## Aspen data introspection

Posted June 15, 2013 at 10:01 AM | categories: programming | tags: aspen

Aspen has *a lot* of variables that control the simulation. These variables are stored in a tree structure. The tree contains nodes, which in turn may contain nodes. Here, we traverse the tree and print all the variables at the end of the tree branches. At each node, we check if the node has an Elements attribute, which means the node contains other nodes. If it does, we recurse on the node, otherwise we print the name and value of the node. We indent each level so it is easier to read and see the structure. Here are the results.

import os import win32com.client as win32 aspen = win32.Dispatch('Apwn.Document') aspen.InitFromArchive2(os.path.abspath('data\Flash_Example.bkp')) def print_elements(obj, level=0): if hasattr(obj, 'Elements'): print ' '*level + obj.Name for o in obj.Elements: print_elements(o, level + 1) else: print ' '*level, obj.Name, ' = ', obj.Value print_elements(aspen.Tree) aspen.Close

Data Setup Main Input Unit Set = None User Table User Tree ATM_PRES = 14.69594878 FREE_WATER = NO INPUT_MODE = STEADY-STATE INTERACTIVE = NO MASSFLOW = MASSFLOW MASSFRAC = MASSFRAC MOLEFLOW = MOLEFLOW MOLEFRAC = MOLEFRAC NPHASE = 2 OPER_YEAR = 8766.0 PHASE = None PROPERTIES RUN_CLASS = FLOWSHEET SCOPE = TOP-LEVEL STDVOLFLOW = NOVOLFLOW STDVOLFRAC = NOVOLFRAC TAMBEQP = 50.0 TFFFILE = GEN_E TITLE = None VISITED = 0 Output Unit Set = Prop Data User Table User Tree CC Nodes ADA = 1 ENTAMB = 0 ENTSECT = 1 ENTSTREAM = 1 ENTTITLE = 1 FLOW = 1 GLMAIN = 1 NOCONVEN = 0 NOPYR = 1 NOVMSUNX = 0 PROP = 1 RUNFLOWSH = 1 Comments Global Input Unit Set = None User Table User Tree BASIS = MOLE GLOBDATASET = ENG INSET = ENG OUTSET = ENG SCLASS = CONVEN Output Unit Set = Prop Data User Table User Tree CC Nodes ENTGLOBAL = 1 Comments Units-Sets ENG Input Unit Set = None User Table User Tree ASKED = 0 BASESET = ENG CURRENCY = None DESCRIPTION = English Engineering Units Output Unit Set = Prop Data User Table User Tree CC Nodes MAIN = 1 Comments Unit-Types AREA = sqft COMPOSITION = mol-fr DENSITY = lb/cuft DIFFUSIVITY = sqft/hr ENERGY = Btu ENTHALPY = Btu/lbmol ENTROPY = Btu/lbmol-R FISCAL = $ FLOW = lb/hr MASS-FLOW = lb/hr MOLE-FLOW = lbmol/hr VOLUME-FLOW = cuft/hr ENTHALPY-FLO = Btu/hr FORCE = lbf MOLE-HEAT-CA = Btu/lbmol-R HEAT-TRANS-C = Btu/hr-sqft-R LENGTH = ft MASS = lb POWER = hp PRESSURE = psia SURFACE-TENS = dyne/cm TEMPERATURE = F THERMAL-COND = Btu-ft/hr-sqft-R TIME = hr VELOCITY = ft/sec VISCOSITY = cP VOLUME = cuft FREQUENCY = rpm UNIT-PRICE = $/lb ENERGY-PRICE = $/Btu DELTA-T = F ANGLE = deg HEAD = ft-lbf/lb BOND-WORK-IN = kWhr/ton FILTER-RESIS = 1/ft SPEC-FLT-RES = ft/lb MOLE-DENSITY = lbmol/cuft MASS-DENSITY = lb/cuft MOLE-ENTHALP = Btu/lbmol MASS-ENTHALP = Btu/lb MOLE-ENTROPY = Btu/lbmol-R MASS-ENTROPY = Btu/lb-R MOLE-VOLUME = cuft/lbmol DIMENSIONLES = Unitless DIPOLEMOMENT = (Btu*cuft)**.5 SOLUPARAM = (Btu/cuft)**.5 ELEC-POWER = kW ELEC-PRICE = $/kWhr MASS-HEAT-CA = Btu/lb-R UA = Btu/hr-R MOLES = lbmol WORK = hp-hr HEAT = Btu AREA-PRICE = $/sqft VOLUME-PRICE = $/cuft ITEM-PRICE = $/item NUM-CONC = no/cuft MASS-CONC = lb/cuft INVERSE-TIME = 1/hr LN-INV-TIME = ln(1/hr) FLUX = cuft/sqft-sec AREA-USAGE = sqft/hr VOLUME-USAGE = cuft/hr MOLE-CONC = lbmol/cuft POWER-VOLUME = hp/cuft MASS-TRANS-C = lb/hr-sqf-lb/cuf SPECIFICAREA = sqft/cuft INVERSE-LENG = 1/ft CHROM-VEL = ft/sec MASS-FLUX = lb/sqft-hr SOLVENT-PERM = lb/sqft-hr-atm SOLUTE-PERM = sqft/ft-hr WATER-RATE = lb/hp-hr PDROP-PER-HT = in-water/ft PDROP = psi PACK-FACTOR = 1/ft NUM-CON-RATE = no/cuft-sec INVERSE-AREA = 1/sqft VOL-HEAT-CAP = Btu/cuft-R HEAT-FLUX = Btu/hr-ft INVERSE-TEMP = 1/R INVERSE-PRES = 1/psi TEMP-VOLUME = cuft-R/lbmol VFLOW-LENGTH = gpm/ft CONTENTS = percent POP-DENSITY = no/ft/cuft INVERSE-HT-C = hr-sqft-R/Btu VOL-ENTHALPY = Btu/cuft MOL-FLOW-LEN = lbmol/hr-ft USR-DUMMY0 = None USR-DUMMY1 = None USR-DUMMY2 = None USR-DUMMY3 = None USR-DUMMY4 = None USR-DUMMY5 = None USR-DUMMY6 = None USR-DUMMY7 = None USR-DUMMY8 = None USR-DUMMY9 = None VFLOW-RPM = cuft/hr/rpm F-FACTOR = (lb-cuft)**.5/hr MASS-CYCL = lb/cycle MOLE-CYCL = lbmol/cycle VOLUME-CYCL = cuft/cycle ENTHALPY-CYC = Btu/cycle MASS-OPER = lb/op-hr MOLE-OPER = lbmol/op-hr VOLUME-OPER = cuft/op-hr ENTHALPY-OPR = Btu/op-hr RHO-VSQRD = lb/ft-sqsec SOUND-LEVEL = decibels MOM-INERTIA = lb-sqft VOLTAGE = kvolt CURRENT = mamp MASS-VOLUME = cuft/lb MASS-PER-LEN = lb/ft ENERGY-VOL = bbl/Btu SIEMENS-M = Siemens/ft COST-RATE = $/hr FLUX-HEAT-AR = Btu/hr-sqft FLUX-MOLE = lbmol/sqft-hr HEAT-RATE-V = Btu/hr-cuft MOLE-RXN-RAT = lbmol/cuft-hr MOL-RXN-RATW = lbmol/lb-hr MOLE-PRICE = $/lbmol VOL-HTR-COEF = Btu/hr-cuft-R POWER-AREA = hp/sqft POWER-MASS = hp/lb MASS-EMISSIO = lb/Btu INVERSE-VEL = sec/ft SPEC-MAT-RES = lb/Btu-ft ACCELERATION = ft/sqsec MASS-CONTENT = lb/lb_dry AREA-SQTIME = sqft/sqsec MET Input Unit Set = None User Table User Tree ASKED = 0 BASESET = MET CURRENCY = None DESCRIPTION = Metric Engineering Units Output Unit Set = Prop Data User Table User Tree CC Nodes MAIN = 1 Comments Unit-Types AREA = sqm COMPOSITION = mol-fr DENSITY = gm/cc DIFFUSIVITY = sqcm/sec ENERGY = cal ENTHALPY = cal/mol ENTROPY = cal/mol-K FISCAL = $ FLOW = kg/hr MASS-FLOW = kg/hr MOLE-FLOW = kmol/hr VOLUME-FLOW = l/min ENTHALPY-FLO = cal/sec FORCE = dyne MOLE-HEAT-CA = cal/mol-K HEAT-TRANS-C = cal/sec-sqcm-K LENGTH = meter MASS = kg POWER = kW PRESSURE = atm SURFACE-TENS = dyne/cm TEMPERATURE = K THERMAL-COND = kcal-m/hr-sqm-K TIME = hr VELOCITY = m/sec VISCOSITY = cP VOLUME = l FREQUENCY = rpm UNIT-PRICE = $/kg ENERGY-PRICE = $/cal DELTA-T = K ANGLE = deg HEAD = m-kgf/kg BOND-WORK-IN = kWhr/ton FILTER-RESIS = 1/meter SPEC-FLT-RES = meter/kg MOLE-DENSITY = mol/cc MASS-DENSITY = gm/cc MOLE-ENTHALP = cal/mol MASS-ENTHALP = cal/gm MOLE-ENTROPY = cal/mol-K MASS-ENTROPY = cal/gm-K MOLE-VOLUME = cc/mol DIMENSIONLES = Unitless DIPOLEMOMENT = debye SOLUPARAM = (cal/cc)**.5 ELEC-POWER = kW ELEC-PRICE = $/kWhr MASS-HEAT-CA = cal/gm-K UA = cal/sec-K MOLES = kmol WORK = kW-hr HEAT = cal AREA-PRICE = $/sqm VOLUME-PRICE = $/l ITEM-PRICE = $/item NUM-CONC = no/l MASS-CONC = gm/l INVERSE-TIME = 1/hr LN-INV-TIME = ln(1/hr) FLUX = l/sqm-sec AREA-USAGE = sqm/hr VOLUME-USAGE = l/hr MOLE-CONC = mol/cc POWER-VOLUME = kW/l MASS-TRANS-C = gm/s-sqcm-gm/cc SPECIFICAREA = sqcm/cc INVERSE-LENG = 1/cm CHROM-VEL = cm/hr MASS-FLUX = kg/sqm-hr SOLVENT-PERM = kg/sqm-hr-atm SOLUTE-PERM = sqm/m-hr WATER-RATE = kg/kW-hr PDROP-PER-HT = mm-water/m PDROP = atm PACK-FACTOR = 1/m NUM-CON-RATE = no/l-sec INVERSE-AREA = 1/sqm VOL-HEAT-CAP = cal/cc-K HEAT-FLUX = cal/sec-m INVERSE-TEMP = 1/K INVERSE-PRES = 1/atm TEMP-VOLUME = cc-K/mol VFLOW-LENGTH = sqcm/sec CONTENTS = fraction POP-DENSITY = no/m/l INVERSE-HT-C = sec-sqcm-K/cal VOL-ENTHALPY = cal/cc MOL-FLOW-LEN = kmol/hr-m USR-DUMMY0 = None USR-DUMMY1 = None USR-DUMMY2 = None USR-DUMMY3 = None USR-DUMMY4 = None USR-DUMMY5 = None USR-DUMMY6 = None USR-DUMMY7 = None USR-DUMMY8 = None USR-DUMMY9 = None VFLOW-RPM = l/min/rpm F-FACTOR = (gm-l)**.5/min MASS-CYCL = kg/cycle MOLE-CYCL = kmol/cycle VOLUME-CYCL = l/cycle ENTHALPY-CYC = cal/cycle MASS-OPER = kg/op-hr MOLE-OPER = kmol/op-hr VOLUME-OPER = l/op-min ENTHALPY-OPR = cal/op-sec RHO-VSQRD = kg/m-sqsec SOUND-LEVEL = decibels MOM-INERTIA = kg-sqm VOLTAGE = volt CURRENT = amp MASS-VOLUME = cc/g MASS-PER-LEN = kg/m ENERGY-VOL = bbl/MMBtu SIEMENS-M = Siemens/m COST-RATE = $/hr FLUX-HEAT-AR = cal/sec-sqm FLUX-MOLE = kmol/sqm-hr HEAT-RATE-V = cal/sec-cum MOLE-RXN-RAT = kmol/cum-hr MOL-RXN-RATW = kmol/kg-hr MOLE-PRICE = $/mol VOL-HTR-COEF = cal/sec-cc-K POWER-AREA = kW/sqm POWER-MASS = kW/kg MASS-EMISSIO = kg/cal INVERSE-VEL = sec/cm SPEC-MAT-RES = gm/cal-cm ACCELERATION = m/sqsec MASS-CONTENT = kg/kg_dry AREA-SQTIME = sqm/sqsec METCBAR Input Unit Set = None User Table User Tree ASKED = 1 BASESET = MET CURRENCY = None DESCRIPTION = Metric Units with C, BAR, GCAL/HR, and CUM Output Unit Set = Prop Data User Table User Tree CC Nodes MAIN = 1 Comments Unit-Types AREA = sqm COMPOSITION = mol-fr DENSITY = gm/cc DIFFUSIVITY = sqcm/sec ENERGY = cal ENTHALPY = cal/mol ENTROPY = cal/mol-K FISCAL = $ FLOW = kg/hr MASS-FLOW = kg/hr MOLE-FLOW = kmol/hr VOLUME-FLOW = cum/hr ENTHALPY-FLO = Gcal/hr FORCE = dyne MOLE-HEAT-CA = cal/mol-K HEAT-TRANS-C = kcal/hr-sqm-K LENGTH = meter MASS = kg POWER = kW PRESSURE = bar SURFACE-TENS = dyne/cm TEMPERATURE = C THERMAL-COND = kcal-m/hr-sqm-K TIME = hr VELOCITY = m/sec VISCOSITY = cP VOLUME = cum FREQUENCY = rpm UNIT-PRICE = $/kg ENERGY-PRICE = $/cal DELTA-T = C ANGLE = deg HEAD = meter BOND-WORK-IN = kWhr/ton FILTER-RESIS = 1/meter SPEC-FLT-RES = meter/kg MOLE-DENSITY = kmol/cum MASS-DENSITY = kg/cum MOLE-ENTHALP = kcal/mol MASS-ENTHALP = kcal/kg MOLE-ENTROPY = cal/mol-K MASS-ENTROPY = cal/gm-K MOLE-VOLUME = cc/mol DIMENSIONLES = Unitless DIPOLEMOMENT = debye SOLUPARAM = (cal/cc)**.5 ELEC-POWER = kW ELEC-PRICE = $/kWhr MASS-HEAT-CA = cal/gm-K UA = cal/sec-K MOLES = kmol WORK = kW-hr HEAT = Gcal AREA-PRICE = $/sqm VOLUME-PRICE = $/l ITEM-PRICE = $/item NUM-CONC = no/l MASS-CONC = gm/l INVERSE-TIME = 1/hr LN-INV-TIME = ln(1/hr) FLUX = l/sqm-sec AREA-USAGE = sqm/hr VOLUME-USAGE = l/hr MOLE-CONC = mol/l POWER-VOLUME = kW/l MASS-TRANS-C = gm/s-sqcm-gm/cc SPECIFICAREA = sqcm/cc INVERSE-LENG = 1/cm CHROM-VEL = cm/hr MASS-FLUX = kg/sqm-hr SOLVENT-PERM = kg/sqm-hr-atm SOLUTE-PERM = sqm/m-hr WATER-RATE = kg/kW-hr PDROP-PER-HT = mbar/m PDROP = bar PACK-FACTOR = 1/m NUM-CON-RATE = no/l-sec INVERSE-AREA = 1/sqm VOL-HEAT-CAP = cal/cc-K HEAT-FLUX = cal/sec-m INVERSE-TEMP = 1/K INVERSE-PRES = 1/atm TEMP-VOLUME = cc-K/mol VFLOW-LENGTH = sqcm/sec CONTENTS = fraction POP-DENSITY = no/m/l INVERSE-HT-C = sec-sqcm-K/cal VOL-ENTHALPY = cal/cc MOL-FLOW-LEN = kmol/hr-m USR-DUMMY0 = None USR-DUMMY1 = None USR-DUMMY2 = None USR-DUMMY3 = None USR-DUMMY4 = None USR-DUMMY5 = None USR-DUMMY6 = None USR-DUMMY7 = None USR-DUMMY8 = None USR-DUMMY9 = None VFLOW-RPM = l/min/rpm F-FACTOR = (gm-l)**.5/min MASS-CYCL = kg/cycle MOLE-CYCL = kmol/cycle VOLUME-CYCL = l/cycle ENTHALPY-CYC = cal/cycle MASS-OPER = kg/op-hr MOLE-OPER = kmol/op-hr VOLUME-OPER = l/op-min ENTHALPY-OPR = cal/op-sec RHO-VSQRD = kg/m-sqsec SOUND-LEVEL = decibels MOM-INERTIA = kg-sqm VOLTAGE = None CURRENT = None MASS-VOLUME = cc/g MASS-PER-LEN = kg/m ENERGY-VOL = bbl/MMBtu SIEMENS-M = Siemens/m COST-RATE = $/hr FLUX-HEAT-AR = cal/sec-sqm FLUX-MOLE = kmol/sqm-hr HEAT-RATE-V = cal/sec-cum MOLE-RXN-RAT = kmol/cum-hr MOL-RXN-RATW = kmol/kg-hr MOLE-PRICE = $/mol VOL-HTR-COEF = cal/sec-cc-K POWER-AREA = kW/sqm POWER-MASS = kW/kg MASS-EMISSIO = kg/cal INVERSE-VEL = sec/cm SPEC-MAT-RES = gm/cal-cm ACCELERATION = m/sqsec MASS-CONTENT = kg/kg_dry AREA-SQTIME = sqm/sqsec METCKGCM Input Unit Set = None User Table User Tree ASKED = 1 BASESET = MET CURRENCY = None DESCRIPTION = Metric Units with C, KG/SQCM, GCAL/HR, and CUM Output Unit Set = Prop Data User Table User Tree CC Nodes MAIN = 1 Comments Unit-Types AREA = sqm COMPOSITION = mol-fr DENSITY = gm/cc DIFFUSIVITY = sqcm/sec ENERGY = cal ENTHALPY = cal/mol ENTROPY = cal/mol-K FISCAL = $ FLOW = kg/hr MASS-FLOW = kg/hr MOLE-FLOW = kmol/hr VOLUME-FLOW = cum/hr ENTHALPY-FLO = Gcal/hr FORCE = dyne MOLE-HEAT-CA = cal/mol-K HEAT-TRANS-C = kcal/hr-sqm-K LENGTH = meter MASS = kg POWER = kW PRESSURE = kg/sqcm SURFACE-TENS = dyne/cm TEMPERATURE = C THERMAL-COND = kcal-m/hr-sqm-K TIME = hr VELOCITY = m/sec VISCOSITY = cP VOLUME = cum FREQUENCY = rpm UNIT-PRICE = $/kg ENERGY-PRICE = $/cal DELTA-T = C ANGLE = deg HEAD = meter BOND-WORK-IN = kWhr/ton FILTER-RESIS = 1/meter SPEC-FLT-RES = meter/kg MOLE-DENSITY = mol/cc MASS-DENSITY = gm/cc MOLE-ENTHALP = kcal/mol MASS-ENTHALP = kcal/kg MOLE-ENTROPY = cal/mol-K MASS-ENTROPY = cal/gm-K MOLE-VOLUME = cc/mol DIMENSIONLES = Unitless DIPOLEMOMENT = debye SOLUPARAM = (cal/cc)**.5 ELEC-POWER = kW ELEC-PRICE = $/kWhr MASS-HEAT-CA = cal/gm-K UA = cal/sec-K MOLES = kmol WORK = kW-hr HEAT = Gcal AREA-PRICE = $/sqm VOLUME-PRICE = $/l ITEM-PRICE = $/item NUM-CONC = no/l MASS-CONC = gm/l INVERSE-TIME = 1/hr LN-INV-TIME = ln(1/hr) FLUX = l/sqm-sec AREA-USAGE = sqm/hr VOLUME-USAGE = l/hr MOLE-CONC = mol/l POWER-VOLUME = kW/l MASS-TRANS-C = gm/s-sqcm-gm/cc SPECIFICAREA = sqcm/cc INVERSE-LENG = 1/cm CHROM-VEL = cm/hr MASS-FLUX = kg/sqm-hr SOLVENT-PERM = kg/sqm-hr-atm SOLUTE-PERM = sqm/m-hr WATER-RATE = kg/kW-hr PDROP-PER-HT = mbar/m PDROP = kg/sqcm PACK-FACTOR = 1/m NUM-CON-RATE = no/l-sec INVERSE-AREA = 1/sqm VOL-HEAT-CAP = cal/cc-K HEAT-FLUX = cal/sec-m INVERSE-TEMP = 1/K INVERSE-PRES = 1/atm TEMP-VOLUME = cc-K/mol VFLOW-LENGTH = sqcm/sec CONTENTS = fraction POP-DENSITY = no/m/l INVERSE-HT-C = sec-sqcm-K/cal VOL-ENTHALPY = cal/cc MOL-FLOW-LEN = kmol/hr-m USR-DUMMY0 = None USR-DUMMY1 = None USR-DUMMY2 = None USR-DUMMY3 = None USR-DUMMY4 = None USR-DUMMY5 = None USR-DUMMY6 = None USR-DUMMY7 = None USR-DUMMY8 = None USR-DUMMY9 = None VFLOW-RPM = l/min/rpm F-FACTOR = (gm-l)**.5/min MASS-CYCL = kg/cycle MOLE-CYCL = kmol/cycle VOLUME-CYCL = l/cycle ENTHALPY-CYC = cal/cycle MASS-OPER = kg/op-hr MOLE-OPER = kmol/op-hr VOLUME-OPER = l/op-min ENTHALPY-OPR = cal/op-sec RHO-VSQRD = kg/m-sqsec SOUND-LEVEL = decibels MOM-INERTIA = kg-sqm VOLTAGE = None CURRENT = None MASS-VOLUME = cc/g MASS-PER-LEN = kg/m ENERGY-VOL = bbl/MMBtu SIEMENS-M = Siemens/m COST-RATE = $/hr FLUX-HEAT-AR = cal/sec-sqm FLUX-MOLE = kmol/sqm-hr HEAT-RATE-V = cal/sec-cum MOLE-RXN-RAT = kmol/cum-hr MOL-RXN-RATW = kmol/kg-hr MOLE-PRICE = $/mol VOL-HTR-COEF = cal/sec-cc-K POWER-AREA = kW/sqm POWER-MASS = kW/kg MASS-EMISSIO = kg/cal INVERSE-VEL = sec/cm SPEC-MAT-RES = gm/cal-cm ACCELERATION = m/sqsec MASS-CONTENT = kg/kg_dry AREA-SQTIME = sqm/sqsec SI Input Unit Set = None User Table User Tree ASKED = 0 BASESET = SI CURRENCY = None DESCRIPTION = International System Units Output Unit Set = Prop Data User Table User Tree CC Nodes MAIN = 1 Comments Unit-Types AREA = sqm COMPOSITION = mol-fr DENSITY = kg/cum DIFFUSIVITY = sqm/sec ENERGY = J ENTHALPY = J/kmol ENTROPY = J/kmol-K FISCAL = $ FLOW = kg/sec MASS-FLOW = kg/sec MOLE-FLOW = kmol/sec VOLUME-FLOW = cum/sec ENTHALPY-FLO = Watt FORCE = Newton MOLE-HEAT-CA = J/kmol-K HEAT-TRANS-C = Watt/sqm-K LENGTH = meter MASS = kg POWER = Watt PRESSURE = N/sqm SURFACE-TENS = N/m TEMPERATURE = K THERMAL-COND = Watt/m-K TIME = sec VELOCITY = m/sec VISCOSITY = N-sec/sqm VOLUME = cum FREQUENCY = Hz UNIT-PRICE = $/kg ENERGY-PRICE = $/J DELTA-T = K ANGLE = rad HEAD = J/kg BOND-WORK-IN = J/kg FILTER-RESIS = 1/meter SPEC-FLT-RES = meter/kg MOLE-DENSITY = kmol/cum MASS-DENSITY = kg/cum MOLE-ENTHALP = J/kmol MASS-ENTHALP = J/kg MOLE-ENTROPY = J/kmol-K MASS-ENTROPY = J/kg-K MOLE-VOLUME = cum/kmol DIMENSIONLES = Unitless DIPOLEMOMENT = (J*cum)**.5 SOLUPARAM = (J/cum)**.5 ELEC-POWER = Watt ELEC-PRICE = $/J MASS-HEAT-CA = J/kg-K UA = J/sec-K MOLES = kmol WORK = J HEAT = J AREA-PRICE = $/sqm