \ \ DESCRIPTION DESCRIPTION = "TANK T-530 FOR MIXING FRESH H2O AND RECYCLE H2O" \ \ PARAM NPHASE = 1 PHASE = L \ ? BLOCK MIXER S600 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";------------------------------------------------------------" "; DIGESTION (WASTE WATER TREATMENT) BLOCKS - AREA 6000" ";----------------------------------------------------------" ";" ) \ \ DESCRIPTION DESCRIPTION = "TANK T-603 TO MIX PROCESS WASTEWATER AND OTHER WASTES" \ \ PARAM PRES = 2.0 <20> <3> \ ? BLOCK MIXER NUTMIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "DUMMMY MIXER FOR WWT CHEMICALS AND NUTRIENTS" \ ? BLOCK HEATER DCOOLE ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";-----------------------------------------------------------" "; STORAGE BLOCKS - AREA 7000 & 7100" ";-----------------------------------------------------------" ";" ) \ \ DESCRIPTION DESCRIPTION = "DUMMY COOLER TO SET ETHANOL DENSITY" \ \ PARAM TEMP = 20.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK MIXER PRODMIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "ETHANOL AND DENATURANT MIXER" \ \ PARAM PRES = 1.0 <20> <3> \ ? BLOCK MIXER TSTORE ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "GENERAL STORAGE TANK" \ ? BLOCK MIXER M802MIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";--------------------------------------------------------------" "; BOILER BLOCKS - AREA 8000" ";-------------------------------------------------------------" ";" ) \ \ DESCRIPTION DESCRIPTION = "MIX PNEUMAPRESS VENTS AND INCOMING AIR" \ ? BLOCK MIXER BTUTOT ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "COMBINES BOILER FEED STREAMS 615, 571 AND 531" \ ? BLOCK MIXER BLRWTR ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "BOILER MAKEUP WATER AND CHEMICALS" \ ? BLOCK COMPR M802 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "COMBUSTION FAN" \ \ PARAM TYPE = ISENTROPIC PRES = 1.01388490 <20> <3> SEFF = .750 <0> <0> NPHASE = 2 SB-MAXIT = 100 \ ? BLOCK RSTOIC BURNER ? ; SET3 ; \ COMMENTS COMMENTS = ( ";" ";" ) \ \ PARAM TEMP = 160.0 <22> <4> PRES = -.03402298 <20> <5> NPHASE = 1 \ \ 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 = 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 = 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 = 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 = 18 STOIC-CID = C6SUGAR STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 18 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 22 STOIC-CID = C5SUGAR STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 22 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <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 = 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 = ORGANISM STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 29 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1.20 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = C5SOLID STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -5.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = C6SOLID STOIC-SSID = CISOLID COEF = -1.0 <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -6.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = NH4ACET STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -2.750 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = CH4 STOIC-SSID = MIXED COEF = -1.0 <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -2.0 <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> \ \ 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 4.0 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 5.0 <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 6.0 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 2.0 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 3.50 <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = .50 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1.0 <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 2.0 <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> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = CISOLID KEY-CID = CELLULOS CONV = .990 <0> <0> / EXT-REACNO = 3 KEY-SSID = CISOLID KEY-CID = XYLAN CONV = .990 <0> <0> / EXT-REACNO = 6 KEY-SSID = CISOLID KEY-CID = LIGNIN CONV = .990 <0> <0> / EXT-REACNO = 8 KEY-SSID = CISOLID KEY-CID = ACETATE CONV = .990 <0> <0> / EXT-REACNO = 11 KEY-SSID = MIXED KEY-CID = GLUCOSE CONV = .990 <0> <0> / EXT-REACNO = 12 KEY-SSID = MIXED KEY-CID = HMF CONV = .990 <0> <0> / EXT-REACNO = 14 KEY-SSID = MIXED KEY-CID = XYLOSE CONV = .990 <0> <0> / EXT-REACNO = 15 KEY-SSID = MIXED KEY-CID = FURFURAL CONV = .990 <0> <0> / EXT-REACNO = 18 KEY-SSID = MIXED KEY-CID = C6SUGAR CONV = .990 <0> <0> / EXT-REACNO = 22 KEY-SSID = MIXED KEY-CID = C5SUGAR CONV = .990 <0> <0> / EXT-REACNO = 24 KEY-SSID = MIXED KEY-CID = AACID CONV = .990 <0> <0> / EXT-REACNO = 25 KEY-SSID = MIXED KEY-CID = LACID CONV = .990 <0> <0> / EXT-REACNO = 27 KEY-SSID = MIXED KEY-CID = SOLSLDS CONV = .990 <0> <0> / EXT-REACNO = 28 KEY-SSID = MIXED KEY-CID = ETHANOL CONV = .990 <0> <0> / EXT-REACNO = 29 KEY-SSID = CISOLID KEY-CID = ORGANISM CONV = .990 <0> <0> / EXT-REACNO = 1 KEY-SSID = CISOLID KEY-CID = C5SOLID CONV = .990 <0> <0> / EXT-REACNO = 4 KEY-SSID = CISOLID KEY-CID = C6SOLID CONV = .990 <0> <0> / EXT-REACNO = 5 KEY-SSID = MIXED KEY-CID = NH4ACET CONV = .990 <0> <0> / EXT-REACNO = 7 KEY-SSID = MIXED KEY-CID = CH4 CONV = .990 <0> <0> / EXT-REACNO = 45 KEY-SSID = MIXED KEY-CID = LGNSOL CONV = .990 <0> <0> \ ? BLOCK DUPL CHCWDUP ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";-------------------------------------------------------------" "; TURBOGENERATOR BLOCKS - AREA 8100" ";-------------------------------------------------------------" ";" ";------------------------------------------------------------" "; UTILITY BLOCKS - AREA 10000" ";------------------------------------------------------------" ";" ) \ \ DESCRIPTION DESCRIPTION = "DUPLICATES QH914 FOR CHW AND CW CAPITAL & OP COSTING" \ ? BLOCK MIXER CHCWMIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "SSCF & SEED CHW/CW DEMAND MIXER" \ ? BLOCK MIXER HEATCHW- ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "CHILLED WATER HEAT DEMAND MIXER" \ ? BLOCK MIXER SSCFCW ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "SSCF COOLING WATER DEMAND MIXER" \ ? BLOCK MIXER HEATCW-S ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "COOLING WATER HEAT DEMAND MIXER" \ ? BLOCK MIXER QCWMIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "CW CAPITAL HEAT DEMAND MIXER" \ ? BLOCK MIXER QCHWMIX ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "CHILLED WATER CAPITAL HEAT DEMAND MIXER" \ ? BLOCK FSPLIT ASPLT ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "FERMENTATION AIR SPLITTER" \ \ PARAM SID = 413 FRAC = .90 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? BLOCK MIXER CIPCS ? ; SET1 ; \ COMMENTS COMMENTS = ( "; Controlled by fortran AIRREQ" ";" ) \ \ DESCRIPTION DESCRIPTION = "CIP/CS SYSTEM TANKS AND PUMPS" \ ? BLOCK MIXER T914 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "DUMMY BLOCK TO CALCULATE TOTAL WATER DEMAND" \ ? BLOCK HEATER H910 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "WATER STERILIZER" \ \ PARAM TEMP = 121.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK HEATER H914 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "WELL WATER COOLER FOR SSCF BROTH" \ \ PARAM TEMP = 26.0 <22> <4> PRES = 0.0 <20> <3> \ ? BLOCK COMPR ACOMP ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "AIR COMPRESSOR FOR FERMENTATIONS" \ \ PARAM TYPE = ISENTROPIC PRES = 3.0 <20> <3> \ ? BLOCK HEATER AFLSH ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "PRESSURE REDUCER FOR FERMENTATION AIR" \ \ PARAM TEMP = 40.0 <22> <4> PRES = 1.0 <20> <3> \ ? BLOCK FSPLIT QH14BSP ? ; SET1 ; \ DESCRIPTION DESCRIPTION = "SETS FRACTION OF YEAR THAT CHW IS REQ. FOR SSCF COOLING" \ \ PARAM SID = QH14BCHW FRAC = 1.0000E-08 <0> <0> \ \ COMMENTS COMMENTS = ( ";" ) \ ? BLOCK MIXER SSCFSDCW ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "SSCF SEED TRAIN HEAT MIXER" \ ? BLOCK MIXER QHXLOW ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "HEAT TOTALIZER FOR 65 PSIA HX STEAM DEMANDS" \ ? BLOCK MIXER QHXMED ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "HEAT TOTALIZER FOR 165 PSIA HX STEAM DEMANDS" \ ? BLOCK MIXER QSTMVLO ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "HEAT TOTALIZER FOR 25 PSIA STEAM DEMANDS" \ ? BLOCK MIXER CWMAKUP ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ DESCRIPTION DESCRIPTION = "DUMMY BLOCK TO GET CWMAKEUP AND CW CHEMS OUT" \ ? CONV-OPTIONS ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ SECANT BRACKET = YES \ \ WEGSTEIN WEG-MAXIT = 100 WEG-QMAX = .50 <0> <0> \ ? DESIGN-SPEC ACIDCONC ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";-----------------------------------------------------------------------" "; DESIGN SPECIFICATIONS" "; PRETREATMENT DESIGN-SPECS" ";------------------------------------------------------------------------" ";" ";F COMMON /RXCON/ SETACD" ";CONTROLS THE ACID CONCENTRATION OF STREAM 217" ) \ \ 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 \ \ SPEC EXPR1 = "ACDCNC" EXPR2 = "0.011" \ \ TOL-SPEC TOL = "0.00001" \ \ VARY 1 VARY-VARTYPE = STREAM-VAR VARYSTREAM = 212 VARYSUBS = MIXED VARYVARIABLE = MASS-FLOW \ \ LIMITS LOWER = "100" UPPER = "10000" \ \ FORTRAN FORTRAN-EXEC = ( "F ACDCNC = ACIDFL/(WATFLW+ACIDFL)" ) \ ? DESIGN-SPEC LPSTMFLO ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";CONTROLS THE AMOUNT OF LP STEAM TO PRETREATMENT TO" ";ACHIEVE 100 C." ) \ \ DEFINE FVN = THTR FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QM202LO \ \ SPEC EXPR1 = "THTR" EXPR2 = "0" \ \ TOL-SPEC TOL = "10.0" \ \ VARY 1 VARY-VARTYPE = STREAM-VAR VARYSTREAM = 215 VARYSUBS = MIXED VARYVARIABLE = MASS-FLOW \ \ LIMITS LOWER = "100" UPPER = "500000" \ ? DESIGN-SPEC REACHEAT ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";CALCULATES THE AMOUNT OF HP STEAM REQUIRED TO OBTAIN" ";THE CORRECT RXN TEMPERATURE IN PRETREATMENT." ) \ \ DEFINE FVN = QRXNXS FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QM202HI \ \ SPEC EXPR1 = "QRXNXS" EXPR2 = "0" \ \ TOL-SPEC TOL = "5" \ \ VARY 1 VARY-VARTYPE = STREAM-VAR VARYSTREAM = 216 VARYSUBS = MIXED VARYVARIABLE = MASS-FLOW \ \ LIMITS LOWER = "200" UPPER = "100000" \ ? DESIGN-SPEC CT-S205A ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; The spec of 0.548 is from Pneumapress Test #9" "; under the Harris 2000 subcontract" ) \ \ 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 1 VARY-VARTYPE = BLOCK-VAR VARYBLOCK = S205A VARYSENTENCE = "FLOW/FRAC" VARYVARIABLE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 225 \ \ LIMITS LOWER = "0.01" UPPER = "1.0" \ ? DESIGN-SPEC CT-S205B ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; The spec of 0.548 is from Pneumapress Test #9" "; under the Harris 2000 subcontract" ) \ \ 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 1 VARY-VARTYPE = BLOCK-VAR VARYBLOCK = S205B VARYSENTENCE = "FLOW/FRAC" VARYVARIABLE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 256 VARYID3 = H2O \ \ LIMITS LOWER = "0.70" UPPER = "0.999" \ ? DESIGN-SPEC CT-S222 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ 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 1 VARY-VARTYPE = BLOCK-VAR VARYBLOCK = S222 VARYSENTENCE = "FLOW/FRAC" VARYVARIABLE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 229 \ \ LIMITS LOWER = "0.0" UPPER = "1.0" \ ? DESIGN-SPEC SCRBFLOW ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";---------------------------------------------------------------" "; SACCHARIFICATION AND FERMENTATION DESIGN-SPECS" ";---------------------------------------------------------------" ";---------------------------------------------------------------" "; 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" ) \ \ 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 1 VARY-VARTYPE = STREAM-VAR VARYSTREAM = 524 VARYSUBS = MIXED VARYVARIABLE = MASS-FLOW \ \ LIMITS LOWER = "5000" UPPER = "40000" \ ? DESIGN-SPEC H201TEMP ? ; SET1 ; \ 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." ) \ \ 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 1 VARY-VARTYPE = BLOCK-VAR VARYBLOCK = QH201SPT VARYSENTENCE = "FLOW/FRAC" VARYVARIABLE = "FLOW/FRAC" VARYID1 = QH201 \ \ LIMITS LOWER = "0.5" UPPER = "1.0" \ ? SETUP UNITS-SET SET5 ? \ 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) \ ? DESIGN-SPEC EVAPCONC ? ; SET5 ; \ COMMENTS COMMENTS = ( ";" "; SETS FLOW OF QE501A to set moisture concentration in 531" ) \ \ 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 1 VARY-VARTYPE = HEAT-DUTY VARYSTREAM = QE501A \ \ LIMITS LOWER = "0.0" UPPER = "50.0" \ ? DESIGN-SPEC MS-BTM ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; Specification of 0.005 mass fraction H2O in product ethanol" ) \ \ 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 1 VARY-VARTYPE = BLOCK-VAR VARYBLOCK = T507-8 VARYSENTENCE = "FLOW/FRAC" VARYVARIABLE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 514 VARYID3 = H2O \ \ LIMITS LOWER = "0.001" UPPER = "0.3" \ ? DESIGN-SPEC MS-OVHD ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; Specification of 0.7 mass frac ethanol in recycle to Rectification" ) \ \ 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 1 VARY-VARTYPE = BLOCK-VAR VARYBLOCK = T507-8 VARYSENTENCE = "FLOW/FRAC" VARYVARIABLE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 515A VARYID3 = ETHANOL \ \ LIMITS LOWER = "0.05" UPPER = "0.5" \ ? DESIGN-SPEC D502BTMS ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; Adjust mole-frac specification in D502 SEP2 to meet a specified" "; MASS-FRAC" ) \ \ 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 1 VARY-VARTYPE = BLOCK-VAR VARYBLOCK = D502 VARYSENTENCE = "FLOW/FRAC" VARYVARIABLE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 516 VARYID3 = ETHANOL \ \ LIMITS LOWER = ".0001" UPPER = ".1" \ ? DESIGN-SPEC D502OVHD ? ; SET1 ; \ COMMENTS COMMENTS = ( "; Adjust mole-frac specification in D502 SEP2 to meet a specified" "; MASS-FRAC" ) \ \ 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 1 VARY-VARTYPE = BLOCK-VAR VARYBLOCK = D502 VARYSENTENCE = "FLOW/FRAC" VARYVARIABLE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 511 VARYID3 = ETHANOL \ \ LIMITS LOWER = ".75" UPPER = ".999" \ ? DESIGN-SPEC CFUGE3S ? ; SET1 ; \ 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" ";" ) \ \ 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 \ \ SPEC EXPR1 = "RATIO" EXPR2 = "0.45" \ \ TOL-SPEC TOL = "0.01" \ \ VARY 1 VARY-VARTYPE = BLOCK-VAR VARYBLOCK = S505 VARYSENTENCE = "FLOW/FRAC" VARYVARIABLE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 571B VARYID3 = H2O \ \ LIMITS LOWER = "0.000001" UPPER = "0.40" \ \ FORTRAN FORTRAN-EXEC = ( "F RATIO = FH2O / (SOLIDS + TMIXED)" "F WRITE(NHSTRY,101)RATIO" "F 101 FORMAT(' CFUGE 3 DESIGN SPEC',/,' FRACTION MOISTURE',G12.5)" ) \ ? CALCULATOR MW ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";---------------------------------------------------------------" "; DESIGN SPECS" "; DIGESTER (AREA 6000)" ";---------------------------------------------------------------" ";" ";----------------------------------------------------------------" "; BOILER DESIGN-SPECS" ";---------------------------------------------------------------" ";" ";---------------------------------------------------------------------" "; STEAM CYCLE DESIGN-SPECS" ";--------------------------------------------------------------------" ";" ";----------------------------------------------------------------" "; UTILITY DESIGN-SPECS" ";-----------------------------------------------------------------" ";" ";-------------------------------------------------------" "; *FORTRAN BLOCKS*" "; Common Block Holder" ";-------------------------------------------------------" ) \ \ DEFINE FVN = SOLMW FVN-VARTYPE = UNARY-PARAM FVN-VARIABLE = MW FVN-ID1 = SOLSLDS FVN-ID2 = 1 \ \ EXECUTE WHEN = AFTER ANY-ID = SETVAR \ \ FORTRAN FORTRAN-EXEC = ( "F WRITE (NHSTRY,*) 'FEEDPROP MOLECULAR WEIGHT:'" "F WRITE(NHSTRY,*)'SOLSLD MW = ', SOLMW" ) \ ? CALCULATOR SETVAR ? ; SET1 ; \ COMMENTS COMMENTS = ( ";F COMMON /CLSSET/ CLYLD, CLPROD, CLVES, CLVOL, CLWV" "; Inputs are entered here to be used in common blocks throughout" "; the model" ";" ";" ";" ";" ";" ) \ \ 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 = 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 \ \ WRITE-VARS WRITE-VAR = (SSFDAY SSFVOL SSFWV SACDAY SACVOL SACWV CLYLD CLPROD CLVOL CLWV) \ \ FORTRAN FORTRAN-EXEC = ( "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 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" ) \ ? CALCULATOR POLY1 ? ; SET1 ; \ COMMENTS COMMENTS = ( "; EXECUTE FIRST" ";" ";----------------------------------------------------" "; FEED HANDLING FORTRAN BLOCKS - AREA 1000" ";----------------------------------------------------" ";" ";" ) \ \ 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 \ \ READ-VARS READ-VAR = (FEEDMX FEEDSL) \ \ WRITE-VARS WRITE-VAR = (POLY) \ \ 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" ) \ ? CALCULATOR S205WASH ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";----------------------------------------------------" "; PRETREATMENT FORTRAN BLOCKS - AREA 2000" ";----------------------------------------------------" ";" ";" "; calculation of air requirement" "; airflw = required flow in CFM" "; airp = pressure of airflw (psig)" "; airt = temperature of airflw (C)" "; conversion of AIRRQ to kmol/hr" ) \ \ 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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = 252 \ \ DEFINE FVN = AIRRQ FVN-VARTYPE = STREAM-VAR FVN-STREAM = 257 FVN-SUBS = MIXED FVN-VARIABLE = MOLE-FLOW \ \ READ-VARS READ-VAR = (SOL220 WAT220) \ \ WRITE-VARS WRITE-VAR = (WSH252 AIRRQ) \ \ 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" ) \ ? CALCULATOR S205SOL ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; 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" "; EXECUTE BEFORE BLOCK S205B" ";" ) \ \ DEFINE FVN = FS2 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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 = FS11 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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 = FS12 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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 = FS13 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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 = FS14 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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 = FS18 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = C6SUGAR \ \ DEFINE FVN = GAL220 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = GAL221 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = GAL254 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = GAL252 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = FS15 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = C5SUGAR \ \ DEFINE FVN = ARA220 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = ARA221 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = ARA254 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = ARA252 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = FS16 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = NH4SO4 \ \ DEFINE FVN = XNS220 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = NH4SO4 \ \ DEFINE FVN = XNS221 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = NH4SO4 \ \ DEFINE FVN = XNS254 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = NH4SO4 \ \ DEFINE FVN = XNS252 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = NH4SO4 \ \ DEFINE FVN = FS17 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 256 FVN-ID3 = NH4ACET \ \ DEFINE FVN = XNA220 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 220 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = XNA221 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 221 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = XNA254 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 254 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = XNA252 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 252 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = FS19 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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 = FS20 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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 = FS21 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S205B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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 \ \ 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) \ \ 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 (XNO254.GT.0) THEN" "F FS10 = ((RECOV * XNO220) - XNO221 + XNO252) / XNO254" "F ELSE" "F FS10 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'NO2 RECOVERY IN S205B= ',FS10" "F IF (XNH254.GT.0) THEN" "F FS11 = ((RECOV * XNH220) - XNH221 + XNH252) / XNH254" "F ELSE" "F FS11 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'NH3 RECOVERY IN S205B= ',FS11" "F IF (SOL254.GT.0) THEN" "F FS12 = ((RECOV * SOL220) - SOL221 + SOL252) / SOL254" "F ELSE" "F FS12 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'SOLSLDS RECOVERY IN S205B= ',FS12" "F IF (GLU254.GT.0) THEN" "F FS13 = ((RECOV * GLU220) - GLU221 + GLU252) / GLU254" "F ELSE" "F FS13 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'GLUCOSE RECOVERY IN S205B= ',FS13" "F IF (XYL254.GT.0) THEN" "F FS14 = ((RECOV * XYL220) - XYL221 + XYL252) / XYL254" "F ELSE" "F FS14 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'XYLOSE RECOVERY IN S205B= ',FS14" "F IF (GAL254.GT.0) THEN" "F FS18 = ((RECOV * GAL220) - GAL221 + GAL252) / GAL254" "F ELSE" "F FS18 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'C6SUGAR RECOVERY IN S205B= ',FS18" "F IF (ARA254.GT.0) THEN" "F FS15 = ((RECOV * ARA220) - ARA221 + ARA252) / ARA254" "F ELSE" "F FS15 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'C5SUGAR RECOVERY IN S205B= ',FS15" "F IF (XNS254.GT.0) THEN" "F FS16 = ((RECOV * XNS220) - XNS221 + XNS252) / XNS254" "F ELSE" "F FS16 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'NH4SO4 RECOVERY IN S205B= ',FS16" "F IF (XNA254.GT.0) THEN" "F FS17 = ((RECOV * XNA220) - XNA221 + XNA252) / XNA254" "F ELSE" "F FS17 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'NH4ACET RECOVERY IN S205B= ',FS17" "F IF (AAC254.GT.0) THEN" "F FS19 = ((RECOV * AAC220) - AAC221 + AAC252) / AAC254" "F ELSE" "F FS19 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'AACID RECOVERY IN S205B= ',FS19" "F IF (LAC254.GT.0) THEN" "F FS20 = ((RECOV * LAC220) - LAC221 + LAC252) / LAC254" "F ELSE" "F FS20 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'LACID RECOVERY IN S205B= ',FS20" "F IF (SLG254.GT.0) THEN" "F FS21 = ((RECOV * SLG220) - SLG221 + SLG252) / SLG254" "F ELSE" "F FS21 = 0.0" "F ENDIF" "F WRITE(NHSTRY,*)'LGNSOL RECOVERY IN S205B= ',FS21" "F FACTOR = 0.009/3" ) \ ? CALCULATOR OLIME ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; WM(Ca(OH)*2)=74.09" "; 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 2 due to increased flow with S/L was before IX" ) \ \ 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 \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = T209 \ \ FORTRAN FORTRAN-EXEC = ( "F WM227=74.09" "F FACTOR = 0.01/3" "F FL227 = FACTOR * FL240 + FA240 * WM227" ) \ ? CALCULATOR REACID ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ 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 \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = T224 \ \ FORTRAN FORTRAN-EXEC = ( "F FL233=CA228-HS228" "F IF (FL233.LT.0) FL233=0" ) \ ? CALCULATOR FERMCSL ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";----------------------------------------------------------------------" "; SSCF FORTRAN BLOCKS - AREA 3000" ";----------------------------------------------------------------------" ";" "; 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)" ) \ \ 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 = H2O \ \ DEFINE FVN = FL311A FVN-VARTYPE = MASS-FLOW FVN-STREAM = 311A FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = BLOCK BLK-ID = T310 \ \ FORTRAN FORTRAN-EXEC = ( "F CSLSD=0.005" "F CSLPRD=0.0025" "F FL310A=CSLSD*(FL303A+FS303A)" "F FL311A=CSLPRD*(FL304A+FS304A)" ) \ ? CALCULATOR FERMDAP ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; 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)" ";" ) \ \ 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 \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = CALCULAT BLK-ID = FERMCSL \ \ 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'" ) \ ? CALCULATOR ENZ2 ? ; SET1 ; \ 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 \ \ READ-VARS READ-VAR = (CL301A) \ \ WRITE-VARS WRITE-VAR = (XM312 CI312) \ \ 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, STREAM 301A" ) \ \ 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" ) \ ? CALCULATOR ENZYME ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";-------------------------------------------------------" "; CELLULASE FORTRAN BLOCKS - AREA 4000" ";------------------------------------------------------" ";" ";F COMMON /CLSSET/ CLYLD, CLPROD, CLVES, CLVOL, CLWV" ";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" ";" ) \ \ 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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = 401 \ \ DEFINE FVN = CSDSPT FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = CLFDSPLT FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = 421 \ \ DEFINE FVN = CLYLD FVN-VARTYPE = PARAMETER FVN-PARAMNO = 41 \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = BTMSSPLT \ \ FORTRAN FORTRAN-EXEC = ( "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" "C ENZYME LOADING ENZYL (FPU/G CELLULOSE IN PRIMARY FEED) TO SSCF" "C" "F ENZYL=0.00001" "C" "C CELLULASE DEMAND BY SACCHARIFICATION" "C" "F EZDMD = CELL1 * ENZYL" "C" "C CELLULASE DEMAND BY SSCF SEED" "C" "F EZDMDS = 0.0" "C" "C SUBSTRATE NEEDED BY CELLULASE REACTOR TO PRODUCE SSCF 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 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)" ) \ ? CALCULATOR NUTRA ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ 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 = C6SUGA FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 412A FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = C6SUGB FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 433 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ 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 = C5SUGA FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 412A FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = C5SUGB FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 433 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ 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 = C6SOLA FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 412A FVN-SUBS = CISOLID FVN-COMPONEN = C6SOLID \ \ DEFINE FVN = C6SOLB FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 433 FVN-SUBS = CISOLID FVN-COMPONEN = C6SOLID \ \ 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 \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = F400 \ \ FORTRAN FORTRAN-EXEC = ( "F GLUCOS = GLUCA + GLUCB" "F C6SUGR = S6SUGA + S6SUGB" "F XYLOSE = XYLOA + XYLOB" "F C5SUGR = C5SUGA + C5SUGB" "F CELLOS = CELLA + CELLB" "F C6SOLD = C6SOLA + S6SOLB" "F ANH3 = (((GLUCOS + C6SUGR) * (.4684/1.))" "F 1 + ((XYLOSE + C5SUGR) * (.6096/1.))" "F 2 + ((CELLOS + C6SOLD) * (.5416/1.))) - XNH3 - YNH3" ) \ ? CALCULATOR NUTRB ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";" ";" ) \ \ DEFINE FVN = GLUC FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 431 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = C6SUG FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 431 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ 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 = C5SUG FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 431 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = CELL FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 431 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = C6SOL FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 431 FVN-SUBS = CISOLID FVN-COMPONEN = C6SOLID \ \ DEFINE FVN = BNH3 FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 434 FVN-SUBS = MIXED FVN-COMPONEN = NH3 \ \ FLASH-SPECS FLASH-STREAM = 434 KODE = TP TEMP = 28.0 <22> <4> PRES = 1.0 <20> <3> \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = F401-4 \ \ FORTRAN FORTRAN-EXEC = ( "F BNH3 = (((GLUC+C6SUG) * (.4684/1.))" "F 1 + ((XYLO+S5SUG) * (.6096/1.))" "F 2 + ((CELL+C6SOL) * (.5416/1.))) * 2." ) \ ? CALCULATOR FRWD501 ? ; ENG ; \ COMMENTS COMMENTS = ( ";" ";--------------------------------------------------------" "; DISTILLATION FORTRAN BLOCKS - AREA 5000" ";-------------------------------------------------------" ";" "; Feed forward control for 501 column. Estimates the distillate" "; flow and specification bounds for 501" ";" ) \ \ DEFINE FVN = D501D FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = D501 FVN-SENTENCE = COL-SPECS FVN-VARIABLE = MASS-D \ \ 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-SENTENCE = VARY FVN-VARIABLE = LB FVN-ID1 = 3 \ \ DEFINE FVN = D501DH FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = D501 FVN-SENTENCE = VARY FVN-VARIABLE = UB FVN-ID1 = 3 \ \ DEFINE FVN = D501V FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = D501 FVN-SENTENCE = PRODUCTS FVN-VARIABLE = MASS-FLOW 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-SENTENCE = VARY FVN-VARIABLE = LB FVN-ID1 = 2 \ \ DEFINE FVN = D501VU FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = D501 FVN-SENTENCE = VARY FVN-VARIABLE = UB FVN-ID1 = 2 \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = D501 \ \ 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)" ) \ ? CALCULATOR D502QCR ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ 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 \ \ READ-VARS READ-VAR = (FD502) \ \ WRITE-VARS WRITE-VAR = (Q502R Q502C) \ \ 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" ) \ ? CALCULATOR CFUGESLD ? ; SET1 ; \ 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." ";" ";" ) \ \ DEFINE FVN = F1 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = H2O \ \ DEFINE FVN = F2 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = ETHANOL \ \ DEFINE FVN = F3 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = FURFURAL \ \ DEFINE FVN = F4 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = HMF \ \ DEFINE FVN = F5 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = H2SO4 \ \ DEFINE FVN = F6 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = N2 \ \ DEFINE FVN = F7 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CO2 \ \ DEFINE FVN = F8 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = O2 \ \ DEFINE FVN = F9 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = CH4 \ \ DEFINE FVN = F10 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = NH3 \ \ DEFINE FVN = F11 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = SOLSLDS \ \ DEFINE FVN = F12 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = GLUCOSE \ \ DEFINE FVN = F15 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = NO2 \ \ DEFINE FVN = F16 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = C5SUGAR \ \ DEFINE FVN = F17 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = AACID \ \ DEFINE FVN = F18 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = LACID \ \ DEFINE FVN = F19 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = LGNSOL \ \ DEFINE FVN = F20 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = NH4SO4 \ \ DEFINE FVN = F21 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = S505 FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 571B FVN-ID3 = NH4ACET \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = S505 \ \ FORTRAN FORTRAN-EXEC = ( "F F2=F1" "F F3=F1" "F F4=F1" "F F5=F1" "F F6=F1" "F F7=F1" "F F8=F1" "F F9=F1" "F F10=F1" "F F11=F1" "F F12=F1" "F F15=F1" "F F16=F1" "F F17=F1" "F F18=F1" "F F19=F1" "F F20=F1" "F F21=F1" ) \ ? CALCULATOR RECYCLE ? ; SET1 ; \ COMMENTS COMMENTS = ( ";------------------------------------------------------" "; DIGESTOR FORTRAN BLOCKS - AREA 6000" ";------------------------------------------------------" ";" "; 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 SSCF Production)" ";" ";" "; DEFINE THE COMPONENTS OF STREAM 311 (DAP to SSCF 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 STREAM 311A (CSL to SSCF Production)" ";" "; DEFINE THE COMPONENTS OF STREAM 312 (Enzyme to SSCF Production)" ";" ";" "; DEFINE THE COMPONENTS OF STREAM 303 (Feed to SSCF Seed)" ";" ";" "; DEFINE THE COMPONENTS OF STREAM 304 (SSCF 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" ) \ \ 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 = RC5S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = RC6S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = RLGS FVN-VARTYPE = MASS-FLOW FVN-STREAM = 219 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ 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 = HC5S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = HC6S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = HLGS FVN-VARTYPE = MASS-FLOW FVN-STREAM = 232 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ 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 = CFC5S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = CFC6S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = CFLGS FVN-VARTYPE = MASS-FLOW FVN-STREAM = 401 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ 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 = CPC5S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = CPC6S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = CPLGS FVN-VARTYPE = MASS-FLOW FVN-STREAM = 422 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ 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 = H2O \ \ 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 = EZC5S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = EZC6S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = EZLGS FVN-VARTYPE = MASS-FLOW FVN-STREAM = 312 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ 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 = SFC5S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = SFC6S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = SFLGS FVN-VARTYPE = MASS-FLOW FVN-STREAM = 303 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ 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 = SPC5S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = SPC6S FVN-VARTYPE = MASS-FLOW FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = SPLGS FVN-VARTYPE = MASS-FLOW FVN-STREAM = 304 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ 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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = 219 \ \ DEFINE FVN = F3 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = RWSPLT FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "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 \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = FWMIX \ \ 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 TTL219: TOTAL FLOW IN STREAM 219" "C CNC219: TOTAL SOLIDS CONC IN STREAM 219" "C OTHSLD: TOTAL OTHER SOLIDS" "C OTHTTL: TOTAL OTHER FLOW" "C" "C CONC2 IS THE DESIRED SSCF 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 SLD232 = HS1 + HGLU + HXYE + HSSL + HC5S + HC6S + HLGS" "F SLD219 = RI2 + RGLU + RXYE + RSSL + RC5S + RC6S + RLGS" "F SLD401 = CFS1 + CFGLU + CFXYE + CFSSL + CFC5S + CFC6S + CFLGS" "F SLD422 = CPS1 + CPGLU + CPXYE + CPSSL + CPC5S + CPC6S + CPLGS" "F SLD312 = EZS1 + EZGLU + EZXYE + EZSSL + EZC5S + EZC6S + EZLGS" "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)" "F AV2 = CAL219 - RI2" "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 + SLD311 + SLD31A - SLD303" "F 1 + SLD304) / (TTL232 - TTL401 + TTL422 + TTL311 + TTL31A" "F 2 - TTL303 + TTL304)" "F CNC2B = (RI2 - CFS1 + CPS1 + DPS1 + CLS1 - SFS1 + SPS1)" "F 1 / (TTL232 - TTL401 + TTL422 + TTL311 + TTL31A - TTL303" "F 2 + TTL304)" "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 6 ' OTHER CONCENTRATIONS',/," "F 5 ' 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 5 ' CONC2: ',G12.5,/," "F 5 ' 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" ) \ ? CALCULATOR RECCOND ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";" "; DEFINE VARIABLES FOR RECYCLE WATER STREAM #1. THIS STREAM" "; CONTROLS THE SOLIDS CONCENTRATION IN THE IMPREGNATOR." ";" ) \ \ 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 = 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 = AV1 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = E501SPT FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = 211 \ \ DEFINE FVN = DRTSEP FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = C103B FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = 104B \ \ DEFINE FVN = EVPSEP FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = M104LOSS FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = 103 \ \ DEFINE FVN = WAT102 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = E501SPT FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = 102 \ \ READ-VARS READ-VAR = (CI1 STV1 STV2 ACV1 FDV2 FDS2 SSL2 FDV1 SSL1) \ \ WRITE-VARS WRITE-VAR = (DRTSEP EVPSEP WAT102 AV1) \ \ 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) / 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)" "C" "C AV1 RECYCLE WATER FLOW (STREAM 211)" "C" "F AV1 = CV1 - STV1 - STV2 - ACV1 - ( FDV1 - SSL1)" "C" "F CNC1A = CI1 / (CV1 + CI1 + STV1)" "F CNC1 = CI1 / (CV1 + CI1 + STV1 + STV2)" ) \ ? CALCULATOR WWT ? ; SET1 ; \ COMMENTS COMMENTS = ( "; EXECUTE BEFORE E501MIX" ";" ";" ";F WWTNUT2 = WWTFAC*COD2" ) \ \ DEFINE FVN = WWTCST FVN-VARTYPE = PARAMETER FVN-PARAMNO = 2 \ \ DEFINE FVN = WMWWT FVN-VARTYPE = PARAMETER FVN-PARAMNO = 3 \ \ DEFINE FVN = GLUC FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = XYLO FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = SOLS FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = C5SUG FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = C6SUG FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = ETOH FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FURF FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = XHMF FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = XLACI FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = AACI FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = XNNH4 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = SLLGN FVN-VARTYPE = MASS-FLOW FVN-STREAM = 612 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = TOTWWT FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 612 \ \ DEFINE FVN = WWTQ FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QH602 \ \ DEFINE FVN = WWTNT1 FVN-VARTYPE = STREAM-VAR FVN-STREAM = 630 FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ DEFINE FVN = WWTNT2 FVN-VARTYPE = STREAM-VAR FVN-STREAM = 631 FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ DEFINE FVN = CH4 FVN-VARTYPE = STREAM-VAR FVN-STREAM = 615 FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ READ-VARS READ-VAR = (GLUC XYLO SOLS C5SUG C6SUG ETOH FURF XHMF XLACI AACI XNNH4 SLLGN TOTWWT) \ \ WRITE-VARS WRITE-VAR = (WWTNT1 WWTNT2 WMWWT WWTCST CH4) \ \ DECLARE FORTRAN-DEC = ( "C CALCULATES THE INCOMMING COD, WWT CAPITAL, QH602, POWER," "C NUTRIENTS, CH4 PROD" "F COMMON/ WWLOAD/ CODTOT, BODTOT, CODDAY, BODDAY" ) \ \ 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" "C SOLUBLE C-CONTAINING COMPOUNDS" "F CGLUC = 1.07" "F CXYLO = 1.07" "F CSOLS = 0.71" "F CETOH = 2.09" "F CC5SG = 1.07" "F CC6SG = 1.07" "F CFURF = 1.67" "F CHMF = 1.52" "F CLACI = 1.07" "F CAACI = 1.07" "F CNNH4 = 1.1557" "F CSLGN = 1.6" "C" "C" "C CALCULATE HOURLY COD LOADINGS (KG/HR)" "C" "F CODTOT = GLUC*CGLUC + XYLO*CXYLO + SOLS*CSOLS +" "F 1 C5SUG*CC5SG + C6SUG*CC6SG +" "F 2 ETOH*CETOH + FURF*CFURF +" "F 3 XHMF*CHMF + XACI*CLACI + AACI*CAACI +" "F 4 CNNH4*XNNH4 + SLLGN*CSLGN" "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" "C CALCULATE CAPITAL COST OF WWT USING J. SHEEHAN FORMULA (10/99)" "C BASED ON GPM OF STREAM 612 AND CODTOT" "C THIS FORMULA IS GOOD FOR THE FOLLOWING RANGES:" "C FLOW: 500 TO 1500 GPM" "C COD: 2000 TO 10000 KG/HR" "C" "C" "C CALCULATE WWT FLOW IN GALLONS PER MINUTE" "F TOTVOL = TOTWWT * 2.205 / (8.3 * 60)" "C" "C" "C CALCULATE WWT CAPITAL IN MM$" "C ACTUAL FLOW OF 612 IN I0302B IS ABOUT 400 GPM, SO USING IT AND CODTOT" "C KNI ADJUSTED THE INTERCEPT VALUE." "C CODTOT = 1357" "C TOTVOL = 393" "C" "F WWTCST = (1810.550 * TOTVOL) + (761.156 * CODTOT) + 1214678.0" "C" "C CALCULATE WWT POWER" "C RATIO WWT POWER TO CAPITAL COST USING POWER (-WS600), COST IN I0302B" "C" "C" "F WMWWT = 279 * (WWTCST / (3082344 - 123231))" "C" "C CALCULATE QH602 HEAT LOAD WITH STREAM 612 FLOW RATE RATIO" "C ORIGINAL DUTY AND FLOW FROM I0302B, DUTY IN CAL/S, FLOW IN KG/HR" "C" "C" "F WWTQ = 637944. * (TOTWWT / 89073.)" "C" "C WRITE ANSWERS TO THE HISTORY FILE" "C" "F WRITE(NHSTRY,*)'TOTWWT, TOTVOL, CODTOT=', TOTWWT, TOTVOL, CODTOT" "C" "C CALCULATE WWT CHEMICAL USAGE BASED ON CODTOT" "C" "F WWTFAC = 3.675E-2" "C" "C THE AMOUNT OF PHOSPHORIC ACID, UREA, MICRONUTRIENTS AND CAUSTIC" "C" "F WWTNT1 = WWTFAC*CODTOT" "C" "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" "C RATIO AEROBIC NUTRIENT FROM (COD2/CODTOT) IN I0302B, SINCE" "C COD OUT OF ANAEROBIC IS NOT CALC'D HERE." "F WWTNT2 = WWTFAC*CODTOT*.0736" "C" "C CALCULATE METHANE PRODUCED FROM CODTOT" "C ASSUME 90% COD CONVERSION" "C USE USRAN4 WWT ASSUMPTIONS OF 0.2289 KG CH4/KG COD AT 35 C" "C CH4MAX*RHO*C4MW*CH4YLD(350*4.08E-5*16*1)" "C" "C" "F CH4 = CODTOT * 0.9 * 0.2289" "C" ) \ ? CALCULATOR CSL-ENZY ? ; SET1 ; \ 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" ) \ \ 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 = H2O \ \ DEFINE FVN = FCLS FVN-VARTYPE = MASS-FLOW FVN-STREAM = 311A FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ 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 \ \ READ-VARS READ-VAR = (CF CFS CND SD SND FSCLS FCLS CFD CFSD CODD CNDD) \ \ WRITE-VARS WRITE-VAR = (CLSP CLSS CLNUTR TTLCSL CO) \ \ 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" ) \ ? CALCULATOR DENATURE ? ; SET1 ; \ COMMENTS COMMENTS = ( "; EXECUTE BEFORE F400" ";THIS BLOCK CALCULATES THE AMOUNT OF DENATURANT REQUIRED." ";IT ALSO CALCULATES THE SIZE OF THE GASOLINE (DENATURANT)" ";TANK." "; INPUTS" "; Since gas was removed from the component, need to use true" "; gas density instead of stream 701 density, which is water," "; to get correct flow rate and storage equipment size." ";" "; OUTPUT" ";" ";SPECIFY THE DENATURANT ADDITION (PART DENAT / 100 PARTS ETHANOL FUEL)" ";4.75 PER MARK RUTH MEMO 3 NOVEMBER 1999" ";" ) \ \ 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 = GGAS FVN-VARTYPE = STREAM-VAR FVN-STREAM = 701 FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ READ-VARS READ-VAR = (PDENS PROD) \ \ WRITE-VARS WRITE-VAR = (GGAS) \ \ FORTRAN FORTRAN-EXEC = ( "F GDENS = 0.6875" "F DPERC = 4.75" "C" "C CALCULATE THE FLOWRATE OF DENATURANT INTO THE SYSTEM." "C" "F GGAS = DPERC / 100 * (PROD / PDENS) * GDENS" "C" ) \ ? CALCULATOR STORE ? ; SET1 ; \ 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" ";" ";F DNH3=0.00685" ";F 1 + DNH3*PRFLOW" ) \ \ 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 \ \ EXECUTE WHEN = AFTER BLOCK-TYPE = BLOCK BLK-ID = T507-8 \ \ FORTRAN FORTRAN-EXEC = ( "F TAFLOW = AFLOW1 + AFLOW2 + AFLOW3" "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 = AMFLW1 + 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" ) \ ? CALCULATOR BOILECON ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";-------------------------------------------------------------" "; BURNER FORTRAN BLOCKS - AREA 800" ";------------------------------------------------------------" ";" ";" "; DEFINE STM237 STREAM-VAR STREAM=237 SUBSTREAM=MIXED &" "; VARIABLE=MASS-FLOW" ";C Calculate BFW and IX feed water chemicals" "; DEFINE FLWIX3 STREAM-VAR STREAM=243 SUBSTREAM=MIXED VARIABLE=MASS-FLOW" ) \ \ DEFINE FVN = CAPCST FVN-VARTYPE = PARAMETER FVN-PARAMNO = 4 \ \ DEFINE FVN = WNET FVN-VARTYPE = PARAMETER FVN-PARAMNO = 8 \ \ DEFINE FVN = QBOIL FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QM803 \ \ DEFINE FVN = STM216 FVN-VARTYPE = STREAM-VAR FVN-STREAM = 216 FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ DEFINE FVN = STM215 FVN-VARTYPE = STREAM-VAR FVN-STREAM = 215 FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ DEFINE FVN = QMDMDH FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QRD502 \ \ DEFINE FVN = QLDMDH FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QHXLOW \ \ DEFINE FVN = QVLDMD FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QVLOW \ \ DEFINE FVN = QDUTY FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QM811 \ \ DEFINE FVN = WCFAN FVN-VARTYPE = WORK-POWER FVN-STREAM = WCOMBFAN \ \ DEFINE FVN = BLRMU FVN-VARTYPE = STREAM-VAR FVN-STREAM = 811 FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ DEFINE FVN = BLODWN FVN-VARTYPE = STREAM-VAR FVN-STREAM = 821 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 \ \ READ-VARS READ-VAR = (QBOIL STM216 STM215 QMDMDH QLDMDH QVLDMD FLXTRA WCFAN) \ \ WRITE-VARS WRITE-VAR = (CAPCST WNET QDUTY BFC BLRMU) \ \ FORTRAN FORTRAN-EXEC = ( "C" "C" "C INPUTS FROM ASPEN" "C QBOIL: HEAT FROM BOILER" "C STMXXX: HEAT REQUIRED BY PT STEAM INJ. IN PLANT, MED P, CAL/S" "C STMXXX: HEAT REQUIRED BY STEAM INJECTION IN PLANT, MED P, CAL/S" "C QMDMDH: HEAT REQUIRED BY STEAM HEAT EXCHANGERS IN PLANT, MED P, CAL/S" "C QLDMDH: HEAT REQUIRED BY STEAM HEAT EXCHANGERS IN PLANT, LOW P,CAL/S" "C QVLDMD: HEAT REQUIRED BY PLANT, VL P, CAL/S" "C WCFAN: INLET AIR COMPRESSOR WORK, KW" "C" "C USER PARAMETERS" "C RATIOS CALCULATED FROM RIGOROUS MODEL RESULTS" "C WHITRB: WORK FROM HI P TURBINE KW/KG/HR STEAM THROUGH TURBINE" "C WMTRB: WORK FROM MED P TURBINE KW/KG/HR STEAM THROUGH TURBINE" "C WLOTRB: WORK FROM LOW P TURBINE KW/KG/HR STEAM THROUGH TURBINE" "C WVLTRB: WORK FROM VL P TURBINE KW/KG/HR STEAM THROUGH TURBINE" "C WUSED: WORK USED IN BOILER AREA, KW/CAL/S" "C QSTMHI: RATIO OF STEAM/HEAT GENERATED AT HI P, KG/HR/CAL/S (812)" "C QSTM_M: RATIO OF STEAM/HEAT GENERATED AT MED P, KG/HR/CAL/S (814)" "C QSTMLO: RATIO OF STEAM/HEAT GENERATED AT LOW P, KG/HR/CAL/S (815)" "C QSTMVL: RATIO OF STEAM/HEAT GENERATED AT VL P, KG/HR/CAL/S (860)" "C QCOND: RATIO OF STEAM/HEAT GENERATED AT VACUUM, KG/HR/CAL/S (815E)" "C PMREC: MED P RECYCLE STEAM FRACTION OF BOILER STEAM" "C PLREC: LOW P RECYCLE STEAM FRACTION OF BOILER STEAM" "C BCOST: RATIO OF CAPITAL COST OF BOILER/QBOIL, $/CAL/S" "C" "C CALCULATED PARAMETERS" "C W_HIP: WORK GENERATED BY HI P TURBINE, KW" "C W_MEDP: WORK GENERATED BY MED P TURBINE, KW" "C W_LOP: WORK GENERATED IN LOW P TURBINE, KW" "C W_VLP: WORK GENERATED IN VL P TURBINE, KW" "C WINTNL: WORK USED INTERNALLY BY THE BOILER/BURNER, KW" "C WTOTAL: TOTAL POWER GENERATED, KW" "C PSTM_M: MED P PLANT STEAM DEMAND, KG" "C STM_M: STEAM TO MED P TURBINE, KG" "C PSTMLO: LOW P PLANT STEAM DEMAND, KG" "C STMLO: STEAM TO LOW P TURBINE, KG" "C PSTMVL: VL P PLANT STEAM DEMAND, KG" "C STMVL: STEAM TO VL P TURBINE, KG" "C" "C OUTPUTS TO ASPEN MODEL" "C QDUTY: CONDENSER DUTY, CAL/SEC (QM811)" "C CAPCST: CAPITAL COST OF BOILER, $" "C WNET: NET WORK PRODUCED (TOTAL - LOSS), KW" "C" "F WHITRB = 0.1205" "F WMTRB = 0.0529" "F WLOTRB = 0.0400" "F WVLTRB = 0.0949" "F WUSED = 2.87E-5" "F PMREC = 0.0770715" "F PLREC = 0.0781471" "F BCOST = 1.1371" "C" "F QSTMHI = 0.0054943" "F QSTM_M = -0.0070039" "F QSTMLO = -0.0070039" "F QSTMVL = 0.0068053" "F QCOND = 0.0072144" "C" "C" "F STMHI = QBOIL * QSTMHI" "C" "C CALCULATE THE POWER GENERATED AT HIGH PRESSURE" "C" "F WHIP = WHITRB * STMHI" "C" "C CALCULATE THE KG OF MED P STEAM TO PLANT" "C QMDMDH IS NEGATIVE" "C" "F PSTMM = STM216 + STM215 + (QSTM_M * QMDMDH)" "C" "C CALCULATE STEAM TO MED P TURBINE" "C" "F STMM = STMHI - PSTMM - PMREC * STMHI" "C" "C CALCULATE THE POWER GENERATED AT MEDIUM PRESSURE" "C" "F WMEDP = STMM * WMTRB" "C" "C CALCULATE THE KG OF LOW P STEAM TO PLANT" "C QLDMDH IS NEGATIVE" "C" "F PSTMLO = QSTMLO * QLDMDH" "C" "C CALCULATE THE STEAM TO LO P TURBINE" "C" "F STMLO = STMM - PSTMLO - PLREC * STMHI" "C" "C CALCULATE THE POWER GENERATED AT LOW PRESSURE" "C" "F WLOP = STMLO * WLOTRB" "C" "C CALCULATE THE KG OF VL P STEAM TO PLANT" "C" "F PSTMVL = QSTMVL * QVLDMD" "C" "C CALCULATE THE STEAM TO V-L PRESSURE TURBINE" "C" "F STMVL = STMLO - PSTMVL" "C" "C CALCULATE THE POWER GENERATED AT V-LOW PRESSURE" "C" "F WVLP = STMVL * WVLTRB" "C" "C CALCULATE THE POWER USED INTERALLY" "C" "F WINTNL = ( QBOIL * WUSED ) + WCFAN" "C" "C CALCULATE THE COOLING DUTY" "C" "F QDUTY = STMVL / QCOND" "C" "C CALCULATE THE TOTAL WORK FROM TURBINES" "C" "F WTOTAL = WHIP + WMEDP + WLOP + WVLP" "C" "C CALCULATE NET WORK OUT" "C" "F WNET = -WTOTAL * (1-.04) + WINTNL" "C" "C CALCULATE THE CAPITAL COST OF THE AREA" "C" "F CAPCST = QBOIL * BCOST" "C" "C" "C" "C CALCULATE BOILER BLOWDOWN AND MAKEUP FOR WATERDEM" "C AND CHEMICALS" "C" "C" "C RATIO BOILER BLOWDOWN BLODWN FROM I0302B.INP AND QBOIL" "C STREAM 821 IS 5722 KG/HR AND QBOILER IS 118 MKCAL/HR, OR 32,916,667 CAL/S" "C" "C" "F BLODWN = QBOIL * (5722.0 / 32.917E6)" "C" "F BLRMU = STM215 + STM216 + BLODWN" "C" "C" "F BFCREQ=7.E-6" "C BFCREQ IS THE BFW CHEMICAL REQ IN LB/LB BFW" "C REQUIREMENT FROM RADIAN REPORT. BACK-CALCULATED FROM CASES" "C" "C" "C CHECK TO SEE IF THERE IS MORE CLEAN RECYCLE WATER THAN 811 MAKEUP:" "F IF (BLRMU.GT.FLXTRA) THEN" "F BFC=BFCREQ*(BLRMU - FLXTRA)" "F ELSE" "F BFC=1.0" "F END IF" "C" "F WRITE(NHSTRY,101)QBOIL, QLDMDH, QVLDMD," "F 1 STMHI, PSTMM, STMM, PSTMLO, STMLO, PSTMVL, STMVL," "F 2 WHIP, WMEDP, WLOP, WVLP, WTOTAL," "F 3 WINTNL, WNET, QDUTY, CAPCST, BLODWN" "F 101 FORMAT(' QBOILER: ',G12.5,/," "F 3 ' Q LOW P HX PLANT DEMAND:',G12.5,/," "F 4 ' Q VL P PLANT DEMAND: ',G12.5,/," "F 5 ' HI P STEAM FLOW: ',G12.5,/," "F 6 ' MED P PLANT STEAM FLOW: ',G12.5,/," "F 7 ' MED P TURB STEAM FLOW: ',G12.5,/," "F 8 ' LOW P PLANT STEAM FLOW: ',G12.5,/," "F 9 ' LOW P TURB STEAM FLOW: ',G12.5,/," "F 1 ' VL P PLANT STEAM FLOW: ',G12.5,/," "F 2 ' VL P TURB STEAM FLOW: ',G12.5,/," "F 3 ' POWER FROM HI P TURB: ',G12.5,/," "F 4 ' POWER FROM MED P TURB: ',G12.5,/," "F 5 ' POWER FROM LOW P TURB: ',G12.5,/," "F 6 ' POWER FROM VL P TURB: ',G12.5,/," "F 7 ' TOTAL POWER: ',G12.5,/," "F 8 ' POWER USED INTERNALLY: ',G12.5,/," "F 9 ' NEW POWER PRODUCED: ',G12.5,/," "F 1 ' CONDENSER DUTY: ',G12.5,/," "F 2 ' BURNER/BOILER CAP COST: ',G12.5,/," "F 3 'BOILER BLOWDOWN: ',G12.5)" "C" "C" ) \ ? CALCULATOR BOILRAIR ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";" ";" ";" ) \ \ DEFINE FVN = FGLUC FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = GLUCOSE \ \ DEFINE FVN = FCELLU FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = FXYLOS FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = XYLOSE \ \ DEFINE FVN = FXYLAN FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = FLIGN FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = LIGNIN \ \ DEFINE FVN = FORGAN FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ORGANISM \ \ DEFINE FVN = FSOLSL FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = SOLSLDS \ \ DEFINE FVN = FC5SUG FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = C5SUGAR \ \ DEFINE FVN = FC6SUG FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = C6SUGAR \ \ DEFINE FVN = FC5SLD FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = C5SOLID \ \ DEFINE FVN = FACETA FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = ACETATE \ \ DEFINE FVN = FETOH FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FURFUR FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = FURFURAL \ \ DEFINE FVN = FHMF FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = HMF \ \ DEFINE FVN = FO2 FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = FLACID FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = LACID \ \ DEFINE FVN = FAACID FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = AACID \ \ DEFINE FVN = FNH4AC FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = NH4ACET \ \ DEFINE FVN = FC6SLD FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = CISOLID FVN-COMPONEN = C6SOLID \ \ DEFINE FVN = FSLLGN FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 803 FVN-SUBS = MIXED FVN-COMPONEN = LGNSOL \ \ DEFINE FVN = REQN2 FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 804 FVN-SUBS = MIXED FVN-COMPONEN = N2 \ \ DEFINE FVN = REQO2 FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 804 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = REQH2O FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 804 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = OXY261 FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 261 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = OXY560 FVN-VARTYPE = MOLE-FLOW FVN-STREAM = 560 FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = M802MIX \ \ FORTRAN FORTRAN-EXEC = ( "C SUBTRACT THE O2 COMING IN WITH 261 AND 560" "C" "F REQO2 = ((6.*(FGLUC+FCELLU+FC6SUG+FC6SLD+FHMF)+FACETA*2." "F 1 + 5.*(FXYLOS+FXYLAN+FC5SUG+FC5SLD+FURFUR)" "F 2 + (FLIGN+FSLLGN)*12.825 + FORGAN*1.2 + FSOLSL*1.4995" "F 3 + FETOH*3. + FLACID*3 + FAACID*2 + FNH4AC*2.75 - FO2)" "F 4 * 1.2) - OXY261 - OXY560" "F WRITE(NHSTRY,103)REQO2" "F 103 FORMAT(' REQO2 ',G12.5)" "F WRITE(NHSTRY,102)FGLUC,FCELLU,FC6SUG,FC6SLD,FHMF,FACETA,FXYLOS," "F 1FXYLAN,FC5SUG,FC5SLD,FURFUR,FLIGN,FORGAN,FSOLSL,FETOH,FLACID," "F 2FAACID,FNH4AC,FO2,FSLLGN" "F 102 FORMAT('FGLUC:',G12.5,'FCELLU:',G12.5,'FC6SUG:',G12.5,/," "F 1'FC6SLD:',G12.5,'FHMF:',G12.5,'FACETA:',G12.5,'FXYLOS:',G12.5,/," "F 1'FXYLAN:',G12.5,'FC5SUG:',G12.5,'FC5SLD:',G12.5,'FURFUR:',G12.5,/," "F 1'FLIGN:',G12.5,'FORGAN:',G12.5,'FSOLSL:',G12.5,'FETOH:',G12.5,/," "F 1'FLACID:',G12.5,'FAACID:',G12.5,'FNH4AC:',G12.5,'FO2:',G12.5,/," "F 1'FSLLGN:',G12.5)" "F REQAIR = REQO2 / 0.23" "F REQN2 = REQAIR * 0.7572" "F REQH2O = REQAIR * 0.0128" ) \ ? CALCULATOR AIRREQ ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";--------------------------------------------------------" "; UTILITY FORTRAN BLOCKS - AREA 900" ";-------------------------------------------------------" ";" ";" ";F COMMON /CLSSET/ CLYLD, CLPROD, CLVES, CLVOL, CLWV" ";" ";CONTROLS THE AMOUNT OF AIR NEEDED IN CELLULASE" ";PRODUCTION AND SEED FERMENTORS" ";" ";STIN IS ALSO DV1" ";ARFIN IS ALSO DV2" "; CLYLD IS THE CELLULASE YIELD (FPU/G CELLULOSE + G XYLOSE)" "; AND IS ENTERED IN SETVAR" ";F CLYLD=150" "; CLPROD IS THE CELLULASE PRODUCTION PRODUCTIVITY (FPU/L HR)" "; AND IS ENTERED IN SETVAR" ";F CLPROD=30" "; IS ENTERED IN SETVAR (CLWV)" ";F WV1=0.8" ) \ \ 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-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = 413 \ \ READ-VARS READ-VAR = (STDEN ARFDEN SDIN SDDEN CL412A XY412A CLYLD CLPROD CLVOL CLWV) \ \ WRITE-VARS WRITE-VAR = (AIRIN F1 CLVES) \ \ 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,ARFIN,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 'ARFIN ',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)" ) \ ? CALCULATOR WATERDEM ? ; SET1 ; \ 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 - Feed to IX, removed from recycle flow" "; DEFINE FLIX3 STREAM-VAR STREAM=243 SUBSTREAM=MIXED VARIABLE=MASS-FLOW" "; Read Variable - Additional Stream to reduce flow of 535 to Digestor" "; Write variable - amount of well water mixed with treated water" ";" ";Feed to WWT; used to calculate treated WW returned to process" ";" ";CIP/CS LOSS IS SET AT 320 LB/HR BY THE BASE CASE." ";" ";Treated WW that is used in the process is calculated here from a" ";ratio of feed to WWT (612) and treated WW (624) from I0302B.inp:" ";F 6 ' CWBL2(Cooling Tower Blowdown, Calc Here) = ',g12.5,/," ";F 6 ' CWBL1(Cooling Tower Blowdown, Specified) = ',g12.5,/," ";" ) \ \ 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 \ \ DEFINE FVN = WWTFD FVN-VARTYPE = STREAM-VAR FVN-STREAM = 612 FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ READ-VARS READ-VAR = (PWMU STLOSS SCRBWT EXTRA CWMKUP WWTFD) \ \ WRITE-VARS WRITE-VAR = (WATI WELLMX CIPCS TRTWW) \ \ FORTRAN FORTRAN-EXEC = ( "F CIPCS=145" "C" "C" "F TRTWW = WWTFD * (87816. / 89073.)" "C" "F WATI = PWMU + STLOSS + CIPCS + CWMKUP - TRTWW + SCRBWT" "F 1 - EXTRA" "F WELLMX = WATI - STLOSS - SCRBWT" "C" "F IF (WELLMX.LT.0) WELLMX = 0" "C" "F WRITE(NHSTRY,50)CWMKUP,EXTRA,CIPCS,SCRBWT,PWMU," "F 1 STLOSS,TRTWW,WELLMX,WATI" "F 50 FORMAT(' WATER RESULTS',/," "F 9 ' CWMKUP(COOLING TOWER MAKEUP) = ',G12.5,/," "F 1 ' EXTRA (STREAM 251) = ',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)" ) \ ? CALCULATOR CW ? ; SET1 ; \ COMMENTS COMMENTS = ( "; EXECUTE BEFORE T914" ";" "; Calculate makeup and chemicals for CW tower." "; Calculate CW flow from QCWTOT" "; QTOT in cal/s" "; DT in deg C" "; CP in cal/g.sec at 30 C" "; CW flow in kg/hr" ";" ";" "; Total Cooling Tower Make-up" ";" ";CALCULATE COOLING TOWER CHEMICALS." ";VALUES ARE SCALED FROM THE SPREADSHEET VALUES." ";" "; 44.3 psi=100 ft head" ";" "; P-902 Cooling Water Pump" ";" ";" ) \ \ DEFINE FVN = AP902 FVN-VARTYPE = PARAMETER FVN-PARAMNO = 6 \ \ DEFINE FVN = WM902 FVN-VARTYPE = PARAMETER FVN-PARAMNO = 7 \ \ DEFINE FVN = QTOT FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QCWTOT \ \ DEFINE FVN = CWMKUP FVN-VARTYPE = STREAM-VAR FVN-STREAM = 941A FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ DEFINE FVN = CWBL2 FVN-VARTYPE = STREAM-VAR FVN-STREAM = 944 FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ DEFINE FVN = CWC FVN-VARTYPE = STREAM-VAR FVN-STREAM = 922 FVN-SUBS = MIXED FVN-VARIABLE = MASS-FLOW \ \ READ-VARS READ-VAR = (QTOT) \ \ WRITE-VARS WRITE-VAR = (CWMKUP CWC CWBL2 AP902 WM902) \ \ FORTRAN FORTRAN-EXEC = ( "C" "F DT = 37.0 - 28.0" "F CP = 0.9987" "F CWF = (3600 * QTOT) / (DT * CP * 1000)" "F WRITE(NHSTRY,*)'CWF: ',CWF, 'QTOT: ',QTOT" "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 * CWF" "C USE % FOR CWEVAP BASED ON I0302B RESULTS OF CWFLSH BLOCK." "F CWEVAP = 0.011 * CWF" "F CWBL2 = 0.1 * (CWWNDG + CWEVAP)" "F CWMKUP = CWBL2 + CWWNDG + CWEVAP" "C DEFINE RATIOS OF CHEMICALS" "F CWCREQ=2.E-7" "C CWCREQ IS THE COOLING TOWER CHEMICAL REQ" "C IN LB/LB COOLING WATER FLOW" "C" "F CWC=CWCREQ*CWF" "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 WP946 =((CWMKUP/(1000*3600)) * (DP946*6894.8)/(EPM*EEL) )/1000." "F WM902=(CT*QTOT) + WP946" "F AP902=CWF/(1000*3600)" ) \ ? CONVERGENCE SECANT CFUGE3SC ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";-------------------------------------------------------------------" "; RECYCLE/SEQUENCING" ";-------------------------------------------------------------------" ";" ";" ) \ \ SPEC SPECID = "CFUGE3S" \ ? CONVERGENCE SECANT EVAPCNCC ? ; SET1 ; \ SPEC SPECID = "EVAPCONC" \ ? SENSITIVITY MASSFLOW ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ";F COMMON /CLSSET/ CLYLD, CLPROD, CLVES, CLVOL, CLWV" ";" "; DEFINE AA220 MOLE-FLOW STREAM=220 SUBSTREAM=MIXED COMPONENT=AACID" "; Use Diameter of 501 squared for scaling" ";" ";" ";" "; Heat Exchangers" ";" "; H200" ";" ";" "; H201" ";" ";" ";" "; H205" ";" ";" "; H244" ";" "; H302" ";" ";" "; E502 EVAPORATORS" ";" ";" "; H512" ";" ";" ";" ";" "; Unless Otherwise Stated" ";HMT - HYDROLYSATE MIX TANK AGITATOR (A-205)" ";" "; HMTV is VOLFS205 in Excel sheet" ";" ";OL - OVERLIMING TANK AGITATOR (A-209)" "; Uses variable AP209 - VOLFM209 in Excel sheet" ";" ";XNT - REACIDIFICATION TANK AGITATOR (A-224)" "; Uses variable AP239 - VOLFM239 in Excel sheet" ";" ";SLT - SLURRYING TANK AGITATOR (A-232)" ";" "; SLV is VOLFS232 in Excel sheet" ";" ";SD - ZYMOMONAS SEED FERMENTOR AGITATORS (A-304-305A/B)" ";" "; Calculate the volumetric flow to F-305 (stream 306)" "; Calculate the volume of F-305 as 10% (inoculum level)" "; SDV is VOLFS305 in Excel sheet" ";" "; Calculate Power" "; SDV2 is VOLFS304 in Excel sheet" ";" ";ZM - ZYMOMONAS HOLD TANK AGITATORS (A-301)" ";" "; ZMINC=VOLUME RATIO OF SEED HOLD TO LARGEST SEED TANK" ";" ";" "; SDV (calculated earlier), volumetric flow to F-305" "; SDV*ZMR = volume of F-305" ";" "; ZMV is VOLFS301 in Excel sheet" ";" ";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" "; SACDAY is the Sacch. residence time in days." "; SAVT is VOLFS310 in Excel sheet" "; Calculate the number of Sacch. tanks required for costing" ";" ";SM - FERMENTOR AGITATORS (A-300)" ";" "; Calculate Volumetric Flow Rate" "; SSFDAY is the SSCF residence time in days." "; SMVT is VOLFS300 in Excel sheet" "; Calculate the number of SSCF vessels required for costing" ";" ";BW - BEER WELL (A-306)" "; Uses AP306 - VOLFM306 in Excel sheet" ";" ";CS - CELLULASE SEED FERMENTOR AGITATORS (A-402-4A/B)" "; REMOVED FROM EXCEL AGITATOR POWER SHEET KI 7/02" ";" ";CL - CELLULASE FERMENTOR AGITATORS (A-400A-L)" "; REMOVED FROM EXCEL AGITATOR POWER SHEET KI 7/02" ";" ";" ";PM - MEDIA PREP TANK AGITATOR (T-405)" "; REMOVED FROM EXCEL AGITATOR POWER SHEET KI 7/02" "; Uses VOLFM405 in Excel sheet" ";" ";RW - RECYCLE WATER TANK AGITATOR (A-530)" "; Uses AP530 - VOLFM530 in Excel sheet" ";" ";CSL - CSL STORAGE TANK AGITATOR (A-720)" "; Uses AP720 - VOLFM720 in Excel sheet" ";" ";DAP - CSL/DAP DAY TANK AGITATOR (A-760)" "; Uses AP760 - VOLFM760 in Excel sheet" ";" "; Other Calculated Variables to be Tabulated" ";" ";" ";" ";" ";" "; Pumps" ";" ";" ";NEED TO CONVERT AREA 100 PUMPS TO USE IN SPREADSHEET" "; Uses VOLFM101 in Excel sheet" "; EP101 is the number of units" "; Wash Water Pump (P-102)" "; Uses VOLFM102 in Excel sheet" "; Clarifier Underflow Feed Pump (P-103)" "; Uses VOLFM103 in Excel sheet" "; EP103 is the number of units" "; Clarified Water Pump (P-104)" "; Uses VOLFM104 in Excel sheet" "; EP104 is the number of units" "; Belt Press Sump Pump (P-105)" "; Uses VOLFM105 in Excel sheet" "; EP105 is the number of units" "; P-201 Sulfuric Acid Pump" ";" "; P-205 Pneumapress Feed Pumps" "; Uses SOLD0220 in Excel sheet" ";" "; P-209 Overlimed Hydrolysate Pump" ";" "; P-211 Concentrated Filtrate Pumps" "; Uses STRM0221 in Excel sheet" "; P-213 Wash Filtrate Pump #2" "; Uses STRM0256 in Excel sheet" "; P-222 Overlimed Hydrolysate Liquor Pump" ";" "; 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 stream 301B" "; FRCCI = CI solids fraction of stream 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 stream 306" "; FRCCI = CI solids fraction of stream 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" ";" ";" "; P-301 SSCF Seed Transfer Pump" ";" "; P-302 Seed Transfer Pump" "; P-306 Beer Transfer Pump" ";" "; P-400 Cellulase Transfer Pump" "; REMOVED FROM EXCEL PUMP SHEET KI 7/02" ";" "; P-401 Cellulase Seed Transfer Pump" "; REMOVED FROM EXCEL PUMP SHEET KI 7/02" ";" ";" "; P-405 Media Pump" "; REMOVED FROM EXCEL PUMP SHEET KI 7/02" ";" "; P-420 Antifoam Pump" "; REMOVED FROM EXCEL PUMP SHEET KI 7/02" ";" "; P-501 Beer Column Bottoms Pump" "; P-503 Beer Column Reflux Pump" ";" "; P-504 Rectification Column Bottoms Pump" ";" ";+(FCP504/3600.)/(RCP504*1000.)" ";" "; P-505 Rectification Column Reflux Pump" ";" "; 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-701 Ethanol Product Pump" ";" "; P-703 Sulfuric Acid Pump" ";" "; P-710 Gasoline Pump" ";" "; P-720 CSL Pump" ";" "; P-750 Cellulase Enzyme Pump" ";" "; P-760 CSL/DAP Pump" ";" "; P-902 CW pump is now in FORTRAN CW block" "; P-912 Makeup Water Pump" ";" "; P-914 Process Water Circulating Pump" ";" "; AREA 200 MISC POWER" "; Uses STRM0220 in Excel sheet" "; Uses SOLD0220 in Excel sheet" "; Uses STRM0255 in Excel sheet" "; Uses STRM0227 in Excel sheet" "; Uses STRM0101 in Excel sheet" "; Uses STRM0227 in Excel sheet" "; Uses STRM0239 in Excel sheet" "; Uses SOLD0220 (stream 220 solids) in Excel sheet" "; AREA 500 MISC POWER" "; Uses STRM0571 in Excel sheet" "; Uses VOLFM701 in Excel sheet" "; Uses STRM0570 in Excel sheet" "; AREA 600 MISC POWER" "; WWT power variable (WMWWT) is in Fortran WWT" "; AREA 700 MISC POWER" "; Uses STRM0755 in Excel sheet" "; Uses STRM0755 in Excel sheet" "; AREA 900 MISC POWER" ";CW Tower power variable (WM902) is in Fortran CW" ";Power req of 250 hp total (2 units at 125 hp each) for plant air" "; 250 hp = 186 KW" ";Add Pneumapress power for S-205 and S-505" ";" "; Uses STRM0101 in Excel sheet" ";" "; REMOVED FROM EXCEL MISC POWER SHEET KI 7/02" ";" ";" "; Uses stream 914 in Excel sheets" ";" "; TABULATE 1 AA220 COL-LABEL=ACET220A" ) \ \ DEFINE FVN = DD501 FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = D501 FVN-SENTENCE = TSIZE-RESULT FVN-VARIABLE = TS-DIAM FVN-ID1 = 1 \ \ DEFINE FVN = WWTCST FVN-VARTYPE = PARAMETER FVN-PARAMNO = 2 \ \ DEFINE FVN = WMWWT FVN-VARTYPE = PARAMETER FVN-PARAMNO = 3 \ \ DEFINE FVN = CAPCST FVN-VARTYPE = PARAMETER FVN-PARAMNO = 4 \ \ DEFINE FVN = AP902 FVN-VARTYPE = PARAMETER FVN-PARAMNO = 6 \ \ DEFINE FVN = WM902 FVN-VARTYPE = PARAMETER FVN-PARAMNO = 7 \ \ DEFINE FVN = WNET FVN-VARTYPE = PARAMETER FVN-PARAMNO = 8 \ \ 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 = 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 = CLVES FVN-VARTYPE = PARAMETER FVN-PARAMNO = 43 \ \ DEFINE FVN = QCD501 FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QCD501 \ \ DEFINE FVN = QCD502 FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QCD502 \ \ DEFINE FVN = QCW FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QCWTOT \ \ DEFINE FVN = QCHW FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QCHWTOT \ \ DEFINE FVN = QF300A FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QF300A \ \ DEFINE FVN = QF0300 FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QF300 \ \ DEFINE FVN = QF301 FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QF301-6B \ \ DEFINE FVN = QF0400 FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QF400 \ \ DEFINE FVN = QSH301 FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QH301 \ \ DEFINE FVN = QH0517 FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QH517 \ \ DEFINE FVN = QRD501 FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QRD501 \ \ DEFINE FVN = QRD502 FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QRD502 \ \ DEFINE FVN = S220S FVN-VARTYPE = STREAM-VAR FVN-STREAM = 220 FVN-SUBS = CISOLID FVN-VARIABLE = MASS-FLOW \ \ DEFINE FVN = S570S FVN-VARTYPE = STREAM-VAR FVN-STREAM = 570 FVN-SUBS = CISOLID FVN-VARIABLE = MASS-FLOW \ \ DEFINE FVN = S101 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 101 \ \ DEFINE FVN = S107 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 107 \ \ DEFINE FVN = S214 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 214 \ \ DEFINE FVN = S217 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 217 \ \ DEFINE FVN = S220 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 220 \ \ DEFINE FVN = S221 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 221 \ \ DEFINE FVN = S225 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 225 \ \ DEFINE FVN = S227 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 227 \ \ DEFINE FVN = S228 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 228 \ \ DEFINE FVN = S229 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 229 \ \ DEFINE FVN = S230 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 230 \ \ DEFINE FVN = S232 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 232 \ \ DEFINE FVN = S239 