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A600.A600ST.PROP600G Heater Built-In HEATER >VERSION 0 A600.A600ST.PROP600K Heater Built-In HEATER >VERSION 0 A600.A600ST.M-602A Compr Built-In COMPR >VERSION 0 A600.A600ST.M-602B Compr Built-In COMPR >VERSION 0 A600.A600ST.SP600B FSplit Built-In FSPLIT >VERSION 0 A600.A600ST.M-602C Compr Built-In COMPR >VERSION 0 A600.A600ST.H-601 Heater Built-In HEATER >VERSION 0 A600.A600ST.V600F Valve Built-In VALVE >VERSION 0 A600.A600ST.SP602B FSplit Built-In FSPLIT >VERSION 0 A600.A600ST.SP602A FSplit Built-In FSPLIT >VERSION 0 A600.A600ST.P-602 Pump Built-In PUMP >VERSION 0 A600.A600ST.H-602C Heater Built-In HEATER >VERSION 0 A600.A600ST.H-602B Heater Built-In HEATER >VERSION 0 A600.A600WTR.PROP600A Heater Built-In HEATER >VERSION 0 A600.A600WTR.SP400B Mixer Built-In MIXER >VERSION 0 A600.A600WTR.T-601A Sep Built-In SEP >VERSION 0 A600.A600WTR.P-601 Pump Built-In PUMP >VERSION 0 A600.A600WTR.V600A Valve Built-In VALVE >VERSION 0 A600.A600WTR.MX600A Mixer Built-In MIXER >VERSION 0 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Heater Built-In HEATER >VERSION 0 A700.H-414-CT Heater Built-In HEATER >VERSION 0 A700.HX900B Heater Built-In HEATER >VERSION 0 A900.WMX900A Mixer Built-In MIXER >VERSION 0 A900.WMX900B Mixer Built-In MIXER >VERSION 0 A900.WMXHOLD Mixer Built-In MIXER >VERSION 0 AREFRNC.HX100A Heater Built-In HEATER >VERSION 0 AREFRNC.HX100B Heater Built-In HEATER >VERSION 0 A400.K-412 Compr Built-In COMPR >VERSION 0 AREFRNC.MEFF-A Pump Built-In PUMP >VERSION 0 AREFRNC.DUMSEP Sep Built-In SEP >VERSION 0 A400.A400SGR.R410 RStoic Built-In RSTOIC >VERSION 0 A300.A300TR.MX300H Mixer Built-In MIXER >VERSION 0 A300.A300TR.H315A Heater Built-In HEATER >VERSION 0 A300.A300TR.H315B Heater Built-In HEATER >VERSION 0 A300.A300TR.H315C Heater Built-In HEATER >VERSION 0 A300.A300TR.H315D Heater Built-In HEATER >VERSION 0 A300.A300TR.MX300I Mixer Built-In MIXER >VERSION 0 A500.V500A Valve Built-In VALVE >VERSION 0 A500.V500B Valve Built-In VALVE >VERSION 0 A700.H-591-CT Heater Built-In HEATER >VERSION 0 A700.H-593-CT Heater Built-In HEATER >VERSION 0 A500.HLOSS2 Heater Built-In HEATER >VERSION 0 A500.HLOSS1 Heater Built-In HEATER >VERSION 0 A300.A300S.H-304+ Heater Built-In HEATER >VERSION 0 A300.A300S.MIXQH304 Mixer Built-In MIXER >VERSION 0 A300.A300Q.H-301B Heater Built-In HEATER >VERSION 0 A400.A400SGR.H-410B Heater Built-In HEATER >VERSION 0 A400.A400SGR.MX410 Mixer Built-In MIXER >VERSION 0 A300.A300Q.MX301 Mixer Built-In MIXER >VERSION 0 A400.H-416B Heater Built-In HEATER >VERSION 0 A400.MX416 Mixer Built-In MIXER >VERSION 0 A600.A600BL.MX605 Mixer Built-In MIXER >VERSION 0 A600.A600BL.H-605B Heater Built-In HEATER >VERSION 0 A600.MX607 Mixer Built-In MIXER >VERSION 0 A600.H-607B Heater Built-In HEATER >VERSION 0 A300.A300AGR.P-300AM Pump Built-In PUMP ? HIDE_BUFFER CONVERGENCE ? PASTE_ITEMS ? 1 LEVEL = 2 CONVERGENCE NEWTON AMISTM CANPARAM = 1 USENAME = AMISTM \ LEVEL = 2 CONVERGENCE SECANT AMINE CANPARAM = 1 USENAME = AMINE DELETED = 1 \ LEVEL = 2 CONVERGENCE NEWTON QAMINE CANPARAM = 1 USENAME = QAMINE DELETED = 1 \ MM "12.1" FLAVOR "NO" VERSION "12.1" DATETIME "Mon Sep 11 18:18:19 2006" MACHINE "WIN-NT/VC" ? CONVERGENCE NEWTON AMISTM ? \ SPEC SPECID = STMAMIN SPEC = 0.001 <0> <0> \ \@ ? CONVERGENCE SECANT AMINE ? \ SPEC SPECID = STMAMIN \ \@ ? CONVERGENCE NEWTON QAMINE ? \@ END_HIDEBUF ? HIDE_BUFFER SEQUENCE ? PASTE_ITEMS ? 2 LEVEL = 1 SEQUENCE STM1 CANPARAM = 1 USENAME = STM1 \ LEVEL = 1 SEQUENCE STM2 CANPARAM = 1 USENAME = STM2 \ MM "12.1" FLAVOR "NO" VERSION "12.1" DATETIME "Mon Sep 11 17:17:33 2006" MACHINE "WIN-NT/VC" ? SEQUENCE STM1 ? \ DESCRIPTION DESCRIPTION = "Sequence for Steam System" \ \ SEQUENCE BLOCK-TYPE = BLOCK BLOCK-ID = "A600.S-601" / BLOCK-TYPE = BLOCK BLOCK-ID = "A600.H-602" / BLOCK-TYPE = BLOCK BLOCK-ID = "A600.V600D" / BLOCK-TYPE = BLOCK BLOCK-ID = "A600.H-403404" / BLOCK-TYPE = BLOCK BLOCK-ID = "A600.A600TURB.M-602A" / BLOCK-TYPE = BLOCK BLOCK-ID = "A600.A600TURB.M-602B" / RETURN = BEGIN BLOCK-TYPE = CONVERGENCE BLOCK-ID = AMISTM / RETURN = RETURNTO BLOCK-TYPE = CONVERGENCE BLOCK-ID = AMISTM / BLOCK-TYPE = CALCULATOR BLOCK-ID = LPSTMDEM / RETURN = BEGIN BLOCK-TYPE = CONVERGENCE BLOCK-ID = TEAR / RETURN = RETURNTO BLOCK-TYPE = CONVERGENCE BLOCK-ID = TEAR / BLOCK-TYPE = BLOCK BLOCK-ID = "A600.A600TURB.SP600B" \ \ COMMENTS COMMENTS = ( ";Use this version when the QBALANCE design spec is " ";active" ) \ \@ ? SEQUENCE STM2 ? \ SEQUENCE RETURN = BEGIN BLOCK-TYPE = CONVERGENCE / BLOCK-TYPE = CALCULATOR BLOCK-ID = LPSTMDEM / BLOCK-TYPE = BLOCK BLOCK-ID = "A600.A600TURB.SP600B" / RETURN = RETURNTO BLOCK-TYPE = CONVERGENCE \ \@ END_HIDEBUF ? HIDE_BUFFER CALCULATOR ? PASTE_ITEMS ? 11 LEVEL = 1 CALCULATOR MIXALC CANPARAM = 1 USENAME = MIXALC \ LEVEL = 1 CALCULATOR NGTRM1 CANPARAM = 1 USENAME = NGTRM1 \ LEVEL = 1 CALCULATOR "C-D503" CANPARAM = 1 USENAME = "C-D503" \ LEVEL = 1 CALCULATOR DISTIL CANPARAM = 1 USENAME = DISTIL \ LEVEL = 1 CALCULATOR STMAMIN CANPARAM = 1 USENAME = STMAMIN \ LEVEL = 1 CALCULATOR P601VF CANPARAM = 1 USENAME = P601VF \ LEVEL = 1 CALCULATOR HPSTMDEM COULDPARAM = 1 USENAME = HPSTMDEM \ LEVEL = 1 CALCULATOR ALCOMB CANPARAM = 1 USENAME = ALCOMB \ LEVEL = 1 CALCULATOR NGCOMB CANPARAM = 1 USENAME = NGCOMB \ LEVEL = 1 CALCULATOR SYNCOMB CANPARAM = 1 USENAME = SYNCOMB \ LEVEL = 1 CALCULATOR W400GEN CANPARAM = 1 USENAME = W400GEN \ LEVEL = 1 CALCULATOR AMFLOW CANPARAM = 1 USENAME = AMFLOW DELETED = 1 \ LEVEL = 1 CALCULATOR ST2CARB CANPARAM = 1 USENAME = ST2CARB \ MM "12.1" FLAVOR "NO" VERSION "12.1" DATETIME "Fri Aug 19 15:39:58 2005" MACHINE "WIN-NT/VC" ? CALCULATOR MIXALC ? ; "ENG_MOLE" ; \ DEFINE FVN = COIN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 485 FVN-SUBS = MIXED FVN-COMPONEN = CO \ \ DEFINE FVN = COFR1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "R-410" FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 1 OPT-CATEG = ALL \ \ DEFINE FVN = COFR2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "R-410" FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 2 \ \ DEFINE FVN = COFR3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "R-410" FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 3 \ \ DEFINE FVN = COFR4 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "R-410" FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 4 \ \ DEFINE FVN = COFR5 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "R-410" FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 5 \ \ DEFINE FVN = COFR6 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "R-410" FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 6 \ \ DEFINE FVN = COFR7 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "R-410" FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 7 \ \ DEFINE FVN = COFR8 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "R-410" FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 8 \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the conversions in the mixed alcohol reactor." "C RXN1: CO + 2H2 = CH3OH" "C RXN2: CO + 2H2 + CH3OH = C2H5OH + H2O" "C RXN3: 3CO + 6H2 = C3H7OH + H2O" "C RXN4: 4CO + 8H2 = C4H9OH + H2O" "C RXN5: 5CO + 10H2 = C5H11OH + H2O" "C RXN6: CO + 3H2 = CH4 + H2O" "C RXN7: 2CO + 5H2 = C2H6 + 2H2O" "C RXN8: CO + H2O = CO2 + H2" "C" "F COFR1 = 0.098" "F COFR2 = 0.057" "F COFR3 = 0.03" "F COFR4 = 0.01" "F COFR5 = 0.005" "F COFR6 = 0.045" "F COFR7 = 0.005" "F COFR8 = 0.13" ) \ \ "READ-VARS" READ-VAR = ( COIN ) \ \ "WRITE-VARS" WRITE-VAR = ( COFR1 COFR2 COFR3 COFR4 COFR5 COFR6 COFR7 COFR8 ) \ \@ ? CALCULATOR NGTRM1 ? ; "ENG_MOLE" ; \ DEFINE FVN = MOLPSA FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FH2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = H2 OPT-CATEG = STREAM \ \ DEFINE FVN = FCH4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = CH4 OPT-CATEG = STREAM \ \ DEFINE FVN = FNH3 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = NH3 OPT-CATEG = STREAM \ \ DEFINE FVN = FC2H6 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = C2H6 OPT-CATEG = STREAM \ \ DEFINE FVN = FC2H4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = C2H4 OPT-CATEG = STREAM \ \ DEFINE FVN = FC2H2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = C2H2 OPT-CATEG = STREAM \ \ DEFINE FVN = GCH4 FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = 427 FVN-SUBS = MIXED FVN-COMPONEN = CH4 OPT-CATEG = STREAM \ \ DEFINE FVN = GC2H6 FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = 427 FVN-SUBS = MIXED FVN-COMPONEN = C2H6 OPT-CATEG = STREAM \ \ DEFINE FVN = GC3H8 FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = 427 FVN-SUBS = MIXED FVN-COMPONEN = C3H8 OPT-CATEG = STREAM \ \ DEFINE FVN = GIC4 FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = 427 FVN-SUBS = MIXED FVN-COMPONEN = "I-C4H10" OPT-CATEG = STREAM \ \ DEFINE FVN = GNC4 FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = 427 FVN-SUBS = MIXED FVN-COMPONEN = "N-C4H10" OPT-CATEG = STREAM \ \ DEFINE FVN = GC5 FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = 427 FVN-SUBS = MIXED FVN-COMPONEN = "PENTANE+" OPT-CATEG = STREAM \ \ DEFINE FVN = GH2S FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = 427 FVN-SUBS = MIXED FVN-COMPONEN = H2S OPT-CATEG = STREAM \ \ DEFINE FVN = GAS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 427 FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = QLOSS FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "R-401A" FVN-VARIABLE = DUTY FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = FCO FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = CO \ \ DEFINE FVN = FCAL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = METHANOL \ \ DEFINE FVN = FC2AL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FC3AL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = PROPANOL \ \ DEFINE FVN = FC4AL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = NBUTANOL \ \ DEFINE FVN = FC5AL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = 426 FVN-SUBS = MIXED FVN-COMPONEN = PENTANOL \ \ FORTRAN FORTRAN-EXEC = ( "C This computes the HHV of the purge gas and the natural gas trim." "C It also sets the heat loss for the tar reformer regenerator." "C" "C First set the HHV in Btu/SCF for each species of interest" "C" "F HVH2 = 324.2" "F HVCH4 = 1010.0" "F HVC2H6 = 1769.7" "F HVC2H4 = 1599.8" "F HVC2H2 = 1474.3" "F HVC3H8 = 2516.2" "F HVIC4 = 3252.0" "F HVNC4 = 3262.4" "F HVC5 = 4008.7" "F HVH2S = 637.1" "F HVNH3 = 434.2" "F HVCO = 322" "C methanol hhv" "F HVCH4O = 868" "C ethanol hhv" "F HC2H6O = 1600" "C propanol hhv" "F HC3H8O = 2338" "C butanol hhv" "F C4H10O = 3074" "C pentanol hhv" "F C5H12O = 3826" "C" "C Now compute the total HHV of the PSA offgas" "C" "F SCFMOL = 10.73*(60+459.67)/14.696" "F TOTHV = SCFMOL * ( FH2*HVH2 + FCH4*HVCH4 + FC2H6*HVC2H6 +" "F 1 FC2H4*HVC2H4 + FC2H2*HVC2H2 + FNH3*HVNH3 +FCO*HVCO +" "F 2 FCAL*HVCH4O + FC2AL*HC2H6O + FC3AL*HC3H8O + " "F 3 FC4AL*C4H10O + FC4AL*C5H12O )" "F HHVPSA = TOTHV / MOLPSA / SCFMOL" "F WRITE(NHSTRY,10) HHVPSA" "F 10 FORMAT(1x,""Higher heating value of purge gas, Btu/SCF = "",E13.5)" "C" "C Now compute the HHV of the Natural Gas trim (in Btu/SCF)" "C" "F HVGAS = ( GCH4*HVCH4 + GC2H6*HVC2H6 + GC3H8*HVC3H8 +" "F 1 GIC4*HVIC4 + GNC4*HVNC4 + GC5*HVC5 + GH2S*HVH2S )" "C" "C" "C Set the heat loss at 2% of HHV" "C" "F QLOSS = -0.02 * SCFMOL * (MOLPSA*HHVPSA + GAS*HVGAS)" ) \ \ "READ-VARS" READ-VAR = ( FNH3 FC2H6 FC2H4 FC2H2 GCH4 GIC4 GNC4 GC5 GH2S GC2H6 MOLPSA FCO FCAL FC2AL FC3AL FC4AL FC5AL ) \ \ "WRITE-VARS" WRITE-VAR = ( GAS QLOSS ) \ \@ ? CALCULATOR "C-D503" ? ; "ENG_MOLE" ; \ DEFINE FVN = MEOH FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.503" FVN-SUBS = MIXED FVN-COMPONEN = METHANOL OPT-CATEG = STREAM \ \ DEFINE FVN = WATER FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.503" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = SPEC FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.D502" FVN-VARIABLE = VALUE FVN-SENTENCE = SPEC FVN-ID1 = 1 OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( " WRITE (*,*) 'PRIOR TO D503:'" " WRITE (*,*) 'WATER: ', WATER" " WRITE (*,*) 'MEOH: ', MEOH" " WRITE (*,*) 'SPEC: ', SPEC " " " "c REC = SPEC * WATER / MEOH" "c RECMAX = 0.90" "c IF (REC.GT.RECMAX) THEN" "c SPEC = RECMAX * MEOH / WATER" "c ELSE " "c SPEC = 1.1" "c END IF" "c WRITE (*,*) 'NEW SPEC:', SPEC" ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = "A500.D502" \ \@ ? CALCULATOR DISTIL ? ; "ENG_MOLE" ; \ DEFINE FVN = REBOIL FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.582" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = STMFLW FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A600.A600TURB.SP600B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 652 \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the steam flow to the methanol column reboiler" " " "F STMFLW = REBOIL" ) \ \ "READ-VARS" READ-VAR = ( REBOIL ) \ \ "WRITE-VARS" WRITE-VAR = ( STMFLW ) \ \@ ? CALCULATOR STMAMIN ? ; "ENG_MOLE" ; \ DEFINE FVN = FCO2A FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A300.319" FVN-SUBS = MIXED FVN-COMPONEN = CO2 OPT-CATEG = STREAM \ \ DEFINE FVN = FCO2B FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A300.360" FVN-SUBS = MIXED FVN-COMPONEN = CO2 OPT-CATEG = STREAM \ \ DEFINE FVN = FCO2C FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A400.A403.481" FVN-SUBS = MIXED FVN-COMPONEN = CO2 OPT-CATEG = STREAM \ \ DEFINE FVN = ASTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A600.A600TURB.650" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C Calculate the steam requirement for Amine System reboiler" "C" "F FCO2 = FCO2A + FCO2B + FCO2C" "F ASTM = FCO2 * 0.6424" ) \ \ "READ-VARS" READ-VAR = ( FCO2A FCO2B FCO2C ) \ \ "WRITE-VARS" WRITE-VAR = ( ASTM ) \ \@ ? CALCULATOR P601VF ? ; "ENG_MOLE" ; \ DEFINE FVN = VFIN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A600.624" FVN-SUBS = MIXED FVN-VARIABLE = VFRAC OPT-CATEG = STREAM \ \ DEFINE FVN = TIN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A600.624" FVN-SUBS = MIXED FVN-VARIABLE = TEMP \ \ DEFINE FVN = TOUT FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A600.H-610" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C Added by S. Phillips on 10/2/06" "C Prevents vapor into pump inlet error if too high" "C if stream is already below bubble point temperature" "C then no additional cooling or heating occurs." "C" "F TOUT = TIN" " IF (VFIN .GE. 0.01) THEN" " TOUT = TIN - 5.0" " ENDIF" ) \ \ "READ-VARS" READ-VAR = ( VFIN TIN ) \ \ "WRITE-VARS" WRITE-VAR = ( TOUT ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = "A600.H-610" \ \@ ? CALCULATOR HPSTMDEM ? ; "ENG_MOLE" ; \ DEFINE FVN = COMPHP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A300.A300Q.WK301" OPT-CATEG = STREAM \ \ DEFINE FVN = SP602A FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A600.A600ST.SP602A" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 607A OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C Phillips 10/10/06 Add HP steam demand to balance turbine shaft power" "C with K-301 compressor requirements" "C" "C for now - shaft 1 hp = 11.96 lb/hr steam" "C" "F SP602A = COMPHP / .98 / .98 * 11.96" ) \ \ "READ-VARS" READ-VAR = ( COMPHP ) \ \ "WRITE-VARS" WRITE-VAR = ( SP602A ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = "A600.A600ST.SP602A" \ \@ ? CALCULATOR ALCOMB ? ; "ENG_MOLE" ; \ DEFINE FVN = C2ALIN FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = O2C2 FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = C3ALIN FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = C4ALIN FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = C5ALIN FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = O2MIX FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = O2ALC FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = C1MAL FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = C2MAL FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = C3MAL FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = C4MAL FVN-VARTYPE = "MOLE-FLOW" \ \ DEFINE FVN = C5MAL FVN-VARTYPE = "MOLE-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C This computes the amount of oxygen needed to combust the ethanol" "C product...part of plant efficiency calcs" "C" "C C2H6O + 3O2 --> 3H2O + 2CO2" "C" "F O2C2 = 3 * C2ALIN" "C" "C Now see how much oxygen is needed to combust the remaining higher" "C alcohols...part of efficiency calcs" "C" "C C3H8O + 4.5O2 --> 4H2O + 3CO2" "C C4H10O + 6O2 --> 5H2O + 4CO2" "C C5H12O + 7.5O2 --> 6H2O + 5CO2" "F O2MIX = 4.5*C3ALIN + 6*C4ALIN + 7.5*C5ALIN" " O2MIX = 1.2 * O2MIX" "C" "C Combust the entire mixed alcohol stream" "C Include methanol" "C CH4O + O2 --> 2H2O + 1.5CO2" "C" "F O2ALC = C1MAL + 3*C2MAL +4.5*C3MAL + 6*C4MAL + 7.5*C5MAL" "F O2ALC = 1.1 * O2ALC" ) \ \ "READ-VARS" READ-VAR = ( C2ALIN C3ALIN C4ALIN C5ALIN C1MAL C2MAL C3MAL C4MAL C5MAL ) \ \ "WRITE-VARS" WRITE-VAR = ( O2C2 O2MIX O2ALC ) \ \ EXECUTE BLOCK-TYPE = BLOCK BLK-ID = "A500.A504.HV-MXALC.B3" \ \@ ? CALCULATOR NGCOMB ? ; "ENG_MOLE" ; \ DEFINE FVN = O2REQ FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = H2S FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = CH4 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = C2H6 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = C3H8 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = IC4H10 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = NC4H10 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = C5H12 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This computes the amount of oxygen needed to combust the natural" "C gas to the reformer combustor...part of plant efficiency calcs" "C" "C Here are the combustion reactions:" "C" "C H2S + 1.5*O2 -> H2O + SO2" "C CH4 + 2*O2 -> CO2 + 2*H2O" "C C2H6 + 3.5*O2 -> 2*CO2 + 3*H2O" "C C3H8 + 5*O2 -> 3*CO2 + 4*H2O" "C IC4H10 + 6.5*O2 -> 4*CO2 + 5*H2O" "C NC4H10 + 6.5*O2 -> 4*CO2 + 5*H2O" "C C5H12 + 8*O2 -> 5*CO2 + 6*H2O" "C" "C Now compute the O2 required" "C" "F O2REQ = 1.5*H2S + 2*CH4 + 3.5*C2H6 + 5*C3H8 + 6.5*IC4H10" "F 1 + 6.5*NC4H10 + 8*C5H12" ) \ \ "READ-VARS" READ-VAR = ( H2S CH4 C2H6 C3H8 NC4H10 C5H12 ) \ \ "WRITE-VARS" WRITE-VAR = ( O2REQ ) \ \@ ? CALCULATOR SYNCOMB ? ; "ENG_MOLE" ; \ DEFINE FVN = H2 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = CO FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = H2S FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = NH3 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = CH4 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = C2H6 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = C2H4 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = C2H2 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = C3H8 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = IC4H10 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = NC4H10 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = C5H12 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = C6H6 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = C10H8 FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = O2REQ FVN-VARTYPE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This block computes the amount of oxygen needed to combust the" "C raw syngas products...required for gasifier efficiency calcs." "C" "C Here are the combustion reactions:" "C" "C H2 + 0.5*O2 -> H2O" "C CO + 0.5*O2 -> CO2" "C H2S + 1.5*O2 -> H2O + SO2" "C NH3 + 1.75*O2 -> 1.5*H2O + NO2" "C CH4 + 2*O2 -> CO2 + 2*H2O" "C C2H6 + 3.5*O2 -> 2*CO2 + 3*H2O" "C C2H4 + 3*O2 -> 2*CO2 + 2*H2O" "C C2H2 + 2.5*O2 -> 2*CO2 + H2O" "C C3H8 + 5*O2 -> 3*CO2 + 4*H2O" "C IC4H10 + 6.5*O2 -> 4*CO2 + 5*H2O" "C NC4H10 + 6.5*O2 -> 4*CO2 + 5*H2O" "C C5H12 + 8*O2 -> 5*CO2 + 6*H2O" "C C6H6 + 7.5*O2 -> 6*CO2 + 3*H2O" "C C10H8 + 12*O2 -> 10*CO2 + 4*H2O" "C" "C Now compute the O2 required" "C" "F O2REQ = 0.5*H2 + 0.5*CO + 1.5*H2S + 1.75*NH3 + 2*CH4 + 3.5*C2H6" "F 1 + 3*C2H4 + 2.5*C2H2 + 5*C3H8 + 6.5*IC4H10 + 6.5*NC4H10 " "F 2 + 8*C5H12 + 7.5*C6H6 + 12*C10H8" "F O2REQ = 1.000001 * O2REQ" ) \ \ "READ-VARS" READ-VAR = ( H2 CO H2S NH3 CH4 C2H6 C2H4 C2H2 C3H8 IC4H10 NC4H10 C5H12 C6H6 C10H8 ) \ \ "WRITE-VARS" WRITE-VAR = ( O2REQ ) \ \ EXECUTE BLOCK-TYPE = BLOCK BLK-ID = "A200.A200FC.K-203" \ \@ ? CALCULATOR AMFLOW ? ; "ENG_MOLE" ; \ DEFINE FVN = WTOTAQ FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300AGR.AM-COLD" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = XAMWTP FVN-VARTYPE = "MASS-FRAC" FVN-STREAM = "A300.A300AGR.AM-COLD" FVN-SUBS = MIXED FVN-COMPONEN = AMINE \ \ DEFINE FVN = AMMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = AMINE FVN-ID2 = 1 \ \ DEFINE FVN = FCO2OU FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300AGR.319" FVN-SUBS = MIXED FVN-COMPONEN = CO2 \ \ DEFINE FVN = FH2SOU FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300AGR.319" FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ FORTRAN FORTRAN-EXEC = ( "C" "C Method for calculating Amine System duties from GPSA 21-12." "C Basic Simplified Design Calculations" "C Assumes that all of the CO2 is removed essentially, so" "C need to calculate for less than total removal using MolAG/Molamine" "C" "C GPM = Amine circulation rate in gallons/minute" "C CF = Constant for different Amine types" "C QMSCFD = Sour gas to be processed in MMscfd" "C y = Acid gas concentration in sour gas, mole%" "C x = Amine concentration in liquid solution, wt%" "C TPG = Temperature of process acid gas, F" "C PPG = Pressure of process acid gas, psia" "C" "C CF Amine mol AG/mol amine assumed" "C 41 MEA 0.33" "C 45 DEA (conv. loading) 0.5" "C 32 DEA (high loading) 0.7" "C 55.8 DGA (normally 50-60 wt%) 0.39" "C" "C Calculate the amine circulation rate in gpm. MEA is used." "C Calculate Q in scfd from acfh from ASPEN" "C" "C Calculate for actual amount of acid gas removed" "C" "F FAGRM = FCO2OU + FH2SOU" "F FAMINE = (FAGRM / 0.33)" "C" "C Convert molar flow of Amine into mass flow of aqueous amine at" "C specified wt% amine as indicated by AM-COLD stream" "C" "F WAMINE = FAMINE * AMMW" "F WTOTAQ = WAMINE / XAMWTP" "C" ) \ \ "READ-VARS" READ-VAR = ( XAMWTP AMMW FCO2OU FH2SOU ) \ \ "WRITE-VARS" WRITE-VAR = ( WTOTAQ ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = CONVERGENCE BLK-ID = AMREBOIL \ \@ ? CALCULATOR ST2CARB ? ; "ENG_MOLE" ; \ DEFINE FVN = FSTM FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = FCH4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = CH4 OPT-CATEG = STREAM \ \ DEFINE FVN = FC2H2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C2H2 OPT-CATEG = STREAM \ \ DEFINE FVN = FC2H4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C2H4 OPT-CATEG = STREAM \ \ DEFINE FVN = FC2H6 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C2H6 OPT-CATEG = STREAM \ \ DEFINE FVN = FC3H8 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C3H8 OPT-CATEG = STREAM \ \ DEFINE FVN = FIC4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = "I-C4H10" OPT-CATEG = STREAM \ \ DEFINE FVN = FNC4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = "N-C4H10" \ \ DEFINE FVN = FC5H12 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = "PENTANE+" OPT-CATEG = STREAM \ \ DEFINE FVN = FC6H6 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C6H6 OPT-CATEG = STREAM \ \ DEFINE FVN = FC10H8 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C10H8 \ \ DEFINE FVN = FTRSTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.393" FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C added by S. Phillips 9/30/06" "C calculates molar ratio of steam to reformable C" "C in the Tar Reformer inlet gas. No spec is given" "C for this ratio currently but is usually about 4" "C in methane steam reformers. Because of CO2 in gas" "C may not need to be this high." "C" "F FCARB = FCH4" " 1 + 2.0 * (FC2H2 + FC2H4 + FC2H6)" " 2 + 3.0 * FC3H8" " 3 + 4.0 * (FIC4 + FNC4)" " 4 + 5.0 * FC5" " 5 + 6.0 * FC6H6" " 6 + 10.0 * FC10H8" "C" "C Set the ratio to 2 for now. If ratio is greater than 2, nothing" "C is added." "C" "F SPEC = 2.0" "C " "F FRATIO = FSTM / FCARB" "C" "F FTRSTM = (SPEC * FCARB) - FSTM" "F IF (FTRSTM .LT. 0.0) FTRSTM = 1.0" "F WRITE(NHSTRY,20) FSTM, FCARB, FRATIO, FTRSTM, SPEC" "F 20 FORMAT(" "F 1 1x,""STEAM TO TAR REFORMER, lbmol/hr :"",F10.3,/," "F 2 1x,""Reformable Carbon to TR, lbmol/hr :"",F10.3,/," "F 3 1x,""Steam to Carbon Ratio at TR inlet"",F10.3,/," "F 4 1x,""Steam added at TR inlet"",F10.3,/," "F 5 1x,""User spec for Steam to Carbon Ratio"",F10.3)" ) \ \ "READ-VARS" READ-VAR = ( FSTM FCH4 FC2H2 FC2H4 FC2H6 FC3H8 FIC4 FNC4 FC5H12 FC6H6 FC10H8 ) \ \ "WRITE-VARS" WRITE-VAR = ( FTRSTM ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = "A300.A300TR.H315" \ \@ ? CALCULATOR W400GEN ? ; "ENG_MOLE" ; \ DEFINE FVN = WEXPAN FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A400.WK412" OPT-CATEG = STREAM \ \ DEFINE FVN = MEFF1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = EFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = W400G FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W400G" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C Pressure recovery of unconverted syngas through turboexpander on" "C way back to front end of process for fuel use or reforming" "C" "F WEEXPD = WEXPAN * MEFF1 * 0.97" "C" "C Now sum" "C" "F W400G = WEEXPD" "C" "C Now write" "C" "F WRITE (NHSTRY,*) 'W400G POWER:', " "F 1 W400G, WEEXPD, MEFF1" "C" ) \ \ "READ-VARS" READ-VAR = ( WEXPAN MEFF1 ) \ \ "WRITE-VARS" WRITE-VAR = ( W400G ) \ \@ END_HIDEBUF ? SETUP MAIN ? \ TITLE TITLE = "IGCC_Biorefinery Simulation" \ \ SIMULATE INTERACTIVE = NO MASSFLOW = MASSFLOW PROPERTIES = ( HMIXTP ) TFFFILE = "GAS_E" VISITED = 1 \ ? SETUP GLOBAL ? \ "IN-UNITS" INSET = ENG \ \ "STREAM-CLASS" SCLASS = MIXCINC \ ? SETUP DIAGNOSTICS ? \ TERMINAL T-SIM-LEVEL = 0 T-CONV-LEVEL = 0 T-COST-LEVEL = 0 T-PROP-LEVEL = 0 T-ECON-LEVEL = 0 T-STRM-LEVEL = 0 T-SYS-LEVEL = 0 \ ? SETUP "SIM-OPTIONS" ? ; "ENG_MOLE" ; \ "SIM-OPTIONS" TOL = 1E-007 <0> <0> \ ? SETUP "CUSTOM-UOM" ? ? SETUP "UNITS-SET" METCBAR ? \ DESCRIPTION DESCRIPTION = "Metric Units with C, BAR, MMKCAL/HR, and CUM" \ \ MMLOCAL \ \ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 7 7 3 3 5 3 3 3 5 3 4 3 3 3 3 1 3 3 3 4 3 7 3 3 3 1 1 4 4 3 3 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3 3 3 3 3 3 4 3 3 3 3 3 3 3 3 3 4 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 3 3 3 3 ) \ ? SETUP "UNITS-SET" METCKGCM ? \ DESCRIPTION DESCRIPTION = "Metric Units with C, KG/SQCM, MMKCAL/HR, and CUM" \ \ MMLOCAL \ \ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 7 7 3 3 5 3 3 3 8 3 4 3 3 3 3 1 3 3 3 4 3 7 3 3 3 3 3 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 4 8 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \ ? SETUP "UNITS-SET" "SI-CBAR" ? \ DESCRIPTION DESCRIPTION = "International System Units with C, BAR, and /HR" \ \ MMLOCAL \ \ UNITSET BASESET = SI ( 1 1 1 1 1 1 1 1 1 3 3 7 1 1 1 1 1 1 1 5 1 4 1 1 1 1 1 1 1 1 4 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 4 5 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 ) \ ? SETUP "SYS-OPTIONS" ? ? SETUP "ACCOUNT-INFO" ? ? SETUP "RUN-CONTROL" ? \ PARAMETER MAX-TIME = 20000. <0> <0> MAX-ERRORS = 5000 MAX-FORT-ERR = 1000 \ ? SETUP DESCRIPTION ? \ DESCRIP DESCRIP = ( "NREL Thermochemical Ethanol Process " "NREL Protected Information " "Original Authors: Pam Spath, Andy Aden " "Original Date: March 2006 " " " "Changes" " " "SP0612K;" " 1. Corrected Amine Pumping energy calculation for WEAPMP in Calc Block" " W300." " " "SP0612J;" " " "SP0612I; 18 Dec 2006: Pinch Analysis Base Case" " 1. Moved V500A, V500B, HLOSS1, HLOSS2 in A500" " to ALCOHL property section from STEAM property section." " 2. Corrected Cooling Tower fan power calculation in CWBAL calc block." " 3. Added calculation for interstage cooling fan power req. in A400." " Calc are in W400." " 4. Connected WK412 (turboexpander) in A400 into shaft power for " " WM602 turbines in A600. Removed separate power calc for" " turboexpander electricity gen from W400G and corresponding" " work stream in A900." " 5. Changed calc in WGEN so that shaft power is balanced by either" " making electricity (WNet<0) or using electric motor to make" " up power needs." " " "TE0612A; 13 Dec 2006: Pinch Analysis Base Case" " 1. Converted SP0612H to Aspen 2004.1 GUI (w/ Updates) Build Version" " 13.2.5.3291, Build Date: Aug. 8, 2006" " 2. Split-up A300TR.H315 into four exchangers on each feed stream." " This allows for proper pinch analysis." " 3. Adjusted blowdown of the system to 2% of circulation. Was set at" " 0.1%, which is too low for normal operations" " 4. Changed DP of H-201402 back to 0 psi from 5 psi...doesn't make " " sense to have a pressure drop across the steam drum, plus it" " causes havoc with pinch analysis because there is a temperature" " drop across the exchanger even though this is a cold stream that" " is being heated." " 5. Cleaned-up heat exchanger network around K-412. Removed H-417 from" " service." " 6. Changed spec value for RB301BTMP to 1700 F to reduce the amount of" " syngas being combusted to a reasonable minimum." " 7. Increased outlet temperature of H-416B. You now manipulate" " outlet temperature of H-416B to close the power balance." " 8. Cleaned-up pressure drop and temperature profile across H-592 and" " ECOOL2 so there isn't accidental vaporization and the product" " isn't cooled below cooling water temperature. Also set-up a" " calculator block called SETPINCH to ensure no cross pinch" " exchange." " 9. Ditto previous comment, but applied to H-590 and MACOOL2" "10. Changed name of A700.H-413-CT to A700.H-414-CT and changed name" " of A700.QCH413CT to A700.QCH414CT...names are now consistent" " with the cooling water duty from A400.H-414" "11. Renamed A500.QCH505 to A500.QAH505, renamed A500.QCH504 to" " A500.QAH504, renamed A500.QC504TOT to A500.QA504TOT. Names" " are now consistent across hierarchy boundaries and indicate" " these streams are from air coolers." "12. Renamed A500.A504.513 to A500.A504.592A to maintain consistency" " across hierarchy boundary." "13. Renamed A500.MACOOL2 to A500.H-591. Renamed A500.QCMACOO2 to" " A500.QCH591. Hooked-up the excahnger to the cooling water system." " Added A500.HLOSS1 and associated heat stream to cool product" " to 60 F at 1 atm." "14. Renamed A500.ECOOL2 to A500.H-592. Renamed A500.QECOOL2 to" " A500.QCH593. Hooked-up the exchanger to the cooling water system." " Added A500.HLOSS2 and associated heat stream to cool product" " to 60 F and 1 atm." "15. Reduced flow of A300.A300TR.393 to 1e-6 lb/hr from 18 lb/hr. This" " is closer to a zero value, so now I'll ignore the heater on" " this stream for the pinch analysis" "16. Zeroed out the duty for A600.H-602. The amount of heat available" " from the blowdown is too small to worry about at this level of" " design." "17. Changed/Improved documentation of each hierarchy sheet so that" " the acutal hierarchy name now appears on each sheet" "18. Renamed A600.A600WTR.651 to A600.A600WTR.351 to maintain name" " consistency across hierarchy levels." "19. Added calculator SETPINCH to set the upper and lower pinch" " temperatures for stream that either cross or approach the pinch" " point. Renamed A300.A300Q.H-301302 to H-301 and split it across" " the pinch. Split H-410 across the pinch. Split H-416 across the" " pinch. Renamed A600.A600BL.H-202405 to A600.A600BL.H-605. Split" " H-605 across the pinch. Renamed A600.H-403404 to A600.H-607. Split" " H-607 across the pinch." "----------------------------------------------------------------------" "SP0612H ; 10 Dec 2006: Design Report base/targer case" " 1. Set H-507 outlet condition to V/F = 0" " 2. Set H-315 outlet condition to 570F" " 3. Removed Calc Block ST2CARB (hid it)." " 4. Added QH315 to QBALANCE as QCLD12" " 5. Removed H215315 and heat stream from A300.A300TR.A300FC" " 6. Set R301BTEM design spec to 2451.5F and SP382 to 0.95 to" " achieve WNET near zero for base case." " 7. Reset initial temperature guesses for steam streams 200,350,393,534" " to match those leaving area 600." " 8. Changed pressure drop spec (-5atm) in SP400B in area 600WTR to 0atm" "-----------------------------------------------------------------------" "SP0612G; 9 Dec 2006: Design Report base/target case" " 1. Lowered steam cycle pressure to better match temperature of" " synthesis reactor operation. Pressure and temperature" " at inlet of first turbine set to 850 psia and 900F. Pressure" " at pump outlet set to 935 psia to allow for pressure drop." " 2. Adjusted pressure of 644 to meet new steam system specs. Pressure" " at that location in cycle is 865 psia." "-----------------------------------------------------------------------" "JJ0612F; 9 Dec 2006: Design Report base/target case" " 1. Remove QHOT11 & QHOT12 (duplicates) and QHOT4 (not included in pinch" " analysis) from QBALANCE." " 2. Adjusted the pressure of 644 in A600 to 1450 psig (to match 643 in " " A600BL)." " 3. Adjusted conversions in R-410 to achieve 60% CO conversion " " and 90% alcohols selectivity." " 4. Change the fraction of unconverted syngas to the tar reformer (split" " in A300.A300TR.SP382) to 0.95." " 5. Adjusted temperature in R301BTEM to make WNET essentially zero." "-----------------------------------------------------------------------" "SP0612E; 7 Dec 2006: Design Report" " 1. New R410 synthesis model" " 2. Rerouted stream 513 from Fuel Combustor to Tar Reformer heat" " exchanger H-315" " 3. Set M-602C turbine outlet pressure to 1.5 psia (where it used to" " be) and matching biochem model." " " "SP0612D; 7 Dec 2006: Design report" " 1. Changed TARCRACK calc block to draw data from stream 325A instead" " of stream 222." " 2. Deleted block R-301CR" " 3. Inserted alcohol cracking reactions into tar reformer R-303A." " " "SP0612C; 6 Dec 2006: Design Report" " 1. Created Flowsheet Section Global in AREFRNC and changed Pipe to Sep " " block with Global property set of RKS-BM" " 2. Modified MAR reactions to generate more propanol in outlet" " 3. Lowered air temperature to 90 F for forced air cooling" " to make consistent with design report spec." " " "SP0612A; 1 Dec 2006: Design Report" " 1. Separated turbocharge power into W400G work stream and removed from" " W400 calc block." " 2. Gasifier now points to BATYD5 routine" " 3. Changed calc for MISC power to the lesser of 10% of total power or" " 1000 kW." " " "SP0611J; 30 Nov 2006: Design Report" " 1. Set K-412 isentropic efficiency to 0.85 (was default value)" " 2. Set W400 turboexpander power generation efficiencies" " to 0.98 and 0.97 to be consistent with power generation" " efficiency in steam turbine power generation calcs (WGEN)" " 3. Changed P03OFAIR calc block to use 20% excess air for fuel" " combustion - was 10% excess." " 4. Added reference stream to AREFRNC for air to permit air temperature" " to be changed anywhere this reference is used instead of hard coded." " 5. Added reference block MEFF-A to store efficiency values used in" " calculations. EFF is the mechanical efficiency and DERR is the" " motor efficiency." " 6. Added references to values described in #4 and #5 above" " to calc blocks everywhere." " " "SP0611I; 30 Nov 2006: Design Report" " 1. Moved fan work calcs for Fuel Comb from W400 to W300" " 2. Cleaned out unused code in W100 - W900." " 3. Corrected turboexpander calculation in W400." " " "SP0611H; 29 Nov 2006: Design Report" " 1. Put ethanol recovery back to .99 in dist columns" " 2. Changed Convergence Sequence parameters to" " Inside-simultaneous and Inside" " " "SP0611G; 28 Nov 2006: Design Report" " 1. Connected stream 531 to Block PROP531B to mix streams" " 513 and 531 plus change to GLOBAL section. 531 was deleted" " everywhere else outside of A500 and stream 513 recycles the" " offgases to Fuel Combustion in A300." " 2. Removed DRYINTEM spec. Dryer inlet temp decreased by decreasing" " outlet temperature on H-311 or H-285. Upper limit on dryer" " inlet varies by feedstock. Currently thought to be 1200F." " 3. Turned off SP225 flow to char combustor (225C)" " 4. Changed design spec QM104B to vary H-311 outlet temperature" " to meet duty spec of 0 for M-104B (dryer)." " 5. Moved K-303 to upsream of R-301A on natural gas stream" " and increased outlet P to 1.2 atm. All other streams into" " R-301A are at sufficiently high pressure and don't need compr." " 6. Increased K-305 outlet pressure to 1.2 atm." " 7. Changed delta P for H-311 to -1 psi" " 8. Set H-285 outlet temp at 1100F" " 9. Increased ethanol recovery in both columns to .995 (vs. .99)" " " "AA0611G; 22 Nov 2006: Design Report" " 1. Added WP514 to calc for W500" " 2. flue gas was leaving at less than atmospheric pres." " raised outlet pressure of WK303 (tar reformer blower) from" " 1.01 atm to 1.1atm" " 3. Changed pressure of 384RECIN to 20 psi to match 384REC" " 4. Changed initial guess in stream 357 to 20 psi and 150F" " 5. K-313/Wk313 and H-384/QH384 were eliminated but comments " " did not reflect this." " 6. ....." " 7. Renamed stream A300.319 as A300.319B to keep consistent with" " A300agr section nomenclature" " 8. renamed stream 648 to 200 to match with gasifier" " renamed stream 653 to 534 to match distillation demand " " 9. Changed initial temp for stream 534 to match 534 leaving" " steam system: 380.7021" "10. matched temps for streams 200 and 350 and 393 also" "11. Eliminated QCT320CT cooling water demand for amine system" " Changed all cooling to air-cooling. Adjusted calcs in " " W300 accordingly" "12. added work stream WK333FAN to account for duty of amine cooler" " added calculation of wk333fan to section w300, cooling lean" " amine before it reenters contact vessel" "13. Blocks LEANCOOL, CONDUTY, and AMCOLDTY are all dummy exchangers" " simply there to give physical homes to heat streams for duties:" " amine condenser duty, amine cooler duty, and amine circulation" " (AM-Cold). Need to make sure that amine cooling duties match" " reboiler duty " "14. anywhere AMFLOW was defined in STDVOL, changed it to calc" " by lb/hr div by mass density (lb/cu ft) to get real ft3/hr" " instead of std cu ft per hr" " " "SP0611E; 20 Nov 2006: Design Report" " 1. Renamed H-304/QH-304 in fuel combustion area to H-311/QH311" " 2. Renamed R-301, R301A and assoc heat streams in Sulfur area" " to R-304, R-304A, QR-304, and QR-304A." " 3. Increased the manipulated variable upper limit to 2100F in" " design spec ADIABAT and COMBCTL2." " 4. Added Design Spec DRYINTEM to control dryer inlet temperature" " at 1100F +/- 50F by varying stream 225F (dirty syngas)" " to char combustor." " 5. Changed Steam-to-Carbon ratio minimum in ST2CARB to 3.0" " 6. Adjusted cooling duty calculation in amine scrubber to equal" " reboiler duty in same section. Cooling set to be proportional" " to amine ciculation rate and was split with 1/3 provided by" " cooling water for the lean amine stream and 2/3 provided by" " fan cooling as calculated in W300 block. Heat exchanger blocks" " were added to A300AGR area for condenser cooling duty and amine" " cross exchanging duty to provide simulation stream to hold" " value calulated in calc block." " 7. Renamed Design Spec R201B to R301BTEM." " 8. Deleted H-413B and QCH413B" " 9. Added air pre-heaters H-209 to char combustor and H-330 to fuel" " combustor with heat streams QH209 and QH330. Both streams added" " to QBALANCE as QCOLD2 and QCOLD5, respectively." "11. Changed turbine efficiency to 0.78 isentropic from 0.85" "12. Added pump P-314 to S-301 condensate stream and to W300 work." "13. Split H-503 into two exchangers adding H-503B for superheating." "14. Added H-620 for makeup water pre-heater. QH620 added to QBALANCE as" " QCOLD7." "15. Deleted pressure recovery and associated streams in A300S. Removed" " references in calc and design spec blocks as needed." "16. Renamed H-413AC as H-413 and QH413AC as QAH413" "17. Renamed QRH300RB to QH300RB" "18. Moved P-601 upstream to increase pressure before exchanger H-620" "19. Renamed QCH504 and QCH505 to QAH504 and QAH505." "20. Renamed stream MS condenser heat stream to QAS513" "21. Rename ECOOL and MACOOL heat streams and assoc. exchangers to" " H-592/QH592 and H-590/QH590, respectively. Added to QBALANCE as" " QHOT11 and QHOT12." " " "AA0611B; 15 Nov 2006: Design report" " 1. Added heat streamS to PROP300E, PROP400A,PROP400B,PROP500A," " PROP600K." " 2. Added heat streams QECOOL2 and QMACOL2 to product storage cooling." " this is to make sure energy balance closes" " 3. Renamed stream 225 to 225A at highest level hierarchy " " Renamed stream 226F as 225C in 200CC" " Renamed stream 363 as 463" " Renamed block QH411B AS QH411" " Renamed stream 499 as 470" " Renamed stream 469 as 471" " Renamed block 503MS as A503MS" " Maintained streams 511/511B consistency" " 4. In 200FC, eliminated H531 (wasn't doing anything) and stream" " 531G. Stream 284G now leaves the mixer" " 5. Added heat stream to S310 (QS310)." " 6. Added new prop block PROP500B and assoc. heat stream." " 7. Cleaned up CWBAL, deleted old variables not being used in" " calcs" " 8. Changed outlet pressure of M-602C from 1.5psia to 3.0 psia" " " "SP0611A; 13 Nov 2006: TC Mixed Alcohols Design Report Target Case" " 1. Renamed streams to eliminate duplicate names in separate" " Hierarchial blocks unless a continuation of stream." " 2. Modified design spec R201B. Spec varies SP225F to achieve" " outlet Temp for R201B. User manually sets SP226 split now" " to determine amount of residual syngas reformed vs. burned." " 3. Corrected Flowsheet Section assignments in A400 to keep" " equipment in ALCOHOL property set whereever liquid alcohols" " present." " 4. Added a heat stream for H-413AC. It is not used in QBALANCE." " 5. Removed heat stream from H-384 to H-413B. Added heat stream to" " H-413B (QCH413B) and placed into QBALANCE as QHOT11." " 6. Added heat stream to H-384 (QCH384) and to QBALANCE as QCLD10." " 7. Moved H-384 upstream of Split Block SP-384." " 8. Removed H-610 and related heat stream." " 9. Increased stages in D-504 and D-505. Moved feed stages to minimize" " reboiler and condenser duties while meeting column design specs." "10. Connected 384REC to H-315 in Tar Reformer block." "11. Removed SP602C and related streams." "12. Added code to Calc block ST2CARB to provide steam to TR to maintain" " steam to reformable carbon ratio at 4.0." "--------------------------------------------------------------------" "JJ0611H; 9 Nov 2006: TC Mixed Alcohols Design Report Target Case " " 1. Modify SETFEED to overwrite the ultimate & proximate analyses for" " steam 101 in addition to setting the moisture content. " " 2. Modify the calculation for the heating value of 101 to take into" " account the inert nature of the ash: change conversion fraction in" " calculator RX-100. " " 3. Modify design spec on char combustor for setting air rate & char" " combustor temperature." " a. COMBCTL1 specifies air rate as fraction of minimum air." " b. COMBCTL2 adjusts reaction temperature until duty is zero." "--------------------------------------------------------------------" "SP0610Q; 31 Oct 2006: TC Mixed Alcohols Design Report Target Case" " 1. Modified Synthesis reactor model to reflect ASF distribution and" " permit user to enter CO conversion." " 2. Tied Fuel Combustion flue gas into dryer flue gas before dryer inlet" " 3. Moved H-101 from A100 to A200 and renamed. Still in char combustor" " flue gas stream." " 4. Decreased H-416 outlet temperature." " 5. Added superheaters after 1st turbine and 2nd turbine - not used." " Can be used for extracting more power if heat available to heat" " steam streams in future cases." " 6. Added design spec QM104B to keep dryer heat exchanger duty slightly" " positive by varying H-286 outlet temperature." " 7. Made design spec TSTACK vary M-104B outlet temperature to meet" " spec of flue gas temperaure at 62.5F above dew point." "---------------------------------------------------------------------" "SP0610P; 25 Oct 2006: TC Mixed Alcohols Design Report Target Case" " 1. Added Design Spec R201B for R-201B outlet temperature - varies" " SP226." " 2. Modified turboexpander K-412 outlet pressure specification" " to 20 psig to permit recycle to tar reformer and fuel combustor." " 3. Increased inlet temperature to K-412 by hiding design spec TPURGE" " and setting outlet of H-416 to 675F." " 4. Decreased temperature to K-313 inlet by specifying no delta T for" " H-312. CO2 stream chilled through T.E. is used to cool H-413" " before venting." "----------------------------------------------------------------------" "SP0610N; 19 Oct 2006: TC Mixed Alcohols Design Report Target Case" " 1. Modify the stream 100 heating value HIERARCHY. " " a. Rename streams & blocks in HV-100 to make them more descriptive. " " b. Change the combustion reactor to let Aspen generate the" " combustion reactions & stoichiometry for any MIXED & CISOLID" " components. " " c. Rename WOODCOMB calculator as RX-100 & have it adjust the " " combustion reactions for the NC components (WOOD & CHAR). " " d. Add design spec O2-100 to minimize the amount of oxygen for the" " combustion operation." " e. Add calculator HV-100 to calculate HHV & LHV values." " 2. Use HV-100 block as template for heating values of the:" " a. Syngas (stream A200.224). Dry basis, sulfur free, no inerts," " no CISOLIDs, no NCs. " " b. natural gas (stream A200.A200FC.227), " " c. mixed alcohols (stream A400.475), " " d. ethanol product (stream A500.592), " " e. the C3+ alcohols (stream A500.590). " " 3. Modify plant efficiency calculations to use the heating values" " of the final products, not an intermediate stream." " 4. Remove *old* heating value blocks that are no longer needed." "--------------------------------------------------------------------" "SP0610M; 16 Oct 2006: TC Mixed Alcohols Design Report Target Case" " 1. Removed distillation column for separating higher alcohols. Mixed" " alcohol stream is co-product." " 2. Added split block in A200 to permit recycled syngas to be sent to" " gasifier and/or tar reformer." " 3. Added syngas bypass stream to char combustor block" " 4. Added heat exchanger in Fuel Combustor block to split heat exchange" " between tar reformer catalyst and tar reformer gas pre-heater." " 5. Added fan-driven air cooling for process stream above 170F with air " " air temp out at 160F and process stream out at 140F or higher " " includes: H-412, D-502 and D-504 condensers, and others. See Work" " calculation blocks." " 6. Added heat exchangers to recover heat from hot product streams." " 7. Reroute stream from knock out vessel S-303 to T-301 sludge tank" " 8. Removed Amine CO2 scrubber after Mixed Alcohol reactor." " 9. Removed H-410 after second syngas compressor." " 10.Removed compressor cooling on outlet stage." " 11.Added equilibrium reactor as last of series of reactors to make" " water-gas shift reaction be at equilibrium at the outlet" " 12.Removed syngas recycle running from S-502 to MAR inlet." " 13.Added stuff to mol sieve block to make condense flush stream prior" " to pumping liquid up to MAR inlet pressure." " 14.Changed Amine reboiler steam duty calculation" " to match method used on distillation reboilers." " 15.Decreased steam cycle blowdown from 2% per pass to .1% per pass." " 16.Adjusted turbine outlet pressures to match BC model.160 and 50 psig" " for the first 2 turbines and 1.5 psia for the last turbine." " 17. Turbine power streams coupled and compressor work stream connected" " to last turbine work input. This makes compressors turbine-driven." " 18. Took out cooling tower heat exchangers replaced by fan cooled H.E." " 19. Added power calculations for fan-cooled exchangers" " 20. Added a work mixer block in A900 to provide a place to hang values." " 21. Added dew point calculations to flue gas streams and design specs" " to keep temperature 62 degrees F above dew point." " 22. Increased cyclone separator efficiencies for sand to 99.99wt% from" " 99.9%" " 23. Changed H531 exchanger (unused currently but available) pressure" " drop to 0." " 24. Added H215H for pre-heating recycle stream to tar reformer." " 25. Added alcohol cracking reactions to recycled gases to tar reformer" " 26. Added reactor from 2005 MA report (Aden, et al) into A400MAR block" " for comparisons purposes - outlet streams not tied to simulation." " 27. Added REQUIL block to A400MAR block for comparison purposes. This" " block uses extents for all reactions except water-gas shift which" " has 0 degree approach to equilibrium." " 28. Added cross exchanging to cool MAR outlet stream with MAR inlet" " stream." " 29. Added heat stream from REQUIL reactor used in A400MAR block to" " account for heat from reaction." " 30. Reactor conversions changed from earlier cases." " 31. Added split blocks in steam cycle turbine area to permit steam to" " be bypassed around turbines and as a steam take-off location." "SP0609D; 13 Sept 2006: Modified 2012 $1.07 case" " 1. Added syngas bypasses to divert syngas from pre-reformer," " post reformer, and post-amine streams to fuel block in A-200." " 2. Put char combustion and associated blocks into own Hierarchy A-202." " 3. Renamed stream 531 to 571 to match stream ID inside A500. Rename" " stream 10 to 574." " 4. Reroute wet alcohol stream used to flush mol sieve from fuel use" " to feed into MAS reactor R410." " " "SP0609C1; 12 Sept 2006: Modified 2012 $1.07 case" " 1. Modified CO2 recycle method to eliminate physical recycle" " stream in simulation. Design spec varies an inlet stream" " to Reformer block" " 2. Removed S-410B. All CO2 removal upstream of MAS reactor" " occurs in S-410 with venting at S-484. Also removed" " CO2SPLT design spec associated with CO2 conc at MAS inlet." "SP0609C; 12 Sept 2006: Modified 2012 $1.07 case" " 1. Renamed blocks and streams in A300 to 300-series names" " 2. Modified Steam and CW requiements for Amine Scrubber" " reboiler and partial condenser" " 3. Changed molsieve electricity req. to scale on water and" " flushing methanol leaving the unit vs. scaling on entire" " wet alcohol stream (sream 514 vs. stream 507)" "SP0609B; 8 Sept 2006: Modified 2012 $1.07 case" " 1. Moved A401 (Fuel) Block into A200 Block and moved Tar Reformer" " and related items from A200 into a newly created A300TR block that" " was then moved into A300 block. Cleaned up block and stream" " positions for improved readability." " 2. Turned off STM1 sequence." " 3. Changed STMAMIN Design spec to use 2000 Btu/lb CO2 removed as" " energy requirement to calculate steam usage. This may still be high" " as some reports mention values about half of this." " 4. Moved calculations in DISTIL block into LPSTMDEM block; DISTIL" " turned off." "J0609A; 6 Sept 2006: Modified 2012 $1.07 case" " 1. TEMPORARILY disconnect stream 484 from A300-S & hide design spec" " CO2AMINE. TEMPORARILY disconnect stream 10 from A500. Set " " compositions & flows for 484 & 10 and CO2 split fraction in " " A400.S-410 to what was there from the previous case. " " 2. Change the steam stream reference in calculator DISTIL from " " A500.580 -> A500.582. " " 3. Replace the column D502 with a simple separator S502." " a. Remove the preheater H-501 & its heat stream from design spec" " QBALANCE (QCOLD4)." " b. Remove the steam side of the reboiler H-502-. Remove steam " " condensate return 511 from global flowsheet & A600." " c. Remove the condenser duty. Remove condenser duty from " " calculator CWDUTY. Remove block B7 & heat stream 12. Remove" " associated exchanger (H-502-CT) & streams from A700." " d. Remove design spec REBOIL. " " e. Remove calculator SEPCOND. " " f. Remove FBD502 & FTD502 from calculator W500. " " g. Remove DD502 & FLD502 from sensitivity MASSFLOW." " h. Remove column D502 & put in flash S502." " 4. Change value of splitter A500.S506 to make a single mixed " " C3OH+ product." " 5. Add FEEDS & FEEDN to MASSFLOW sensitivity." " 6. Fixed the theoretical ethanol yield calculation in the spreadsheet." "-----------------------------------------------------------------------" "J0606AD; 16 June 2006: Modified 2012 $1.07 case " " 1. Move A400.10 to mix with recycled syngas before the CO2/H2S " " rejection unit (S-413). Modify conditions on K-501 & H-505 to " " match those of stream A400.472A." " 2. Change condenser spec on Syngas Stripper (A500.D502) from a " " recovery spec to temperature (110°F). This causes fewer convergence" " problems." "-----------------------------------------------------------------------" "J0606AA; 13 June 2006: 2012 $1.07 case " "Additonal detail to process & model " " 1. Include the heat to vaporize mixed alcohols to total for alcohol" " separation (A500)." " 2. Added gasifier & overall plant efficiencies to the MASSFLOW " " sensitivity block." " 3. Return the molar flows to the report file (needed in various " " spreadsheets used for post-processing)." " 4. Add HIERARCHY in A400 to model the single-pass alcohol conversion." " 5. Modify power calculation in W500 to take into account all product " " pumps & the reflux/bottoms pumps for the distillation columns." "-----------------------------------------------------------------------" "J0605AD; 31 May 2006: 2012 $1.07 case " "Add detail to the alcohol separation section (A500) " " 1. Replace A500 first separator (S-502) with RADFRAC column (D502)." " Only use a condenser to control the amount of methanol washed down" " to the separation process." " 2. Add a HIERARCHY block for the mole sieve. Let the stream to flush" " the water out be general. Remove the DESIGN SPECS MOLSIV & " " MOLSIV2." " 3. Add in the remaining alcohol separation columns (D504, D505, D506," " & D507). Connect all reboiler duties to determine steam usage." " Connect all condensers for cooling water calculations. Specify" " fairly loose recoveries for the higher alcohols to make sure that" " they will converge." " 4. Update estimates for recycle streams A300.315, " " & A400.485 in attempt to speed up execution. " " 5. Remove the molar flows from the report file." "-----------------------------------------------------------------------" "J0605AA_GUI; 15 May 2006: 2012 $1.07 case for 30X30 Support " "Move operations into HIERARCHY blocks. " " 1. Move heat of combustion calculations into HIERARCHY blocks HV-101, " " HV-224, HV-427, HV474, & HV-475." " 2. Move all other operations into process sections (A100, A200, etc.)