VOLUME-PRICE = $/cum ITEM-PRICE = $/item NUM-CONC = no/cum MASS-CONC = kg/cum INVERSE-TIME = 1/sec LN-INV-TIME = ln(1/sec) FLUX = cum/sqm-sec AREA-USAGE = sqm/sec VOLUME-USAGE = cum/sec MOLE-CONC = kmol/cum POWER-VOLUME = Watt/cum MASS-TRANS-C = kg/s-sqm-kg/cum SPECIFICAREA = sqm/cum INVERSE-LENG = 1/m CHROM-VEL = m/sec MASS-FLUX = kg/sqm-s SOLVENT-PERM = kg/sqm-s-Pa SOLUTE-PERM = sqm/m-s WATER-RATE = kg/J PDROP-PER-HT = N/cum PDROP = N/sqm PACK-FACTOR = 1/m NUM-CON-RATE = no/cum-sec INVERSE-AREA = 1/sqm VOL-HEAT-CAP = J/cum-K HEAT-FLUX = Watt/m INVERSE-TEMP = 1/K INVERSE-PRES = sqm/N TEMP-VOLUME = cum-K/kmol VFLOW-LENGTH = sqm/sec CONTENTS = fraction POP-DENSITY = no/m/cum INVERSE-HT-C = sqm-K/Watt VOL-ENTHALPY = J/cum MOL-FLOW-LEN = kmol/sec-m USR-DUMMY0 = base-units USR-DUMMY1 = base-units USR-DUMMY2 = base-units USR-DUMMY3 = base-units USR-DUMMY4 = base-units USR-DUMMY5 = base-units USR-DUMMY6 = base-units USR-DUMMY7 = base-units USR-DUMMY8 = base-units USR-DUMMY9 = base-units VFLOW-RPM = cum/sec/rpm F-FACTOR = (kg-cum)**.5/sec MASS-CYCL = kg/cycle MOLE-CYCL = kmol/cycle VOLUME-CYCL = cum/cycle ENTHALPY-CYC = Watt/cycle MASS-OPER = kg/op-sec MOLE-OPER = kmol/op-sec VOLUME-OPER = cum/op-sec ENTHALPY-OPR = Watt/cycle RHO-VSQRD = kg/m-sqsec SOUND-LEVEL = decibels MOM-INERTIA = kg-sqm VOLTAGE = volt CURRENT = amp MASS-VOLUME = cum/kg MASS-PER-LEN = kg/m ENERGY-VOL = cum/J SIEMENS-M = Siemens/m COST-RATE = $/sec FLUX-HEAT-AR = Watt/sqm FLUX-MOLE = kmol/sqm-s HEAT-RATE-V = Watt/cum MOLE-RXN-RAT = kmol/cum-s MOL-RXN-RATW = kmol/kg-s MOLE-PRICE = $/kmol VOL-HTR-COEF = Watt/cum-K POWER-AREA = Watt/sqm POWER-MASS = Watt/kg MASS-EMISSIO = kg/J INVERSE-VEL = sec/m SPEC-MAT-RES = kg/J-m ACCELERATION = m/sqsec MASS-CONTENT = kg/kg_dry AREA-SQTIME = sqm/sqsec SI-CBAR Input Unit Set = None User Table User Tree ASKED = 1 BASESET = SI CURRENCY = None DESCRIPTION = International System Units with C, BAR, and /HR Output Unit Set = Prop Data User Table User Tree CC Nodes MAIN = 1 Comments Unit-Types AREA = sqm COMPOSITION = mol-fr DENSITY = kg/cum DIFFUSIVITY = sqm/sec ENERGY = J ENTHALPY = J/kmol ENTROPY = J/kmol-K FISCAL = $ FLOW = kg/sec MASS-FLOW = kg/hr MOLE-FLOW = kmol/hr VOLUME-FLOW = cum/hr ENTHALPY-FLO = Watt FORCE = Newton MOLE-HEAT-CA = J/kmol-K HEAT-TRANS-C = Watt/sqm-K LENGTH = meter MASS = kg POWER = Watt PRESSURE = bar SURFACE-TENS = N/m TEMPERATURE = C THERMAL-COND = Watt/m-K TIME = sec VELOCITY = m/sec VISCOSITY = N-sec/sqm VOLUME = cum FREQUENCY = Hz UNIT-PRICE = $/kg ENERGY-PRICE = $/J DELTA-T = C ANGLE = rad HEAD = J/kg BOND-WORK-IN = J/kg FILTER-RESIS = 1/meter SPEC-FLT-RES = meter/kg MOLE-DENSITY = kmol/cum MASS-DENSITY = kg/cum MOLE-ENTHALP = J/kmol MASS-ENTHALP = J/kg MOLE-ENTROPY = J/kmol-K MASS-ENTROPY = J/kg-K MOLE-VOLUME = cum/kmol DIMENSIONLES = Unitless DIPOLEMOMENT = (J*cum)**.5 SOLUPARAM = (J/cum)**.5 ELEC-POWER = Watt ELEC-PRICE = $/J MASS-HEAT-CA = J/kg-K UA = J/sec-K MOLES = kmol WORK = J HEAT = J AREA-PRICE = $/sqm VOLUME-PRICE = $/cum ITEM-PRICE = $/item NUM-CONC = no/cum MASS-CONC = kg/cum INVERSE-TIME = 1/sec LN-INV-TIME = ln(1/sec) FLUX = cum/sqm-sec AREA-USAGE = sqm/sec VOLUME-USAGE = cum/sec MOLE-CONC = kmol/cum POWER-VOLUME = Watt/cum MASS-TRANS-C = kg/s-sqm-kg/cum SPECIFICAREA = sqm/cum INVERSE-LENG = 1/m CHROM-VEL = m/sec MASS-FLUX = kg/sqm-s SOLVENT-PERM = kg/sqm-s-Pa SOLUTE-PERM = sqm/m-s WATER-RATE = kg/J PDROP-PER-HT = mbar/m PDROP = bar PACK-FACTOR = 1/m NUM-CON-RATE = no/cum-sec INVERSE-AREA = 1/sqm VOL-HEAT-CAP = J/cum-K HEAT-FLUX = Watt/m INVERSE-TEMP = 1/K INVERSE-PRES = sqm/N TEMP-VOLUME = cum-K/kmol VFLOW-LENGTH = sqm/sec CONTENTS = fraction POP-DENSITY = no/m/cum INVERSE-HT-C = sqm-K/Watt VOL-ENTHALPY = J/cum MOL-FLOW-LEN = kmol/sec-m USR-DUMMY0 = base-units USR-DUMMY1 = base-units USR-DUMMY2 = base-units USR-DUMMY3 = base-units USR-DUMMY4 = base-units USR-DUMMY5 = base-units USR-DUMMY6 = base-units USR-DUMMY7 = base-units USR-DUMMY8 = base-units USR-DUMMY9 = base-units VFLOW-RPM = cum/sec/rpm F-FACTOR = (kg-cum)**.5/sec MASS-CYCL = kg/cycle MOLE-CYCL = kmol/cycle VOLUME-CYCL = cum/cycle ENTHALPY-CYC = Watt/cycle MASS-OPER = kg/op-sec MOLE-OPER = kmol/op-sec VOLUME-OPER = cum/op-sec ENTHALPY-OPR = Watt/cycle RHO-VSQRD = kg/m-sqsec SOUND-LEVEL = decibels MOM-INERTIA = kg-sqm VOLTAGE = volt CURRENT = amp MASS-VOLUME = cum/kg MASS-PER-LEN = kg/m ENERGY-VOL = cum/J SIEMENS-M = Siemens/m COST-RATE = $/sec FLUX-HEAT-AR = Watt/sqm FLUX-MOLE = kmol/sqm-s HEAT-RATE-V = Watt/cum MOLE-RXN-RAT = kmol/cum-s MOL-RXN-RATW = kmol/kg-s MOLE-PRICE = $/kmol VOL-HTR-COEF = Watt/cum-K POWER-AREA = Watt/sqm POWER-MASS = Watt/kg MASS-EMISSIO = kg/J INVERSE-VEL = sec/m SPEC-MAT-RES = kg/J-m ACCELERATION = m/sqsec MASS-CONTENT = kg/kg_dry AREA-SQTIME = sqm/sqsec Account-Info Input Unit Set = None User Table User Tree ACCOUNT = None PROJECT_ID = None PROJECT_NAME = None USER_NAME = None Output Unit Set = Prop Data User Table User Tree CC Nodes ACINFOFLAG = 0 ENTACCOUN = 0 MAIN1 = 1 Comments Diagnostics Input Unit Set = None User Table User Tree CONV_LEVEL = 4 COST_LEVEL = 4 ECON_LEVEL = 4 INSERT = YES PROP_LEVEL = 4 PROP_LIMIT = 200 SIM_LEVEL = 4 SIM_LIMIT = 200 SORTED = YES STREAM_LEVEL = 4 SYS_LEVEL = 4 SYS_LIMIT = 200 TVAR_LEVEL = 4 T_CONV_LEVEL = 4 T_COST_LEVEL = 4 T_ECON_LEVEL = 4 T_PROP_LEVEL = 4 T_SIM_LEVEL = 4 T_STRM_LEVEL = 4 T_SYS_LEVEL = 4 VAR_LEVEL = 4 Output Unit Set = Prop Data User Table User Tree CC Nodes ENTDIAG = 0 ENTMAX = 0 Comments Sim-Options Input Unit Set = ENG User Table User Tree ATM_PRES = 14.69594878 BYPASS_PROP = YES CARBON_FEE = 0.0 DESCRIPTION = None DN_REQUIRED = YES DUMPXML = NO DX_REQUIRED = NO ELEC_CHK_TOL = 0.0001 ENERGY_BAL = YES ENG_ELECPAR = YES FLASH3_OPT = 3PHASE FLASH_METHOD = None FLASH_PSEUDO = ERROR FREE_WATER = NO GAMMA_BASIS = UNSYMMETRIC GAMUS_BASIS = MIXED-SOLVENT GHG_STANDARD = IPCC-2007 HF_FL3_DAMP = None MASS_BAL_CHE = YES MASS_BAL_TOL = 0.0001 MAXIT = 30 MAXSOL_CHECK = YES MW_CALC = YES NEW_SPLIT = YES NPHASE = None NPHASE_AC = 1 NPHASE_CR = 2 NPHASE_FL = 2 NPHASE_HI = 2 NPHASE_MC = None NPHASE_RB = 1 OLD_DATABANK = NO OPER_YEAR = 8766.0 PACKING_DB = LATEST PACK_FLOW = 1e-15 PACK_FRAC = 1e-15 PARADIGM = SM PEQ_CHECK = NONE PEQ_CHK_FRAC = 1e-15 PEQ_CHK_TOL = 0.0001 PHASE = None PHASE_HI = None PHASE_RB = L PHASE_RC = V PLANT_LIFE = None PLOWER = 0.0 PROP_DERIV = ANALYTICAL PUPPER = 1450377.38 REF_PRES = 14.69594878 REF_TEMP = 77.0 RESTART = NO ROOT_EXTR = 0.1 SCENARIO = None SOLID_DERIV = YES STARTUP = None START_DAY = None START_MONTH = None START_YEAR = None STOIC_MB_CHE = ERROR STOIC_MB_TOL = 1.0 TEMPLATE = None TLOWER = -441.67 TOL = 0.0001 TUPPER = 17540.33 UTL_REQD = NO VAPOR = YES VLE_CHECK = NONE VLLE_CHECK = NONE XW_H2OPHASE = 0.98 Output Unit Set = Prop Data User Table User Tree CC Nodes COSTOP = 1 ENTCALC = 0 ENTCOSTOP = 0 ENTFLASH = 0 ENTPHASE = 0 ENTREAC = 0 ENTRESL = 0 ENTSMETH = 0 ENTSMLIM = 0 GLOBL = 1 MAIN = 1 MASSCK = 1 NOPYR = 1 SOLUMETH = 0 Comments Sys-Options Input Unit Set = None User Table User Tree BLOCK_CHECK = YES INTERPRET = YES TRACE = NO Output Unit Set = Prop Data User Table User Tree CC Nodes ENTSYSTEM = 0 Comments Run-Control Input Unit Set = None User Table User Tree MAX_ERRORS = 50 MAX_FORT_ERR = 100 MAX_TIME = None Output Unit Set = Prop Data User Table User Tree CC Nodes ENTLIMIT = 0 Comments Stream-Class Subs-Attr PSD Input Unit Set = ENG User Table User Tree CHANGED = 0 DESCRIPTION = None GMESH = NO INTERVAL #0 = 1 #1 = 2 #2 = 3 #3 = 4 #4 = 5 #5 = 6 #6 = 7 #7 = 8 #8 = 9 #9 = 10 INTERVALS = 10 LOWER = None PARTICLESIZ2 #0 = 20.0 #1 = 40.0 #2 = 60.0 #3 = 80.0 #4 = 100.0 #5 = 120.0 #6 = 140.0 #7 = 160.0 #8 = 180.0 #9 = 200.0 PARTICLESIZE #0 = 0.0 #1 = 20.0 #2 = 40.0 #3 = 60.0 #4 = 80.0 #5 = 100.0 #6 = 120.0 #7 = 140.0 #8 = 160.0 #9 = 180.0 TYPE = USER UPPER = None Output Unit Set = Prop Data User Table User Tree CC Nodes ATTRE = 1 CMESH = 0 EXINT = 1 EXINT1 = 1 LIMIT = 1 LOWERLIMIT1 = 1 LOWERLIMIT2 = 1 MESHLOWER #0 = 1 #1 = 1 #2 = 1 #3 = 1 #4 = 1 #5 = 1 #6 = 1 #7 = 1 #8 = 1 #9 = 1 MESHUPPER #0 = 1 #1 = 1 #2 = 1 #3 = 1 #4 = 1 #5 = 1 #6 = 1 #7 = 1 #8 = 1 #9 = 1 MN1 = 1 UPPERLIMIT1 = 1 UPPERLIMIT2 = 1 USER = 1 Comments Substreams Input Unit Set = None User Table User Tree ATTRIBUTES MIXED = None CISOLID = None NC = None NCPSD = PSD CIPSD = PSD CHANGED MIXED = None CISOLID = None NC = None NCPSD = None CIPSD = None FLAG MIXED = 1 CISOLID = 1 NC = 1 NCPSD = 2 CIPSD = 2 TYPE MIXED = MIXED CISOLID = CISOLID NC = NC NCPSD = NC CIPSD = CISOLID Output Unit Set = Prop Data User Table User Tree CC Nodes MN2 = 1 SUBSE MIXED = 0 CISOLID = 0 NC = 0 NCPSD = 0 CIPSD = 0 Comments Stream-Class Input Unit Set = None User Table User Tree CHANGED CONVEN = None MIXNC = None MIXCISLD = None MIXNCPSD = None MIXCIPSD = None MIXCINC = None MCINCPSD = None FLAG CONVEN = 1 MIXNC = 1 MIXCISLD = 1 MIXNCPSD = 1 MIXCIPSD = 1 MIXCINC = 1 MCINCPSD = 1 STREAM_ATTR HEAT = HEAT LOAD = LOAD SUBSTREAMS CONVEN #0 = MIXED MIXNC #0 = MIXED #1 = NC MIXCISLD #0 = MIXED #1 = CISOLID MIXNCPSD #0 = MIXED #1 = NCPSD MIXCIPSD #0 = MIXED #1 = CIPSD MIXCINC #0 = MIXED #1 = CISOLID #2 = NC MCINCPSD #0 = MIXED #1 = CIPSD #2 = NCPSD Output Unit Set = Prop Data User Table User Tree CC Nodes FIRSTMIXED CONVEN = 1 MIXNC = 1 MIXCISLD = 1 MIXNCPSD = 1 MIXCIPSD = 1 MIXCINC = 1 MCINCPSD = 1 HEATDEF HEAT = 1 LOAD = 1 LATERMIXED CONVEN = 1 MIXNC = 1 MIXCISLD = 1 MIXNCPSD = 1 MIXCIPSD = 1 MIXCINC = 1 MCINCPSD = 1 MN3 = 1 MN4 CONVEN = 1 MIXNC = 1 MIXCISLD = 1 MIXNCPSD = 1 MIXCIPSD = 1 MIXCINC = 1 MCINCPSD = 1 MN5 HEAT = 1 LOAD = 1 STRCLE CONVEN = 1 MIXNC = 1 MIXCISLD = 1 MIXNCPSD = 1 MIXCIPSD = 1 MIXCINC = 1 MCINCPSD = 1 Comments Stream-Attributes HEAT Input Unit Set = ENG User Table User Tree CHANGED = 0 DESCRIPTION = None NPOINT = 0 Output Unit Set = Prop Data User Table User Tree CC Nodes ENTNPOINT = 0 HEATLOAD = 1 HEATLOAD1 = 1 MN1 = 1 Comments LOAD Input Unit Set = ENG User Table User Tree CHANGED = 0 DESCRIPTION = None NPOINT = 20 Output Unit Set = Prop Data User Table User Tree CC Nodes ENTNPOINT = 0 HEATLOAD = 1 HEATLOAD1 = 1 MN1 = 1 Comments Description Input Unit Set = None User Table User Tree DESCRIP #0 = General Simulation with English Units : #1 = F, psi, lb/hr, lbmol/hr, Btu/hr, cuft/hr. #2 = #3 = Property Method: None #4 = #5 = Flow basis for input: Mole #6 = #7 = Stream report composition: Mole flow Output Unit Set = Prop Data User Table User Tree CC Nodes ENTDESC = 1 Comments Custom-Uom Input Unit Set = None User Table User Tree BASE_UNIT COLNO CUSTOM_UNIT MULTIPLIER OFFSET PHYS_QTY Output Unit Set = Prop Data User Table User Tree CC Nodes CURRENCY ENTN SPEC UNIT1 UNIT2 Comments ReportOptions Report Input Unit Set = None User Table User Tree ADA = ADA BLOCKS = BLOCKS COSTBLOCK = COSTBLOCK ECONOMIC = ECONOMIC FLOWSHEET = FLOWSHEET INPUT = NOINPUT INSERT = INSERT LINES = 60 PROPERTIES = PROPERTIES REPORT = REPORT SENSITIVITY = SENSITIVITY STREAMS = STREAMS UNITS = UNITS UTILITIES = UTILITIES Output Unit Set = Prop Data User Table User Tree CC Nodes ADA = 1 BLOCK = 1 ENTGLOB = 0 FLOWS = 1 GLOB = 1 PROP = 1 STRM = 1 SUPP = 1 Comments Block-Report Input Unit Set = None User Table User Tree COMPBAL = NOCOMPBAL EXCL_BLOCKS INCL_BLOCKS INPUT = INPUT NEWPAGE = NONEWPAGE REPORT = REPORT RESULTS = RESULTS SORT = SORT TOTBAL = TOTBAL Output Unit Set = Prop Data User Table User Tree CC Nodes ENTBLOCK = 0 EXCLD = 1 INCLD = 1 Comments Stream-Report Input Unit Set = None User Table User Tree ATTR_DESC = ATTR-DESC BPS_REPORT = NOBPS-REP COMP_ATTR = COMP-ATTR EXCL_STREAMS GLOBAL_PROPS HEADING INCL_STREAMS MASSFLOW = MASSFLOW MASSFRAC = MASSFRAC MOLEFLOW = MOLEFLOW MOLEFRAC = MOLEFRAC NAMES = NAMES PROPERTIES REPORT = REPORT SORT = SORT STDVOLFLOW = NOVOLFLOW STDVOLFRAC = NOVOLFRAC STRUCTURE = NOSTRUCTURE SUBROUTINE SUBS_ATTR = SUBS-ATTR SUPP_EXCL_ST SUPP_INCL_ST SUPP_PROPS SUPP_REPORT SUPP_SORT SUPP_WIDE SUP_MASSFLOW SUP_MASSFRAC SUP_MOLEFLOW SUP_MOLEFRAC SUP_ZEROFLOW S_ATTR_DESC S_COMP_ATTR S_STDVOLFLOW S_STDVOLFRAC S_STRUCTURE S_SUBS_ATTR WIDE = NARROW ZEROFLOW = ZEROFLOW Output Unit Set = Prop Data User Table User Tree CC Nodes ENTSTRM = 1 EXCLD = 1 INCLD = 1 STRM = 1 SUPP Comments Flowsheet-Report Input Unit Set = None User Table User Tree COMPBAL = COMPBAL CONSTRAINT = CONSTRAINT CONVERGENCE = CONVERGENCE DESCRIPTION = DESCRIPTION DESIGN_SPEC = DESIGN-SPEC FORTRAN = FORTRAN OPTIMIZATION = OPTIMIZATION SEQUENCE = SEQUENCE TOTBAL = TOTBAL TRANSFER = TRANSFER Output Unit Set = Prop Data User Table User Tree CC Nodes ENTFLOWS = 0 Comments Property-Report Input Unit Set = None User Table User Tree COMPS = COMPS DFMS = NODFMS NEUTRAL = NONEUTRAL PARAMS = NOPARAMS PARPLUS = NOPARAM-PLUS PCES = NOPCES PROJECT = NOPROJECT PROP_DATA = NOPROP-DATA Output Unit Set = Prop Data User Table User Tree CC Nodes ENTPROP = 0 NOTPCES = 1 PARA = 1 Comments ADA-Report Input Unit Set = None User Table User Tree COMPS = COMPS CURVES = CURVES PARAMS = NOPARAMS Output Unit Set = Prop Data User Table User Tree CC Nodes ENTADA = 0 Comments Batch-Operation Input Unit Set = ENG User Table User Tree CYCLE_TIME DOWN_TIME NTRAIN OP_TIME Output Unit Set = Prop Data User Table User Tree CC Nodes SPEC = 1 Comments Stream-Names Input Unit Set = None User Table User Tree TEXT Output Unit Set = Prop Data User Table User Tree CC Nodes ENTSTREAM SPEC Comments Currency Input Unit Set = None User Table User Tree FACTOR Output Unit Set = Prop Data User Table User Tree CC Nodes ENTN SPEC Comments Stream-Price Input Unit Set = ENG User Table User Tree DESCRIPTION = None DESTBLK HIER_STREAM = YES PRICE SOURCEBLK Output Unit Set = Prop Data User Table User Tree BLKSTAT = None COST MASS_PRICE MOLE_PRICE PROPSTAT = None STDVOL_PRICE VOL_PRICE CC Nodes ENTN SPEC Comments Pure Databanks Input Unit Set = None User Table User Tree FILE_SYM_NAM #0 = APV80 PURE27 #1 = APV80 AQUEOUS #2 = APV80 SOLIDS #3 = APV80 INORGANIC PASSWORD = None Output Unit Set = Prop Data User Table User Tree CC Nodes COMPDBANK = 1 ENTDBANK = 1 Comments Other Databanks Input Unit Set = None User Table User Tree AUTO_PARAM = YES FILE_SYM_NAM PASSWORD = None Output Unit Set = Prop Data User Table User Tree CC Nodes LOADPURE = 1 REVIEW = 1 Comments Components Specifications Input Unit Set = None User Table User Tree ANAME WATER = H2O ETHANOL = C2H6O-2 ANAME1 WATER = H2O ETHANOL = C2H6O-2 ASSAYID BLENDID CASN WATER = 7732-18-5 ETHANOL = 64-17-5 CHARGE WATER = 0 ETHANOL = 0 DBNAME WATER = WATER ETHANOL = ETHANOL DBNAME1 WATER = WATER ETHANOL = ETHANOL MAXIT = 30 NONCONVID OUTNAME WATER = WATER ETHANOL = ETHANOL PSEUDOCOMPID TYPE WATER = CONV ETHANOL = CONV Output Unit Set = Prop Data User Table User Tree ALIAS 1 = H2O 2 = C2H6O-2 COMPID 1 = WATER 2 = ETHANOL COMPTYPE 1 = C 2 = C FORMULA 1 = H2O 2 = C2H6O-2 REPNAME 1 = WATER 2 = ETHANOL CC Nodes ENTNC = 0 ENTPET = 0 ISN WATER = 0 ETHANOL = 0 MAIN = 1 NOTADA = 1 NUMUSRPP = 1 UNIQ = 1 UNIQUE = 1 WATOK = 1 