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 239 \ \ DEFINE FVN = S240 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 240 \ \ DEFINE FVN = S250 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 250 \ \ DEFINE FVN = S255 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 255 \ \ DEFINE FVN = S256 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 256 \ \ DEFINE FVN = S257 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 257 \ \ DEFINE FVN = S304 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 304 \ \ DEFINE FVN = S415 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 415 \ \ DEFINE FVN = S416 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 416 \ \ DEFINE FVN = S417 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 417 \ \ DEFINE FVN = S420 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 420 \ \ DEFINE FVN = S433 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 433 \ \ DEFINE FVN = S440 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 440 \ \ DEFINE FVN = S502 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 502 \ \ DEFINE FVN = S510 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 510 \ \ DEFINE FVN = S515 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 515 \ \ DEFINE FVN = S516 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 516 \ \ DEFINE FVN = S521 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 521 \ \ DEFINE FVN = S523 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 523 \ \ DEFINE FVN = S525 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 525 \ \ DEFINE FVN = S528 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 528 \ \ DEFINE FVN = S531 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 531 \ \ DEFINE FVN = S551 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 551 \ \ DEFINE FVN = S557 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 557 \ \ DEFINE FVN = S571 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 571 \ \ DEFINE FVN = S572 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 572 \ \ DEFINE FVN = S612 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 612 \ \ DEFINE FVN = S630 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 630 \ \ DEFINE FVN = S631 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 631 \ \ DEFINE FVN = S701 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 701 \ \ DEFINE FVN = S703 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 703 \ \ DEFINE FVN = S710 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 710 \ \ DEFINE FVN = S713 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 713 \ \ DEFINE FVN = S717 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 717 \ \ DEFINE FVN = S723 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 723 \ \ DEFINE FVN = S735 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 735 \ \ DEFINE FVN = S745 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 745 \ \ DEFINE FVN = S750 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 750 \ \ DEFINE FVN = S755 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 755 \ \ DEFINE FVN = S903 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 903 \ \ DEFINE FVN = S904 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 904 \ \ DEFINE FVN = S905 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 905 \ \ DEFINE FVN = S914 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 914 \ \ DEFINE FVN = S921 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 921 \ \ DEFINE FVN = S922 FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 922 \ \ DEFINE FVN = S534A FVN-VARTYPE = STREAM-PROP FVN-PROPSET = MASSFLW FVN-STREAM = 534A \ \ DEFINE FVN = S804C FVN-VARTYPE = STREAM-VAR FVN-STREAM = 804C FVN-SUBS = CISOLID FVN-VARIABLE = MASS-FLOW \ \ DEFINE FVN = Z5101 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = C5SOLID \ \ DEFINE FVN = Z6101 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = C6SOLID \ \ DEFINE FVN = ZC101 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = CELLULOS \ \ DEFINE FVN = ZW101 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 101 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ DEFINE FVN = ZX101 FVN-VARTYPE = MASS-FLOW FVN-STREAM = 101 FVN-SUBS = CISOLID FVN-COMPONEN = XYLAN \ \ DEFINE FVN = ZD515 FVN-VARTYPE = STREAM-VAR FVN-STREAM = 515E FVN-SUBS = MIXED FVN-VARIABLE = MASS-DENSITY \ \ 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = QSAC FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QF300A \ \ 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 = QREM FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QF300 \ \ 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = 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 = W205 FVN-VARTYPE = WORK-POWER FVN-STREAM = WM205 \ \ DEFINE FVN = W505 FVN-VARTYPE = WORK-POWER FVN-STREAM = WM505 \ \ DEFINE FVN = QREF FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QCHW \ \ DEFINE FVN = QSSF FVN-VARTYPE = HEAT-DUTY FVN-STREAM = QH914C \ \ DEFINE FVN = CHWSPT FVN-VARTYPE = BLOCK-VAR FVN-BLOCK = QH14BSP FVN-SENTENCE = "FLOW/FRAC" FVN-VARIABLE = "FLOW/FRAC" FVN-ID1 = QH14BCHW \ \ TABULATE COLNO = 2 EXPR = "CAPCST" LINE1 = "BLRCAPTL" \ \ TABULATE COLNO = 5 EXPR = "CODTOT" LINE1 = "CODTOTAL" \ \ TABULATE COLNO = 6 EXPR = "DI501" LINE1 = "DIAMD501" \ \ TABULATE COLNO = 7 EXPR = "ISACAG" LINE1 = "INUMSACA" \ \ TABULATE COLNO = 8 EXPR = "ISAC" LINE1 = "INUMSACC" \ \ TABULATE COLNO = 9 EXPR = "ISSF" LINE1 = "INUMSSCF" \ \ TABULATE COLNO = 10 EXPR = "ISSFAG" LINE1 = "INUMSSFA" \ \ TABULATE COLNO = 11 EXPR = "P501GP" LINE1 = "P501FLOW" \ \ TABULATE COLNO = 12 EXPR = "QCHW" LINE1 = "QCHWTOTA" \ \ TABULATE COLNO = 13 EXPR = "QCD501" LINE1 = "QCND0501" \ \ TABULATE COLNO = 14 EXPR = "QCD502" LINE1 = "QCND0502" \ \ TABULATE COLNO = 15 EXPR = "QCW" LINE1 = "QCWTOTAL" \ \ TABULATE COLNO = 16 EXPR = "QF301" LINE1 = "QF301-6B" \ \ TABULATE COLNO = 17 EXPR = "QH0517" LINE1 = "QHET0517" \ \ TABULATE COLNO = 18 EXPR = "QEH300" LINE1 = "QHX300EA" \ \ TABULATE COLNO = 19 EXPR = "QH300A" LINE1 = "QHX310EA" \ \ TABULATE COLNO = 20 EXPR = "QT200" LINE1 = "QLMT0200" \ \ TABULATE COLNO = 21 EXPR = "QT201" LINE1 = "QLMT0201" \ \ TABULATE COLNO = 22 EXPR = "QT205" LINE1 = "QLMT0205" \ \ TABULATE COLNO = 23 EXPR = "QT244" LINE1 = "QLMT0244" \ \ TABULATE COLNO = 31 EXPR = "QT301" LINE1 = "QLMT0301" \ \ TABULATE COLNO = 32 EXPR = "QT302" LINE1 = "QLMT0302" \ \ TABULATE COLNO = 33 EXPR = "QT512" LINE1 = "QLMT0512" \ \ TABULATE COLNO = 34 EXPR = "QTE502" LINE1 = "QLMTE502" \ \ TABULATE COLNO = 35 EXPR = "QRD501" LINE1 = "QRFD0501" \ \ TABULATE COLNO = 36 EXPR = "QRD502" LINE1 = "QRFD0502" \ \ TABULATE COLNO = 37 EXPR = "QSH301" LINE1 = "QSTMH301" \ \ TABULATE COLNO = 38 EXPR = "QTM908" LINE1 = "QTOTM908" \ \ TABULATE COLNO = 39 EXPR = "S51021" LINE1 = "S510S521" \ \ TABULATE COLNO = 42 EXPR = "S220S" LINE1 = "SOLD0220" \ \ TABULATE COLNO = 43 EXPR = "S570S" LINE1 = "SOLD0570" \ \ TABULATE COLNO = 44 EXPR = "S101" LINE1 = "STRM0101" \ \ TABULATE COLNO = 45 EXPR = "S107" LINE1 = "STRM0107" \ \ TABULATE COLNO = 46 EXPR = "S214" LINE1 = "STRM0214" \ \ TABULATE COLNO = 47 EXPR = "S217" LINE1 = "STRM0217" \ \ TABULATE COLNO = 48 EXPR = "S220" LINE1 = "STRM0220" \ \ TABULATE COLNO = 49 EXPR = "S221" LINE1 = "STRM0221" \ \ TABULATE COLNO = 50 EXPR = "S225" LINE1 = "STRM0225" \ \ TABULATE COLNO = 51 EXPR = "S227" LINE1 = "STRM0227" \ \ TABULATE COLNO = 52 EXPR = "S228" LINE1 = "STRM0228" \ \ TABULATE COLNO = 53 EXPR = "S229" LINE1 = "STRM0229" \ \ TABULATE COLNO = 54 EXPR = "S230" LINE1 = "STRM0230" \ \ TABULATE COLNO = 55 EXPR = "S232" LINE1 = "STRM0232" \ \ TABULATE COLNO = 56 EXPR = "S239" LINE1 = "STRM0239" \ \ TABULATE COLNO = 57 EXPR = "S240" LINE1 = "STRM0240" \ \ TABULATE COLNO = 60 EXPR = "S250" LINE1 = "STRM0250" \ \ TABULATE COLNO = 61 EXPR = "S255" LINE1 = "STRM0255" \ \ TABULATE COLNO = 62 EXPR = "S256" LINE1 = "STRM0256" \ \ TABULATE COLNO = 63 EXPR = "S257" LINE1 = "STRM0257" \ \ TABULATE COLNO = 64 EXPR = "S304" LINE1 = "STRM0304" \ \ TABULATE COLNO = 73 EXPR = "S502" LINE1 = "STRM0502" \ \ TABULATE COLNO = 77 EXPR = "S515" LINE1 = "STRM0515" \ \ TABULATE COLNO = 78 EXPR = "S516" LINE1 = "STRM0516" \ \ TABULATE COLNO = 80 EXPR = "S523" LINE1 = "STRM0523" \ \ TABULATE COLNO = 81 EXPR = "S525" LINE1 = "STRM0525" \ \ TABULATE COLNO = 82 EXPR = "S528" LINE1 = "STRM0528" \ \ TABULATE COLNO = 83 EXPR = "S531" LINE1 = "STRM0531" \ \ TABULATE COLNO = 84 EXPR = "S551" LINE1 = "STRM0551" \ \ TABULATE COLNO = 85 EXPR = "S557" LINE1 = "STRM0557" \ \ TABULATE COLNO = 86 EXPR = "S571" LINE1 = "STRM0571" \ \ TABULATE COLNO = 87 EXPR = "S572" LINE1 = "STRM0572" \ \ TABULATE COLNO = 88 EXPR = "S612" LINE1 = "STRM0612" \ \ TABULATE COLNO = 91 EXPR = "S630" LINE1 = "STRM0630" \ \ TABULATE COLNO = 92 EXPR = "S631" LINE1 = "STRM0631" \ \ TABULATE COLNO = 93 EXPR = "S701" LINE1 = "STRM0701" \ \ TABULATE COLNO = 94 EXPR = "S703" LINE1 = "STRM0703" \ \ TABULATE COLNO = 95 EXPR = "S710" LINE1 = "STRM0710" \ \ TABULATE COLNO = 96 EXPR = "S713" LINE1 = "STRM0713" \ \ TABULATE COLNO = 97 EXPR = "S717" LINE1 = "STRM0717" \ \ TABULATE COLNO = 98 EXPR = "S723" LINE1 = "STRM0723" \ \ TABULATE COLNO = 99 EXPR = "S735" LINE1 = "STRM0735" \ \ TABULATE COLNO = 100 EXPR = "S745" LINE1 = "STRM0745" \ \ TABULATE COLNO = 101 EXPR = "S750" LINE1 = "STRM0750" \ \ TABULATE COLNO = 102 EXPR = "S755" LINE1 = "STRM0755" \ \ TABULATE COLNO = 103 EXPR = "S903" LINE1 = "STRM0903" \ \ TABULATE COLNO = 104 EXPR = "S904" LINE1 = "STRM0904" \ \ TABULATE COLNO = 105 EXPR = "S905" LINE1 = "STRM0905" \ \ TABULATE COLNO = 106 EXPR = "S914" LINE1 = "STRM0914" \ \ TABULATE COLNO = 107 EXPR = "S921" LINE1 = "STRM0921" \ \ TABULATE COLNO = 108 EXPR = "S922" LINE1 = "STRM0922" \ \ TABULATE COLNO = 109 EXPR = "S534A" LINE1 = "STRM534A" \ \ TABULATE COLNO = 110 EXPR = "S804C" LINE1 = "STRM804C" \ \ TABULATE COLNO = 112 EXPR = "APL224" LINE1 = "VOLFL224" \ \ TABULATE COLNO = 113 EXPR = "APL301" LINE1 = "VOLFL301" \ \ TABULATE COLNO = 114 EXPR = "APL302" LINE1 = "VOLFL302" \ \ TABULATE COLNO = 116 EXPR = "AP101" LINE1 = "VOLFM101" \ \ TABULATE COLNO = 117 EXPR = "AP102" LINE1 = "VOLFM102" \ \ TABULATE COLNO = 118 EXPR = "AP103" LINE1 = "VOLFM103" \ \ TABULATE COLNO = 119 EXPR = "AP104" LINE1 = "VOLFM104" \ \ TABULATE COLNO = 120 EXPR = "AP105" LINE1 = "VOLFM105" \ \ TABULATE COLNO = 121 EXPR = "AP201" LINE1 = "VOLFM201" \ \ TABULATE COLNO = 122 EXPR = "AP209" LINE1 = "VOLFM209" \ \ TABULATE COLNO = 123 EXPR = "AP222" LINE1 = "VOLFM222" \ \ TABULATE COLNO = 126 EXPR = "AP239" LINE1 = "VOLFM239" \ \ TABULATE COLNO = 127 EXPR = "AP300" LINE1 = "VOLFM300" \ \ TABULATE COLNO = 128 EXPR = "AP306" LINE1 = "VOLFM306" \ \ TABULATE COLNO = 129 EXPR = "AP310" LINE1 = "VOLFM310" \ \ TABULATE COLNO = 133 EXPR = "AP501" LINE1 = "VOLFM501" \ \ TABULATE COLNO = 134 EXPR = "AP503" LINE1 = "VOLFM503" \ \ TABULATE COLNO = 135 EXPR = "AP504" LINE1 = "VOLFM504" \ \ TABULATE COLNO = 136 EXPR = "AP505" LINE1 = "VOLFM505" \ \ TABULATE COLNO = 137 EXPR = "AP511" LINE1 = "VOLFM511" \ \ TABULATE COLNO = 138 EXPR = "AP512" LINE1 = "VOLFM512" \ \ TABULATE COLNO = 139 EXPR = "AP513" LINE1 = "VOLFM513" \ \ TABULATE COLNO = 140 EXPR = "AP514" LINE1 = "VOLFM514" \ \ TABULATE COLNO = 141 EXPR = "AP515" LINE1 = "VOLFM515" \ \ TABULATE