." " 3. Change SECTION for HX100B from GLOBAL to STEAM." "-----------------------------------------------------------------------" "J0603AA_GUI; 27 March 2006: 2012 $1.07 case for 30X30 Support " "Starting model: ps0601a_BmaG_rec_MAR_2013_etoh " " " " 1. Update estimates for recycle streams 315, 463, 465, & 485 to " " speed up execution. " " 2. Set total simulation time to 20,000 seconds. " " 3. Add separator block B5 to split the alcohols into separate " " streams. Put these blocks into the ALCOHL flowsheet section." " 4. Tighten tolerance in QBALANCE 10 -> 1." "-----------------------------------------------------------------------" " " " *****PARAMETER VALUES IN USE***** " " 2 HHVEFF" " 3 LHVEFF" " 4 GASHHV" " 5 GASLHV" " 6 INHHV" " 7 INLHV" " " ) \ ? DATABANKS ? \ DATABANKS FILE-SYM-NAM = ( ASPENPCD PURE10 AQUEOUS SOLIDS INORGANIC PURE12 ) \ ? COMPONENTS MAIN ? \ COMPONENTS CID = H2 ANAME = H2 OUTNAME = H2 TYPE = CONV DBNAME1 = "HYDROGEN" ANAME1 = "H2" / CID = CO ANAME = CO OUTNAME = CO TYPE = CONV DBNAME1 = "CARBON-MONOXIDE" ANAME1 = "CO" / CID = N2 ANAME = N2 OUTNAME = N2 TYPE = CONV DBNAME1 = "NITROGEN" ANAME1 = "N2" / CID = O2 ANAME = O2 OUTNAME = O2 TYPE = CONV DBNAME1 = "OXYGEN" ANAME1 = "O2" / CID = AR ANAME = AR OUTNAME = AR TYPE = CONV DBNAME1 = "ARGON" ANAME1 = "AR" / CID = CO2 ANAME = CO2 OUTNAME = CO2 TYPE = CONV DBNAME1 = "CARBON-DIOXIDE" ANAME1 = "CO2" / CID = H2O ANAME = H2O OUTNAME = H2O TYPE = CONV DBNAME1 = "WATER" ANAME1 = "H2O" / CID = H2S ANAME = H2S OUTNAME = H2S TYPE = CONV DBNAME1 = "HYDROGEN-SULFIDE" ANAME1 = "H2S" / CID = SO2 ANAME = O2S OUTNAME = SO2 TYPE = CONV DBNAME1 = "SULFUR-DIOXIDE" ANAME1 = "O2S" / CID = NH3 ANAME = H3N OUTNAME = NH3 TYPE = CONV DBNAME1 = "AMMONIA" ANAME1 = "H3N" / CID = NO2 ANAME = NO2 OUTNAME = NO2 TYPE = CONV DBNAME1 = "NITROGEN-DIOXIDE" ANAME1 = "NO2" / CID = CH4 ANAME = CH4 OUTNAME = CH4 TYPE = CONV DBNAME1 = "METHANE" ANAME1 = "CH4" / CID = C2H6 ANAME = C2H6 OUTNAME = C2H6 TYPE = CONV DBNAME1 = "ETHANE" ANAME1 = "C2H6" / CID = C2H4 ANAME = C2H4 OUTNAME = C2H4 TYPE = CONV DBNAME1 = "ETHYLENE" ANAME1 = "C2H4" / CID = C2H2 ANAME = C2H2 OUTNAME = C2H2 TYPE = CONV DBNAME1 = "ACETYLENE" ANAME1 = "C2H2" / CID = C3H8 ANAME = C3H8 OUTNAME = C3H8 TYPE = CONV DBNAME1 = "PROPANE" ANAME1 = "C3H8" / CID = "I-C4H10" ANAME = C4H10-2 OUTNAME = "I-C4H10" TYPE = CONV DBNAME1 = "ISOBUTANE" ANAME1 = "C4H10-2" / CID = "N-C4H10" ANAME = C4H10-1 OUTNAME = "N-C4H10" TYPE = CONV DBNAME1 = "N-BUTANE" ANAME1 = "C4H10-1" / CID = "PENTANE+" ANAME = C5H12-1 OUTNAME = "PENTANE+" TYPE = CONV DBNAME1 = "N-PENTANE" ANAME1 = "C5H12-1" / CID = C6H6 ANAME = C6H6 OUTNAME = C6H6 TYPE = CONV DBNAME1 = "BENZENE" ANAME1 = "C6H6" / CID = C10H8 ANAME = C10H8 OUTNAME = C10H8 TYPE = CONV DBNAME1 = "NAPHTHALENE" ANAME1 = "C10H8" / CID = CARBON ANAME = C OUTNAME = CARBON TYPE = SOLID DBNAME1 = "CARBON-GRAPHITE" ANAME1 = "C" / CID = SULFUR ANAME = S OUTNAME = SULFUR TYPE = SOLID DBNAME1 = "SULFUR" ANAME1 = "S" / CID = OLIVINE ANAME = SIO2 OUTNAME = OLIVINE TYPE = SOLID DBNAME1 = "SILICON-DIOXIDE" ANAME1 = "SIO2" / CID = WOOD OUTNAME = WOOD TYPE = NC / CID = ASH OUTNAME = ASH TYPE = NC / CID = CHAR OUTNAME = CHAR TYPE = NC / CID = "NH4+" ANAME = NH4+ OUTNAME = "NH4+" DBNAME1 = "NH4+" ANAME1 = "NH4+" / CID = "H3O+" ANAME = H3O+ OUTNAME = "H3O+" DBNAME1 = "H3O+" ANAME1 = "H3O+" / CID = "NH2COO-" ANAME = NH2COO- OUTNAME = "NH2COO-" DBNAME1 = "CARBAMATE" ANAME1 = "NH2COO-" / CID = "OH-" ANAME = OH- OUTNAME = "OH-" DBNAME1 = "OH-" ANAME1 = "OH-" / CID = "HCO3-" ANAME = HCO3- OUTNAME = "HCO3-" DBNAME1 = "HCO3-" ANAME1 = "HCO3-" / CID = "HS-" ANAME = HS- OUTNAME = "HS-" DBNAME1 = "HS-" ANAME1 = "HS-" / CID = "CO3--" ANAME = CO3-2 OUTNAME = "CO3--" DBNAME1 = "CO3--" ANAME1 = "CO3-2" / CID = "S--" ANAME = S-2 OUTNAME = "S--" DBNAME1 = "S--" ANAME1 = "S-2" / CID = METHANOL ANAME = CH4O OUTNAME = METHANOL DBNAME1 = "METHANOL" ANAME1 = "CH4O" / CID = ETHANOL ANAME = C2H6O-2 OUTNAME = ETHANOL TYPE = CONV DBNAME1 = "ETHANOL" ANAME1 = "C2H6O-2" / CID = PROPANOL ANAME = C3H8O-1 OUTNAME = PROPANOL TYPE = CONV DBNAME1 = "1-PROPANOL" ANAME1 = "C3H8O-1" / CID = NBUTANOL ANAME = C4H10O-1 OUTNAME = NBUTANOL DBNAME1 = "N-BUTANOL" ANAME1 = "C4H10O-1" / CID = PENTANOL ANAME = C5H12O-1 OUTNAME = PENTANOL DBNAME1 = "1-PENTANOL" ANAME1 = "C5H12O-1" / CID = AMINE ANAME = C2H7NO OUTNAME = AMINE TYPE = CONV DBNAME1 = "MONOETHANOLAMINE" ANAME1 = "C2H7NO" \ \ NONCONVS \ ? COMPONENTS "HENRY-COMPS" AMINE ? \ "HENRY-COMPS" CID = ( CO2 H2S SO2 NH3 H2 O2 N2 ) \ ? COMPONENTS "HENRY-COMPS" "HC-1" ? \ "HENRY-COMPS" CID = ( H2 CO CO2 CH4 C2H6 C2H4 C2H2 O2 N2 ) \ ? COMPONENTS "HENRY-COMPS" SOURHENR ? \ "HENRY-COMPS" CID = ( CO2 H2S SO2 NH3 H2 O2 N2 ) \ ? COMPONENTS "COMP-LIST" GLOBAL ? ? SOLVE ? ? CHEMISTRY SOURCHEM ? ; "ENG_MOLE" ; \ STOIC REACNO = 1 STOIC-CID = H2O COEF = -2 <0> <0> / REACNO = 2 STOIC-CID = H2S COEF = -1 <0> <0> / REACNO = 2 STOIC-CID = H2O COEF = -1 <0> <0> / REACNO = 3 STOIC-CID = "HS-" COEF = -1 <0> <0> / REACNO = 3 STOIC-CID = H2O COEF = -1 <0> <0> / REACNO = 4 STOIC-CID = CO2 COEF = -1 <0> <0> / REACNO = 4 STOIC-CID = H2O COEF = -2 <0> <0> / REACNO = 5 STOIC-CID = "HCO3-" COEF = -1 <0> <0> / REACNO = 5 STOIC-CID = H2O COEF = -1 <0> <0> / REACNO = 6 STOIC-CID = NH3 COEF = -1 <0> <0> / REACNO = 6 STOIC-CID = H2O COEF = -1 <0> <0> / REACNO = 7 STOIC-CID = NH3 COEF = -1 <0> <0> / REACNO = 7 STOIC-CID = "HCO3-" COEF = -1 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = "H3O+" COEF1 = 1 <0> <0> / REACNO1 = 1 STOIC-CID1 = "OH-" COEF1 = 1 <0> <0> / REACNO1 = 2 STOIC-CID1 = "H3O+" COEF1 = 1 <0> <0> / REACNO1 = 2 STOIC-CID1 = "HS-" COEF1 = 1 <0> <0> / REACNO1 = 3 STOIC-CID1 = "H3O+" COEF1 = 1 <0> <0> / REACNO1 = 3 STOIC-CID1 = "S--" COEF1 = 1 <0> <0> / REACNO1 = 4 STOIC-CID1 = "H3O+" COEF1 = 1 <0> <0> / REACNO1 = 4 STOIC-CID1 = "HCO3-" COEF1 = 1 <0> <0> / REACNO1 = 5 STOIC-CID1 = "H3O+" COEF1 = 1 <0> <0> / REACNO1 = 5 STOIC-CID1 = "CO3--" COEF1 = 1 <0> <0> / REACNO1 = 6 STOIC-CID1 = "NH4+" COEF1 = 1 <0> <0> / REACNO1 = 6 STOIC-CID1 = "OH-" COEF1 = 1 <0> <0> / REACNO1 = 7 STOIC-CID1 = "NH2COO-" COEF1 = 1 <0> <0> / REACNO1 = 7 STOIC-CID1 = H2O COEF1 = 1 <0> <0> \ \ K-STOIC K-S-REACNO = 1 A = 132.89888 <0> <0> B = -13445.9 <0> <0> C = -22.4773 <0> <0> D = 0 <0> <0> \ \ K-STOIC K-S-REACNO = 2 A = 214.582443 <0> <0> B = -12995.4 <0> <0> C = -33.5471 <0> <0> D = 0 <0> <0> \ \ K-STOIC K-S-REACNO = 3 A = -9.741963 <0> <0> B = -8585.47 <0> <0> C = 0 <0> <0> D = 0 <0> <0> \ \ K-STOIC K-S-REACNO = 4 A = 231.465439 <0> <0> B = -12092.1 <0> <0> C = -36.7816 <0> <0> D = 0 <0> <0> \ \ K-STOIC K-S-REACNO = 5 A = 216.05043 <0> <0> B = -12431.7 <0> <0> C = -35.4819 <0> <0> D = 0 <0> <0> \ \ K-STOIC K-S-REACNO = 6 A = -1.256563 <0> <0> B = -3335.7 <0> <0> C = 1.4971 <0> <0> D = -0.0370566 <0> <0> \ \ K-STOIC K-S-REACNO = 7 A = -4.583437 <0> <0> B = 2900 <0> <0> C = 0 <0> <0> D = 0 <0> <0> \ \ ALLREACT RXNID = "1" RXNSTRING = "2 H2O <--> H3O+ + OH-" RXNTYPE = "Equilibrium" / RXNID = "2" RXNSTRING = "H2S + H2O <--> H3O+ + HS-" RXNTYPE = "Equilibrium" / RXNID = "3" RXNSTRING = "HS- + H2O <--> H3O+ + S--" RXNTYPE = "Equilibrium" / RXNID = "4" RXNSTRING = "CO2 + 2 H2O <--> H3O+ + HCO3-" RXNTYPE = "Equilibrium" / RXNID = "5" RXNSTRING = "HCO3- + H2O <--> H3O+ + CO3--" RXNTYPE = "Equilibrium" / RXNID = "6" RXNSTRING = "NH3 + H2O <--> NH4+ + OH-" RXNTYPE = "Equilibrium" / RXNID = "7" RXNSTRING = "NH3 + HCO3- <--> NH2COO- + H2O" RXNTYPE = "Equilibrium" \ ? FLOWSHEET GLOBAL ? \ BLOCK BLKID = A100 BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-13" IN = ( 100 M3-0 ) OUT = ( "A100.100" M3-0 ) \ \ CONNECT BLKID = "$C-27" IN = ( 287 M4-0 ) OUT = ( "A100.287" M4-0 ) \ \ CONNECT BLKID = "$C-65" IN = ( 335 M5-0 ) OUT = ( "A100.335" M5-0 ) \ \ CONNECT BLKID = "$C-12" IN = ( "A100.105" M6-0 ) OUT = ( 105 M3-0 ) \ \ CONNECT BLKID = "$C-2" IN = ( "A100.112" M7-0 ) OUT = ( 112 M4-0 ) \ \ BLOCK BLKID = A200 BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-28" IN = ( 105 M3-0 ) OUT = ( "A200.105" M3-0 ) \ \ CONNECT BLKID = "$C-26" IN = ( 200 M4-0 ) OUT = ( "A200.200" M4-0 ) \ \ CONNECT BLKID = "$C-23" IN = ( 206 M5-0 ) OUT = ( "A200.206" M5-0 ) \ \ CONNECT BLKID = "$C-18" IN = ( 220 M6-0 ) OUT = ( "A200.220" M6-0 ) \ \ CONNECT BLKID = "$C-1" IN = ( 221 M7-0 ) OUT = ( "A200.221" M7-0 ) \ \ CONNECT BLKID = "$C-15" IN = ( "A200.219" M8-0 ) OUT = ( 219 M3-0 ) \ \ CONNECT BLKID = "$C-14" IN = ( "A200.225A" M9-0 ) OUT = ( 225A M4-0 ) \ \ CONNECT BLKID = "$C-9" IN = ( "A200.287" M10-0 ) OUT = ( 287 M5-0 ) \ \ CONNECT BLKID = "$C-37" IN = ( "A200.225F" M11-0 ) OUT = ( 225F M6-0 ) \ \ BLOCK BLKID = A300 BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-4" IN = ( 225A M3-0 ) OUT = ( "A300.225A" M3-0 ) \ \ CONNECT BLKID = "$C-21" IN = ( 322 M4-0 ) OUT = ( "A300.322" M4-0 ) \ \ CONNECT BLKID = "$C-24" IN = ( 463 M5-0 ) OUT = ( "A300.463" M5-0 ) \ \ CONNECT BLKID = "$C-3" IN = ( 513 M6-0 ) OUT = ( "A300.513" M6-0 ) \ \ CONNECT BLKID = "$C-34" IN = ( 225F M7-0 ) OUT = ( "A300.225F" M7-0 ) \ \ CONNECT BLKID = "$C-40" IN = ( 426 M8-0 ) OUT = ( "A300.426" M8-0 ) \ \ CONNECT BLKID = "$C-19" IN = ( "A300.305" M9-0 ) OUT = ( 305 M3-0 ) \ \ CONNECT BLKID = "$C-31" IN = ( "A300.314" M10-0 ) OUT = ( 314 M4-0 ) \ \ CONNECT BLKID = "$C-20" IN = ( "A300.324" M11-0 ) OUT = ( 324 M5-0 ) \ \ CONNECT BLKID = "$C-30" IN = ( "A300.361" M12-0 ) OUT = ( 361 M6-0 ) \ \ CONNECT BLKID = "$C-29" IN = ( "A300.362" M13-0 ) OUT = ( 362 M7-0 ) \ \ CONNECT BLKID = "$C-38" IN = ( "A300.WK301" W14-0 ) OUT = ( WK301 W8-0 ) \ \ CONNECT BLKID = "$C-62" IN = ( "A300.351" M15-0 ) OUT = ( 351 M9-0 ) \ \ CONNECT BLKID = "$C-25" IN = ( "A300.335" M16-0 ) OUT = ( 335 M10-0 ) \ \ CONNECT BLKID = "$C-8" IN = ( "A300.395" M17-0 ) OUT = ( 395 M11-0 ) \ \ BLOCK BLKID = A400 BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-45" IN = ( 362 M3-0 ) OUT = ( "A400.362" M3-0 ) \ \ CONNECT BLKID = "$C-36" IN = ( 515 M4-0 ) OUT = ( "A400.515" M4-0 ) \ \ CONNECT BLKID = "$C-5" IN = ( "A400.503" M5-0 ) OUT = ( 503 M3-0 ) \ \ CONNECT BLKID = "$C-33" IN = ( "A400.463" M6-0 ) OUT = ( 463 M4-0 ) \ \ CONNECT BLKID = "$C-58" IN = ( "A400.WK410" W7-0 ) OUT = ( WK410 W5-0 ) \ \ CONNECT BLKID = "$C-7" IN = ( "A400.426" M8-0 ) OUT = ( 426 M6-0 ) \ \ CONNECT BLKID = "$C-17" IN = ( "A400.WK412" W9-0 ) OUT = ( WK412 W7-0 ) \ \ BLOCK BLKID = A500 BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-42" IN = ( 503 M3-0 ) OUT = ( "A500.503" M3-0 ) \ \ CONNECT BLKID = "$C-41" IN = ( "A500.536" M4-0 ) OUT = ( 536 M3-0 ) \ \ CONNECT BLKID = "$C-10" IN = ( "A500.592" M5-0 ) OUT = ( 592 M4-0 ) \ \ CONNECT BLKID = "$C-11" IN = ( "A500.590" M6-0 ) OUT = ( 590 M5-0 ) \ \ CONNECT BLKID = "$C-32" IN = ( "A500.515" M7-0 ) OUT = ( 515 M6-0 ) \ \ CONNECT BLKID = "$C-6" IN = ( "A500.513" M8-0 ) OUT = ( 513 M7-0 ) \ \ BLOCK BLKID = A600 BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-55" IN = ( 635 M3-0 ) OUT = ( "A600.635" M3-0 ) \ \ CONNECT BLKID = "$C-49" IN = ( 536 M4-0 ) OUT = ( "A600.536" M4-0 ) \ \ CONNECT BLKID = "$C-48" IN = ( 618 M5-0 ) OUT = ( "A600.618" M5-0 ) \ \ CONNECT BLKID = "$C-51" IN = ( 314 M6-0 ) OUT = ( "A600.314" M6-0 ) \ \ CONNECT BLKID = "$C-47" IN = ( 361 M7-0 ) OUT = ( "A600.361" M7-0 ) \ \ CONNECT BLKID = "$C-50" IN = ( WK301 W8-0 ) OUT = ( "A600.WK301" W8-0 ) \ \ CONNECT BLKID = "$C-59" IN = ( WK410 W9-0 ) OUT = ( "A600.WK410" W9-0 ) \ \ CONNECT BLKID = "$C-63" IN = ( 351 M10-0 ) OUT = ( "A600.351" M10-0 ) \ \ CONNECT BLKID = "$C-16" IN = ( 395 M11-0 ) OUT = ( "A600.395" M11-0 ) \ \ CONNECT BLKID = "$C-22" IN = ( WK412 W12-0 ) OUT = ( "A600.WK412" W12-0 ) \ \ CONNECT BLKID = "$C-56" IN = ( "A600.634" M13-0 ) OUT = ( 634 M3-0 ) \ \ CONNECT BLKID = "$C-44" IN = ( "A600.600" M14-0 ) OUT = ( 600 M4-0 ) \ \ CONNECT BLKID = "$C-39" IN = ( "A600.WM602SFT" W15-0 ) OUT = ( WM602SFT W5-0 ) \ \ BLOCK BLKID = A700 BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-57" IN = ( 711 M3-0 ) OUT = ( "A700.711" M3-0 ) \ \ CONNECT BLKID = "$C-54" IN = ( 710 M4-0 ) OUT = ( "A700.710" M4-0 ) \ \ CONNECT BLKID = "$C-53" IN = ( 600 M5-0 ) OUT = ( "A700.600" M5-0 ) \ \ BLOCK BLKID = A900 BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-46" IN = ( "A900.WNET" W3-0 ) OUT = ( WNET W3-0 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? FLOWSHEET STEAM ? \ BLOCK BLKID = AREFRNC BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ ? PROPERTIES MAIN ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ \ PROPERTIES SECID-LIST = STEAM BASEOPSET = "STEAM-TA" OPSETNAME = "STEAM-TA" \ ? PROPERTIES "OPTION-SETS" AMINES ? \ PARAM BASE = AMINES \ ? PROPERTIES "OPTION-SETS" ELECNRTL ? \ PARAM BASE = ELECNRTL \ ? PROPERTIES "OPTION-SETS" NRTL ? \ PARAM BASE = NRTL \ ? PROPERTIES "OPTION-SETS" "PENG-ROB" ? \ PARAM BASE = "PENG-ROB" \ ? PROPERTIES "OPTION-SETS" "PR-BM" ? \ PARAM BASE = "PR-BM" \ ? PROPERTIES "OPTION-SETS" "RKS-BM" ? \ PARAM BASE = "RKS-BM" \ ? PROPERTIES "OPTION-SETS" SOLIDS ? \ PARAM BASE = SOLIDS \ ? PROPERTIES "OPTION-SETS" SYSOP3 ? \ PARAM BASE = "RKS-BM" \ ? PROPERTIES "NC-PROPS" ? \ ATTR-COMPS COMP = WOOD TYPE-LIST = ( ULTANAL SULFANAL PROXANAL ) ENTH-MODEL = HCOALGEN EOPCODE = ( 1 1 1 1 ) DENS-MODEL = DCOALIGT NTBSYM = WOOD \ \ ATTR-COMPS COMP = ASH TYPE-LIST = ( GENANAL PROXANAL ULTANAL SULFANAL ) ENTH-MODEL = HCOALGEN EOPCODE = ( 1 1 1 1 ) DENS-MODEL = DNSTYGEN NTBSYM = ASH \ \ ATTR-COMPS COMP = CHAR TYPE-LIST = ( ULTANAL SULFANAL PROXANAL ) ENTH-MODEL = HCOALGEN EOPCODE = ( 1 1 1 1 ) DENS-MODEL = DCHARIGT NTBSYM = CHAR \ ? PROPERTIES "MOLEC-STRUCT" AMINE ? ? PROPERTIES "MOLEC-STRUCT" AR ? ? PROPERTIES "MOLEC-STRUCT" C2H2 ? ? PROPERTIES "MOLEC-STRUCT" C2H4 ? ? PROPERTIES "MOLEC-STRUCT" C2H6 ? ? PROPERTIES "MOLEC-STRUCT" C3H8 ? ? PROPERTIES "MOLEC-STRUCT" C6H6 ? ? PROPERTIES "MOLEC-STRUCT" C10H8 ? ? PROPERTIES "MOLEC-STRUCT" CARBON ? ? PROPERTIES "MOLEC-STRUCT" CH4 ? ? PROPERTIES "MOLEC-STRUCT" CO ? ? PROPERTIES "MOLEC-STRUCT" CO2 ? ? PROPERTIES "MOLEC-STRUCT" "CO3--" ? ? PROPERTIES "MOLEC-STRUCT" ETHANOL ? ? PROPERTIES "MOLEC-STRUCT" H2 ? ? PROPERTIES "MOLEC-STRUCT" H2O ? ? PROPERTIES "MOLEC-STRUCT" H2S ? ? PROPERTIES "MOLEC-STRUCT" "H3O+" ? ? PROPERTIES "MOLEC-STRUCT" "HCO3-" ? ? PROPERTIES "MOLEC-STRUCT" "HS-" ? ? PROPERTIES "MOLEC-STRUCT" "I-C4H10" ? ? PROPERTIES "MOLEC-STRUCT" METHANOL ? ? PROPERTIES "MOLEC-STRUCT" "N-C4H10" ? ? PROPERTIES "MOLEC-STRUCT" N2 ? ? PROPERTIES "MOLEC-STRUCT" NBUTANOL ? ? PROPERTIES "MOLEC-STRUCT" "NH2COO-" ? ? PROPERTIES "MOLEC-STRUCT" NH3 ? ? PROPERTIES "MOLEC-STRUCT" "NH4+" ? ? PROPERTIES "MOLEC-STRUCT" NO2 ? ? PROPERTIES "MOLEC-STRUCT" O2 ? ? PROPERTIES "MOLEC-STRUCT" "OH-" ? ? PROPERTIES "MOLEC-STRUCT" OLIVINE ? ? PROPERTIES "MOLEC-STRUCT" "PENTANE+" ? ? PROPERTIES "MOLEC-STRUCT" PENTANOL ? ? PROPERTIES "MOLEC-STRUCT" PROPANOL ? ? PROPERTIES "MOLEC-STRUCT" "S--" ? ? PROPERTIES "MOLEC-STRUCT" SO2 ? ? PROPERTIES "MOLEC-STRUCT" SULFUR ? ? PROPERTIES PARAMETERS UNARY SCALAR PO3DATA1 ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = DGSFRM SETNO = 1 UNITROW = 39 UNITLABEL = "Btu/lbmol" / PARAMNAME = DHSFRM SETNO = 1 UNITROW = 39 UNITLABEL = "Btu/lbmol" / PARAMNAME = MW SETNO = 1 UNITROW = 0 \ \ PVAL PARAMNAME2 = DGSFRM CID = OLIVINE UVALUE = 0 <0> <0> \ \ PVAL PARAMNAME2 = DGSFRM CID = CARBON UVALUE = 0 <0> <0> \ \ PVAL PARAMNAME2 = DGSFRM CID = SULFUR UVALUE = 0 <0> <0> \ \ PVAL PARAMNAME2 = DHSFRM CID = OLIVINE UVALUE = 0 <0> <0> \ \ PVAL PARAMNAME2 = DHSFRM CID = CARBON UVALUE = 0 <0> <0> \ \ PVAL PARAMNAME2 = DHSFRM CID = SULFUR UVALUE = 0 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = OLIVINE UVALUE = 60.086 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = CARBON UVALUE = 12.011 <0> <0> \ \ PVAL PARAMNAME2 = MW CID = SULFUR UVALUE = 32.064 <0> <0> \ ? PROPERTIES PARAMETERS UNARY "T-DEPENDENT" "CPSPO1-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = CPSPO1 SETNO = 1 UNITROW = 15 UNITLABEL = "Btu/lbmol-R" TUNITROW = 22 TUNITLABEL = F NEL = 8 \ \ PVAL PARAMNAME2 = CPSPO1 CID = CARBON UNITROW2 = 15 UNITLABEL2 = "cal/mol-K" TUNITROW2 = 22 TUNITLABEL2 = K NEL2 = 8 UVAL1 = 2.673 <0> <0> UVAL2 = 0.002617 <0> <0> UVAL3 = 0 <0> <0> UVAL4 = 0 <0> <0> UVAL5 = -116900 <0> <0> UVAL6 = 0 <0> <0> UVAL7 = 273 <0> <0> UVAL8 = 1373 <0> <0> \ \ PVAL PARAMNAME2 = CPSPO1 CID = OLIVINE UNITROW2 = 15 UNITLABEL2 = "cal/mol-K" TUNITROW2 = 22 TUNITLABEL2 = K NEL2 = 8 UVAL1 = 12.8 <0> <0> UVAL2 = 0.00447 <0> <0> UVAL3 = 0 <0> <0> UVAL4 = 0 <0> <0> UVAL5 = -302000 <0> <0> UVAL6 = 0 <0> <0> UVAL7 = 273 <0> <0> UVAL8 = 1973 <0> <0> \ \ PVAL PARAMNAME2 = CPSPO1 CID = SULFUR UNITROW2 = 15 UNITLABEL2 = "cal/mol-K" TUNITROW2 = 22 TUNITLABEL2 = K NEL2 = 8 UVAL1 = 3.63 <0> <0> UVAL2 = 0.0064 <0> <0> UVAL3 = 0 <0> <0> UVAL4 = 0 <0> <0> UVAL5 = 0 <0> <0> UVAL6 = 0 <0> <0> UVAL7 = 0 <0> <0> UVAL8 = 1000 <0> <0> \ ? PROPERTIES PARAMETERS UNARY "T-DEPENDENT" "VSPOLY-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = VSPOLY SETNO = 1 UNITROW = 43 UNITLABEL = "cuft/lbmol" TUNITROW = 22 TUNITLABEL = F NEL = 7 \ \ PVAL PARAMNAME2 = VSPOLY CID = CARBON UNITROW2 = 43 UNITLABEL2 = "cum/kmol" TUNITROW2 = 22 TUNITLABEL2 = F NEL2 = 7 UVAL1 = 0.00534 <0> <0> UVAL2 = 0 <0> <0> UVAL3 = 0 <0> <0> UVAL4 = 0 <0> <0> UVAL5 = 0 <0> <0> UVAL6 = 0 <0> <0> UVAL7 = 2500 <0> <0> \ \ PVAL PARAMNAME2 = VSPOLY CID = SULFUR UNITROW2 = 43 UNITLABEL2 = "cum/kmol" TUNITROW2 = 22 TUNITLABEL2 = F NEL2 = 7 UVAL1 = 0.01550 <0> <0> UVAL2 = 0 <0> <0> UVAL3 = 0 <0> <0> UVAL4 = 0 <0> <0> UVAL5 = 0 <0> <0> UVAL6 = 0 <0> <0> UVAL7 = 2500 <0> <0> \ ? PROPERTIES PARAMETERS UNARY "NC-PARAMS" "PO3U-2" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = DENGEN UNITROW = 38 UNITLABEL = "kg/cum" TUNITROW = 22 TUNITLABEL = K NEL = 80 \ \ PVAL PARAMNAME2 = DENGEN CID = ASH VAL = ( 2000. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ ? PROPERTIES PARAMETERS BINARY SCALAR "GMSHXL-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = GMSHXL SETNO = 1 UNITROW = 0 \ ? PROPERTIES PARAMETERS BINARY SCALAR "HOCETA-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = HOCETA SETNO = 1 UNITROW = 0 \ ? PROPERTIES PARAMETERS BINARY SCALAR "RKTKIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = RKTKIJ SETNO = 1 UNITROW = 0 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "ANDKIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = ANDKIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F NEL = 2 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "ANDMIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = ANDMIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F NEL = 2 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "HENRY-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = HENRY SETNO = 1 UNITROW = 20 UNITLABEL = psi TUNITROW = 22 TUNITLABEL = F BDBANK = ( "ENRTL-RK" BINARY HENRY ) NEL = 7 \ \ BPVAL PARAMNAME2 = HENRY CID1 = H2 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = BINARY VAL2 = BINARY VAL3 = BINARY VAL4 = BINARY VAL5 = BINARY VAL6 = BINARY VAL7 = BINARY / PARAMNAME2 = HENRY CID1 = H2 CID2 = NH3 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2 CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2 CID2 = "PENTANE+" UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = O2 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = BINARY VAL2 = BINARY VAL3 = BINARY VAL4 = BINARY VAL5 = BINARY VAL6 = BINARY VAL7 = BINARY / PARAMNAME2 = HENRY CID1 = O2 CID2 = NH3 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = O2 CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = N2 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = BINARY VAL2 = BINARY VAL3 = BINARY VAL4 = BINARY VAL5 = BINARY VAL6 = BINARY VAL7 = BINARY / PARAMNAME2 = HENRY CID1 = N2 CID2 = NH3 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = N2 CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = N2 CID2 = "PENTANE+" UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO2 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ENRTL-RK VAL2 = ENRTL-RK VAL3 = ENRTL-RK VAL4 = ENRTL-RK VAL5 = ENRTL-RK VAL6 = ENRTL-RK VAL7 = ENRTL-RK / PARAMNAME2 = HENRY CID1 = CO2 CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO2 CID2 = "PENTANE+" UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = BINARY VAL2 = BINARY VAL3 = BINARY VAL4 = BINARY VAL5 = BINARY VAL6 = BINARY VAL7 = BINARY / PARAMNAME2 = HENRY CID1 = CO CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO CID2 = "PENTANE+" UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CH4 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = BINARY VAL2 = BINARY VAL3 = BINARY VAL4 = BINARY VAL5 = BINARY VAL6 = BINARY VAL7 = BINARY / PARAMNAME2 = HENRY CID1 = H2S CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ENRTL-RK VAL2 = ENRTL-RK VAL3 = ENRTL-RK VAL4 = ENRTL-RK VAL5 = ENRTL-RK VAL6 = ENRTL-RK VAL7 = ENRTL-RK / PARAMNAME2 = HENRY CID1 = NH3 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ENRTL-RK VAL2 = ENRTL-RK VAL3 = ENRTL-RK VAL4 = ENRTL-RK VAL5 = ENRTL-RK VAL6 = ENRTL-RK VAL7 = ENRTL-RK / PARAMNAME2 = HENRY CID1 = SO2 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ENRTL-RK VAL2 = ENRTL-RK VAL3 = ENRTL-RK VAL4 = ENRTL-RK VAL5 = ENRTL-RK VAL6 = ENRTL-RK VAL7 = ENRTL-RK / PARAMNAME2 = HENRY CID1 = C2H6 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = BINARY VAL2 = BINARY VAL3 = BINARY VAL4 = BINARY VAL5 = BINARY VAL6 = BINARY VAL7 = BINARY / PARAMNAME2 = HENRY CID1 = C2H4 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = BINARY VAL2 = BINARY VAL3 = BINARY VAL4 = BINARY VAL5 = BINARY VAL6 = BINARY VAL7 = BINARY / PARAMNAME2 = HENRY CID1 = C2H2 CID2 = H2O UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = BINARY VAL2 = BINARY VAL3 = BINARY VAL4 = BINARY VAL5 = BINARY VAL6 = BINARY VAL7 = BINARY / PARAMNAME2 = HENRY CID1 = CH4 CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CH4 CID2 = "PENTANE+" UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2S CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2S CID2 = "PENTANE+" UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = NH3 CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = SO2 CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = SO2 CID2 = "PENTANE+" UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H6 CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H4 CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H2 CID2 = C6H6 UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H6 CID2 = "PENTANE+" UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H4 CID2 = "PENTANE+" UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2 CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = N2 CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = O2 CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO2 CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2S CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = SO2 CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = NH3 CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CH4 CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H6 CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H4 CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H2 CID2 = METHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2 CID2 = NBUTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO CID2 = NBUTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = N2 CID2 = NBUTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = O2 CID2 = NBUTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO2 CID2 = NBUTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2S CID2 = NBUTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = NH3 CID2 = NBUTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CH4 CID2 = NBUTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H6 CID2 = NBUTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H4 CID2 = NBUTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = N2 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = O2 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO2 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = SO2 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = NH3 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CH4 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H6 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H4 CID2 = ETHANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2 CID2 = PROPANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO CID2 = PROPANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = N2 CID2 = PROPANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = O2 CID2 = PROPANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO2 CID2 = PROPANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CH4 CID2 = PROPANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H6 CID2 = PROPANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H4 CID2 = PROPANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = H2 CID2 = PENTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO CID2 = PENTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = N2 CID2 = PENTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = O2 CID2 = PENTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CO2 CID2 = PENTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = CH4 CID2 = PENTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H6 CID2 = PENTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY / PARAMNAME2 = HENRY CID1 = C2H4 CID2 = PENTANOL UNITROW2 = 20 UNITLABEL2 = psi TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = HENRY VAL2 = HENRY VAL3 = HENRY VAL4 = HENRY VAL5 = HENRY VAL6 = HENRY VAL7 = HENRY \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "NRTL-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = NRTL SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F BDBANK = ( "ENRTL-RK" ) NEL = 12 \ \ BPVAL PARAMNAME2 = NRTL CID1 = CO2 CID2 = H2O UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ENRTL-RK VAL2 = ENRTL-RK VAL3 = ENRTL-RK VAL4 = ENRTL-RK VAL5 = ENRTL-RK VAL6 = ENRTL-RK VAL7 = ENRTL-RK VAL8 = ENRTL-RK VAL9 = ENRTL-RK VAL10 = ENRTL-RK VAL11 = ENRTL-RK VAL12 = ENRTL-RK / PARAMNAME2 = NRTL CID1 = H2O CID2 = H2S UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ENRTL-RK VAL2 = ENRTL-RK VAL3 = ENRTL-RK VAL4 = ENRTL-RK VAL5 = ENRTL-RK VAL6 = ENRTL-RK VAL7 = ENRTL-RK VAL8 = ENRTL-RK VAL9 = ENRTL-RK VAL10 = ENRTL-RK VAL11 = ENRTL-RK VAL12 = ENRTL-RK / PARAMNAME2 = NRTL CID1 = H2O CID2 = NH3 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ENRTL-RK VAL2 = ENRTL-RK VAL3 = ENRTL-RK VAL4 = ENRTL-RK VAL5 = ENRTL-RK VAL6 = ENRTL-RK VAL7 = ENRTL-RK VAL8 = ENRTL-RK VAL9 = ENRTL-RK VAL10 = ENRTL-RK VAL11 = ENRTL-RK VAL12 = ENRTL-RK / PARAMNAME2 = NRTL CID1 = NBUTANOL CID2 = PENTANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F UVAL1 = 17.21350000 <0> <0> UVAL2 = 6.677900000 <0> <0> UVAL3 = -8999.999928 <0> <0> UVAL4 = -5125.185319 <0> <0> UVAL5 = .3000000000 <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 = 178.8440026 <0> <0> UVAL12 = 208.4000023 <0> <0> / PARAMNAME2 = NRTL CID1 = H2O CID2 = AMINE UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ENRTL-RK VAL2 = ENRTL-RK VAL3 = ENRTL-RK VAL4 = ENRTL-RK VAL5 = ENRTL-RK VAL6 = ENRTL-RK VAL7 = ENRTL-RK VAL8 = ENRTL-RK VAL9 = ENRTL-RK VAL10 = ENRTL-RK VAL11 = ENRTL-RK VAL12 = ENRTL-RK \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "PRKBV-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = PRKBV SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F BDBANK = ( "ASPEN-BM" ) NEL = 5 \ \ BPVAL PARAMNAME2 = PRKBV CID1 = H2 CID2 = CO UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2 CID2 = N2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2 CID2 = CO2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2 CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2 CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2 CID2 = C2H4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2 CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO CID2 = N2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO CID2 = H2S UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = CO2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = C2H4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = H2S UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = O2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = AR UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = SO2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = NH3 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = N2 CID2 = METHANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = O2 CID2 = AR UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = AR CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = AR CID2 = NH3 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = C2H4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = H2S UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = METHANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CO2 CID2 = H2O UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2O CID2 = H2S UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2O CID2 = NH3 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2O CID2 = METHANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2S CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2S CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2S CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = H2S CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = SO2 CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = SO2 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CH4 CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CH4 CID2 = C2H4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CH4 CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CH4 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CH4 CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CH4 CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = CH4 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C2H6 CID2 = C2H4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C2H6 CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C2H6 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C2H6 CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C2H6 CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C2H6 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C2H6 CID2 = METHANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C2H4 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C2H4 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C2H4 CID2 = C2H2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C3H8 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C3H8 CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C3H8 CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C3H8 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = C3H8 CID2 = ETHANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = "I-C4H10" CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = "N-C4H10" CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = PRKBV CID1 = "PENTANE+" CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "PRLIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = PRLIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F NEL = 8 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "RKSKBV-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = RKSKBV SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F BDBANK = ( "ASPEN-BM" ) NEL = 5 \ \ BPVAL PARAMNAME2 = RKSKBV CID1 = H2 CID2 = CO UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2 CID2 = N2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2 CID2 = CO2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2 CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2 CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2 CID2 = C2H4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2 CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO CID2 = N2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO CID2 = H2S UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = O2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = AR UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = CO2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = H2S UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = SO2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = NH3 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = C2H4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = N2 CID2 = METHANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = O2 CID2 = AR UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = AR CID2 = NH3 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = AR CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = H2O UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = H2S UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = C2H4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CO2 CID2 = METHANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2O CID2 = H2S UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2O CID2 = NH3 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2O CID2 = METHANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2S CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2S CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2S CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = H2S CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = SO2 CID2 = CH4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = SO2 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CH4 CID2 = C2H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CH4 CID2 = C2H4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CH4 CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CH4 CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CH4 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CH4 CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = CH4 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C2H6 CID2 = C2H4 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C2H6 CID2 = C3H8 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C2H6 CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C2H6 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C2H6 CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C2H6 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C2H6 CID2 = METHANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C2H4 CID2 = C2H2 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C2H4 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C2H4 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C3H8 CID2 = "I-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C3H8 CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C3H8 CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C3H8 CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = C3H8 CID2 = ETHANOL UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = "I-C4H10" CID2 = "N-C4H10" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = "N-C4H10" CID2 = "PENTANE+" UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM / PARAMNAME2 = RKSKBV CID1 = "PENTANE+" CID2 = C6H6 UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = ASPEN-BM VAL2 = ASPEN-BM VAL3 = ASPEN-BM VAL4 = ASPEN-BM VAL5 = ASPEN-BM \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "RKSLBV-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = RKSLBV SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F NEL = 8 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "VLCLK-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = VLCLK SETNO = 1 UNITROW = 43 UNITLABEL = "cuft/lbmol" TUNITROW = 0 BDBANK = ( "ENRTL-RK" ) NEL = 2 \ ? PROPERTIES PARAMETERS PAIR "GMELCC-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = GMELCC SETNO = 1 UNITROW = 0 BDBANK = ( "ENRTL-RK" ) \ \ PPVAL PARAMNAME2 = GMELCC 1 CID1A = CO2 CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 2 CID1A = "H3O+" CID1B = "OH-" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 3 CID1A = CO2 CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 4 CID1A = "H3O+" CID1B = "HCO3-" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 5 CID1A = CO2 CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 6 CID1A = "H3O+" CID1B = "HS-" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 7 CID1A = CO2 CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 8 CID1A = "H3O+" CID1B = "CO3--" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 9 CID1A = CO2 CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 10 CID1A = "H3O+" CID1B = "S--" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 11 CID1A = H2O CID2A = "NH4+" CID2B = "NH2COO-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 12 CID1A = "NH4+" CID1B = "NH2COO-" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 13 CID1A = H2O CID2A = "NH4+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 14 CID1A = "NH4+" CID1B = "OH-" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 15 CID1A = H2O CID2A = "NH4+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 16 CID1A = "NH4+" CID1B = "HCO3-" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 17 CID1A = H2O CID2A = "NH4+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 18 CID1A = "NH4+" CID1B = "HS-" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 19 CID1A = H2O CID2A = "NH4+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 20 CID1A = "NH4+" CID1B = "CO3--" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 21 CID1A = H2O CID2A = "NH4+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 22 CID1A = "NH4+" CID1B = "S--" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 23 CID1A = H2O CID2A = "H3O+" CID2B = "NH2COO-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 24 CID1A = "H3O+" CID1B = "NH2COO-" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 25 CID1A = H2O CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 26 CID1A = "H3O+" CID1B = "OH-" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 27 CID1A = H2O CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 28 CID1A = "H3O+" CID1B = "HCO3-" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 29 CID1A = H2O CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 30 CID1A = "H3O+" CID1B = "HS-" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 31 CID1A = H2O CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 32 CID1A = "H3O+" CID1B = "CO3--" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 33 CID1A = H2O CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 34 CID1A = "H3O+" CID1B = "S--" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 35 CID1A = H2S CID2A = "NH4+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 36 CID1A = "NH4+" CID1B = "HS-" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 37 CID1A = H2S CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 38 CID1A = "H3O+" CID1B = "OH-" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 39 CID1A = H2S CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 40 CID1A = "H3O+" CID1B = "HCO3-" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 41 CID1A = H2S CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 42 CID1A = "H3O+" CID1B = "HS-" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 43 CID1A = H2S CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 44 CID1A = "H3O+" CID1B = "CO3--" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 45 CID1A = H2S CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 46 CID1A = "H3O+" CID1B = "S--" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 47 CID1A = NH3 CID2A = "NH4+" CID2B = "NH2COO-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 48 CID1A = "NH4+" CID1B = "NH2COO-" CID2A = NH3 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 49 CID1A = NH3 CID2A = "NH4+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 50 CID1A = "NH4+" CID1B = "HCO3-" CID2A = NH3 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 51 CID1A = NH3 CID2A = "NH4+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 52 CID1A = "NH4+" CID1B = "HS-" CID2A = NH3 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 53 CID1A = AMINE CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 54 CID1A = "H3O+" CID1B = "OH-" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 55 CID1A = AMINE CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 56 CID1A = "H3O+" CID1B = "HCO3-" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 57 CID1A = AMINE CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 58 CID1A = "H3O+" CID1B = "HS-" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 59 CID1A = AMINE CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 60 CID1A = "H3O+" CID1B = "CO3--" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 61 CID1A = AMINE CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCC 62 CID1A = "H3O+" CID1B = "S--" CID2A = AMINE VALUE = ENRTL-RK \ ? PROPERTIES PARAMETERS PAIR "GMELCD-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = GMELCD SETNO = 1 UNITROW = 22 UNITLABEL = F BDBANK = ( "ENRTL-RK" ) \ \ PPVAL PARAMNAME2 = GMELCD 1 CID1A = CO2 CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 2 CID1A = "H3O+" CID1B = "OH-" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 3 CID1A = CO2 CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 4 CID1A = "H3O+" CID1B = "HCO3-" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 5 CID1A = CO2 CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 6 CID1A = "H3O+" CID1B = "HS-" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 7 CID1A = CO2 CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 8 CID1A = "H3O+" CID1B = "CO3--" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 9 CID1A = CO2 CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 10 CID1A = "H3O+" CID1B = "S--" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 11 CID1A = H2O CID2A = "NH4+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 12 CID1A = "NH4+" CID1B = "HCO3-" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 13 CID1A = H2O CID2A = "NH4+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 14 CID1A = "NH4+" CID1B = "HS-" CID2A = H2O VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 15 CID1A = H2S CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 16 CID1A = "H3O+" CID1B = "OH-" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 17 CID1A = H2S CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 18 CID1A = "H3O+" CID1B = "HCO3-" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 19 CID1A = H2S CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 20 CID1A = "H3O+" CID1B = "HS-" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 21 CID1A = H2S CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 22 CID1A = "H3O+" CID1B = "CO3--" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 23 CID1A = H2S CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 24 CID1A = "H3O+" CID1B = "S--" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 25 CID1A = AMINE CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 26 CID1A = "H3O+" CID1B = "OH-" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 27 CID1A = AMINE CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 28 CID1A = "H3O+" CID1B = "HCO3-" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 29 CID1A = AMINE CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 30 CID1A = "H3O+" CID1B = "HS-" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 31 CID1A = AMINE CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 32 CID1A = "H3O+" CID1B = "CO3--" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 33 CID1A = AMINE CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCD 34 CID1A = "H3O+" CID1B = "S--" CID2A = AMINE VALUE = ENRTL-RK \ ? PROPERTIES PARAMETERS PAIR "GMELCE-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = GMELCE SETNO = 1 UNITROW = 0 BDBANK = ( "ENRTL-RK" ) \ \ PPVAL PARAMNAME2 = GMELCE 1 CID1A = CO2 CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 2 CID1A = "H3O+" CID1B = "OH-" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 3 CID1A = CO2 CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 4 CID1A = "H3O+" CID1B = "HCO3-" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 5 CID1A = CO2 CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 6 CID1A = "H3O+" CID1B = "HS-" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 7 CID1A = CO2 CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 8 CID1A = "H3O+" CID1B = "CO3--" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 9 CID1A = CO2 CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 10 CID1A = "H3O+" CID1B = "S--" CID2A = CO2 VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 11 CID1A = H2S CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 12 CID1A = "H3O+" CID1B = "OH-" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 13 CID1A = H2S CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 14 CID1A = "H3O+" CID1B = "HCO3-" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 15 CID1A = H2S CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 16 CID1A = "H3O+" CID1B = "HS-" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 17 CID1A = H2S CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 18 CID1A = "H3O+" CID1B = "CO3--" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 19 CID1A = H2S CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 20 CID1A = "H3O+" CID1B = "S--" CID2A = H2S VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 21 CID1A = AMINE CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 22 CID1A = "H3O+" CID1B = "OH-" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 23 CID1A = AMINE CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 24 CID1A = "H3O+" CID1B = "HCO3-" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 25 CID1A = AMINE CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 26 CID1A = "H3O+" CID1B = "HS-" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 27 CID1A = AMINE CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 28 CID1A = "H3O+" CID1B = "CO3--" CID2A = AMINE VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 29 CID1A = AMINE CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCE 30 CID1A = "H3O+" CID1B = "S--" CID2A = AMINE VALUE = ENRTL-RK \ ? PROPERTIES PARAMETERS PAIR "GMELCN-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = GMELCN SETNO = 1 UNITROW = 0 BDBANK = ( "ENRTL-RK" ) \ \ PPVAL PARAMNAME2 = GMELCN 1 CID1A = CO2 CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 2 CID1A = CO2 CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 3 CID1A = CO2 CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 4 CID1A = CO2 CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 5 CID1A = CO2 CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 6 CID1A = H2S CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 7 CID1A = H2S CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 8 CID1A = H2S CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 9 CID1A = H2S CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 10 CID1A = H2S CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 11 CID1A = AMINE CID2A = "H3O+" CID2B = "OH-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 12 CID1A = AMINE CID2A = "H3O+" CID2B = "HCO3-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 13 CID1A = AMINE CID2A = "H3O+" CID2B = "HS-" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 14 CID1A = AMINE CID2A = "H3O+" CID2B = "CO3--" VALUE = ENRTL-RK \ \ PPVAL PARAMNAME2 = GMELCN 15 CID1A = AMINE CID2A = "H3O+" CID2B = "S--" VALUE = ENRTL-RK \ ? "STREAM-CLASS" SUBSTREAMS ? \ DEF-SUBS-CLA SUBSTREAMS = MIXED \ \ DEF-SUBS-CLA SUBSTREAMS = CISOLID \ \ DEF-SUBS-CLA SUBSTREAMS = NC \ \ DEF-SUBS-CLA SUBSTREAMS = NCPSD \ \ DEF-SUBS-CLA SUBSTREAMS = CIPSD \ ? "STREAM-CLASS" "STREAM-CLASS" ? \ DEFINITION SCLASS = CONVEN \ \ DEFINITION SCLASS = MIXNC \ \ DEFINITION SCLASS = MIXCISLD \ \ DEFINITION SCLASS = MIXNCPSD \ \ DEFINITION SCLASS = MIXCIPSD \ \ DEFINITION SCLASS = MIXCINC \ \ DEFINITION SCLASS = MCINCPSD \ \ HEAT-DEFINE H-SCLASS = HEAT STREAM-ATTR = HEAT \ \ HEAT-DEFINE H-SCLASS = LOAD STREAM-ATTR = LOAD \ ? "STREAM-CLASS" "DEF-STREAMS" ? ? "PROP-SET" MAIN HMIXTP ? ; "ENG_MOLE" ; \ P1 ID = HMX UNITS = ( "Btu/lbmol" ) \ \ P1 ID = CPMX UNITS = ( "Btu/lb-R" ) \ \ P2 SYSPRES = YES \ ? "STREAM-NAMES" ? \ NAMES STREAM = 220 TEXT = "MgO Make-Up" \ \ NAMES STREAM = 100 TEXT = "Biomass Feedstock" \ ? STREAM MATERIAL 100 ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 1.E-006 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TEMP = 60. <22> <2> PRES = 1. <20> <3> TOTAL = 3.E-006 <-80> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = WOOD FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = ASH FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = CHAR FLOW = 1E-006 <-80> <2> \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = ULTANAL ELEM = ( 0.92 <0> <0> 50.88 <0> <0> 6.04 <0> <0> 0.17 <0> <0> 0. <0> <0> 0.09 <0> <0> 41.9 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.045 <0> <0> 0.045 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 15.29 <0> <0> 83.84 <0> <0> 0.87 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = GENANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> 100. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = ULTANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = ULTANAL ELEM = ( 3.168 <0> <0> 65.894 <0> <0> 3.064 <0> <0> 0.281 <0> <0> 0. <0> <0> 0.149 <0> <0> 27.444 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.0745 <0> <0> 0.0745 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 87.18 <0> <0> 12.81 <0> <0> 0.01 <0> <0> ) \ \ COMMENTS COMMENTS = ( ";Ultimate analysis overwritten by values in " ";SETFEED. (Jechura 9 Nov 2006)." ";Poplar composition per Craig, K.R., Mann, M.K., " ";""Cost and Performance Analysis of Biomass-Bases " ";Integrated Gasification Combined-Cycle (BIGCC) " ";Power Systems"", National Renewable Energy " ";Laboratory, NREL/TP-430-21657, October, 1996." ";Modified sulfur analysis as follows: Evenly " ";distributed sulfur between sulfate and organic, " ";with no sulfur being classified as pyritic" ) \ ? STREAM MATERIAL 200 ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 382.7486 <22> <2> PRES = 25. <20> <2> BASIS = "MASS-FLOW" TOTAL = 73120. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 73120. <-80> <2> \ \ COMMENTS COMMENTS = ( ";Note: a manual change of T & P is required if the " ";steam turbine T & P is changed. The flow rate is a " ";calculated value." ) \ ? STREAM MATERIAL 206 ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 22. <20> <2> BASIS = "MOLE-FRAC" FLOWBASE = MOLE TOTFLOW = 1E-006 <-89> <2> TOTAL = 1. <-4> <0> JUNK = 9 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.011 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.005 <-4> <0> / SSID1 = MIXED CID = H2S FLOW = 4E-006 <-4> <0> / SSID1 = MIXED CID = CH4 FLOW = 0.943996 <-4> <0> / SSID1 = MIXED CID = C2H6 FLOW = 0.031 <-4> <0> / SSID1 = MIXED CID = C3H8 FLOW = 0.005 <-4> <0> / SSID1 = MIXED CID = "I-C4H10" FLOW = 0.001 <-4> <0> / SSID1 = MIXED CID = "N-C4H10" FLOW = 0.001 <-4> <0> / SSID1 = MIXED CID = "PENTANE+" FLOW = 0.002 <-4> <0> \ ? STREAM MATERIAL 220 ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 25. <20> <2> TOTAL = 1.E-009 <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TEMP = 60. <22> <2> PRES = 25. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2S FLOW = 1E-009 <-89> <2> / SSID1 = CISOLID CID = OLIVINE FLOW = 1. <-3> <0> \ \ COMMENTS COMMENTS = ( ";Substitued Olivine for MgO in composition" ) \ ? STREAM MATERIAL 221 ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 22. <20> <2> TOTAL = 1.E-007 <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TEMP = 60. <22> <2> PRES = 22. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2S FLOW = 1E-007 <-89> <2> / SSID1 = CISOLID CID = OLIVINE FLOW = 1. <-3> <0> \ ? STREAM MATERIAL 322 ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 1. <20> <3> BASIS = "MOLE-FRAC" TOTFLOW = 1E-006 <-89> <2> TOTAL = 1. <-4> <0> JUNK = 5 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.75666 <-4> <0> / SSID1 = MIXED CID = O2 FLOW = 0.202967 <-4> <0> / SSID1 = MIXED CID = AR FLOW = 0.00905 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.00032 <-4> <0> / SSID1 = MIXED CID = H2O FLOW = 0.031003 <-4> <0> \ ? STREAM MATERIAL 618 ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL 635 ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 22. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL 710 ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL 711 ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? "STREAM-SUM" ? ? BLOCK HIERARCHY A100 ? ; BLOCK ; ? "A100.SOLVE" ? ? FLOWSHEET "A100.GLOBAL" ? \ BLOCK BLKID = A100DRYR BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-6" IN = ( 107 M3-0 ) OUT = ( "A100DRYR.107" M3-0 ) \ \ CONNECT BLKID = "$C-8" IN = ( 101 M4-0 ) OUT = ( "A100DRYR.101" M4-0 ) \ \ CONNECT BLKID = "$C-5" IN = ( "A100DRYR.110" M5-0 ) OUT = ( 110 M3-0 ) \ \ CONNECT BLKID = "$C-7" IN = ( "A100DRYR.103" M6-0 ) OUT = ( 103 M4-0 ) \ \ BLOCK BLKID = A100DWPT BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-4" IN = ( 110 M3-0 ) OUT = ( "A100DWPT.110" M3-0 ) \ \ CONNECT BLKID = "$C-3" IN = ( "A100DWPT.112" M4-0 ) OUT = ( 112 M3-0 ) \ \ BLOCK BLKID = "HV-100" BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-2" IN = ( 100 M3-0 ) OUT = ( "HV-100.100-IN" M3-0 ) \ \ CONNECT BLKID = "$C-1" IN = ( "HV-100.100-OUT" M4-0 ) OUT = ( 101 M3-0 ) \ \ BLOCK BLKID = "T-104" BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 103 M0-1 ) OUT = ( 104 M0-1 ) \ \ BLOCK BLKID = "C-105" BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 104 M0-1 ) OUT = ( 105 M0-1 ) \ \ BLOCK BLKID = MX104 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 287 M0-1 335 M0-1 ) OUT = ( 107 M0-1 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A100.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A100.STREAM-NAMES" ? \ NAMES STREAM = 100 TEXT = "Feed material" \ ? STREAM MATERIAL "A100.100" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 1.E-006 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TEMP = 60. <22> <2> PRES = 1. <20> <3> TOTAL = 3.E-006 <-80> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = WOOD FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = ASH FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = CHAR FLOW = 1E-006 <-80> <2> \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = ULTANAL ELEM = ( 0.92 <0> <0> 50.88 <0> <0> 6.04 <0> <0> 0.17 <0> <0> 0. <0> <0> 0.09 <0> <0> 41.9 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.045 <0> <0> 0.045 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 15.29 <0> <0> 83.84 <0> <0> 0.87 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = GENANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> 100. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = ULTANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = ULTANAL ELEM = ( 3.168 <0> <0> 65.894 <0> <0> 3.064 <0> <0> 0.281 <0> <0> 0. <0> <0> 0.149 <0> <0> 27.444 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.0745 <0> <0> 0.0745 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 87.18 <0> <0> 12.81 <0> <0> 0.01 <0> <0> ) \ \ COMMENTS COMMENTS = ( ";Poplar composition per Craig, K.R., Mann, M.K., " ";""Cost and Performance Analysis of Biomass-Bases " ";Integrated Gasification Combined-Cycle (BIGCC) Power " ";Systems"", National Renewable Energy Laboratory, " ";NREL/TP-430-21657, October, 1996." ";Modified sulfur analysis as follows: Evenly " ";distributed sulfur between sulfate and organic, with " ";no sulfur being classified as pyritic" ) \ ? BLOCK MIXER "A100.C-105" ? ; "ENG_MOLE" ; ; SCREW ; \ DESCRIPTION DESCRIPTION = "Gasifier Feed Screw Conveyor" \ \ PARAM PRES = 25. <20> <2> \ ? BLOCK MIXER "A100.MX104" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A100.T-104" ? ; "ENG_MOLE" ; ; TANK ; \ DESCRIPTION DESCRIPTION = "Dried Biomass Hopper" \ ? BLOCK HIERARCHY "A100.A100DRYR" ? ; BLOCK ; ? "A100.A100DRYR.SOLVE" ? ? FLOWSHEET "A100.A100DRYR.GLOBAL" ? \ BLOCK BLKID = MX200E BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 108 M0-1 109 M0-1 ) OUT = ( 110 M0-1 ) \ \ BLOCK BLKID = "M-104A" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 102 M0-1 ) OUT = ( QM104 Q3-4 103 M1-2 109 M0-1 ) \ \ BLOCK BLKID = "M-104B" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( QM104 Q1-2 107 M0-1 ) OUT = ( 108 M0-1 QM104B Q2-3 ) \ \ BLOCK BLKID = "C-104" BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 101 M0-1 ) OUT = ( 102 M0-1 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A100.A100DRYR.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A100.A100DRYR.STREAM-NAMES" ? ? BLOCK MIXER "A100.A100DRYR.C-104" ? ; "ENG_MOLE" ; ; SCREW ; \ DESCRIPTION DESCRIPTION = "Dryer Feed Screw Conveyor" \ \ PARAM PRES = 15.696 <20> <2> \ ? BLOCK MIXER "A100.A100DRYR.MX200E" ? ; "ENG_MASS" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "Mixes moisture from the wood with flue gas" \ \ COMMENTS COMMENTS = ( ";The inlet moisture stream to this block is set by " ";calculator block setfeed." ) \ ? BLOCK HEATER "A100.A100DRYR.M-104B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 231. <22> <2> PRES = -1. <20> <2> \ ? BLOCK FLASH2 "A100.A100DRYR.M-104A" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Rotary Biomass Dryer" \ \ PARAM PRES = 0. <20> <2> VFRAC = 0.89 <0> <0> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ \ COMMENTS COMMENTS = ( ";Vapor fraction is set by calculator block DRYER" ) \ ? REPORT "A100.A100DRYR.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A100.A100DWPT" ? ; BLOCK ; ? "A100.A100DWPT.SOLVE" ? ? FLOWSHEET "A100.A100DWPT.GLOBAL" ? \ BLOCK BLKID = HX900A BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 113 M0-1 ) OUT = ( 114 M0-1 QB65 Q2-3 ) \ \ BLOCK BLKID = DPL100A BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( 110 M0-1 ) OUT = ( 112 M0-1 113 M0-1 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A100.A100DWPT.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? BLOCK HEATER "A100.A100DWPT.HX900A" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Checks dewpoint of flue gas" \ \ PARAM PRES = 0. <20> <2> VFRAC = 1. <0> <0> \ \ COMMENTS COMMENTS = ( ";Not included in the PFD; only a modelling tool. " ) \ ? BLOCK DUPL "A100.A100DWPT.DPL100A" ? ; "ENG_MOLE" ; ; BLOCK ; ? REPORT "A100.A100DWPT.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A100.HV-100" ? ; BLOCK ; ? "A100.HV-100.SOLVE" ? ? FLOWSHEET "A100.HV-100.GLOBAL" ? \ BLOCK BLKID = DPL100 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( "100-IN" M0-1 ) OUT = ( "100-OUT" M0-1 RAW M0-1 ) \ \ BLOCK BLKID = REJECT BLKTYPE = SEP MDLTYPE = "Sep" IN = ( RAW M0-1 ) OUT = ( BASIS M0-1 REJECT M0-1 QREJECT Q1-4 ) \ \ BLOCK BLKID = BURN BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( BASIS M0-1 O2 M0-1 ) OUT = ( QCOMB Q2-3 "PROD-1" M0-1 ) \ \ BLOCK BLKID = COMBSEP BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( "PROD-2" M0-1 ) OUT = ( COMBVAP M0-1 COMBLIQ M1-2 ) \ \ BLOCK BLKID = VAPWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( COMBLIQ M0-1 ) OUT = ( DPT M0-1 "QVAP-1" Q2-3 ) \ \ BLOCK BLKID = CONDWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( "WATER-V" M0-1 ) OUT = ( "WATER-L" M0-1 "QVAP-2" Q2-3 ) \ \ BLOCK BLKID = DRYER BLKTYPE = SEP MDLTYPE = "Sep" IN = ( DPT M0-1 COMBVAP M0-1 ) OUT = ( "WATER-V" M0-1 RESIDUE M0-1 ) \ \ BLOCK BLKID = NET BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-1" Q1-4 QCOMB Q1-4 QSHIFT Q1-4 ) OUT = ( QNET Q1-3 ) \ \ BLOCK BLKID = GROSS BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-2" Q1-4 QNET Q1-4 ) OUT = ( QGROSS Q1-3 ) \ \ BLOCK BLKID = SHIFT BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( "PROD-1" M0-1 ) OUT = ( "PROD-2" M0-1 QSHIFT Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A100.HV-100.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A100.HV-100.STREAM-NAMES" ? \ NAMES STREAM = "100-IN" TEXT = "Feed material" \ ? STREAM MATERIAL "A100.HV-100.100-IN" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 1.E-006 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TEMP = 60. <22> <2> PRES = 1. <20> <3> TOTAL = 3.E-006 <-80> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = WOOD FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = ASH FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = CHAR FLOW = 1E-006 <-80> <2> \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = ULTANAL ELEM = ( 0.92 <0> <0> 50.88 <0> <0> 6.04 <0> <0> 0.17 <0> <0> 0. <0> <0> 0.09 <0> <0> 41.9 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.045 <0> <0> 0.045 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 15.29 <0> <0> 83.84 <0> <0> 0.87 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = GENANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> 100. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = ULTANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = ULTANAL ELEM = ( 3.168 <0> <0> 65.894 <0> <0> 3.064 <0> <0> 0.281 <0> <0> 0. <0> <0> 0.149 <0> <0> 27.444 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.0745 <0> <0> 0.0745 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 87.18 <0> <0> 12.81 <0> <0> 0.01 <0> <0> ) \ \ COMMENTS COMMENTS = ( ";Poplar composition per Craig, K.R., Mann, M.K., " ";""Cost and Performance Analysis of Biomass-Bases " ";Integrated Gasification Combined-Cycle (BIGCC) Power " ";Systems"", National Renewable Energy Laboratory, " ";NREL/TP-430-21657, October, 1996." ";Modified sulfur analysis as follows: Evenly " ";distributed sulfur between sulfate and organic, with " ";no sulfur being classified as pyritic" ) \ ? STREAM MATERIAL "A100.HV-100.O2" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 77. <22> <2> PRES = 1. <20> <3> TOTAL = 9000. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = O2 FLOW = 9000. <-89> <2> \ ? BLOCK MIXER "A100.HV-100.GROSS" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A100.HV-100.NET" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK SEP "A100.HV-100.DRYER" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = METHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = "WATER-V" TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK SEP "A100.HV-100.REJECT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = N2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = O2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2O FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2S FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NH3 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H4 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C3H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C6H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C10H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = METHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = WOOD FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = BASIS TEMP = 77. <22> <2> PRES = 1. <20> <3> \ ? BLOCK HEATER "A100.HV-100.CONDWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A100.HV-100.VAPWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK FLASH2 "A100.HV-100.COMBSEP" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK RSTOIC "A100.HV-100.BURN" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 0. <20> <2> COMBUSTION = YES PROD-NOX = NO2 \ \ STOIC REACNO = 1 STOIC-CID = WOOD STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = NC KEY-CID = WOOD CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = NO2 \ ? BLOCK RSTOIC "A100.HV-100.SHIFT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 1. <20> <3> \ \ STOIC REACNO = 1 STOIC-CID = NO2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = 0.5 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = NO2 CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = O2 \ ? BLOCK DUPL "A100.HV-100.DPL100" ? ; "ENG_MOLE" ; ; BLOCK ; ? REPORT "A100.HV-100.BLOCK-REPORT" ? ? REPORT "A100.BLOCK-REPORT" ? ? BLOCK HIERARCHY A200 ? ; BLOCK ; ? "A200.SOLVE" ? ? FLOWSHEET "A200.GLOBAL" ? \ BLOCK BLKID = A200CC BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-8" IN = ( 206 M3-0 ) OUT = ( "A200CC.206" M3-0 ) \ \ CONNECT BLKID = "$C-9" IN = ( 203 M4-0 ) OUT = ( "A200CC.203" M4-0 ) \ \ CONNECT BLKID = "$C-1" IN = ( 223 M5-0 ) OUT = ( "A200CC.223" M5-0 ) \ \ CONNECT BLKID = "$C-5" IN = ( 220 M6-0 ) OUT = ( "A200CC.220" M6-0 ) \ \ CONNECT BLKID = "$C-2" IN = ( 221 M7-0 ) OUT = ( "A200CC.221" M7-0 ) \ \ CONNECT BLKID = "$C-11" IN = ( 225C M8-0 ) OUT = ( "A200CC.225C" M8-0 ) \ \ CONNECT BLKID = "$C-6" IN = ( "A200CC.219" M9-0 ) OUT = ( 219 M3-0 ) \ \ CONNECT BLKID = "$C-7" IN = ( "A200CC.211" M10-0 ) OUT = ( 211 M4-0 ) \ \ CONNECT BLKID = "$C-10" IN = ( "A200CC.287" M11-0 ) OUT = ( 287 M5-0 ) \ \ BLOCK BLKID = "HV-224" BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-4" IN = ( 224 M3-0 ) OUT = ( "HV-224.100-IN" M3-0 ) \ \ CONNECT BLKID = "$C-3" IN = ( "HV-224.100-OUT" M4-0 ) OUT = ( 225 M3-0 ) \ \ BLOCK BLKID = MX200A BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 105 M0-1 200 M0-1 211 M0-1 ) OUT = ( 201 M0-1 ) \ \ BLOCK BLKID = "R-201" BLKTYPE = RYIELD MDLTYPE = "RYield" IN = ( 201 M0-1 ) OUT = ( 202 M0-1 QR201 Q2-3 ) \ \ BLOCK BLKID = "S-201" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 202 M0-1 ) OUT = ( 203 M0-1 222 M0-1 QS201 Q1-4 ) \ \ BLOCK BLKID = "S-202" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 222 M0-1 ) OUT = ( QS202 Q1-4 223 M0-1 224 M0-1 ) \ \ BLOCK BLKID = SP225 BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 225 M0-1 ) OUT = ( 225C M0-1 225A M0-1 225F M0-1 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A200.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A200.STREAM-NAMES" ? \ NAMES STREAM = 220 TEXT = "MgO Make-Up" \ ? STREAM MATERIAL "A200.200" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 259.857773 <22> <2> PRES = 25. <20> <2> BASIS = "MASS-FLOW" TOTAL = 398. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 398. <-80> <2> \ \ COMMENTS COMMENTS = ( ";Note: a manual change of T & P is required if the " ";steam turbine T & P is changed. The flow rate is a " ";calculated value." ) \ ? STREAM MATERIAL "A200.206" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 22. <20> <2> BASIS = "MOLE-FRAC" FLOWBASE = MOLE TOTFLOW = 1E-006 <-89> <2> TOTAL = 1. <-4> <0> JUNK = 9 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.011 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.005 <-4> <0> / SSID1 = MIXED CID = H2S FLOW = 4E-006 <-4> <0> / SSID1 = MIXED CID = CH4 FLOW = 0.943996 <-4> <0> / SSID1 = MIXED CID = C2H6 FLOW = 0.031 <-4> <0> / SSID1 = MIXED CID = C3H8 FLOW = 0.005 <-4> <0> / SSID1 = MIXED CID = "I-C4H10" FLOW = 0.001 <-4> <0> / SSID1 = MIXED CID = "N-C4H10" FLOW = 0.001 <-4> <0> / SSID1 = MIXED CID = "PENTANE+" FLOW = 0.002 <-4> <0> \ ? STREAM MATERIAL "A200.220" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 60. <22> <2> PRES = 25. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = CISOLID CID = OLIVINE FLOW = 1. <-3> <0> \ \ COMMENTS COMMENTS = ( ";Substitued Olivine for MgO in composition" ) \ ? STREAM MATERIAL "A200.221" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 60. <22> <2> PRES = 25. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = CISOLID CID = OLIVINE FLOW = 1. <-3> <0> \ ? BLOCK MIXER "A200.MX200A" ? ; "ENG_MASS" ; ; TRIANGLE ; \ DESCRIPTION DESCRIPTION = "Combines the wood feed, gasifier steam, and sand" \ ? BLOCK FSPLIT "A200.SP225" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM SID = 225C FLOW-BASIS = MASS BASIS-FLOW = 0.001 <-80> <2> / SID = 225A / SID = 225F FLOW-BASIS = MASS BASIS-FLOW = 70000. <-80> <2> \ \ STREAM-ORDER ORDER-STREAM = 225C ORDER = 1 / ORDER-STREAM = 225A / ORDER-STREAM = 225F ORDER = 2 \ ? BLOCK SEP "A200.S-201" ? ; "ENG_MASS" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Primary Gasifier Cyclone Filter" \ \ PARAM1 PRES1 = -6. <20> <7> FLAG = 0 \ \ PARAM PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = CARBON FRACS = 0.999 <0> <0> / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0.999 <0> <0> / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0.999 <0> <0> / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 203 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 203 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0.99 <0> <0> / PARAM-STREAM = 203 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0.99 <0> <0> / PARAM-STREAM = 203 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0.999 <0> <0> / PARAM-STREAM = 203 SUBSTREAM = NC COMPS = WOOD FRACS = 0.99 <0> <0> / PARAM-STREAM = 203 SUBSTREAM = NC COMPS = ASH FRACS = 0.99 <0> <0> / PARAM-STREAM = 203 SUBSTREAM = NC COMPS = CHAR FRACS = 0.99 <0> <0> / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 222 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 222 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 222 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 222 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 222 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 222 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 222 SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = 203 PRES = -1. <20> <2> \ \ FLASH-SPECS FLASH-STREAM = 222 PRES = -1. <20> <2> \ ? BLOCK SEP "A200.S-202" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Secondary Gasifier Cyclone Filter" \ \ PARAM1 PRES1 = -10. <20> <7> FLAG = 0 \ \ PARAM PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = CARBON FRACS = 0.999 <0> <0> / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0.999 <0> <0> / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0.999 <0> <0> / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 223 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 223 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0.99 <0> <0> / PARAM-STREAM = 223 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0.99 <0> <0> / PARAM-STREAM = 223 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0.99 <0> <0> / PARAM-STREAM = 223 SUBSTREAM = NC COMPS = WOOD FRACS = 0.99 <0> <0> / PARAM-STREAM = 223 SUBSTREAM = NC COMPS = ASH FRACS = 0.99 <0> <0> / PARAM-STREAM = 223 SUBSTREAM = NC COMPS = CHAR FRACS = 0.99 <0> <0> / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 224 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 224 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 224 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 224 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 224 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 224 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 224 SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = 223 PRES = 0. <20> <2> \ \ FLASH-SPECS FLASH-STREAM = 224 PRES = 0. <20> <2> \ ? BLOCK RYIELD "A200.R-201" ? ; "ENG_MASS" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "Indirectly-Heater Biomass Gasifier" \ \ SUBROUTINE YIELD = BATYD5 \ \ "USER-VECS" NREAL = 8 \ \ REAL RVALUE-LIST = ( 1500. <0> <0> 25. <0> <0> 6.6 <0> <0> 8.3 <0> <0> 0.0465 <0> <0> 4. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ PARAM TEMP = 1607. <22> <2> PRES = -2. <20> <2> USER-YIELD = YES \ \ FORCONTROL FCVAR1 = AMINE \ \ COMMENTS COMMENTS = ( ";Uses a fortran routine to determine the gasifier " ";outlet gas and char" ";Real (1) = gasifier temperature" ";Real (2) = gasifier pressure" ";Real (3) = % of the wood nitrogen retained in the " ";char" ";Real (4) = % of the wood sulfur retained in the " ";char" ";Real (5) = H/C mass ratio in the char" ";Real (6) = % of the wood oxygen retained in the " ";char" ) \ ? BLOCK HIERARCHY "A200.A200CC" ? ; BLOCK ; ? "A200.A200CC.SOLVE" ? ? FLOWSHEET "A200.A200CC.GLOBAL" ? \ BLOCK BLKID = "K-202" BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 208 M0-1 ) OUT = ( WK202 W2-3 209A M0-1 ) \ \ BLOCK BLKID = "R-202" BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( QUSR200A Q1-2 209B M0-1 207 M0-1 ) OUT = ( 210 M0-1 QR202 Q2-3 ) \ \ BLOCK BLKID = "M-201" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 216 M0-1 ) OUT = ( 217 M0-1 QCM201 Q2-3 ) \ \ BLOCK BLKID = MX200C BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 205 M0-1 206 M0-1 225C M0-1 ) OUT = ( 207 M0-1 ) \ \ BLOCK BLKID = "C-201" BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 217 M0-1 218 M0-1 ) OUT = ( 219 M0-1 ) \ \ BLOCK BLKID = MX200B BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 203 M0-1 223 M0-1 220 M0-1 221 M0-1 ) OUT = ( 204 M0-1 ) \ \ BLOCK BLKID = "S-203" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 210 M0-1 ) OUT = ( QS203 Q1-4 211 M0-1 212 M0-1 ) \ \ BLOCK BLKID = "S-204" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 212 M0-1 ) OUT = ( QS204 Q1-4 214 M0-1 213 M0-1 ) \ \ BLOCK BLKID = "S-205" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 213 M0-1 ) OUT = ( QS205 Q1-4 215 M0-1 286 M0-1 ) \ \ BLOCK BLKID = MX200D BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 214 M0-1 215 M0-1 ) OUT = ( 216 M0-1 ) \ \ BLOCK BLKID = USER200A BLKTYPE = USER MDLTYPE = "User" IN = ( 204 M0-1 ) OUT = ( 205 M0-1 QUSR200A Q1-2 ) \ \ BLOCK BLKID = "H-286" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 286 M0-1 ) OUT = ( 287 M0-1 QH286 Q2-3 ) \ \ BLOCK BLKID = "H-209" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 209A M0-1 ) OUT = ( 209B M0-1 QH209 Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A200.A200CC.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A200.A200CC.STREAM-NAMES" ? \ NAMES STREAM = 220 TEXT = "MgO Make-Up" \ ? STREAM MATERIAL "A200.A200CC.204" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 1597.9 <22> <2> PRES = 22. <20> <2> BASIS = "MASS-FLOW" TOTAL = 4951850. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = NC TEMP = 1597.9 <22> <2> PRES = 22. <20> <2> TOTAL = 39935.5012 <-80> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = CISOLID CID = OLIVINE FLOW = 4951850. <-80> <2> / SSID1 = NC CID = WOOD FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = ASH FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = CHAR FLOW = 39935.5012 <-80> <2> \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = ULTANAL ELEM = ( 0.92 <0> <0> 50.88 <0> <0> 6.04 <0> <0> 0.17 <0> <0> 0. <0> <0> 0.09 <0> <0> 41.9 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.045 <0> <0> 0.045 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 15.29 <0> <0> 83.84 <0> <0> 0.87 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = GENANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> 100. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = ULTANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = ULTANAL ELEM = ( 4.23192238 <0> <0> 72.0117114 <0> <0> 6.12402559 <0> <0> 0.05161105 <0> <0> 0. <0> <0> 0.03436137 <0> <0> 17.5463682 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.01718068 <0> <0> 0.01718068 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 87.18 <0> <0> 12.81 <0> <0> 0.01 <0> <0> ) \ ? STREAM MATERIAL "A200.A200CC.206" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 22. <20> <2> BASIS = "MOLE-FRAC" FLOWBASE = MOLE TOTFLOW = 1E-006 <-89> <2> TOTAL = 1. <-4> <0> JUNK = 9 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.011 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.005 <-4> <0> / SSID1 = MIXED CID = H2S FLOW = 4E-006 <-4> <0> / SSID1 = MIXED CID = CH4 FLOW = 0.943996 <-4> <0> / SSID1 = MIXED CID = C2H6 FLOW = 0.031 <-4> <0> / SSID1 = MIXED CID = C3H8 FLOW = 0.005 <-4> <0> / SSID1 = MIXED CID = "I-C4H10" FLOW = 0.001 <-4> <0> / SSID1 = MIXED CID = "N-C4H10" FLOW = 0.001 <-4> <0> / SSID1 = MIXED CID = "PENTANE+" FLOW = 0.002 <-4> <0> \ ? STREAM MATERIAL "A200.A200CC.208" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 1. <20> <3> BASIS = "MOLE-FRAC" FLOWBASE = MOLE TOTFLOW = 14000. <-89> <2> TOTAL = 1. <-4> <0> JUNK = 5 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.75666 <-4> <0> / SSID1 = MIXED CID = O2 FLOW = 0.202967 <-4> <0> / SSID1 = MIXED CID = AR FLOW = 0.00905 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.00032 <-4> <0> / SSID1 = MIXED CID = H2O FLOW = 0.031003 <-4> <0> \ ? STREAM MATERIAL "A200.A200CC.218" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A200.A200CC.220" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 60. <22> <2> PRES = 25. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = CISOLID CID = OLIVINE FLOW = 1. <-3> <0> \ \ COMMENTS COMMENTS = ( ";Substitued Olivine for MgO in composition" ) \ ? STREAM MATERIAL "A200.A200CC.221" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 60. <22> <2> PRES = 22. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-3> <0> JUNK = 1 \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = CISOLID CID = OLIVINE FLOW = 1. <-3> <0> \ ? STREAM HEAT "A200.A200CC.QR202" ? ; "ENG_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 1000. <13> <2> \ ? BLOCK MIXER "A200.A200CC.C-201" ? ; "ENG_MOLE" ; ; SCREW ; \ DESCRIPTION DESCRIPTION = "Sand/Ash Conditioner/Cooler" \ ? BLOCK MIXER "A200.A200CC.MX200B" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM NPHASE = 1 PHASE = S MAXIT = 150 TOL = 0.1 <0> <0> T-EST = 1620. <22> <2> \ \ PROPERTIES OPSETNAME = SOLIDS \ \ "BLOCK-OPTION" TERM-LEVEL = 0 BLKOPFREWAT = NO \ ? BLOCK MIXER "A200.A200CC.MX200C" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A200.A200CC.MX200D" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK SEP "A200.A200CC.S-203" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Primary Combustor Cyclone Filter" \ \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = CARBON FRACS = 0.99 <0> <0> / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0.99 <0> <0> / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0.9999 <0> <0> / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 211 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 211 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0.6 <0> <0> / PARAM-STREAM = 211 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0.6 <0> <0> / PARAM-STREAM = 211 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0.9999 <0> <0> / PARAM-STREAM = 211 SUBSTREAM = NC COMPS = WOOD FRACS = 0.999 <0> <0> / PARAM-STREAM = 211 SUBSTREAM = NC COMPS = ASH FRACS = 0.05 <0> <0> / PARAM-STREAM = 211 SUBSTREAM = NC COMPS = CHAR FRACS = 0.999 <0> <0> / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 212 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 212 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 212 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 212 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 212 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 212 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 212 SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = 211 PRES = 25. <20> <2> \ \ FLASH-SPECS FLASH-STREAM = 212 PRES = 22. <20> <2> \ ? BLOCK SEP "A200.A200CC.S-204" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Secondary Combustion Cyclone Filter" \ \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = CARBON FRACS = 0.999 <0> <0> / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0.999 <0> <0> / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0.999 <0> <0> / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 214 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 214 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0.999 <0> <0> / PARAM-STREAM = 214 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0.999 <0> <0> / PARAM-STREAM = 214 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0.999 <0> <0> / PARAM-STREAM = 214 SUBSTREAM = NC COMPS = WOOD FRACS = 0.999 <0> <0> / PARAM-STREAM = 214 SUBSTREAM = NC COMPS = ASH FRACS = 0.999 <0> <0> / PARAM-STREAM = 214 SUBSTREAM = NC COMPS = CHAR FRACS = 0.999 <0> <0> / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 213 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 213 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 213 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 213 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 213 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 213 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 213 SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = 214 PRES = -0.3 <20> <2> \ \ FLASH-SPECS FLASH-STREAM = 213 PRES = 0. <20> <2> \ ? BLOCK SEP "A200.A200CC.S-205" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Electrostatic Precipitator" \ \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 1. <0> <0> / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 215 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 215 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = 215 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = 215 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 1. <0> <0> / PARAM-STREAM = 215 SUBSTREAM = NC COMPS = WOOD FRACS = 1. <0> <0> / PARAM-STREAM = 215 SUBSTREAM = NC COMPS = ASH FRACS = 1. <0> <0> / PARAM-STREAM = 215 SUBSTREAM = NC COMPS = CHAR FRACS = 1. <0> <0> / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 286 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 286 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 286 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 286 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 286 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 286 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 286 SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = 215 PRES = -0.3 <20> <2> \ \ FLASH-SPECS FLASH-STREAM = 286 PRES = 0. <20> <2> \ ? BLOCK HEATER "A200.A200CC.H-209" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 400. <22> <2> PRES = -0.1 <20> <2> \ ? BLOCK HEATER "A200.A200CC.H-286" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Flue Gas Cooler/Steam Generator #3" \ \ PARAM TEMP = 1100. <22> <2> PRES = -0.1 <20> <2> \ ? BLOCK HEATER "A200.A200CC.M-201" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Sand/Ash Cooler" \ \ PARAM TEMP = 300. <22> <2> PRES = 1. <20> <3> \ \ COMMENTS COMMENTS = ( ";Hollow Flite Screw Conveyor" ) \ ? BLOCK RSTOIC "A200.A200CC.R-202" ? ; "ENG_MASS" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Char Combustor" \ \ PARAM TEMP = 1805. <22> <2> PRES = 0. <20> <2> HEAT-OF-REAC = "NO-CALC-SPEC" COMBUSTION = YES PROD-NOX = NO2 \ \ FORCONTROL FCVAR1 = H2O \ \ COMMENTS COMMENTS = ( ";Combusts char supplying heat for gasifier (design " ";spec combctrl)" ) \ ? BLOCK COMPR "A200.A200CC.K-202" ? ; "ENG_MASS" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "Combustion Air Blower" \ \ PARAM TYPE = "GPSA-POLYTROP" OPT-SPEC = PRES PRES = 22. <20> <2> \ \ COMMENTS COMMENTS = ( ";Air blower to provide combustion air to the char " ";combustor." ) \ ? BLOCK USER "A200.A200CC.USER200A" ? ; "ENG_MASS" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Char decomposition block" \ \ SUBROUTINE USRMODEL = USRDC1 \ \ PROPERTIES OPSETNAME = SYSOP3 COPSETNAME = SYSOP3 \ \ COMMENTS COMMENTS = ( ";Decomposes the char into elemental molecules: H2, O2, N2, " ";C and S; ash and water are not changed." ) \ ? REPORT "A200.A200CC.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A200.HV-224" ? ; BLOCK ; ? "A200.HV-224.SOLVE" ? ? FLOWSHEET "A200.HV-224.GLOBAL" ? \ BLOCK BLKID = DPL100 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( "100-IN" M0-1 ) OUT = ( "100-OUT" M0-1 RAW M0-1 ) \ \ BLOCK BLKID = REJECT BLKTYPE = SEP MDLTYPE = "Sep" IN = ( RAW M0-1 ) OUT = ( BASIS M0-1 REJECT M0-1 QREJECT Q1-4 ) \ \ BLOCK BLKID = BURN BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( BASIS M0-1 O2 M0-1 ) OUT = ( QCOMB Q2-3 "PROD-1" M0-1 ) \ \ BLOCK BLKID = COMBSEP BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( "PROD-2" M0-1 ) OUT = ( COMBVAP M0-1 COMBLIQ M1-2 ) \ \ BLOCK BLKID = VAPWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( COMBLIQ M0-1 ) OUT = ( DPT M0-1 "QVAP-1" Q2-3 ) \ \ BLOCK BLKID = CONDWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( "WATER-V" M0-1 ) OUT = ( "WATER-L" M0-1 "QVAP-2" Q2-3 ) \ \ BLOCK BLKID = DRYER BLKTYPE = SEP MDLTYPE = "Sep" IN = ( DPT M0-1 COMBVAP M0-1 ) OUT = ( "WATER-V" M0-1 RESIDUE M0-1 ) \ \ BLOCK BLKID = NET BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-1" Q1-4 QCOMB Q1-4 QSHIFT Q1-4 ) OUT = ( QNET Q1-3 ) \ \ BLOCK BLKID = GROSS BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-2" Q1-4 QNET Q1-4 ) OUT = ( QGROSS Q1-3 ) \ \ BLOCK BLKID = SHIFT BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( "PROD-1" M0-1 ) OUT = ( "PROD-2" M0-1 QSHIFT Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A200.HV-224.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A200.HV-224.STREAM-NAMES" ? \ NAMES STREAM = "100-IN" TEXT = "Feed material" \ ? STREAM MATERIAL "A200.HV-224.100-IN" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 1.E-006 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TEMP = 60. <22> <2> PRES = 1. <20> <3> TOTAL = 3.E-006 <-80> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = WOOD FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = ASH FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = CHAR FLOW = 1E-006 <-80> <2> \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = ULTANAL ELEM = ( 0.92 <0> <0> 50.88 <0> <0> 6.04 <0> <0> 0.17 <0> <0> 0. <0> <0> 0.09 <0> <0> 41.9 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.045 <0> <0> 0.045 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 15.29 <0> <0> 83.84 <0> <0> 0.87 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = GENANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> 100. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = ULTANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = ULTANAL ELEM = ( 3.168 <0> <0> 65.894 <0> <0> 3.064 <0> <0> 0.281 <0> <0> 0. <0> <0> 0.149 <0> <0> 27.444 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.0745 <0> <0> 0.0745 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 87.18 <0> <0> 12.81 <0> <0> 0.01 <0> <0> ) \ \ COMMENTS COMMENTS = ( ";Poplar composition per Craig, K.R., Mann, M.K., " ";""Cost and Performance Analysis of Biomass-Bases " ";Integrated Gasification Combined-Cycle (BIGCC) Power " ";Systems"", National Renewable Energy Laboratory, " ";NREL/TP-430-21657, October, 1996." ";Modified sulfur analysis as follows: Evenly " ";distributed sulfur between sulfate and organic, with " ";no sulfur being classified as pyritic" ) \ ? STREAM MATERIAL "A200.HV-224.O2" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 77. <22> <2> PRES = 1. <20> <3> TOTAL = 9000. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = O2 FLOW = 9000. <-89> <2> \ ? BLOCK MIXER "A200.HV-224.GROSS" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A200.HV-224.NET" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK SEP "A200.HV-224.DRYER" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = METHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = "WATER-V" TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK SEP "A200.HV-224.REJECT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2O FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2S FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NH3 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CH4 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H4 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C3H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C6H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C10H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = METHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = BASIS TEMP = 77. <22> <2> PRES = 1. <20> <3> \ ? BLOCK HEATER "A200.HV-224.CONDWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A200.HV-224.VAPWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK FLASH2 "A200.HV-224.COMBSEP" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK RSTOIC "A200.HV-224.BURN" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 0. <20> <2> COMBUSTION = YES PROD-NOX = NO2 \ \ STOIC REACNO = 1 STOIC-CID = WOOD STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CHAR STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = NC KEY-CID = WOOD CONV = 1. <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = NC KEY-CID = CHAR CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = NO2 \ ? BLOCK RSTOIC "A200.HV-224.SHIFT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 1. <20> <3> \ \ STOIC REACNO = 1 STOIC-CID = NO2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = 0.5 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = NO2 CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = O2 \ ? BLOCK DUPL "A200.HV-224.DPL100" ? ; "ENG_MOLE" ; ; BLOCK ; ? REPORT "A200.HV-224.BLOCK-REPORT" ? ? REPORT "A200.BLOCK-REPORT" ? ? BLOCK HIERARCHY A300 ? ; BLOCK ; ? "A300.SOLVE" ? ? FLOWSHEET "A300.GLOBAL" ? \ BLOCK BLKID = A300AGR BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-14" IN = ( 463 M3-0 ) OUT = ( "A300AGR.463" M3-0 ) \ \ CONNECT BLKID = "$C-17" IN = ( 331 M4-0 ) OUT = ( "A300AGR.331" M4-0 ) \ \ CONNECT BLKID = "$C-15" IN = ( "A300AGR.362" M5-0 ) OUT = ( 362 M3-0 ) \ \ CONNECT BLKID = "$C-16" IN = ( "A300AGR.361" M6-0 ) OUT = ( 361 M4-0 ) \ \ CONNECT BLKID = "$C-19" IN = ( "A300AGR.351" M7-0 ) OUT = ( 351 M5-0 ) \ \ CONNECT BLKID = "$C-18" IN = ( "A300AGR.319B" M8-0 ) OUT = ( 319B M6-0 ) \ \ BLOCK BLKID = A300Q BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-9" IN = ( 330 M3-0 ) OUT = ( "A300Q.330" M3-0 ) \ \ CONNECT BLKID = "$C-3" IN = ( "A300Q.331" M4-0 ) OUT = ( 331 M3-0 ) \ \ CONNECT BLKID = "$C-8" IN = ( "A300Q.305" M5-0 ) OUT = ( 305 M4-0 ) \ \ CONNECT BLKID = "$C-4" IN = ( "A300Q.314" M6-0 ) OUT = ( 314 M5-0 ) \ \ CONNECT BLKID = "$C-11" IN = ( "A300Q.WK301" W7-0 ) OUT = ( WK301 W6-0 ) \ \ CONNECT BLKID = "$C-6" IN = ( "A300Q.QAK301" Q8-0 ) OUT = ( QAK301 Q7-0 ) \ \ BLOCK BLKID = A300S BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-20" IN = ( 322 M3-0 ) OUT = ( "A300S.322" M3-0 ) \ \ CONNECT BLKID = "$C-21" IN = ( 319B M4-0 ) OUT = ( "A300S.319B" M4-0 ) \ \ CONNECT BLKID = "$C-25" IN = ( "A300S.324" M5-0 ) OUT = ( 324 M3-0 ) \ \ CONNECT BLKID = "$C-10" IN = ( "A300S.384REC" M6-0 ) OUT = ( 384REC M4-0 ) \ \ CONNECT BLKID = "$C-23" IN = ( "A300S.384VENT" M7-0 ) OUT = ( 384VENT M5-0 ) \ \ CONNECT BLKID = "$C-1" IN = ( "A300S.395" M8-0 ) OUT = ( 395 M6-0 ) \ \ BLOCK BLKID = A300TR BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-7" IN = ( 225A M3-0 ) OUT = ( "A300TR.225A" M3-0 ) \ \ CONNECT BLKID = "$C-2" IN = ( 384RECIN M4-0 ) OUT = ( "A300TR.384REC" M4-0 ) \ \ CONNECT BLKID = "$C-12" IN = ( 513 M5-0 ) OUT = ( "A300TR.513" M5-0 ) \ \ CONNECT BLKID = "$C-27" IN = ( 225F M6-0 ) OUT = ( "A300TR.225F" M6-0 ) \ \ CONNECT BLKID = "$C-13" IN = ( 426 M7-0 ) OUT = ( "A300TR.426F" M7-0 ) \ \ CONNECT BLKID = "$C-5" IN = ( "A300TR.330" M8-0 ) OUT = ( 330 M3-0 ) \ \ CONNECT BLKID = "$C-26" IN = ( "A300TR.335" M9-0 ) OUT = ( 335 M4-0 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A300.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ ? "A300.STREAM-NAMES" ? ? STREAM MATERIAL "A300.322" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 1. <20> <3> BASIS = "MOLE-FRAC" TOTFLOW = 1E-006 <-89> <2> TOTAL = 1. <-4> <0> JUNK = 5 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.75666 <-4> <0> / SSID1 = MIXED CID = O2 FLOW = 0.202967 <-4> <0> / SSID1 = MIXED CID = AR FLOW = 0.00905 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.00032 <-4> <0> / SSID1 = MIXED CID = H2O FLOW = 0.031003 <-4> <0> \ ? STREAM MATERIAL "A300.384RECIN" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 28.1 <22> <2> PRES = 20. <20> <2> BASIS = "MOLE-FRAC" FLOWBASE = MOLE TOTFLOW = 1E-005 <-89> <2> TOTAL = 1. <-4> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = CO2 FLOW = 0.99999 <-4> <0> / SSID1 = MIXED CID = H2S FLOW = 1E-005 <-4> <0> \ ? STREAM MATERIAL "A300.463" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 142.3 <22> <2> PRES = 450. <20> <2> BASIS = "MASS-FLOW" TOTAL = 1.E-003 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 0.001 <-80> <2> \ ? BLOCK HIERARCHY "A300.A300AGR" ? ; BLOCK ; ? "A300.A300AGR.SOLVE" ? ? FLOWSHEET "A300.A300AGR.GLOBAL" ? \ BLOCK BLKID = "S-311" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 463 M0-1 358 M0-1 ) OUT = ( 362 M0-1 361 M1-2 ) \ \ BLOCK BLKID = "S-310" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 331 M0-1 ) OUT = ( 319 M0-1 358 M0-1 QS310 Q1-4 ) \ \ BLOCK BLKID = LEANCOOL BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( "AM-CLDHP" M0-1 ) OUT = ( "AM-HOT" M0-1 "QH-LEANA" Q2-3 ) \ \ BLOCK BLKID = CONDUTY BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( AIRCOOL M0-1 QAMCON Q1-2 ) OUT = ( AIRHOT M0-1 ) \ \ BLOCK BLKID = "H-300D" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 319 M0-1 ) OUT = ( 319B M0-1 QH300D Q2-3 ) \ \ BLOCK BLKID = AMCOLDTY BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( AIRDUMY M0-1 QACOOL Q1-2 ) OUT = ( AIRDUMO M0-1 ) \ \ BLOCK BLKID = "P-300AM" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( "AM-COLD" M0-1 ) OUT = ( "AM-CLDHP" M0-1 WKAMLIQ W2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? FLOWSHEET "A300.A300AGR.STEAM" ? \ BLOCK BLKID = "H-300RB" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 350 M0-1 ) OUT = ( QH300RB Q2-3 351 M0-1 ) \ ? PROPERTIES "A300.A300AGR.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ \ PROPERTIES SECID-LIST = STEAM BASEOPSET = "STEAM-TA" OPSETNAME = "STEAM-TA" \ ? "A300.A300AGR.STREAM-NAMES" ? ? STREAM MATERIAL "A300.A300AGR.350" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 394.9828 <22> <2> PRES = 50. <20> <13> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1000. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A300.A300AGR.463" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 142.3 <22> <2> PRES = 450. <20> <2> BASIS = "MASS-FLOW" TOTAL = 1.E-003 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 0.001 <-80> <2> \ ? STREAM MATERIAL "A300.A300AGR.AIRCOOL" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 1.01 <20> <3> BASIS = "MOLE-FRAC" FLOWBASE = MASS TOTFLOW = 2000000. <-80> <2> TOTAL = 1. <-4> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.79 <-4> <0> / SSID1 = MIXED CID = O2 FLOW = 0.21 <-4> <0> \ ? STREAM MATERIAL "A300.A300AGR.AIRDUMY" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 1.01 <20> <3> FLOWBASE = MASS TOTFLOW = 2000000. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.79 <-89> <2> / SSID1 = MIXED CID = O2 FLOW = 0.21 <-89> <2> \ ? STREAM MATERIAL "A300.A300AGR.AM-COLD" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 110. <22> <2> PRES = 15. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = VOLUME TOTFLOW = 1. <-99> <4> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 0.65 <-3> <0> / SSID1 = MIXED CID = AMINE FLOW = 0.35 <-3> <0> \ ? STREAM HEAT "A300.A300AGR.QACOOL" ? ; "ENG_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 1. <13> <2> TEMP = 212. <22> <2> TEND = 140. <22> <2> \ ? STREAM HEAT "A300.A300AGR.QAMCON" ? ; "ENG_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 1. <13> <2> TEMP = 212. <22> <2> TEND = 212. <22> <2> \ ? BLOCK SEP "A300.A300AGR.S-310" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 PRES1 = -5. <20> <2> FLAG = 0 \ \ PARAM PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = CO2 FRACS = 0.50299 <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = H2O FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = H2S FRACS = 0.84287 <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = METHANOL FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 319 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = 319 SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 358 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 358 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 358 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 358 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 358 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 358 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 358 SUBSTREAM = NC COMPS = CHAR \ \ PROPERTIES OPSETNAME = SYSOP3 FRWATEROPSET = "STEAM-TA" \ ? BLOCK HEATER "A300.A300AGR.AMCOLDTY" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = 0. <20> <3> \ ? BLOCK HEATER "A300.A300AGR.CONDUTY" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "dummy block just to enable QAMCOND to have a physical location" \ \ PARAM PRES = 0. <20> <3> \ ? BLOCK HEATER "A300.A300AGR.H-300D" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 140. <22> <2> PRES = 35. <20> <2> \ ? BLOCK HEATER "A300.A300AGR.H-300RB" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 230. <22> <2> PRES = -5. <20> <2> \ ? BLOCK HEATER "A300.A300AGR.LEANCOOL" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 232. <22> <2> PRES = 450. <20> <2> \ ? BLOCK FLASH2 "A300.A300AGR.S-311" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ \ PROPERTIES OPSETNAME = SYSOP3 \ ? BLOCK PUMP "A300.A300AGR.P-300AM" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PRES = 450. <20> <2> OPT-SPEC = PRES \ ? REPORT "A300.A300AGR.