Comments Assay/Blend LightEndProperties Input Unit Set = ENG User Table User Tree DESCRIPTION = None PROP_BASIS PROP_VALUE Output Unit Set = Prop Data User Table User Tree CC Nodes AAAAA = 1 CISINASY CPLEPROP HASBASIS LEPIS1STP PISINASY UNLEPPBAS UNLEPROP Comments PetroCharacterization Generation Analysis Options Assay Procedures Input Unit Set = None User Table User Tree D1160_METH = API63 D2887_METH = API94 D86_METH = EDMISTER EP = 99.0 EXTRAP_METH = PROBABILITY IBP = 0.5 MW_INTGR_H = 0.1 PROCEDURE = REL9 SPLINE_FIT = HARWELL TBP_GEN = ASPEN Output Unit Set = Prop Data User Table User Tree CC Nodes ADA = 1 ADAADV = 0 ADAOPT = 0 PROCA = 1 PROCB = 0 Comments Blend Options Input Unit Set = None User Table User Tree BLEND_METHOD BLEND_OPTION EXTRAPOLATE PROP_NAME Output Unit Set = Prop Data User Table User Tree CC Nodes PPROP = 1 PPROPOPT = 0 Comments Properties Pseudocomponents Specifications Input Unit Set = ENG User Table User Tree API GRAV GRAVTYPE = GRAV LDEN MW NBP PCOPSETNAME VIEWLAYOUT = BASIC Output Unit Set = Prop Data User Table User Tree CC Nodes DISABLE = 0 GENAPI = 0 GENDEN = 0 GENSG = 1 MAIN = 1 OPTIONA = 0 OPTIONB = 1 OPT_DEN = 0 Comments Properties Input Unit Set = ENG User Table User Tree MTEMP TEMP VALUE VISC VITEMP VP WSOL Output Unit Set = Prop Data User Table User Tree CC Nodes CPPROP ENPP NOUSRPROP = 0 SOLU = 1 SOLU2 UNPP VAPOR = 1 VAPOR2 VICOMP VIOPT = 0 VIOPT2 VISC = 1 VISC2 VPCOMP VPOPT = 0 VPOPT2 WSCOMP WSOPT = 0 WSOPT2 Comments Attr-Comps Input Unit Set = None User Table User Tree NTBSYM TYPE_LIST Output Unit Set = Prop Data User Table User Tree CC Nodes ENTSPEC MAIN = 1 Comments Henry-Comps Moisture-Comps Input Unit Set = None User Table User Tree COMP Output Unit Set = Prop Data User Table User Tree CC Nodes ENTSELE = 0 Comments UNIFAC-Groups Input Unit Set = None User Table User Tree DESCRIPTION = None GROUPNO Output Unit Set = Prop Data User Table User Tree CC Nodes ENTSELE GR = 1 Comments Comp-Groups Comp-Lists GLOBAL Input Unit Set = None User Table User Tree CID #0 = WATER #1 = ETHANOL DESCRIPTION = None Output Unit Set = Prop Data User Table User Tree CC Nodes ENTCID = 0 NOTFLOWSHEETRUN2 = 0 OVERALL = 1 Comments Polymers Input Unit Set = None User Table User Tree ATT_LISTC ATT_LISTP BEGIN BR3ID BR4ID CAT_GROUP DISPLAY DISTTYPE END ENDID FUNCLOG MODIFIED MXSITE NCATS = None NENDS = None NOLIGS = None NPOINTS NPOLYS = None NSEGS = None NSITES = None NTBSYMC NTBSYMP NUMBER N_BIFUN_INIT = None OCNT OPT_ATTR REPID SCNT SEG_TYPE SITCOM = CATALYST SQBEG SQEND SQSNO UPPER Output Unit Set = Prop Data User Table User Tree CC Nodes ACCSEGD = 0 CAID = 1 CAID1 CAID2 CATT CATT2 CATT3 = 1 CATTS DISTRI DUM = 0 ENTCAT ENTDIS ENTOLI ENTPOL ENTSEG EXOLI EXPOL = 0 GMOD HASDPN HASFMOM HASSFLOW HASSFRAC HASZMOM OLID = 1 OLID1 OPTSC1 = 0 OPTSCO = 1 PID = 1 POLYENABLED = 1 SEGS = 1 SEQNC Comments Attr-Scaling Input Unit Set = ENG User Table User Tree SCALE UPPER Output Unit Set = Prop Data User Table User Tree CC Nodes ENTSC EXIST MAIN = 1 Comments Properties Specifications Input Unit Set = None User Table User Tree BASEOPSET BOPSETNAME CHEMISTRY EOSSETNO FMODIFY FREE_WATER GBASEOPSET = PENG-ROB GCHEMISTRY = None GEOSSETNO = 1 GFREE_WATER = STEAM-TA GHEATOFMIX = NO GHEN = None GISEOS = 1 GLGAMMASETNO = None GLIQDENSITY = VLMX20 GLIQENTHALPY = HLMX106 GLIQGAMMA = None GLIQREFSTATE = NO GMODIFY = NO GOPSETNAME = PENG-ROB GPOYNTING = NO GPPROCTYPE = COMMON GSOLU_WATER = 3 GTRUE_COMPS = YES GVAPOREOS = ESPRSTD HEATOFMIX H_COMPS ISEOS LGAMMASETNO LIQDENSITY LIQENTHALPY LIQGAMMA LIQREFSTATE OPSETNAME PARCON = -1 POYNTING PPROCTYPE SOLU_WATER TRUE_COMPS VAPOREOS Output Unit Set = Prop Data User Table User Tree CC Nodes CHEML CHEMLOCK = 1 ENTFLOW ENTREF GCHEML = 0 GENBLKOP = 1 GOPISEOS = 1 GRHS = 0 HCLOCK = 1 MAIN = 1 MAIN2 = 1 OPISEOS RHS SCHEMLOCK SHCLOCK Comments Property Methods PENG-ROB Input Unit Set = None User Table User Tree BASE = PENG-ROB CPROP #0 = PHIVMX #1 = PHILMX #2 = DHVMX #3 = DHLMX #4 = DGVMX #5 = DGLMX #6 = DSVMX #7 = DSLMX #8 = VVMX #9 = VLMX #10 = MUVMXLP #11 = MUVLP #12 = MUVMXPC #13 = VVMX #14 = MULMX #15 = KVMXLP #16 = KVLP #17 = KLMX #18 = DVMX #19 = DLMX #20 = SIGLMX #21 = PHIV #22 = PHIL #23 = DHV #24 = DHL #25 = DGV #26 = DGL #27 = DSV #28 = DSL #29 = VV #30 = VL #31 = DL #32 = DV #33 = MUL #34 = KVPC #35 = VV #36 = KL #37 = SIGL #38 = PHIS #39 = GAMMA #40 = HS #41 = GS #42 = VSMX #43 = VS #44 = KSMX #45 = KS #46 = SS #47 = WSL #48 = HCSL DESCRIPTION = None DHLMXRTE = None LCPROP #0 = Volume, liquid mixture #1 = Volume, vapor mixture #2 = Volume, liquid mixture #3 = Volume, liquid mixture #4 = Gibbs energy departure, vapor mixture #5 = Gibbs energy departure, liquid mixture #6 = Gibbs energy departure, vapor mixture #7 = Gibbs energy departure, liquid mixture #8 = Volume, vapor mixture #9 = Volume, liquid mixture #10 = Viscosity-low pressure, vapor mixture #11 = Viscosity-low pressure, vapor pure #12 = P correction, viscosity, vapor mixture #13 = Volume, vapor mixture #14 = Viscosity, liquid mixture #15 = Thermal cond-low P, vapor mixture #16 = Thermal cond.- low pressure, vapor pure #17 = Thermal cond, liquid mixture #18 = Diff coeff, vapor mixture #19 = Diff coeff, liquid mixture #20 = Surface tension, liquid mixture #21 = Fugacity coeff, vapor pure #22 = Fugacity coeff, liquid pure #23 = Enthalpy departure, vapor pure #24 = Enthalpy departure, liquid pure #25 = Gibbs energy departure, vapor pure #26 = Gibbs energy departure, liquid pure #27 = Entropy departure, vapor pure #28 = Entropy departure, liquid pure #29 = Volume, vapor pure #30 = Volume, liquid pure #31 = Binary diff coeff, liquid #32 = Binary diff coeff, vapor #33 = Viscosity, liquid pure #34 = P correction, thermal cond, vapor pure #35 = Volume, vapor pure #36 = Thermal cond, liquid pure #37 = Surface tension, liquid pure #38 = Fugacity coeff, solid pure #39 = Liquid activity coefficient #40 = Enthalpy, solid pure #41 = Gibbs energy, solid pure #42 = Volume, solid mixture #43 = Volume, solid pure #44 = Thermal cond, solid mixture #45 = Thermal cond, solid pure #46 = Entropy, solid pure #47 = Solubility of water in organics #48 = Solubility of hydrocarbon in water phase LMPROP_NAME #0 = Fugacity coeff, vapor mixture #1 = Fugacity coeff, liquid mixture #2 = Enthalpy, vapor mixture #3 = Enthalpy, liquid mixture #4 = Gibbs energy, vapor mixture #5 = Gibbs energy, liquid mixture #6 = Entropy, vapor mixture #7 = Entropy, liquid mixture #8 = Volume, vapor mixture #9 = Volume, liquid mixture #10 = Viscosity, vapor mixture #11 = Viscosity, liquid mixture #12 = Thermal cond, vapor mixture #13 = Thermal cond, liquid mixture #14 = Diff coeff, vapor mixture #15 = Diff coeff, liquid mixture #16 = Surface tension, liquid mixture #17 = Fugacity coeff, vapor pure #18 = Fugacity coeff, liquid pure #19 = Enthalpy, vapor pure #20 = Enthalpy, liquid pure #21 = Gibbs energy, vapor pure #22 = Gibbs energy, liquid pure #23 = Entropy, vapor pure #24 = Entropy, liquid pure #25 = Volume, vapor pure #26 = Volume, liquid pure #27 = Binary diff coeff, liquid #28 = Binary diff coeff, vapor #29 = Viscosity, liquid pure #30 = Viscosity, vapor pure #31 = Thermal cond, vapor pure #32 = Thermal cond, liquid pure #33 = Surface tension, liquid pure #34 = Fugacity coeff, solid pure #35 = Fugacity coeff, solid mixture #36 = Enthalpy, solid mixture #37 = Gibbs energy, solid mixture #38 = Entropy, solid mixture #39 = Volume, solid mixture #40 = Thermal cond, solid mixture #41 = Enthalpy, solid pure #42 = Gibbs energy, solid pure #43 = Entropy, solid pure #44 = Volume, solid pure #45 = Thermal cond, solid pure #46 = Solubility of water in organics #47 = Solubility of hydrocarbon in water phase #48 = Volume, vapor mixture #49 = Volume, vapor pure LSPROP_NAME #0 = Enthalpy departure, vapor mixture #1 = Enthalpy departure, liquid mixture #2 = Gibbs energy departure, vapor mixture #3 = Gibbs energy departure, liquid mixture #4 = Entropy departure, vapor mixture #5 = Entropy departure, liquid mixture #6 = Viscosity-low pressure, vapor mixture #7 = Viscosity-low pressure, vapor pure #8 = P correction, viscosity, vapor mixture #9 = Thermal cond-low P, vapor mixture #10 = Thermal cond.- low pressure, vapor pure #11 = Enthalpy departure, vapor pure #12 = Enthalpy departure, liquid pure #13 = Gibbs energy departure, vapor pure #14 = Gibbs energy departure, liquid pure #15 = Entropy departure, vapor pure #16 = Entropy departure, liquid pure #17 = P correction, thermal cond, vapor pure MAJORMINOR = None MCHANGED #0 = - #1 = - #2 = - #3 = - #4 = - #5 = - #6 = - #7 = - #8 = - #9 = - #10 = - #11 = - #12 = - #13 = - #14 = - #15 = - #16 = - #17 = - #18 = - #19 = - #20 = - #21 = - #22 = - #23 = - #24 = - #25 = - #26 = - #27 = - #28 = - #29 = - #30 = - #31 = - #32 = - #33 = - #34 = - #35 = - #36 = - #37 = - #38 = - #39 = - #40 = - #41 = - #42 = - #43 = - #44 = - #45 = - #46 = - #47 = - #48 = - #49 = - MNREQ #0 = 0 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #5 = 0 #6 = 0 #7 = 0 #8 = 0 #9 = 0 #10 = 0 #11 = 0 #12 = 0 #13 = 0 #14 = 0 #15 = 0 #16 = 0 #17 = 0 #18 = 0 #19 = 0 #20 = 0 #21 = 0 #22 = 0 #23 = 0 #24 = 0 #25 = 0 #26 = 0 #27 = 0 #28 = 0 #29 = 0 #30 = 0 #31 = 0 #32 = 0 #33 = 0 #34 = 0 #35 = 0 #36 = 0 #37 = 0 #38 = 0 #39 = 0 #40 = 0 #41 = 0 #42 = 0 #43 = 0 #44 = 0 #45 = 0 #46 = 0 #47 = 0 #48 = 0 #49 = 0 MODCHANGED #0 = - #1 = - #2 = - #3 = - #4 = - #5 = - #6 = - #7 = - #8 = - #9 = - #10 = - #11 = - #12 = - #13 = - #14 = - #15 = - #16 = - #17 = - #18 = - #19 = - #20 = - #21 = - #22 = - #23 = - #24 = - #25 = - #26 = - #27 = - #28 = - #29 = - #30 = - #31 = - #32 = - #33 = - #34 = - #35 = - #36 = - #37 = - #38 = - #39 = - #40 = - #41 = - #42 = - #43 = - #44 = - #45 = - #46 = - #47 = - #48 = - MODELNAME #0 = ESPRSTD #1 = ESPRSTD #2 = ESPRSTD #3 = ESPRSTD #4 = ESPRSTD #5 = ESPRSTD #6 = ESPRSTD #7 = ESPRSTD #8 = ESPRSTD #9 = VL2API #10 = MUV2WILK #11 = MUV0CEB #12 = MUV2DSPC #13 = ESRK #14 = MUL2API #15 = KV2WMSM #16 = KV0STLP #17 = KL2SRVR #18 = DV1DKK #19 = DL1WCA #20 = SIG2API #21 = ESPRSTD0 #22 = ESPRSTD0 #23 = ESPRSTD0 #24 = ESPRSTD0 #25 = ESPRSTD0 #26 = ESPRSTD0 #27 = ESPRSTD0 #28 = ESPRSTD0 #29 = ESPRSTD0 #30 = VL0RKT #31 = DL0WCA #32 = DV0DKK #33 = MUL0ANDR #34 = KV0STPC #35 = ESRK0 #36 = KL0SR #37 = SIG0HSS #38 = PHS0LIQ #39 = GMIDL #40 = HS0POL1 #41 = GS0POL1 #42 = VS2IS #43 = VS0POLY #44 = KS2IDL #45 = KS0POLY #46 = SS0POL1 #47 = WSL001 #48 = HCSOL1 MPROPTYPE = ALL MPROP_NAME #0 = PHIVMX #1 = PHILMX #2 = HVMX #3 = HLMX #4 = GVMX #5 = GLMX #6 = SVMX #7 = SLMX #8 = VVMX #9 = VLMX #10 = MUVMX #11 = MULMX #12 = KVMX #13 = KLMX #14 = DVMX #15 = DLMX #16 = SIGLMX #17 = PHIV #18 = PHIL #19 = HV #20 = HL #21 = GV #22 = GL #23 = SV #24 = SL #25 = VV #26 = VL #27 = DL #28 = DV #29 = MUL #30 = MUV #31 = KV #32 = KL #33 = SIGL #34 = PHIS #35 = PHISMX #36 = HSMX #37 = GSMX #38 = SSMX #39 = VSMX #40 = KSMX #41 = HS #42 = GS #43 = SS #44 = VS #45 = KS #46 = WSL #47 = HCSL #48 = VVMX #49 = VV MRCPROP #0 = MULMX #1 = KVMXLP #2 = KLMX #3 = DVMX #4 = DLMX #5 = SIGLMX #6 = DL #7 = DV #8 = KSMX MRLCPROP #0 = Viscosity, liquid mixture #1 = Thermal cond-low P, vapor mixture #2 = Thermal cond, liquid mixture #3 = Diff coeff, vapor mixture #4 = Diff coeff, liquid mixture #5 = Surface tension, liquid mixture #6 = Binary diff coeff, liquid #7 = Binary diff coeff, vapor #8 = Thermal cond, solid mixture MRLMPROPNAME #0 = Viscosity, vapor mixture #1 = Viscosity, liquid mixture #2 = Thermal cond, vapor mixture #3 = Thermal cond, liquid mixture #4 = Diff coeff, vapor mixture #5 = Diff coeff, liquid mixture #6 = Surface tension, liquid mixture #7 = Binary diff coeff, liquid #8 = Binary diff coeff, vapor #9 = Thermal cond, solid mixture MRLSPROPNAME #0 = Thermal cond-low P, vapor mixture MRMODCHANGED #0 = None #1 = None #2 = None #3 = None #4 = None #5 = None #6 = None #7 = None #8 = None MRMODELNAME #0 = MUL2API #1 = KV2WMSM #2 = KL2SRVR #3 = DV1DKK #4 = DL1WCA #5 = SIG2API #6 = DL0WCA #7 = DV0DKK #8 = KS2IDL MRMPROPNAME #0 = MUVMX #1 = MULMX #2 = KVMX #3 = KLMX #4 = DVMX #5 = DLMX #6 = SIGLMX #7 = DL #8 = DV #9 = KSMX MRMROUTEID #0 = MUVMX02 #1 = MULMX03 #2 = KVMX01 #3 = KLMX01 #4 = DVMX02 #5 = DLMX02 #6 = SIGLMX02 #7 = DL01 #8 = DV02 #9 = KSMX01 MROPCODE #0 #1 #2 #3 #4 #5 #6 #7 #8 MROUTEID #0 = PHIVMX38 #1 = PHILM104 #2 = HVMX24 #3 = HLMX106 #4 = GVMX30 #5 = GLMX106 #6 = SVMX24 #7 = SLMX98 #8 = VVMX24 #9 = VLMX20 #10 = MUVMX02 #11 = MULMX03 #12 = KVMX01 #13 = KLMX01 #14 = DVMX02 #15 = DLMX02 #16 = SIGLMX02 #17 = PHIV09 #18 = PHIL11 #19 = HV09 #20 = HL12 #21 = GV09 #22 = GL11 #23 = SV09 #24 = SL10 #25 = VV07 #26 = VL01 #27 = DL01 #28 = DV02 #29 = MUL01 #30 = MUV01 #31 = KV01 #32 = KL01 #33 = SIGL01 #34 = PHIS08 #35 = PHISMX07 #36 = HSMX02 #37 = GSMX02 #38 = SSMX01 #39 = VSMX02 #40 = KSMX01 #41 = HS02 #42 = GS02 #43 = SS02 #44 = VS01 #45 = KS01 #46 = WATSOL00 #47 = HCSOL01 #48 = VVMX01 #49 = VV01 MRPROPLIST #0 #1 #2 #3 #4 #5 #6 #7 #8 MRSETNO #0 = None #1 = None #2 = None #3 = None #4 = None #5 = None #6 = None #7 = None #8 = None MRSPROPNAME #0 = KVMXLP MRSROUTEID #0 = KVMXLP01 MTCPROP #0 = PHIVMX #1 = PHILMX #2 = DHVMX #3 = DHLMX #4 = DGVMX #5 = DGLMX #6 = DSVMX #7 = DSLMX #8 = VVMX #9 = VLMX #10 = MUVMXLP #11 = MUVMXPC #12 = VVMX #13 = GAMMA #14 = VSMX MTLCPROP #0 = Volume, liquid mixture #1 = Volume, vapor mixture #2 = Volume, liquid mixture #3 = Volume, liquid mixture #4 = Gibbs energy departure, vapor mixture #5 = Gibbs energy departure, liquid mixture #6 = Gibbs energy departure, vapor mixture #7 = Gibbs energy departure, liquid mixture #8 = Volume, vapor mixture #9 = Volume, liquid mixture #10 = Viscosity-low pressure, vapor mixture #11 = P correction, viscosity, vapor mixture #12 = Volume, vapor mixture #13 = Liquid activity coefficient #14 = Volume, solid mixture MTLMPROPNAME #0 = Fugacity coeff, vapor mixture #1 = Fugacity coeff, liquid mixture #2 = Enthalpy, vapor mixture #3 = Enthalpy, liquid mixture #4 = Gibbs energy, vapor mixture #5 = Gibbs energy, liquid mixture #6 = Entropy, vapor mixture #7 = Entropy, liquid mixture #8 = Volume, vapor mixture #9 = Volume, liquid mixture #10 = Fugacity coeff, solid mixture #11 = Enthalpy, solid mixture #12 = Gibbs energy, solid mixture #13 = Entropy, solid mixture #14 = Volume, solid mixture #15 = Volume, vapor mixture MTLSPROPNAME #0 = Enthalpy departure, vapor mixture #1 = Enthalpy departure, liquid mixture #2 = Gibbs energy departure, vapor mixture #3 = Gibbs energy departure, liquid mixture #4 = Entropy departure, vapor mixture #5 = Entropy departure, liquid mixture #6 = Viscosity-low pressure, vapor mixture #7 = P correction, viscosity, vapor mixture MTMODCHANGED #0 = None #1 = None #2 = None #3 = None #4 = None #5 = None #6 = None #7 = None #8 = None #9 = None #10 = None #11 = None #12 = None #13 = None #14 = None MTMODELNAME #0 = ESPRSTD #1 = ESPRSTD #2 = ESPRSTD #3 = ESPRSTD #4 = ESPRSTD #5 = ESPRSTD #6 = ESPRSTD #7 = ESPRSTD #8 = ESPRSTD #9 = VL2API #10 = MUV2WILK #11 = MUV2DSPC #12 = ESRK #13 = GMIDL #14 = VS2IS MTMPROPNAME #0 = PHIVMX #1 = PHILMX #2 = HVMX #3 = HLMX #4 = GVMX #5 = GLMX #6 = SVMX #7 = SLMX #8 = VVMX #9 = VLMX #10 = PHISMX #11 = HSMX #12 = GSMX #13 = SSMX #14 = VSMX #15 = VVMX MTMROUTEID #0 = PHIVMX38 #1 = PHILM104 #2 = HVMX24 #3 = HLMX106 #4 = GVMX30 #5 = GLMX106 #6 = SVMX24 #7 = SLMX98 #8 = VVMX24 #9 = VLMX20 #10 = PHISMX07 #11 = HSMX02 #12 = GSMX02 #13 = SSMX01 #14 = VSMX02 #15 = VVMX01 MTOPCODE #0 #1 #2 #3 #4 #5 #6 #7 #8 #9 #10 #11 #12 #13 #14 MTPROPLIST #0 #1 #2 #3 #4 #5 #6 #7 #8 #9 #10 #11 #12 #13 #14 MTSETNO #0 = None #1 = None #2 = None #3 = None #4 = None #5 = None #6 = None #7 = None #8 = None #9 = None #10 = None #11 = None #12 = None #13 = None #14 = None MTSPROPNAME #0 = DHVMX #1 = DHLMX #2 = DGVMX #3 = DGLMX #4 = DSVMX #5 = DSLMX #6 = MUVMXLP #7 = MUVMXPC MTSROUTEID #0 = DHVMX10 #1 = DHLMX106 #2 = DGVMX09 #3 = DGLMX18 #4 = DSVMX09 #5 = DSLMX18 #6 = MUVMXLP1 #7 = MUVMXPC2 OPCODE #0 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #1 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #2 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #3 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #4 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #5 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #6 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #7 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #8 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #9 #10 #11 #12 #13 #14 #0 = 0 #15 #16 #17 #0 = 0 #1 = 0 #18 #0 = 0 #19 #0 = 0 #1 = 0 #20 #0 = 0 #21 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #22 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #23 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #24 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #25 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #26 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #27 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #28 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #29 #0 = 1 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #30 #31 #0 = 0 #32 #33 #34 #35 #36 #37 #38 #0 = 0 #39 #40 #0 = 0 #41 #0 = 0 #42 #43 #44 #45 #46 #0 = 0 #47 #0 = 0 #48 #0 = 0 PRCPROP #0 = KVLP #1 = MUL #2 = KVPC #3 = KL #4 = SIGL #5 = KS PRLCPROP #0 = Thermal cond.- low pressure, vapor pure #1 = Viscosity, liquid pure #2 = P correction, thermal cond, vapor pure #3 = Thermal cond, liquid pure #4 = Surface tension, liquid pure #5 = Thermal cond, solid pure PRLMPROPNAME #0 = Viscosity, liquid pure #1 = Viscosity, vapor pure #2 = Thermal cond, vapor pure #3 = Thermal cond, liquid pure #4 = Surface tension, liquid pure #5 = Thermal cond, solid pure PRLSPROPNAME #0 = Thermal cond.- low pressure, vapor pure #1 = P correction, thermal cond, vapor pure PRMODCHANGED #0 = None #1 = None #2 = None #3 = None #4 = None #5 = None PRMODELNAME #0 = KV0STLP #1 = MUL0ANDR #2 = KV0STPC #3 = KL0SR #4 = SIG0HSS #5 = KS0POLY PRMPROPNAME #0 = MUL #1 = MUV #2 = KV #3 = KL #4 = SIGL #5 = KS PRMROUTEID #0 = MUL01 #1 = MUV01 #2 = KV01 #3 = KL01 #4 = SIGL01 #5 = KS01 PROPCODE #0 #1 #2 #3 #4 #5 PROPLIST #0 #0 = PHIVMX #1 #0 = PHILMX #2 #0 = HVMX #3 #0 = HLMX #4 #0 = GVMX #5 #0 = GLMX #6 #0 = SVMX #7 #0 = SLMX #8 #0 = VVMX #9 #0 = VLMX #10 #0 = MUVMX #11 #0 = MUVMX #1 = KVMX #2 = MUV #3 = KV #12 #0 = MUVMX #13 #0 = MUVMX #14 #0 = MULMX #15 #0 = KVMX #16 #0 = KVMX #1 = KV #17 #0 = KLMX #18 #0 = DVMX #19 #0 = DLMX #20 #0 = SIGLMX #21 #0 = PHIV #22 #0 = PHIL #1 = PHIS #2 = PHISMX #23 #0 = HV #24 #0 = HL #25 #0 = GV #26 #0 = GL #27 #0 = SV #28 #0 = SL #29 #0 = VV #30 #0 = VL #31 #0 = DL #32 #0 = DV #33 #0 = MUL #34 #0 = KV #35 #0 = KV #36 #0 = KL #37 #0 = SIGL #38 #0 = PHIS #1 = PHISMX #39 #0 = PHISMX #40 #0 = HSMX #1 = SSMX #2 = HS #41 #0 = GSMX #1 = SSMX #2 = GS #42 #0 = VSMX #43 #0 = VSMX #1 = VS #44 #0 = KSMX #45 #0 = KSMX #1 = KS #46 #0 = SS #47 #0 = WSL #48 #0 = HCSL PRPROPLIST #0 #1 #2 #3 #4 #5 PRSETNO #0 = None #1 = None #2 = None #3 = None #4 = None #5 = None PRSPROPNAME #0 = KVLP #1 = KVPC PRSROUTEID #0 = KVLP01 #1 = KVPC01 PTCPROP #0 = MUVLP #1 = PHIV #2 = PHIL #3 = DHV #4 = DHL #5 = DGV #6 = DGL #7 = DSV #8 = DSL #9 = VV #10 = VL #11 = VV #12 = PHIS #13 = HS #14 = GS #15 = VS #16 = SS #17 = WSL #18 = HCSL PTLCPROP #0 = Viscosity-low pressure, vapor pure #1 = Fugacity coeff, vapor pure #2 = Fugacity coeff, liquid pure #3 = Enthalpy departure, vapor pure #4 = Enthalpy departure, liquid pure #5 = Gibbs energy departure, vapor pure #6 = Gibbs energy departure, liquid pure #7 = Entropy departure, vapor pure #8 = Entropy departure, liquid pure #9 = Volume, vapor pure #10 = Volume, liquid pure #11 = Volume, vapor pure #12 = Fugacity coeff, solid pure #13 = Enthalpy, solid pure #14 = Gibbs energy, solid pure #15 = Volume, solid pure #16 = Entropy, solid pure #17 = Solubility of water in organics #18 = Solubility of hydrocarbon in water phase PTLMPROPNAME #0 = Fugacity coeff, vapor pure #1 = Fugacity coeff, liquid pure #2 = Enthalpy, vapor pure #3 = Enthalpy, liquid pure #4 = Gibbs energy, vapor pure #5 = Gibbs energy, liquid pure #6 = Entropy, vapor pure #7 = Entropy, liquid pure #8 = Volume, vapor pure #9 = Volume, liquid pure #10 = Fugacity coeff, solid pure #11 = Enthalpy, solid pure #12 = Gibbs energy, solid pure #13 = Entropy, solid pure #14 = Volume, solid pure #15 = Solubility of water in organics #16 = Solubility of hydrocarbon in water phase #17 = Volume, vapor pure PTLSPROPNAME #0 = Viscosity-low pressure, vapor pure #1 = Enthalpy departure, vapor pure #2 = Enthalpy departure, liquid pure #3 = Gibbs energy departure, vapor pure #4 = Gibbs energy departure, liquid pure #5 = Entropy departure, vapor pure #6 = Entropy departure, liquid pure PTMODCHANGED #0 = None #1 = None #2 = None #3 = None #4 = None #5 = None #6 = None #7 = None #8 = None #9 = None #10 = None #11 = None #12 = None #13 = None #14 = None #15 = None #16 = None #17 = None #18 = None PTMODELNAME #0 = MUV0CEB #1 = ESPRSTD0 #2 = ESPRSTD0 #3 = ESPRSTD0 #4 = ESPRSTD0 #5 = ESPRSTD0 #6 = ESPRSTD0 #7 = ESPRSTD0 #8 = ESPRSTD0 #9 = ESPRSTD0 #10 = VL0RKT #11 = ESRK0 #12 = PHS0LIQ #13 = HS0POL1 #14 = GS0POL1 #15 = VS0POLY #16 = SS0POL1 #17 = WSL001 #18 = HCSOL1 PTMPROPNAME #0 = PHIV #1 = PHIL #2 = HV #3 = HL #4 = GV #5 = GL #6 = SV #7 = SL #8 = VV #9 = VL #10 = PHIS #11 = HS #12 = GS #13 = SS #14 = VS #15 = WSL #16 = HCSL #17 = VV PTMROUTEID #0 = PHIV09 #1 = PHIL11 #2 = HV09 #3 = HL12 #4 = GV09 #5 = GL11 #6 = SV09 #7 = SL10 #8 = VV07 #9 = VL01 #10 = PHIS08 #11 = HS02 #12 = GS02 #13 = SS02 #14 = VS01 #15 = WATSOL00 #16 = HCSOL01 #17 = VV01 PTOPCODE #0 #1 #2 #3 #4 #5 #6 #7 #8 #9 #10 #11 #12 #13 #14 #15 #16 #17 #18 PTPROPLIST #0 #1 #2 #3 #4 #5 #6 #7 #8 #9 #10 #11 #12 #13 #14 #15 #16 #17 #18 PTSETNO #0 = None #1 = None #2 = None #3 = None #4 = None #5 = None #6 = None #7 = None #8 = None #9 = None #10 = None #11 = None #12 = None #13 = None #14 = None #15 = None #16 = None #17 = None #18 = None PTSPROPNAME #0 = MUVLP #1 = DHV #2 = DHL #3 = DGV #4 = DGL #5 = DSV #6 = DSL PTSROUTEID #0 = MUVLP01 #1 = DHV09 #2 = DHL12 #3 = DGV09 #4 = DGL10 #5 = DSV09 #6 = DSL10 RPROPTYPE = ALL SCHANGED #0 = - #1 = - #2 = - #3 = - #4 = - #5 = - #6 = - #7 = - #8 = - #9 = - #10 = - #11 = - #12 = - #13 = - #14 = - #15 = - #16 = - #17 = - SETNO #0 = 1 #1 = 1 #2 = 1 #3 = 1 #4 = 1 #5 = 1 #6 = 1 #7 = 1 #8 = 1 #9 = 1 #10 = 1 #11 = 1 #12 = 1 #13 = 1 #14 = 1 #15 = 1 #16 = 1 #17 = 1 #18 = 1 #19 = 1 #20 = 1 #21 = 1 #22 = 1 #23 = 1 #24 = 1 #25 = 1 #26 = 1 #27 = 1 #28 = 1 #29 = 1 #30 = 1 #31 = 1 #32 = 1 #33 = 1 #34 = 1 #35 = 1 #36 = 1 #37 = 1 #38 = 1 #39 = 1 #40 = 1 #41 = 1 #42 = 1 #43 = 1 #44 = 1 #45 = 1 #46 = 1 #47 = 1 #48 = 1 SNREQ #0 = 0 #1 = 0 #2 = 0 #3 = 0 #4 = 0 #5 = 0 #6 = 0 #7 = 0 #8 = 0 #9 = 0 #10 = 0 #11 = 0 #12 = 0 #13 = 0 #14 = 0 #15 = 0 #16 = 0 #17 = 0 SPROP_NAME #0 = DHVMX #1 = DHLMX #2 = DGVMX #3 = DGLMX #4 = DSVMX #5 = DSLMX #6 = MUVMXLP #7 = MUVLP #8 = MUVMXPC #9 = KVMXLP #10 = KVLP #11 = DHV #12 = DHL #13 = DGV #14 = DGL #15 = DSV #16 = DSL #17 = KVPC SROUTEID #0 = DHVMX10 #1 = DHLMX106 #2 = DGVMX09 #3 = DGLMX18 #4 = DSVMX09 #5 = DSLMX18 #6 = MUVMXLP1 #7 = MUVLP01 #8 = MUVMXPC2 #9 = KVMXLP01 #10 = KVLP01 #11 = DHV09 #12 = DHL12 #13 = DGV09 #14 = DGL10 #15 = DSV09 #16 = DSL10 #17 = KVPC01 Output Unit Set = Prop Data User Table User Tree CC Nodes MAIN = 1 MAIN2 = 1 Comments Estimation Estimate Input Unit Set = ENG User Table User Tree ALLONLY = NONE BINCHOICE = NO COMPT DATA DESCRIPTION = None GRPCHOICE = YES METHOD METHODG METHODT METHODU PROPERTY TCHOICE = YES TEMP TLOWER TUPPER UNCHOICE = YES WEIGHT Output Unit Set = Prop Data User Table User Tree BLKSTAT = None COMPID COMPID2 COMPID3 COMP_NAMES ESTMETHOD ESTMETHOD2 ESTMETHOD3 ESTMETHOD4 ESTMETHOD5 ESTMETHOD6 ESTMETHOD7 ESTVALUE ESTVALUE2 ESTVALUE3 ESTVALUE4 ESTVALUE5 ESTVALUE6 EXP_VALUE EXP_VALUE2 EXP_VALUE3 NODENAME PARANAME PARANAME2 PARANAME3 PARANAME4 PARANAME5 PER_ERROR PER_ERROR2 PER_ERROR3 PROPNAME PROPNAME2 PROPNAME3 PROPNAME4 PROPNAME5 PROPNAME6 PROPSTAT = None TEMP VAL1 VAL2 VAL3 VAL4 VAL5 VAR_UNIT VAR_UNIT2 CC Nodes ALLOWDATA BI = 1 BIC = 0 BINESTI = 0 DIFFCOMP = 1 ENTBIN = 0 ENTGRP = 0 ENTT = 0 ENTU = 0 EXISTB1 = 1 EXISTB2 = 1 EXISTPAR = 0 GR = 1 GRC = 0 GRPESTI = 1 ISPCES = 0 LOADDATA MAIN = 1 METHISDATA OPEN = 1 OPENB = 0 OPENG = 1 OPENT = 1 OPENU = 1 REVCOMP = 0 TESTI = 1 UESTI = 1 UN = 1 UNC = 0 UT = 1 UTC = 0 Comments Compare Input Unit Set = None User Table User Tree COMP COMP1 COMP2 DESCRIPTION = None GROUP GROUP1 GROUP2 Output Unit Set = Prop Data User Table User Tree CC Nodes COMP = 1 ENTSET = 0 Comments Molecular Structure ETHANOL Input Unit Set = None User Table User Tree AMBROSE = 0 AQU_DATA = -1 AQU_EST1 = -1 AQU_EST2 = -1 ASKED = 0 ATOM1 ATOM2 ATOMNUM ATOMTYPE BENSON = 0 BENSONR8 = 0 BONDI = 0 BONDTYPE BROCK_BI = -1 DATA = -1 DEFINITI = -1 DESCRIPTION = None DISPATOM1 DISPATOM2 DUCROS = 0 EXISTENCE FEDORS = 0 GANI = 0 GUNN_YAM = -1 HAKIM_ST = -1 HELGESON = -1 HG_AQU = -1 HG_CRIS = -1 HG_EST = -1 JOBACK = 0 LEBAS = 0 LEE_KESL = -1 LETSOU_S = -1 LI_MA = 0 LYDERSEN = 0 MANI = -1 MCLEOD_S = -1 MOLFILEPATH = None MOLSTRUCT MOSTAFA = 0 NOATOM NOCCUR OGATA_TS = 0 ORRICK_E = 0 PARACHOR = 0 REICHENB = 0 RIEDEL = -1 RUZICKA = 0 SATO_RIE = -1 SIMPLE = -1 STIEL_TH = -1 THERMO = -1 UNIFAC = 0 UNIF_DMD = 0 UNIF_LBY = 0 UNIF_LL = 0 UNIF_R4 = 0 VANKREV = 0 VELZEN_C = -1 VETERE = -1 Output Unit Set = Prop Data User Table User Tree CC Nodes ENTFORM ENTGEN ENTMETH FORMULA GEN = 1 HASAMBROSE HASANYTHING = 0 HASBENSON HASBENSONR8 HASDATA = 0 HASDBNAME = 1 HASFEDORS HASFORMUL HASJOBACK HASLYDERSEN HASOGATA ISCOMP1 = 1 ISCOMP2 = 1 LEFTOUT = 1 MAIN = 1 OPENGEN = 1 SPE = 1 SPE1 UNIFLIMIT = 1 Comments WATER Input Unit Set = None User Table User Tree AMBROSE = 0 AQU_DATA = -1 AQU_EST1 = -1 AQU_EST2 = -1 ASKED = 0 ATOM1 ATOM2 ATOMNUM ATOMTYPE BENSON = 0 BENSONR8 = 0 BONDI = 0 BONDTYPE BROCK_BI = -1 DATA = -1 DEFINITI = -1 DESCRIPTION = None DISPATOM1 DISPATOM2 DUCROS = 0 EXISTENCE FEDORS = 0 GANI = 0 GUNN_YAM = -1 HAKIM_ST = -1 HELGESON = -1 HG_AQU = -1 HG_CRIS = -1 HG_EST = -1 JOBACK = 0 LEBAS = 0 LEE_KESL = -1 LETSOU_S = -1 LI_MA = 0 LYDERSEN = 0 MANI = -1 MCLEOD_S = -1 MOLFILEPATH = None MOLSTRUCT MOSTAFA = 0 NOATOM NOCCUR OGATA_TS = 0 ORRICK_E = 0 PARACHOR = 0 REICHENB = 0 RIEDEL = -1 RUZICKA = 0 SATO_RIE = -1 SIMPLE = -1 STIEL_TH = -1 THERMO = -1 UNIFAC = 0 UNIF_DMD = 0 UNIF_LBY = 0 UNIF_LL = 0 UNIF_R4 = 0 VANKREV = 0 VELZEN_C = -1 VETERE = -1 Output Unit Set = Prop Data User Table User Tree CC Nodes ENTFORM ENTGEN ENTMETH FORMULA GEN = 1 HASAMBROSE HASANYTHING = 0 HASBENSON HASBENSONR8 HASDATA = 0 HASDBNAME = 1 HASFEDORS HASFORMUL HASJOBACK HASLYDERSEN HASOGATA ISCOMP1 = 1 ISCOMP2 = 1 LEFTOUT = 1 MAIN = 1 OPENGEN = 1 SPE = 1 SPE1 UNIFLIMIT = 1 Comments Parameters Pure Components Binary Interaction ANDKIJ-1 Input Unit Set = ENG User Table User Tree BDBANK ANDKIJ BDBANK2 ANDKIJ COMPNAME = CompID i: COMSEARCH1 ANDKIJ = None COMSEARCH2 ANDKIJ = None COMTYPE1 = 4194313 COMTYPE2 = 4194313 DESCRIPTION = None ESTIMATE ANDKIJ = None LABEL1 ANDKIJ = kij LABEL10 ANDKIJ = None LABEL11 ANDKIJ = None LABEL12 ANDKIJ = None LABEL2 ANDKIJ = lij LABEL3 ANDKIJ = None LABEL4 ANDKIJ = None LABEL5 ANDKIJ = None LABEL6 ANDKIJ = None LABEL7 ANDKIJ = None LABEL8 ANDKIJ = None LABEL9 ANDKIJ = None NEL ANDKIJ = 2 NEL2 ANDKIJ OPT_SOURCE ANDKIJ SETNO ANDKIJ = 1 TUNITLABEL ANDKIJ = F TUNITLABEL2 ANDKIJ TUNITROW ANDKIJ = 22 TUNITROW2 ANDKIJ UNITLABEL ANDKIJ = None UNITLABEL2 ANDKIJ UNITROW ANDKIJ = 0 UNITROW2 ANDKIJ UVAL1 ANDKIJ UVAL10 ANDKIJ UVAL11 ANDKIJ UVAL12 ANDKIJ UVAL2 ANDKIJ UVAL3 ANDKIJ UVAL4 ANDKIJ UVAL5 ANDKIJ UVAL6 ANDKIJ UVAL7 ANDKIJ UVAL8 ANDKIJ UVAL9 ANDKIJ VAL1 ANDKIJ VAL10 ANDKIJ VAL11 ANDKIJ VAL12 ANDKIJ VAL2 ANDKIJ VAL3 ANDKIJ VAL4 ANDKIJ VAL5 ANDKIJ VAL6 ANDKIJ VAL7 ANDKIJ VAL8 ANDKIJ VAL9 ANDKIJ VALALPHA ANDKIJ VALI ANDKIJ VALJ ANDKIJ VI ANDKIJ VJ ANDKIJ Output Unit Set = Prop Data User Table User Tree CID1 CID2 DATABANK PARAMNAME = None PER_ERROR SETNO = None TUNITLABEL UNITLABEL VALUE CC Nodes ACCESSDB ANDKIJ = 0 ALLOWEST ANDKIJ = 0 ALLOWEST2 ANDKIJ = 0 ENTDB ANDKIJ = 0 ISUSER ANDKIJ = 0 LBLLE ANDKIJ LBVLE ANDKIJ LOADCODE3 ANDKIJ = 1 LOADDECH ANDKIJ = 1 MAIN = 1 REVID ANDKIJ SAMEID ANDKIJ Comments ANDMIJ-1 Input Unit Set = ENG User Table User Tree BDBANK ANDMIJ BDBANK2 ANDMIJ COMPNAME = CompID i: COMSEARCH1 ANDMIJ = None COMSEARCH2 ANDMIJ = None COMTYPE1 = 4194313 COMTYPE2 = 4194313 DESCRIPTION = None ESTIMATE ANDMIJ = None LABEL1 ANDMIJ = mij LABEL10 ANDMIJ = None LABEL11 ANDMIJ = None LABEL12 ANDMIJ = None LABEL2 ANDMIJ = nij LABEL3 ANDMIJ = None LABEL4 ANDMIJ = None LABEL5 ANDMIJ = None LABEL6 ANDMIJ = None LABEL7 ANDMIJ = None LABEL8 ANDMIJ = None LABEL9 ANDMIJ = None NEL ANDMIJ = 2 NEL2 ANDMIJ OPT_SOURCE ANDMIJ SETNO ANDMIJ = 1 TUNITLABEL ANDMIJ = F TUNITLABEL2 ANDMIJ TUNITROW ANDMIJ = 22 TUNITROW2 ANDMIJ UNITLABEL ANDMIJ = None UNITLABEL2 ANDMIJ UNITROW ANDMIJ = 0 UNITROW2 ANDMIJ UVAL1 ANDMIJ UVAL10 ANDMIJ UVAL11 ANDMIJ UVAL12 ANDMIJ UVAL2 ANDMIJ UVAL3 ANDMIJ UVAL4 ANDMIJ UVAL5 ANDMIJ UVAL6 ANDMIJ UVAL7 ANDMIJ UVAL8 ANDMIJ UVAL9 ANDMIJ VAL1 ANDMIJ VAL10 ANDMIJ VAL11 ANDMIJ VAL12 ANDMIJ VAL2 ANDMIJ VAL3 ANDMIJ VAL4 ANDMIJ VAL5 ANDMIJ VAL6 ANDMIJ VAL7 ANDMIJ VAL8 ANDMIJ VAL9 ANDMIJ VALALPHA ANDMIJ VALI ANDMIJ VALJ ANDMIJ VI ANDMIJ VJ ANDMIJ Output Unit Set = Prop Data User Table User Tree CID1 CID2 DATABANK PARAMNAME = None PER_ERROR SETNO = None TUNITLABEL UNITLABEL VALUE CC Nodes ACCESSDB ANDMIJ = 0 ALLOWEST ANDMIJ = 0 ALLOWEST2 ANDMIJ = 0 ENTDB ANDMIJ = 0 ISUSER ANDMIJ = 0 LBLLE ANDMIJ LBVLE ANDMIJ LOADCODE3 ANDMIJ = 1 LOADDECH ANDMIJ = 1 MAIN = 1 REVID ANDMIJ SAMEID ANDMIJ Comments MLQKIJ-1 Input Unit Set = ENG User Table User Tree ANCHOR MLQKIJ BDBANK MLQKIJ COMPNAME = CompID j: COMSEARCH1 MLQKIJ = None COMSEARCH2 MLQKIJ = None COMTYPE = 4194313 DESCRIPTION = None SETNO MLQKIJ = 1 UNITLABEL MLQKIJ = None UNITROW MLQKIJ = 0 UVALUE