COLNO = 142 EXPR = "AP530" LINE1 = "VOLFM530" \ \ TABULATE COLNO = 143 EXPR = "AP701" LINE1 = "VOLFM701" \ \ TABULATE COLNO = 144 EXPR = "AP703" LINE1 = "VOLFM703" \ \ TABULATE COLNO = 147 EXPR = "AP710" LINE1 = "VOLFM710" \ \ TABULATE COLNO = 148 EXPR = "AP720" LINE1 = "VOLFM720" \ \ TABULATE COLNO = 149 EXPR = "AP750" LINE1 = "VOLFM750" \ \ TABULATE COLNO = 150 EXPR = "AP760" LINE1 = "VOLFM760" \ \ TABULATE COLNO = 151 EXPR = "AP902" LINE1 = "VOLFM902" \ \ TABULATE COLNO = 152 EXPR = "AP912" LINE1 = "VOLFM912" \ \ TABULATE COLNO = 153 EXPR = "AP914" LINE1 = "VOLFM914" \ \ TABULATE COLNO = 154 EXPR = "HMTV" LINE1 = "VOLFS205" \ \ TABULATE COLNO = 155 EXPR = "SLV" LINE1 = "VOLFS232" \ \ TABULATE COLNO = 156 EXPR = "SMVT" LINE1 = "VOLFS300" \ \ TABULATE COLNO = 157 EXPR = "ZMV" LINE1 = "VOLFS301" \ \ TABULATE COLNO = 158 EXPR = "SDV2" LINE1 = "VOLFS304" \ \ TABULATE COLNO = 159 EXPR = "SDV" LINE1 = "VOLFS305" \ \ TABULATE COLNO = 160 EXPR = "SAVT" LINE1 = "VOLFS310" \ \ TABULATE COLNO = 162 EXPR = "WCMP" LINE1 = "WKAIRCMP" \ \ TABULATE COLNO = 166 EXPR = "WNET" LINE1 = "WKBLRNET" \ \ TABULATE COLNO = 167 EXPR = "WM902" LINE1 = "WKCWTOWR" \ \ TABULATE COLNO = 168 EXPR = "WMWWT" LINE1 = "WKWWTRMT" \ \ TABULATE COLNO = 169 EXPR = "WWTCST" LINE1 = "WWTCOSTS" \ \ TABULATE COLNO = 170 EXPR = "Z5101" LINE1 = "Z5101FLW" \ \ TABULATE COLNO = 171 EXPR = "Z6101" LINE1 = "Z6101FLW" \ \ TABULATE COLNO = 172 EXPR = "ZC101" LINE1 = "ZC101FLW" \ \ TABULATE COLNO = 173 EXPR = "ZW101" LINE1 = "ZW101FLW" \ \ TABULATE COLNO = 174 EXPR = "ZX101" LINE1 = "ZX101FLW" \ \ TABULATE COLNO = 175 EXPR = "ZD515" LINE1 = "ZZDEN515" \ \ PARAM BASE-CASE = NO \ \ VARY 1 VARY-VARTYPE = STREAM-VAR VARYSTREAM = 101 VARYSUBS = MIXED VARYVARIABLE = TEMP VARYLINE1 = "101 TEMP" \ \ VARY 1 LIST = (20.0 <0> <0> ) \ \ DECLARE FORTRAN-DEC = ( "F COMMON /WWLOAD/ CODTOT, BODTOT, CODDAY, BODDAY" ) \ \ FORTRAN FORTRAN-EXEC = ( "F DI501 = DD501 * DD501" "C DUTY Q OVER LMTD DT (IN BTU/HR-F) IS CALCULATED FOR USE IN EXCEL HEAT" "C EXCHANGER AREA CALCULATION SHEET. U VALUES ARE INPUT INTO EXCEL SHEET." "F T945 = 28." "F T940 = 37." "F DT=((T223-T940)-(T240-T945))/DLOG((T223-T940)/(T240-T945))" "F DT = DABS(DT * 1.8)" "C CONVERT FROM CAL/S TO BTU/HR" "F Q = QHX200 * 14.2869" "F QT200 = DABS(Q) / DT" "F WRITE(NHSTRY,101)DT,Q" "F 101 FORMAT(' HX200 CALC RESULTS',/," "F 1 ' DT = ',G12.5,/," "F 2 ' Q = ',G12.5)" "F DT201=((T218-T501)-(T520A-T502))/DLOG((T218-T501)/(T520A-T502))" "F DT201 = DABS(DT201 * 1.8)" "C CONVERT FROM CAL/S TO BTU/HR" "F Q201 = QH201 * 14.2869" "F QT201 = DABS(Q201) / DT201" "F WRITE(NHSTRY,102)DT201,Q201,QT201" "F 102 FORMAT(' HX201 CALC RESULTS',/," "F 1 ' DT201 = ',G12.5,/," "F 2 ' Q201 = ',G12.5,/," "F 3 ' QT201 = ',G12.5)" "F DT205=((T260-T940)-(T262-T945))/DLOG((T260-T940)/(T262-T945))" "F DT205 = DABS(DT205 * 1.8)" "C CONVERT FROM CAL/S TO BTU/HR" "F Q205 = QHX205 * 14.2869" "F QT205 = DABS(Q205) / DT205" "F WRITE(NHSTRY,120)DT205,Q205" "F 120 FORMAT(' HX205 CALC RESULTS',/," "F 1 ' DT205 = ',G12.5,/," "F 2 ' Q205 = ',G12.5)" "C LATENT HEAT FIRST" "F DTLAT=((T520A-T940)-(T520A-T945))/DLOG((T520A-T940)/(T520A-T945))" "F DTLAT = DABS(DTLAT * 1.8)" "C CONVERT FROM CAL/S TO BTU/HR" "F QLAT = QHX201 * 14.2869" "F QTLAT = DABS(QLAT) / DTLAT" "C" "C SENSIBLE HEAT NEXT" "F DTSNS=((T520A-T940)-(T520-T945))/DLOG((T520A-T940)/(T520-T945))" "F DTSNS = DABS(DTSNS * 1.8)" "C CONVERT FROM CAL/S TO BTU/HR" "F QSNS = QHX244 * 14.2869" "F QTSNS = DABS(QSNS) / DTSNS" "C" "F QT244 = QTLAT + QTSNS" "F WRITE(NHSTRY,112)DTLAT,QLAT,DTSNS,QSNS,QT244" "F 112 FORMAT(' HX CALC RESULTS',/," "F 1 ' DTLAT = ',G12.5,/," "F 2 ' QLAT = ' ,G12.5,/," "F 3 ' DTSNS = ',G12.5,/," "F 4 ' QSNS = ',G12.5,/," "F 5 ' QT244 = ',G12.5)" "F DT=((T301B-T940)-(T301C-T945))/DLOG((T301B-T940)/(T301C-T945))" "F DT = DABS(DT * 1.8)" "C CONVERT FROM CAL/S TO BTU/HR" "F Q = QHX302 * 14.2869" "F QT302 = DABS(Q) / DT" "F WRITE(NHSTRY,104)DT,Q" "F 104 FORMAT(' HX302 CALC RESULTS',/," "F 1 ' DT = ',G12.5,/," "F 2 ' Q = ',G12.5)" "F DT = T526-T528" "F DT = DABS(DT * 1.8)" "C CONVERT FROM CAL/S TO BTU/HR" "F Q = QEX502 * 14.2869" "F QTE502 = DABS(Q) / DT" "F WRITE(NHSTRY,105)DT,Q" "F 105 FORMAT(' HXAE502 CALC RESULTS',/," "F 1 ' DT = ',G12.5,/," "F 2 ' Q = ',G12.5)" "C" "F DT512=((T501-T518A)-(T506-T518))/DLOG((T501-T518A)/(T506-T518))" "F DT512 = DABS(DT512 * 1.8)" "C CONVERT FROM CAL/S TO BTU/HR" "F Q512 = QHX512 * 14.2869" "F QT512 = DABS(Q512) / DT512" "F WRITE(NHSTRY,106)DT512,Q512" "F 106 FORMAT(' HX512 CALC RESULTS',/," "F 1 ' DT512 = ',G12.5,/," "F 2 ' Q512 = ',G12.5)" "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" "F HMTV=HMT/HMTD+HMTS/HMTDS" "F SLV=SLT/SLTD+SLTS/SLTDS" "F SDV = (SD/SDD + SDS/SDSD)" "F SDV = SDV * 0.1" "C THEN A-304" "C SDN2 IS THE VOLUME RATIO OF F-304 TO F-305" "F SDN2 = 0.1" "F SDV2 = SDV * SDN2" "F ZMINC=1.2" "F ZMV=SDV * ZMINC" "F SAV = SA/SAD + SAS/SASD" "F SAR = SACDAY * 24" "F SAVT = SAV * SAR" "F SACVES = SAV * SAR / SACVOL / SACWV" "F SMV = SM/SMD + SMS/SMSD" "F SMR = SSFDAY * 24" "F SMVT = SMV * SMR" "F SSFVES = SMV * SMR / SSFVOL / SSFWV" "C FIRST CALCULATE FOR A-403" "F CSV=CSD/CSDD+CSDS/CSDSD" "C THEN FOR A-402" "C CSR3 IS THE VOLUME RATIO OF F-403 TO F-404" "F CSR3=0.05" "F CSV2=CSV*CSR3" "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" "F S51021 = S510 + S521" "C HEAT DUTY TO EACH SACCH. COOLER" "F ISAC = SACVES" "F ISAC = ISAC + 1" "F SACAGT = 2. * SACVES" "F ISACAG = 2 * ISAC" "F QH300A = QF300A / ISAC" "C HEAT DUTY TO EACH FERM COOLER" "F ISSF = SSFVES" "F ISSF = ISSF + 1" "F SSFAGT = 2. * SSFVES" "F ISSFAG = 2 * ISSF" "F QEH300 = QF0300 / ISSF" "C HEAT DUTY TO EACH CELLULASE COOLER (COILS)" "F ICLVES = CLVES" "C 3 CELLULASE REACTORS NOT IN USE" "F ICLVES = ICLVES + 1 - 3" "F QEH400 = QF0400 / ICLVES" "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) IN EXCEL SPREADSHEET" "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" "F PMPREQ = 0.5" "F EP101 = 2.0" "F AP101 = 0.1578 * PMPREQ * EP101" "C EP102 IS THE NUMBER OF UNITS" "F EP102 = 2.0" "F AP102 = 0.3155 * PMPREQ * EP102" "F EP103 = 1.0" "F AP103 = 0.00631 * PMPREQ * EP103" "F EP104 = 1.0" "F AP104 = 0.3155 * PMPREQ * EP104" "F EP105 = 1.0" "F AP105 = 0.00631 * PMPREQ * EP105" "F AP201 =(FMP201/3600.)/(RMP201*1000.)" "C POWER BASED ON THE SOLIDS FLOW OF STREAM 220" "F AP209 =(FMP209/3600.)/(RMP209*1000.)+(FCP209/3600.)/(RCP209*1000.)" "C POWER BASED ON THE TOTAL FLOW OF 221" "C POWER BASED ON THE TOTAL FLOW OF 256" "F AP222 =(FMP222/3600.)/(RMP222*1000.)+(FCP222/3600.)/(RCP222*1000.)" "F APL224 =(FMP224/60.)/(RMP224)+(FCP224/60.)/(RCP224)" "F AP239 =(FMP239/3600.)/(RMP239*1000.)+(FCP239/3600.)/(RCP239*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 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,*)' 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 AP300 =(PMPSSF*FRCMIX/3600.)/(RMP300*1000.)" "F AP300 =AP300+(FCP300*(1-FRCMIX)/3600.)/(RCP300*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,*)' PMPSSF: ',PMPSSF" "F WRITE(NHSTRY,*)' FRWFLW: ',FRWFLW" "F WRITE(NHSTRY,*)' RECFLW: ',RECFLW" "F APL301 = (FMP301/60.)/(RMP301)+(FCP301/60.)/(RCP301)" "F APL302 = APL301" "F AP306 =(FMP306/3600.)/(RMP306*1000.)+(FCP306/3600.)/(RCP306*1000.)" "F AP400 =(FMP400/3600.)/(RMP400*1000.)+(FCP400/3600.)/(RCP400*1000.)" "F APL401 =(FMP401/60.)/(RMP401)+(FCP401/60.)/(RCP401)" "F AP405 =(FMP405/3600.)/(RMP405*1000.)" "F AP420 =(FMP420/3600.)/(RMP420*1000.)" "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" "C TOTAL FLOW" "F AP501 = AP501 + APREC" "F P501GP = AP501 * 15850.45" "C ASSUME FLOW IS 2500 KG/HR & DENSITY IS 1KG/L" "F AP503 =(2500/3600.)/(1.*1000.)" "F AP504 =(FMP504/3600.)/(RMP504*1000.)" "C ASSUME FLOW IS 80000 KG/HR AND DENSITY IS 1KG/L" "F AP505 =(80000/3600.)/(1*1000.)" "F AP511 =(FMP511/3600.)/(RMP511*1000.)+(FCP511/3600.)/(RCP511*1000.)" "C RECIRCULATION RATIO = 3" "F AP511 = AP511 * (3. + 1.)" "F AP512 =(FMP512/3600.)/(RMP512*1000.)+(FCP512/3600.)/(RCP512*1000.)" "C RECIRCULATION RATIO = 1.9" "F AP512 = AP512 * (1.9 + 1.)" "F AP513 =(FMP513/3600.)/(RMP513*1000.)+(FCP513/3600.)/(RCP513*1000.)" "C RECIRCULATION RATIO = 3" "F AP513 = AP513 * (3. + 1.)" "F AP514 =(FMP514/3600.)/(RMP514*1000.)" "F AP515 =(FMP515/3600.)/(RMP515*1000.)" "F AP530 =(FMP530/3600.)/(RMP530*1000.)+(FCP530/3600.)/(RCP530*1000.)" "F AP701 =(FMP701/3600.)/(RMP701*1000.)" "F AP703 =(FMP703/3600.)/(RMP703*1000.)" "F AP710 =(FMP710/3600.)/(RMP710*1000.)" "F AP720 =(FMP720/3600.)/(RMP720*1000.)" "F AP750 =(FMP750/3600.)/(RMP750*1000.)+(FCP750/3600.)/(RCP750*1000.)" "F AP760 =(FMP760/3600.)/(RMP760*1000.)+(FCP760/3600.)/(RCP760*1000.)" "F AP912=(FM912/3600.)/(RM912*1000.)" "F AP914=(FM914/3600.)/(RM914*1000.)" "C FL=FLASH TANK SCREW CONVEYOR (C-201)" "C HF=HYDROLYSATE PNEUMAPRESS (S-205)" "C POWER BASED ON THE SOLIDS FLOW OF STREAM 220" "C CK=CAKE WASHING CONVEYOR (C-202)" "C FL=LIME SOLIDS AIR LOCK (C-225)" "C PH=PREHYDROLYSIS SCREW FEEDER / IMPREGNATOR / REACTOR (M-202)" "C ULOAD=LIME UNLOADER BLOWER (P-223)" "C GYPREM = GYPSUM FILTER(S-222)" "C HF = HYDROLYSATE PNEUMAPRESS (S-205)" "C S1=SLUDGE SCREWS (C-501A/B)" "C SVE=MOLE SIEVE SYSTEM (T-507-8)" "C CF=PNEUMAPRESS (S-505)" "C FD=DAP SOLIDS AIR LOCK (C-755)" "C UNLDAP=DAP UNLOADER BLOWER (P-755)" "C EM904=PLANT AND INSTRUMENT AIR COMPRESSOR (M-904)" "F PAIR = 250 * .7457" "F WCMP = PAIR + W205 + W505" "C ES904=INSTRUMENT AIR DRYER (S-904)" "C EM908=CHILLED WATER SYSTEM CALCULATION (M-908A/S)" "F QTM908 = (QREF + QSSF * CHWSPT)" "C EM910=CIP SYSTEM CALCULATION (M-910)" ) \ ? SEQUENCE SEQ3 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ SEQUENCE BLOCK-TYPE = BLOCK BLOCK-ID = T507-8 / BLOCK-TYPE = CALCULATOR BLOCK-ID = STORE / BLOCK-TYPE = BLOCK BLOCK-ID = PRODMIX / BLOCK-TYPE = BLOCK BLOCK-ID = TSTORE \ ? SEQUENCE SEQ10 ? ; SET1 ; \ COMMENTS COMMENTS = ( ";SEQUENCE SEQ9 IXRGNFLW S221A S221B" ) \ \ SEQUENCE BLOCK-TYPE = BLOCK BLOCK-ID = S600 / BLOCK-TYPE = CALCULATOR BLOCK-ID = WWT \ ? SEQUENCE SEQ12 ? ; SET1 ; \ 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 ? ; SET1 ; \ SEQUENCE RETURN = BEGIN BLOCK-TYPE = CONVERGENCE BLOCK-ID = EVAPCNCC / BLOCK-TYPE = BLOCK BLOCK-ID = STMDUP / BLOCK-TYPE = BLOCK BLOCK-ID = E501L / BLOCK-TYPE = BLOCK BLOCK-ID = E502V / BLOCK-TYPE = BLOCK BLOCK-ID = DCOOL2 / BLOCK-TYPE = SEQUENCE BLOCK-ID = SEQ12 / BLOCK-TYPE = BLOCK BLOCK-ID = T530 / BLOCK-TYPE = BLOCK BLOCK-ID = E502L / BLOCK-TYPE = BLOCK BLOCK-ID = E503V / BLOCK-TYPE = BLOCK BLOCK-ID = E503L / RETURN = RETURNTO BLOCK-TYPE = CONVERGENCE BLOCK-ID = EVAPCNCC \ ? SEQUENCE SEQ14 ? ; SET1 ; \ SEQUENCE BLOCK-TYPE = CALCULATOR BLOCK-ID = BOILRAIR / BLOCK-TYPE = BLOCK BLOCK-ID = M802MIX / BLOCK-TYPE = BLOCK BLOCK-ID = M802 / BLOCK-TYPE = BLOCK BLOCK-ID = BURNER \ ? REPORT FLOWSHEET-RE ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" ) \ \ OPTIONS TOTBAL = NOTOTBAL FORTRAN = NOFORTRAN DESIGN-SPEC = NODESIGN-SPE COMPBAL = NOCOMPBAL CONVERGENCE = NOCONVERGENC \ ? REPORT STREAM-REPOR ? ; SET1 ; \ COMMENTS COMMENTS = ( ";" "; Use EXCL-BLOCKS = or INCL-BLOCKS = to reduce the number of blocks reported" ";" ";STREAM-REPORT MASSFLOW NOZEROFLOW NOCOMP-ATTR NOSUBS-ATTR &" ) \ \ OPTIONS WIDE = WIDE MASSFLOW = MASSFLOW ZEROFLOW = NOZEROFLOW COMP-ATTR = NOCOMP-ATTR SUBS-ATTR = NOSUBS-ATTR MOLEFLOW = NOMOLEFLOW \ "\@"