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A300.A300Q" ? ; BLOCK ; ? "A300.A300Q.SOLVE" ? ? FLOWSHEET "A300.A300Q.GLOBAL" ? \ BLOCK BLKID = "K-301" BLKTYPE = MCOMPR MDLTYPE = "MCompr" IN = ( 315 M0-1 ) OUT = ( 316 M1-2 317 M0-1 WK301A W3-4 WK301B W3-4 WK301C W3-4 WK301D W3-4 WK301E W3-4 QAK301A Q4-5 QAK301B Q4-5 QAK301C Q4-5 QAK301D Q4-5 QAK301E Q4-5 ) \ \ BLOCK BLKID = "H-303" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 317 M0-1 ) OUT = ( QCH303 Q2-3 318 M0-1 ) \ \ BLOCK BLKID = "S-303" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 318 M0-1 ) OUT = ( 332 M1-2 QS303 Q3-4 331 M0-1 ) \ \ BLOCK BLKID = PROP300C BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 304 M0-1 ) OUT = ( 305 M0-1 QPRP300C Q2-3 ) \ \ BLOCK BLKID = PROP300B BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 312 M0-1 ) OUT = ( QPRP300B Q2-3 313 M0-1 ) \ \ BLOCK BLKID = "S-301" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 313 M0-1 316 M0-1 ) OUT = ( 315 M0-1 315L M1-2 ) \ \ BLOCK BLKID = MX300A BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WK301A W2-7 WK301B W2-7 WK301C W2-7 WK301D W2-7 WK301E W2-7 ) OUT = ( WK301 W2-4 ) \ \ BLOCK BLKID = MX300B BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QAK301A Q1-4 QAK301C Q1-4 QAK301D Q1-4 QAK301B Q1-4 QAK301E Q1-4 ) OUT = ( QAK301 Q1-3 ) \ \ BLOCK BLKID = PROP300D BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 334 M0-1 ) OUT = ( 335 M0-1 QPRP300D Q2-3 ) \ \ BLOCK BLKID = "P-301" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 335 M0-1 ) OUT = ( 336 M0-1 WP301 W2-3 ) \ \ BLOCK BLKID = "H-301A" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 330 M0-1 ) OUT = ( QH301A Q2-3 330B M0-1 ) \ \ BLOCK BLKID = "H-301B" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 330B M0-1 ) OUT = ( 300 M0-1 QH301B Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? FLOWSHEET "A300.A300Q.SOUR" ? \ BLOCK BLKID = MULT300B BLKTYPE = MULT MDLTYPE = "Mult" IN = ( 306 M0-1 ) OUT = ( 307 M0-1 ) \ \ BLOCK BLKID = "P-302" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 307 M0-1 ) OUT = ( 308 M0-1 WP302 W2-3 ) \ \ BLOCK BLKID = V300A BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 308 M0-1 ) OUT = ( 309 M0-1 ) \ \ BLOCK BLKID = "M-301A" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( "QCM301-" Q1-2 309 M0-1 ) OUT = ( 310 M0-1 ) \ \ BLOCK BLKID = V300B BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 310 M0-1 ) OUT = ( 311 M0-1 ) \ \ BLOCK BLKID = MULT300A BLKTYPE = MULT MDLTYPE = "Mult" IN = ( QCM301 Q1-2 ) OUT = ( "QCM301-" Q1-2 ) \ \ BLOCK BLKID = DPL300A BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( 303 M0-1 ) OUT = ( 304 M0-1 306 M0-1 ) \ \ BLOCK BLKID = PROP300A BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 300 M0-1 ) OUT = ( 301 M0-1 QPRP300A Q2-3 ) \ \ BLOCK BLKID = "M-301" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 301 M0-1 ) OUT = ( QCM301 Q3-4 312 M0-1 302 M1-2 ) \ \ BLOCK BLKID = "T-301" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 302 M0-1 332B M0-1 ) OUT = ( QT301 Q1-4 334 M0-1 303 M0-1 ) \ \ BLOCK BLKID = PROP300E BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 332 M0-1 ) OUT = ( 332B M0-1 QPRP300E Q2-3 ) \ \ BLOCK BLKID = "P-314" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 315L M0-1 ) OUT = ( 314 M0-1 WP314 W2-3 ) \ \ BLOCK BLKID = MX301 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QH301A Q1-4 QH301B Q1-4 ) OUT = ( QH301 Q1-3 ) \ ? PROPERTIES "A300.A300Q.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ \ PROPERTIES SECID-LIST = SOUR BASEOPSET = ELECNRTL OPSETNAME = ELECNRTL H-COMPS = SOURHENR CHEMISTRY = SOURCHEM TRUE-COMPS = NO \ ? "A300.A300Q.STREAM-NAMES" ? ? STREAM MATERIAL "A300.A300Q.315" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 146.5 <22> <2> PRES = 15. <20> <2> BASIS = "MASS-FLOW" TOTAL = 342315.0035 <-80> <0> JUNK = 21 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2 FLOW = 10110.4938 <-80> <2> / SSID1 = MIXED CID = CO FLOW = 130547.693 <-80> <2> / SSID1 = MIXED CID = N2 FLOW = 262.537045 <-80> <2> / SSID1 = MIXED CID = O2 FLOW = 0. <-80> <2> / SSID1 = MIXED CID = AR FLOW = 0. <-80> <2> / SSID1 = MIXED CID = CO2 FLOW = 140702.7 <-80> <2> / SSID1 = MIXED CID = H2O FLOW = 56465.4136 <-80> <2> / SSID1 = MIXED CID = H2S FLOW = 162.134561 <-80> <2> / SSID1 = MIXED CID = SO2 FLOW = 0. <-80> <2> / SSID1 = MIXED CID = NH3 FLOW = 33.2529712 <-80> <2> / SSID1 = MIXED CID = NO2 FLOW = 0. <-80> <2> / SSID1 = MIXED CID = CH4 FLOW = 3167.78314 <-80> <2> / SSID1 = MIXED CID = C2H6 FLOW = 5.64251076 <-80> <2> / SSID1 = MIXED CID = C2H4 FLOW = 783.451337 <-80> <2> / SSID1 = MIXED CID = C2H2 FLOW = 68.1493904 <-80> <2> / SSID1 = MIXED CID = C3H8 FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "I-C4H10" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "N-C4H10" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "PENTANE+" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = C6H6 FLOW = 5.64691569 <-80> <2> / SSID1 = MIXED CID = C10H8 FLOW = 0.10526231 <-80> <2> \ ? STREAM MATERIAL "A300.A300Q.316" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 140.1 <22> <2> PRES = 15. <20> <2> BASIS = "MASS-FLOW" TOTAL = 35743.5 <-80> <0> JUNK = 3 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = CO2 FLOW = 2.5 <-80> <2> / SSID1 = MIXED CID = H2O FLOW = 35722. <-80> <2> / SSID1 = MIXED CID = NH3 FLOW = 19. <-80> <2> \ ? STREAM MATERIAL "A300.A300Q.332" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 110. <22> <2> PRES = 460. <20> <2> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 545. <-80> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 542. <-80> <2> / SSID1 = MIXED CID = NH3 FLOW = 3. <-80> <2> \ ? BLOCK MIXER "A300.A300Q.MX300A" ? ; "ENG_MOLE" ; ; WORK ; ? BLOCK MIXER "A300.A300Q.MX300B" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK MIXER "A300.A300Q.MX301" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK SEP "A300.A300Q.T-301" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Sludge Settling Tank" \ \ PARAM1 FLAG = 1 \ \ PARAM PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = H2O FLOWS = 0. <-80> <2> FLOWBASIS = MASS / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 334 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 334 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = 334 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = 334 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 1. <0> <0> / PARAM-STREAM = 334 SUBSTREAM = NC COMPS = WOOD FRACS = 1. <0> <0> / PARAM-STREAM = 334 SUBSTREAM = NC COMPS = ASH FRACS = 1. <0> <0> / PARAM-STREAM = 334 SUBSTREAM = NC COMPS = CHAR FRACS = 1. <0> <0> / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 303 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 303 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 303 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 303 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 303 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 303 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 303 SUBSTREAM = NC COMPS = CHAR \ ? BLOCK HEATER "A300.A300Q.H-301A" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Post-Tar Reformer Cooler/Steam Generator and BFW Preheater" \ \ PARAM TEMP = 140. <22> <2> PRES = -2. <20> <2> \ \ COMMENTS COMMENTS = ( ";This heat exchanger is actually two heat exchangers " ";on the PFD. The first post tar reformer cooler, and " ";its heat is used to generate system steam. The " ";second post tar reformer cooler, and its heat is " ";used to preheat the boiler feed water for the steam " ";system." ) \ ? BLOCK HEATER "A300.A300Q.H-301B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 140. <22> <2> PRES = 0. <20> <2> \ ? BLOCK HEATER "A300.A300Q.H-303" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Water-Cooler Aftercooler" \ \ PARAM TEMP = 110. <22> <2> PRES = -5. <20> <2> \ \ COMMENTS COMMENTS = ( ";Compressor final stage cooler (cooling water). The " ";final stage aftercooler in the compressor block " ";assumes air cooling." ) \ ? BLOCK HEATER "A300.A300Q.M-301A" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = -5. <20> <2> \ ? BLOCK HEATER "A300.A300Q.PROP300A" ? ; "ENG_MOLE" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Property Change" \ \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ \ COMMENTS COMMENTS = ( ";This is not a physical exchanger. It's purpose is " ";to explicitly handle the conversion from the GLOBAL " ";property package to the SOUR property package. This " ";is needed for cross-checks of the material and " ";energy balances" ) \ ? BLOCK HEATER "A300.A300Q.PROP300B" ? ; "ENG_MOLE" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Property Change" \ \ PARAM PRES = 0. <20> <2> VFRAC = 1. <0> <0> \ \ COMMENTS COMMENTS = ( ";This is not a physical exchanger. It's purpose is to " ";explicitly handle the conversion from the SOUR " ";property package to the GLOBAL property package. " ";This is needed for cross-checks of the material and " ";energy balances" ) \ ? BLOCK HEATER "A300.A300Q.PROP300C" ? ; "ENG_MOLE" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Property Change" \ \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ \ COMMENTS COMMENTS = ( ";This is not a physical exchanger. It's purpose is " ";to explicitly handle the conversion from the SOUR " ";property package to the GLOBAL property package. " ";This is needed for cross-checks of the material and " ";energy balances." ) \ ? BLOCK HEATER "A300.A300Q.PROP300D" ? ; "ENG_MOLE" ; ; BLOCK ; \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ ? BLOCK HEATER "A300.A300Q.PROP300E" ? ; "ENG_MOLE" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Property Change" \ \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ \ COMMENTS COMMENTS = ( ";This is not a physical exchanger. It's purpose is " ";to explicitly handle the conversion from the GLOBAL " ";property package to the SOUR property package. This " ";is needed for cross-checks of the material and " ";energy balances" ) \ ? BLOCK FLASH2 "A300.A300Q.M-301" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "Syngas Quench Chamber" \ \ PARAM TEMP = 130. <22> <2> PRES = 15. <20> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK FLASH2 "A300.A300Q.S-301" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "Pre-Compressor Knock-Out" \ \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK FLASH2 "A300.A300Q.S-303" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "Post-Compressor Knock-Out" \ \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK PUMP "A300.A300Q.P-301" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Sludge Pump" \ \ PARAM PRES = 20. <20> <13> OPT-SPEC = PRES \ ? BLOCK PUMP "A300.A300Q.P-302" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Quench Water Recirculation Pump" \ \ PARAM DELP = 20. <75> <2> OPT-SPEC = DELP \ ? BLOCK PUMP "A300.A300Q.P-314" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PRES = 35. <20> <2> OPT-SPEC = PRES \ ? BLOCK MCOMPR "A300.A300Q.K-301" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Syngas Compressor" \ \ PARAM NSTAGE = 5 TYPE = "ASME-POLYTROPIC" PRES = 430. <20> <2> OPT-SPEC = PRES \ \ FEEDS FEED-SID = 315 FEED-STAGE = 1 \ \ PRODUCTS PROD-STREAM = 316 GLOBAL = Y PROD-PHASE = L / PROD-STREAM = 317 PROD-STAGE = 5 \ \ Q-PRODUCTS Q-PROD-STRM = QAK301A Q-PROD-STAGE = 1 / Q-PROD-STRM = QAK301B Q-PROD-STAGE = 2 / Q-PROD-STRM = QAK301C Q-PROD-STAGE = 3 / Q-PROD-STRM = QAK301D Q-PROD-STAGE = 4 / Q-PROD-STRM = QAK301E Q-PROD-STAGE = 5 \ \ W-PRODUCTS W-PROD-STRM = WK301A W-PROD-STAGE = 1 / W-PROD-STRM = WK301B W-PROD-STAGE = 2 / W-PROD-STRM = WK301C W-PROD-STAGE = 3 / W-PROD-STRM = WK301D W-PROD-STAGE = 4 / W-PROD-STRM = WK301E W-PROD-STAGE = 5 \ \ COMPR-SPECS C-S-STAGE = 1 PEFF = 0.78 <0> <0> / C-S-STAGE = 2 PEFF = 0.78 <0> <0> / C-S-STAGE = 3 PEFF = 0.78 <0> <0> / C-S-STAGE = 4 PEFF = 0.78 <0> <0> / C-S-STAGE = 5 PEFF = 0.78 <0> <0> \ \ COOLER-SPECS CL-STAGE = 1 CL-TEMP = 140. <22> <2> PDROP = 2. <75> <2> OPT-CLSPEC = TEMP / CL-STAGE = 2 CL-TEMP = 140. <22> <2> PDROP = 2. <75> <2> OPT-CLSPEC = TEMP / CL-STAGE = 3 CL-TEMP = 140. <22> <2> PDROP = 5. <75> <2> OPT-CLSPEC = TEMP / CL-STAGE = 4 CL-TEMP = 140. <22> <2> PDROP = 5. <75> <2> OPT-CLSPEC = TEMP / CL-STAGE = 5 CL-TEMP = 140. <22> <2> DUTY = 0. <13> <2> PDROP = 5. <75> <2> OPT-CLSPEC = TEMP \ ? BLOCK MULT "A300.A300Q.MULT300A" ? ; "ENG_MOLE" ; ; HEAT ; \ PARAM FACTOR = -1. <0> <0> \ ? BLOCK MULT "A300.A300Q.MULT300B" ? ; "ENG_MOLE" ; ; BLOCK ; \ PARAM FACTOR = 80. <0> <0> \ ? BLOCK DUPL "A300.A300Q.DPL300A" ? ; "ENG_MOLE" ; ; BLOCK ; ? BLOCK VALVE "A300.A300Q.V300A" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM OPT-DESIGN = "P-DROP" P-DROP = 10. <75> <2> \ ? BLOCK VALVE "A300.A300Q.V300B" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM OPT-DESIGN = "P-DROP" P-DROP = 5. <75> <2> \ ? REPORT "A300.A300Q.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A300.A300S" ? ; BLOCK ; ? "A300.A300S.SOLVE" ? ? FLOWSHEET "A300.A300S.GLOBAL" ? \ BLOCK BLKID = "R-304" BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 322 M0-1 321 M0-1 ) OUT = ( 323 M0-1 QR304 Q2-3 ) \ \ BLOCK BLKID = "R-304A" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 323 M0-1 ) OUT = ( QR304A Q1-4 324 M0-1 325 M0-1 ) \ \ BLOCK BLKID = "SP-384" BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 357 M0-1 ) OUT = ( 384VENT M0-1 384REC M0-1 ) \ \ BLOCK BLKID = "M-304" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 320 M0-1 ) OUT = ( 321 M0-1 QM304 Q1-4 357 M0-1 ) \ \ BLOCK BLKID = "H-304" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 319B M0-1 ) OUT = ( 320 M0-1 QH304 Q2-3 ) \ \ BLOCK BLKID = MIXQH304 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QH304+" Q1-4 QH304 Q1-4 ) OUT = ( QH304EX Q1-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? FLOWSHEET "A300.A300S.STEAM" ? \ BLOCK BLKID = "H-304+" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 394 M0-1 ) OUT = ( 395 M0-1 "QH304+" Q2-3 ) \ ? PROPERTIES "A300.A300S.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 \ \ PROPERTIES SECID-LIST = STEAM BASEOPSET = "STEAM-TA" OPSETNAME = "STEAM-TA" \ ? "A300.A300S.STREAM-NAMES" ? ? STREAM MATERIAL "A300.A300S.322" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 1. <20> <3> BASIS = "MOLE-FRAC" TOTFLOW = 1E-006 <-89> <2> TOTAL = 1. <-4> <0> JUNK = 5 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.75666 <-4> <0> / SSID1 = MIXED CID = O2 FLOW = 0.202967 <-4> <0> / SSID1 = MIXED CID = AR FLOW = 0.00905 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.00032 <-4> <0> / SSID1 = MIXED CID = H2O FLOW = 0.031003 <-4> <0> \ ? STREAM MATERIAL "A300.A300S.357" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 150. <22> <2> PRES = 20. <20> <2> BASIS = "MASS-FLOW" TOTAL = 83175. <-80> <0> JUNK = 6 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2 FLOW = 8000. <-80> <2> / SSID1 = MIXED CID = CO FLOW = 58563. <-80> <2> / SSID1 = MIXED CID = H2O FLOW = 1960. <-80> <2> / SSID1 = MIXED CID = NH3 FLOW = 217. <-80> <2> / SSID1 = MIXED CID = CH4 FLOW = 14427. <-80> <2> / SSID1 = MIXED CID = C10H8 FLOW = 8. <-80> <2> \ ? STREAM MATERIAL "A300.A300S.394" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 394.9828 <22> <2> PRES = 50. <20> <13> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? BLOCK MIXER "A300.A300S.MIXQH304" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK FSPLIT "A300.A300S.SP-384" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM SID = 384VENT / SID = 384REC FLOW-BASIS = MASS BASIS-FLOW = 1E-005 <-80> <2> \ \ STREAM-ORDER ORDER-STREAM = 384VENT ORDER = 2 / ORDER-STREAM = 384REC ORDER = 1 \ ? BLOCK SEP "A300.A300S.M-304" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "LO-CAT Liquid Filled Absorber" \ \ PARAM1 PRES1 = -5. <20> <2> FLAG = 1 \ \ PARAM PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = H2O FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = H2S FRACS = 1. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 321 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 321 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = 321 SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 357 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 357 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 357 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 357 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 357 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 357 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 357 SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = 321 TEMP = 120. <22> <2> \ ? BLOCK SEP "A300.A300S.R-304A" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 1 \ \ PARAM PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = H2O FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 324 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 324 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = 324 SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 325 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 325 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 325 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 325 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 325 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 325 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 325 SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = 324 TEMP = 110. <22> <2> PRES = 1. <20> <3> \ \ FLASH-SPECS FLASH-STREAM = 325 TEMP = 110. <22> <2> PRES = 1. <20> <3> \ ? BLOCK HEATER "A300.A300S.H-304" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "LO-CAT Preheater" \ \ PARAM PRES = -5. <20> <2> DELT = 10. <31> <2> \ \ COMMENTS COMMENTS = ( ";Superheat the feed stream to the LO-CAT to 10F above " ";dew point. This degree of superheating required for " ";LO-CAT system. " ) \ ? BLOCK HEATER "A300.A300S.H-304+" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 230. <22> <2> PRES = -5. <20> <2> \ ? BLOCK RSTOIC "A300.A300S.R-304" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "LO-CAT Oxidizer Vessel" \ \ PARAM TEMP = 110. <22> <2> PRES = 0. <20> <2> \ \ STOIC REACNO = 1 STOIC-CID = H2S STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -0.5 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = SULFUR STOIC-SSID1 = CISOLID COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = H2S CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = SULFUR \ ? REPORT "A300.A300S.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A300.A300TR" ? ; BLOCK ; ? "A300.A300TR.SOLVE" ? ? FLOWSHEET "A300.A300TR.GLOBAL" ? \ BLOCK BLKID = A300DWPT BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-19" IN = ( 334 M3-0 ) OUT = ( "A300DWPT.234" M3-0 ) \ \ CONNECT BLKID = "$C-18" IN = ( "A300DWPT.235" M4-0 ) OUT = ( 335 M3-0 ) \ \ BLOCK BLKID = A300FC BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-63" IN = ( 329B M3-0 ) OUT = ( "A300FC.329" M3-0 ) \ \ CONNECT BLKID = "$C-64" IN = ( 340 M4-0 ) OUT = ( "A300FC.340" M4-0 ) \ \ CONNECT BLKID = "$C-14" IN = ( 225F M5-0 ) OUT = ( "A300FC.225F" M5-0 ) \ \ CONNECT BLKID = "$C-2" IN = ( QR303 Q6-0 ) OUT = ( "A300FC.QR303" Q6-0 ) \ \ CONNECT BLKID = "$C-1" IN = ( 385F M7-0 ) OUT = ( "A300FC.385F" M7-0 ) \ \ CONNECT BLKID = "$C-4" IN = ( "A300FC.334" M8-0 ) OUT = ( 334 M3-0 ) \ \ BLOCK BLKID = "R-303A" BLKTYPE = REQUIL MDLTYPE = "REquil" IN = ( 325A M0-1 ) OUT = ( 327 M0-1 328 M1-2 QR303A Q2-3 ) \ \ BLOCK BLKID = "R-303B" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 328 M0-1 ) OUT = ( QR303B Q1-4 329 M0-1 330A M0-1 ) \ \ BLOCK BLKID = MX300G BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 327 M0-1 330A M0-1 ) OUT = ( 330 M0-1 ) \ \ BLOCK BLKID = MX300F BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QR303A Q1-4 QR303B Q1-4 ) OUT = ( QR303 Q1-3 ) \ \ BLOCK BLKID = MX303A BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 326 M0-1 225A M0-1 386 M0-1 ) OUT = ( 325A M0-1 ) \ \ BLOCK BLKID = SP382 BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 426F M0-1 ) OUT = ( 385F M0-1 385T M0-1 ) \ \ BLOCK BLKID = MX300H BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 370 M0-1 371 M0-1 372 M0-1 373 M0-1 ) OUT = ( 386 M0-1 ) \ \ BLOCK BLKID = H315A BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 513 M0-1 ) OUT = ( 373 M0-1 QH315A Q2-3 ) \ \ BLOCK BLKID = H315B BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 384REC M0-1 ) OUT = ( 372 M0-1 QH315B Q2-3 ) \ \ BLOCK BLKID = H315C BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 393 M0-1 ) OUT = ( 371 M0-1 QH315C Q2-3 ) \ \ BLOCK BLKID = H315D BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 385T M0-1 ) OUT = ( 370 M0-1 QH315D Q2-3 ) \ \ BLOCK BLKID = MX300I BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QH315D Q1-4 QH315C Q1-4 QH315B Q1-4 QH315A Q1-4 ) OUT = ( QH315 Q1-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A300.A300TR.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A300.A300TR.STREAM-NAMES" ? ? STREAM MATERIAL "A300.A300TR.326" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = CISOLID TEMP = 60. <22> <2> PRES = 22. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = CISOLID CID = OLIVINE FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A300.A300TR.329B" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 1. <20> <3> BASIS = "MOLE-FRAC" FLOWBASE = MASS TOTFLOW = 5. <-80> <2> TOTAL = 1. <-4> <0> JUNK = 5 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.75666 <-4> <0> / SSID1 = MIXED CID = O2 FLOW = 0.202967 <-4> <0> / SSID1 = MIXED CID = AR FLOW = 0.00905 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.00032 <-4> <0> / SSID1 = MIXED CID = H2O FLOW = 0.031003 <-4> <0> \ ? STREAM MATERIAL "A300.A300TR.340" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MOLE-FRAC" FLOWBASE = MASS TOTFLOW = 0.1 <-80> <2> TOTAL = 1. <-4> <0> JUNK = 9 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.011 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.005 <-4> <0> / SSID1 = MIXED CID = H2S FLOW = 4E-006 <-4> <0> / SSID1 = MIXED CID = CH4 FLOW = 0.943996 <-4> <0> / SSID1 = MIXED CID = C2H6 FLOW = 0.031 <-4> <0> / SSID1 = MIXED CID = C3H8 FLOW = 0.005 <-4> <0> / SSID1 = MIXED CID = "I-C4H10" FLOW = 0.001 <-4> <0> / SSID1 = MIXED CID = "N-C4H10" FLOW = 0.001 <-4> <0> / SSID1 = MIXED CID = "PENTANE+" FLOW = 0.002 <-4> <0> \ ? STREAM MATERIAL "A300.A300TR.384REC" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 30. <22> <2> PRES = 27. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 50000. <-80> <2> TOTAL = 1.00000111 <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = CO2 FLOW = 0.999993363 <-3> <0> / SSID1 = MIXED CID = H2S FLOW = 7.747E-006 <-3> <0> \ ? STREAM MATERIAL "A300.A300TR.393" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 394.9828 <22> <2> PRES = 50. <20> <13> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? BLOCK MIXER "A300.A300TR.MX300F" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK MIXER "A300.A300TR.MX300G" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A300.A300TR.MX300H" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A300.A300TR.MX300I" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK MIXER "A300.A300TR.MX303A" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK FSPLIT "A300.A300TR.SP382" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM SID = 385F / SID = 385T FRAC = 0.95 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = 385F / ORDER-STREAM = 385T \ ? BLOCK SEP "A300.A300TR.R-303B" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 1 \ \ PARAM PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = OLIVINE FLOWS = 0. <-80> <2> FLOWBASIS = MASS / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 329 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 329 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = 329 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = 329 SUBSTREAM = CISOLID COMPS = OLIVINE FLOWS = 1E-006 <-80> <2> FLOWBASIS = MASS / PARAM-STREAM = 329 SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = 329 SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = 329 SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 330A SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 330A SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 330A SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 330A SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 330A SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 330A SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 330A SUBSTREAM = NC COMPS = CHAR \ ? BLOCK HEATER "A300.A300TR.H315A" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 570. <22> <2> PRES = -0.5 <20> <2> \ ? BLOCK HEATER "A300.A300TR.H315B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 570. <22> <2> PRES = -0.5 <20> <2> \ ? BLOCK HEATER "A300.A300TR.H315C" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 570. <22> <2> PRES = -0.5 <20> <2> \ ? BLOCK HEATER "A300.A300TR.H315D" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 570. <22> <2> PRES = -0.5 <20> <2> \ ? BLOCK REQUIL "A300.A300TR.R-303A" ? ; "ENG_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "Tar cracker" \ \ PARAM NREAC = 13 PRES = -3. <20> <2> DUTY = 0. <13> <2> \ \ STOIC REACNO = 1 STOIC-CID = CO COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = H2O COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CH4 COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = H2O COEF = -1. <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = C2H6 COEF = -1. <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = H2O COEF = -2. <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = C2H4 COEF = -1. <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = H2O COEF = -2. <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = C2H2 COEF = -1. <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = H2O COEF = -2. <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = C6H6 COEF = -1. <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = H2O COEF = -6. <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = C10H8 COEF = -1. <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = H2O COEF = -10. <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = NH3 COEF = -1. <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = METHANOL COEF = -1. <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = ETHANOL COEF = -1. <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = H2O COEF = -1. <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = PROPANOL COEF = -1. <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = H2O COEF = -2. <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = NBUTANOL COEF = -1. <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = H2O COEF = -3. <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = PENTANOL COEF = -1. <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = H2O COEF = -4. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2 COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2 COEF1 = 3. <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = CO COEF1 = 2. <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = H2 COEF1 = 5. <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = CO COEF1 = 2. <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = H2 COEF1 = 4. <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = CO COEF1 = 2. <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = H2 COEF1 = 3. <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = CO COEF1 = 6. <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = H2 COEF1 = 9. <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = CO COEF1 = 10. <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = H2 COEF1 = 14. <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = N2 COEF1 = 0.5 <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = H2 COEF1 = 1.5 <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = CO COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = H2 COEF1 = 2. <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = CO COEF1 = 2. <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = H2 COEF1 = 4. <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = H2 COEF1 = 6. <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = CO COEF1 = 3. <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = H2 COEF1 = 8. <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = CO COEF1 = 4. <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = H2 COEF1 = 10. <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = CO COEF1 = 5. <0> <0> \ \ EXTENT-SPEC EXT-SPREACNO = 1 / EXT-SPREACNO = 2 EXT-SPEC = 0. <11> <2> OPT-EXT-DELT = EXTENT / EXT-SPREACNO = 3 EXT-SPEC = 0. <11> <2> OPT-EXT-DELT = EXTENT / EXT-SPREACNO = 4 EXT-SPEC = 0. <11> <2> OPT-EXT-DELT = EXTENT / EXT-SPREACNO = 5 EXT-SPEC = 0. <11> <2> OPT-EXT-DELT = EXTENT / EXT-SPREACNO = 6 EXT-SPEC = 0. <11> <2> OPT-EXT-DELT = EXTENT / EXT-SPREACNO = 7 EXT-SPEC = 0. <11> <2> OPT-EXT-DELT = EXTENT / EXT-SPREACNO = 8 EXT-SPEC = 0. <11> <2> OPT-EXT-DELT = EXTENT / EXT-SPREACNO = 9 OPT-EXT-DELT = DELT / EXT-SPREACNO = 10 / EXT-SPREACNO = 11 / EXT-SPREACNO = 12 / EXT-SPREACNO = 13 \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK HIERARCHY "A300.A300TR.A300DWPT" ? ; BLOCK ; ? "A300.A300TR.A300DWPT.SOLVE" ? ? FLOWSHEET "A300.A300TR.A300DWPT.GLOBAL" ? \ BLOCK BLKID = "H-234DP" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 235B M0-1 ) OUT = ( 235DP M0-1 ) \ \ BLOCK BLKID = DPL234 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( 234 M0-1 ) OUT = ( 235 M0-1 235B M0-1 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A300.A300TR.A300DWPT.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? BLOCK HEATER "A300.A300TR.A300DWPT.H-234DP" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = 1. <20> <3> VFRAC = 1. <0> <0> \ ? BLOCK DUPL "A300.A300TR.A300DWPT.DPL234" ? ; "ENG_MOLE" ; ; BLOCK ; ? REPORT "A300.A300TR.A300DWPT.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A300.A300TR.A300FC" ? ; BLOCK ; ? "A300.A300TR.A300FC.SOLVE" ? ? FLOWSHEET "A300.A300TR.A300FC.GLOBAL" ? \ BLOCK BLKID = "HV-327" BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-2" IN = ( 340 M3-0 ) OUT = ( "HV-327.100-IN" M3-0 ) \ \ CONNECT BLKID = "$C-1" IN = ( "HV-327.100-OUT" M4-0 ) OUT = ( 340B M3-0 ) \ \ BLOCK BLKID = "K-305" BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 329 M0-1 ) OUT = ( WK305 W2-3 330A M0-1 ) \ \ BLOCK BLKID = "H-311" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 332 M0-1 ) OUT = ( QH311 Q2-3 334 M0-1 ) \ \ BLOCK BLKID = MX300 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 385F M0-1 225F M0-1 340C M0-1 ) OUT = ( 328 M0-1 ) \ \ BLOCK BLKID = "R-301A" BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 330B M0-1 328 M0-1 ) OUT = ( QR301A Q2-3 331 M0-1 ) \ \ BLOCK BLKID = "K-303" BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 340B M0-1 ) OUT = ( WK303 W2-3 340C M0-1 ) \ \ BLOCK BLKID = "R-301B" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 331 M0-1 QR303 Q1-2 ) OUT = ( 332 M0-1 ) \ \ BLOCK BLKID = "H-330" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 330A M0-1 ) OUT = ( 330B M0-1 QH330 Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A300.A300TR.A300FC.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A300.A300TR.A300FC.STREAM-NAMES" ? ? STREAM MATERIAL "A300.A300TR.A300FC.329" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 1. <20> <3> BASIS = "MOLE-FRAC" FLOWBASE = MASS TOTFLOW = 5. <-80> <2> TOTAL = 1. <-4> <0> JUNK = 5 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.75666 <-4> <0> / SSID1 = MIXED CID = O2 FLOW = 0.202967 <-4> <0> / SSID1 = MIXED CID = AR FLOW = 0.00905 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.00032 <-4> <0> / SSID1 = MIXED CID = H2O FLOW = 0.031003 <-4> <0> \ ? BLOCK MIXER "A300.A300TR.A300FC.MX300" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK HEATER "A300.A300TR.A300FC.H-311" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Reformer Flue Gas Cooler/Steam Superheater" \ \ PARAM TEMP = 1879. <22> <2> PRES = -1. <20> <2> \ \ COMMENTS COMMENTS = ( ";The heat from this heat exchanger is used to " ";superheat the steam for the steam system. " ) \ ? BLOCK HEATER "A300.A300TR.A300FC.H-330" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 400. <22> <2> PRES = -0.1 <20> <2> \ ? BLOCK HEATER "A300.A300TR.A300FC.R-301B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = 0. <20> <2> \ \ COMMENTS COMMENTS = ( ";This heat exchanger is used to ""transfer"" the " ";required heat from the reformer combustor to the " ";reformer. In the real plant, this heat exchanger " ";would not actually exist, as the combustor and " ";reformer are integrated." ) \ ? BLOCK RSTOIC "A300.A300TR.A300FC.R-301A" ? ; "ENG_MOLE" ; ; ICON3 ; \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> COMBUSTION = YES PROD-NOX = NO2 \ \ COMMENTS COMMENTS = ( ";This block models the reformer combustor. In an " ";actual reformer, these reformer and combustor are " ";integrated into one unit." ) \ ? BLOCK HIERARCHY "A300.A300TR.A300FC.HV-327" ? ; BLOCK ; ? "A300.A300TR.A300FC.HV-327.SOLVE" ? ? FLOWSHEET "A300.A300TR.A300FC.HV-327.GLOBAL" ? \ BLOCK BLKID = DPL100 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( "100-IN" M0-1 ) OUT = ( "100-OUT" M0-1 RAW M0-1 ) \ \ BLOCK BLKID = REJECT BLKTYPE = SEP MDLTYPE = "Sep" IN = ( RAW M0-1 ) OUT = ( BASIS M0-1 REJECT M0-1 QREJECT Q1-4 ) \ \ BLOCK BLKID = BURN BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( BASIS M0-1 O2 M0-1 ) OUT = ( QCOMB Q2-3 "PROD-1" M0-1 ) \ \ BLOCK BLKID = COMBSEP BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( "PROD-2" M0-1 ) OUT = ( COMBVAP M0-1 COMBLIQ M1-2 ) \ \ BLOCK BLKID = VAPWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( COMBLIQ M0-1 ) OUT = ( DPT M0-1 "QVAP-1" Q2-3 ) \ \ BLOCK BLKID = CONDWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( "WATER-V" M0-1 ) OUT = ( "WATER-L" M0-1 "QVAP-2" Q2-3 ) \ \ BLOCK BLKID = DRYER BLKTYPE = SEP MDLTYPE = "Sep" IN = ( DPT M0-1 COMBVAP M0-1 ) OUT = ( "WATER-V" M0-1 RESIDUE M0-1 ) \ \ BLOCK BLKID = NET BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-1" Q1-4 QCOMB Q1-4 QSHIFT Q1-4 ) OUT = ( QNET Q1-3 ) \ \ BLOCK BLKID = GROSS BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-2" Q1-4 QNET Q1-4 ) OUT = ( QGROSS Q1-3 ) \ \ BLOCK BLKID = SHIFT BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( "PROD-1" M0-1 ) OUT = ( "PROD-2" M0-1 QSHIFT Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A300.A300TR.A300FC.HV-327.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A300.A300TR.A300FC.HV-327.STREAM-NAMES" ? \ NAMES STREAM = "100-IN" TEXT = "Feed material" \ ? STREAM MATERIAL "A300.A300TR.A300FC.HV-327.100-IN" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 1.E-006 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TEMP = 60. <22> <2> PRES = 1. <20> <3> TOTAL = 3.E-006 <-80> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = WOOD FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = ASH FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = CHAR FLOW = 1E-006 <-80> <2> \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = ULTANAL ELEM = ( 0.92 <0> <0> 50.88 <0> <0> 6.04 <0> <0> 0.17 <0> <0> 0. <0> <0> 0.09 <0> <0> 41.9 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.045 <0> <0> 0.045 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 15.29 <0> <0> 83.84 <0> <0> 0.87 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = GENANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> 100. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = ULTANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = ULTANAL ELEM = ( 3.168 <0> <0> 65.894 <0> <0> 3.064 <0> <0> 0.281 <0> <0> 0. <0> <0> 0.149 <0> <0> 27.444 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.0745 <0> <0> 0.0745 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 87.18 <0> <0> 12.81 <0> <0> 0.01 <0> <0> ) \ \ COMMENTS COMMENTS = ( ";Poplar composition per Craig, K.R., Mann, M.K., " ";""Cost and Performance Analysis of Biomass-Bases " ";Integrated Gasification Combined-Cycle (BIGCC) Power " ";Systems"", National Renewable Energy Laboratory, " ";NREL/TP-430-21657, October, 1996." ";Modified sulfur analysis as follows: Evenly " ";distributed sulfur between sulfate and organic, with " ";no sulfur being classified as pyritic" ) \ ? STREAM MATERIAL "A300.A300TR.A300FC.HV-327.O2" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 77. <22> <2> PRES = 1. <20> <3> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = O2 FLOW = 1. <-89> <2> \ ? BLOCK MIXER "A300.A300TR.A300FC.HV-327.GROSS" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A300.A300TR.A300FC.HV-327.NET" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK SEP "A300.A300TR.A300FC.HV-327.DRYER" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = METHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = "WATER-V" TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK SEP "A300.A300TR.A300FC.HV-327.REJECT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = N2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = O2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2O FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2S FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NH3 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CH4 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H4 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C3H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C6H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C10H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = METHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = WOOD FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = CHAR FRACS = 1. <0> <0> / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = BASIS TEMP = 77. <22> <2> PRES = 1. <20> <3> \ \ FLASH-SPECS FLASH-STREAM = REJECT KODE = NOFLASH \ ? BLOCK HEATER "A300.A300TR.A300FC.HV-327.CONDWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A300.A300TR.A300FC.HV-327.VAPWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK FLASH2 "A300.A300TR.A300FC.HV-327.COMBSEP" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK RSTOIC "A300.A300TR.A300FC.HV-327.BURN" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 0. <20> <2> COMBUSTION = YES PROD-NOX = NO2 \ \ STOIC REACNO = 1 STOIC-CID = WOOD STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CHAR STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = NC KEY-CID = WOOD CONV = 1. <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = NC KEY-CID = CHAR CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = NO2 \ ? BLOCK RSTOIC "A300.A300TR.A300FC.HV-327.SHIFT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 1. <20> <3> \ \ STOIC REACNO = 1 STOIC-CID = NO2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = 0.5 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = NO2 CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = O2 \ ? BLOCK DUPL "A300.A300TR.A300FC.HV-327.DPL100" ? ; "ENG_MOLE" ; ; BLOCK ; ? REPORT "A300.A300TR.A300FC.HV-327.BLOCK-REPORT" ? ? BLOCK COMPR "A300.A300TR.A300FC.K-303" ? ; "ENG_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "Reformer Flue Gas Blower" \ \ PARAM TYPE = "GPSA-POLYTROP" OPT-SPEC = PRES PRES = 1.2 <20> <3> \ ? BLOCK COMPR "A300.A300TR.A300FC.K-305" ? ; "ENG_MOLE" ; ; ICON2 ; \ DESCRIPTION DESCRIPTION = "Reformer Combustion Air Blower" \ \ PARAM TYPE = "GPSA-POLYTROP" OPT-SPEC = PRES PRES = 1.2 <20> <3> \ \ COMMENTS COMMENTS = ( ";Air blower for combusting PSA off gas" ) \ ? REPORT "A300.A300TR.A300FC.BLOCK-REPORT" ? ? REPORT "A300.A300TR.BLOCK-REPORT" ? ? REPORT "A300.BLOCK-REPORT" ? ? BLOCK HIERARCHY A400 ? ; BLOCK ; ? "A400.SOLVE" ? ? FLOWSHEET "A400.ALCOHL" ? \ BLOCK BLKID = "H-414" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 473 M0-1 ) OUT = ( 473A M0-1 QCH414 Q2-3 ) \ \ BLOCK BLKID = "S-501" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 473A M0-1 ) OUT = ( 474 M0-1 475 M1-2 ) \ \ BLOCK BLKID = PROP400A BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 471 M0-1 ) OUT = ( 471A M0-1 QPRP400A Q2-3 ) \ \ BLOCK BLKID = "H-412" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 471A M0-1 ) OUT = ( QH412 Q2-3 471B M0-1 ) \ \ BLOCK BLKID = "H-411" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 471B M0-1 ) OUT = ( 472 M0-1 QH411 Q2-3 ) \ \ BLOCK BLKID = "H-413" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 472 M0-1 ) OUT = ( 473 M0-1 QAH413 Q2-3 ) \ ? FLOWSHEET "A400.GLOBAL" ? \ BLOCK BLKID = A400CMPR BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-3" IN = ( 362 M3-0 ) OUT = ( "A400CMPR.362" M3-0 ) \ \ CONNECT BLKID = "$C-2" IN = ( "A400CMPR.463" M4-0 ) OUT = ( 463 M3-0 ) \ \ CONNECT BLKID = "$C-1" IN = ( "A400CMPR.466" M5-0 ) OUT = ( 466 M4-0 ) \ \ CONNECT BLKID = "$C-6" IN = ( "A400CMPR.QAK410" Q6-0 ) OUT = ( QAK410 Q5-0 ) \ \ CONNECT BLKID = "$C-7" IN = ( "A400CMPR.WK410" W7-0 ) OUT = ( WK410 W6-0 ) \ \ BLOCK BLKID = A400SGR BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-4" IN = ( 470 M3-0 ) OUT = ( "A400SGR.470" M3-0 ) \ \ CONNECT BLKID = "$C-8" IN = ( "A400SGR.471" M4-0 ) OUT = ( 471 M3-0 ) \ \ BLOCK BLKID = "HV-475" BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-9" IN = ( 475 M3-0 ) OUT = ( "HV-475.100-IN" M3-0 ) \ \ CONNECT BLKID = "$C-5" IN = ( "HV-475.100-OUT" M4-0 ) OUT = ( 503 M3-0 ) \ \ BLOCK BLKID = PROP400B BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 474 M0-1 ) OUT = ( 482 M0-1 QPRP400B Q2-3 ) \ \ BLOCK BLKID = SP401 BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 482 M0-1 ) OUT = ( 477 M0-1 478 M0-1 ) \ \ BLOCK BLKID = "K-414" BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 478 M0-1 ) OUT = ( 483 M0-1 WK414 W2-3 ) \ \ BLOCK BLKID = "K-412" BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 498 M0-1 ) OUT = ( WK412 W2-3 426 M0-1 ) \ \ BLOCK BLKID = "H-416A" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 477 M0-1 ) OUT = ( QH416A Q2-3 477A M0-1 ) \ \ BLOCK BLKID = "M-403" BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 466 M0-1 483 M0-1 515 M0-1 ) OUT = ( 470 M0-1 ) \ \ BLOCK BLKID = "H-416B" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 477A M0-1 ) OUT = ( QH416B Q2-3 498 M0-1 ) \ \ BLOCK BLKID = MX416 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QH416B Q1-4 QH416A Q1-4 ) OUT = ( QH416 Q1-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A400.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ \ PROPERTIES SECID-LIST = ALCOHL BASEOPSET = NRTL OPSETNAME = NRTL H-COMPS = "HC-1" \ ? "A400.STREAM-NAMES" ? ? STREAM MATERIAL "A400.463" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 142.3 <22> <2> PRES = 450. <20> <2> BASIS = "MASS-FLOW" TOTAL = 1.E-003 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 0.001 <-80> <2> \ ? STREAM MATERIAL "A400.515" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 110. <22> <2> PRES = 1000. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 24000. <-80> <2> TOTAL = 1. <-3> <0> JUNK = 2 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 0.2 <-3> <0> / SSID1 = MIXED CID = METHANOL FLOW = 0.8 <-3> <0> \ ? BLOCK MIXER "A400.M-403" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A400.MX416" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK FSPLIT "A400.SP401" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM SID = 477 / SID = 478 FRAC = 0.001 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = 477 / ORDER-STREAM = 478 \ ? BLOCK HEATER "A400.H-411" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 200. <22> <2> PRES = -2. <20> <2> \ ? BLOCK HEATER "A400.H-412" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = -5. <20> <2> VFRAC = 1. <0> <0> \ ? BLOCK HEATER "A400.H-413" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 140. <22> <2> PRES = -2. <20> <2> \ ? BLOCK HEATER "A400.H-414" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 110. <22> <2> PRES = -5. <20> <2> MAXIT = 100 \ ? BLOCK HEATER "A400.H-416A" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 775. <22> <2> PRES = -5. <20> <2> \ ? BLOCK HEATER "A400.H-416B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 1500. <22> <2> PRES = 0. <20> <2> \ ? BLOCK HEATER "A400.PROP400A" ? ; "ENG_MOLE" ; ; BLOCK ; \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ ? BLOCK HEATER "A400.PROP400B" ? ; "ENG_MOLE" ; ; BLOCK ; \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ ? BLOCK FLASH2 "A400.S-501" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = -2. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK HIERARCHY "A400.A400CMPR" ? ; BLOCK ; ? "A400.A400CMPR.SOLVE" ? ? FLOWSHEET "A400.A400CMPR.GLOBAL" ? \ BLOCK BLKID = "K-410" BLKTYPE = MCOMPR MDLTYPE = "MCompr" IN = ( 362 M0-1 ) OUT = ( QAK410B Q4-5 463 M1-2 QAK410A Q4-5 WK410B W3-4 QAK410C Q4-5 WK410A W3-4 WK410C W3-4 466 M0-1 ) \ \ BLOCK BLKID = MX400F BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QAK410C Q1-4 QAK410B Q1-4 QAK410A Q1-4 ) OUT = ( QAK410 Q1-3 ) \ \ BLOCK BLKID = MX400E BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WK410B W2-7 WK410C W2-7 WK410A W2-7 ) OUT = ( WK410 W2-4 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A400.A400CMPR.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A400.A400CMPR.STREAM-NAMES" ? ? STREAM MATERIAL "A400.A400CMPR.463" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 142.3 <22> <2> PRES = 450. <20> <2> BASIS = "MASS-FLOW" TOTAL = 1.E-003 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 0.001 <-80> <2> \ ? BLOCK MIXER "A400.A400CMPR.MX400E" ? ; "ENG_MOLE" ; ; WORK ; ? BLOCK MIXER "A400.A400CMPR.MX400F" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK MCOMPR "A400.A400CMPR.K-410" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM NSTAGE = 3 TYPE = "ASME-POLYTROPIC" PRES = 1000. <20> <2> COMPR-NPHASE = 2 OPT-SPEC = PRES \ \ FEEDS FEED-SID = 362 FEED-STAGE = 1 \ \ PRODUCTS PROD-STREAM = 463 GLOBAL = Y PROD-PHASE = L / PROD-STREAM = 466 PROD-STAGE = 3 \ \ Q-PRODUCTS Q-PROD-STRM = QAK410B Q-PROD-STAGE = 1 / Q-PROD-STRM = QAK410A Q-PROD-STAGE = 2 / Q-PROD-STRM = QAK410C Q-PROD-STAGE = 3 \ \ W-PRODUCTS W-PROD-STRM = WK410B W-PROD-STAGE = 2 / W-PROD-STRM = WK410A W-PROD-STAGE = 3 / W-PROD-STRM = WK410C W-PROD-STAGE = 1 \ \ COMPR-SPECS C-S-STAGE = 1 PEFF = 0.78 <0> <0> / C-S-STAGE = 2 PEFF = 0.78 <0> <0> / C-S-STAGE = 3 PEFF = 0.78 <0> <0> \ \ COOLER-SPECS CL-STAGE = 1 CL-TEMP = 140. <22> <2> PDROP = 2. <75> <2> OPT-CLSPEC = TEMP / CL-STAGE = 2 CL-TEMP = 140. <22> <2> PDROP = 2. <75> <2> OPT-CLSPEC = TEMP / CL-STAGE = 3 DUTY = 0. <13> <2> OPT-CLSPEC = DUTY \ \ PROPERTIES OPSETNAME = SYSOP3 FRWATEROPSET = "STEAM-TA" \ ? REPORT "A400.A400CMPR.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A400.A400SGR" ? ; BLOCK ; ? "A400.A400SGR.SOLVE" ? ? FLOWSHEET "A400.A400SGR.GLOBAL" ? \ BLOCK BLKID = QR410MX BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QR410-1" Q1-4 QH410WGS Q1-4 ) OUT = ( QR410 Q1-3 ) \ \ BLOCK BLKID = DUP410 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( 485 M0-1 ) OUT = ( "485-0" M0-1 499A M0-1 ) \ \ BLOCK BLKID = "H-410A" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 470 M0-1 ) OUT = ( QH410A Q2-3 470A M0-1 ) \ \ BLOCK BLKID = "R-410-WG" BLKTYPE = REQUIL MDLTYPE = "REquil" IN = ( 499B M0-1 ) OUT = ( 471 M0-1 469L M1-2 QH410WGS Q2-3 ) \ \ BLOCK BLKID = R410 BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 499A M0-1 ) OUT = ( 499B M0-1 "QR410-1" Q2-3 ) \ \ BLOCK BLKID = "H-410B" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 470A M0-1 ) OUT = ( QH410B Q2-3 485 M0-1 ) \ \ BLOCK BLKID = MX410 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QH410B Q1-4 QH410A Q1-4 ) OUT = ( QH410 Q1-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A400.A400SGR.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A400.A400SGR.STREAM-NAMES" ? ? STREAM MATERIAL "A400.A400SGR.485" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 565.5 <22> <2> PRES = 983. <20> <2> BASIS = "MASS-FLOW" TOTAL = 753408.7245 <-80> <0> JUNK = 37 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2 FLOW = 22114.6548 <-80> <2> / SSID1 = MIXED CID = CO FLOW = 256031.583 <-80> <2> / SSID1 = MIXED CID = N2 FLOW = 13139.8612 <-80> <2> / SSID1 = MIXED CID = O2 FLOW = 0. <-80> <2> / SSID1 = MIXED CID = AR FLOW = 0. <-80> <2> / SSID1 = MIXED CID = CO2 FLOW = 2638.72727 <-80> <2> / SSID1 = MIXED CID = H2O FLOW = 504.058151 <-80> <2> / SSID1 = MIXED CID = H2S FLOW = 78.9290532 <-80> <2> / SSID1 = MIXED CID = SO2 FLOW = 0. <-80> <2> / SSID1 = MIXED CID = NH3 FLOW = 1691.52092 <-80> <2> / SSID1 = MIXED CID = NO2 FLOW = 0. <-80> <2> / SSID1 = MIXED CID = CH4 FLOW = 352726.253 <-80> <2> / SSID1 = MIXED CID = C2H6 FLOW = 43223.0686 <-80> <2> / SSID1 = MIXED CID = C2H4 FLOW = 39750.9809 <-80> <2> / SSID1 = MIXED CID = C2H2 FLOW = 3462.97721 <-80> <2> / SSID1 = MIXED CID = C3H8 FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "I-C4H10" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "N-C4H10" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "PENTANE+" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = C6H6 FLOW = 8.98200818 <-80> <2> / SSID1 = MIXED CID = C10H8 FLOW = 0.10530249 <-80> <2> / SSID1 = MIXED CID = CARBON FLOW = 0. <-80> <2> / SSID1 = MIXED CID = SULFUR FLOW = 0. <-80> <2> / SSID1 = MIXED CID = OLIVINE FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "NH4+" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "H3O+" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "NH2COO-" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "OH-" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "HCO3-" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "HS-" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "CO3--" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = "S--" FLOW = 0. <-80> <2> / SSID1 = MIXED CID = METHANOL FLOW = 12520.0947 <-80> <2> / SSID1 = MIXED CID = ETHANOL FLOW = 5336.86808 <-80> <2> / SSID1 = MIXED CID = PROPANOL FLOW = 153.42902 <-80> <2> / SSID1 = MIXED CID = NBUTANOL FLOW = 22.5609453 <-80> <2> / SSID1 = MIXED CID = PENTANOL FLOW = 4.07035365 <-80> <2> \ ? BLOCK MIXER "A400.A400SGR.MX410" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK MIXER "A400.A400SGR.QR410MX" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK HEATER "A400.A400SGR.H-410A" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 570. <22> <2> PRES = -2. <20> <2> \ ? BLOCK HEATER "A400.A400SGR.H-410B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 570. <22> <2> PRES = 0. <20> <2> \ ? BLOCK RSTOIC "A400.A400SGR.R410" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 570. <22> <2> PRES = -5. <20> <2> SERIES = YES HEAT-OF-REAC = CALCULATE \ \ STOIC REACNO = 1 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -2. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = PROPANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -2. <0> <0> \ \ STOIC REACNO = 3 STOIC-CID = ETHANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -2. <0> <0> \ \ STOIC REACNO = 4 STOIC-CID = METHANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 5 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 6 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -2. <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -2. <0> <0> \ \ STOIC REACNO = 7 STOIC-CID = METHANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = METHANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 8 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 9 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -2. <0> <0> \ \ STOIC REACNO = 10 STOIC-CID = ETHANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = ETHANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 11 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -2. <0> <0> \ \ STOIC REACNO = 12 STOIC-CID = PROPANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = PROPANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 13 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 14 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 14 STOIC-CID = H2O STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = CO STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -2. <0> <0> \ \ STOIC REACNO = 15 STOIC-CID = NBUTANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 16 STOIC-CID = NBUTANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 16 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = PENTANOL STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 17 STOIC-CID = H2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = NBUTANOL STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = PROPANOL STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 3 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 4 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = H2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 5 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 6 STOIC-CID1 = METHANOL STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = ETHANOL STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 7 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = CH4 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 8 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = H2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 9 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = PROPANOL STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 10 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = C2H6 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 11 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = NBUTANOL STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 12 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = C3H8 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 13 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 14 STOIC-CID1 = H2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 14 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 15 STOIC-CID1 = PENTANOL STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 15 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = "N-C4H10" STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 16 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = "PENTANE+" STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 17 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = H2O CONV = 0.98 <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = MIXED KEY-CID = PROPANOL CONV = 0.98 <0> <0> \ \ CONVEX EXT-REACNO = 3 KEY-SSID = MIXED KEY-CID = ETHANOL CONV = 0.98 <0> <0> \ \ CONVEX EXT-REACNO = 4 KEY-SSID = MIXED KEY-CID = METHANOL CONV = 0.999 <0> <0> \ \ CONVEX EXT-REACNO = 5 KEY-SSID = MIXED KEY-CID = H2O CONV = 0.98 <0> <0> \ \ CONVEX EXT-REACNO = 6 KEY-SSID = MIXED KEY-CID = CO CONV = 0.205 <0> <0> \ \ CONVEX EXT-REACNO = 7 KEY-SSID = MIXED KEY-CID = METHANOL CONV = 0.75 <0> <0> \ \ CONVEX EXT-REACNO = 8 KEY-SSID = MIXED KEY-CID = METHANOL CONV = 0.7 <0> <0> \ \ CONVEX EXT-REACNO = 9 KEY-SSID = MIXED KEY-CID = H2O CONV = 0.98 <0> <0> \ \ CONVEX EXT-REACNO = 10 KEY-SSID = MIXED KEY-CID = ETHANOL CONV = 0.1 <0> <0> \ \ CONVEX EXT-REACNO = 11 KEY-SSID = MIXED KEY-CID = ETHANOL CONV = 0.01 <0> <0> \ \ CONVEX EXT-REACNO = 12 KEY-SSID = MIXED KEY-CID = PROPANOL CONV = 0.1 <0> <0> \ \ CONVEX EXT-REACNO = 13 KEY-SSID = MIXED KEY-CID = PROPANOL CONV = 0.01 <0> <0> \ \ CONVEX EXT-REACNO = 14 KEY-SSID = MIXED KEY-CID = H2O CONV = 0.9 <0> <0> \ \ CONVEX EXT-REACNO = 15 KEY-SSID = MIXED KEY-CID = NBUTANOL CONV = 0.1 <0> <0> \ \ CONVEX EXT-REACNO = 16 KEY-SSID = MIXED KEY-CID = NBUTANOL CONV = 0.01 <0> <0> \ \ CONVEX EXT-REACNO = 17 KEY-SSID = MIXED KEY-CID = PENTANOL CONV = 0.01 <0> <0> \ \ HEAT-RXN H-REACNO = 1 HREF-CID = CO / H-REACNO = 2 HREF-CID = CO / H-REACNO = 3 HREF-CID = CO / H-REACNO = 4 HREF-CID = CO / H-REACNO = 5 HREF-CID = CO / H-REACNO = 6 HREF-CID = CO / H-REACNO = 7 HREF-CID = CO / H-REACNO = 8 HREF-CID = METHANOL / H-REACNO = 9 HREF-CID = CO / H-REACNO = 10 HREF-CID = CO / H-REACNO = 11 HREF-CID = ETHANOL / H-REACNO = 12 HREF-CID = CO / H-REACNO = 13 HREF-CID = PROPANOL / H-REACNO = 14 HREF-CID = CO / H-REACNO = 15 HREF-CID = CO / H-REACNO = 16 HREF-CID = NBUTANOL / H-REACNO = 17 HREF-CID = PENTANOL \ \ FORCONTROL FCVAR1 = H2O \ ? BLOCK REQUIL "A400.A400SGR.R-410-WG" ? ; "ENG_MOLE" ; ; ICON2 ; \ PARAM NREAC = 1 TEMP = 570. <22> <2> PRES = 0. <20> <2> \ \ STOIC REACNO = 1 STOIC-CID = CO COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = H2O COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2 COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 COEF1 = 1. <0> <0> \ \ EXTENT-SPEC EXT-SPREACNO = 1 \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK DUPL "A400.A400SGR.DUP410" ? ; "ENG_MOLE" ; ; BLOCK ; \ PROPERTIES OPSETNAME = "PR-BM" \ ? REPORT "A400.A400SGR.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A400.HV-475" ? ; BLOCK ; ? "A400.HV-475.SOLVE" ? ? FLOWSHEET "A400.HV-475.GLOBAL" ? \ BLOCK BLKID = DPL100 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( "100-IN" M0-1 ) OUT = ( "100-OUT" M0-1 RAW M0-1 ) \ \ BLOCK BLKID = REJECT BLKTYPE = SEP MDLTYPE = "Sep" IN = ( RAW M0-1 ) OUT = ( BASIS M0-1 REJECT M0-1 QREJECT Q1-4 ) \ \ BLOCK BLKID = BURN BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( BASIS M0-1 O2 M0-1 ) OUT = ( QCOMB Q2-3 "PROD-1" M0-1 ) \ \ BLOCK BLKID = COMBSEP BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( "PROD-2" M0-1 ) OUT = ( COMBVAP M0-1 COMBLIQ M1-2 ) \ \ BLOCK BLKID = VAPWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( COMBLIQ M0-1 ) OUT = ( DPT M0-1 "QVAP-1" Q2-3 ) \ \ BLOCK BLKID = CONDWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( "WATER-V" M0-1 ) OUT = ( "WATER-L" M0-1 "QVAP-2" Q2-3 ) \ \ BLOCK BLKID = DRYER BLKTYPE = SEP MDLTYPE = "Sep" IN = ( DPT M0-1 COMBVAP M0-1 ) OUT = ( "WATER-V" M0-1 RESIDUE M0-1 ) \ \ BLOCK BLKID = NET BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-1" Q1-4 QCOMB Q1-4 QSHIFT Q1-4 ) OUT = ( QNET Q1-3 ) \ \ BLOCK BLKID = GROSS BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-2" Q1-4 QNET Q1-4 ) OUT = ( QGROSS Q1-3 ) \ \ BLOCK BLKID = SHIFT BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( "PROD-1" M0-1 ) OUT = ( "PROD-2" M0-1 QSHIFT Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A400.HV-475.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A400.HV-475.STREAM-NAMES" ? \ NAMES STREAM = "100-IN" TEXT = "Feed material" \ ? STREAM MATERIAL "A400.HV-475.100-IN" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 1.E-006 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TEMP = 60. <22> <2> PRES = 1. <20> <3> TOTAL = 3.E-006 <-80> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = WOOD FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = ASH FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = CHAR FLOW = 1E-006 <-80> <2> \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = ULTANAL ELEM = ( 0.92 <0> <0> 50.88 <0> <0> 6.04 <0> <0> 0.17 <0> <0> 0. <0> <0> 0.09 <0> <0> 41.9 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.045 <0> <0> 0.045 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 15.29 <0> <0> 83.84 <0> <0> 0.87 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = GENANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> 100. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = ULTANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = ULTANAL ELEM = ( 3.168 <0> <0> 65.894 <0> <0> 3.064 <0> <0> 0.281 <0> <0> 0. <0> <0> 0.149 <0> <0> 27.444 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.0745 <0> <0> 0.0745 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 87.18 <0> <0> 12.81 <0> <0> 0.01 <0> <0> ) \ \ COMMENTS COMMENTS = ( ";Poplar composition per Craig, K.R., Mann, M.K., " ";""Cost and Performance Analysis of Biomass-Bases " ";Integrated Gasification Combined-Cycle (BIGCC) Power " ";Systems"", National Renewable Energy Laboratory, " ";NREL/TP-430-21657, October, 1996." ";Modified sulfur analysis as follows: Evenly " ";distributed sulfur between sulfate and organic, with " ";no sulfur being classified as pyritic" ) \ ? STREAM MATERIAL "A400.HV-475.O2" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 77. <22> <2> PRES = 1. <20> <3> TOTAL = 9000. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = O2 FLOW = 9000. <-89> <2> \ ? BLOCK MIXER "A400.HV-475.GROSS" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A400.HV-475.NET" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK SEP "A400.HV-475.DRYER" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = METHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = "WATER-V" TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK SEP "A400.HV-475.REJECT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2O FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = METHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = BASIS TEMP = 77. <22> <2> PRES = 1. <20> <3> \ ? BLOCK HEATER "A400.HV-475.CONDWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A400.HV-475.VAPWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK FLASH2 "A400.HV-475.COMBSEP" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK RSTOIC "A400.HV-475.BURN" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 0. <20> <2> COMBUSTION = YES PROD-NOX = NO2 \ \ STOIC REACNO = 1 STOIC-CID = WOOD STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CHAR STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = NC KEY-CID = WOOD CONV = 1. <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = NC KEY-CID = CHAR CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = NO2 \ ? BLOCK RSTOIC "A400.HV-475.SHIFT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 1. <20> <3> \ \ STOIC REACNO = 1 STOIC-CID = NO2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = 0.5 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = NO2 CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = O2 \ ? BLOCK DUPL "A400.HV-475.DPL100" ? ; "ENG_MOLE" ; ; BLOCK ; ? REPORT "A400.HV-475.BLOCK-REPORT" ? ? BLOCK COMPR "A400.K-412" ? ; "ENG_MOLE" ; ; ICON3 ; \ PARAM TYPE = ISENTROPIC OPT-SPEC = PRES PRES = 19. <20> <13> SEFF = 0.85 <0> <0> NPHASE = 2 \ \ "BLOCK-OPTION" BLKOPFREWAT = NO \ ? BLOCK COMPR "A400.K-414" ? ; "ENG_MOLE" ; ; ICON2 ; \ PARAM TYPE = "GPSA-POLYTROP" OPT-SPEC = PRES PRES = 993. <20> <2> NPHASE = 2 \ \ "BLOCK-OPTION" BLKOPFREWAT = NO \ ? REPORT "A400.BLOCK-REPORT" ? ? BLOCK HIERARCHY A500 ? ; BLOCK ; ? "A500.SOLVE" ? ? FLOWSHEET "A500.ALCOHL" ? \ BLOCK BLKID = A503MS BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-3" IN = ( 506 M3-0 ) OUT = ( "A503MS.WET" M3-0 ) \ \ CONNECT BLKID = "$C-4" IN = ( 512 M4-0 ) OUT = ( "A503MS.FLUSH" M4-0 ) \ \ CONNECT BLKID = "$C-6" IN = ( "A503MS.MS-DRY" M5-0 ) OUT = ( 507 M3-0 ) \ \ CONNECT BLKID = "$C-2" IN = ( "A503MS.514" M6-0 ) OUT = ( 514 M4-0 ) \ \ CONNECT BLKID = "$C-9" IN = ( "A503MS.513V" M7-0 ) OUT = ( 513V M5-0 ) \ \ BLOCK BLKID = "H-503" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 505 M0-1 ) OUT = ( QH503 Q2-3 505B M0-1 ) \ \ BLOCK BLKID = "H-590" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 511B M0-1 ) OUT = ( QH590 Q2-3 590B M0-1 ) \ \ BLOCK BLKID = S502 BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 503 M0-1 ) OUT = ( 505 M1-2 531 M0-1 ) \ \ BLOCK BLKID = "H-592" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 592A M0-1 ) OUT = ( QH592 Q2-3 592B M0-1 ) \ \ BLOCK BLKID = "H-593" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 592B M0-1 ) OUT = ( 592C M0-1 QCH593 Q2-3 ) \ \ BLOCK BLKID = "H-591" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 590B M0-1 ) OUT = ( 590C M0-1 QCH591 Q2-3 ) \ \ BLOCK BLKID = "H-503B" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 505B M0-1 ) OUT = ( 506 M0-1 QH503B Q2-3 ) \ \ BLOCK BLKID = V500A BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 592C M0-1 ) OUT = ( 592D M0-1 ) \ \ BLOCK BLKID = HLOSS2 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 592D M0-1 ) OUT = ( QHLOSS2 Q2-3 592E M0-1 ) \ \ BLOCK BLKID = V500B BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 590C M0-1 ) OUT = ( 590D M0-1 ) \ \ BLOCK BLKID = HLOSS1 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 590D M0-1 ) OUT = ( QHLOSS1 Q2-3 590E M0-1 ) \ ? FLOWSHEET "A500.GLOBAL" ? \ BLOCK BLKID = A504 BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-21" IN = ( 507 M3-0 ) OUT = ( "A504.507" M3-0 ) \ \ CONNECT BLKID = "$C-5" IN = ( "A504.QRH504" Q4-0 ) OUT = ( QRH504 Q3-0 ) \ \ CONNECT BLKID = "$C-17" IN = ( "A504.QAH504" Q5-0 ) OUT = ( QAH504 Q4-0 ) \ \ CONNECT BLKID = "$C-19" IN = ( "A504.512" M6-0 ) OUT = ( 512 M5-0 ) \ \ CONNECT BLKID = "$C-1" IN = ( "A504.QRH505" Q7-0 ) OUT = ( QRH505 Q6-0 ) \ \ CONNECT BLKID = "$C-16" IN = ( "A504.QAH505" Q8-0 ) OUT = ( QAH505 Q7-0 ) \ \ CONNECT BLKID = "$C-8" IN = ( "A504.511B" M9-0 ) OUT = ( 511B M8-0 ) \ \ CONNECT BLKID = "$C-7" IN = ( "A504.592A" M10-0 ) OUT = ( 592A M9-0 ) \ \ BLOCK BLKID = "HV-590" BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-12" IN = ( 590E M3-0 ) OUT = ( "HV-590.100-IN" M3-0 ) \ \ CONNECT BLKID = "$C-11" IN = ( "HV-590.100-OUT" M4-0 ) OUT = ( 590 M3-0 ) \ \ BLOCK BLKID = "HV-592" BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-13" IN = ( 592E M3-0 ) OUT = ( "HV-592.100-IN" M3-0 ) \ \ CONNECT BLKID = "$C-10" IN = ( "HV-592.100-OUT" M4-0 ) OUT = ( 592 M3-0 ) \ \ BLOCK BLKID = PROP500A BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 514 M0-1 ) OUT = ( 515 M0-1 QPRP500A Q2-3 ) \ \ BLOCK BLKID = PROP500B BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 513V M0-1 531 M0-1 ) OUT = ( QPRP500B Q2-3 513 M0-1 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? FLOWSHEET "A500.STEAM" ? \ BLOCK BLKID = "H-507" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 534 M0-1 QRH504 Q1-2 QRH505 Q1-2 ) OUT = ( 536 M0-1 QXCS Q2-3 ) \ \ BLOCK BLKID = CONDSRS BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QAH504 Q1-4 QAH505 Q1-4 ) OUT = ( QA504TOT Q1-3 ) \ ? PROPERTIES "A500.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ \ PROPERTIES SECID-LIST = ALCOHL BASEOPSET = NRTL OPSETNAME = NRTL H-COMPS = "HC-1" / SECID-LIST = STEAM BASEOPSET = "STEAM-TA" OPSETNAME = "STEAM-TA" \ ? "A500.STREAM-NAMES" ? ? STREAM MATERIAL "A500.512" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED PRES = 45. <20> <2> VFRAC = 1. <0> <0> TOTAL = 100. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = METHANOL FLOW = 100. <-89> <2> \ ? STREAM MATERIAL "A500.534" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 394.9828 <22> <2> PRES = 50. <20> <13> TOTAL = 1.E-003 <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 0.001 <-89> <2> \ ? BLOCK MIXER "A500.CONDSRS" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK HEATER "A500.H-503" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = -5. <20> <2> VFRAC = 1. <0> <0> \ ? BLOCK HEATER "A500.H-503B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = 0. <20> <2> DEGSUP = 20. <31> <2> \ ? BLOCK HEATER "A500.H-507" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = -5. <20> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A500.H-590" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 120. <22> <2> PRES = -5. <20> <2> \ ? BLOCK HEATER "A500.H-591" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Cool stream to 60F for standard condition calcs" \ \ PARAM TEMP = 110. <22> <2> PRES = -5. <20> <2> \ \ COMMENTS COMMENTS = ( ";Not a real exchanger in PFD - sole purpose is to " ";allow calcs at standard temperature and pressure" ) \ ? BLOCK HEATER "A500.H-592" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 120. <22> <2> PRES = -5. <20> <2> \ ? BLOCK HEATER "A500.H-593" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 110. <22> <2> PRES = -5. <20> <2> \ ? BLOCK HEATER "A500.HLOSS1" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 60. <22> <2> PRES = 1. <20> <3> \ ? BLOCK HEATER "A500.HLOSS2" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 60. <22> <2> PRES = 1. <20> <3> \ ? BLOCK HEATER "A500.PROP500A" ? ; "ENG_MOLE" ; ; BLOCK ; \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ ? BLOCK HEATER "A500.PROP500B" ? ; "ENG_MOLE" ; ; BLOCK ; \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ ? BLOCK FLASH2 "A500.S502" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = 60. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK HIERARCHY "A500.A503MS" ? ; BLOCK ; ? "A500.A503MS.SOLVE" ? ? FLOWSHEET "A500.A503MS.ALCOHL" ? \ BLOCK BLKID = SEP BLKTYPE = SEP MDLTYPE = "Sep" IN = ( WET M0-1 ) OUT = ( "MS-DRY" M0-1 "MS-WATER" M0-1 "Q-SEP" Q1-4 ) \ \ BLOCK BLKID = FLUSH BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "MS-WATER" M0-1 FLUSH M0-1 ) OUT = ( 513F M0-1 ) \ \ BLOCK BLKID = "P-514" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 513L M0-1 ) OUT = ( 514 M0-1 WP514 W2-3 ) \ \ BLOCK BLKID = "S-513" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 513F M0-1 ) OUT = ( 513L M1-2 QAS513 Q3-4 513V M0-1 ) \ ? PROPERTIES "A500.A503MS.MAIN" ? \ GPROPERTIES GBASEOPSET = NRTL \ \ PROPERTIES SECID-LIST = ALCOHL BASEOPSET = NRTL OPSETNAME = NRTL H-COMPS = "HC-1" \ ? "A500.A503MS.STREAM-NAMES" ? ? BLOCK MIXER "A500.A503MS.FLUSH" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM T-EST = 240. <22> <2> \ ? BLOCK SEP "A500.A503MS.SEP" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 1 \ \ PARAM PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = "MS-DRY" SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = "MS-DRY" SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = "MS-DRY" SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = "MS-DRY" SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = "MS-DRY" SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = "MS-DRY" SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = "MS-DRY" SUBSTREAM = NC COMPS = CHAR / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = METHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = "MS-WATER" SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = "MS-WATER" SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> \ \ FLASH-SPECS FLASH-STREAM = "MS-DRY" PRES = 0. <20> <2> VFRAC = 1. <0> <0> \ \ FLASH-SPECS FLASH-STREAM = "MS-WATER" PRES = 0. <20> <2> VFRAC = 1. <0> <0> \ ? BLOCK FLASH2 "A500.A503MS.S-513" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM TEMP = 140. <22> <2> PRES = -5. <20> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK PUMP "A500.A503MS.P-514" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PRES = 1000. <20> <2> OPT-SPEC = PRES \ ? REPORT "A500.A503MS.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A500.A504" ? ; BLOCK ; ? "A500.A504.SOLVE" ? ? FLOWSHEET "A500.A504.ALCOHL" ? \ BLOCK BLKID = D504 BLKTYPE = RADFRAC MDLTYPE = "RadFrac" IN = ( 507A M0-1 ) OUT = ( 510 M0-1 QRH504 Q6-7 QAH504 Q5-6 511 M2-3 ) \ \ BLOCK BLKID = D505 BLKTYPE = RADFRAC MDLTYPE = "RadFrac" IN = ( 510 M0-1 ) OUT = ( 592A M2-3 512 M0-1 QRH505 Q6-7 QAH505 Q5-6 ) \ ? FLOWSHEET "A500.A504.GLOBAL" ? \ BLOCK BLKID = "HV-507" BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-1" IN = ( 507 M3-0 ) OUT = ( "HV-507.100-IN" M3-0 ) \ \ CONNECT BLKID = "$C-6" IN = ( "HV-507.100-OUT" M4-0 ) OUT = ( 507A M3-0 ) \ \ BLOCK BLKID = "HV-MXALC" BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-2" IN = ( 511 M3-0 ) OUT = ( "HV-MXALC.100" M3-0 ) \ \ CONNECT BLKID = "$C-3" IN = ( "HV-MXALC.100B" M4-0 ) OUT = ( 511B M3-0 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A500.A504.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ \ PROPERTIES SECID-LIST = ALCOHL BASEOPSET = NRTL OPSETNAME = NRTL H-COMPS = "HC-1" \ ? "A500.A504.STREAM-NAMES" ? ? STREAM MATERIAL "A500.A504.512" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED PRES = 45. <20> <2> VFRAC = 1. <0> <0> TOTAL = 100. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = METHANOL FLOW = 100. <-89> <2> \ ? BLOCK RADFRAC "A500.A504.D504" ? ; "ENG_MOLE" ; ; FRACT1 ; \ PARAM NSTAGE = 55 OPT-PRES = "DP-STAGE" OPT-PRES-TOP = "DP-COND" NSTAGEMAX = 56 \ \ "COL-CONFIG" CONDENSER = "PARTIAL-V" \ \ FEEDS FEED-SID = 507A FEED-STAGE = 44 \ \ PRODUCTS PROD-STREAM = 510 PROD-STAGE = 1 PROD-PHASE = V P-S = N / PROD-STREAM = 511 PROD-STAGE = 55 PROD-PHASE = L P-S = N \ \ H-PRODUCTS H-PROD-SID = QRH504 H-PROD-STAGE = 55 / H-PROD-SID = QAH504 H-PROD-STAGE = 1 \ \ "P-SPEC2" PRES1 = 45. <20> <2> \ \ "COL-SPECS" DP-STAGE = 0. <75> <2> BASIS-RDV = 1.0 <0> <0> RR-BASIS = MOLE BASIS-RR = 1.1 <-1> <0> BR-BASIS = MOLE BASIS-BR = 7.5 <-1> <0> DP-COND = 0. <75> <2> \ \ SPEC SPEC-NO = 1 SPEC-TYPE = "MASS-RECOV" VALUE = 0.99 <0> <0> SPEC-COMPS = ( ETHANOL ) SPEC-STREAMS = ( 510 ) SPEC-HIDE = REVEAL \ \ SPEC SPEC-NO = 2 SPEC-TYPE = "MASS-RECOV" VALUE = 0.99 <0> <0> SPEC-COMPS = ( PROPANOL ) SPEC-STREAMS = ( 511 ) SPEC-HIDE = REVEAL \ \ VARY VARY-NO = 1 VARTYPE = BR LB = 0.1 <0> <0> UB = 20. <0> <0> STEP = 1. <0> <0> VARY-HIDE = REVEAL \ \ VARY VARY-NO = 2 VARTYPE = RR LB = 0.2 <0> <0> UB = 5. <0> <0> VARY-HIDE = REVEAL \ \ TRAY-SIZE TS-SECNO = 1 TS-STAGE1 = 2 TS-STAGE2 = 24 TS-TRAYTYPE = FLOAT \ \ "KLL-VECS" \ \ "TRSZ-VECS" \ \ "PCKSR-VECS" \ ? BLOCK RADFRAC "A500.A504.D505" ? ; "ENG_MOLE" ; ; FRACT1 ; \ PARAM NSTAGE = 70 MAXOL = 50 OPT-PRES-TOP = "DP-COND" NSTAGEMAX = 71 \ \ "COL-CONFIG" CONDENSER = "PARTIAL-V" \ \ FEEDS FEED-SID = 510 FEED-STAGE = 25 \ \ PRODUCTS PROD-STREAM = 592A PROD-STAGE = 70 PROD-PHASE = L P-S = N / PROD-STREAM = 512 PROD-STAGE = 1 PROD-PHASE = V P-S = N \ \ H-PRODUCTS H-PROD-SID = QRH505 H-PROD-STAGE = 70 / H-PROD-SID = QAH505 H-PROD-STAGE = 1 \ \ "P-SPEC2" PRES1 = 45. <20> <2> \ \ "COL-SPECS" DP-STAGE = 0. <75> <2> BASIS-RDV = 1.0 <0> <0> RR-BASIS = MOLE BASIS-RR = 1. <-1> <0> BR-BASIS = MOLE BASIS-BR = 1.86 <-1> <0> DP-COND = 0. <75> <2> \ \ SPEC SPEC-NO = 1 SPEC-TYPE = "STDVOL-FRAC" VALUE = 0.005 <0> <0> SPEC-COMPS = ( METHANOL ) SPEC-STREAMS = ( 592A ) SPEC-HIDE = REVEAL \ \ SPEC SPEC-NO = 2 SPEC-TYPE = "MASS-RECOV" VALUE = 0.99 <0> <0> SPEC-COMPS = ( ETHANOL ) SPEC-STREAMS = ( 592A ) SPEC-HIDE = REVEAL \ \ VARY VARY-NO = 1 VARTYPE = BR LB = 0.1 <0> <0> UB = 5. <0> <0> VARY-HIDE = REVEAL \ \ VARY VARY-NO = 2 VARTYPE = RR LB = 0.1 <0> <0> UB = 40. <0> <0> VARY-HIDE = REVEAL \ \ TRAY-SIZE TS-SECNO = 1 TS-STAGE1 = 2 TS-STAGE2 = 39 TS-TRAYTYPE = FLOAT \ \ "KLL-VECS" \ \ "TRSZ-VECS" \ \ "PCKSR-VECS" \ ? BLOCK HIERARCHY "A500.A504.HV-507" ? ; BLOCK ; ? "A500.A504.HV-507.SOLVE" ? ? FLOWSHEET "A500.A504.HV-507.GLOBAL" ? \ BLOCK BLKID = DPL100 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( "100-IN" M0-1 ) OUT = ( "100-OUT" M0-1 RAW M0-1 ) \ \ BLOCK BLKID = REJECT BLKTYPE = SEP MDLTYPE = "Sep" IN = ( RAW M0-1 ) OUT = ( BASIS M0-1 REJECT M0-1 QREJECT Q1-4 ) \ \ BLOCK BLKID = BURN BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( BASIS M0-1 O2 M0-1 ) OUT = ( QCOMB Q2-3 "PROD-1" M0-1 ) \ \ BLOCK BLKID = COMBSEP BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( "PROD-2" M0-1 ) OUT = ( COMBVAP M0-1 COMBLIQ M1-2 ) \ \ BLOCK BLKID = VAPWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( COMBLIQ M0-1 ) OUT = ( DPT M0-1 "QVAP-1" Q2-3 ) \ \ BLOCK BLKID = CONDWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( "WATER-V" M0-1 ) OUT = ( "WATER-L" M0-1 "QVAP-2" Q2-3 ) \ \ BLOCK BLKID = DRYER BLKTYPE = SEP MDLTYPE = "Sep" IN = ( DPT M0-1 COMBVAP M0-1 ) OUT = ( "WATER-V" M0-1 RESIDUE M0-1 ) \ \ BLOCK BLKID = NET BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-1" Q1-4 QCOMB Q1-4 QSHIFT Q1-4 ) OUT = ( QNET Q1-3 ) \ \ BLOCK BLKID = GROSS BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-2" Q1-4 QNET Q1-4 ) OUT = ( QGROSS Q1-3 ) \ \ BLOCK BLKID = SHIFT BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( "PROD-1" M0-1 ) OUT = ( "PROD-2" M0-1 QSHIFT Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A500.A504.HV-507.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A500.A504.HV-507.STREAM-NAMES" ? \ NAMES STREAM = "100-IN" TEXT = "Feed material" \ ? STREAM MATERIAL "A500.A504.HV-507.100-IN" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 1.E-006 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TEMP = 60. <22> <2> PRES = 1. <20> <3> TOTAL = 3.E-006 <-80> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = WOOD FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = ASH FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = CHAR FLOW = 1E-006 <-80> <2> \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = ULTANAL ELEM = ( 0.92 <0> <0> 50.88 <0> <0> 6.04 <0> <0> 0.17 <0> <0> 0. <0> <0> 0.09 <0> <0> 41.9 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.045 <0> <0> 0.045 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 15.29 <0> <0> 83.84 <0> <0> 0.87 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = GENANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> 100. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = ULTANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = ULTANAL ELEM = ( 3.168 <0> <0> 65.894 <0> <0> 3.064 <0> <0> 0.281 <0> <0> 0. <0> <0> 0.149 <0> <0> 27.444 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.0745 <0> <0> 0.0745 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 87.18 <0> <0> 12.81 <0> <0> 0.01 <0> <0> ) \ \ COMMENTS COMMENTS = ( ";Poplar composition per Craig, K.R., Mann, M.K., " ";""Cost and Performance Analysis of Biomass-Bases " ";Integrated Gasification Combined-Cycle (BIGCC) Power " ";Systems"", National Renewable Energy Laboratory, " ";NREL/TP-430-21657, October, 1996." ";Modified sulfur analysis as follows: Evenly " ";distributed sulfur between sulfate and organic, with " ";no sulfur being classified as pyritic" ) \ ? STREAM MATERIAL "A500.A504.HV-507.O2" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 77. <22> <2> PRES = 1. <20> <3> TOTAL = 9000. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = O2 FLOW = 9000. <-89> <2> \ ? BLOCK MIXER "A500.A504.HV-507.GROSS" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A500.A504.HV-507.NET" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK SEP "A500.A504.HV-507.DRYER" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = METHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = "WATER-V" TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK SEP "A500.A504.HV-507.REJECT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = N2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = O2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2S FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NH3 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CH4 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H4 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C3H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C6H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C10H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = METHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = BASIS TEMP = 77. <22> <2> PRES = 1. <20> <3> \ \ FLASH-SPECS FLASH-STREAM = REJECT KODE = NOFLASH \ ? BLOCK HEATER "A500.A504.HV-507.CONDWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A500.A504.HV-507.VAPWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK FLASH2 "A500.A504.HV-507.COMBSEP" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK RSTOIC "A500.A504.HV-507.BURN" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 0. <20> <2> COMBUSTION = YES PROD-NOX = NO2 \ \ STOIC REACNO = 1 STOIC-CID = WOOD STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CHAR STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = NC KEY-CID = WOOD CONV = 1. <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = NC KEY-CID = CHAR CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = NO2 \ ? BLOCK RSTOIC "A500.A504.HV-507.SHIFT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 1. <20> <3> \ \ STOIC REACNO = 1 STOIC-CID = NO2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = 0.5 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = NO2 CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = O2 \ ? BLOCK DUPL "A500.A504.HV-507.DPL100" ? ; "ENG_MOLE" ; ; BLOCK ; ? REPORT "A500.A504.HV-507.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A500.A504.HV-MXALC" ? ; BLOCK ; ? "A500.A504.HV-MXALC.SOLVE" ? ? FLOWSHEET "A500.A504.HV-MXALC.GLOBAL" ? \ BLOCK BLKID = B2 BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 100A M0-1 ) OUT = ( 2 Q2-3 5IN M0-1 ) \ \ BLOCK BLKID = B3 BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( 5 M0-1 8A M0-1 ) OUT = ( 1 Q2-3 6 M0-1 ) \ \ BLOCK BLKID = B4 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( 100 M0-1 ) OUT = ( 100A M0-1 100B M0-1 ) \ \ BLOCK BLKID = DUPL5 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( 5IN M0-1 ) OUT = ( 5 M0-1 5B M0-1 ) \ \ BLOCK BLKID = DUPL8 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( 8 M0-1 ) OUT = ( 8A M0-1 8B M0-1 ) \ \ BLOCK BLKID = B3ALC BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( ALCIN M0-1 8B M0-1 ) OUT = ( COMGAS M0-1 QHVMALC Q2-3 ) \ \ BLOCK BLKID = SEPALC BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 5B M0-1 ) OUT = ( NONALC M0-1 ALCIN M0-1 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A500.A504.HV-MXALC.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A500.A504.HV-MXALC.STREAM-NAMES" ? ? STREAM MATERIAL "A500.A504.HV-MXALC.8" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 77. <22> <2> PRES = 1. <20> <3> TOTAL = 1.E-006 <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = O2 FLOW = 1E-006 <-89> <2> \ ? BLOCK SEP "A500.A504.HV-MXALC.SEPALC" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = NONALC SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = NONALC SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = NONALC SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = NONALC SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = NONALC SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = NONALC SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = NONALC SUBSTREAM = NC COMPS = CHAR / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = H2O FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = METHANOL FRACS = 1. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 1. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 1. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 1. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 1. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = ALCIN SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = ALCIN SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> \ \ FLASH-SPECS FLASH-STREAM = ALCIN TEMP = 77. <22> <2> PRES = 0. <20> <13> \ ? BLOCK HEATER "A500.A504.HV-MXALC.B2" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> PRES = 1. <20> <3> \ ? BLOCK RSTOIC "A500.A504.HV-MXALC.B3" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 0. <20> <2> HEAT-OF-REAC = "NO-CALC-SPEC" COMBUSTION = YES PROD-NOX = NO2 \ ? BLOCK RSTOIC "A500.A504.HV-MXALC.B3ALC" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 0. <20> <2> HEAT-OF-REAC = "NO-CALC-SPEC" COMBUSTION = YES PROD-NOX = NO2 \ ? BLOCK DUPL "A500.A504.HV-MXALC.B4" ? ; "ENG_MOLE" ; ; BLOCK ; ? BLOCK DUPL "A500.A504.HV-MXALC.DUPL5" ? ; "ENG_MOLE" ; ; BLOCK ; ? BLOCK DUPL "A500.A504.HV-MXALC.DUPL8" ? ; "ENG_MOLE" ; ; BLOCK ; ? REPORT "A500.A504.HV-MXALC.BLOCK-REPORT" ? ? REPORT "A500.A504.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A500.HV-590" ? ; BLOCK ; ? "A500.HV-590.SOLVE" ? ? FLOWSHEET "A500.HV-590.GLOBAL" ? \ BLOCK BLKID = DPL100 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( "100-IN" M0-1 ) OUT = ( "100-OUT" M0-1 RAW M0-1 ) \ \ BLOCK BLKID = REJECT BLKTYPE = SEP MDLTYPE = "Sep" IN = ( RAW M0-1 ) OUT = ( BASIS M0-1 REJECT M0-1 QREJECT Q1-4 ) \ \ BLOCK BLKID = BURN BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( BASIS M0-1 O2 M0-1 ) OUT = ( QCOMB Q2-3 "PROD-1" M0-1 ) \ \ BLOCK BLKID = COMBSEP BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( "PROD-2" M0-1 ) OUT = ( COMBVAP M0-1 COMBLIQ M1-2 ) \ \ BLOCK BLKID = VAPWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( COMBLIQ M0-1 ) OUT = ( DPT M0-1 "QVAP-1" Q2-3 ) \ \ BLOCK BLKID = CONDWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( "WATER-V" M0-1 ) OUT = ( "WATER-L" M0-1 "QVAP-2" Q2-3 ) \ \ BLOCK BLKID = DRYER BLKTYPE = SEP MDLTYPE = "Sep" IN = ( DPT M0-1 COMBVAP M0-1 ) OUT = ( "WATER-V" M0-1 RESIDUE M0-1 ) \ \ BLOCK BLKID = NET BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-1" Q1-4 QCOMB Q1-4 QSHIFT Q1-4 ) OUT = ( QNET Q1-3 ) \ \ BLOCK BLKID = GROSS BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-2" Q1-4 QNET Q1-4 ) OUT = ( QGROSS Q1-3 ) \ \ BLOCK BLKID = SHIFT BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( "PROD-1" M0-1 ) OUT = ( "PROD-2" M0-1 QSHIFT Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A500.HV-590.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A500.HV-590.STREAM-NAMES" ? \ NAMES STREAM = "100-IN" TEXT = "Feed material" \ ? STREAM MATERIAL "A500.HV-590.100-IN" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 1.E-006 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TEMP = 60. <22> <2> PRES = 1. <20> <3> TOTAL = 3.E-006 <-80> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = WOOD FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = ASH FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = CHAR FLOW = 1E-006 <-80> <2> \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = ULTANAL ELEM = ( 0.92 <0> <0> 50.88 <0> <0> 6.04 <0> <0> 0.17 <0> <0> 0. <0> <0> 0.09 <0> <0> 41.9 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.045 <0> <0> 0.045 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 15.29 <0> <0> 83.84 <0> <0> 0.87 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = GENANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> 100. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = ULTANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = ULTANAL ELEM = ( 3.168 <0> <0> 65.894 <0> <0> 3.064 <0> <0> 0.281 <0> <0> 0. <0> <0> 0.149 <0> <0> 27.444 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.0745 <0> <0> 0.0745 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 87.18 <0> <0> 12.81 <0> <0> 0.01 <0> <0> ) \ \ COMMENTS COMMENTS = ( ";Poplar composition per Craig, K.R., Mann, M.K., " ";""Cost and Performance Analysis of Biomass-Bases " ";Integrated Gasification Combined-Cycle (BIGCC) Power " ";Systems"", National Renewable Energy Laboratory, " ";NREL/TP-430-21657, October, 1996." ";Modified sulfur analysis as follows: Evenly " ";distributed sulfur between sulfate and organic, with " ";no sulfur being classified as pyritic" ) \ ? STREAM MATERIAL "A500.HV-590.O2" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 77. <22> <2> PRES = 1. <20> <3> TOTAL = 9000. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = O2 FLOW = 9000. <-89> <2> \ ? BLOCK MIXER "A500.HV-590.GROSS" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A500.HV-590.NET" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK SEP "A500.HV-590.DRYER" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = METHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = "WATER-V" TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK SEP "A500.HV-590.REJECT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = N2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = O2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2O FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2S FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NH3 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H4 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C3H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C6H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C10H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = METHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = WOOD FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = BASIS TEMP = 77. <22> <2> PRES = 1. <20> <3> \ ? BLOCK HEATER "A500.HV-590.CONDWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A500.HV-590.VAPWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK FLASH2 "A500.HV-590.COMBSEP" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK RSTOIC "A500.HV-590.BURN" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 0. <20> <2> COMBUSTION = YES PROD-NOX = NO2 \ \ STOIC REACNO = 1 STOIC-CID = WOOD STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CHAR STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = NC KEY-CID = WOOD CONV = 1. <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = NC KEY-CID = CHAR CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = NO2 \ ? BLOCK RSTOIC "A500.HV-590.SHIFT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 1. <20> <3> \ \ STOIC REACNO = 1 STOIC-CID = NO2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = 0.5 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = NO2 CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = O2 \ ? BLOCK DUPL "A500.HV-590.DPL100" ? ; "ENG_MOLE" ; ; BLOCK ; ? REPORT "A500.HV-590.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A500.HV-592" ? ; BLOCK ; ? "A500.HV-592.SOLVE" ? ? FLOWSHEET "A500.HV-592.GLOBAL" ? \ BLOCK BLKID = DPL100 BLKTYPE = DUPL MDLTYPE = "Dupl" IN = ( "100-IN" M0-1 ) OUT = ( "100-OUT" M0-1 RAW M0-1 ) \ \ BLOCK BLKID = REJECT BLKTYPE = SEP MDLTYPE = "Sep" IN = ( RAW M0-1 ) OUT = ( BASIS M0-1 REJECT M0-1 QREJECT Q1-4 ) \ \ BLOCK BLKID = BURN BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( BASIS M0-1 O2 M0-1 ) OUT = ( QCOMB Q2-3 "PROD-1" M0-1 ) \ \ BLOCK BLKID = COMBSEP BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( "PROD-2" M0-1 ) OUT = ( COMBVAP M0-1 COMBLIQ M1-2 ) \ \ BLOCK BLKID = VAPWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( COMBLIQ M0-1 ) OUT = ( DPT M0-1 "QVAP-1" Q2-3 ) \ \ BLOCK BLKID = CONDWAT BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( "WATER-V" M0-1 ) OUT = ( "WATER-L" M0-1 "QVAP-2" Q2-3 ) \ \ BLOCK BLKID = DRYER BLKTYPE = SEP MDLTYPE = "Sep" IN = ( DPT M0-1 COMBVAP M0-1 ) OUT = ( "WATER-V" M0-1 RESIDUE M0-1 ) \ \ BLOCK BLKID = NET BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-1" Q1-4 QCOMB Q1-4 QSHIFT Q1-4 ) OUT = ( QNET Q1-3 ) \ \ BLOCK BLKID = GROSS BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( "QVAP-2" Q1-4 QNET Q1-4 ) OUT = ( QGROSS Q1-3 ) \ \ BLOCK BLKID = SHIFT BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = ( "PROD-1" M0-1 ) OUT = ( "PROD-2" M0-1 QSHIFT Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A500.HV-592.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A500.HV-592.STREAM-NAMES" ? \ NAMES STREAM = "100-IN" TEXT = "Feed material" \ ? STREAM MATERIAL "A500.HV-592.100-IN" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 1.E-006 <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TEMP = 60. <22> <2> PRES = 1. <20> <3> TOTAL = 3.E-006 <-80> <0> JUNK = 3 \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = WOOD FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = ASH FLOW = 1E-006 <-80> <2> / SSID1 = NC CID = CHAR FLOW = 1E-006 <-80> <2> \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = ULTANAL ELEM = ( 0.92 <0> <0> 50.88 <0> <0> 6.04 <0> <0> 0.17 <0> <0> 0. <0> <0> 0.09 <0> <0> 41.9 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.045 <0> <0> 0.045 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = WOOD CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 15.29 <0> <0> 83.84 <0> <0> 0.87 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = GENANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> 100. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = ULTANAL ELEM = ( 100. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = ASH CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0. <0> <0> 0. <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = ULTANAL ELEM = ( 3.168 <0> <0> 65.894 <0> <0> 3.064 <0> <0> 0.281 <0> <0> 0. <0> <0> 0.149 <0> <0> 27.444 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = SULFANAL ELEM = ( 0. <0> <0> 0.0745 <0> <0> 0.0745 <0> <0> ) \ \ COMP-ATTR CATTSUB = NC CATTCID = CHAR CATTRIBUTE = PROXANAL ELEM = ( 0. <0> <0> 87.18 <0> <0> 12.81 <0> <0> 0.01 <0> <0> ) \ \ COMMENTS COMMENTS = ( ";Poplar composition per Craig, K.R., Mann, M.K., " ";""Cost and Performance Analysis of Biomass-Bases " ";Integrated Gasification Combined-Cycle (BIGCC) Power " ";Systems"", National Renewable Energy Laboratory, " ";NREL/TP-430-21657, October, 1996." ";Modified sulfur analysis as follows: Evenly " ";distributed sulfur between sulfate and organic, with " ";no sulfur being classified as pyritic" ) \ ? STREAM MATERIAL "A500.HV-592.O2" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 77. <22> <2> PRES = 1. <20> <3> TOTAL = 9000. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = O2 FLOW = 9000. <-89> <2> \ ? BLOCK MIXER "A500.HV-592.GROSS" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A500.HV-592.NET" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK SEP "A500.HV-592.DRYER" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = METHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = "WATER-V" SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = RESIDUE SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = RESIDUE SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = RESIDUE SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = "WATER-V" TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK SEP "A500.HV-592.REJECT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = N2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = O2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = H2S FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NH3 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NO2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CH4 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H4 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C2H2 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C3H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C6H6 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = C10H8 FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = METHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = ETHANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PROPANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = NBUTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = PENTANOL FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = CARBON FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 1. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = BASIS SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = REJECT SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = REJECT SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = REJECT SUBSTREAM = NC COMPS = CHAR \ \ FLASH-SPECS FLASH-STREAM = BASIS TEMP = 77. <22> <2> PRES = 1. <20> <3> \ \ FLASH-SPECS FLASH-STREAM = REJECT KODE = NOFLASH \ ? BLOCK HEATER "A500.HV-592.CONDWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A500.HV-592.VAPWAT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 77. <22> <2> VFRAC = 1. <0> <0> \ ? BLOCK FLASH2 "A500.HV-592.COMBSEP" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK RSTOIC "A500.HV-592.BURN" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 0. <20> <2> COMBUSTION = YES PROD-NOX = NO2 \ \ STOIC REACNO = 1 STOIC-CID = WOOD STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = CHAR STOIC-SSID = NC COEF = -1. <0> <0> \ \ STOIC REACNO = 2 STOIC-CID = O2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = CO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = H2O STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = SO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ STOIC1 REACNO1 = 2 STOIC-CID1 = NO2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = NC KEY-CID = WOOD CONV = 1. <0> <0> \ \ CONVEX EXT-REACNO = 2 KEY-SSID = NC KEY-CID = CHAR CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = NO2 \ ? BLOCK RSTOIC "A500.HV-592.SHIFT" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM TEMP = 77. <22> <2> PRES = 1. <20> <3> \ \ STOIC REACNO = 1 STOIC-CID = NO2 STOIC-SSID = MIXED COEF = -1. <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = N2 STOIC-SSID1 = MIXED COEF1 = 0.5 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = O2 STOIC-SSID1 = MIXED COEF1 = 1. <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID = MIXED KEY-CID = NO2 CONV = 1. <0> <0> \ \ FORCONTROL FCVAR1 = O2 \ ? BLOCK DUPL "A500.HV-592.DPL100" ? ; "ENG_MOLE" ; ; BLOCK ; ? REPORT "A500.HV-592.BLOCK-REPORT" ? ? BLOCK VALVE "A500.V500A" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM P-OUT = 5. <20> <13> \ ? BLOCK VALVE "A500.V500B" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM P-OUT = 1. <20> <3> \ ? REPORT "A500.BLOCK-REPORT" ? ? BLOCK HIERARCHY A600 ? ; BLOCK ; ? "A600.SOLVE" ? ? FLOWSHEET "A600.GLOBAL" ? \ BLOCK BLKID = A600BL BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-12" IN = ( 635 M3-0 ) OUT = ( "A600BL.635" M3-0 ) \ \ CONNECT BLKID = "$C-13" IN = ( 633 M4-0 ) OUT = ( "A600BL.633" M4-0 ) \ \ CONNECT BLKID = "$C-21" IN = ( "A600BL.643" M5-0 ) OUT = ( 643 M3-0 ) \ \ BLOCK BLKID = A600ST BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-10" IN = ( 607 M3-0 ) OUT = ( "A600ST.607" M3-0 ) \ \ CONNECT BLKID = "$C-1" IN = ( WK301 W4-0 ) OUT = ( "A600ST.WK301" W4-0 ) \ \ CONNECT BLKID = "$C-2" IN = ( WK410 W5-0 ) OUT = ( "A600ST.WK410" W5-0 ) \ \ CONNECT BLKID = "$C-23" IN = ( WK412 W6-0 ) OUT = ( "A600ST.WK412" W6-0 ) \ \ CONNECT BLKID = "$C-8" IN = ( "A600ST.200" M7-0 ) OUT = ( 200 M3-0 ) \ \ CONNECT BLKID = "$C-6" IN = ( "A600ST.534" M8-0 ) OUT = ( 534 M4-0 ) \ \ CONNECT BLKID = "$C-3" IN = ( "A600ST.616" M9-0 ) OUT = ( 616 M5-0 ) \ \ CONNECT BLKID = "$C-7" IN = ( "A600ST.WM602A" W10-0 ) OUT = ( WM602SFT W6-0 ) \ \ BLOCK BLKID = A600WTR BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-17" IN = ( 618 M3-0 ) OUT = ( "A600WTR.618" M3-0 ) \ \ CONNECT BLKID = "$C-20" IN = ( 314 M4-0 ) OUT = ( "A600WTR.314" M4-0 ) \ \ CONNECT BLKID = "$C-19" IN = ( 361 M5-0 ) OUT = ( "A600WTR.361" M5-0 ) \ \ CONNECT BLKID = "$C-14" IN = ( 351 M6-0 ) OUT = ( "A600WTR.351" M6-0 ) \ \ CONNECT BLKID = "$C-18" IN = ( 536 M7-0 ) OUT = ( "A600WTR.536" M7-0 ) \ \ CONNECT BLKID = "$C-22" IN = ( 395 M8-0 ) OUT = ( "A600WTR.395" M8-0 ) \ \ CONNECT BLKID = "$C-16" IN = ( "A600WTR.621" M9-0 ) OUT = ( 621 M3-0 ) \ \ CONNECT BLKID = "$C-15" IN = ( "A600WTR.626" M10-0 ) OUT = ( 626 M4-0 ) \ \ BLOCK BLKID = MX600B BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 632 M0-1 621 M0-1 ) OUT = ( 634 M0-1 ) \ \ BLOCK BLKID = PROP600H BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 601 M0-1 ) OUT = ( 600 M0-1 QPRP600H Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? FLOWSHEET "A600.STEAM" ? \ BLOCK BLKID = A600BF BLKTYPE = HIERARCHY MDLTYPE = "Hierarchy" \ \ CONNECT BLKID = "$C-11" IN = ( 616 M3-0 ) OUT = ( "A600BF.616" M3-0 ) \ \ CONNECT BLKID = "$C-9" IN = ( 626 M4-0 ) OUT = ( "A600BF.626" M4-0 ) \ \ CONNECT BLKID = "$C-5" IN = ( "A600BF.632" M5-0 ) OUT = ( 632 M3-0 ) \ \ CONNECT BLKID = "$C-4" IN = ( "A600BF.633" M6-0 ) OUT = ( 633 M4-0 ) \ \ BLOCK BLKID = "S-601" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 644 M0-1 ) OUT = ( QS601 Q3-4 605 M0-1 604 M1-2 ) \ \ BLOCK BLKID = "H-607A" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 606 M0-1 ) OUT = ( 606A M0-1 QH607A Q2-3 ) \ \ BLOCK BLKID = V600D BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 605 M0-1 ) OUT = ( 606 M0-1 ) \ \ BLOCK BLKID = "H-602" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 604 M0-1 ) OUT = ( 603 M0-1 QH602 Q2-3 ) \ \ BLOCK BLKID = "H-603" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 603 M0-1 ) OUT = ( 602 M0-1 QCH603 Q2-3 ) \ \ BLOCK BLKID = V600I BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 602 M0-1 ) OUT = ( 601 M0-1 ) \ \ BLOCK BLKID = MX607 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QH607A Q1-4 QH607B Q1-4 ) OUT = ( QH607 Q1-3 ) \ \ BLOCK BLKID = "H-607B" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 606A M0-1 ) OUT = ( 607 M0-1 QH607B Q2-3 ) \ ? PROPERTIES "A600.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ \ PROPERTIES SECID-LIST = STEAM BASEOPSET = "STEAM-TA" OPSETNAME = "STEAM-TA" \ ? "A600.STREAM-NAMES" ? ? STREAM MATERIAL "A600.351" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED PRES = 1.1 <20> <13> VFRAC = 0. <0> <0> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A600.607" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 1000. <22> <2> PRES = 850. <20> <2> BASIS = "MASS-FLOW" TOTAL = 500000. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 500000. <-80> <2> \ ? STREAM MATERIAL "A600.618" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A600.635" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 20. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A600.644" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED PRES = 865. <20> <35> VFRAC = 0.98 <0> <0> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 400000. <-80> <2> TOTAL = 1. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? BLOCK MIXER "A600.MX600B" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A600.MX607" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK HEATER "A600.H-602" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Blowdown Cooler" \ \ PARAM PRES = -5. <20> <2> DUTY = 0. <13> <2> \ ? BLOCK HEATER "A600.H-603" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Blowdown Water-Cooled Cooler" \ \ PARAM TEMP = 110. <22> <2> PRES = -5. <20> <2> \ ? BLOCK HEATER "A600.H-607A" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Steam superheater" \ \ PARAM TEMP = 900. <22> <2> PRES = -5. <20> <2> \ \ COMMENTS COMMENTS = ( ";Superheated steam temperature is a standard that " ";comes from Perry, R.H., Green, D.W., Maloney, J.O. " ";(1997). Perry's Chemical Engineers' Handbook, 7th " ";ed., McGraw-Hill. This heat exchanger uses a " ";combination the heat from Reformed syngas cooler " ";and reformer flue gas cooler to superheat the " ";steam. In the PFD, this heat exchanger does not " ";exist, as the required heat exchange occurs in the " ";two previously mentioned heat exchangers." ) \ ? BLOCK HEATER "A600.H-607B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 900. <22> <2> PRES = 0. <20> <2> \ ? BLOCK HEATER "A600.PROP600H" ? ; "ENG_MOLE" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Property Change" \ \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ \ COMMENTS COMMENTS = ( ";This is not a physical exchanger. It's purpose is " ";to explicitly handle the conversion from the STEAM " ";property package to the GLOBAL property package. " ";This is needed for cross-checks of the material and " ";energy balances." ) \ ? BLOCK FLASH2 "A600.S-601" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ DESCRIPTION DESCRIPTION = "Blowdown Flash Drum" \ \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK HIERARCHY "A600.A600BF" ? ; BLOCK ; ? "A600.A600BF.SOLVE" ? ? FLOWSHEET "A600.A600BF.STEAM" ? \ BLOCK BLKID = V600G BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 616 M0-1 ) OUT = ( 617 M0-1 ) \ \ BLOCK BLKID = "T-601" BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 617 M0-1 626 M0-1 ) OUT = ( 627 M0-1 ) \ \ BLOCK BLKID = "H-406407" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 630 M0-1 ) OUT = ( QH406407 Q2-3 631 M0-1 ) \ \ BLOCK BLKID = "T-603" BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = ( 631 M0-1 ) OUT = ( QT603 Q3-4 632 M0-1 633 M1-2 ) \ \ BLOCK BLKID = "P-603" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 627 M0-1 ) OUT = ( 628 M0-1 WP603 W2-3 ) \ \ BLOCK BLKID = V600H BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 628 M0-1 ) OUT = ( 629 M0-1 ) \ \ BLOCK BLKID = "M-602" BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 629 M0-1 ) OUT = ( 630 M0-1 ) \ ? PROPERTIES "A600.A600BF.MAIN" ? \ GPROPERTIES GBASEOPSET = "STEAM-TA" \ \ PROPERTIES SECID-LIST = STEAM BASEOPSET = "STEAM-TA" OPSETNAME = "STEAM-TA" \ ? "A600.A600BF.STREAM-NAMES" ? ? BLOCK MIXER "A600.A600BF.T-601" ? ; "ENG_MOLE" ; ; TANK ; \ DESCRIPTION DESCRIPTION = "Condensate Collection Tank" \ ? BLOCK HEATER "A600.A600BF.H-406407" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Deaerator Preheater" \ \ PARAM PRES = -3. <20> <2> VFRAC = 0. <0> <0> \ \ COMMENTS COMMENTS = ( ";This heat exchanger uses a combination the heat from " ";the LT shift precooler and the PSA precooler to " ";preheat the deaerator. In the PFD, this heat " ";exchanger does not exist, as the required heat " ";exchange occurs in the two previously mentioned heat " ";exchangers." ) \ ? BLOCK FLASH2 "A600.A600BF.T-603" ? ; "ENG_MOLE" ; ; "V-DRUM1" ; \ PARAM PRES = 0. <20> <2> DUTY = 0. <13> <2> \ \ FRAC SUBSTREAM = CISOLID \ \ FRAC SUBSTREAM = NC \ ? BLOCK PUMP "A600.A600BF.P-603" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Deaerator Feed Pump" \ \ PARAM PRES = 25. <20> <13> OPT-SPEC = PRES NPHASE = 2 \ \ "BLOCK-OPTION" BLKOPFREWAT = NO \ ? BLOCK VALVE "A600.A600BF.M-602" ? ; "ENG_MOLE" ; ; BLOCK ; \ PARAM OPT-DESIGN = "P-DROP" P-DROP = 5. <75> <2> \ ? BLOCK VALVE "A600.A600BF.V600G" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM OPT-DESIGN = "P-OUT" P-OUT = 1. <20> <3> P-DROP = 10. <75> <2> \ ? BLOCK VALVE "A600.A600BF.V600H" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM OPT-DESIGN = "P-DROP" P-DROP = 10. <75> <2> \ ? REPORT "A600.A600BF.