MLQKIJ VALUE MLQKIJ Output Unit Set = Prop Data User Table User Tree PARAMNAME = None PER_ERROR SETNO = None UNITLABEL = None VALUE CC Nodes ACCESSDBS = 0 ENTDB MLQKIJ = 0 MAIN = 1 Comments MUKIJ-1 Input Unit Set = ENG User Table User Tree BDBANK MUKIJ BDBANK2 MUKIJ COMPNAME = CompID i: COMSEARCH1 MUKIJ = None COMSEARCH2 MUKIJ = None COMTYPE1 = 4194313 COMTYPE2 = 4194313 DESCRIPTION = None ESTIMATE MUKIJ = None LABEL1 MUKIJ = aij LABEL10 MUKIJ = None LABEL11 MUKIJ = None LABEL12 MUKIJ = None LABEL2 MUKIJ = bij LABEL3 MUKIJ = cij LABEL4 MUKIJ = dij LABEL5 MUKIJ = eij LABEL6 MUKIJ = Tref LABEL7 MUKIJ = None LABEL8 MUKIJ = None LABEL9 MUKIJ = None NEL MUKIJ = 6 NEL2 MUKIJ OPT_SOURCE MUKIJ SETNO MUKIJ = 1 TUNITLABEL MUKIJ = F TUNITLABEL2 MUKIJ TUNITROW MUKIJ = 22 TUNITROW2 MUKIJ UNITLABEL MUKIJ = None UNITLABEL2 MUKIJ UNITROW MUKIJ = 0 UNITROW2 MUKIJ UVAL1 MUKIJ UVAL10 MUKIJ UVAL11 MUKIJ UVAL12 MUKIJ UVAL2 MUKIJ UVAL3 MUKIJ UVAL4 MUKIJ UVAL5 MUKIJ UVAL6 MUKIJ UVAL7 MUKIJ UVAL8 MUKIJ UVAL9 MUKIJ VAL1 MUKIJ VAL10 MUKIJ VAL11 MUKIJ VAL12 MUKIJ VAL2 MUKIJ VAL3 MUKIJ VAL4 MUKIJ VAL5 MUKIJ VAL6 MUKIJ VAL7 MUKIJ VAL8 MUKIJ VAL9 MUKIJ VALALPHA MUKIJ VALI MUKIJ VALJ MUKIJ VI MUKIJ VJ MUKIJ Output Unit Set = Prop Data User Table User Tree CID1 CID2 DATABANK PARAMNAME = None PER_ERROR SETNO = None TUNITLABEL UNITLABEL VALUE CC Nodes ACCESSDB MUKIJ = 1 ALLOWEST MUKIJ = 0 ALLOWEST2 MUKIJ = 0 ENTDB MUKIJ = 0 ISUSER MUKIJ = 0 LBLLE MUKIJ LBVLE MUKIJ LOADCODE3 MUKIJ = 1 LOADDECH MUKIJ = 1 MAIN = 1 REVID MUKIJ SAMEID MUKIJ Comments MULIJ-1 Input Unit Set = ENG User Table User Tree BDBANK MULIJ BDBANK2 MULIJ COMPNAME = CompID i: COMSEARCH1 MULIJ = None COMSEARCH2 MULIJ = None COMTYPE1 = 4194313 COMTYPE2 = 4194313 DESCRIPTION = None ESTIMATE MULIJ = None LABEL1 MULIJ = aij LABEL10 MULIJ = eji LABEL11 MULIJ = Tref LABEL12 MULIJ = None LABEL2 MULIJ = aji LABEL3 MULIJ = bij LABEL4 MULIJ = bji LABEL5 MULIJ = cij LABEL6 MULIJ = cji LABEL7 MULIJ = dij LABEL8 MULIJ = dji LABEL9 MULIJ = eij NEL MULIJ = 11 NEL2 MULIJ OPT_SOURCE MULIJ SETNO MULIJ = 1 TUNITLABEL MULIJ = F TUNITLABEL2 MULIJ TUNITROW MULIJ = 22 TUNITROW2 MULIJ UNITLABEL MULIJ = None UNITLABEL2 MULIJ UNITROW MULIJ = 0 UNITROW2 MULIJ UVAL1 MULIJ UVAL10 MULIJ UVAL11 MULIJ UVAL12 MULIJ UVAL2 MULIJ UVAL3 MULIJ UVAL4 MULIJ UVAL5 MULIJ UVAL6 MULIJ UVAL7 MULIJ UVAL8 MULIJ UVAL9 MULIJ VAL1 MULIJ VAL10 MULIJ VAL11 MULIJ VAL12 MULIJ VAL2 MULIJ VAL3 MULIJ VAL4 MULIJ VAL5 MULIJ VAL6 MULIJ VAL7 MULIJ VAL8 MULIJ VAL9 MULIJ VALALPHA MULIJ VALI MULIJ VALJ MULIJ VI MULIJ VJ MULIJ Output Unit Set = Prop Data User Table User Tree CID1 CID2 DATABANK PARAMNAME = None PER_ERROR SETNO = None TUNITLABEL UNITLABEL VALUE CC Nodes ACCESSDB MULIJ = 1 ALLOWEST MULIJ = 0 ALLOWEST2 MULIJ = 0 ENTDB MULIJ = 0 ISUSER MULIJ = 0 LBLLE MULIJ LBVLE MULIJ LOADCODE3 MULIJ = 1 LOADDECH MULIJ = 1 MAIN = 1 REVID MULIJ SAMEID MULIJ Comments PRKBV-1 Input Unit Set = ENG User Table User Tree BDBANK PRKBV #0 = APV80 EOS-LIT BDBANK2 PRKBV COMPNAME = CompID i: COMSEARCH1 PRKBV = None COMSEARCH2 PRKBV = None COMTYPE1 = 4194313 COMTYPE2 = 4194313 DESCRIPTION = None ESTIMATE PRKBV = None LABEL1 PRKBV = kaij LABEL10 PRKBV = None LABEL11 PRKBV = None LABEL12 PRKBV = None LABEL2 PRKBV = kbij LABEL3 PRKBV = kcij LABEL4 PRKBV = Tlower LABEL5 PRKBV = Tuppper LABEL6 PRKBV = None LABEL7 PRKBV = None LABEL8 PRKBV = None LABEL9 PRKBV = None NEL PRKBV = 5 NEL2 PRKBV OPT_SOURCE PRKBV SETNO PRKBV = 1 TUNITLABEL PRKBV = F TUNITLABEL2 PRKBV TUNITROW PRKBV = 22 TUNITROW2 PRKBV UNITLABEL PRKBV = None UNITLABEL2 PRKBV UNITROW PRKBV = 0 UNITROW2 PRKBV UVAL1 PRKBV UVAL10 PRKBV UVAL11 PRKBV UVAL12 PRKBV UVAL2 PRKBV UVAL3 PRKBV UVAL4 PRKBV UVAL5 PRKBV UVAL6 PRKBV UVAL7 PRKBV UVAL8 PRKBV UVAL9 PRKBV VAL1 PRKBV VAL10 PRKBV VAL11 PRKBV VAL12 PRKBV VAL2 PRKBV VAL3 PRKBV VAL4 PRKBV VAL5 PRKBV VAL6 PRKBV VAL7 PRKBV VAL8 PRKBV VAL9 PRKBV VALALPHA PRKBV VALI PRKBV VALJ PRKBV VI PRKBV VJ PRKBV Output Unit Set = Prop Data User Table User Tree CID1 CID2 DATABANK PARAMNAME = None PER_ERROR SETNO = None TUNITLABEL UNITLABEL VALUE CC Nodes ACCESSDB PRKBV = 1 ALLOWEST PRKBV = 0 ALLOWEST2 PRKBV = 0 ENTDB PRKBV = 1 ISUSER PRKBV = 0 LBLLE PRKBV LBVLE PRKBV LOADCODE3 PRKBV = 1 LOADDECH PRKBV = 1 MAIN = 1 REVID PRKBV SAMEID PRKBV Comments PRLIJ-1 Input Unit Set = ENG User Table User Tree BDBANK PRLIJ BDBANK2 PRLIJ COMPNAME = CompID i: COMSEARCH1 PRLIJ = None COMSEARCH2 PRLIJ = None COMTYPE1 = 4194313 COMTYPE2 = 4194313 DESCRIPTION = None ESTIMATE PRLIJ = None LABEL1 PRLIJ = laij LABEL10 PRLIJ = None LABEL11 PRLIJ = None LABEL12 PRLIJ = None LABEL2 PRLIJ = laji LABEL3 PRLIJ = lbij LABEL4 PRLIJ = lbji LABEL5 PRLIJ = lcij LABEL6 PRLIJ = lcji LABEL7 PRLIJ = Tlower LABEL8 PRLIJ = Tupper LABEL9 PRLIJ = None NEL PRLIJ = 8 NEL2 PRLIJ OPT_SOURCE PRLIJ SETNO PRLIJ = 1 TUNITLABEL PRLIJ = F TUNITLABEL2 PRLIJ TUNITROW PRLIJ = 22 TUNITROW2 PRLIJ UNITLABEL PRLIJ = None UNITLABEL2 PRLIJ UNITROW PRLIJ = 0 UNITROW2 PRLIJ UVAL1 PRLIJ UVAL10 PRLIJ UVAL11 PRLIJ UVAL12 PRLIJ UVAL2 PRLIJ UVAL3 PRLIJ UVAL4 PRLIJ UVAL5 PRLIJ UVAL6 PRLIJ UVAL7 PRLIJ UVAL8 PRLIJ UVAL9 PRLIJ VAL1 PRLIJ VAL10 PRLIJ VAL11 PRLIJ VAL12 PRLIJ VAL2 PRLIJ VAL3 PRLIJ VAL4 PRLIJ VAL5 PRLIJ VAL6 PRLIJ VAL7 PRLIJ VAL8 PRLIJ VAL9 PRLIJ VALALPHA PRLIJ VALI PRLIJ VALJ PRLIJ VI PRLIJ VJ PRLIJ Output Unit Set = Prop Data User Table User Tree CID1 CID2 DATABANK PARAMNAME = None PER_ERROR SETNO = None TUNITLABEL UNITLABEL VALUE CC Nodes ACCESSDB PRLIJ = 0 ALLOWEST PRLIJ = 0 ALLOWEST2 PRLIJ = 0 ENTDB PRLIJ = 0 ISUSER PRLIJ = 0 LBLLE PRLIJ LBVLE PRLIJ LOADCODE3 PRLIJ = 1 LOADDECH PRLIJ = 1 MAIN = 1 REVID PRLIJ SAMEID PRLIJ Comments RKTKIJ-1 Input Unit Set = ENG User Table User Tree ANCHOR RKTKIJ BDBANK RKTKIJ COMPNAME = CompID j: COMSEARCH1 RKTKIJ = None COMSEARCH2 RKTKIJ = None COMTYPE = 4194313 DESCRIPTION = None SETNO RKTKIJ = 1 UNITLABEL RKTKIJ = None UNITROW RKTKIJ = 0 UVALUE RKTKIJ VALUE RKTKIJ Output Unit Set = Prop Data User Table User Tree PARAMNAME = None PER_ERROR SETNO = None UNITLABEL = None VALUE CC Nodes ACCESSDBS = 0 ENTDB RKTKIJ = 0 MAIN = 1 Comments Electrolyte Pair Electrolyte Ternary UNIFAC Groups UNIFAC Groups Binary Results Input Unit Set = None User Table User Tree DESCRIPTION = None Output Unit Set = Prop Data User Table User Tree BGSCOMP BGSPROP BGS_DB BGS_UNIT BGS_VAL BGTCID1 BGTCID2 BGTCOMP BGTPROP BGTUNITROW BGT_DB BGT_UNIT BGT_VAL BLKSTAT = None BSCOMP BSPROP BS_DB BS_UNIT BS_UNIT1 BS_VAL BTCID1 BTCID2 BTCID3 BTCID4 BTCOMP BTPARAM = None BTPROP BTUNITROW BT_DB BT_UNIT BT_VAL COMPID DATABANK ELECCIDI1 ELECCIDI2 ELECCIDJ1 ELECCIDJ2 ELEC_UNIT ELEC_VAL PER_ERROR PROPNAME PROPNAME2 PROPNAME3 PROPNAME4 PROPNAME5 PROPNAME6 PROPNAME7 PROPNAME8 PROPSTAT = None PROPTYPE SETNO = None TUNITLABEL TYPE TYPE2 TYPE3 TYPE4 TYPE5 TYPE6 TYPE7 TYPE8 TYPEBGS TYPEBGT TYPEBS TYPEBT TYPEUG TYPEUS TYPEUT UGCOMP UGPROP UGPROP2 UG_VAL UNITLABEL USCOMP USPROP USSPARM US_DB US_UNIT US_VAL UTCID UTCOMP UTPROP UTSPARM UTUNITROW UT_DB UT_UNIT UT_VAL VALUE CC Nodes Comments Data Analysis Prop-Sets HXDESIGN Input Unit Set = ENG User Table User Tree BASE_COMPS BASE_GROUPS BASE_TBL = None BASE_TBU = None BASIS COMPS COMP_GROUPS DESCRIPTION = Thermal and Transport, for heat exchanger design ISPLUS = NO L2_COMPS LVPCT PHASE #0 = T #1 = V #2 = L PRES SHOWDLG = None SUBSTREAM = MIXED SYSPRES = YES SYSTEMP = YES TB_LOWER = None TB_UPPER = None TEMP UNITS MASSVFRA MASSFLMX #0 = kg/sec HMX #0 = J/kg RHOMX #0 = kg/cum CPMX #0 = J/kg-K PCMX #0 = N/sqm MUMX #0 = N-sec/sqm KMX #0 = Watt/m-K SIGMAMX #0 = N/m MWMX Output Unit Set = Prop Data User Table User Tree CC Nodes ALLCONVOK = 1 ALLNCOK = 1 BASECOMPOK = 1 BASECPROK = 1 BASEGRPOK = 1 BASEGRPROK = 1 BASETBLOK = 1 BASETBLROK = 1 BASETBUOK = 1 BASETBUROK = 1 BASISOK = 1 BCMPQUAL = 1 BGRPQUAL = 1 BTBQUAL = 1 CMPQUAL = 1 COMPGROUPOK = 1 COMPSOK = 1 EMPTYENT = 1 ENTQUAL = 1 GRPQUAL = 1 HASL = 1 HASLL1L2 = 1 HASLL1L2S = 1 HASLS = 1 HASS = 0 HASV = 1 HASVL = 1 HASVLL1L2 = 1 HASVLL1L2S = 1 L2COMPSOK = 1 LVPCTOK = 1 LVPCTROK = 1 MAIN = 1 PHASENOTS = 1 PHASEOK = 1 PRESOK = 1 QUAL = 1 REQL = 0 REQLL1L2 = 1 REQLL1L2S = 0 REQLS = 0 REQS = 0 REQV = 0 REQVL = 0 REQVLL1L2 = 1 REQVLL1L2S = 1 SYSPOK = 1 TBLOWEROK = 1 TBQUAL = 1 TBUPPEROK = 1 TEMPOK = 1 TEMPROK = 1 TYPENCCI = 0 Comments HXDSGN2 Input Unit Set = ENG User Table User Tree BASE_COMPS BASE_GROUPS BASE_TBL = None BASE_TBU = None BASIS COMPS COMP_GROUPS DESCRIPTION = Thermal and Transport, for heat exchanger design ISPLUS = NO L2_COMPS LVPCT PHASE #0 = T #1 = V #2 = L1 #3 = L2 PRES SHOWDLG = None SUBSTREAM = MIXED SYSPRES = YES SYSTEMP = YES TB_LOWER = None TB_UPPER = None TEMP UNITS MASSVFRA MASSFLMX #0 = kg/sec HMX #0 = J/kg RHOMX #0 = kg/cum CPMX #0 = J/kg-K PCMX #0 = N/sqm MUMX #0 = N-sec/sqm KMX #0 = Watt/m-K SIGMAMX #0 = N/m MWMX Output Unit Set = Prop Data User Table User Tree CC Nodes ALLCONVOK = 1 ALLNCOK = 1 BASECOMPOK = 1 BASECPROK = 1 BASEGRPOK = 1 BASEGRPROK = 1 BASETBLOK = 1 BASETBLROK = 1 BASETBUOK = 1 BASETBUROK = 1 BASISOK = 1 BCMPQUAL = 1 BGRPQUAL = 1 BTBQUAL = 1 CMPQUAL = 1 COMPGROUPOK = 1 COMPSOK = 1 EMPTYENT = 1 ENTQUAL = 1 GRPQUAL = 1 HASL = 0 HASLL1L2 = 1 HASLL1L2S = 1 HASLS = 0 HASS = 0 HASV = 1 HASVL = 1 HASVLL1L2 = 1 HASVLL1L2S = 1 L2COMPSOK = 1 LVPCTOK = 1 LVPCTROK = 1 MAIN = 1 PHASENOTS = 1 PHASEOK = 1 PRESOK = 1 QUAL = 1 REQL = 0 REQLL1L2 = 1 REQLL1L2S = 0 REQLS = 0 REQS = 0 REQV = 0 REQVL = 0 REQVLL1L2 = 1 REQVLL1L2S = 1 SYSPOK = 1 TBLOWEROK = 1 TBQUAL = 1 TBUPPEROK = 1 TEMPOK = 1 TEMPROK = 1 TYPENCCI = 0 Comments THERMAL Input Unit Set = ENG User Table User Tree BASE_COMPS BASE_GROUPS BASE_TBL = None BASE_TBU = None BASIS COMPS COMP_GROUPS DESCRIPTION = Enthalpy, heat capacity, and thermal conductivity ISPLUS = NO L2_COMPS LVPCT PHASE #0 = V #1 = L PRES SHOWDLG = None SUBSTREAM = MIXED SYSPRES = YES SYSTEMP = YES TB_LOWER = None TB_UPPER = None TEMP UNITS HMX #0 = Btu/lb CPMX #0 = Btu/lb-R KMX Output Unit Set = Prop Data User Table User Tree CC Nodes ALLCONVOK = 1 ALLNCOK = 1 BASECOMPOK = 1 BASECPROK = 1 BASEGRPOK = 1 BASEGRPROK = 1 BASETBLOK = 1 BASETBLROK = 1 BASETBUOK = 1 BASETBUROK = 1 BASISOK = 1 BCMPQUAL = 1 BGRPQUAL = 1 BTBQUAL = 1 CMPQUAL = 1 COMPGROUPOK = 1 COMPSOK = 1 EMPTYENT = 1 ENTQUAL = 1 GRPQUAL = 1 HASL = 1 HASLL1L2 = 1 HASLL1L2S = 1 HASLS = 1 HASS = 0 HASV = 1 HASVL = 1 HASVLL1L2 = 1 HASVLL1L2S = 1 L2COMPSOK = 1 LVPCTOK = 1 LVPCTROK = 1 MAIN = 1 PHASENOTS = 1 PHASEOK = 1 PRESOK = 1 QUAL = 1 REQL = 0 REQLL1L2 = 0 REQLL1L2S = 0 REQLS = 0 REQS = 0 REQV = 0 REQVL = 0 REQVLL1L2 = 0 REQVLL1L2S = 1 SYSPOK = 1 TBLOWEROK = 1 TBQUAL = 1 TBUPPEROK = 1 TEMPOK = 1 TEMPROK = 1 TYPENCCI = 0 Comments THERMAL2 Input Unit Set = ENG User Table User Tree BASE_COMPS BASE_GROUPS BASE_TBL = None BASE_TBU = None BASIS COMPS COMP_GROUPS DESCRIPTION = Enthalpy, heat capacity, and thermal conductivity ISPLUS = NO L2_COMPS LVPCT PHASE #0 = V #1 = L1 #2 = L2 PRES SHOWDLG = None SUBSTREAM = MIXED SYSPRES = YES SYSTEMP = YES TB_LOWER = None TB_UPPER = None TEMP UNITS HMX #0 = Btu/lb CPMX #0 = Btu/lb-R KMX Output Unit Set = Prop Data User Table User Tree CC Nodes ALLCONVOK = 1 ALLNCOK = 1 BASECOMPOK = 1 BASECPROK = 1 BASEGRPOK = 1 BASEGRPROK = 1 BASETBLOK = 1 BASETBLROK = 1 BASETBUOK = 1 BASETBUROK = 1 BASISOK = 1 BCMPQUAL = 1 BGRPQUAL = 1 BTBQUAL = 1 CMPQUAL = 1 COMPGROUPOK = 1 COMPSOK = 1 EMPTYENT = 1 ENTQUAL = 1 GRPQUAL = 1 HASL = 0 HASLL1L2 = 1 HASLL1L2S = 1 HASLS = 0 HASS = 0 HASV = 1 HASVL = 1 HASVLL1L2 = 1 HASVLL1L2S = 1 L2COMPSOK = 1 LVPCTOK = 1 LVPCTROK = 1 MAIN = 1 PHASENOTS = 1 PHASEOK = 1 PRESOK = 1 QUAL = 1 REQL = 0 REQLL1L2 = 0 REQLL1L2S = 0 REQLS = 0 REQS = 0 REQV = 0 REQVL = 0 REQVLL1L2 = 0 REQVLL1L2S = 1 SYSPOK = 1 TBLOWEROK = 1 TBQUAL = 1 TBUPPEROK = 1 TEMPOK = 1 TEMPROK = 1 TYPENCCI = 0 Comments TXPORT Input Unit Set = ENG User Table User Tree BASE_COMPS BASE_GROUPS BASE_TBL = None BASE_TBU = None BASIS COMPS COMP_GROUPS DESCRIPTION = Density, viscosity, and surface tension ISPLUS = NO L2_COMPS LVPCT PHASE #0 = V #1 = L PRES SHOWDLG = None SUBSTREAM = MIXED SYSPRES = YES SYSTEMP = YES TB_LOWER = None TB_UPPER = None TEMP UNITS RHOMX #0 = lb/cuft MUMX SIGMAMX Output Unit Set = Prop Data User Table User Tree CC Nodes ALLCONVOK = 1 ALLNCOK = 1 BASECOMPOK = 1 BASECPROK = 1 BASEGRPOK = 1 BASEGRPROK = 1 BASETBLOK = 1 BASETBLROK = 1 BASETBUOK = 1 BASETBUROK = 1 BASISOK = 1 BCMPQUAL = 1 BGRPQUAL = 1 BTBQUAL = 1 CMPQUAL = 1 COMPGROUPOK = 1 COMPSOK = 1 EMPTYENT = 1 ENTQUAL = 1 GRPQUAL = 1 HASL = 1 HASLL1L2 = 1 HASLL1L2S = 1 HASLS = 1 HASS = 0 HASV = 1 HASVL = 1 HASVLL1L2 = 1 HASVLL1L2S = 1 L2COMPSOK = 1 LVPCTOK = 1 LVPCTROK = 1 MAIN = 1 PHASENOTS = 1 PHASEOK = 1 PRESOK = 1 QUAL = 1 REQL = 0 REQLL1L2 = 1 REQLL1L2S = 0 REQLS = 0 REQS = 0 REQV = 0 REQVL = 0 REQVLL1L2 = 1 REQVLL1L2S = 0 SYSPOK = 1 TBLOWEROK = 1 TBQUAL = 1 TBUPPEROK = 1 TEMPOK = 1 TEMPROK = 1 TYPENCCI = 0 Comments TXPORT2 Input Unit Set = ENG User Table User Tree BASE_COMPS BASE_GROUPS BASE_TBL = None BASE_TBU = None BASIS COMPS COMP_GROUPS DESCRIPTION = Density, viscosity, and surface tension ISPLUS = NO L2_COMPS LVPCT PHASE #0 = V #1 = L1 #2 = L2 PRES SHOWDLG = None SUBSTREAM = MIXED SYSPRES = YES SYSTEMP = YES TB_LOWER = None TB_UPPER = None TEMP UNITS RHOMX #0 = lb/cuft MUMX SIGMAMX Output Unit Set = Prop Data User Table User Tree CC Nodes ALLCONVOK = 1 ALLNCOK = 1 BASECOMPOK = 1 BASECPROK = 1 BASEGRPOK = 1 BASEGRPROK = 1 BASETBLOK = 1 BASETBLROK = 1 BASETBUOK = 1 BASETBUROK = 1 BASISOK = 1 BCMPQUAL = 1 BGRPQUAL = 1 BTBQUAL = 1 CMPQUAL = 1 COMPGROUPOK = 1 COMPSOK = 1 EMPTYENT = 1 ENTQUAL = 1 GRPQUAL = 1 HASL = 0 HASLL1L2 = 1 HASLL1L2S = 1 HASLS = 0 HASS = 0 HASV = 1 HASVL = 1 HASVLL1L2 = 1 HASVLL1L2S = 1 L2COMPSOK = 1 LVPCTOK = 1 LVPCTROK = 1 MAIN = 1 PHASENOTS = 1 PHASEOK = 1 PRESOK = 1 QUAL = 1 REQL = 0 REQLL1L2 = 1 REQLL1L2S = 0 REQLS = 0 REQS = 0 REQV = 0 REQVL = 0 REQVLL1L2 = 1 REQVLL1L2S = 0 SYSPOK = 1 TBLOWEROK = 1 TBQUAL = 1 TBUPPEROK = 1 TEMPOK = 1 TEMPROK = 1 TYPENCCI = 0 Comments VLE Input Unit Set = ENG User Table User Tree BASE_COMPS BASE_GROUPS BASE_TBL = None BASE_TBU = None BASIS COMPS COMP_GROUPS DESCRIPTION = Fugacity, activity, and vapor pressure ISPLUS = NO L2_COMPS LVPCT PHASE #0 = V #1 = L PRES SHOWDLG = None SUBSTREAM = MIXED SYSPRES = YES SYSTEMP = YES TB_LOWER = None TB_UPPER = None TEMP UNITS PHIMX GAMMA PL Output Unit Set = Prop Data User Table User Tree CC Nodes ALLCONVOK = 1 ALLNCOK = 1 BASECOMPOK = 1 BASECPROK = 1 BASEGRPOK = 1 BASEGRPROK = 1 BASETBLOK = 1 BASETBLROK = 1 BASETBUOK = 1 BASETBUROK = 1 BASISOK = 1 BCMPQUAL = 1 BGRPQUAL = 1 BTBQUAL = 1 CMPQUAL = 1 COMPGROUPOK = 1 COMPSOK = 1 EMPTYENT = 1 ENTQUAL = 1 GRPQUAL = 1 HASL = 1 HASLL1L2 = 1 HASLL1L2S = 1 HASLS = 1 HASS = 0 HASV = 1 HASVL = 1 HASVLL1L2 = 1 HASVLL1L2S = 1 L2COMPSOK = 1 LVPCTOK = 1 LVPCTROK = 1 MAIN = 1 PHASENOTS = 1 PHASEOK = 1 PRESOK = 1 QUAL = 1 REQL = 0 REQLL1L2 = 0 REQLL1L2S = 1 REQLS = 0 REQS = 0 REQV = 0 REQVL = 0 REQVLL1L2 = 0 REQVLL1L2S = 1 SYSPOK = 1 TBLOWEROK = 1 