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A600.A600BL" ? ; BLOCK ; ? "A600.A600BL.SOLVE" ? ? FLOWSHEET "A600.A600BL.GLOBAL" ? \ BLOCK BLKID = PROP600D BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 635 M0-1 ) OUT = ( QPRP600D Q2-3 636 M0-1 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? FLOWSHEET "A600.A600BL.STEAM" ? \ BLOCK BLKID = "P-604" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 638 M0-1 ) OUT = ( 639 M0-1 WP604 W2-3 ) \ \ BLOCK BLKID = V600B BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 639 M0-1 ) OUT = ( 640 M0-1 ) \ \ BLOCK BLKID = V600C BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 641 M0-1 ) OUT = ( 642 M0-1 ) \ \ BLOCK BLKID = PROP600E BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 636 M0-1 ) OUT = ( 637 M0-1 QPRP600E Q2-3 ) \ \ BLOCK BLKID = "H-605A" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 640 M0-1 ) OUT = ( QH605A Q2-3 640A M0-1 ) \ \ BLOCK BLKID = "H-201402" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 642 M0-1 ) OUT = ( QH201402 Q2-3 643 M0-1 ) \ \ BLOCK BLKID = MX600C BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 637 M0-1 633 M0-1 ) OUT = ( 638 M0-1 ) \ \ BLOCK BLKID = MX605 BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( QH605A Q1-4 QH605B Q1-4 ) OUT = ( QH605 Q1-3 ) \ \ BLOCK BLKID = "H-605B" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 640A M0-1 ) OUT = ( 641 M0-1 QH605B Q2-3 ) \ ? PROPERTIES "A600.A600BL.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ \ PROPERTIES SECID-LIST = STEAM BASEOPSET = "STEAM-TA" OPSETNAME = "STEAM-TA" \ ? STREAM MATERIAL "A600.A600BL.635" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 20. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? BLOCK MIXER "A600.A600BL.MX600C" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM NPHASE = 1 PHASE = L MAXIT = 100 \ \ "BLOCK-OPTION" BLKOPFREWAT = NO \ ? BLOCK MIXER "A600.A600BL.MX605" ? ; "ENG_MOLE" ; ; HEAT ; ? BLOCK HEATER "A600.A600BL.H-605A" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Boiler Feedwater Preheater" \ \ PARAM TEMP = 500. <22> <2> PRES = -5. <20> <2> \ \ COMMENTS COMMENTS = ( ";This heat exchanger uses a combination the heat from " ";the post tar cracker cooler and the LT Shift " ";precooler to preheat the boiler feed water. In the " ";PFD, this heat exchanger does not exist, as the " ";required heat exchange occurs the other two " ";previously mentioned heat exchangers." ) \ ? BLOCK HEATER "A600.A600BL.H-605B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = 0. <20> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A600.A600BL.H-201402" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Steam generator (boiler)" \ \ PARAM PRES = 0. <20> <2> VFRAC = 0.98 <0> <0> \ \ COMMENTS COMMENTS = ( ";This heat exchanger uses a combination the heat from " ";post tar cracker cooler and reformed syngas cooler " ";to generate steam. In the PFD, this heat exchanger " ";does not exist, as the required heat exchange occurs " ";in the other two previously mentioned heat " ";exchangers." ) \ ? BLOCK HEATER "A600.A600BL.PROP600D" ? ; "ENG_MOLE" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Property Change" \ \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ \ COMMENTS COMMENTS = ( ";This is not a physical exchanger. It's purpose is " ";to force the feed stream to be evaluated with the " ";GLOBAL property package. This is needed for cross-" ";checks of the material and energy balances." ) \ ? BLOCK HEATER "A600.A600BL.PROP600E" ? ; "ENG_MOLE" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Property Change" \ \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ \ COMMENTS COMMENTS = ( ";This is not a physical exchanger. It's purpose is " ";to explicitly handle the conversion from the GLOBAL " ";property package to the STEAM property package. " ";This is needed for cross-checks of the material and " ";energy balances." ) \ ? BLOCK PUMP "A600.A600BL.P-604" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Boiler Feed Water Pump" \ \ PARAM PRES = 930. <20> <35> OPT-SPEC = PRES \ ? BLOCK VALVE "A600.A600BL.V600B" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM OPT-DESIGN = "P-DROP" P-DROP = 50. <75> <2> \ ? BLOCK VALVE "A600.A600BL.V600C" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM OPT-DESIGN = "P-DROP" P-DROP = 10. <75> <2> \ ? REPORT "A600.A600BL.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A600.A600ST" ? ; BLOCK ; ? "A600.A600ST.SOLVE" ? ? FLOWSHEET "A600.A600ST.GLOBAL" ? \ BLOCK BLKID = PROP600G BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 647 M0-1 ) OUT = ( 200 M0-1 QPRP600G Q2-3 ) \ \ BLOCK BLKID = PROP600K BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 652 M0-1 ) OUT = ( 534 M0-1 QPRP600K Q2-3 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? FLOWSHEET "A600.A600ST.STEAM" ? \ BLOCK BLKID = "M-602A" BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( 607A M0-1 WM602B W1-2 ) OUT = ( WM602A W2-3 608 M0-1 ) \ \ BLOCK BLKID = "M-602B" BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( WM602C W1-2 602C M0-1 ) OUT = ( WM602B W2-3 610 M0-1 ) \ \ BLOCK BLKID = SP600B BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 610 M0-1 609B M0-1 ) OUT = ( 611 M0-1 612 M0-1 652 M0-1 350 M0-1 393 M0-1 394 M0-1 ) \ \ BLOCK BLKID = "M-602C" BLKTYPE = COMPR MDLTYPE = "Compr" IN = ( WK301 W1-2 WK410 W1-2 611C M0-1 WK412 W1-2 ) OUT = ( 614 M0-1 WM602C W2-3 ) \ \ BLOCK BLKID = "H-601" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 614 M0-1 ) OUT = ( 615 M0-1 QCH601 Q2-3 ) \ \ BLOCK BLKID = V600F BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 612 M0-1 ) OUT = ( 647 M0-1 ) \ \ BLOCK BLKID = SP602B BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 608 M0-1 607B M0-1 ) OUT = ( 609A M0-1 609B M0-1 ) \ \ BLOCK BLKID = SP602A BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 607 M0-1 ) OUT = ( 607A M0-1 607B M0-1 ) \ \ BLOCK BLKID = "P-602" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 615 M0-1 ) OUT = ( 616 M0-1 WP602 W2-3 ) \ \ BLOCK BLKID = "H-602C" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 611 M0-1 ) OUT = ( 611C M0-1 QH602C Q2-3 ) \ \ BLOCK BLKID = "H-602B" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 609A M0-1 ) OUT = ( 602C M0-1 QH602B Q2-3 ) \ ? PROPERTIES "A600.A600ST.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ \ PROPERTIES SECID-LIST = STEAM BASEOPSET = "STEAM-TA" OPSETNAME = "STEAM-TA" \ ? "A600.A600ST.STREAM-NAMES" ? ? STREAM MATERIAL "A600.A600ST.607" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 1000. <22> <2> PRES = 1264.696 <20> <2> BASIS = "MASS-FLOW" TOTAL = 500000. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 500000. <-80> <2> \ ? STREAM MATERIAL "A600.A600ST.612" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 265.8 <22> <2> PRES = 35. <20> <2> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 398. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 398. <-80> <2> \ ? BLOCK FSPLIT "A600.A600ST.SP600B" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM1 TOL1 = 1E-007 <0> <0> \ \ PARAM SID = 611 / SID = 612 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 652 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 350 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 393 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 394 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> \ \ STREAM-ORDER ORDER-STREAM = 611 ORDER = 5 / ORDER-STREAM = 612 ORDER = 1 / ORDER-STREAM = 652 ORDER = 3 / ORDER-STREAM = 350 ORDER = 4 / ORDER-STREAM = 393 ORDER = 2 / ORDER-STREAM = 394 \ ? BLOCK FSPLIT "A600.A600ST.SP602A" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM SID = 607A / SID = 607B FLOW-BASIS = MASS BASIS-FLOW = 1E-005 <-80> <2> \ \ STREAM-ORDER ORDER-STREAM = 607A / ORDER-STREAM = 607B \ ? BLOCK FSPLIT "A600.A600ST.SP602B" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM SID = 609A / SID = 609B FRAC = 1E-006 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = 609A / ORDER-STREAM = 609B \ ? BLOCK HEATER "A600.A600ST.H-601" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Steam turbine condenser" \ \ PARAM PRES = 0. <20> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A600.A600ST.H-602B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ ? BLOCK HEATER "A600.A600ST.H-602C" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ ? BLOCK HEATER "A600.A600ST.PROP600G" ? ; "ENG_MOLE" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Property Change" \ \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> TOL = 1E-007 <0> <0> \ \ COMMENTS COMMENTS = ( ";This is not a physical exchanger. It's purpose is " ";to explicitly handle the conversion from the STEAM " ";property package to the GLOBAL property package. " ";This is needed for cross-checks of the material and " ";energy balances." ) \ ? BLOCK HEATER "A600.A600ST.PROP600K" ? ; "ENG_MOLE" ; ; BLOCK ; \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ ? BLOCK PUMP "A600.A600ST.P-602" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Condensate Pump" \ \ PARAM PRES = 24.696 <20> <2> OPT-SPEC = PRES \ ? BLOCK COMPR "A600.A600ST.M-602A" ? ; "ENG_MOLE" ; ; ICON3 ; \ DESCRIPTION DESCRIPTION = "Extraction Steam Turbine/Generator" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = PRES PRES = 176. <20> <2> PEFF = 0.85 <0> <0> SEFF = 0.78 <0> <0> MEFF = 1. <0> <0> NPHASE = 2 SB-TOL = 0.0001 <0> <0> TOL = 1E-006 <0> <0> \ \ "BLOCK-OPTION" BLKOPFREWAT = NO \ \ COMMENTS COMMENTS = ( ";1st Turbine Stage" ) \ ? BLOCK COMPR "A600.A600ST.M-602B" ? ; "ENG_MOLE" ; ; ICON3 ; \ DESCRIPTION DESCRIPTION = "Extraction Steam Turbine/Generator" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = PRES PRES = 50. <20> <13> SEFF = 0.78 <0> <0> MEFF = 1. <0> <0> NPHASE = 2 \ \ "BLOCK-OPTION" BLKOPFREWAT = NO \ \ COMMENTS COMMENTS = ( ";2nd Turbine Stage" ) \ ? BLOCK COMPR "A600.A600ST.M-602C" ? ; "ENG_MOLE" ; ; ICON3 ; \ DESCRIPTION DESCRIPTION = "Extraction Steam Turbine/Generator" \ \ PARAM TYPE = ISENTROPIC OPT-SPEC = PRES PRES = 1.5 <20> <35> SEFF = 0.78 <0> <0> MEFF = 1. <0> <0> NPHASE = 2 \ \ "BLOCK-OPTION" BLKOPFREWAT = NO \ \ COMMENTS COMMENTS = ( ";3rd Turbine Stage" ) \ ? BLOCK VALVE "A600.A600ST.V600F" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM OPT-DESIGN = "P-OUT" P-OUT = 25. <20> <2> P-DROP = 10. <75> <2> \ ? REPORT "A600.A600ST.BLOCK-REPORT" ? ? BLOCK HIERARCHY "A600.A600WTR" ? ; BLOCK ; ? "A600.A600WTR.SOLVE" ? ? FLOWSHEET "A600.A600WTR.GLOBAL" ? \ BLOCK BLKID = PROP600A BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 618B M0-1 ) OUT = ( 619 M0-1 QPRP600A Q2-3 ) \ \ BLOCK BLKID = SP400B BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 314 M0-1 361 M0-1 ) OUT = ( 333 M0-1 ) \ \ BLOCK BLKID = "T-601A" BLKTYPE = SEP MDLTYPE = "Sep" IN = ( 333 M0-1 ) OUT = ( 621 M0-1 622 M0-1 QT601A Q1-4 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? FLOWSHEET "A600.A600WTR.STEAM" ? \ BLOCK BLKID = "P-601" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 618 M0-1 ) OUT = ( WP601 W2-3 618B M0-1 ) \ \ BLOCK BLKID = V600A BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 624 M0-1 ) OUT = ( 626 M0-1 ) \ \ BLOCK BLKID = MX600A BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 623 M0-1 351 M0-1 536 M0-1 620B M0-1 395 M0-1 ) OUT = ( 624 M0-1 ) \ \ BLOCK BLKID = PROP600C BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 622 M0-1 ) OUT = ( 623 M0-1 QPRP600C Q2-3 ) \ \ BLOCK BLKID = PROP600B BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 619 M0-1 ) OUT = ( 620 M0-1 QPRP600B Q2-3 ) \ \ BLOCK BLKID = "H-620" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 620 M0-1 ) OUT = ( 620B M0-1 QH620 Q2-3 ) \ ? PROPERTIES "A600.A600WTR.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ \ PROPERTIES SECID-LIST = STEAM BASEOPSET = "STEAM-TA" OPSETNAME = "STEAM-TA" \ ? "A600.A600WTR.STREAM-NAMES" ? ? STREAM MATERIAL "A600.A600WTR.618" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A600.A600WTR.624" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" FLOWBASE = MASS TOTAL = 200000. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 200000. <-80> <2> \ ? BLOCK MIXER "A600.A600WTR.MX600A" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM PRES = 0. <20> <2> \ ? BLOCK MIXER "A600.A600WTR.SP400B" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM PRES = 0. <20> <3> \ ? BLOCK SEP "A600.A600WTR.T-601A" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 1 \ \ PARAM PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 621 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 621 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = 621 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = 621 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = 621 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = 621 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = 621 SUBSTREAM = NC COMPS = CHAR / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = H2 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = CO FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = N2 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = O2 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = AR FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = CO2 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = H2O FRACS = 1. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = H2S FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = SO2 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = NH3 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = NO2 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = CH4 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = C2H6 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = C2H4 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = C2H2 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = C3H8 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "I-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "N-C4H10" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "PENTANE+" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = C6H6 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = C10H8 FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "NH4+" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "H3O+" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "NH2COO-" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "OH-" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "HCO3-" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "HS-" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "CO3--" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = "S--" FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = 622 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = 622 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = 622 SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> \ \ COMMENTS COMMENTS = ( ";Degas the stream before sending the water component to the " ";steam cycle" ) \ ? BLOCK HEATER "A600.A600WTR.H-620" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = -1. <20> <2> VFRAC = 0. <0> <0> \ ? BLOCK HEATER "A600.A600WTR.PROP600A" ? ; "ENG_MOLE" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Property Change" \ \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ \ COMMENTS COMMENTS = ( ";This is not a physical exchanger. It's purpose is " ";the force the feed stream to be evaluated with the " ";GLOBAL property package. This is needed for cross-" ";checks of the material and energy balances." ) \ ? BLOCK HEATER "A600.A600WTR.PROP600B" ? ; "ENG_MOLE" ; ; BLOCK ; \ DESCRIPTION DESCRIPTION = "Property Change" \ \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ \ COMMENTS COMMENTS = ( ";This is not a physical exchanger. It's purpose is " ";to explicitly handle the conversion from the GLOBAL " ";property package to the STEAM property package. " ";This is needed for cross-checks of the material and " ";energy balances." ) \ ? BLOCK HEATER "A600.A600WTR.PROP600C" ? ; "ENG_MOLE" ; ; BLOCK ; \ PARAM PRES = 0. <20> <2> DELT = 0. <31> <2> \ ? BLOCK PUMP "A600.A600WTR.P-601" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Collection Pump" \ \ PARAM PRES = 24.696 <20> <2> OPT-SPEC = PRES \ ? BLOCK VALVE "A600.A600WTR.V600A" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM OPT-DESIGN = "P-OUT" P-OUT = 1. <20> <3> P-DROP = 10. <75> <2> \ ? REPORT "A600.A600WTR.BLOCK-REPORT" ? ? BLOCK VALVE "A600.V600D" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM OPT-DESIGN = "P-DROP" P-DROP = 10. <75> <2> \ ? BLOCK VALVE "A600.V600I" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM P-OUT = 1. <20> <3> \ ? REPORT "A600.BLOCK-REPORT" ? ? BLOCK HIERARCHY A700 ? ; BLOCK ; ? "A700.SOLVE" ? ? FLOWSHEET "A700.GLOBAL" ? \ BLOCK BLKID = "H-601-CT" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( QCH601CT Q1-2 720 M0-1 ) OUT = ( 721 M0-1 ) \ \ BLOCK BLKID = V700B BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 718 M0-1 ) OUT = ( 719 M0-1 ) \ \ BLOCK BLKID = SP700A BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 712 M0-1 ) OUT = ( 714 M0-1 713 M0-1 ) \ \ BLOCK BLKID = MX700B BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 711 M0-1 710 M0-1 709 M0-1 600 M0-1 ) OUT = ( 712 M0-1 ) \ \ BLOCK BLKID = "P-701" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( 714 M0-1 ) OUT = ( 715 M0-1 WP701 W2-3 ) \ \ BLOCK BLKID = V700A BLKTYPE = VALVE MDLTYPE = "Valve" IN = ( 715 M0-1 ) OUT = ( 716 M0-1 ) \ \ BLOCK BLKID = MX700A BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 704 M0-1 705 M0-1 ) OUT = ( 706 M0-1 ) \ \ BLOCK BLKID = MX700D BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 701 M0-1 700 M0-1 ) OUT = ( 702 M0-1 ) \ \ BLOCK BLKID = HX700C BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 702 M0-1 ) OUT = ( 703 M0-1 QHX700C Q2-3 ) \ \ BLOCK BLKID = "H-CTREF" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 707 M0-1 ) OUT = ( 708 M0-1 ) \ \ BLOCK BLKID = MX700E BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WM701 W2-7 WP701 W2-7 ) OUT = ( W700A W2-4 ) \ \ BLOCK BLKID = MX700C BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( 721 M0-1 723 M0-1 725 M0-1 729 M0-1 731 M0-1 733 M0-1 737 M0-1 739 M0-1 741 M0-1 ) OUT = ( 718 M0-1 ) \ \ BLOCK BLKID = SP700B BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( 717 M0-1 ) OUT = ( 720 M0-1 722 M0-1 724 M0-1 728 M0-1 730 M0-1 732 M0-1 736 M0-1 738 M0-1 740 M0-1 ) \ \ BLOCK BLKID = "H-305-CT" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( QCH305CT Q1-2 730 M0-1 ) OUT = ( 731 M0-1 ) \ \ BLOCK BLKID = "H-603-CT" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( QCH603CT Q1-2 728 M0-1 ) OUT = ( 729 M0-1 ) \ \ BLOCK BLKID = "H-303-CT" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( QCH303CT Q1-2 724 M0-1 ) OUT = ( 725 M0-1 ) \ \ BLOCK BLKID = "M-301-CT" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( QCM301CT Q1-2 722 M0-1 ) OUT = ( 723 M0-1 ) \ \ BLOCK BLKID = SP700C BLKTYPE = FSPLIT MDLTYPE = "FSplit" IN = ( QCTOTAL Q1-2 ) OUT = ( QCH305CT Q1-4 QCH603CT Q1-4 QCH303CT Q1-4 QCM301CT Q1-4 QCH601CT Q1-4 QCM201CT Q1-4 QCH414CT Q1-4 QCH591CT Q1-4 QCH593CT Q1-4 ) \ \ BLOCK BLKID = "M-201-CT" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 732 M0-1 QCM201CT Q1-2 ) OUT = ( 733 M0-1 ) \ \ BLOCK BLKID = "H-414-CT" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 736 M0-1 QCH414CT Q1-2 ) OUT = ( 737 M0-1 ) \ \ BLOCK BLKID = HX900B BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 435 M0-1 ) OUT = ( 436 M0-1 QHX900B Q2-3 ) \ \ BLOCK BLKID = "H-591-CT" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( QCH591CT Q1-2 738 M0-1 ) OUT = ( 739 M0-1 ) \ \ BLOCK BLKID = "H-593-CT" BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( QCH593CT Q1-2 740 M0-1 ) OUT = ( 741 M0-1 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A700.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" GOPSETNAME = SYSOP3 GTRUE-COMPS = YES PARCON = -2 \ ? "A700.STREAM-NAMES" ? ? STREAM MATERIAL "A700.435" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 1. <20> <3> BASIS = "MOLE-FRAC" FLOWBASE = MASS TOTFLOW = 1000000. <-80> <2> TOTAL = 1. <-4> <0> JUNK = 5 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.75666 <-4> <0> / SSID1 = MIXED CID = O2 FLOW = 0.202967 <-4> <0> / SSID1 = MIXED CID = AR FLOW = 0.00905 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.00032 <-4> <0> / SSID1 = MIXED CID = H2O FLOW = 0.031003 <-4> <0> \ ? STREAM MATERIAL "A700.700" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 32. <22> <2> PRES = 1. <20> <3> BASIS = "MOLE-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-4> <0> JUNK = 4 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.78087 <-4> <0> / SSID1 = MIXED CID = O2 FLOW = 0.20946 <-4> <0> / SSID1 = MIXED CID = AR FLOW = 0.00934 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.00033 <-4> <0> \ ? STREAM MATERIAL "A700.701" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 32. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A700.703" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 10. <22> <2> PRES = 14.7 <20> <2> TOTFLOW = 1. <-89> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-89> <2> \ ? STREAM MATERIAL "A700.704" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 102. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A700.705" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 102. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FLOW" TOTAL = 1. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 1. <-80> <2> \ ? STREAM MATERIAL "A700.706" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 50. <22> <2> PRES = 14.7 <20> <2> TOTFLOW = 1. <-89> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-89> <2> \ ? STREAM MATERIAL "A700.707" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 64.696 <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A700.709" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 92.5 <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A700.710" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A700.711" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 1. <20> <3> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A700.713" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 50. <22> <2> PRES = 14.7 <20> <2> TOTFLOW = 1. <-89> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-89> <2> \ ? STREAM MATERIAL "A700.717" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 64.696 <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1. <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? STREAM MATERIAL "A700.719" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 50. <22> <2> PRES = 14.7 <20> <2> TOTFLOW = 1. <-89> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-89> <2> \ ? STREAM HEAT "A700.QCH303CT" ? ; "ENG_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 1E-006 <13> <2> \ ? STREAM HEAT "A700.QCH305CT" ? ; "ENG_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 1E-006 <13> <2> \ ? STREAM HEAT "A700.QCH601CT" ? ; "ENG_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 1E-006 <13> <2> \ ? STREAM HEAT "A700.QCH603CT" ? ; "ENG_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 1E-006 <13> <2> \ ? STREAM HEAT "A700.QCM301CT" ? ; "ENG_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 1E-006 <13> <2> \ ? STREAM HEAT "A700.QCTOTAL" ? ; "ENG_MOLE" ; \ INFO H-SCLASS = HEAT DUTY = 1. <13> <2> \ ? STREAM WORK "A700.WM701" ? ; "ENG_MOLE" ; \ INFO POWER = 1E-006 <19> <2> \ ? BLOCK MIXER "A700.MX700A" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A700.MX700B" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A700.MX700C" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A700.MX700D" ? ; "ENG_MOLE" ; ; TRIANGLE ; ? BLOCK MIXER "A700.MX700E" ? ; "ENG_MOLE" ; ; WORK ; \ COMMENTS COMMENTS = ( ";This mixer is here so that the GUI will run....the " ";work stream for the cooling tower fan has to be " ";connected to something." ) \ ? BLOCK FSPLIT "A700.SP700A" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM SID = 714 / SID = 713 FLOW-BASIS = MASS BASIS-FLOW = 0.1 <-80> <2> \ \ STREAM-ORDER ORDER-STREAM = 714 / ORDER-STREAM = 713 \ ? BLOCK FSPLIT "A700.SP700B" ? ; "ENG_MOLE" ; ; TRIANGLE ; \ PARAM SID = 720 FLOW-BASIS = MASS / SID = 722 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 724 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 728 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 730 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 732 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 736 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 738 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> / SID = 740 FLOW-BASIS = MASS BASIS-FLOW = 1. <-80> <2> \ \ STREAM-ORDER ORDER-STREAM = 720 / ORDER-STREAM = 722 / ORDER-STREAM = 724 / ORDER-STREAM = 728 / ORDER-STREAM = 730 / ORDER-STREAM = 732 / ORDER-STREAM = 736 / ORDER-STREAM = 738 / ORDER-STREAM = 740 \ ? BLOCK FSPLIT "A700.SP700C" ? ; "ENG_MOLE" ; ; HEAT ; \ PARAM SID = QCH305CT FRAC = 0.1 <0> <0> / SID = QCH603CT FRAC = 0.1 <0> <0> / SID = QCH303CT FRAC = 0.1 <0> <0> / SID = QCM301CT FRAC = 0.1 <0> <0> / SID = QCH601CT / SID = QCM201CT FRAC = 0.1 <0> <0> / SID = QCH414CT FRAC = 0.1 <0> <0> / SID = QCH591CT FRAC = 0.1 <0> <0> / SID = QCH593CT FRAC = 0.1 <0> <0> \ \ STREAM-ORDER ORDER-STREAM = QCH305CT / ORDER-STREAM = QCH603CT / ORDER-STREAM = QCH303CT / ORDER-STREAM = QCM301CT / ORDER-STREAM = QCH601CT / ORDER-STREAM = QCM201CT / ORDER-STREAM = QCH414CT / ORDER-STREAM = QCH591CT / ORDER-STREAM = QCH593CT \ ? BLOCK HEATER "A700.H-303-CT" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "CW side water-cooled aftercooler exchanger (syngas compressor)" \ \ PARAM PRES = -5. <20> <2> \ ? BLOCK HEATER "A700.H-305-CT" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Cooling water requirement for LO-CAT" \ \ PARAM PRES = -5. <20> <2> \ \ COMMENTS COMMENTS = ( ";This exchanger approximates the cooling water use " ";for the LO-CAT absorbent cooler, H-309, which is " ";included in the PFD but not in the simulation." ) \ ? BLOCK HEATER "A700.H-414-CT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = -5. <20> <2> \ ? BLOCK HEATER "A700.H-591-CT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = -5. <20> <2> \ ? BLOCK HEATER "A700.H-593-CT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = -5. <20> <2> \ ? BLOCK HEATER "A700.H-601-CT" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "CW side of steam turbine condenser" \ \ PARAM PRES = -5. <20> <2> \ ? BLOCK HEATER "A700.H-603-CT" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "CW side of blowdown water-cooled cooler" \ \ PARAM PRES = -5. <20> <2> \ ? BLOCK HEATER "A700.H-CTREF" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "Reference For Calculating Cooling Water Flows" \ \ PARAM TEMP = 110. <22> <2> PRES = -5. <20> <2> \ \ COMMENTS COMMENTS = ( ";This block is used to provide reference enthalpy data for " ";calculating the cooling water flows for the various cooling water " ";heat exchangers" ) \ ? BLOCK HEATER "A700.HX700C" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM TEMP = 90. <22> <2> PRES = 0. <20> <2> \ ? BLOCK HEATER "A700.HX900B" ? ; "ENG_MOLE" ; ; AIRCOOLER ; \ DESCRIPTION DESCRIPTION = "Reference For Air Coolers" \ \ PARAM TEMP = 150. <22> <2> PRES = 0. <20> <2> \ \ COMMENTS COMMENTS = ( ";This block is here to provide reference enthalpy " ";data for air streams entering and exiting air " ";coolers." ) \ ? BLOCK HEATER "A700.M-201-CT" ? ; "ENG_MOLE" ; ; HEATER ; \ DESCRIPTION DESCRIPTION = "CW side of sand/ash cooler" \ \ PARAM PRES = -5. <20> <2> \ ? BLOCK HEATER "A700.M-301-CT" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = -5. <20> <2> \ ? BLOCK PUMP "A700.P-701" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM PRES = 74.696 <20> <2> OPT-SPEC = PRES \ ? BLOCK VALVE "A700.V700A" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM OPT-DESIGN = "P-DROP" P-DROP = 10. <75> <2> \ ? BLOCK VALVE "A700.V700B" ? ; "ENG_MOLE" ; ; VALVE2 ; \ PARAM P-OUT = 1. <20> <3> \ ? REPORT "A700.BLOCK-REPORT" ? ? BLOCK HIERARCHY A900 ? ; BLOCK ; ? "A900.SOLVE" ? ? FLOWSHEET "A900.GLOBAL" ? \ BLOCK BLKID = WMX900A BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( W200 W2-7 W300 W2-7 W400 W2-7 W600 W2-7 W700 W2-7 WMISC W2-7 W100 W2-7 W500 W2-7 ) OUT = ( WPLANT W2-4 ) \ \ BLOCK BLKID = WMX900B BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WGEN W2-7 WPLANT W2-7 ) OUT = ( WNET W2-4 ) \ \ BLOCK BLKID = WMXHOLD BLKTYPE = MIXER MDLTYPE = "Mixer" IN = ( WK332FAN W2-7 WK513FAN W2-7 WK413FAN W2-7 WK505FAN W2-7 WK504FAN W2-7 WK333FAN W2-7 ) OUT = ( WKMXHOUT W2-4 ) \ \ "DEF-STREAM" SCLASS = MIXCINC \ ? PROPERTIES "A900.MAIN" ? \ GPROPERTIES GBASEOPSET = "RKS-BM" \ ? "A900.STREAM-NAMES" ? ? STREAM WORK "A900.W100" ? ; "ENG_MOLE" ; \ INFO POWER = 1E-006 <19> <2> \ ? STREAM WORK "A900.W200" ? ; "ENG_MOLE" ; \ INFO POWER = 1E-006 <19> <2> \ ? STREAM WORK "A900.W300" ? ; "ENG_MOLE" ; \ INFO POWER = 1E-006 <19> <2> \ ? STREAM WORK "A900.W400" ? ; "ENG_MOLE" ; \ INFO POWER = 1E-006 <19> <2> \ ? STREAM WORK "A900.W500" ? ; "ENG_MOLE" ; \ INFO POWER = 1E-006 <19> <2> \ ? STREAM WORK "A900.W600" ? ; "ENG_MOLE" ; \ INFO POWER = 1E-006 <19> <2> \ ? STREAM WORK "A900.W700" ? ; "ENG_MOLE" ; \ INFO POWER = 1E-006 <19> <2> \ ? STREAM WORK "A900.WGEN" ? ; "ENG_MOLE" ; \ INFO POWER = 1E-006 <19> <2> \ ? STREAM WORK "A900.WK332FAN" ? ; "ENG_MOLE" ; \ INFO POWER = 0.1 <19> <2> \ ? STREAM WORK "A900.WK333FAN" ? ; "ENG_MOLE" ; \ INFO POWER = 0.1 <19> <2> \ ? STREAM WORK "A900.WK413FAN" ? ; "ENG_MOLE" ; \ INFO POWER = 1. <19> <2> \ ? STREAM WORK "A900.WK504FAN" ? ; "ENG_MOLE" ; \ INFO POWER = 1. <19> <2> \ ? STREAM WORK "A900.WK505FAN" ? ; "ENG_MOLE" ; \ INFO POWER = 1. <19> <2> \ ? STREAM WORK "A900.WK513FAN" ? ; "ENG_MOLE" ; \ INFO POWER = 1. <19> <2> \ ? STREAM WORK "A900.WMISC" ? ; "ENG_MOLE" ; \ INFO POWER = 1E-006 <19> <2> \ ? BLOCK MIXER "A900.WMX900A" ? ; "ENG_MOLE" ; ; WORK ; ? BLOCK MIXER "A900.WMX900B" ? ; "ENG_MOLE" ; ; WORK ; ? BLOCK MIXER "A900.WMXHOLD" ? ; "ENG_MOLE" ; ; WORK ; ? REPORT "A900.BLOCK-REPORT" ? ? BLOCK HIERARCHY AREFRNC ? ; BLOCK ; ? "AREFRNC.SOLVE" ? ? FLOWSHEET "AREFRNC.GLOBAL" ? \ BLOCK BLKID = DUMSEP BLKTYPE = SEP MDLTYPE = "Sep" IN = ( AMBAIR M0-1 ) OUT = ( DUMMY3 M0-1 DUMMY4 M0-1 ) \ \ BLOCK BLKID = "MEFF-A" BLKTYPE = PUMP MDLTYPE = "Pump" IN = ( DUMMY1 M0-1 ) OUT = ( DUMMY2 M0-1 ) \ ? FLOWSHEET "AREFRNC.STEAM" ? \ BLOCK BLKID = HX100A BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 124 M0-1 ) OUT = ( 125 M0-1 QHX100A Q2-3 ) \ \ BLOCK BLKID = HX100B BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( 122 M0-1 ) OUT = ( QHX100B Q2-3 123 M0-1 ) \ ? PROPERTIES "AREFRNC.MAIN" ? \ GPROPERTIES GBASEOPSET = "STEAM-TA" \ \ PROPERTIES SECID-LIST = STEAM BASEOPSET = "STEAM-TA" OPSETNAME = "STEAM-TA" \ ? "STREAM-CLASS" "AREFRNC.DEF-STREAMS" ? ? "AREFRNC.STREAM-NAMES" ? \ NAMES STREAM = AMBAIR TEXT = "reference for ambient air" \ ? STREAM MATERIAL "AREFRNC.122" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 77. <22> <2> VFRAC = 0. <0> <0> BASIS = "MASS-FLOW" TOTAL = 1. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-80> <2> \ ? STREAM MATERIAL "AREFRNC.124" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 77. <22> <2> VFRAC = 0. <0> <0> BASIS = "MASS-FLOW" TOTAL = 1. <-80> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-80> <2> \ ? STREAM MATERIAL "AREFRNC.AMBAIR" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 90. <22> <2> PRES = 1. <20> <3> BASIS = "MOLE-FRAC" FLOWBASE = MASS TOTFLOW = 1E-005 <-80> <2> TOTAL = 1. <-4> <0> JUNK = 5 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = N2 FLOW = 0.75666 <-4> <0> / SSID1 = MIXED CID = O2 FLOW = 0.202967 <-4> <0> / SSID1 = MIXED CID = AR FLOW = 0.00905 <-4> <0> / SSID1 = MIXED CID = CO2 FLOW = 0.00032 <-4> <0> / SSID1 = MIXED CID = H2O FLOW = 0.031003 <-4> <0> \ \ COMMENTS COMMENTS = ( ";allows easy modification to air temp if used in calc " ";blocks throughout simulation" ) \ ? STREAM MATERIAL "AREFRNC.DUMMY1" ? ; "ENG_MOLE" ; \ SUBSTREAM SSID = MIXED TEMP = 60. <22> <2> PRES = 15. <20> <2> BASIS = "MASS-FRAC" FLOWBASE = MASS TOTFLOW = 1E-006 <-80> <2> TOTAL = 1. <-89> <0> JUNK = 1 \ \ SUBSTREAM SSID = CISOLID TOTAL = 0. <0> <0> \ \ SUBSTREAM SSID = NC TOTAL = 0. <0> <0> \ \ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 1. <-3> <0> \ ? BLOCK SEP "AREFRNC.DUMSEP" ? ; "ENG_MOLE" ; ; ICON1 ; \ PARAM1 FLAG = 0 \ \ PARAM PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = N2 FRACS = 0.5 <0> <0> / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = DUMMY3 SUBSTREAM = MIXED COMPS = AMINE FRACS = 1. <0> <0> / PARAM-STREAM = DUMMY3 SUBSTREAM = CISOLID COMPS = CARBON FRACS = 0. <0> <0> / PARAM-STREAM = DUMMY3 SUBSTREAM = CISOLID COMPS = SULFUR FRACS = 0. <0> <0> / PARAM-STREAM = DUMMY3 SUBSTREAM = CISOLID COMPS = OLIVINE FRACS = 0. <0> <0> / PARAM-STREAM = DUMMY3 SUBSTREAM = NC COMPS = WOOD FRACS = 0. <0> <0> / PARAM-STREAM = DUMMY3 SUBSTREAM = NC COMPS = ASH FRACS = 0. <0> <0> / PARAM-STREAM = DUMMY3 SUBSTREAM = NC COMPS = CHAR FRACS = 0. <0> <0> / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = H2 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = CO / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = N2 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = O2 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = AR / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = CO2 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = H2O / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = H2S / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = SO2 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = NH3 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = NO2 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = CH4 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = C2H6 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = C2H4 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = C2H2 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = C3H8 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "I-C4H10" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "N-C4H10" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "PENTANE+" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = C6H6 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = C10H8 / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = CARBON / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = SULFUR / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = OLIVINE / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "NH4+" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "H3O+" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "NH2COO-" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "OH-" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "HCO3-" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "HS-" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "CO3--" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = "S--" / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = METHANOL / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = ETHANOL / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = PROPANOL / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = NBUTANOL / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = PENTANOL / PARAM-STREAM = DUMMY4 SUBSTREAM = MIXED COMPS = AMINE / PARAM-STREAM = DUMMY4 SUBSTREAM = CISOLID COMPS = CARBON / PARAM-STREAM = DUMMY4 SUBSTREAM = CISOLID COMPS = SULFUR / PARAM-STREAM = DUMMY4 SUBSTREAM = CISOLID COMPS = OLIVINE / PARAM-STREAM = DUMMY4 SUBSTREAM = NC COMPS = WOOD / PARAM-STREAM = DUMMY4 SUBSTREAM = NC COMPS = ASH / PARAM-STREAM = DUMMY4 SUBSTREAM = NC COMPS = CHAR \ \ PROPERTIES OPSETNAME = "RKS-BM" \ ? BLOCK HEATER "AREFRNC.HX100A" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = 0. <20> <2> VFRAC = 1. <0> <0> \ \ PROPERTIES OPSETNAME = "STEAM-TA" \ ? BLOCK HEATER "AREFRNC.HX100B" ? ; "ENG_MOLE" ; ; HEATER ; \ PARAM PRES = 0. <20> <2> VFRAC = 1. <0> <0> \ ? BLOCK PUMP "AREFRNC.MEFF-A" ? ; "ENG_MOLE" ; ; ICON1 ; \ DESCRIPTION DESCRIPTION = "Placeholder for pump and motor efficiencies" \ \ PARAM PRES = 50. <20> <2> EFF = 0.98 <0> <0> DEFF = 0.95 <0> <0> OPT-SPEC = PRES \ \ COMMENTS COMMENTS = ( ";Provides and easy way to change efficiencies " ";throughout simulation to evaluate effect of using " ";different efficiency motors" ) \ ? REPORT "AREFRNC.BLOCK-REPORT" ? ? "DESIGN-SPEC" ADIABAT ? ; "ENG_MOLE" ; \ DESCRIPTION DESCRIPTION = "Varies gasifer temp until gasifer heat loss = 0" \ \ DEFINE FVN = QGAS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A200.QR201" FVN-PHYS-QTY = "ENTHALPY-FLO" \ \ SPEC EXPR1 = "QGAS" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "60" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = "A200.R-201" VARYVARIABLE = TEMP VARYSENTENCE = PARAM \ \ LIMITS LOWER = "1550" UPPER = "2100" \ ? "DESIGN-SPEC" AMREBOIL ? ; "ENG_MOLE" ; \ DEFINE FVN = DUTY FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300AGR.QH300RB" FVN-PHYS-QTY = "ENTHALPY-FLO" \ \ DEFINE FVN = FCO2OU FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300AGR.319" FVN-SUBS = MIXED FVN-COMPONEN = CO2 \ \ DEFINE FVN = AMDEN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300AGR.AM-COLD" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = AMFLOW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300AGR.AM-COLD" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C" "C This block calculates the steam requirement for the" "C Amine systems " "C" "C" "C Duty from GPSA simplified method using Amine flow rate" "C in gpm. Reboiler duty in Btu/hr is 72000 * GPM." "C AMFLOW = Amine flow rate in CFH from ASPEN" "C MUST USE ACTUAL CUFT/HR INSTEAD OF STD VOL" "C" "F ADUTY = 72000.0 * ((AMFLOW/AMDEN) * 7.4805 / 60.0)" "c ratio isn't used anywhere " "F RATIO = ADUTY / FCO2OU" "F QDIFF = ADUTY - DUTY " "C" ) \ \ SPEC EXPR1 = "QDIFF" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "10" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = "A300.A300AGR.350" VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "0" UPPER = "200000" \ ? "DESIGN-SPEC" CO2SPEC ? ; "ENG_MOLE" ; \ DEFINE FVN = YCO2 FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = "A400.470" FVN-SUBS = MIXED FVN-COMPONEN = CO2 OPT-CATEG = STREAM \ \ SPEC EXPR1 = "YCO2" EXPR2 = ".05" \ \ "TOL-SPEC" TOL = ".001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = "A300.A300AGR.S-310" VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 319 VARYID3 = CO2 \ \ LIMITS LOWER = "0.0001" UPPER = "0.9999" STEP-SIZE = 0.05 <0> <0> MAX-STEP-SIZ = 0.1 <0> <0> \ ? "DESIGN-SPEC" COMBCTL1 ? ; "ENG_MOLE" ; \ DESCRIPTION DESCRIPTION = "Design Spec Logic" \ \ DEFINE FVN = O2IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A200.A200CC.208" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = O2OUT FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A200.A200CC.210" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = YO2IN FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = "A200.A200CC.208" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = AIRIN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.A200CC.208" FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = QEX FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A200.A200CC.QR202" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This computes the minimal amount of air required for combustion" "C and the percent excess air" "C" " AIRMIN = (O2IN - O2OUT)/YO2IN" " IF (O2OUT.LE.0.) AIRMIN = AIRMIN * 10." " WRITE(NHSTRY,10) AIRMIN, (AIRIN-AIRMIN)/AIRMIN*100" " 10 FORMAT(1x,""Minimum Air, Percent Excess Air = "",E13.5,1x,F5.1)" ) \ \ SPEC EXPR1 = "AIRIN" EXPR2 = "AIRMIN * 1.2" \ \ "TOL-SPEC" TOL = "1" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = "A200.A200CC.208" VARYSUBS = MIXED VARYVARIABLE = "MOLE-FLOW" \ \ LIMITS LOWER = "1000" UPPER = "100000" \ \ COMMENTS COMMENTS = ( ";The combustion air is varied from 5-20% excess air " ";until the stack temperature of the dryer flue gas " ";reaches 250°F. Check to see if this is above the " ";dew point of the gas (It should be)." ) \ ? "DESIGN-SPEC" COMBCTL2 ? ; "ENG_MOLE" ; \ DEFINE FVN = QEX FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A200.A200CC.QR202" \ \ DEFINE FVN = TRXN FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A200.A200CC.R-202" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM \ \ SPEC EXPR1 = "QEX" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "100" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = "A200.A200CC.R-202" VARYVARIABLE = TEMP VARYSENTENCE = PARAM \ \ LIMITS LOWER = "1750" UPPER = "2100" \ ? "DESIGN-SPEC" CWTEMP ? ; "ENG_MOLE" ; \ DEFINE FVN = FTARG FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.717" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = HTARG FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.717" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-ENTHALP" OPT-CATEG = STREAM \ \ DEFINE FVN = FMEAS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.716" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = HMEAS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.716" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-ENTHALP" OPT-CATEG = STREAM \ \ SPEC EXPR1 = "FMEAS*HMEAS" EXPR2 = "FTARG*HTARG" \ \ "TOL-SPEC" TOL = "2000" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = "A700.709" VARYSUBS = MIXED VARYVARIABLE = TEMP \ \ LIMITS LOWER = "89" UPPER = "92" \ \ COMMENTS COMMENTS = ( ";Manipulates the cooling water tower outlet " ";temperature to force the enthaply of the CWS streams " ";to match." ) \ ? "DESIGN-SPEC" "O2-100" ? ; "ENG_MOLE" ; \ DEFINE FVN = O2IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A100.HV-100.O2" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = O2OUT FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A100.HV-100.PROD-1" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = FEEDMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( " FEED = FEEDMX + FEEDCI + FEEDNC" ) \ \ SPEC EXPR1 = "O2OUT" EXPR2 = ".1" \ \ "TOL-SPEC" TOL = ".05" \ \ VARY VARY-VARTYPE = "MOLE-FLOW" VARYSTREAM = "A100.HV-100.O2" VARYSUBS = MIXED VARYCOMPONEN = O2 \ \ LIMITS LOWER = "0" UPPER = "0.1 * FEED" \ ? "DESIGN-SPEC" "O2-224" ? ; "ENG_MOLE" ; \ DEFINE FVN = O2IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A200.HV-224.O2" FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = O2OUT FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A200.HV-224.PROD-1" FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = FEEDMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.HV-224.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.HV-224.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.HV-224.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( " FEED = FEEDMX + FEEDCI + FEEDNC" ) \ \ SPEC EXPR1 = "O2OUT" EXPR2 = ".1" \ \ "TOL-SPEC" TOL = ".05" \ \ VARY VARY-VARTYPE = "MOLE-FLOW" VARYSTREAM = "A200.HV-224.O2" VARYSUBS = MIXED VARYCOMPONEN = O2 \ \ LIMITS LOWER = "0" UPPER = "0.1 * FEED" \ ? "DESIGN-SPEC" "O2-227" ? ; "ENG_MOLE" ; \ DEFINE FVN = O2IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.HV-327.O2" FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = O2OUT FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.HV-327.PROD-1" FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = FEEDMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.A300FC.HV-327.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.A300FC.HV-327.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.A300FC.HV-327.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( " FEED = FEEDMX + FEEDCI + FEEDNC" ) \ \ SPEC EXPR1 = "O2OUT" EXPR2 = "0.1" \ \ "TOL-SPEC" TOL = "0.05" \ \ VARY VARY-VARTYPE = "MOLE-FLOW" VARYSTREAM = "A300.A300TR.A300FC.HV-327.O2" VARYSUBS = MIXED VARYCOMPONEN = O2 \ \ LIMITS LOWER = "0" UPPER = "10 * FEED" \ ? "DESIGN-SPEC" "O2-475" ? ; "ENG_MOLE" ; \ DEFINE FVN = O2IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A400.HV-475.O2" FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = O2OUT FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A400.HV-475.PROD-1" FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = FEEDMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A400.HV-475.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A400.HV-475.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A400.HV-475.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( " FEED = FEEDMX + FEEDCI + FEEDNC" ) \ \ SPEC EXPR1 = "O2OUT" EXPR2 = "0.1" \ \ "TOL-SPEC" TOL = "0.05" \ \ VARY VARY-VARTYPE = "MOLE-FLOW" VARYSTREAM = "A400.HV-475.O2" VARYSUBS = MIXED VARYCOMPONEN = O2 \ \ LIMITS LOWER = "0" UPPER = "0.1 * FEED" \ ? "DESIGN-SPEC" "O2-590" ? ; "ENG_MOLE" ; \ DEFINE FVN = O2IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.HV-590.O2" FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = O2OUT FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.HV-590.PROD-1" FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = FEEDMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-590.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-590.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-590.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( " FEED = FEEDMX + FEEDCI + FEEDNC" ) \ \ SPEC EXPR1 = "O2OUT" EXPR2 = "0.1" \ \ "TOL-SPEC" TOL = "0.05" \ \ VARY VARY-VARTYPE = "MOLE-FLOW" VARYSTREAM = "A500.HV-590.O2" VARYSUBS = MIXED VARYCOMPONEN = O2 \ \ LIMITS LOWER = "0" UPPER = "0.1 * FEED" \ ? "DESIGN-SPEC" "O2-592" ? ; "ENG_MOLE" ; \ DEFINE FVN = O2IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.HV-592.O2" FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = O2OUT FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.HV-592.PROD-1" FVN-SUBS = MIXED FVN-COMPONEN = O2 \ \ DEFINE FVN = FEEDMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-592.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-592.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FEEDNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-592.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( " FEED = FEEDMX + FEEDCI + FEEDNC" ) \ \ SPEC EXPR1 = "O2OUT" EXPR2 = "0.1" \ \ "TOL-SPEC" TOL = "0.05" \ \ VARY VARY-VARTYPE = "MOLE-FLOW" VARYSTREAM = "A500.HV-592.O2" VARYSUBS = MIXED VARYCOMPONEN = O2 \ \ LIMITS LOWER = "0" UPPER = "9000" \ ? "DESIGN-SPEC" QBALANCE ? ; "ENG_MOLE" ; \ DEFINE FVN = QHOT1 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300Q.QH301" OPT-CATEG = STREAM \ \ DEFINE FVN = QHOT2 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.QH590" \ \ DEFINE FVN = QHOT3 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.QH592" FVN-PHYS-QTY = "ENTHALPY-FLO" \ \ DEFINE FVN = QHOT5 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A600.QH602" FVN-PHYS-QTY = "ENTHALPY-FLO" FVN-UOM = "Btu/hr" OPT-CATEG = STREAM \ \ DEFINE FVN = QHOT6 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300TR.A300FC.QH311" FVN-PHYS-QTY = "ENTHALPY-FLO" OPT-CATEG = STREAM \ \ DEFINE FVN = QHOT7 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A200.A200CC.QH286" OPT-CATEG = STREAM \ \ DEFINE FVN = QHOT8 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A400.A400SGR.QR410" \ \ DEFINE FVN = QHOT9 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A400.QH412" FVN-PHYS-QTY = "ENTHALPY-FLO" FVN-UOM = "Btu/hr" \ \ DEFINE FVN = QHOT10 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A400.QH411" OPT-CATEG = STREAM \ \ DEFINE FVN = QSTM1 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A600.A600BF.QH406407" OPT-CATEG = STREAM \ \ DEFINE FVN = QSTM2 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A600.A600BL.QH605" OPT-CATEG = STREAM \ \ DEFINE FVN = QSTM3 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A600.A600BL.QH201402" OPT-CATEG = STREAM \ \ DEFINE FVN = QSTM4 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A600.QH607" OPT-CATEG = STREAM \ \ DEFINE FVN = QCOLD1 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300S.QH304" OPT-CATEG = STREAM \ \ DEFINE FVN = QCOLD2 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A200.A200CC.QH209" OPT-CATEG = STREAM \ \ DEFINE FVN = QCOLD3 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A400.A400SGR.QH410" \ \ DEFINE FVN = QCOLD4 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.QH503" OPT-CATEG = STREAM \ \ DEFINE FVN = QCOLD5 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300TR.A300FC.QH330" OPT-CATEG = STREAM \ \ DEFINE FVN = QCOLD6 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A400.QH416" FVN-PHYS-QTY = "ENTHALPY-FLO" FVN-UOM = "Btu/hr" \ \ DEFINE FVN = QCOLD7 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A600.A600WTR.QH620" OPT-CATEG = STREAM \ \ DEFINE FVN = QCOLD8 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A600.A600ST.QH602C" OPT-CATEG = STREAM \ \ DEFINE FVN = QCOLD9 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A600.A600ST.QH602B" OPT-CATEG = STREAM \ \ DEFINE FVN = QCLD10 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.QH503B" OPT-CATEG = STREAM \ \ DEFINE FVN = QCLD12 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300TR.QH315" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This design spec closes the heat balance for the plant. Streams" "C are labeled as:" "C" "C QHOTi = Process stream which needs to be cooled" "C QCOLDi = Process stream which needs to be heated" "C QSTMi = Steam system stream which needs to be heated" "C" "F QHOT = QHOT1 + QHOT2 + QHOT3" "F 1 + QHOT5 + QHOT6 + QHOT7 + QHOT8 " "F 2 + QHOT9 + QHOT10 " "F QCOLD = QCOLD1 + QCOLD2 + QCOLD3 + QCOLD4 + QCOLD5 + " "F 1 QCOLD6 + QCOLD7 + QCOLD8 + QCOLD9 + QCLD10 +" "F 2 QCLD12" "C Streams QCLD12 - 14 are zeroed out for now" "C" "F QSTM = QSTM1 + QSTM2 + QSTM3 + QSTM4" "C" "F QDIFF = QHOT + QCOLD + QSTM" ) \ \ SPEC EXPR1 = "QDIFF" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "50" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = "A600.644" VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "10000" UPPER = "1000000" \ ? "DESIGN-SPEC" QM104B ? ; "ENG_MOLE" ; \ DEFINE FVN = DUTY FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A100.A100DRYR.QM104B" OPT-CATEG = STREAM \ \ DEFINE FVN = T332 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.A300FC.332" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ SPEC EXPR1 = "DUTY" EXPR2 = "75" \ \ "TOL-SPEC" TOL = "50" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = "A300.A300TR.A300FC.H-311" VARYVARIABLE = TEMP VARYSENTENCE = PARAM \ \ LIMITS LOWER = "250" UPPER = "T332" STEP-SIZE = 0.01 <0> <0> MAX-STEP-SIZ = 0.1 <0> <0> \ ? "DESIGN-SPEC" QUENCHFL ? ; "ENG_MOLE" ; \ DESCRIPTION DESCRIPTION = "Design Spec Logic" \ \ DEFINE FVN = TCOOL FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300Q.310" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ SPEC EXPR1 = "TCOOL" EXPR2 = "110" \ \ "TOL-SPEC" TOL = ".1" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = "A300.A300Q.MULT300B" VARYVARIABLE = FACTOR VARYSENTENCE = PARAM \ \ LIMITS LOWER = "1" UPPER = "10000" \ \ COMMENTS COMMENTS = ( ";Adjusts the water circulation rate until the exit temperature from " ";the cooling water heat exchanger is 110F." ) \ ? "DESIGN-SPEC" R301BTEM ? ; "ENG_MOLE" ; \ DESCRIPTION DESCRIPTION = "R301B outlet temperature spec" \ \ DEFINE FVN = TEMP FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.A300FC.332" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ SPEC EXPR1 = "TEMP" EXPR2 = "1775.5" \ \ "TOL-SPEC" TOL = ".5" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = "A200.SP225" VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = 225F \ \ LIMITS LOWER = "1" UPPER = "120000" STEP-SIZE = 0.001 <0> <0> MAX-STEP-SIZ = 0.1 <0> <0> \ \ COMMENTS COMMENTS = ( ";varies 225F (dirty syngas) to fuel combustor to meet " ";temperature spec." ) \ ? "DESIGN-SPEC" REBOIL2 ? ; "ENG_MOLE" ; \ DEFINE FVN = STM507 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.QXCS" FVN-PHYS-QTY = "ENTHALPY-FLO" \ \ FORTRAN FORTRAN-EXEC = ( "C" "C This block calculates the reboiler steam useage for " "C seperation of the alcohols based on spreadsheet from PNNL" "c" "c DUTY = 164.44 * 1000000 * mixed alcohol prod /101607" ) \ \ SPEC EXPR1 = "STM507" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "10" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = "A500.534" VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "10" UPPER = "7500000" \ ? "DESIGN-SPEC" SRHEAT ? ; "ENG_MOLE" ; \ DEFINE FVN = QEX FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300S.QH304EX" OPT-CATEG = STREAM \ \ SPEC EXPR1 = "QEX" EXPR2 = "0" \ \ "TOL-SPEC" TOL = "100" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = "A300.A300S.394" VARYSUBS = MIXED VARYVARIABLE = "MASS-FLOW" \ \ LIMITS LOWER = "0" UPPER = "100000" \ ? "DESIGN-SPEC" STACKT ? ; "ENG_MOLE" ; \ DEFINE FVN = STACKT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A100.112" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = DWPT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A100.A100DWPT.114" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ SPEC EXPR1 = "STACKT" EXPR2 = "DWPT + 62.0" \ \ "TOL-SPEC" TOL = "1" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = "A100.A100DRYR.M-104B" VARYVARIABLE = TEMP VARYSENTENCE = PARAM \ \ LIMITS LOWER = "200" UPPER = "500" \ ? "DESIGN-SPEC" SULFAD ? ; "ENG_MOLE" ; \ DEFINE FVN = SULFUR FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = "A400.A400SGR.485" FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ SPEC EXPR1 = "SULFUR" EXPR2 = ".00005" \ \ "TOL-SPEC" TOL = ".00001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = "A300.A300AGR.S-310" VARYVARIABLE = "FLOW/FRAC" VARYSENTENCE = "FLOW/FRAC" VARYID1 = MIXED VARYID2 = 319 VARYID3 = H2S \ \ LIMITS LOWER = "1E-6" UPPER = "1" \ ? "DESIGN-SPEC" TAIRO ? ; "ENG_MOLE" ; \ DEFINE FVN = FH2OI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.719" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = HH2OI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.719" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-ENTHALP" OPT-CATEG = STREAM \ \ DEFINE FVN = FAIRI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.703" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = HAIRI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.703" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-ENTHALP" OPT-CATEG = STREAM \ \ DEFINE FVN = FAIRO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.705" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = HAIRO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.705" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-ENTHALP" OPT-CATEG = STREAM \ \ DEFINE FVN = FDRIFT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.704" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = HDRIFT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.704" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-ENTHALP" OPT-CATEG = STREAM \ \ DEFINE FVN = HFAN FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A700.WM701" OPT-CATEG = STREAM \ \ DEFINE FVN = FH2OO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.709" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = HH2OO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.709" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-ENTHALP" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This closes the enthalpy balance around the cooling water tower" "C" "F HIN = FH2OI*HH2OI + FAIRI*HAIRI + 2545*HFAN" "F HOUT = FAIRO*HAIRO + FDRIFT*HDRIFT + FH2OO*HH2OO" ) \ \ SPEC EXPR1 = "HOUT" EXPR2 = "HIN" \ \ "TOL-SPEC" TOL = "2000" \ \ VARY VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = "A700.705" VARYSUBS = MIXED VARYVARIABLE = TEMP \ \ LIMITS LOWER = "80" UPPER = "150" \ ? "EO-CONV-OPTI" ? \ DMO-PARAMS MODE = DEFAULT \ \ DMO-PARAMS MODE = SIMULATION \ \ DMO-PARAMS MODE = "PARAMETER-ESTIMATION" \ \ DMO-PARAMS MODE = RECONCILIATION \ \ DMO-PARAMS MODE = OPTIMIZATION \ \ LSSQP-PARAMS MODE-L = DEFAULT \ \ LSSQP-PARAMS MODE-L = SIMULATION \ \ LSSQP-PARAMS MODE-L = "PARAMETER-ESTIMATION" \ \ LSSQP-PARAMS MODE-L = RECONCILIATION \ \ LSSQP-PARAMS MODE-L = OPTIMIZATION \ \ NSOLVE-PARAM NSOLVE-MODE = DEFAULT \ \ NSOLVE-PARAM NSOLVE-MODE = SIMULATION \ \ NSOLVE-PARAM NSOLVE-MODE = "PARAMETER-ESTIMATION" \ ? CALCULATOR ALCOMB2 ? ; "ENG_MOLE" ; \ DEFINE FVN = C1MAL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.A504.HV-MXALC.100" FVN-SUBS = MIXED FVN-COMPONEN = METHANOL OPT-CATEG = STREAM \ \ DEFINE FVN = C2MAL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.A504.HV-MXALC.100" FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = C3MAL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.A504.HV-MXALC.100" FVN-SUBS = MIXED FVN-COMPONEN = PROPANOL \ \ DEFINE FVN = C4MAL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.A504.HV-MXALC.100" FVN-SUBS = MIXED FVN-COMPONEN = NBUTANOL OPT-CATEG = STREAM \ \ DEFINE FVN = C5MAL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.A504.HV-MXALC.100" FVN-SUBS = MIXED FVN-COMPONEN = PENTANOL OPT-CATEG = STREAM \ \ DEFINE FVN = FO2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A500.A504.HV-MXALC.8" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C Now see how much oxygen is needed to combust the remaining higher" "C alcohols" "C" "C C3H8O + 4.5O2 --> 4H2O + 3CO2" "C C4H10O + 6O2 --> 5H2O + 4CO2" "C C5H12O + 7.5O2 --> 6H2O + 5CO2" "C" "C Combust the entire mixed alcohol stream" "C Include methanol" "C CH4O + O2 --> 2H2O + 1.5CO2" "C" "F FO2 = C1MAL + 3*C2MAL +4.5*C3MAL + 6*C4MAL + 7.5*C5MAL" "F FO2 = 1.05 * FO2" ) \ \ "READ-VARS" READ-VAR = ( C1MAL C2MAL C3MAL C4MAL C5MAL ) \ \ "WRITE-VARS" WRITE-VAR = ( FO2 ) \ ? CALCULATOR AMFLOW ? ; "ENG_MOLE" ; \ DEFINE FVN = WTOTAQ FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300AGR.AM-COLD" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = XAMWTP FVN-VARTYPE = "MASS-FRAC" FVN-STREAM = "A300.A300AGR.AM-COLD" FVN-SUBS = MIXED FVN-COMPONEN = AMINE \ \ DEFINE FVN = AMMW FVN-VARTYPE = "UNARY-PARAM" FVN-VARIABLE = MW FVN-ID1 = AMINE FVN-ID2 = 1 \ \ DEFINE FVN = FCO2OU FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300AGR.319" FVN-SUBS = MIXED FVN-COMPONEN = CO2 \ \ DEFINE FVN = FH2SOU FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300AGR.319" FVN-SUBS = MIXED FVN-COMPONEN = H2S \ \ FORTRAN FORTRAN-EXEC = ( "C" "C Method for calculating Amine System duties from GPSA 21-12." "C Basic Simplified Design Calculations" "C Assumes that all of the CO2 is removed essentially, so" "C need to calculate for less than total removal using MolAG/Molamine" "C" "C GPM = Amine circulation rate in gallons/minute" "C CF = Constant for different Amine types" "C QMSCFD = Sour gas to be processed in MMscfd" "C y = Acid gas concentration in sour gas, mole%" "C x = Amine concentration in liquid solution, wt%" "C TPG = Temperature of process acid gas, F" "C PPG = Pressure of process acid gas, psia" "C" "C CF Amine mol AG/mol amine assumed" "C 41 MEA 0.33" "C 45 DEA (conv. loading) 0.5" "C 32 DEA (high loading) 0.7" "C 55.8 DGA (normally 50-60 wt%) 0.39" "C" "C Calculate the amine circulation rate in gpm. MEA is used." "C Calculate Q in scfd from acfh from ASPEN" "C" "C Calculate for actual amount of acid gas removed" "C" "F FAGRM = FCO2OU + FH2SOU" "F FAMINE = (FAGRM / 0.33)" "C" "C Convert molar flow of Amine into mass flow of aqueous amine at" "C specified wt% amine as indicated by AM-COLD stream" "C" "F WAMINE = FAMINE * AMMW" "F WTOTAQ = WAMINE / XAMWTP" "C" ) \ \ "READ-VARS" READ-VAR = ( XAMWTP AMMW FCO2OU FH2SOU ) \ \ "WRITE-VARS" WRITE-VAR = ( WTOTAQ ) \ \ EXECUTE BLOCK-TYPE = CONVERGENCE \ ? CALCULATOR ASHCOND ? ; "ENG_MOLE" ; \ DEFINE FVN = FCISOL FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.A200CC.217" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.A200CC.217" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = WATER FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.A200CC.218" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This computes the amount of water needed to condition the ash" "C so that it is not too dusty to handle." "C" "C Assume final water content is 10 wt%" "C" "F XH2O = 0.1" "C" "F WATER = XH2O*(FCISOL+FNC)/(1-XH2O)" ) \ \ "READ-VARS" READ-VAR = ( FNC FCISOL ) \ \ "WRITE-VARS" WRITE-VAR = ( WATER ) \ ? CALCULATOR "C-MSWAT1" ? ; "ENG_MOLE" ; \ DEFINE FVN = X FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A503MS.SEP" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = "MS-WATER" FVN-ID3 = H2O OPT-CATEG = BLOCK \ \ DEFINE FVN = WATER FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A500.A503MS.WET" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = TOTAL FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.A503MS.WET" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C SET THE SPECIFICATIONS FOR THE RESIDual WATER CONTENT OF THE" "C DRIED inlet STREAM." "F SPEC = 0.005" "F" "C CALCULATE THE SPLIT AMOUNT SO THAT THIS COMPOSITON CAN" "C BE ACHIEVED." "F" "F X = (TOTAL - WATER) * SPEC / (1. - SPEC)" "F X = 1. - X / WATER" "F IF (X.GT.1.) THEN" "F X = 1." "F ELSEIF (X.LT.0.) THEN" "F X = 0." "F END IF " ) \ \ "READ-VARS" READ-VAR = ( WATER TOTAL ) \ \ "WRITE-VARS" WRITE-VAR = ( X ) \ ? CALCULATOR CO2VENT ? ; "ENG_MOLE" ; \ DEFINE FVN = F484 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300S.SP-384" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 384REC OPT-CATEG = BLOCK \ \ DEFINE FVN = F484TR FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A300.A300TR.384REC" FVN-SUBS = MIXED FVN-COMPONEN = CO2 OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C sets the recycle flow in SP-384. this flow goes to Tar" "C reformer via a design spec and is not physically connected" "C may go to the gasifier also." "C" "F F484 = F484TR" ) \ \ "READ-VARS" READ-VAR = ( F484TR ) \ \ "WRITE-VARS" WRITE-VAR = ( F484 ) \ \ EXECUTE WHEN = LAST \ ? CALCULATOR CWAIRI ? ; "ENG_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F REAL LBYG" ) \ \ DEFINE FVN = CIRC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.719" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = DRYAIR FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.700" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = HUMID FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.701" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This computes the inlet air flow to the tower" "C" "C assume L/G = 1" "C and H = 0.0199 lb H2O per lb dry air for wet bulb temp of 80 F" "C" "F LBYG = 1.0" "F DRYAIR = CIRC / LBYG" "F H = 0.0199" "F HUMID = H * DRYAIR" ) \ \ "READ-VARS" READ-VAR = ( CIRC ) \ \ "WRITE-VARS" WRITE-VAR = ( DRYAIR HUMID ) \ ? CALCULATOR CWBAL ? ; "ENG_MOLE" ; \ DEFINE FVN = TH2OI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.719" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = TH2OO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.709" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = FH2OI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.719" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = STMBLW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 600 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = CIRC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.717" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = HUMID FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.701" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FH2OO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.709" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = BLWDWN FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700A" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 713 OPT-CATEG = BLOCK \ \ DEFINE FVN = CWCHEM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 711 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = MAKEUP FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 710 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = DRIFT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.704" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = RHOAIR FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.703" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" OPT-CATEG = STREAM \ \ DEFINE FVN = FAIRI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.703" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FANHP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A700.WM701" OPT-CATEG = STREAM \ \ DEFINE FVN = AIN2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.703" FVN-SUBS = MIXED FVN-COMPONEN = N2 OPT-CATEG = STREAM \ \ DEFINE FVN = AIO2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.703" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = AIAR FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.703" FVN-SUBS = MIXED FVN-COMPONEN = AR OPT-CATEG = STREAM \ \ DEFINE FVN = AICO2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.703" FVN-SUBS = MIXED FVN-COMPONEN = CO2 OPT-CATEG = STREAM \ \ DEFINE FVN = AIH2O FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.703" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = AON2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.705" FVN-SUBS = MIXED FVN-COMPONEN = N2 OPT-CATEG = STREAM \ \ DEFINE FVN = AOO2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.705" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = AOAR FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.705" FVN-SUBS = MIXED FVN-COMPONEN = AR OPT-CATEG = STREAM \ \ DEFINE FVN = AOCO2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.705" FVN-SUBS = MIXED FVN-COMPONEN = CO2 OPT-CATEG = STREAM \ \ DEFINE FVN = AOH2O FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.705" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This completes the material and energy balances for the" "C cooling water system." "C" "C Evaporation loss equation is from eq. 12-10 of ""Perry's Chemical" "C Engineers' Handbook"", 7th ed." "C Drift is a fraction of the inlet water flow." "C Blowdown is based on cycles of concentration." "C Chemical addition rate is set as a fraction of circulation" "C Make-up is set by water balance for the cooling water system" "C Outlet flow of water from tower (FH2OO) is set by water balance" "C around tower" "C " "F EVAP = 0.00085 * FH2OI * (TH2OI - TH2OO)" "F DRIFT = 0.2/100 * FH2OI" "F CYCLES = 5.0" "F BLWDWN = EVAP / (CYCLES-1)" "F FRACT = 2.0e-7" "F CWCHEM = FRACT * CIRC" "F MAKEUP = EVAP + DRIFT + BLWDWN - STMBLW - CWCHEM" "F FH2OO = FH2OI - EVAP - DRIFT" "C" "C Use eq. 12-13 of Perry's (cited above) to set fan horsepower..." "C assume 2"" of head and 70% efficiency" "C Modified fan hp calcs to match Perry's 12-13. Eff = 1.0 and " "C lowered HEAD to 1.5 i.w.c. This gives results closer to several" "C manufacturer and literature sources for power requirements." "C" "F HEAD = 1.5" "F EFF = 1.0" "F FANHP = (FAIRI/RHOAIR/60) * HEAD * 62.4/33000/12/EFF" "C" "C Now update the outlet air composition" "C" "F AON2 = AIN2" "F AOO2 = AIO2" "F AOAR = AIAR" "F AOCO2 = AICO2" "F AOH2O = AIH2O + EVAP" ) \ \ "READ-VARS" READ-VAR = ( TH2OI TH2OO FH2OI STMBLW CIRC HUMID FAIRI AIH2O RHOAIR AIN2 AIO2 AIAR AICO2 ) \ \ "WRITE-VARS" WRITE-VAR = ( FH2OO BLWDWN CWCHEM MAKEUP DRIFT FANHP AON2 AOO2 AOAR AOCO2 AOH2O ) \ ? CALCULATOR CWDUTY ? ; "ENG_MOLE" ; \ DEFINE FVN = HCWS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.707" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-ENTHALP" OPT-CATEG = STREAM \ \ DEFINE FVN = HCWR FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.708" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-ENTHALP" OPT-CATEG = STREAM \ \ DEFINE FVN = CIRC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.717" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = POWCON FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A600.A600ST.QCH601" OPT-CATEG = STREAM \ \ DEFINE FVN = QUENCH FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300Q.QCM301" OPT-CATEG = STREAM \ \ DEFINE FVN = QQUENC FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700C" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = QCM301CT OPT-CATEG = BLOCK \ \ DEFINE FVN = FQUENC FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 722 OPT-CATEG = BLOCK \ \ DEFINE FVN = AFCOOL FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300Q.QCH303" OPT-CATEG = STREAM \ \ DEFINE FVN = QAFCOO FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700C" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = QCH303CT OPT-CATEG = BLOCK \ \ DEFINE FVN = FAFCOO FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 724 OPT-CATEG = BLOCK \ \ DEFINE FVN = STMBLW FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A600.QCH603" FVN-PHYS-QTY = "ENTHALPY-FLO" OPT-CATEG = STREAM \ \ DEFINE FVN = QSTMBL FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700C" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = QCH603CT OPT-CATEG = BLOCK \ \ DEFINE FVN = FSTMBL FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 728 OPT-CATEG = BLOCK \ \ DEFINE FVN = SULFUR FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 324 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = QSULFU FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700C" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = QCH305CT OPT-CATEG = BLOCK \ \ DEFINE FVN = FSULFU FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 730 OPT-CATEG = BLOCK \ \ DEFINE FVN = ASH FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A200.A200CC.QCM201" OPT-CATEG = STREAM \ \ DEFINE FVN = QASH FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700C" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = QCM201CT OPT-CATEG = BLOCK \ \ DEFINE FVN = FASH FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 732 OPT-CATEG = BLOCK \ \ DEFINE FVN = DUTY FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A700.QCTOTAL" FVN-PHYS-QTY = "ENTHALPY-FLO" OPT-CATEG = STREAM \ \ DEFINE FVN = COND2 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A400.QCH414" FVN-PHYS-QTY = "ENTHALPY-FLO" \ \ DEFINE FVN = FCOND2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 736 \ \ DEFINE FVN = QCOND2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700C" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = QCH414CT \ \ DEFINE FVN = PROD1 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.QCH591" OPT-CATEG = STREAM \ \ DEFINE FVN = QPROD1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700C" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = QCH591CT OPT-CATEG = BLOCK \ \ DEFINE FVN = FPROD1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 738 OPT-CATEG = BLOCK \ \ DEFINE FVN = PROD2 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.QCH593" OPT-CATEG = STREAM \ \ DEFINE FVN = QPROD2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700C" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = QCH593CT OPT-CATEG = BLOCK \ \ DEFINE FVN = FPROD2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A700.SP700B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 740 OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the cooling water circulation through each exchanger" "C serviced by cooling water and also sets the overall cooling" "C water circulation rate" "C " "C Estimate duty for sulfur removal unit" "C" "F SULFU = SULFUR*24/2240 * 40032.0/1.7" "C" "C" "C Use estimate from GPSA pg. 21-12 - adjust values which were for" "C lower CO2 concentrations than these cases" "C Lean amine cooling duty(Btu/hr)= 25000 * GPM amine circ which is" "C 1/3 of the reboiler duty. 2/3 is cooling fan in W300 block." "C CHANGE 11/22/06 - AADEN, ALL COOLING FOR AMINE NOW BY AIR" "C" "C AMINE = 25000.0 * (AMFLOW * 7.4805 / 60.0)" "C" "C Only lean solvent cooled with CW. Acid Gas Condenser uses cooling" "C fans - see W300 block." "C" "C Now sum and set total circulation" "C" "F DUTY = POWCON + QUENCH + AFCOOL + STMBLW + SULFU + ASH" "F 1 + COND2 " "F CIRC = DUTY / (HCWR - HCWS)" "C" "C now set the individual flows and duties...set for all but the" "C power condenser" "C" "F QQUENC = QUENCH / DUTY" "F FQUENC = QUENCH / (HCWR - HCWS)" "C" "F QAFCOO = AFCOOL / DUTY" "F FAFCOO = AFCOOL / (HCWR - HCWS)" "C" "F QSTMBL = STMBLW / DUTY" "F FSTMBL = STMBLW / (HCWR - HCWS)" "C" "F QSULFU = SULFU / DUTY" "F FSULFU = SULFU / (HCWR - HCWS)" "C" "F QASH = ASH / DUTY" "F FASH = ASH / (HCWR - HCWS)" "C" "C" "F QCOND2 = COND2 / DUTY" "F FCOND2 = COND2 / (HCWR - HCWS)" "C" "F QPROD1 = PROD1 / DUTY" "F FPROD1 = PROD1 / (HCWR - HCWS)" "C" "F QPROD2 = PROD2 / DUTY" "F FPROD2 = PROD2 / (HCWR - HCWS)" ) \ \ "READ-VARS" READ-VAR = ( POWCON QUENCH AFCOOL STMBLW SULFUR HCWS HCWR ASH COND2 PROD1 PROD2 ) \ \ "WRITE-VARS" WRITE-VAR = ( CIRC QQUENC FQUENC QAFCOO FAFCOO QSTMBL FSTMBL QSULFU FSULFU DUTY QASH FASH FCOND2 QCOND2 FPROD1 QPROD1 QPROD2 FPROD2 ) \ ? CALCULATOR DESULF ? ; "ENG_MOLE" ; \ DEFINE FVN = H2SIN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300S.321" FVN-SUBS = MIXED FVN-COMPONEN = H2S OPT-CATEG = STREAM \ \ DEFINE FVN = XO2 FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = 322 FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = AIRFLW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 322 FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the air flow used for reoxidizing the LO-CAT " "C caltalyst solution" "C" "F O2REQ = 0.5*H2SIN" "F AIRFLW = 1.1*O2REQ/XO2" ) \ \ "READ-VARS" READ-VAR = ( XO2 H2SIN ) \ \ "WRITE-VARS" WRITE-VAR = ( AIRFLW ) \ ? CALCULATOR DRYER ? ; "ENG_MOLE" ; \ DEFINE FVN = BDWOOD FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A100.A100DRYR.102" FVN-SUBS = NC FVN-COMPONEN = WOOD OPT-CATEG = STREAM \ \ DEFINE FVN = H2OIN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A100.A100DRYR.102" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = VF FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A100.A100DRYR.M-104A" FVN-VARIABLE = VFRAC FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the amount of water removed in the dryer." "C" "C The variable WLEVEL is the total water content, in wt%, of the dried" "C wood." "C" "F WLEVEL = 5.0" "C" "C Now compute the water content of the feed and" "C the required vapor fraction for the dryer" "C" "F XH2OIN = H2OIN / (BDWOOD + H2OIN)" "F VF = ( XH2OIN/(1-XH2OIN)- WLEVEL/(100-WLEVEL) ) / " "F 1 ( XH2OIN/(1-XH2OIN) )" ) \ \ "READ-VARS" READ-VAR = ( BDWOOD H2OIN ) \ \ "WRITE-VARS" WRITE-VAR = ( VF ) \ ? CALCULATOR EFFICIEN ? ; "ENG_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F REAL LHVW" "F REAL LHVH2" "F REAL LHVEFF" "F REAL LHVNG" ) \ \ DEFINE FVN = HHVEFF FVN-VARTYPE = PARAMETER FVN-PARAMNO = 2 \ \ DEFINE FVN = LHVEFF FVN-VARTYPE = PARAMETER FVN-PARAMNO = 3 \ \ DEFINE FVN = GASHHV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 4 \ \ DEFINE FVN = GASLHV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 5 \ \ DEFINE FVN = C2HHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.HV-592.QGROSS" \ \ DEFINE FVN = C2LHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.HV-592.QNET" \ \ DEFINE FVN = MAHHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.HV-590.QGROSS" \ \ DEFINE FVN = MALHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.HV-590.QNET" \ \ DEFINE FVN = INHHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A100.HV-100.QGROSS" \ \ DEFINE FVN = INLHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A100.HV-100.QNET" \ \ DEFINE FVN = NGHHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300TR.A300FC.HV-327.QGROSS" FVN-PHYS-QTY = "ENTHALPY-FLO" \ \ DEFINE FVN = NGLHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300TR.A300FC.HV-327.QNET" FVN-PHYS-QTY = "ENTHALPY-FLO" \ \ DEFINE FVN = SGHHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A200.HV-224.QGROSS" \ \ DEFINE FVN = SGLHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A200.HV-224.QNET" \ \ DEFINE FVN = ALCHHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A400.HV-475.QGROSS" \ \ DEFINE FVN = ALCLHV FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A400.HV-475.QNET" \ \ DEFINE FVN = WNET FVN-VARTYPE = "WORK-POWER" FVN-STREAM = WNET \ \ FORTRAN FORTRAN-EXEC = ( "C This computes the overall plant and gasifier efficiencies." "C Modified 10/19/2006 (Jechura) to use final alcohol products &" "C heat flows from the heating value blocks." "C" "C Specify electricity basis" "C" " EFFHHV = 0.38" " EFFLHV = 0.36" "C" " WRITE(NHSTRY,10) WNET, EFFHHV*100, EFFLHV*100" " 10 FORMAT(//," " 1 1x,""Plant Efficiency Calculations"",//," " 2 1x,""Net Power Required, hp: "", E13.5,/," " 3 1x,""Assumed Power Plant Efficiency, % HHV : "", F5.1, /," " 4 1x,""Assumed Power Plant Efficiency, % LHV : "", F5.1,/)" "C" "C Thermal equivalents for electricity" "C" " EHHV = WNET * 2545 / EFFHHV" " ELHV = WNET * 2545 / EFFLHV" " " "C" "C Overall plant efficiencies based upon final products" "C" " IF( WNET .GE. 0.0 )THEN" " HHVEFF = (C2HHV + MAHHV)/(INHHV + EHHV + NGHHV) * 100." " LHVEFF = (C2LHV + MALHV)/(INLHV + ELHV + NGLHV) * 100." " ELSE" " HHVEFF = (C2HHV + MAHHV - EHHV)/(INHHV + NGHHV) * 100." " LHVEFF = (C2LHV + MALHV - EHHV)/(INLHV + NGLHV) * 100. " " END IF" "C" " WRITE(NHSTRY,70) HHVEFF, LHVEFF" " 70 FORMAT("" Overall Plant Efficiency (Based on products)"",/" " 1 "" HHV %: "",F10.5,/" " 2 "" LHV %: "",F10.5,/)" "C" "C Gasifier efficiencies" "C" " GASHHV = SGHHV/INHHV * 100." " GASLHV = SGLHV/INLHV * 100." " WRITE(NHSTRY,75) GASHHV, GASLHV " " 75 FORMAT("" Gasifier Efficiency"",/" " 1 "" HHV %: "",F10.5,/" " 2 "" LHV %: "",F10.5,/)" ) \ \ "READ-VARS" READ-VAR = ( C2HHV C2LHV MAHHV MALHV INHHV INLHV NGHHV NGLHV SGHHV SGLHV WNET ) \ \ "WRITE-VARS" WRITE-VAR = ( HHVEFF LHVEFF GASHHV GASLHV ) \ ? CALCULATOR GASISTM ? ; "ENG_MOLE" ; \ DEFINE FVN = WOOD FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 105 FVN-SUBS = NC FVN-COMPONEN = WOOD OPT-CATEG = STREAM \ \ DEFINE FVN = XH2O FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 105 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = PROXANAL FVN-ELEM = 1 OPT-CATEG = STREAM \ \ DEFINE FVN = GASSTM FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 200 FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = GASST2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A200.200" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the steam feed rate to the gasifier" "C" "C for now...set steam rate at 0.398*Bone Dry Wood rate" "C " "F GASSTM = 0.398*WOOD*(1.0 -XH2O/100.0)" "F GASST2 = GASSTM" ) \ \ "READ-VARS" READ-VAR = ( WOOD XH2O ) \ \ "WRITE-VARS" WRITE-VAR = ( GASSTM GASST2 ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = "A200.MX200A" \ ? CALCULATOR GSTEMP ? ; "ENG_MOLE" ; \ DEFINE FVN = TGAS FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A200.R-201" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM \ \ DEFINE FVN = TBATYD FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A200.R-201" FVN-VARIABLE = "REAL-VAR" FVN-SENTENCE = REAL FVN-ELEM = 1 \ \ FORTRAN FORTRAN-EXEC = ( "C *********************************************************************" "C This block sets the temperature that is sent to the BATYD " "C subroutine equal to the temperature of the gasifier. It allows " "C the temperature sent to the BATYD subroutine to be varied." "C *********************************************************************" "C" "C" "F TBATYD = TGAS" ) \ \ "READ-VARS" READ-VAR = ( TGAS ) \ \ "WRITE-VARS" WRITE-VAR = ( TBATYD ) \ \ EXECUTE WHEN = BEFORE BLOCK-TYPE = BLOCK BLK-ID = "A200.R-201" \ ? CALCULATOR H2SSPLIT ? ; "ENG_MOLE" ; \ DEFINE FVN = FGAS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300S.320" FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FH2S FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300S.320" FVN-SUBS = MIXED FVN-COMPONEN = H2S OPT-CATEG = STREAM \ \ DEFINE FVN = SPLIT FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300S.M-304" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 321 FVN-ID3 = H2S OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This block sets the H2S concentration in the outlet of the" "C main H2S scrubber" "C" "C H2SLEV is set to make the process outlet H2S level at 10 ppmv" "C" "F H2SLEV = 0.00001" "C" "C Now compute how much H2S remains in the process stream" "C" "F H2SOUT = H2SLEV*(FGAS-FH2S)/(1-H2SLEV)" "C" "C and then set the split fraction" "C" "F SPLIT = (FH2S-H2SOUT) / FH2S" ) \ \ "READ-VARS" READ-VAR = ( FGAS FH2S ) \ \ "WRITE-VARS" WRITE-VAR = ( SPLIT ) \ ? CALCULATOR "HV-100" ? ; "ENG_MOLE" ; \ DEFINE FVN = QGROSS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A100.HV-100.QGROSS" \ \ DEFINE FVN = QNET FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A100.HV-100.QNET" \ \ DEFINE FVN = FLOWMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = ASH FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = NC FVN-COMPONEN = ASH OPT-CATEG = STREAM \ \ DEFINE FVN = INHHV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 6 \ \ DEFINE FVN = INLHV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 7 \ \ FORTRAN FORTRAN-EXEC = ( "C CALCULATE HEATING VALUES IN UNITS OF BTU/LB" "C" " FLOW = FLOWMX + FLOWCI + FLOWNC" " INHHV = QGROSS / FLOW" " HVHIAF = QGROSS / (FLOW - ASH)" " INLHV = QNET / FLOW" " HVLOAF = QNET / (FLOW - ASH)" " " " WRITE (*,10) INHHV, INLHV" "C WRITE (*,20) HVHIAF, HVLOAF" " " " WRITE (NHSTRY,10) INHHV, INLHV" "C WRITE (NHSTRY,20) HVHIAF, HVLOAF" " " " 10 FORMAT (/' HEATING VALUES FOR STREAM 100 (DRY BASIS):'/" " 1 ' HHV (BTU/LB) = ', F10.4/" " 2 ' LHV (BTU/LB) = ', F10.4/)" " 20 FORMAT ( ' HEATING VALUES FOR STREAM 100 (DRY & ASH FREE):'/" " 1 ' HHV (BTU/LB) = ', F10.4/" " 2 ' LHV (BTU/LB) = ', F10.4/)" ) \ \ "READ-VARS" READ-VAR = ( QGROSS QNET FLOWMX FLOWCI FLOWNC ASH ) \ \ "WRITE-VARS" WRITE-VAR = ( INHHV INLHV ) \ ? CALCULATOR "HV-224" ? ; "ENG_MOLE" ; \ DEFINE FVN = QGROSS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A200.HV-224.QGROSS" \ \ DEFINE FVN = QNET FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A200.HV-224.QNET" \ \ DEFINE FVN = FLOWMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.HV-224.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.HV-224.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.HV-224.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = ASH FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A200.HV-224.BASIS" FVN-SUBS = NC FVN-COMPONEN = ASH \ \ FORTRAN FORTRAN-EXEC = ( "C CALCULATE HEATING VALUES IN UNITS OF BTU/LB" "C" " FLOW = FLOWMX + FLOWCI + FLOWNC" " HVHI = QGROSS / FLOW" " HVHIAF = QGROSS / (FLOW - ASH)" " HVLO = QNET / FLOW" " HVLOAF = QNET / (FLOW - ASH)" " " " WRITE (*,10) HVHI, HVLO" "C WRITE (*,20) HVHIAF, HVLOAF" " " " WRITE (NHSTRY,10) HVHI, HVLO" "C WRITE (NHSTRY,20) HVHIAF, HVLOAF" " " " 10 FORMAT (/' HEATING VALUES FOR STREAM 224 (DRY BASIS):'/" " 1 ' HHV (BTU/LB) = ', F10.4/" " 2 ' LHV (BTU/LB) = ', F10.4/)" " 20 FORMAT ( ' HEATING VALUES FOR STREAM 224 (DRY & ASH FREE):'/" " 1 ' HHV (BTU/LB) = ', F10.4/" " 2 ' LHV (BTU/LB) = ', F10.4/)" ) \ \ "READ-VARS" READ-VAR = ( QGROSS QNET FLOWMX FLOWCI FLOWNC ) \ ? CALCULATOR "HV-227" ? ; "ENG_MOLE" ; \ DEFINE FVN = QGROSS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300TR.A300FC.HV-327.QGROSS" FVN-PHYS-QTY = "ENTHALPY-FLO" \ \ DEFINE FVN = QNET FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300TR.A300FC.HV-327.QNET" FVN-PHYS-QTY = "ENTHALPY-FLO" \ \ DEFINE FVN = FLOWMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.A300FC.HV-327.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.A300FC.HV-327.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.A300FC.HV-327.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C CALCULATE HEATING VALUES IN UNITS OF BTU/LB" "C" " FLOW = FLOWMX + FLOWCI + FLOWNC" " HVHI = QGROSS / FLOW" " HVLO = QNET / FLOW" " " " WRITE (*,10) HVHI, HVLO " " WRITE (NHSTRY,10) HVHI, HVLO" " " " 10 FORMAT (/' HEATING VALUES FOR STREAM 227 (WET BASIS):'/" " 1 ' HHV (BTU/LB) = ', F10.4/" " 2 ' LHV (BTU/LB) = ', F10.4/)" ) \ \ "READ-VARS" READ-VAR = ( QGROSS QNET FLOWMX FLOWCI FLOWNC ) \ ? CALCULATOR "HV-475" ? ; "ENG_MOLE" ; \ DEFINE FVN = QGROSS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A400.HV-475.QGROSS" \ \ DEFINE FVN = QNET FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A400.HV-475.QNET" \ \ DEFINE FVN = FLOWMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A400.HV-475.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A400.HV-475.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A400.HV-475.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = ASH FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A400.HV-475.BASIS" FVN-SUBS = NC FVN-COMPONEN = ASH \ \ FORTRAN FORTRAN-EXEC = ( "C CALCULATE HEATING VALUES IN UNITS OF BTU/LB" "C" " FLOW = FLOWMX + FLOWCI + FLOWNC" " HVHI = QGROSS / FLOW" " HVHIAF = QGROSS / (FLOW - ASH)" " HVLO = QNET / FLOW" " HVLOAF = QNET / (FLOW - ASH)" " " " WRITE (*,10) HVHI, HVLO" "C WRITE (*,20) HVHIAF, HVLOAF" " " " WRITE (NHSTRY,10) HVHI, HVLO" "C WRITE (NHSTRY,20) HVHIAF, HVLOAF" " " " 10 FORMAT (/' HEATING VALUES FOR STREAM 475 (DRY BASIS):'/" " 1 ' HHV (BTU/LB) = ', F10.4/" " 2 ' LHV (BTU/LB) = ', F10.4/)" " 20 FORMAT ( ' HEATING VALUES FOR STREAM 475 (DRY & ASH FREE):'/" " 1 ' HHV (BTU/LB) = ', F10.4/" " 2 ' LHV (BTU/LB) = ', F10.4/)" ) \ \ "READ-VARS" READ-VAR = ( QGROSS QNET FLOWMX FLOWCI FLOWNC ASH ) \ ? CALCULATOR "HV-590" ? ; "ENG_MOLE" ; \ DEFINE FVN = QGROSS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.HV-590.QGROSS" \ \ DEFINE FVN = QNET FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.HV-590.QNET" \ \ DEFINE FVN = FLOWMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-590.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-590.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-590.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C CALCULATE HEATING VALUES IN UNITS OF BTU/LB" "C" " FLOW = FLOWMX + FLOWCI + FLOWNC" " HVHI = QGROSS / FLOW" " HVLO = QNET / FLOW" " " " WRITE (*,10) HVHI, HVLO " " WRITE (NHSTRY,10) HVHI, HVLO" " " " 10 FORMAT (/' HEATING VALUES FOR STREAM 590 (WET BASIS):'/" " 1 ' HHV (BTU/LB) = ', F10.4/" " 2 ' LHV (BTU/LB) = ', F10.4/)" ) \ \ "READ-VARS" READ-VAR = ( QGROSS QNET FLOWMX FLOWCI FLOWNC ) \ ? CALCULATOR "HV-592" ? ; "ENG_MOLE" ; \ DEFINE FVN = QGROSS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.HV-592.QGROSS" \ \ DEFINE FVN = QNET FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.HV-592.QNET" \ \ DEFINE FVN = FLOWMX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-592.BASIS" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-592.BASIS" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = FLOWNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.HV-592.BASIS" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C CALCULATE HEATING VALUES IN UNITS OF BTU/LB" "C" " FLOW = FLOWMX + FLOWCI + FLOWNC" " HVHI = QGROSS / FLOW" " HVLO = QNET / FLOW" " " " WRITE (*,10) HVHI, HVLO " " WRITE (NHSTRY,10) HVHI, HVLO" " " " 10 FORMAT (/' HEATING VALUES FOR STREAM 592 (WET BASIS):'/" " 1 ' HHV (BTU/LB) = ', F10.4/" " 2 ' LHV (BTU/LB) = ', F10.4/)" ) \ \ "READ-VARS" READ-VAR = ( QGROSS QNET FLOWMX FLOWCI FLOWNC ) \ ? CALCULATOR MGORATE ? ; "ENG_MOLE" ; \ DEFINE FVN = WOOD FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD OPT-CATEG = STREAM \ \ DEFINE FVN = XH2O FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = PROXANAL FVN-ELEM = 1 OPT-CATEG = STREAM \ \ DEFINE FVN = XASH FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 1 OPT-CATEG = STREAM \ \ DEFINE FVN = FMGO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 220 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the MgO flowrate. The MgO is to titrate the potassium in" "C the feed ash. Without MgO addition, the potassium will form the" "C glass K2SiO4 with the silica in the system. K2SiO4 has a low" "C melting point (~500 C) and its formation will cause the bed media" "C to become sticky, agglomerate, and eventually defluidize. Adding" "C MgO makes the potassium form a high melting (~1300 C) ternary" "C eutectic with the silica, thus sequestering it. Potassium carry over" "C in the gasifier/combuster overheads is also significantly reduced." "C" "C Assume the ash content of the feed contains 0.2 wt% potassium...this" "C the correct order of magnitude for wood feedstocks, but would be" "C much higher for ag residues like corn stover." "C" "F XK = 0.002" "C" "C Compute the number of moles of potassium in the feed..." "C" "F FK = WOOD * (1 - XH2O/100) * XASH/100 * XK / 39.0983" "C" "C Set the MgO flow rate at 2X minimum" "C" "F FMGO = 2 * FK * (24.3050 + 15.9994 )" ) \ \ "READ-VARS" READ-VAR = ( XASH ) \ \ "WRITE-VARS" WRITE-VAR = ( FMGO ) \ ? CALCULATOR P03OFAIR ? ; "ENG_MOLE" ; \ DEFINE FVN = FH2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = H2 OPT-CATEG = STREAM \ \ DEFINE FVN = FCO FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = CO OPT-CATEG = STREAM \ \ DEFINE FVN = FCH4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = CH4 OPT-CATEG = STREAM \ \ DEFINE FVN = FC2H6 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = C2H6 OPT-CATEG = STREAM \ \ DEFINE FVN = FC2H4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = C2H4 OPT-CATEG = STREAM \ \ DEFINE FVN = FC2H2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = C2H2 OPT-CATEG = STREAM \ \ DEFINE FVN = AIRFLO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.329B" FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FO2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = FC3H8 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = C3H8 OPT-CATEG = STREAM \ \ DEFINE FVN = FIC4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = "I-C4H10" OPT-CATEG = STREAM \ \ DEFINE FVN = FNC4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = "N-C4H10" OPT-CATEG = STREAM \ \ DEFINE FVN = FC5 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = "PENTANE+" OPT-CATEG = STREAM \ \ DEFINE FVN = FH2S FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = H2S OPT-CATEG = STREAM \ \ DEFINE FVN = XO2 FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = "A300.A300TR.329B" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = FCAL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = METHANOL \ \ DEFINE FVN = FC2AL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = ETHANOL \ \ DEFINE FVN = FC3AL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = PROPANOL \ \ DEFINE FVN = FC4AL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = NBUTANOL \ \ DEFINE FVN = FC5AL FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.A300FC.328" FVN-SUBS = MIXED FVN-COMPONEN = PENTANOL \ \ FORTRAN FORTRAN-EXEC = ( "C ********************************************************************" "C This block calculates the amount of air required for the syngas fuel" "C combustor. First, it determines the amount of oxygen (in mole flow)" "C required to completely combust the products in the feed stream." "C The components that can combust are the hydrogen, carbon monoxide, " "C methane, ethane, ethylene and acetylene, propane, iC4, nC4,C5,H2S" "C and alcohols according to the following" "C reactions:" "C H2 + 0.5O2 --> H2O" "C CO + 0.5O2 --> CO2" "C CH4 + 2O2 --> 2H2O + CO2" "C C2H6 + 3.5O2 --> 3H2O + 2CO2" "C C2H4 + 3O2 --> 2H2O + 2CO2" "C C2H2 + 2.5O2 --> H2O + 2CO2" "C C3H8 + 5O2 --> 4H2O + 3CO2" "C iC4H10 + 6.5O2 --> 5H2O + 4CO2" "C nC4H10 + 6.5O2 --> 5H2O + 4CO2" "C C5H12 + 8O2 --> 6H2O + 5CO2" "C H2S +1.5O2 --> H2O + SO2" "C CH4O + 1.5O2 --> 2H2O + CO2" "C C2H6O + 3O2 --> 3H2O + 2CO2" "C C3H8O + 4.5O2 --> 4H2O + 3CO2" "C C4H10O + 6O2 --> 5H2O + 4CO2" "C C5H12O + 7.5O2 --> 6H2O + 5CO2" "C" "C moleflowO2 = 0.5*moleflowH2 + 0.5*moleflowCO + 2*moleflowCH4" "C 3.5*moleflowC2H6 + 3*moleflowC2H4 +" "C 2.5*moleflowC2H2 +" "C 5*C3H8 + 6.5*(iC4+nC4) + 8*C5 + 1.5*H2S" "C 5*C3H8 + 6.5*(iC4+nC4) + 8*C5 + 1.5*H2S +" "C 1.5*CH4O + 3*C2H6O + 4.5*C3H8O + 6*C4H10O +" "C 7.5*C5H12O" "C be subtracted from the total O2 required for combustion. The " "C remaining O2 must be supplied in the PSA Offgas combustion air" "C stream." "C *********************************************************************" "C" "C First line of code calculates amount of O2 required for combustion." "F TOTO2 = 0.5*FH2+0.5*FCO+2.0*FCH4+3.5*FC2H5+3.0*FC2H4+2.5*FC2H2" "F 1 + 5*FC3H8 + 6.5*(FIC4+FNC4) + 8*FC5 + 1.5*FH2S + 1.5*FCAL" "F 2 + 3*FC2AL + 4.5*FC3AL + 6*FC4AL + 7.5*FC5AL" "C" "C This line of code calculates amount of O2 required from air supply." "F TOTO2A = TOTO2 - FO2" "C " "C We want to have 20% more air than necessary for combustion. The next" "C line of code determines this amount." "F TOTO2B = 1.2*TOTO2A" "C" "C The total air flowrate is then determined by using the air " "C composition in " "F AIRFLO = TOTO2B/XO2" "F WRITE(NHSTRY,*) FH2, FCO, FCH4, FC2H5, FC2H4, FC2H2, FC3H8, " "F 1 FIC4, FNC4, FC5, FH2S, FO2, XO2, AIRFLO" ) \ \ "READ-VARS" READ-VAR = ( FO2 FH2 FCO FCH4 FC2H6 FC2H2 FC2H4 FC3H8 FIC4 FNC4 FC5 FH2S XO2 FCAL FC2AL FC3AL FC4AL FC5AL ) \ \ "WRITE-VARS" WRITE-VAR = ( AIRFLO ) \ ? CALCULATOR REFSTM ? ; "ENG_MOLE" ; \ DEFINE FVN = RSTMFR FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.393" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = CO FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = CO OPT-CATEG = STREAM \ \ DEFINE FVN = CH4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = CH4 OPT-CATEG = STREAM \ \ DEFINE FVN = C2H6 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C2H6 OPT-CATEG = STREAM \ \ DEFINE FVN = C2H4 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C2H4 OPT-CATEG = STREAM \ \ DEFINE FVN = C2H2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C2H2 OPT-CATEG = STREAM \ \ DEFINE FVN = TAR FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C10H8 OPT-CATEG = STREAM \ \ DEFINE FVN = EXIST FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.225A" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = C6H6 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C6H6 OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C ********************************************************************" "C This section calculates the amount of steam needed for reforming" "C the steam/carbon ratio is set to 3.0 mol H2O/mol C (which is a" "C typical value for a steam reformer). The calculation determines the " "C amount of carbon in the reformer gas feed stream and subtracts off " "C the amount of water vapor already in the reformer feed" "C ********************************************************************" "C" "C This is the lbmole/hr of steam needed for the reformer" "C" "F RSTMFR = 1.74*(CH4+2*(C2H6+C2H4+C2H2)+ 6*C6H6 +10*TAR)-EXIST" "C" ) \ \ "READ-VARS" READ-VAR = ( CO CH4 C2H6 C2H4 C2H2 TAR EXIST C6H6 ) \ \ "WRITE-VARS" WRITE-VAR = ( RSTMFR ) \ \ EXECUTE BLOCK-TYPE = BLOCK \ ? CALCULATOR "RX-100" ? ; "ENG_MOLE" ; \ DECLARE FORTRAN-DEC = ( "F REAL MWC" "F REAL MWH" "F REAL MWN" "F REAL MWS" "F REAL MWO" ) \ \ DEFINE FVN = WOOD FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = NC FVN-COMPONEN = WOOD OPT-CATEG = STREAM \ \ DEFINE FVN = XC FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 2 OPT-CATEG = STREAM \ \ DEFINE FVN = XH FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 3 OPT-CATEG = STREAM \ \ DEFINE FVN = XN FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 4 OPT-CATEG = STREAM \ \ DEFINE FVN = XS FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 6 OPT-CATEG = STREAM \ \ DEFINE FVN = XO FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 7 OPT-CATEG = STREAM \ \ DEFINE FVN = TOTO2 FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A100.HV-100.O2" FVN-SUBS = MIXED FVN-COMPONEN = O2 OPT-CATEG = STREAM \ \ DEFINE FVN = CWOOD FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A100.HV-100.BURN" FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 1 FVN-ID2 = WOOD FVN-ID3 = NC OPT-CATEG = BLOCK \ \ DEFINE FVN = CO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A100.HV-100.BURN" FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 1 FVN-ID2 = O2 FVN-ID3 = MIXED OPT-CATEG = BLOCK \ \ DEFINE FVN = CCO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A100.HV-100.BURN" FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 1 FVN-ID2 = CO2 FVN-ID3 = MIXED OPT-CATEG = BLOCK \ \ DEFINE FVN = CH2O FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A100.HV-100.BURN" FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 1 FVN-ID2 = H2O FVN-ID3 = MIXED OPT-CATEG = BLOCK \ \ DEFINE FVN = CSO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A100.HV-100.BURN" FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 1 FVN-ID2 = SO2 FVN-ID3 = MIXED OPT-CATEG = BLOCK \ \ DEFINE FVN = CNO2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A100.HV-100.BURN" FVN-VARIABLE = COEF FVN-SENTENCE = STOIC FVN-ID1 = 1 FVN-ID2 = NO2 FVN-ID3 = MIXED OPT-CATEG = BLOCK \ \ DEFINE FVN = XA FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = "A100.HV-100.BASIS" FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 1 \ \ DEFINE FVN = CONV FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A100.HV-100.BURN" FVN-VARIABLE = CONV FVN-SENTENCE = CONV FVN-ID1 = 1 \ \ FORTRAN FORTRAN-EXEC = ( "C This computes how much oxygen is needed to combust the feed...part" "C of plant efficiency calcs." "C" "C Set molecular weights for the elements" "C" " MWC = 12.011" " MWH = 1.00794" " MWN = 14.00674" " MWS = 32.066" " MWO = 15.9994" "C" "C Modify the coefficients for the combustion reaction based on" "C the ultimate analysis. First figure out relative molar ratios" "C wrt C for H, N, S, and O. For notation, assume wood molar" "C formuala is: CHaNbScOd:" "C" " A = (XH/MWH) / (XC/MWC)" " B = (XN/MWN) / (XC/MWC)" " C = (XS/MWS) / (XC/MWC)" " D = (XO/MWO) / (XC/MWC)" "C" "C now set the reaction coeffients according to:" "C" "C CHaNbScOd + (1+a/4+c+b) O2 -> CO2 + a/2 H2O + c SO2 + b NO2" "C" "C Aspen assumes molecular weight of NC components is unity...so " "C we also need to adjust the coefficient for wood" "C" " CWOOD = -( MWC + A*MWH + B*MWN + C*MWS + D*MWO )" " CO2 = -( 1 + A/4 + C + B - D/2)" " CCO2 = 1" " CH2O = A/2" " CSO2 = C" " CNO2 = B" "C " "C Take into account the ash content by lowering the conversion " " CONV = 1 - XA/100. " "C" "C Set the amount of oxygen needed" "C" "C TOTO2 = WOOD / CWOOD * CO2" ) \ \ "READ-VARS" READ-VAR = ( WOOD XC XN XS XO XH ) \ \ "WRITE-VARS" WRITE-VAR = ( CWOOD CO2 CCO2 CH2O CSO2 CNO2 ) \ ? CALCULATOR SANDMAKE ? ; "ENG_MOLE" ; \ DEFINE FVN = GASLOS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A200.224" FVN-SUBS = CISOLID FVN-COMPONEN = OLIVINE OPT-CATEG = STREAM \ \ DEFINE FVN = CMBLOS FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A200.A200CC.216" FVN-SUBS = CISOLID FVN-COMPONEN = OLIVINE OPT-CATEG = STREAM \ \ DEFINE FVN = MGO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A200.220" FVN-SUBS = CISOLID FVN-COMPONEN = OLIVINE OPT-CATEG = STREAM \ \ DEFINE FVN = MAKEUP FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 221 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This computes the amount of make-up bed material (sand or olivine)" "C" "F MAKEUP = GASLOS + CMBLOS - MGO" ) \ \ "READ-VARS" READ-VAR = ( CMBLOS MGO ) \ \ "WRITE-VARS" WRITE-VAR = ( MAKEUP ) \ ? CALCULATOR SETFEED ? ; "ENG_MOLE" ; \ DEFINE FVN = BDWOOD FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD \ \ DEFINE FVN = XH2O FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = PROXANAL FVN-ELEM = 1 OPT-CATEG = STREAM \ \ DEFINE FVN = WATFLO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 100 FVN-SUBS = MIXED FVN-COMPONEN = H2O \ \ FORTRAN FORTRAN-EXEC = ( "C ********************************************************************" "C This block sets the feed rate to the plant" "C ********************************************************************" "C" "C Bone Dry Wood rate = 2000 tonne (dry)/ day," "C Total Water content at 50 wt%" "C" " RATE = 