TBQUAL = 1 TBUPPEROK = 1 TEMPOK = 1 TEMPROK = 1 TYPENCCI = 0 Comments VLLE Input Unit Set = ENG User Table User Tree BASE_COMPS BASE_GROUPS BASE_TBL = None BASE_TBU = None BASIS COMPS COMP_GROUPS DESCRIPTION = Fugacity, activity, and vapor pressure ISPLUS = NO L2_COMPS LVPCT PHASE #0 = V #1 = L1 #2 = L2 PRES SHOWDLG = None SUBSTREAM = MIXED SYSPRES = YES SYSTEMP = YES TB_LOWER = None TB_UPPER = None TEMP UNITS PHIMX GAMMA PL Output Unit Set = Prop Data User Table User Tree CC Nodes ALLCONVOK = 1 ALLNCOK = 1 BASECOMPOK = 1 BASECPROK = 1 BASEGRPOK = 1 BASEGRPROK = 1 BASETBLOK = 1 BASETBLROK = 1 BASETBUOK = 1 BASETBUROK = 1 BASISOK = 1 BCMPQUAL = 1 BGRPQUAL = 1 BTBQUAL = 1 CMPQUAL = 1 COMPGROUPOK = 1 COMPSOK = 1 EMPTYENT = 1 ENTQUAL = 1 GRPQUAL = 1 HASL = 0 HASLL1L2 = 1 HASLL1L2S = 1 HASLS = 0 HASS = 0 HASV = 1 HASVL = 1 HASVLL1L2 = 1 HASVLL1L2S = 1 L2COMPSOK = 1 LVPCTOK = 1 LVPCTROK = 1 MAIN = 1 PHASENOTS = 1 PHASEOK = 1 PRESOK = 1 QUAL = 1 REQL = 0 REQLL1L2 = 0 REQLL1L2S = 1 REQLS = 0 REQS = 0 REQV = 0 REQVL = 0 REQVLL1L2 = 0 REQVLL1L2S = 1 SYSPOK = 1 TBLOWEROK = 1 TBQUAL = 1 TBUPPEROK = 1 TEMPOK = 1 TEMPROK = 1 TYPENCCI = 0 Comments Advanced Route User-Parameters Input Unit Set = None User Table User Tree DESCRIPTION = None DIM NEL NSET SYSALLOWED = NO Output Unit Set = Prop Data User Table User Tree CC Nodes ENTSELE = 1 MAIN = 1 Comments NC-Props Input Unit Set = None User Table User Tree COMPDUMMY = None DENS_MODEL DOPCODE ENTH_MODEL EOPCODE HBIOCOMP HBIOSTATE HGENANAL HMACROSTA HPROXANAL HSULFANAL HULTANAL NTBSYM RBIOCOMP RGENANAL RPROXANAL RSULFANAL RULTANAL TYPE_LIST Output Unit Set = Prop Data User Table User Tree CC Nodes ENTMAIN MAIN MAIN2 Comments Tabpoly User-Property CO-Package Flowsheet Section GLOBAL Input Unit Set = None User Table User Tree BLKTYPE FLASH = FLASH2 DESCRIPTION = None INPORT FLASH #0 = F(IN) INSTRM FLASH #0 = FEED MDLTYPE FLASH = Flash2 OUTPORT FLASH #0 = V(OUT) #1 = L(OUT) OUTSTRM FLASH #0 = VAPOR #1 = LIQUID SCLASS = CONVEN Output Unit Set = Prop Data User Table User Tree CC Nodes COMPLETE FLASH = 1 CONNVALID FLASH = 1 MAIN = 1 MHEAT FLASH = 1 NOTPFSLOCK = 1 PFSLOCK = 0 VALID FLASH = 1 Comments Def-Streams Input Unit Set = None User Table User Tree H_SCLASS H_SLIST SCLASS SLIST Output Unit Set = Prop Data User Table User Tree CC Nodes DEF1 DEFS = 1 ENTLOAD ENTLOAD1 ENTOPT ENTOPT1 Comments Custom Forms Streams FEED Input Unit Set = ENG User Table User Tree ALWAYS_INST = NO ATTOTAL AUTO_COMPS = None AUTO_COMPS_T = 0.0 AUTO_PHASE = YES AUTO_PHASE_T = 0.1 BASIS MIXED = MOLE-FRAC CHECK_FREE_W = YES CHEM_METHOD = YES COMP_TOL = 1e-15 CONC_TREF MIXED = None CUM_SUBSATT D50 D63 DERIV_METHOD = None DESCRIPTION = None DIAM ELEM EO_COMPS = None EO_DEP_COMPS = None EO_FORM = None EO_HEAVY_KEY = None EO_L2_COMP = None EO_LIGHT_KEY = None EO_TEMP_TOL = 0.0018 FLASH_FORM = PML FLOW MIXED WATER = 0.91095 ETHANOL = 0.08905 FLOWBASE MIXED = MOLE FLOW_TOL = 0.7936641439 FL_OPTION MIXED = None FREE_WATER MIXED = NO GGS_N GMDEV INIT_SCRIPT = None INLET_PHASE = None INTERACTIVE = None INTERVAL JUNK MIXED = 2 L2_COMP_MODE = AUTO LAB LIMUNITS LOWER MAXIT MIXED = 30 MIXED_SPEC MIXED = TP NEG_COMP_CHK = -1e-08 NEG_FLOW_CHK = 0.0 NEL NPHASE MIXED = 2 ON_SMEO_DIFF = USE-CLOSED PASS_THROUGH = NO PHASE MIXED = V PRES MIXED = 50.0 PRICE = None PSDID REBWIZ = None RRSB_N SFRAC_TOL = 0.0001 SOLVENT MIXED = None SOLVE_METHOD = None SOLVE_OPEN = None SPARSITY = None STDDEV STRSUM1 MIXED = None SUBSATT SUBSATT_OPT TEMP MIXED = 100.0 TOL MIXED = 0.0001 TOTAL MIXED = 1.0 TOTFLOW MIXED = 48.7488 TYPE UPPER VFRAC MIXED = None VFRACX_TOL = 1e-05 VFRAC_TOL = 0.001 VOL_TREF MIXED = None WTFRAC_OPT Output Unit Set = Prop Data User Table User Tree BETA BLKSTAT = 0 B_VFRAC = 0.0 CHEMTRUE = 0 CMOLE_CYCLE CMOLE_TIME COMPTYPE = LIQUID COMP_ATTR COST CYCLE_TIME DESCRIPTION = None DESTINATION = FLASH ENTH_CYCLE ENTH_TIME FULLDEST = None FULLSOURCE = None GAMMA GUID = None HMX MIXED = -5954.00012 HMX2 L1_ENTH = -122137.187 L1_ENTR = -42.0577379 L1_FLOW = 48.7488 L1_MW = 20.5134673 L1_RHO = 2.84931642 L2_ENTH = None L2_ENTR = None L2_FLOW = 0.0 L2_MW = None L2_RHO = None LFRAC MIXED = 1.0 LIQ_ENTH = -122137.187 LIQ_FLOW = 48.7488 LIQ_RATIO = 1.0 L_ENTR = -42.0577379 MASSFLMX MIXED = 1000.00692 MASSFLMX_GAS = 0.0 MASSFLMX_LIQ = 1000.00692 MASSFLOW MIXED WATER = 800.017498 ETHANOL = 199.989418 MASSFLOW2 MASSFLOW3 WATER = 800.017498 ETHANOL = 199.989418 MASSFRAC MIXED WATER = 0.800011965 ETHANOL = 0.199988035 MASSFRAC2 MASSSFRA = 0.0 MASSVFRA = 0.0 MASS_CYCLE MASS_PRICE = None MASS_TIME MOLEFLMX MIXED = 48.7488 MOLEFLOW MIXED WATER = 44.4077194 ETHANOL = 4.34108064 MOLEFRAC MIXED WATER = 0.91095 ETHANOL = 0.08905 MOLEFRAC2 MOLE_CYCLE MOLE_PRICE = None MOLE_TIME MW = 20.5134673 MWMX MIXED = 20.5134673 MW_GAS = None MW_LIQ = 20.5134673 NTRAIN OPER_TIME PER_ERROR PHIMX PL PRES_OUT MIXED = 50.0 PROPSTAT = 0 RES_MASSFLOW = 1000.00692 RES_MOLEFLOW = 48.7488 RES_PRES = 50.0 RES_TEMP = 100.0 RES_VFRAC = 0.0 RES_VOLFLOW = 17.1089461 RHOMX MIXED = 58.4493592 RHOMX2 RHO_GAS = None RHO_LIQ = 2.84931642 SFRAC MIXED = 0.0 SMX MIXED = -2.05025007 SOURCE = None STCOST = None STDVFLOW = 16.8849295 STDVOL_PRICE = None STREAMNAME = None STRM_UPP STR_CATT STR_MAIN SOURCE = None DESTINATION = FLASH COMPTYPE = LIQUID HMX MIXED = -5954.00012 SMX MIXED = -2.05025007 TEMP MIXED = 100.0 PRES MIXED = 50.0 VFRAC MIXED = 0.0 LFRAC MIXED = 1.0 SFRAC MIXED = 0.0 MOLEFLMX MIXED = 48.7488 MOLEFRAC MIXED WATER = 0.91095 ETHANOL = 0.08905 MASSFLMX MIXED = 1000.00692 MASSFRAC MIXED WATER = 0.800011965 ETHANOL = 0.199988035 VLSTDMX MIXED = 16.8849295 VOLFLMX MIXED = 17.1089461 MOLEFLOW MIXED WATER = 44.4077194 ETHANOL = 4.34108064 MASSFLOW MIXED WATER = 800.017498 ETHANOL = 199.989418 RHOMX MIXED = 58.4493592 MWMX MIXED = 20.5134673 SUBS-ATTR SUBSATTR TEMP_OUT MIXED = 100.0 TOT_FLOW = 48.7488 VAP_ENTH = None VAP_FLOW = 0.0 VFRAC_OUT MIXED = 0.0 VFRAC_OUT2 VLSTD VLSTDFR VLSTDMX MIXED = 16.8849295 VOLFLMX MIXED = 17.1089461 VOLFLMX2 = 17.1089461 VOLFLMX_GAS = None VOLFLMX_LIQ = 17.1089461 VOL_CYCLE VOL_PRICE = None VOL_TIME V_ENTR = None X WATER = 0.91095 ETHANOL = 0.08905 X1 WATER = 0.91095 ETHANOL = 0.08905 X2 WATER = 0.91095 ETHANOL = 0.08905 Y WATER = 0.0759686582 ETHANOL = 0.924031342 CC Nodes ATTR CMP1 CNVATTR CNVLOWER CNVPSD CNVPSD1 CNVSPEC2 MIXED = 1 CNVSPEC3 = 1 CNVSPECS = 1 CNVUPPER CSFRAC CSFRAC2 CSFRAC3 CSFYES CSFYES2 CSFYES3 CSSUB = 0 CSTAB = 0 EDPN EDPN2 EDPN3 EMWN EMWN2 EMWN3 ENTCOMP ENTCOST = 0 ENTEOMOD = 0 ENTERED = 1 ENTREF MIXED = 0 ENTSUBSTR EQTO1 EQTO100 EQUA = 1 ESFL ESFL2 ESFL3 ESFR ESFR2 ESFR3 EZMO EZMO2 EZMO3 FLSHE MIXED = 0 FLSOPT MIXED = 1 FRAC MIXED = 0 FRAC1 MIXED = 1 GRTHEN1 GRTN100 L2CP1 = 0 L2CP2 = 1 MACEQTO1 MACGRTN1 MIXED MIXED = 1 MIXLOWER MIXPSD MIXPSD1 MIXUPPER NCLOWER NCPSD NCPSD1 NCSPEC2 MIXED = 1 NCSPEC3 = 1 NCSPECS = 1 NCSUB = 0 NCTAB = 0 NCUPPER NCVATTR NOFL MIXED = 1 NOFLOW1 MIXED = 0 NOFLOW10 MIXED = 0 NOFLOW11 MIXED = 0 NOFLOW2 MIXED = 0 NOFLOW3 MIXED = 0 NOFLOW4 MIXED = 0 NOFLOW5 MIXED = 0 NOFLOW6 MIXED = 0 NOFLOW7 MIXED = 0 NOFLOW8 MIXED = 0 NOFLOW9 MIXED = 0 NOTNC MIXED = 1 OUTLETSTRM1 = 0 OUTLETSTRM2 = 0 OUTLETSTRM3 = 0 OUTLETSTRM4 = 0 POLTRU POLTRU2 POLTRU3 POLYES POLYES2 POLYES3 PRES MIXED = 1 PSD1 PSD10 PSD11 PSD2 PSD3 PSD4 PSD5 PSD6 PSD7 PSD8 PSD9 PSPEC MIXED = 1 PSPEC2 MIXED = 1 PSPEC3 MIXED = 1 REFT1 MIXED = 0 REFT2 MIXED = 0 RMODE = 1 SAMEPRES1 MIXED = 1 SAMEPRES2 MIXED = 1 SAMEPRES3 MIXED = 1 SFRC = 0 SOLV MIXED = 0 SP3C2 = 1 SPAR = 1 SPEC2 MIXED = 1 SPEC3 = 1 SPEC4 MIXED = 1 SPECS = 1 SSCISOLID1 MIXED = 0 SSCISOLID2 MIXED = 0 SSCISORNC1 MIXED = 0 SSCISORNC2 SSCISORNC3 MIXED = 0 SSCISORNC4 SSMIXED1 MIXED = 1 SSMIXED2 MIXED = 1 SSMIXED3 MIXED = 1 SSMIXED4 MIXED = 1 SSMIXED5 MIXED = 1 SSMIXED6 MIXED = 1 SSMIXED7 MIXED = 1 SSMIXORCIS1 MIXED = 1 SSMIXORCIS2 MIXED = 1 SSMIXORCIS3 SSMIXORCIS4 SSMIXORNC1 MIXED = 1 SSMIXORNC2 MIXED = 1 SSMIXORNC3 SSMIXORNC4 SSNC1 MIXED = 0 SSNC2 MIXED = 0 SSNC3 MIXED = 0 SSNC4 MIXED = 0 SSREFTC MIXED = 0 TEMP MIXED = 1 VFRAC = 1 WFONE1 WFONE2 WFONE3 Ports DEST FLASH = FLASH SOURCE Connections FLASH = DEST #1 = SOURCE Comments Stream Results Display = STREAMS Units = TFF File = GEN_E Table Temperature F FEED = 100.0 Temperature F #1 = Pressure psia FEED = 50.00 Pressure psia #1 = Vapor Frac FEED = 0.000 Vapor Frac #1 = Mole Flow lbmol/hr FEED = 48.749 Mole Flow lbmol/hr #1 = Mass Flow lb/hr FEED = 1000.007 Mass Flow lb/hr #1 = Volume Flow cuft/hr FEED = 17.109 Volume Flow cuft/hr #1 = Enthalpy MMBtu/hr FEED = -5.954 Enthalpy MMBtu/hr #1 = Mass Flow FEED = Mass Flow #1 = WATER FEED = 800.017 WATER #1 = ETHANOL FEED = 199.989 ETHANOL #1 = Mass Frac FEED = Mass Frac #1 = WATER FEED = 0.800 WATER #1 = ETHANOL FEED = 0.200 ETHANOL #1 = Mole Flow FEED = Mole Flow #1 = WATER FEED = 44.408 WATER #1 = ETHANOL FEED = 4.341 ETHANOL #1 = Mole Frac FEED = Mole Frac #1 = WATER FEED = 0.911 WATER #1 = ETHANOL FEED = 0.089 ETHANOL #1 = LIQUID Input Unit Set = ENG User Table User Tree ALWAYS_INST = NO ATTOTAL AUTO_COMPS = None AUTO_COMPS_T = 0.0 AUTO_PHASE = YES AUTO_PHASE_T = 0.1 BASIS MIXED = MOLE-FLOW CHECK_FREE_W = YES CHEM_METHOD = YES COMP_TOL = 1e-15 CONC_TREF MIXED = None CUM_SUBSATT D50 D63 DERIV_METHOD = None DESCRIPTION = None DIAM ELEM EO_COMPS = None EO_DEP_COMPS = None EO_FORM = None EO_HEAVY_KEY = None EO_L2_COMP = None EO_LIGHT_KEY = None EO_TEMP_TOL = 0.0018 FLASH_FORM = PML FLOW MIXED WATER = None ETHANOL = None FLOWBASE MIXED = MOLE FLOW_TOL = 0.7936641439 FL_OPTION MIXED = None FREE_WATER MIXED = NO GGS_N GMDEV INIT_SCRIPT = None INLET_PHASE = None INTERACTIVE = None INTERVAL JUNK MIXED = 0 L2_COMP_MODE = AUTO LAB LIMUNITS LOWER MAXIT MIXED = 30 MIXED_SPEC MIXED = TP NEG_COMP_CHK = -1e-08 NEG_FLOW_CHK = 0.0 NEL NPHASE MIXED = 2 ON_SMEO_DIFF = USE-CLOSED PASS_THROUGH = NO PHASE MIXED = V PRES MIXED = None PRICE = None PSDID REBWIZ = None RRSB_N SFRAC_TOL = 0.0001 SOLVENT MIXED = None SOLVE_METHOD = None SOLVE_OPEN = None SPARSITY = None STDDEV STRSUM1 MIXED = None SUBSATT SUBSATT_OPT TEMP MIXED = None TOL MIXED = 0.0001 TOTAL MIXED = 0.0 TOTFLOW MIXED = None TYPE UPPER VFRAC MIXED = None VFRACX_TOL = 1e-05 VFRAC_TOL = 0.001 VOL_TREF MIXED = None WTFRAC_OPT Output Unit Set = Prop Data User Table User Tree BETA BLKSTAT = 0 B_VFRAC = 0.0 CHEMTRUE = None CMOLE_CYCLE CMOLE_TIME COMPTYPE = LIQUID COMP_ATTR COST CYCLE_TIME DESCRIPTION = None DESTINATION = None ENTH_CYCLE ENTH_TIME FULLDEST = None FULLSOURCE = None GAMMA GUID = None HMX MIXED = -6674.37924 HMX2 L1_ENTH = -122128.612 L1_ENTR = -37.8640035 L1_FLOW = 44.077524 L1_MW = 18.2981229 L1_RHO = 3.2334619 L2_ENTH = None L2_ENTR = None L2_FLOW = 0.0 L2_MW = None L2_RHO = None LFRAC MIXED = 1.0 LIQ_ENTH = -122128.612 LIQ_FLOW = 44.077524 LIQ_RATIO = 1.0 L_ENTR = -37.8640035 MASSFLMX MIXED = 806.53595 MASSFLMX_GAS = 0.0 MASSFLMX_LIQ = 806.53595 MASSFLOW MIXED WATER = 786.062996 ETHANOL = 20.4729543 MASSFLOW2 MASSFLOW3 WATER = 786.062996 ETHANOL = 20.4729543 MASSFRAC MIXED WATER = 0.974616191 ETHANOL = 0.0253838087 MASSFRAC2 MASSSFRA = 0.0 MASSVFRA = 0.0 MASS_CYCLE MASS_PRICE = None MASS_TIME MOLEFLMX MIXED = 44.077524 MOLEFLOW MIXED WATER = 43.6331268 ETHANOL = 0.444397241 MOLEFRAC MIXED WATER = 0.989917827 ETHANOL = 0.0100821734 MOLEFRAC2 MOLE_CYCLE MOLE_PRICE = None MOLE_TIME MW = 18.2981229 MWMX MIXED = 18.2981229 MW_GAS = None MW_LIQ = 18.2981229 NTRAIN OPER_TIME PER_ERROR PHIMX PL PRES_OUT MIXED = 20.0 PROPSTAT = 0 RES_MASSFLOW = 806.53595 RES_MOLEFLOW = 44.077524 RES_PRES = 20.0 RES_TEMP = 150.0 RES_VFRAC = 0.0 RES_VOLFLOW = 13.6316822 RHOMX MIXED = 59.1662831 RHOMX2 RHO_GAS = None RHO_LIQ = 3.2334619 SFRAC MIXED = 0.0 SMX MIXED = -2.06928349 SOURCE = FLASH STCOST = None STDVFLOW = 13.0298942 STDVOL_PRICE = None STREAMNAME = None STRM_UPP STR_CATT STR_MAIN SOURCE = FLASH DESTINATION = None COMPTYPE = LIQUID HMX MIXED = -6674.37924 SMX MIXED = -2.06928349 TEMP MIXED = 150.0 PRES MIXED = 20.0 VFRAC MIXED = 0.0 LFRAC MIXED = 1.0 SFRAC MIXED = 0.0 MOLEFLMX MIXED = 44.077524 MOLEFRAC MIXED WATER = 0.989917827 ETHANOL = 0.0100821734 MASSFLMX MIXED = 806.53595 MASSFRAC MIXED WATER = 0.974616191 ETHANOL = 0.0253838087 VLSTDMX MIXED = 13.0298942 VOLFLMX MIXED = 13.6316822 MOLEFLOW MIXED WATER = 43.6331268 ETHANOL = 0.444397241 MASSFLOW MIXED WATER = 786.062996 ETHANOL = 20.4729543 RHOMX MIXED = 59.1662831 MWMX MIXED = 18.2981229 SUBS-ATTR SUBSATTR TEMP_OUT MIXED = 150.0 TOT_FLOW = 44.077524 VAP_ENTH = None VAP_FLOW = 0.0 VFRAC_OUT MIXED = 0.0 VFRAC_OUT2 VLSTD VLSTDFR VLSTDMX MIXED = 13.0298942 VOLFLMX MIXED = 13.6316822 VOLFLMX2 = 13.6316822 VOLFLMX_GAS = None VOLFLMX_LIQ = 13.6316822 VOL_CYCLE VOL_PRICE = None VOL_TIME V_ENTR = None X WATER = 0.989917827 ETHANOL = 0.0100821734 X1 WATER = 0.989917827 ETHANOL = 0.0100821734 X2 WATER = 0.989917827 ETHANOL = 0.0100821734 Y WATER = 0.165820381 ETHANOL = 0.834179619 CC Nodes ATTR CMP1 CNVATTR CNVLOWER CNVPSD CNVPSD1 CNVSPEC2 MIXED = 1 CNVSPEC3 = 1 CNVSPECS = 1 CNVUPPER CSFRAC CSFRAC2 CSFRAC3 CSFYES CSFYES2 CSFYES3 CSSUB = 0 CSTAB = 0 EDPN EDPN2 EDPN3 EMWN EMWN2 EMWN3 ENTCOMP ENTCOST = 0 ENTEOMOD = 0 ENTERED = 0 ENTREF MIXED = 0 ENTSUBSTR EQTO1 EQTO100 EQUA = 1 ESFL ESFL2 ESFL3 ESFR ESFR2 ESFR3 EZMO EZMO2 EZMO3 FLSHE MIXED = 0 FLSOPT MIXED = 1 FRAC MIXED = 0 FRAC1 MIXED = 1 GRTHEN1 GRTN100 L2CP1 = 0 L2CP2 = 1 MACEQTO1 MACGRTN1 MIXED MIXED = 1 MIXLOWER MIXPSD MIXPSD1 MIXUPPER NCLOWER NCPSD NCPSD1 NCSPEC2 MIXED = 1 NCSPEC3 = 1 NCSPECS = 1 NCSUB = 0 NCTAB = 0 NCUPPER NCVATTR NOFL MIXED = 1 NOFLOW1 MIXED = 1 NOFLOW10 MIXED = 1 NOFLOW11 MIXED = 1 NOFLOW2 MIXED = 1 NOFLOW3 MIXED = 1 NOFLOW4 MIXED = 1 NOFLOW5 MIXED = 1 NOFLOW6 MIXED = 1 NOFLOW7 MIXED = 1 NOFLOW8 MIXED = 1 NOFLOW9 MIXED = 1 NOTNC MIXED = 1 OUTLETSTRM1 = 1 OUTLETSTRM2 = 1 OUTLETSTRM3 = 1 OUTLETSTRM4 = 1 POLTRU POLTRU2 POLTRU3 POLYES POLYES2 POLYES3 PRES MIXED = 1 PSD1 PSD10 PSD11 PSD2 PSD3 PSD4 PSD5 PSD6 PSD7 PSD8 PSD9 PSPEC MIXED = 1 PSPEC2 MIXED = 1 PSPEC3 MIXED = 1 REFT1 MIXED = 0 REFT2 MIXED = 0 RMODE = 1 SAMEPRES1 MIXED = 1 SAMEPRES2 MIXED = 1 SAMEPRES3 MIXED = 1 SFRC = 0 SOLV MIXED = 0 SP3C2 = 1 SPAR = 1 SPEC2 MIXED = 1 SPEC3 = 1 SPEC4 MIXED = 1 SPECS = 1 SSCISOLID1 MIXED = 0 SSCISOLID2 MIXED = 0 SSCISORNC1 MIXED = 0 SSCISORNC2 SSCISORNC3 MIXED = 0 SSCISORNC4 SSMIXED1 MIXED = 1 SSMIXED2 MIXED = 1 SSMIXED3 MIXED = 1 SSMIXED4 MIXED = 1 SSMIXED5 MIXED = 1 SSMIXED6 MIXED = 1 SSMIXED7 MIXED = 1 SSMIXORCIS1 MIXED = 1 SSMIXORCIS2 MIXED = 1 SSMIXORCIS3 SSMIXORCIS4 SSMIXORNC1 MIXED = 1 SSMIXORNC2 MIXED = 1 SSMIXORNC3 SSMIXORNC4 SSNC1 MIXED = 0 SSNC2 MIXED = 0 SSNC3 MIXED = 0 SSNC4 MIXED = 0 SSREFTC MIXED = 0 TEMP MIXED = 1 VFRAC = 1 WFONE1 WFONE2 WFONE3 Ports DEST SOURCE FLASH = FLASH Connections #0 = DEST FLASH = SOURCE Comments Stream Results Display = STREAMS Units = TFF File = GEN_E Table Temperature F LIQUID = 150.0 Temperature F #1 = Pressure psia LIQUID = 20.00 Pressure psia #1 = Vapor Frac LIQUID = 0.000 Vapor Frac #1 = Mole Flow lbmol/hr LIQUID = 44.078 Mole Flow lbmol/hr #1 = Mass Flow lb/hr LIQUID = 806.536 Mass Flow lb/hr #1 = Volume Flow cuft/hr LIQUID = 13.632 Volume Flow cuft/hr #1 = Enthalpy MMBtu/hr LIQUID = -5.383 Enthalpy MMBtu/hr #1 = Mass Flow LIQUID = Mass Flow #1 = WATER LIQUID = 786.063 WATER #1 = ETHANOL LIQUID = 20.473 ETHANOL #1 = Mass Frac LIQUID = Mass Frac #1 = WATER LIQUID = 0.975 WATER #1 = ETHANOL LIQUID = 0.025 ETHANOL #1 = Mole Flow LIQUID = Mole Flow #1 = WATER LIQUID = 43.633 WATER #1 = ETHANOL LIQUID = 0.444 ETHANOL #1 = Mole Frac LIQUID = Mole Frac #1 = WATER LIQUID = 0.990 WATER #1 = ETHANOL LIQUID = 0.010 ETHANOL #1 = VAPOR Input Unit Set = ENG User Table User Tree ALWAYS_INST = NO ATTOTAL AUTO_COMPS = None AUTO_COMPS_T = 0.0 AUTO_PHASE = YES AUTO_PHASE_T = 0.1 BASIS MIXED = MOLE-FLOW CHECK_FREE_W = YES CHEM_METHOD = YES COMP_TOL = 1e-15 CONC_TREF MIXED = None CUM_SUBSATT D50 D63 DERIV_METHOD = None DESCRIPTION = None DIAM ELEM EO_COMPS = None EO_DEP_COMPS = None EO_FORM = None EO_HEAVY_KEY = None EO_L2_COMP = None EO_LIGHT_KEY = None EO_TEMP_TOL = 0.0018 FLASH_FORM = PML FLOW MIXED WATER = None ETHANOL = None FLOWBASE MIXED = MOLE FLOW_TOL = 0.7936641439 FL_OPTION MIXED = None FREE_WATER MIXED = NO GGS_N GMDEV INIT_SCRIPT = None INLET_PHASE = None INTERACTIVE = None INTERVAL JUNK MIXED = 0 L2_COMP_MODE = AUTO LAB LIMUNITS LOWER MAXIT MIXED = 30 MIXED_SPEC MIXED = TP NEG_COMP_CHK = -1e-08 NEG_FLOW_CHK = 0.0 NEL NPHASE MIXED = 2 ON_SMEO_DIFF = USE-CLOSED PASS_THROUGH = NO PHASE MIXED = V PRES MIXED = None PRICE = None PSDID REBWIZ = None RRSB_N SFRAC_TOL = 0.0001 SOLVENT MIXED = None SOLVE_METHOD = None SOLVE_OPEN = None SPARSITY = None STDDEV STRSUM1 MIXED = None SUBSATT SUBSATT_OPT TEMP MIXED = None TOL MIXED = 0.0001 TOTAL MIXED = 0.0 TOTFLOW MIXED = None TYPE UPPER VFRAC MIXED = None VFRACX_TOL = 1e-05 VFRAC_TOL = 0.001 VOL_TREF MIXED = None WTFRAC_OPT Output Unit Set = Prop Data User Table User Tree BETA BLKSTAT = 0 B_VFRAC = 1.0 CHEMTRUE = None CMOLE_CYCLE CMOLE_TIME COMPTYPE = VAPOR COMP_ATTR COST CYCLE_TIME DESCRIPTION = None DESTINATION = None ENTH_CYCLE ENTH_TIME FULLDEST = None FULLSOURCE = None GAMMA GUID = None HMX MIXED = -2426.90294 HMX2 L1_ENTH = None L1_ENTR = None L1_FLOW = 0.0 L1_MW = None L1_RHO = None L2_ENTH = None L2_ENTR = None L2_FLOW = 0.0 L2_MW = None L2_RHO = None LFRAC MIXED = 0.0 LIQ_ENTH = None LIQ_FLOW = 0.0 LIQ_RATIO = 1.0 L_ENTR = None MASSFLMX MIXED = 193.470961 MASSFLMX_GAS = 193.470961 MASSFLMX_LIQ = 0.0 MASSFLOW MIXED WATER = 13.9545055 ETHANOL = 179.516456 MASSFLOW2 MASSFLOW3 WATER = 13.9545055 ETHANOL = 179.516456 MASSFRAC MIXED WATER = 0.0721271319 ETHANOL = 0.927872868 MASSFRAC2 MASSSFRA = 0.0 MASSVFRA = 1.0 MASS_CYCLE MASS_PRICE = None MASS_TIME MOLEFLMX MIXED = 4.67127599 MOLEFLOW MIXED WATER = 0.774592763 ETHANOL = 3.89668323 MOLEFRAC MIXED WATER = 0.165820381 ETHANOL = 0.834179619 MOLEFRAC2 MOLE_CYCLE MOLE_PRICE = None MOLE_TIME MW = 41.4171548 MWMX MIXED = 41.4171548 MW_GAS = 41.4171548 MW_LIQ = None NTRAIN OPER_TIME PER_ERROR PHIMX PL PRES_OUT MIXED = 20.0 PROPSTAT = 0 RES_MASSFLOW = 193.470961 RES_MOLEFLOW = 4.67127599 RES_PRES = 20.0 RES_TEMP = 150.0 RES_VFRAC = 1.0 RES_VOLFLOW = 1481.4341 RHOMX MIXED = 0.130597079 RHOMX2 RHO_GAS = 0.00315321221 RHO_LIQ = None SFRAC MIXED = 0.0 SMX MIXED = -1.07509436 SOURCE = FLASH STCOST = None STDVFLOW = 3.85503517 STDVOL_PRICE = None STREAMNAME = None STRM_UPP STR_CATT STR_MAIN SOURCE = FLASH DESTINATION = None COMPTYPE = VAPOR HMX MIXED = -2426.90294 SMX MIXED = -1.07509436 TEMP MIXED = 150.0 PRES MIXED = 20.0 VFRAC MIXED = 1.0 LFRAC MIXED = 0.0 SFRAC MIXED = 0.0 MOLEFLMX MIXED = 4.67127599 MOLEFRAC MIXED WATER = 0.165820381 ETHANOL = 0.834179619 MASSFLMX MIXED = 193.470961 MASSFRAC MIXED WATER = 0.0721271319 ETHANOL = 0.927872868 VLSTDMX MIXED = 3.85503517 VOLFLMX MIXED = 1481.4341 MOLEFLOW MIXED WATER = 0.774592763 ETHANOL = 3.89668323 MASSFLOW MIXED WATER = 13.9545055 ETHANOL = 179.516456 RHOMX MIXED = 0.130597079 MWMX MIXED = 41.4171548 SUBS-ATTR SUBSATTR TEMP_OUT MIXED = 150.0 TOT_FLOW = 4.67127599 VAP_ENTH = -100515.415 VAP_FLOW = 4.67127599 VFRAC_OUT MIXED = 1.0 VFRAC_OUT2 VLSTD VLSTDFR VLSTDMX MIXED = 3.85503517 VOLFLMX MIXED = 1481.4341 VOLFLMX2 = 1481.4341 VOLFLMX_GAS = 1481.4341 VOLFLMX_LIQ = None VOL_CYCLE VOL_PRICE = None VOL_TIME V_ENTR = -44.5273497 X WATER = 0.989917827 ETHANOL = 0.0100821734 X1 WATER = 0.989917827 ETHANOL = 0.0100821734 X2 WATER = 0.165820381 ETHANOL = 0.834179619 Y WATER = 0.165820381 ETHANOL = 0.834179619 CC Nodes ATTR CMP1 CNVATTR CNVLOWER CNVPSD CNVPSD1 CNVSPEC2 MIXED = 1 CNVSPEC3 = 1 CNVSPECS = 1 CNVUPPER CSFRAC CSFRAC2 CSFRAC3 CSFYES CSFYES2 CSFYES3 CSSUB = 0 CSTAB = 0 EDPN EDPN2 EDPN3 EMWN EMWN2 EMWN3 ENTCOMP ENTCOST = 0 ENTEOMOD = 0 ENTERED = 0 ENTREF MIXED = 0 ENTSUBSTR EQTO1 EQTO100 EQUA = 1 ESFL ESFL2 ESFL3 ESFR ESFR2 ESFR3 EZMO EZMO2 EZMO3 FLSHE MIXED = 0 FLSOPT MIXED = 1 FRAC MIXED = 0 FRAC1 MIXED = 1 GRTHEN1 GRTN100 L2CP1 = 0 L2CP2 = 1 MACEQTO1 MACGRTN1 MIXED MIXED = 1 MIXLOWER MIXPSD MIXPSD1 MIXUPPER NCLOWER NCPSD NCPSD1 NCSPEC2 MIXED = 1 NCSPEC3 = 1 NCSPECS = 1 NCSUB = 0 NCTAB = 0 NCUPPER NCVATTR NOFL MIXED = 1 NOFLOW1 MIXED = 1 NOFLOW10 MIXED = 1 NOFLOW11 MIXED = 1 NOFLOW2 MIXED = 1 NOFLOW3 MIXED = 1 NOFLOW4 MIXED = 1 NOFLOW5 MIXED = 1 NOFLOW6 MIXED = 1 NOFLOW7 MIXED = 1 NOFLOW8 MIXED = 1 NOFLOW9 MIXED = 1 NOTNC MIXED = 1 OUTLETSTRM1 = 1 OUTLETSTRM2 = 1 OUTLETSTRM3 = 1 OUTLETSTRM4 = 1 POLTRU POLTRU2 POLTRU3 POLYES POLYES2 POLYES3 PRES MIXED = 1 PSD1 PSD10 PSD11 PSD2 PSD3 PSD4 PSD5 PSD6 PSD7 PSD8 PSD9 PSPEC MIXED = 1 PSPEC2 MIXED = 1 PSPEC3 MIXED = 1 REFT1 MIXED = 0 REFT2 MIXED = 0 RMODE = 1 SAMEPRES1 MIXED = 1 SAMEPRES2 MIXED = 1 SAMEPRES3 MIXED = 1 SFRC = 0 SOLV MIXED = 0 SP3C2 = 1 SPAR = 1 SPEC2 MIXED = 1 SPEC3 = 1 SPEC4 MIXED = 1 SPECS = 1 SSCISOLID1 MIXED = 0 SSCISOLID2 MIXED = 0 SSCISORNC1 MIXED = 0 SSCISORNC2 SSCISORNC3 MIXED = 0 SSCISORNC4 SSMIXED1 MIXED = 1 SSMIXED2 MIXED = 1 SSMIXED3 MIXED = 1 SSMIXED4 MIXED = 1 SSMIXED5 MIXED = 1 SSMIXED6 MIXED = 1 SSMIXED7 MIXED = 1 SSMIXORCIS1 MIXED = 1 SSMIXORCIS2 MIXED = 1 SSMIXORCIS3 SSMIXORCIS4 SSMIXORNC1 MIXED = 1 SSMIXORNC2 MIXED = 1 SSMIXORNC3 SSMIXORNC4 SSNC1 MIXED = 0 SSNC2 MIXED = 0 SSNC3 MIXED = 0 SSNC4 MIXED = 0 SSREFTC MIXED = 0 TEMP MIXED = 1 VFRAC = 1 WFONE1 WFONE2 WFONE3 Ports DEST SOURCE FLASH = FLASH Connections #0 = DEST FLASH = SOURCE Comments Stream Results Display = STREAMS Units = TFF File = GEN_E Table Temperature F VAPOR = 150.0 Temperature F #1 = Pressure psia VAPOR = 20.00 Pressure psia #1 = Vapor Frac VAPOR = 1.000 Vapor Frac #1 = Mole Flow lbmol/hr VAPOR = 4.671 Mole Flow lbmol/hr #1 = Mass Flow lb/hr VAPOR = 193.471 Mass Flow lb/hr #1 = Volume Flow cuft/hr VAPOR = 1481.434 Volume Flow cuft/hr #1 = Enthalpy MMBtu/hr VAPOR = -0.470 Enthalpy MMBtu/hr #1 = Mass Flow VAPOR = Mass Flow #1 = WATER VAPOR = 13.955 WATER #1 = ETHANOL VAPOR = 179.516 ETHANOL #1 = Mass Frac VAPOR = Mass Frac #1 = WATER VAPOR = 0.072 WATER #1 = ETHANOL VAPOR = 0.928 ETHANOL #1 = Mole Flow VAPOR = Mole Flow #1 = WATER VAPOR = 0.775 WATER #1 = ETHANOL VAPOR = 3.897 ETHANOL #1 = Mole Frac VAPOR = Mole Frac #1 = WATER VAPOR = 0.166 WATER #1 = ETHANOL VAPOR = 0.834 ETHANOL #1 = Blocks FLASH Input Unit Set = ENG User Table User Tree ADDINPUT ALWAYS_INST = NO AUTO_COMPS = None AUTO_COMPS_T = 0.0 AUTO_PHASE = YES AUTO_PHASE_T = 0.1 BLKOPFREWAT = NO BOUND_TYPE CHECK_FREE_W = YES CHEMISTRY = None CHEM_METHOD = YES COMMENT COMPBAL = NOCOMPBAL CPEQP = 0.1194229483 CPMED = 1.003152766 DERIV_METHOD = None DESCRIPTION = None DIAMETER = None DUTY = None DUTY_TOL = None ENABLED ENERGY_BAL = YES ENTRN = 0.0 EOVAR_TYPE EO_COMPS = None EO_COMP_TOL = 1e-15 EO_DEP_COMPS = None EO_FORM = None EO_HEAVY_KEY = None EO_L2_COMP = None EO_LIGHT_KEY = None EO_PT_COMP EO_PT_PHASE EO_PT_PHYSQT EO_PT_TYPE EO_PT_UOM EO_PT_VALUE EO_TEMP_TOL = 0.0018 EQPHCP = NO FILE FLASH_FORM = PML FLASH_METHOD = None FLOW_TOL = None FRWATEROPSET = STEAM-TA FVC_ID1 FVC_ID2 FVC_SENTENCE FVC_VARIABLE FVN FVN_ELEM FVN_ID1 FVN_ID2 FVN_ID3 FVN_SENTENCE FVN_VARIABLE FVN_VARTYPE GLOBALSCRIPT HEADING HEATOPT = CONST-DUTY HENRY_COMPS = None HIERARCHY HIGH_PREC HOLDUP_MED = None HT2ENV = NO HTCEQP = 0.0880550918 HTYPE = ELLIPTICAL IDESCRIPTION INCR INDEP_VAR INIT_SCRIPT = None INLET_PHASE = None INPUT = INPUT INTERACTIVE = None IVENABLED IVLOWER IVNAME IVSCALE IVSPEC IVSTEP IVUPPER IVVALUE L2_COMP_MODE = AUTO LAMBDA = 975.9243336 LENGTH = None LEVELCONT = YES LINES LIQ1FRAC = None LIQFRAC = 0.5 LISTS LOCALSCRIPT MASSEQP = None MAXIT = 30 MIN_PRES = YES NEG_COMP_CHK = -1e-08 NEG_FLOW_CHK = 0.0 NEWPAGE = NONEWPAGE NPHASE = 2 NPOINTS ON_SMEO_DIFF = None OPSETNAME = PENG-ROB OPT_RANGE PDROP PHYS_QTY PRES = 20.0 PRESCONT = YES PRES_PROFILE PRES_TOL = 0.000145037738 PROPERTIES PROP_LEVEL = 4 P_EST = None RAMPED REBWIZ = None REPORT = REPORT RESTART = NO RESULTS = RESULTS SBWEIGHT SC_METHOD SC_TYPE SFRAC_TOL = 0.0001 SG_SPEC SIM_LEVEL = 4 SOLU_WATER = 3 SOLVE_METHOD = None SOLVE_OPEN = None SPARSITY = None SPC_DPI = YES SPC_HDUTY = YES SPC_PML = NO SPC_PRES = YES SPC_TEMP = YES SPC_VFRAC = YES SPEC_OPT = TP STREAM_LEVEL = 4 TAPPR = 18.0 TEMP = 150.0 TERM_LEVEL = 4 THRESHOLD THRU TMED = None TOL = 0.0001 TOTBAL = TOTBAL TRUE_COMPS = YES T_EST = None UOM USER_METHOD UTILITY_ID = None VAPOR VFRAC = None VFRACX_TOL = 1e-05 VFRAC_TOL = 0.001 VSTYPE = INSTANTANEOUS WALLHTC = 0.0880550918 WALLHTCDRY = 0.0880550918 WALLHTCWET = 0.0880550918 WETHT = NO WIDE Output Unit Set = Prop Data User Table User Tree BAL_ENTH_GEN = None BAL_ENTH_OUT = -5852662.03 BAL_FEEDCO2E = 0.0 BAL_MASG_FLW = None BAL_MASG_TFL = None BAL_MASI_TFL = 1000.00692 BAL_MASO_FLW = 1000.00691 BAL_MASO_TFL = 1000.00691 BAL_MASR_TFL = 4.76421351e-09 BAL_MOLG_FLW = 0.0 BAL_MOLG_TFL = 0.0 BAL_MOLI_TFL = 48.7488 BAL_MOLO_FLW = 48.7488 BAL_MOLO_TFL = 48.7488 BAL_MOLR_TFL = 0.0 BAL_NETSTRCO2E = 0.0 BAL_NNCG_FLW = None BAL_NNCI_FLW = None BAL_NNCO_FLW = None BAL_NNCR_FLW = None BAL_PRODCO2E = 0.0 BAL_TOTCO2E = 0.0 BAL_UTILCO2E = 0.0 BLKMSG = None BLKSTAT = 0 B_K WATER = 0.167509155 ETHANOL = 82.7443267 B_PRES = 20.0 B_PRES_IN = 137895.146 B_TEMP = 150.0 B_TEMP_IN = 338.705554 B_VFRAC = 0.0958234047 B_VFRAC_IN = None CMF_CATT CMF_HMX CMF_LFRAC CMF_MAFL CMF_MAMX CMF_MOFL CMF_MOMX CMF_MWMX CMF_NBOPST CMF_PRES CMF_PTARG CMF_QTARG CMF_RHOMX CMF_SATT CMF_SMX CMF_TEMP CMF_TTARG CMF_VFRAC CMF_VTARG COMP_ATTR DESCRIPTION = None DUTY_IN = None DUTY_OUT F WATER = 0.91095 ETHANOL = 0.08905 F2 GUID = None K1 K2 KODE = 11 LENTRN_IN = 0.0 LIQ_RATIO = 1.0 PDROP = -30.0 PER_ERROR PRES_OUT PROPSTAT = 0 P_EST = None QCALC = 101379.249 QNET = 101379.249 ROWSTAT ROWSTATSG SENTRN_IN SUBS_ATTR TEMP_OUT TOT_ENTH_ABS = -5954041.28 TOT_ENTH_REL = -0.0170269645 TOT_MASS_ABS = 1000.00692 TOT_MASS_REL = 4.76421351e-09 TOT_MOLE_ABS = 48.7488 TOT_MOLE_REL = 0.0 T_EST = None UTIL_CO2RATE = None UTIL_COST = None UTIL_DUTY = None UTL_ID = None UTL_USAGE = None VFRAC_OUT X WATER = 0.989917827 ETHANOL = 0.0100821734 X1 X2 Y WATER = 0.165820381 ETHANOL = 0.834179619 Y2 CC Nodes BKOP = 1 CCDYNFLSH = 0 CCDYNFLSH1 = 1 CCHEATCP = 0 CCHOLDUP = 0 CCHTDYN = 1 CCLAMBDA = 0 CCTAPPR = 0 CCTMED = 0 CHEML = 0 CHEMLOCK = 1 COMPOBJ DYNCSH0 = 1 DYNCSH1 = 1 DYNCSH3 = 1 DYNSH1 = 1 ENTADD = 0 ENTBLKDG = 0 ENTBLKPR = 0 ENTBLKRP = 0 ENTBLKSI = 0 ENTBLKSIB = 0 ENTEOMOD = 0 ENTHCADD ENTHCSET ENTIPT = 0 ENTOPT = 0 ENTRE = 0 ENTUTL = 0 EODEF EOENT EOENT1 EOENT2 EOPT1 EOPT2 EOPT3 EOPT4 EXISTD = 0 EXISTP = 1 EXISTSP = 0 EXISTST = 0 EXISTT = 1 EXISTVF = 0 FILESC FREE2 = 1 FREE3 = 0 FVCID1 FVCID2 FVCSENTENCE FVCVARIABLE FVNELEM FVNID1 FVNID2 FVNID3 FVNPROPSET FVNSENTENCE FVNVARIABLE FVNVARTYPE GENBLKOP = 1 GLOBSC HASDECANT = 0 HASDECANT1 = 0 HASHEAT1 = 0 HASHEAT2 = 0 HASHEAT3 = 0 HASHEAT4 = 0 HCLOCK = 1 HCV HENRYL = 0 IDYNAMIC = 1 IVENT IVSPEC IVUNIT JDYNAMIC = 1 KDYNAMIC = 1 L2CP1 = 0 L2CP2 = 1 LDYNAMIC = 1 LOCASC LOCKS = 0 MDYNAMIC = 1 ONE OPT1 = 1 OPTIONIC OPTIONLS OPTIONNP RMODE = 1 RTOPT = 0 SCMETH SFRC = 0 SGENTS SGENTV SGSPEC SGVAR1 SGVAR2 SGVAR3 SHT01 = 0 SHT0F1 = 0 SHT1F1 = 0 SHT234 = 0 SHT3F2 = 0 SHT3F3 = 0 SHT3O2 = 0 SHT4F1 = 0 SHT4L1 = 1 SHT4L2 = 0 SHT4L3 = 0 SLID1 SMENT SMODE = 1 SMSPEC SPAR = 1 UCSH0 = 0 UCSH1 = 0 UCSH2 = 0 UCSH3 = 0 UCSH4 = 0 UCSH5 = 0 UTLNOTREQD = 1 UTLRED = 1 VAREXIST1 VAREXIST2 VFRAC = 0 Ports F(IN) FEED = FEED HS(IN) V(OUT) VAPOR = VAPOR L(OUT) LIQUID = LIQUID WD(OUT) HS(OUT) Connections FEED = F(IN) VAPOR = V(OUT) LIQUID = L(OUT) Comments Subobjects Hcurves Ports Stream Results Display = STREAMS Units = TFF File = GEN_E Table Temperature F FEED = 100.0 Temperature F VAPOR = 150.0 Temperature F LIQUID = 150.0 Temperature F #3 = Pressure psia FEED = 50.00 Pressure psia VAPOR = 20.00 Pressure psia LIQUID = 20.00 Pressure psia #3 = Vapor Frac FEED = 0.000 Vapor Frac VAPOR = 1.000 Vapor Frac LIQUID = 0.000 Vapor Frac #3 = Mole Flow lbmol/hr FEED = 48.749 Mole Flow lbmol/hr VAPOR = 4.671 Mole Flow lbmol/hr LIQUID = 44.078 Mole Flow lbmol/hr #3 = Mass Flow lb/hr FEED = 1000.007 Mass Flow lb/hr VAPOR = 193.471 Mass Flow lb/hr LIQUID = 806.536 Mass Flow lb/hr #3 = Volume Flow cuft/hr FEED = 17.109 Volume Flow cuft/hr VAPOR = 1481.434 Volume Flow cuft/hr LIQUID = 13.632 Volume Flow cuft/hr #3 = Enthalpy MMBtu/hr FEED = -5.954 Enthalpy MMBtu/hr VAPOR = -0.470 Enthalpy MMBtu/hr LIQUID = -5.383 Enthalpy MMBtu/hr #3 = Mass Flow FEED = Mass Flow VAPOR = Mass Flow LIQUID = Mass Flow #3 = WATER FEED = 800.017 WATER VAPOR = 13.955 WATER LIQUID = 786.063 WATER #3 = ETHANOL FEED = 199.989 ETHANOL VAPOR = 179.516 ETHANOL LIQUID = 20.473 ETHANOL #3 = Mass Frac FEED = Mass Frac VAPOR = Mass Frac LIQUID = Mass Frac #3 = WATER FEED = 0.800 WATER VAPOR = 0.072 WATER LIQUID = 0.975 WATER #3 = ETHANOL FEED = 0.200 ETHANOL VAPOR = 0.928 ETHANOL LIQUID = 0.025 ETHANOL #3 = Mole Flow FEED = Mole Flow VAPOR = Mole Flow LIQUID = Mole Flow #3 = WATER FEED = 44.408 WATER VAPOR = 0.775 WATER LIQUID = 43.633 WATER #3 = ETHANOL FEED = 4.341 ETHANOL VAPOR = 3.897 ETHANOL LIQUID = 0.444 ETHANOL #3 = Mole Frac FEED = Mole Frac VAPOR = Mole Frac LIQUID = Mole Frac #3 = WATER FEED = 0.911 WATER VAPOR = 0.166 WATER LIQUID = 0.990 WATER #3 = ETHANOL FEED = 0.089 ETHANOL VAPOR = 0.834 ETHANOL LIQUID = 0.010 ETHANOL #3 = Heat Results Display = Units = TFF File = Work Results Display = Units = TFF File = Utilities Reactions Chemistry Reactions Convergence Conv-Options Input Unit Set = None User Table User Tree ACCELERATE = 0 AFFECT = YES BRACKET = NO BR_MAXIT = 30 BR_QMAX = 0.0 BR_QMIN = -5.0 BR_TMAXIT = 9999 BR_TRATIO = None BR_TTOL = None BR_WAIT = 2 BR_XTOL = 0.0001 CHECKSEQ = YES COMB_METHOD = BROYDEN COMPS = None CONST_ITER = 2 CONV_TEST = KKT DERIVATIVE = FORWARD DERIV_SWITCH = NO DIR_MAXIT = 30 EST_STEP = NO FLASH = YES LOOP_WEIGHT = 1 MAXLSPASS = 3 MAX_STEP_SIZ = 1.0 MSPEC_METHOD = BROYDEN NACCELERATE = 1 NEW_MAXIT = 30 NEW_MAXPASS = 99999 NEW_WAIT = 2 NEW_XTOL = 0.0001 NLIMIT = 3 N_QMAX = 0.0 N_QMIN = -5.0 N_TMAXIT = 9999 