2000" " XTARG = 0.50" "C" "C Convert to lb/hr (bone dry), make sure the wood proximate" "C analysis is set to 0, and calculate the total water in the feed" "C This is the as-received feed stream, and includes both" "C free water and moisture in the wood" " BDWOOD = RATE / 24 * 2.20462 * 1000" " XH2O = 0" " WATFLO = XTARG * BDWOOD / ( 1 - XTARG )" "C " "C Specify the Ultimate & Proximate analyses. " "C Poplar composition per Craig, K.R., Mann, M.K., ""Cost and " "C Performance Analysis of Biomass-Bases Integrated Gasification " "C Combined-Cycle (BIGCC) Power Systems"", National Renewable " "C Energy Laboratory, NREL/TP-430-21657, October, 1996. " "c Unnormalized values. " " ASH = 0.92" " CAR = 50.88 " " HYD = 6.04 " " NIT = 0.17 " " SUL = 0.09 " " OXY = 41.9 " " PFC = 15.29 " " PVM = 83.84 " " PASH = 0.87 " "C " "C Normalize the Ultimate Analysis " " AFREE = 100. - ASH " " TOTAL = CAR + HYD + NIT + SUL + OXY " " FACTOR = AFREE/TOTAL " " CAR = CAR * FACTOR " " HYD = HYD * FACTOR " " NIT = NIT * FACTOR " " SUL = SUL * FACTOR " " OXY = OXY * FACTOR " "C " "C Normalize the Proximate Analysis. Set ash content to that in " "C the ultimate analysis. " "C PASH = ASH " "C AFREE = 100. - PASH " "C TOTAL = PFC + PVM " "C FACTOR = AFREE/TOTAL " "C PFC = PFC * FACTOR " "C PVM = PVM * FACTOR " "C " "C Modified sulfur analysis as follows: " "C Evenly distributed sulfur between sulfate and organic, " "C with no sulfur being classified as pyritic " " SSULFT = 0.5 * SUL " " SORGNC = 0.5 * SUL " "C " " WRITE (NHSTRY,10) " " 1 ASH, CAR, HYD, NIT, SUL, OXY, PFC, PVM, PASH, SSULFT, " " 2 SORGNC, XTARG*100. " " WRITE (*,10) " " 1 ASH, CAR, HYD, NIT, SUL, OXY, PFC, PVM, PASH, SSULFT, " " 2 SORGNC, XTARG*100. " "C " " 10 FORMAT (/' Ultimate & Proximate analyses for stream 100:'/ " " 1 ' Ash = ', F10.4/ " " 2 ' Carbon = ', F10.4/ " " 3 ' Hydrogen = ', F10.4/ " " 4 ' Nitrogen = ', F10.4/ " " 5 ' Sulfur = ', F10.4/ " " 6 ' Oxygen = ', F10.4/ " " 7 ' Fixed Carbon = ', F10.4/ " " 8 ' Volatile Matter = ', F10.4/ " " 9 ' Prox Ash = ', F10.4/ " " 1 ' Sulfate = ', F10.4/ " " 2 ' Organic Sulfur = ', F10.4/ " " 3 ' Moisture (wt%) = ', F10.4/ ) " ) \ \ "WRITE-VARS" WRITE-VAR = ( WATFLO BDWOOD XH2O ) \ \ EXECUTE WHEN = FIRST BLOCK-TYPE = BLOCK BLK-ID = "A100.A100DRYR.M-104A" \ ? CALCULATOR SETPINCH ? ; "ENG_MOLE" ; \ DEFINE FVN = TH301A FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.H-301A" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = TH410A FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A400.A400SGR.H-410A" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = TH416A FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A400.H-416A" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = TH315A FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.H315A" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = TH315B FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.H315B" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = TH315C FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.H315C" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = TH315D FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.H315D" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = TH605A FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A600.A600BL.H-605A" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = TH607A FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A600.H-607A" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This routine sets the upper and lower pinch temperatures for" "C streams that either cross or approach the pinch" "C" "F TUPPER = 570." "F TLOWER = 527.354291" "C" "C set all of the hot streams to the upper temperature" "C" "F TH301A = TUPPER" "C" "C set all of the cold streams to the lower temperature" "C" "F TH410A = TLOWER" "F TH416A = TLOWER" "F TH315A = TLOWER" "F TH315B = TLOWER" "F TH315C = TLOWER" "F TH315D = TLOWER" "F TH605A = TLOWER" "F TH607A = TLOWER" ) \ \ "WRITE-VARS" WRITE-VAR = ( TH301A TH410A TH416A TH315A TH315B TH315C TH315D TH605A TH607A ) \ ? CALCULATOR SLUDGE ? ; "ENG_MOLE" ; \ DEFINE FVN = FCI FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300Q.302" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300Q.302" FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FH2O FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.T-301" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = MIXED FVN-ID2 = 334 FVN-ID3 = H2O OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the water content of the sludge from the quench system" "C" "C Assume 50 wt% water in sludge" "C" "F XH2O = 0.5" "C" "F FH2O = XH2O * (FCI + FNC) / (1 - XH2O)" ) \ \ "READ-VARS" READ-VAR = ( FCI FNC ) \ \ "WRITE-VARS" WRITE-VAR = ( FH2O ) \ ? CALCULATOR STMDEM ? ; "ENG_MOLE" ; \ DESCRIPTION DESCRIPTION = "SP600B" \ \ DEFINE FVN = GASSTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 200 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = AMISTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300AGR.350" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = DISSTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.534" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = SPL612 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A600.A600ST.SP600B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 612 OPT-CATEG = BLOCK \ \ DEFINE FVN = SPL652 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A600.A600ST.SP600B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 652 OPT-CATEG = BLOCK \ \ DEFINE FVN = SPL350 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A600.A600ST.SP600B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 350 OPT-CATEG = BLOCK \ \ DEFINE FVN = SPL393 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A600.A600ST.SP600B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 393 OPT-CATEG = BLOCK \ \ DEFINE FVN = TRSTM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.393" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = SPL394 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A600.A600ST.SP600B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = 394 OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sums the LP steam use and then updates the splitter in" "C the steam cycle" "F SPL612 = GASSTM" "F SPL350 = AMISTM" "F SPL652 = DISSTM" "F SPL393 = TRSTM" "F SPL394 = SRSTM" ) \ \ "READ-VARS" READ-VAR = ( GASSTM AMISTM DISSTM TRSTM ) \ \ "WRITE-VARS" WRITE-VAR = ( SPL612 SPL652 SPL350 SPL393 SPL394 ) \ \ EXECUTE BLOCK-TYPE = CONVERGENCE BLK-ID = QBALANCE \ \ COMMENTS COMMENTS = ( ";CALCULATOR BLOCK TO SPLIT LOW PRESSURE" ";STEAM BETWEEN VARIOUS USES:" ";STREAM 612 GOES TO GASIFIER ALTHOUGH NOT " ";PHYSICALLY" ";CONNECTED IN THE MODEL," ";STREAM 650 GOES TO AMINE REBOILER FOR CO2 REMOVAL" ";STREAM 652 GOES DISTILLATION REBOILERS" ";STREAM 613 IS EXCESS STEAM" ) \ ? CALCULATOR STMMAKE ? ; "ENG_MOLE" ; \ DEFINE FVN = BLWDWN FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A600.604" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = STMLP FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A600.A600ST.612" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = CIRC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A600.644" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = RECYCL FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A600.A600WTR.622" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = BFWCHM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 635 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = H2OMAK FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 618 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = STMLP2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A600.A600ST.393" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This set the make-up water to the steam system" "C and also sets the BFW Chemicals rate" "C" "C First set BFW Chemicals as a small factor of circulation" "C the factor of 7E-6 is the same as that used for the Etoh" "C design report June 2002" "C" "F FACT = 7E-06" "F BFWCHM = FACT * CIRC" "C" "C Compute make-up by mass balance" "C " "F H2OMAK = STMLP + STMLP2 + BLWDWN - RECYCL - BFWCHM" ) \ \ "READ-VARS" READ-VAR = ( BLWDWN STMLP CIRC RECYCL STMLP2 ) \ \ "WRITE-VARS" WRITE-VAR = ( H2OMAK BFWCHM ) \ \ EXECUTE WHEN = SEQUENCE BLOCK-TYPE = CALCULATOR \ ? CALCULATOR TARCAT ? ; "ENG_MOLE" ; \ DEFINE FVN = GASIN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.224" FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FIN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.326" FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FOUT FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.R-303B" FVN-VARIABLE = "FLOW/FRAC" FVN-SENTENCE = "FLOW/FRAC" FVN-ID1 = CISOLID FVN-ID2 = 329 FVN-ID3 = OLIVINE OPT-CATEG = BLOCK \ \ DEFINE FVN = CO2REC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300TR.386" FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the tar cracker catalyst make-up rate and the tar" "C cracker catalyst purge rate" "C" "C Assume a space velocity of 2000 (1/hr), 0.01% purge per day and a" "C catalyst bulk density of 64 lb/ft3" "C" "F SV = 2000" "F FACT = 0.0001" "F BULK = 64.0" "C" "C Convert lbmol to SCF..." "C" "F CFACT = (459.67 + 60) * 10.73 / 14.696" "C" "C and now just do it" "C" "F FIN = (GASIN + CO2REC) * CFACT / SV * BULK * (FACT / 24)" "F FOUT = FIN" ) \ \ "WRITE-VARS" WRITE-VAR = ( FOUT ) \ ? CALCULATOR TARCRACK ? ; "ENG_MOLE" ; \ DEFINE FVN = CH4IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = CH4 OPT-CATEG = STREAM \ \ DEFINE FVN = C2H6IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C2H6 OPT-CATEG = STREAM \ \ DEFINE FVN = C2H4IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C2H4 OPT-CATEG = STREAM \ \ DEFINE FVN = C2H2IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C2H2 OPT-CATEG = STREAM \ \ DEFINE FVN = C6H6IN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C6H6 OPT-CATEG = STREAM \ \ DEFINE FVN = TARIN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = C10H8 OPT-CATEG = STREAM \ \ DEFINE FVN = AMONIN FVN-VARTYPE = "MOLE-FLOW" FVN-STREAM = "A300.A300TR.325A" FVN-SUBS = MIXED FVN-COMPONEN = NH3 OPT-CATEG = STREAM \ \ DEFINE FVN = CH4EX FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.R-303A" FVN-VARIABLE = "EXT-SPEC" FVN-SENTENCE = "EXTENT-SPEC" FVN-ID1 = 2 OPT-CATEG = BLOCK \ \ DEFINE FVN = C2H6EX FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.R-303A" FVN-VARIABLE = "EXT-SPEC" FVN-SENTENCE = "EXTENT-SPEC" FVN-ID1 = 3 OPT-CATEG = BLOCK \ \ DEFINE FVN = C2H4EX FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.R-303A" FVN-VARIABLE = "EXT-SPEC" FVN-SENTENCE = "EXTENT-SPEC" FVN-ID1 = 4 OPT-CATEG = BLOCK \ \ DEFINE FVN = C2H2EX FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.R-303A" FVN-VARIABLE = "EXT-SPEC" FVN-SENTENCE = "EXTENT-SPEC" FVN-ID1 = 5 OPT-CATEG = BLOCK \ \ DEFINE FVN = C6H6EX FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.R-303A" FVN-VARIABLE = "EXT-SPEC" FVN-SENTENCE = "EXTENT-SPEC" FVN-ID1 = 6 OPT-CATEG = BLOCK \ \ DEFINE FVN = TAREX FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.R-303A" FVN-VARIABLE = "EXT-SPEC" FVN-SENTENCE = "EXTENT-SPEC" FVN-ID1 = 7 OPT-CATEG = BLOCK \ \ DEFINE FVN = AMONEX FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.R-303A" FVN-VARIABLE = "EXT-SPEC" FVN-SENTENCE = "EXTENT-SPEC" FVN-ID1 = 8 OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the conversions in the tar cracker." "F CH4EX = 0.80 * CH4IN" "F C2H6EX = 0.99 * C2H6IN" "F C2H4EX = 0.90 * C2H4IN" "F C2H2EX = 0.90 * C2H2IN" "F C6H6EX = 0.99 * C6H6IN" "F TAREX = 0.999 * TARIN" "F AMONEX = 0.90 * AMONIN" ) \ \ "READ-VARS" READ-VAR = ( TARIN CH4IN C2H6IN C2H4IN C2H2IN C6H6IN AMONIN ) \ \ "WRITE-VARS" WRITE-VAR = ( CH4EX C2H6EX C2H4EX C2H2EX C6H6EX TAREX AMONEX ) \ ? CALCULATOR TARCRKT ? ; "ENG_MOLE" ; \ DEFINE FVN = TIN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.225" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = TOUT FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300TR.R-303A" FVN-VARIABLE = TEMP FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the tar cracker operating temperature to be isothermal" "C" "F TOUT = TIN" ) \ \ "READ-VARS" READ-VAR = ( TIN ) \ \ "WRITE-VARS" WRITE-VAR = ( TOUT ) \ ? CALCULATOR TDRIFT ? ; "ENG_MOLE" ; \ DEFINE FVN = TAIRO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.705" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = FAIRO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.705" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = WAIRO FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A700.705" FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = TDRIFT FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A700.704" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This sets the temperature of the drift equal to the wet bulb" "C temperature of the air leaving the cooling tower" "C" "C Compute Psat for water at the exit air temperature" "C using eq. 9.8 of Walas, S.M., ""Chemical" "C Process Equipment: Selection and Design"",Butterworth-Heinemann," "C 1990...convert to psi." "C" "C Rest of the equations are from Table 7.1 or Eq.7.26 of" "C Treybal, R.E., ""Mass Transfer Operations"", McGraw-Hill, 1980." "C Assume operation at atmospheric pressure." "C" "C Compute the amount of water in the outlet air, and set heat" "C of vaporatization for water in Btu/lb:" "C" "F YP = WAIRO / ( FAIRO - WAIRO )" "F HVAP = 1075.8" "C" "C Make a guess of Twet...use dry bulb temperature as the initial guess" "C" "F TWET1 = TAIRO" "F PSAT = 14.696*EXP(11.9176-7173.9/(TWET1+389.5))" "F YPW = 0.622*PSAT/(14.696-PSAT)" "F F1 = YP - ( YPW - (TAIRO-TWET1)*0.227/HVAP )" "C" "C Make a second guess" "C" "F TWET2 = TWET1 - 5" "F PSAT = 14.696*EXP(11.9176-7173.9/(TWET2+389.5))" "F YPW = 0.622*PSAT/(14.696-PSAT)" "F F2 = YP - ( YPW - (TAIRO-TWET2)*0.227/HVAP )" "C" "C now use secant method to find the correct wet bulb temperature" "C" "F DO 10 I = 1, 30" "C" "F TWET3 = TWET1 - F1*(TWET2-TWET1)/(F2-F1)" "F PSAT = 14.696*EXP(11.9176-7173.9/(TWET3+389.5))" "F YPW = 0.622*PSAT/(14.696-PSAT)" "F F3 = YP - ( YPW - (TAIRO-TWET3)*0.227/HVAP )" "C" "F IF( ABS(F3) .LT. 1E-06 )THEN" "F TDRIFT = TWET3" "F GO TO 20" "F END IF" "C" "F TWET1 = TWET2" "F F1 = F2" "F TWET2 = TWET3" "F F2 = F3" "C" "F 10 CONTINUE" "C" "F WRITE(NHSTRY,15)" "F 15 FORMAT(1X,""WARNING: Wet Bulb Temp not found..."",/" "F 1 1X,""Setting drift temperature to dry bulb temp"")" "F TDRIFT = TAIRO" "C" "F 20 CONTINUE" ) \ \ "READ-VARS" READ-VAR = ( TAIRO FAIRO WAIRO ) \ \ "WRITE-VARS" WRITE-VAR = ( TDRIFT ) \ \ EXECUTE BLOCK-TYPE = CALCULATOR \ ? CALCULATOR VELGASI ? ; "ENG_MOLE" ; \ DEFINE FVN = MOLFLO FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.202" FVN-SUBS = MIXED FVN-VARIABLE = "MOLE-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = T FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.202" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = P FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A200.202" FVN-SUBS = MIXED FVN-VARIABLE = PRES OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C Calculate the superficial velocity ft/s in the gasifier based on " "C mole floW and reactor diameter specified in feet" "C" "F FT3SEC = MOLFLO/3600.*359.*(T/459.)*(14.7/P)" "F WRITE (NHSTRY,*) 'Gasifier Flow:', FT3SEC" ) \ \ "READ-VARS" READ-VAR = ( MOLFLO T P ) \ ? CALCULATOR W100 ? ; "ENG_MOLE" ; \ DEFINE FVN = W100 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W100" OPT-CATEG = STREAM \ \ DEFINE FVN = WOOD FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD OPT-CATEG = STREAM \ \ DEFINE FVN = WATER FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = PROXANAL FVN-ELEM = 1 OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This sums the power requirements for feed preparation" "C" "C Feed handling is not well defined yet...ratio power requirements" "C from 1999 bioethanol design report (i.e. Wooley, R., Ruth, M.," "C Sheehan, J., Ibsen, K., Majdeski, H., Galvez, A., ""Lignocellulosic" "C Biomass to Ethnaol Process Design and Economics Utilizing" "C Co-Current Dilute Acid Prehydrolysis and Enzymatic Hydrolysis" "C Current and Futuristic Scenarios"", NREL TP-580-26157, July 1, 1999." "C This report showed 723.18 kW (motor) required for 2000 metric ton" "C (dry) per day of feed." "C" "F WEFEED = WOOD*(1-WATER/100)*24/2.20462/1000 * 723.18*1.341/2000" "C" "C Assume motive power for the dryer is 25 Hp" "C" "F WEDRY = 25" "C" "C Now sum power usage" "C" "F W100 = WEFEED + WEDRY" ) \ \ "READ-VARS" READ-VAR = ( WOOD WATER ) \ ? CALCULATOR W200 ? ; "ENG_MOLE" ; \ DEFINE FVN = W200 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W200" OPT-CATEG = STREAM \ \ DEFINE FVN = WCOMP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A200.A200CC.WK202" OPT-CATEG = STREAM \ \ DEFINE FVN = WOOD FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD OPT-CATEG = STREAM \ \ DEFINE FVN = XH2O FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = PROXANAL FVN-ELEM = 1 OPT-CATEG = STREAM \ \ DEFINE FVN = ASHFR FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = PROXANAL FVN-ELEM = 4 OPT-CATEG = STREAM \ \ DEFINE FVN = MEFF1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = EFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = MEFF2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = DEFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sums the power requirements for the gasifier section" "C" "C MEFF1 is mechanical efficiency from MEFF-A reference in ARFRNC block" "C MEFF2 is motor efficiency from MEFF-A reference in ARFRNC block" "C First the blower for combustor air...assume mechanical efficiency" "C of 98% and motor efficiency of 90%" "C" "F WECOMP = WCOMP / MEFF1 / MEFF2" "C" "C Now the motor for the ash cooler...assume 3.75 Hp per 100 US ton" "C (dry) per day of biomass feed to the plant which for 1% ash wood" "C becomes 3.75 hp/ton ash." "C" "C Phillips 10/9/06" "C" "C for variations in ash content in the biomass. Assumes all ash goes" "C out in ash handling system." "C" "F BIOFED = WOOD * (1 - XH2O/100) * 24 / 2000" "F WECOOL = 3.75/1 * BIOFED * (ASHFR / 100)" "C" "C Now the motor for the ash conditioner...assume 2.5 Hp per 100 US ton" "C (dry) per day of biomass feed to the plant." "C" "C WECOND = 2.5 * BIOFED / 100" "F WECOND = 2.5/1 * BIOFED * (ASHFR/100)" "C" "C Now the electrostatic precipitator...scaled from Weyerhauser report" "C to give 160 Hp per 2000 BD tonne/day of feed which for 1% ash wood" "C gives 160 hp per 20 tonne/day ash" "C" "C WEESP = 160 * BIOFED / 2000" "F WEESP = 160.4/20 * BIOFED * ASHFR/100" "C" "C Sum all of them" "C" "F W200 = WECOMP + WECOOL + WECOND + WEESP" ) \ \ "READ-VARS" READ-VAR = ( WCOMP WOOD XH2O ASHFR MEFF1 MEFF2 ) \ \ "WRITE-VARS" WRITE-VAR = ( W200 ) \ ? CALCULATOR W300 ? ; "ENG_MOLE" ; \ DEFINE FVN = W300 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W300" OPT-CATEG = STREAM \ \ DEFINE FVN = WSLUDG FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A300.A300Q.WP301" OPT-CATEG = STREAM \ \ DEFINE FVN = WCIRC FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A300.A300Q.WP302" OPT-CATEG = STREAM \ \ DEFINE FVN = MCIRC FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.MULT300B" FVN-VARIABLE = FACTOR FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = WCOMP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A300.A300Q.WK301" OPT-CATEG = STREAM \ \ DEFINE FVN = QCOMP FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "TOT-QCALC" FVN-SENTENCE = RESULTS OPT-CATEG = BLOCK \ \ DEFINE FVN = SULFUR FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 324 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = THOT1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "COMPR-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 1 OPT-CATEG = BLOCK \ \ DEFINE FVN = TCOLD1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "COOLER-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 1 OPT-CATEG = BLOCK \ \ DEFINE FVN = QIC1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = QCALC FVN-SENTENCE = PROFILE FVN-ID1 = 1 OPT-CATEG = BLOCK \ \ DEFINE FVN = THOT2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "COMPR-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 2 OPT-CATEG = BLOCK \ \ DEFINE FVN = TCOLD2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "COOLER-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 2 OPT-CATEG = BLOCK \ \ DEFINE FVN = QIC2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = QCALC FVN-SENTENCE = PROFILE FVN-ID1 = 2 OPT-CATEG = BLOCK \ \ DEFINE FVN = THOT3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "COMPR-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 3 OPT-CATEG = BLOCK \ \ DEFINE FVN = TCOLD3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "COOLER-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 3 OPT-CATEG = BLOCK \ \ DEFINE FVN = QIC3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = QCALC FVN-SENTENCE = PROFILE FVN-ID1 = 3 OPT-CATEG = BLOCK \ \ DEFINE FVN = THOT4 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "COMPR-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 4 OPT-CATEG = BLOCK \ \ DEFINE FVN = TCOLD4 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "COOLER-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 4 OPT-CATEG = BLOCK \ \ DEFINE FVN = QIC4 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = QCALC FVN-SENTENCE = PROFILE FVN-ID1 = 4 \ \ DEFINE FVN = THOT5 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "COMPR-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 5 OPT-CATEG = BLOCK \ \ DEFINE FVN = TCOLD5 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = "COOLER-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 5 OPT-CATEG = BLOCK \ \ DEFINE FVN = QIC5 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A300.A300Q.K-301" FVN-VARIABLE = QCALC FVN-SENTENCE = PROFILE FVN-ID1 = 5 OPT-CATEG = BLOCK \ \ DEFINE FVN = FCO2 FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = "A300.A300S.319B" FVN-SUBS = MIXED FVN-COMPONEN = CO2 OPT-CATEG = STREAM \ \ DEFINE FVN = WEAFAN FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.WK332FAN" OPT-CATEG = STREAM \ \ DEFINE FVN = QACOND FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300AGR.QAMCON" OPT-CATEG = STREAM \ \ DEFINE FVN = PAMLIQ FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300AGR.AM-COLD" FVN-SUBS = MIXED FVN-VARIABLE = PRES OPT-CATEG = STREAM \ \ DEFINE FVN = WP314 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A300.A300Q.WP314" OPT-CATEG = STREAM \ \ DEFINE FVN = WEAFN2 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.WK333FAN" \ \ DEFINE FVN = QACOOL FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A300.A300AGR.QACOOL" \ \ DEFINE FVN = AMFLOW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300AGR.AM-COLD" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = AMDEN FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A300.A300AGR.AM-COLD" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = WIFAN FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A300.A300TR.A300FC.WK305" OPT-CATEG = STREAM \ \ DEFINE FVN = WNFAN FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A300.A300TR.A300FC.WK303" OPT-CATEG = STREAM \ \ DEFINE FVN = AIRTEM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "AREFRNC.AMBAIR" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = MEFF1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = EFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = MEFF2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = DEFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sums the power requirements for gas clean-up" "C" "C Sludge pump...assume 98% mechanical efficiency and 90% motor" "C" "F WESLUD = WSLUDG / MEFF1 / MEFF2" "C" "C Now the quench water circulation pump...ratio-up the horsepower" "C by (MCIRC+1)/MCIRC to account for product draw." "C Assume 98% mechanical efficiency and 90% motor efficiency" "C" "F WECIRC = (MCIRC+1)/MCIRC * WCIRC / MEFF1 / MEFF2" "C" "C Now the compressor...assume 98% mechanical efficiency and" "C 90% motor efficiency" "C Phillips 10/10/06" "C Electric motor replaced with steam turbine-driven compressor" "C any excess power is converted to electricity on output of compressor" "C 602A" "C" "C Alternate method for fan cooling calc" "C Phillips 10/5/06" "C See Calc block for W500 for explanation" "C Stage 1 IC" "F DELT1 = TCOLD1 - AIRTEM" "F DELT2 = THOT1 - 160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN1 = -QIC1 / (3608.0 * TLM) " "C Stage 2 IC" "F DELT1 = TCOLD2 - AIRTEM" "F DELT2 = THOT2 - 160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN2 = -QIC2 / (3608.0 * TLM)" "C Stage 3 IC" "F DELT1 = TCOLD3 - AIRTEM" "F DELT2 = THOT3 - 160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN3 = -QIC3 / (3608.0 * TLM)" "C Stage 4 IC" "F DELT1 = TCOLD4 - AIRTEM" "F DELT2 = THOT4 - 160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN4 = -QIC4 / (3608.0 * TLM)" "C Stage 5 IC" "F DELT1 = TCOLD5 - AIRTEM" "F DELT2 = THOT5-160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN5 = -QIC5 / (3608.0 * TLM)" "C" "C Sum up fan hp for compressor IC coolers" "F WEFAN = WEFAN1 + WEFAN2 + WEFAN3 + WEFAN4 + WEFAN5" "C" "C Amine stripper condenser and amine cooler using air coolers. " "C Calculate cond " "C duty as per GPSA document with cooling forced to match reboiler duty" "C with 2/3 of cooling assumed to be at the condenser and 1/3 in cooler: " "C Duty(Btu/hr)=2/3 * 72000 * GPM amine circulation" "C" "F DELT1 = 212.0 - AIRTEM" "F DELT2 = 212.0 - 160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F QACOND = 48000.0 * ((AMFLOW/AMDEN) * 7.4805 / 60.0)" "F WEAFAN = QACOND / (6850.0 * TLM)" "C" "C Calculate amine cooler duty as per GPSA document, 1/3 of reboiler" "C duty. assumed water for work calc parameter" "F DELT1 = 140.0 - AIRTEM" "F DELT2 = 212.0 - 160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F QACOOL = 24000.0 * ((AMFLOW/AMDEN) * 7.4805 / 60.0)" "F WEAFN2 = QACOOL / (5779.0 * TLM)" "c" "C Amine scrubber pumps power requirements in HP" "C PAMLIQ is pump liquid pressure, psig" "C First product is main amine pump, second term is booster pump, and" "C third is reflux pumps" "C" "F WEAPMP = (AMFLOW/AMDEN)*7.4805/60.0 * ((PAMLIQ * 0.00065)" "F 1 + 0.06 + 0.06)" "C" "C Now the desulfurization skid...place holders estimates until" "C we get some data from vendor" "C" "F WESULF = SULFUR*24/2240 * 300*0.8*1.341/1.7" "C" "C Condensate pump from S-301" "F WEP314 = WP314 / MEFF1 / MEFF2" "C" "C First the inlet fan for the fuel combustor air..." "C assume 98% mechanical efficiency and 90% motor efficiency" "C" "F WEIFAN = WIFAN / MEFF1 / MEFF2" "C" "C This fan was moved to NG inlet stream to raise it to pressure of" "C other stream being recycled to the fuel combustor..." "C assume 98% mechanical efficiency and 90% motor efficiency" "C" "F WENFAN = WNFAN / MEFF1 / MEFF2" "C Sum the power usage" "C" "F W300 = WESLUD + WECIRC + WECOMP + WEFAN + WESULF + WEEXP + WEAFAN" "F 1 + WEAPMP + WEP314 + WEIFAN + WENFAN" "C" "C Now write" "C" "F WRITE (NHSTRY,*) 'W300 POWER:', " "F 1 W300, WESLUD, WECIRC,WECOMP,WEFAN,WESULF,WEEXP," "F 2 WEFAN1, WEFAN2, WEFAN3, WEFAN4, WEFAN5, WEAFAN," "F 3 WEAPMP, WEP314, WEIFAN, WENFAN, MEFF1, MEFF2" ) \ \ "READ-VARS" READ-VAR = ( WCIRC WCOMP SULFUR MCIRC WSLUDG THOT1 TCOLD1 QIC1 THOT2 TCOLD2 QIC2 THOT3 TCOLD3 THOT4 TCOLD4 QIC4 THOT5 TCOLD5 QIC5 QIC3 FCO2 WIFAN WNFAN AIRTEM MEFF2 MEFF1 ) \ \ "WRITE-VARS" WRITE-VAR = ( QACOND WEAFAN PAMLIQ ) \ ? CALCULATOR W400 ? ; "ENG_MOLE" ; \ DEFINE FVN = W400 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W400" OPT-CATEG = STREAM \ \ DEFINE FVN = WCOMP4 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A400.WK414" \ \ DEFINE FVN = QCOMP FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A400.A400CMPR.K-410" FVN-VARIABLE = "TOT-QCALC" FVN-SENTENCE = RESULTS OPT-CATEG = BLOCK \ \ DEFINE FVN = QH413A FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A400.H-413" FVN-VARIABLE = QCALC FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = THOT2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A400.472" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = TCOLD2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A400.473" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = WEFAN2 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.WK413FAN" OPT-CATEG = STREAM \ \ DEFINE FVN = AIRTEM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "AREFRNC.AMBAIR" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = MEFF1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = EFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = MEFF2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = DEFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = QIC1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A400.A400CMPR.K-410" FVN-VARIABLE = QCALC FVN-SENTENCE = PROFILE FVN-ID1 = 1 OPT-CATEG = BLOCK \ \ DEFINE FVN = QIC3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A400.A400CMPR.K-410" FVN-VARIABLE = QCALC FVN-SENTENCE = PROFILE FVN-ID1 = 2 \ \ DEFINE FVN = THOT1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A400.A400CMPR.K-410" FVN-VARIABLE = "COMPR-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 1 \ \ DEFINE FVN = TCOLD1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A400.A400CMPR.K-410" FVN-VARIABLE = "COOLER-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 1 OPT-CATEG = BLOCK \ \ DEFINE FVN = THOT3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A400.A400CMPR.K-410" FVN-VARIABLE = "COMPR-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 2 OPT-CATEG = BLOCK \ \ DEFINE FVN = TCOLD3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A400.A400CMPR.K-410" FVN-VARIABLE = "COOLER-TEMP" FVN-SENTENCE = PROFILE FVN-ID1 = 2 OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( " " "C" "C Now the compressors...assume 98% mechanical efficiency" "C and 90% motor efficiency" "C" "C Phillips 10/6/06" "C Compressor motor replaced by steam-driven turbine in steam cycle" "C Compressor work for unconverted syngas recycle to MAR inlet" "F WECMP4 = WCOMP4 / MEFF1 / MEFF2" "C" "C" "C Air coolers for post MAS reactor cooler HA-413. Same specs as WEFAN." "C" "F DELT1 = TCOLD2 - AIRTEM" "F DELT2 = THOT2 - 160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN2 = -QH413A / (3608.0 * TLM)" "C" "C See Calc block for W500 for explanation" "C Stage 1 IC" "F DELT1 = TCOLD1 - AIRTEM" "F DELT2 = THOT1 - 160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN1 = -QIC1 / (3608.0 * TLM) " "C Stage 2 IC" "F DELT1 = TCOLD2 - AIRTEM" "F DELT2 = THOT2 - 160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN3 = -QIC3 / (3608.0 * TLM)" "C Now sum" "C" "F W400 = WEFAN2 + WECMP4 + WEFAN1 + WEFAN3" "C" "C Now write" "C" "F WRITE (NHSTRY,*) 'W400 POWER:', " "F 1 W400, WECMP4, WEFAN2, AIRTEM, MEFF1, MEFF2" ) \ \ "READ-VARS" READ-VAR = ( WCOMP4 QCOMP THOT2 TCOLD2 AIRTEM MEFF1 MEFF2 TCOLD3 TCOLD1 THOT1 THOT3 QIC1 QIC3 ) \ \ "WRITE-VARS" WRITE-VAR = ( W400 ) \ ? CALCULATOR W500 ? ; "ENG_MOLE" ; \ DEFINE FVN = W500 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W500" \ \ DEFINE FVN = FL590 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 590 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = FL592 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 592 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = DEN590 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 590 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = DEN592 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 592 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = FBD504 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A504.D504" FVN-VARIABLE = "L-VOLFLOW" FVN-SENTENCE = HYDRAULIC FVN-ID1 = 54 \ \ DEFINE FVN = FTD504 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A504.D504" FVN-VARIABLE = "L-VOLFLOW" FVN-SENTENCE = HYDRAULIC FVN-ID1 = 1 \ \ DEFINE FVN = FBD505 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A504.D505" FVN-VARIABLE = "L-VOLFLOW" FVN-SENTENCE = HYDRAULIC FVN-ID1 = 69 \ \ DEFINE FVN = FTD505 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A504.D505" FVN-VARIABLE = "L-VOLFLOW" FVN-SENTENCE = HYDRAULIC FVN-ID1 = 1 \ \ DEFINE FVN = PRODFL FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.A503MS.513L" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" \ \ DEFINE FVN = PRODDE FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.A503MS.513L" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" \ \ DEFINE FVN = QC504 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.QAH504" OPT-CATEG = STREAM \ \ DEFINE FVN = QC505 FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.A504.QAH505" OPT-CATEG = STREAM \ \ DEFINE FVN = QCMS FVN-VARTYPE = "HEAT-DUTY" FVN-STREAM = "A500.A503MS.QAS513" OPT-CATEG = STREAM \ \ DEFINE FVN = THOT1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.A503MS.513F" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = THOT2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A504.D504" FVN-VARIABLE = TEMP FVN-SENTENCE = PROFILE FVN-ID1 = 1 OPT-CATEG = BLOCK \ \ DEFINE FVN = THOT3 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A504.D505" FVN-VARIABLE = TEMP FVN-SENTENCE = PROFILE FVN-ID1 = 1 OPT-CATEG = BLOCK \ \ DEFINE FVN = TCOLD1 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.A503MS.513V" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = TCOLD2 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.A504.510" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = TCOLD3 FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.512" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = WEFAN1 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.WK513FAN" OPT-CATEG = STREAM \ \ DEFINE FVN = WEFAN2 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.WK504FAN" OPT-CATEG = STREAM \ \ DEFINE FVN = WEFAN3 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.WK505FAN" \ \ DEFINE FVN = WP514 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A500.A503MS.WP514" \ \ DEFINE FVN = AIRTEM FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "AREFRNC.AMBAIR" FVN-SUBS = MIXED FVN-VARIABLE = TEMP OPT-CATEG = STREAM \ \ DEFINE FVN = MEFF1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = EFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = MEFF2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = DEFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sums the power requirements for alcohols purification" "C Assume ambient cooling air at 95F and reaches 160F" "C" "C For fan power requirements, The Handbook of Mechanical Engineering" "C Calculation, Hicks, Tyler G., chapter 11, figure 22," "C gives fan hp/100ft^2 of bare tube as a function of U." "C These values range from 1.5 to 2.0 for U" "C between 30 and 120 Btu/h-ft2-F, respectively. Changes in required" "C fan power was essentially flat below and above these limits." " " "C Overall HTC, U in Btu/h-ft2-F, depends on type of stream being cooled" "C and ranges from about 5 to 150. For air-cooled heat exchangers used" "C to cool process streams, Cheresources.com gives the following for" "C U in Btu/h-ft2-F based on outside bare tube surface with Fan P (P)" "C in hp/100s.f. bare tube surface or P/A/100 (taken from Hicks):" "C" "C hot fluid U 100*P/A" "C Water 100-130 1.98-2.0" "C light hydrocarbons 70-95 1.7 -1.95" "C tar 5-10 1.5" "C air or flue gas 10-30 1.5" "C hydrocarbon gas 35-80 1.5 -1.80" "C condensation of l.p. steam 125-150 2.0" "C condensation of organic vapors 65-90 1.65-1.90" "C" "C " "C hot fluid Umidpt A(P)= UA(P)=" "C Water 115 50.3*P 5779*P" "C light hydrocarbons 83 1.83*P 4548*P" "C tar 7 1.5*P 467*P" "C air or flue gas 20 1.5*P 1333*P" "C hydrocarbon gas 57 1.58*P 3608*P" "C condensation of l.p. steam 137 2.0*P 6850*P" "C condensation of organic vapors 77 1.8*P 4278*P" "C" "C With the information and assumptions above for air temperatures," "C the following general formula can be used:" "C " "C Q(Thot, TCold)=U*A*LMTD(Thot, TCold) and after substitution to:" "C Q(Thot, TCold)=UA(P)*LMTD(Thot, TCold)." "C " "C Sinc Q and Thot are known from the simulation, the Fan power data give" "C can be calculated using the appropriate UA(P) to match the fluid" "C" "C 1. Cooling fan for Mol Sieve condenser (condensing water/MeOH mixture)" "C 2. Cooling fan for D-504 condenser (condensing organic vapors)" "C 3. Cooling fan for D-505 condenser (condensing organic vapors) " "C" "F DELT1 = TCOLD1 - AIRTEM" "F DELT2 = THOT1-160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN1 = QCMS / (4278.0 * TLM)" "C" "F DELT1 = TCOLD2 - AIRTEM" "F DELT2 = THOT2-160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN2 = QC504 / (4278.0 * TLM)" "C" "F DELT1 = TCOLD3 - AIRTEM" "F DELT2 = THOT3-160.0" "F TLM = (DELT2 - DELT1)/ LOG(DELT2/DELT1)" "F WEFAN3 = QC505 / (4278.0 * TLM)" "C" "C Now the electricity requirement for the mol sieve" "C flow reads in lb/hr and dens reads in lb/ft3" "C" "C Factor units = kW/gal/hr" "C" "F FACTOR = .0204" "F WSIEVE = FACTOR * 1.341 * (PRODFL/PRODDE*7.4805)" "C" "C Product pumps taken from ethanol design report (2002)" "C 112 Ft head = 49 psi. FLOW is in ft^3/hr" "C" "F head = 49" "F FLOW = FL590/DEN590 + FL592/DEN592 " "F WPUMP = head*144*(FLOW /3600)/550" "C Add wpump2 to account for WP514" "F WPUMP2 = WP514" "C" "C Now add the electricity requirement for separating the alcohols." "C Power requirement from bottoms & reflux pumps. Similar to " "C biochem beer column, use 60.7 psi for reflux pumps & 67.5 psi for" "C bottoms pumps. " "C" "F head = 60.7" "F FLOW = FTD504 + FTD505 " "F WSEP = head*144.0*(FLOW /3600.0)/550.0" "F head = 67.5" "F FLOW = FBD504 + FBD505 " "F WSEP = wsep + head*144.0*(FLOW /3600.0)/550.0" "C" "C Now sum" "C" "F W500 = WSIEVE + WPUMP + WPUMP2 + WSEP + WEFAN1 + WEFAN2 + WEFAN3" "F WRITE (NHSTRY,*) 'W500 POWER:', " "F 1 W500, WSIEVE, WPUMP, WPUMP2, WSEP, WEFAN1, WEFAN2, WEFAN3," "F 2 FTD504, FTD505, FBD504, FBD505, AIRTEM, MEFF1, MEFF2" ) \ \ "READ-VARS" READ-VAR = ( FL590 FL592 DEN590 DEN592 FBD504 FTD504 FBD505 FTD505 PRODFL PRODDE QCMS THOT1 THOT3 TCOLD1 TCOLD2 WP514 AIRTEM MEFF1 MEFF2 ) \ \ "WRITE-VARS" WRITE-VAR = ( W500 WEFAN1 WEFAN2 WEFAN3 ) \ ? CALCULATOR W600 ? ; "ENG_MOLE" ; \ DEFINE FVN = W600 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W600" OPT-CATEG = STREAM \ \ DEFINE FVN = WHWP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A600.A600ST.WP602" OPT-CATEG = STREAM \ \ DEFINE FVN = WDGSP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A600.A600BF.WP603" OPT-CATEG = STREAM \ \ DEFINE FVN = WMAKE FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A600.A600WTR.WP601" OPT-CATEG = STREAM \ \ DEFINE FVN = WBFWP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A600.A600BL.WP604" OPT-CATEG = STREAM \ \ DEFINE FVN = MEFF1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = EFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = MEFF2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = DEFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sums the power requirements for the boiler...power generated" "C is summed in FORTRAN WGEN" "C" "C First the hot well pump..." "C Assume 98% mechanical efficiency and 90% motor efficiency" "C" "F WEHWP = WHWP / MEFF1 / MEFF2" "C" "C Now the degasifier supply pump..." "C Assume 98% mechanical efficiency and 90% motor efficiency" "C" "F WEDGSP = WDGSP / MEFF1 / MEFF2" "C" "C Now the make-up water pump..." "C Assume 98% mechanical efficiency and 90% motor efficiency" "C" "F WEMAKE = WMAKE / MEFF1 / MEFF2" "C" "C Now the boiler feed water pump..." "C Assume 98% mechanical efficiency and 90% motor efficiency" "C" "F WEBFWP = WBFWP / MEFF1 / MEFF2" "C" "C Sum the power usage..." "C" "F W600 = WEHWP + WEDGSP + WEMAKE + WEBFWP" ) \ \ "READ-VARS" READ-VAR = ( WHWP WDGSP WMAKE WBFWP MEFF1 MEFF2 ) \ ? CALCULATOR W700 ? ; "ENG_MOLE" ; \ DEFINE FVN = W700 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W700" OPT-CATEG = STREAM \ \ DEFINE FVN = WFAN FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A700.WM701" OPT-CATEG = STREAM \ \ DEFINE FVN = WCIRC FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A700.WP701" OPT-CATEG = STREAM \ \ DEFINE FVN = MEFF1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = EFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ DEFINE FVN = MEFF2 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = DEFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sums the power needed for the cooling water system" "C" "C First the cooling tower fan..." "C Assume 98% mechanical efficiency and 90% motor efficiency" "C" "F WEFAN = WFAN / MEFF1 / MEFF2" "C" "C Now the circulation pump..." "C Assume 98% mechanical efficiency and 90% motor efficiency" "C" "F WECIRC = WCIRC / MEFF1 / MEFF2" "C" "C Now sum the usage" "C" "F W700 = WEFAN + WECIRC" ) \ \ "READ-VARS" READ-VAR = ( WFAN WCIRC MEFF1 MEFF2 ) \ ? CALCULATOR WGEN ? ; "ENG_MOLE" ; \ DEFINE FVN = WGEN FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.WGEN" \ \ DEFINE FVN = WHP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A600.A600ST.WM602A" OPT-CATEG = STREAM \ \ DEFINE FVN = WCOMP FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A300.A300Q.WK301" OPT-CATEG = STREAM \ \ DEFINE FVN = WCOMP2 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A400.A400CMPR.WK410" OPT-CATEG = STREAM \ \ DEFINE FVN = MEFF1 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "AREFRNC.MEFF-A" FVN-VARIABLE = EFF FVN-SENTENCE = PARAM OPT-CATEG = BLOCK \ \ FORTRAN FORTRAN-EXEC = ( "C This sums the power generation" "C" "C First the high pressure turbine section..." "C Assume 98% mechanical efficiency and 97% generator efficiency" "C Phillips 10/10/06 replaced generator with turbine-driven compressor" "C Match the compressor work needs minus efficiency losses to the turbine" "C shaft output minus efficiency losses - the remainder put into electric" "C generation. Excess power is negative in sign." "F IF (WHP .LT. 0.0)THEN" " WEHP = WHP * MEFF1 * 0.97" " ELSE" " WEHP = WHP / 0.98 / 0.95" " END IF" "C" "C Turbine shafts are coupled and all electricity generated on one" "C generator based on excess power at compressor 602A output" "C" "C" "C Sum the generation" "C" "F WGEN = WEHP" " WSHFT = WCOMP + WCOMP2" "C Now write" "C" "F WRITE (NHSTRY,*) 'WGEN POWER:', " "F 1 WGEN, WSHFT, WEHP, MEFF1" ) \ \ "READ-VARS" READ-VAR = ( WHP WCOMP2 MEFF1 ) \ \ "WRITE-VARS" WRITE-VAR = ( WGEN ) \ ? CALCULATOR WMISC ? ; "ENG_MOLE" ; \ DEFINE FVN = WMISC FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.WMISC" OPT-CATEG = STREAM \ \ DEFINE FVN = W100 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W100" \ \ DEFINE FVN = W200 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W200" OPT-CATEG = STREAM \ \ DEFINE FVN = W300 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W300" OPT-CATEG = STREAM \ \ DEFINE FVN = W400 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W400" OPT-CATEG = STREAM \ \ DEFINE FVN = W500 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W500" OPT-CATEG = STREAM \ \ DEFINE FVN = W600 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W600" OPT-CATEG = STREAM \ \ DEFINE FVN = W700 FVN-VARTYPE = "WORK-POWER" FVN-STREAM = "A900.W700" OPT-CATEG = STREAM \ \ FORTRAN FORTRAN-EXEC = ( "C This computes miscellaneous power consumption." "C" "C Right now, set this at 10% excess of defined power use or 1000" "C" "F WMISC = 0.1*(W100 + W200 + W300 + W400 + W500 + W600 + W700)" "F IF ((WMISC*0.7457) .GT. 1000.) WMISC= 1000.0/0.7457" "C" ) \ \ "READ-VARS" READ-VAR = ( W500 W100 W200 W300 W400 W600 W700 ) \ \ "WRITE-VARS" WRITE-VAR = ( WMISC ) \ ? SENSITIVITY MASSFLOW ? ; "ENG_MOLE" ; \ PARAM BASE-CASE = NO \ \ DEFINE FVN = DD504 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A504.D504" FVN-VARIABLE = "TS-DIAM" FVN-SENTENCE = "TSIZE-RESULT" FVN-ID1 = 1 OPT-CATEG = BLOCK \ \ DEFINE FVN = DD505 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A504.D505" FVN-VARIABLE = "TS-DIAM" FVN-SENTENCE = "TSIZE-RESULT" FVN-ID1 = 1 OPT-CATEG = BLOCK \ \ DEFINE FVN = INMIX FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 100 FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = INCIS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 100 FVN-SUBS = CISOLID FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = INNC FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-VARIABLE = "MASS-FLOW" OPT-CATEG = STREAM \ \ DEFINE FVN = INWAT FVN-VARTYPE = "MASS-FLOW" FVN-STREAM = 100 FVN-SUBS = MIXED FVN-COMPONEN = H2O OPT-CATEG = STREAM \ \ DEFINE FVN = FEEDC FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 2 OPT-CATEG = STREAM \ \ DEFINE FVN = FEEDH FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 3 OPT-CATEG = STREAM \ \ DEFINE FVN = FEEDO FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 7 OPT-CATEG = STREAM \ \ DEFINE FVN = DENETH FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "A500.592" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-DENSITY" OPT-CATEG = STREAM \ \ DEFINE FVN = HHVEFF FVN-VARTYPE = PARAMETER FVN-PARAMNO = 2 \ \ DEFINE FVN = LHVEFF FVN-VARTYPE = PARAMETER FVN-PARAMNO = 3 \ \ DEFINE FVN = GASHHV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 4 \ \ DEFINE FVN = GASLHV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 5 \ \ DEFINE FVN = FLD504 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A504.D504" FVN-VARIABLE = "L-VOLFLOW" FVN-SENTENCE = HYDRAULIC FVN-ID1 = 54 OPT-CATEG = BLOCK \ \ DEFINE FVN = FLD505 FVN-VARTYPE = "BLOCK-VAR" FVN-BLOCK = "A500.A504.D505" FVN-VARIABLE = "L-VOLFLOW" FVN-SENTENCE = HYDRAULIC FVN-ID1 = 69 OPT-CATEG = BLOCK \ \ DEFINE FVN = FEEDS FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 6 \ \ DEFINE FVN = FEEDN FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 4 \ \ DEFINE FVN = FEEDA FVN-VARTYPE = "COMPATTR-VAR" FVN-STREAM = 100 FVN-SUBS = NC FVN-COMPONEN = WOOD FVN-ATTRIB = ULTANAL FVN-ELEM = 1 \ \ DEFINE FVN = INHHV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 6 \ \ DEFINE FVN = INLHV FVN-VARTYPE = PARAMETER FVN-PARAMNO = 7 \ \ FORTRAN FORTRAN-EXEC = ( "F FEEDMSTR = INWAT / ( INMIX + INCIS + INNC )" ) \ \ TABULATE COLNO = 2 EXPR = "DD504" \ \ TABULATE COLNO = 3 EXPR = "DD505" \ \ TABULATE COLNO = 4 EXPR = "FEEDMSTR " \ \ TABULATE COLNO = 5 EXPR = "FEEDC" \ \ TABULATE COLNO = 6 EXPR = "FEEDH" \ \ TABULATE COLNO = 7 EXPR = "FEEDO" \ \ TABULATE COLNO = 8 EXPR = "HHVEFF" \ \ TABULATE COLNO = 9 EXPR = "LHVEFF" \ \ TABULATE COLNO = 10 EXPR = "GASHHV" \ \ TABULATE COLNO = 11 EXPR = "GASLHV" \ \ TABULATE COLNO = 12 EXPR = "FLD504" \ \ TABULATE COLNO = 13 EXPR = "FLD505" \ \ TABULATE COLNO = 14 EXPR = "FEEDN" \ \ TABULATE COLNO = 15 EXPR = "FEEDS" \ \ TABULATE COLNO = 16 EXPR = "FEEDA" \ \ TABULATE COLNO = 17 EXPR = "INHHV" \ \ TABULATE COLNO = 18 EXPR = "INLHV" \ \ VARY SCRUD = 1 VARY-VARTYPE = "STREAM-VAR" VARYSTREAM = 100 VARYSUBS = MIXED VARYVARIABLE = TEMP LIST = ( 60. <0> <0> ) OPT-LIST = OLIST \ \ REINIT TOGBL = NONE \ ? "CONV-OPTIONS" ? \ PARAM UPDATE = YES SPEC-METHOD = SECANT SPEC-LOOP = "IN-SIMUL" USER-LOOP = INSIDE TEAR-VAR = YES TEAR-WEIGHT = 1 LOOP-WEIGHT = 1 \ \ WEGSTEIN WEG-MAXIT = 300 \ \ DIRECT DIR-MAXIT = 100 \ \ SECANT SEC-MAXIT = 100 STEP-SIZ = 0.001 <0> <0> SEC-XTOL = 1E-009 <0> <0> \ \ BROYDEN BR-MAXIT = 100 \ \ NEWTON NEW-MAXIT = 100 \ ? TEAR ? ? CONVERGENCE WEGSTEIN TEAR ? \ TEAR SID = "A200.A200CC.204" TOL = 1E-005 <0> <0> \ ? CONVERGENCE SECANT ADIABATI ? \ SPEC SPECID = ADIABAT TOL = 100. <0> <0> \ \ PARAM STEP-SIZE = 0.0001 <0> <0> MAX-STEP-SIZ = 0.005 <0> <0> BRACKET = YES STOP = NO \ ? CONVERGENCE SECANT COMBCTRL ? \ SPEC SPECID = COMBCTL1 \ \ PARAM MAX-STEP-SIZ = 0.05 <0> <0> BRACKET = YES \ ? CONVERGENCE SECANT QBALANCE ? \ SPEC SPECID = QBALANCE TOL = 1000. <0> <0> \ \ PARAM MAXIT = 100 STEP-SIZE = 0.001 <0> <0> MAX-STEP-SIZ = 1. <0> <0> XTOL = 1E-007 <0> <0> BRACKET = YES XFINAL = FMIN \ ? CONVERGENCE SECANT TAIRO ? \ SPEC SPECID = TAIRO \ ? CONVERGENCE NEWTON CO2SPEC ? \ SPEC SPECID = CO2SPEC SPEC = 0.0005 <0> <0> \ ? CONVERGENCE NEWTON COMCNTR2 ? \ SPEC SPECID = COMBCTL2 \ ? CONVERGENCE NEWTON QM104B ? \ SPEC SPECID = QM104B STEP-SIZE = 0.0001 <0> <0> \ ? CONVERGENCE NEWTON R201B ? \ SPEC SPECID = R301BTEM SPEC = 0.5 <0> <0> \ ? "CONV-ORDER" ? \ CVBLOCKS CVBLOCK = ( COMBCTRL ADIABATI R201B CO2SPEC ) \ ? SEQUENCE CWCALC1 ? \ SEQUENCE BLOCK-TYPE = BLOCK BLOCK-ID = "A700.V700B" / BLOCK-TYPE = CALCULATOR BLOCK-ID = CWAIRI / BLOCK-TYPE = BLOCK BLOCK-ID = "A700.MX700D" / BLOCK-TYPE = BLOCK BLOCK-ID = "A700.HX700C" \ ? SEQUENCE ENDPROC ? \ SEQUENCE BLOCK-TYPE = BLOCK BLOCK-ID = "A300.A300TR.A300FC.K-303" / BLOCK-TYPE = CALCULATOR BLOCK-ID = CO2VENT / BLOCK-TYPE = BLOCK BLOCK-ID = "A300.A300S.SP-384" \ ? SEQUENCE POWER ? \ SEQUENCE BLOCK-TYPE = SEQUENCE BLOCK-ID = TAIRO / BLOCK-TYPE = CALCULATOR BLOCK-ID = W100 / BLOCK-TYPE = CALCULATOR BLOCK-ID = W200 / BLOCK-TYPE = CALCULATOR BLOCK-ID = W300 / BLOCK-TYPE = CALCULATOR BLOCK-ID = W400 / BLOCK-TYPE = CALCULATOR BLOCK-ID = W500 / BLOCK-TYPE = CALCULATOR BLOCK-ID = W600 / BLOCK-TYPE = CALCULATOR BLOCK-ID = W700 / BLOCK-TYPE = CALCULATOR BLOCK-ID = WMISC / BLOCK-TYPE = BLOCK BLOCK-ID = "A900.WMX900A" / BLOCK-TYPE = CALCULATOR BLOCK-ID = WGEN / BLOCK-TYPE = BLOCK BLOCK-ID = "A900.WMX900B" / BLOCK-TYPE = BLOCK BLOCK-ID = "A900.WMXHOLD" / BLOCK-TYPE = BLOCK BLOCK-ID = "A300.A300AGR.LEANCOOL" \ ? SEQUENCE TAIRO ? \ SEQUENCE RETURN = BEGIN BLOCK-TYPE = CONVERGENCE BLOCK-ID = TAIRO / BLOCK-TYPE = CALCULATOR BLOCK-ID = TDRIFT / BLOCK-TYPE = BLOCK BLOCK-ID = "A700.MX700A" / RETURN = RETURNTO BLOCK-TYPE = CONVERGENCE BLOCK-ID = TAIRO \ ? REPORT REPORT ? ? REPORT "BLOCK-REPORT" ? ? REPORT "STREAM-REPOR" ? \ OPTIONS MASSFLOW = MASSFLOW PROPERTIES = ( HMIXTP ) \ ? REPORT "FLOWSHEET-RE" ? ? REPORT "PROPERTY-REP" ? ? REPORT "ADA-REPORT" ? ? REPORT "BATCH-OPERAT" ? ; "ENG_MOLE" ; GRAPHICS_BACKUP PFS V 5.00 $CONFIG paramdata ENRTL-RK paramdata VLE-IG paramdata VLE-RK paramdata VLE-HOC paramdata LLE-LIT paramdata LLE-ASPEN paramdata VLE-LIT paramdata BINARY paramdata EOS-LIT paramdata HENRY paramdata SRK-ASPEN paramdata ASPEN-BM purebank PURE10 purebank AQUEOUS purebank SOLIDS purebank INORGANIC regdbank 1 ftn_check 1 autoblockid 0 autostreamid 0 showblockid 1 showstreamid 1 autoplacement 1 grid 2 gridresolution 0.100000 scale 0 streamprefix blockprefix B labelscale 1.000000 qwformat %.0f tempformat %.0f presformat %.0f flowformat %.0f strmqwformat %.1f vflowformat %.0f mflowformat %.0f vfracformat %.2f pseudobatch 1 partial 1 animation 0 runanyway 0 tooldrawvisible 1 browserheight 11505 browserwidth 14280 browsertreewidth 5025 polyplusenabled 1 dynaplusenabled 1 bfracenabled 1 rtfenabled 1 rspenabled 0 pinchenabled 0 linklimit 500 material_color 0 material_style 983041 material_width 1 material_termid heat_color 0 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