N_TRATIO = None N_TTOL = None OPT_B_TTOL = NO OPT_METHOD = SQP OPT_N_JAC = RED-FACTOR OPT_N_TTOL = NO RED_FACTOR = 0.2 REINIT = None SEC_MAXIT = 30 SEC_XTOL = 1e-08 SPEC_LOOP = INSIDE SPEC_METHOD = SECANT SQP_MAXIT = 30 SQP_MAXPASS = 99999 SQP_OPT_METH = SQP SQP_QMAX = 0.0 SQP_QMIN = -5.0 SQP_TOL = 0.001 SQP_WAIT = 2 STATE = PH STEP_DIR = NEGATIVE STEP_ENTH = 0.01 STEP_FLOW = 0.01 STEP_HEAT = 0.01 STEP_OPT = RANGE STEP_PRES = 0.01 STEP_SIZ = 0.01 STOP = YES TEAR_METHOD = WEGSTEIN TEAR_VAR = NO TEAR_WEIGHT = 1 TOL = 0.0001 TRACE = None TRACEOPT = CUTOFF UPDATE = NO USER_LOOP = OUTSIDE VARITERHIST = NO VAR_MIN = 0.0001 WEG_MAXIT = 30 WEG_QMAX = 0.0 WEG_QMIN = -5.0 WEG_WAIT = 1 XFINAL = XLAST Output Unit Set = Prop Data User Table User Tree CC Nodes BPARM = 0 BQMIN = 1 BRO1 = 1 BTT1 = 0 BTT2 = 0 DEFLT = 0 DEFLT2 = 0 DEFLT3 = 0 DPARM = 0 NEW1 = 1 NJAC1 = 1 NJAC2 = 0 NPARM = 0 NQMIN = 1 NTRA = 1 NTT1 = 0 NTT2 = 0 NTTE = 1 SPARM = 0 SQP1 = 1 SQPPAR = 0 SQQMIN = 1 WEG1 = 1 WPARM = 0 WQMIN = 1 Comments EO-Conv-Options Input Unit Set = None User Table User Tree ACTIVE ACTIVEINIT DEFAULT = NO SIMULATION = NO PARAMETER-ESTIMATION = NO RECONCILIATION = NO OPTIMIZATION = NO ACTIVERPT DEFAULT = NO SIMULATION = NO PARAMETER-ESTIMATION = NO RECONCILIATION = NO OPTIMIZATION = NO ACTIVESAVE DEFAULT = NO SIMULATION = NO PARAMETER-ESTIMATION = NO RECONCILIATION = NO OPTIMIZATION = NO ACTIVESPACE DEFAULT = 2 SIMULATION = 2 PARAMETER-ESTIMATION = 2 RECONCILIATION = 2 OPTIMIZATION = 2 ADCVITER DEFAULT = 100 SIMULATION = 100 PARAMETER-ESTIMATION = 100 RECONCILIATION = 100 OPTIMIZATION = 100 ADCVMETH DEFAULT = NONE SIMULATION = NONE PARAMETER-ESTIMATION = NONE RECONCILIATION = NONE OPTIMIZATION = NONE ADCVOBJCVG DEFAULT = 1e-06 SIMULATION = 1e-06 PARAMETER-ESTIMATION = 1e-06 RECONCILIATION = 1e-06 OPTIMIZATION = 1e-06 ADCVRESCVG DEFAULT = 1e-06 SIMULATION = 1e-06 PARAMETER-ESTIMATION = 1e-06 RECONCILIATION = 1e-06 OPTIMIZATION = 1e-06 ALFALS DEFAULT = 0.25 SIMULATION = 0.25 PARAMETER-ESTIMATION = 0.25 RECONCILIATION = 0.25 OPTIMIZATION = 0.25 ANALTHRESH DEFAULT = 2.0 SIMULATION = 2.0 PARAMETER-ESTIMATION = 2.0 RECONCILIATION = 2.0 OPTIMIZATION = 2.0 AUTOSCALEOBJ DEFAULT = NO SIMULATION = NO PARAMETER-ESTIMATION = NO RECONCILIATION = NO OPTIMIZATION = NO BASEOBJFACT DEFAULT = 1.0 SIMULATION = 1.0 PARAMETER-ESTIMATION = 1.0 RECONCILIATION = 1.0 OPTIMIZATION = 1.0 BASFLP DEFAULT = 100.0 SIMULATION = 100.0 PARAMETER-ESTIMATION = 100.0 RECONCILIATION = 100.0 OPTIMIZATION = 100.0 BIGBND DEFAULT = 1e+20 SIMULATION = 1e+20 PARAMETER-ESTIMATION = 1e+20 RECONCILIATION = 1e+20 OPTIMIZATION = 1e+20 BIGSCL DEFAULT = 10000000000.0 SIMULATION = 10000000000.0 PARAMETER-ESTIMATION = 10000000000.0 RECONCILIATION = 10000000000.0 OPTIMIZATION = 10000000000.0 BNDADJ DEFAULT = 1e-05 SIMULATION = 1e-05 PARAMETER-ESTIMATION = 1e-05 RECONCILIATION = 1e-05 OPTIMIZATION = 1e-05 BNDAPP DEFAULT = 0.99 SIMULATION = 0.99 PARAMETER-ESTIMATION = 0.99 RECONCILIATION = 0.99 OPTIMIZATION = 0.99 BOUNDRPT DEFAULT = YES SIMULATION = YES PARAMETER-ESTIMATION = YES RECONCILIATION = YES OPTIMIZATION = YES BSMALL DEFAULT = 1e-08 SIMULATION = 1e-08 PARAMETER-ESTIMATION = 1e-08 RECONCILIATION = 1e-08 OPTIMIZATION = 1e-08 BTF DEFAULT = YES SIMULATION = YES PARAMETER-ESTIMATION = YES RECONCILIATION = YES OPTIMIZATION = YES CHGBND DEFAULT = 0.25 SIMULATION = 0.25 PARAMETER-ESTIMATION = 0.25 RECONCILIATION = 0.25 OPTIMIZATION = 0.25 CHGMAX DEFAULT = 0.5 SIMULATION = 0.5 PARAMETER-ESTIMATION = 0.5 RECONCILIATION = 0.5 OPTIMIZATION = 0.5 CREEPFLAG DEFAULT = OFF SIMULATION = OFF PARAMETER-ESTIMATION = OFF RECONCILIATION = OFF OPTIMIZATION = OFF CREEPITER DEFAULT = 10 SIMULATION = 10 PARAMETER-ESTIMATION = 10 RECONCILIATION = 10 OPTIMIZATION = 10 CREEPSIZE DEFAULT = 0.1 SIMULATION = 0.1 PARAMETER-ESTIMATION = 0.1 RECONCILIATION = 0.1 OPTIMIZATION = 0.1 CWORKF DEFAULT = 1.0 SIMULATION = 1.0 PARAMETER-ESTIMATION = 1.0 RECONCILIATION = 1.0 OPTIMIZATION = 1.0 DELTLS DEFAULT = 0.1 SIMULATION = 0.1 PARAMETER-ESTIMATION = 0.1 RECONCILIATION = 0.1 OPTIMIZATION = 0.1 DENSITYRATIO DEFAULT = 0.7 SIMULATION = 0.7 PARAMETER-ESTIMATION = 0.7 RECONCILIATION = 0.7 OPTIMIZATION = 0.7 DERDIF DEFAULT = 0.001 SIMULATION = 0.001 PARAMETER-ESTIMATION = 0.001 RECONCILIATION = 0.001 OPTIMIZATION = 0.001 DERMIN DEFAULT = 0.01 SIMULATION = 0.01 PARAMETER-ESTIMATION = 0.01 RECONCILIATION = 0.01 OPTIMIZATION = 0.01 DIAGLEVEL = 2 DPERTF DEFAULT = 1e-06 SIMULATION = 1e-06 PARAMETER-ESTIMATION = 1e-06 RECONCILIATION = 1e-06 OPTIMIZATION = 1e-06 DROPTOL DEFAULT = 1e-20 SIMULATION = 1e-20 PARAMETER-ESTIMATION = 1e-20 RECONCILIATION = 1e-20 OPTIMIZATION = 1e-20 ETASKP DEFAULT = 0.95 SIMULATION = 0.95 PARAMETER-ESTIMATION = 0.95 RECONCILIATION = 0.95 OPTIMIZATION = 0.95 FACTORSPACE DEFAULT = 6 SIMULATION = 6 PARAMETER-ESTIMATION = 6 RECONCILIATION = 6 OPTIMIZATION = 6 FACTORSPEED DEFAULT = NORMAL SIMULATION = NORMAL PARAMETER-ESTIMATION = NORMAL RECONCILIATION = NORMAL OPTIMIZATION = NORMAL FAILFACTOR = 0.5 FEASOBJFACT DEFAULT = 1000000.0 SIMULATION = 1000000.0 PARAMETER-ESTIMATION = 1000000.0 RECONCILIATION = 1000000.0 OPTIMIZATION = 1000000.0 FEASREDUCT DEFAULT = NO SIMULATION = NO PARAMETER-ESTIMATION = NO RECONCILIATION = NO OPTIMIZATION = NO FREEONLY DEFAULT = YES SIMULATION = YES PARAMETER-ESTIMATION = YES RECONCILIATION = YES OPTIMIZATION = YES FSCALF DEFAULT = 0.01 SIMULATION = 0.01 PARAMETER-ESTIMATION = 0.01 RECONCILIATION = 0.01 OPTIMIZATION = 0.01 GLOBALOPTIM DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 GNPMAX DEFAULT = 1000000.0 SIMULATION = 1000000.0 PARAMETER-ESTIMATION = 1000000.0 RECONCILIATION = 1000000.0 OPTIMIZATION = 1000000.0 HESSIANSCL DEFAULT = 1.0 SIMULATION = 1.0 PARAMETER-ESTIMATION = 1.0 RECONCILIATION = 1.0 OPTIMIZATION = 1.0 HESSIANUPD DEFAULT = None SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 10 OPTIMIZATION = 10 HOMOTOPY = NO IDXCHK DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 IFDFREQ DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 IFDITER DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 IFDTYP DEFAULT = HES-NON SIMULATION = HES-NON PARAMETER-ESTIMATION = HES-NON RECONCILIATION = HES-NON OPTIMIZATION = HES-NON INICHK DEFAULT = 20 SIMULATION = 20 PARAMETER-ESTIMATION = 20 RECONCILIATION = 20 OPTIMIZATION = 20 INIHOMSTEP = 0.1 INITIAL IPSIRPT DEFAULT = BRIEF SIMULATION = BRIEF PARAMETER-ESTIMATION = BRIEF RECONCILIATION = BRIEF OPTIMIZATION = BRIEF ISRCHC DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 ITDGLG DEFAULT = 4 SIMULATION = 4 PARAMETER-ESTIMATION = 4 ITRBND DEFAULT = 3 SIMULATION = 3 PARAMETER-ESTIMATION = 3 RECONCILIATION = 3 OPTIMIZATION = 3 IWORKF DEFAULT = 1.0 SIMULATION = 1.0 PARAMETER-ESTIMATION = 1.0 RECONCILIATION = 1.0 OPTIMIZATION = 1.0 IXSCS DEFAULT = 4 SIMULATION = 4 PARAMETER-ESTIMATION = 4 RECONCILIATION = 4 OPTIMIZATION = 4 KBKOUT DEFAULT = 20 SIMULATION = 20 PARAMETER-ESTIMATION = 20 RECONCILIATION = 20 OPTIMIZATION = 20 KFOWDG DEFAULT = 10 SIMULATION = 10 PARAMETER-ESTIMATION = 10 RECONCILIATION = 10 OPTIMIZATION = 10 KMUDEC DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 KPFREQ DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 KPLLEV DEFAULT = 5 SIMULATION = 5 PARAMETER-ESTIMATION = 5 RECONCILIATION = 5 OPTIMIZATION = 5 KPNTOP DEFAULT = 10 SIMULATION = 10 PARAMETER-ESTIMATION = 10 RECONCILIATION = 10 OPTIMIZATION = 10 KPTLEV DEFAULT = 4 SIMULATION = 4 PARAMETER-ESTIMATION = 4 RECONCILIATION = 4 OPTIMIZATION = 4 LCHBAS DEFAULT = YES SIMULATION = YES PARAMETER-ESTIMATION = YES RECONCILIATION = YES OPTIMIZATION = YES LEWBAS DEFAULT = ORTHOGONAL SIMULATION = ORTHOGONAL PARAMETER-ESTIMATION = ORTHOGONAL RECONCILIATION = ORTHOGONAL OPTIMIZATION = ORTHOGONAL LINCST DEFAULT = NO SIMULATION = NO PARAMETER-ESTIMATION = NO RECONCILIATION = NO OPTIMIZATION = NO LINESEARCH DEFAULT = 3 SIMULATION = 3 PARAMETER-ESTIMATION = 3 RECONCILIATION = 3 OPTIMIZATION = 3 LINESRCMODE DEFAULT = NORMAL SIMULATION = NORMAL PARAMETER-ESTIMATION = NORMAL RECONCILIATION = NORMAL OPTIMIZATION = NORMAL LODIAG DEFAULT = 4 SIMULATION = 4 PARAMETER-ESTIMATION = 4 LSCOPT DEFAULT = 4 SIMULATION = 4 PARAMETER-ESTIMATION = 4 RECONCILIATION = 4 OPTIMIZATION = 4 LSIWORKF DEFAULT = 1.0 SIMULATION = 1.0 PARAMETER-ESTIMATION = 1.0 RECONCILIATION = 1.0 OPTIMIZATION = 1.0 LSIZEB1 DEFAULT = YES SIMULATION = YES PARAMETER-ESTIMATION = YES RECONCILIATION = YES OPTIMIZATION = YES LSIZEB2 DEFAULT = SCALED SIMULATION = SCALED PARAMETER-ESTIMATION = SCALED RECONCILIATION = SCALED OPTIMIZATION = SCALED LSMODEITER DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 LSRWORKF DEFAULT = 1.0 SIMULATION = 1.0 PARAMETER-ESTIMATION = 1.0 RECONCILIATION = 1.0 OPTIMIZATION = 1.0 LUBNDS DEFAULT = YES SIMULATION = YES PARAMETER-ESTIMATION = YES RECONCILIATION = YES OPTIMIZATION = YES LUSTATS DEFAULT = OFF SIMULATION = OFF PARAMETER-ESTIMATION = OFF RECONCILIATION = OFF OPTIMIZATION = OFF MAXBND DEFAULT = 20 SIMULATION = 20 PARAMETER-ESTIMATION = 20 MAXDIV DEFAULT = 20 SIMULATION = 20 PARAMETER-ESTIMATION = 20 MAXFITER = None MAXHOMSTEP = 1.0 MAXIMPITER DEFAULT = 13 SIMULATION = 13 PARAMETER-ESTIMATION = 13 RECONCILIATION = 13 OPTIMIZATION = 13 MAXIPASS = None MAXIT = None MAXITER DEFAULT = 50 SIMULATION = 50 PARAMETER-ESTIMATION = 50 RECONCILIATION = 50 OPTIMIZATION = 50 MAXITER_L DEFAULT = 50 SIMULATION = 50 PARAMETER-ESTIMATION = 50 RECONCILIATION = 50 OPTIMIZATION = 50 MAXITER_X DEFAULT = 50 SIMULATION = 50 PARAMETER-ESTIMATION = 50 RECONCILIATION = 50 OPTIMIZATION = 50 MAXIT_N DEFAULT = 100 SIMULATION = 100 PARAMETER-ESTIMATION = 100 MAXLSC DEFAULT = None SIMULATION = 1 PARAMETER-ESTIMATION = 10 RECONCILIATION = 10 OPTIMIZATION = 10 MAXLSF DEFAULT = None SIMULATION = 10 PARAMETER-ESTIMATION = 5 RECONCILIATION = 5 OPTIMIZATION = 5 MAXMIPITER DEFAULT = 100 SIMULATION = 100 PARAMETER-ESTIMATION = 100 RECONCILIATION = 100 OPTIMIZATION = 100 MAXQPF DEFAULT = 10 SIMULATION = 10 PARAMETER-ESTIMATION = 10 RECONCILIATION = 10 OPTIMIZATION = 10 MDHESS DEFAULT = None SIMULATION = 0 PARAMETER-ESTIMATION = 2 RECONCILIATION = 2 OPTIMIZATION = 0 MINBTFSIZE DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 MINHOMSTEP = 0.01 MINITER DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 MINITER_L DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 MINITER_X DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 MSFREQ DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 MSMETH DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 NACCELERATE = None NBDBAS DEFAULT = 10 SIMULATION = 10 PARAMETER-ESTIMATION = 10 RECONCILIATION = 10 OPTIMIZATION = 10 NCSRCH DEFAULT = 5 SIMULATION = 5 PARAMETER-ESTIMATION = 5 RECONCILIATION = 5 OPTIMIZATION = 5 NFEASB DEFAULT = 2 SIMULATION = 2 PARAMETER-ESTIMATION = 2 RECONCILIATION = 2 OPTIMIZATION = 2 NFINFB DEFAULT = 5 SIMULATION = 5 PARAMETER-ESTIMATION = 5 RECONCILIATION = 5 OPTIMIZATION = 5 NNDCMP DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 NUMDER DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 OBJCNVGTOL DEFAULT = 0.001 SIMULATION = 0.001 PARAMETER-ESTIMATION = 0.001 RECONCILIATION = 0.001 OPTIMIZATION = 0.001 OBJCVG DEFAULT = 1e-06 SIMULATION = 1e-06 PARAMETER-ESTIMATION = 1e-06 RECONCILIATION = 1e-06 OPTIMIZATION = 1e-06 PHYS_QTY PIVOTANAL DEFAULT = LOW SIMULATION = LOW PARAMETER-ESTIMATION = LOW RECONCILIATION = LOW OPTIMIZATION = LOW PIVOTSEARCH DEFAULT = 10 SIMULATION = 10 PARAMETER-ESTIMATION = 10 RECONCILIATION = 10 OPTIMIZATION = 10 PIVOTTHRESH DEFAULT = 0.1 SIMULATION = 0.1 PARAMETER-ESTIMATION = 0.1 RECONCILIATION = 0.1 OPTIMIZATION = 0.1 PIVOTZERO DEFAULT = 0.0 SIMULATION = 0.0 PARAMETER-ESTIMATION = 0.0 RECONCILIATION = 0.0 OPTIMIZATION = 0.0 POSTSOLVEID = None POSTSOLVEUSE = NO PRESOLVEID = None PRESOLVEOPS DEFAULT = 511 SIMULATION = 511 PARAMETER-ESTIMATION = 511 RECONCILIATION = 511 OPTIMIZATION = 511 PRESOLVEUSE = NO PRINTFREQ DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 PRINTLEVEL DEFAULT = BRIEF SIMULATION = BRIEF PARAMETER-ESTIMATION = BRIEF RECONCILIATION = BRIEF OPTIMIZATION = BRIEF PRINT_LEVEL = None QMAX = None QMIN = None QPCONVTOL DEFAULT = 1e-10 SIMULATION = 1e-10 PARAMETER-ESTIMATION = 1e-10 RECONCILIATION = 1e-10 OPTIMIZATION = 1e-10 QPDEPDIAGS DEFAULT = YES SIMULATION = YES PARAMETER-ESTIMATION = YES RECONCILIATION = YES OPTIMIZATION = YES QPHESSIANUPD DEFAULT = 20 SIMULATION = 20 PARAMETER-ESTIMATION = 20 RECONCILIATION = 20 OPTIMIZATION = 20 QPINFE DEFAULT = 0.0 SIMULATION = 0.0 PARAMETER-ESTIMATION = 0.0 RECONCILIATION = 0.0 OPTIMIZATION = 0.0 QPITER DEFAULT = 10 SIMULATION = 10 PARAMETER-ESTIMATION = 10 RECONCILIATION = 10 OPTIMIZATION = 10 QPMICROINF DEFAULT = OFF SIMULATION = OFF PARAMETER-ESTIMATION = OFF RECONCILIATION = OFF OPTIMIZATION = OFF QPMICROMAX DEFAULT = 5 SIMULATION = 5 PARAMETER-ESTIMATION = 5 RECONCILIATION = 5 OPTIMIZATION = 5 QPMICROTOL DEFAULT = 1e-12 SIMULATION = 1e-12 PARAMETER-ESTIMATION = 1e-12 RECONCILIATION = 1e-12 OPTIMIZATION = 1e-12 QPSTATS DEFAULT = OFF SIMULATION = OFF PARAMETER-ESTIMATION = OFF RECONCILIATION = OFF OPTIMIZATION = OFF RELAXOBJCVG DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 RELEPS DEFAULT = 0.0001 SIMULATION = 0.0001 PARAMETER-ESTIMATION = 0.0001 RECONCILIATION = 0.0001 OPTIMIZATION = 0.0001 RELMIPITER DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 RESCNVGTOL DEFAULT = 1e-06 SIMULATION = 1e-06 PARAMETER-ESTIMATION = 1e-06 RECONCILIATION = 1e-06 OPTIMIZATION = 1e-06 RESCVG DEFAULT = 1e-06 SIMULATION = 1e-06 PARAMETER-ESTIMATION = 1e-06 RECONCILIATION = 1e-06 OPTIMIZATION = 1e-06 RFEASB DEFAULT = None SIMULATION = 1e-06 PARAMETER-ESTIMATION = 0.01 RECONCILIATION = 0.01 OPTIMIZATION = 0.01 RFINFB DEFAULT = 1e-06 SIMULATION = 1e-06 PARAMETER-ESTIMATION = 1e-06 RECONCILIATION = 1e-06 OPTIMIZATION = 1e-06 RFRAC DEFAULT = 0.1 SIMULATION = 0.1 PARAMETER-ESTIMATION = 0.1 RIGORUPD DEFAULT = 25 SIMULATION = 25 PARAMETER-ESTIMATION = 25 RECONCILIATION = 25 OPTIMIZATION = 25 RRHIGH DEFAULT = 100.0 SIMULATION = 100.0 PARAMETER-ESTIMATION = 100.0 RECONCILIATION = 100.0 OPTIMIZATION = 100.0 RRLOW DEFAULT = 0.2 SIMULATION = 0.2 PARAMETER-ESTIMATION = 0.2 RECONCILIATION = 0.2 OPTIMIZATION = 0.2 RWORKF DEFAULT = 1.0 SIMULATION = 1.0 PARAMETER-ESTIMATION = 1.0 RECONCILIATION = 1.0 OPTIMIZATION = 1.0 SCREENFORM DEFAULT = TERMINAL SIMULATION = TERMINAL PARAMETER-ESTIMATION = TERMINAL RECONCILIATION = TERMINAL OPTIMIZATION = TERMINAL SEARCHMODE DEFAULT = NORMAL SIMULATION = NORMAL PARAMETER-ESTIMATION = NORMAL RECONCILIATION = NORMAL OPTIMIZATION = NORMAL SECORDERALG DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 SINGT1 DEFAULT = 1e-08 SIMULATION = 1e-08 PARAMETER-ESTIMATION = 1e-08 RECONCILIATION = 1e-08 OPTIMIZATION = 1e-08 SINGT2 DEFAULT = 1e-10 SIMULATION = 1e-10 PARAMETER-ESTIMATION = 1e-10 RECONCILIATION = 1e-10 OPTIMIZATION = 1e-10 SINGULARHAND DEFAULT = NORMAL SIMULATION = NORMAL PARAMETER-ESTIMATION = NORMAL RECONCILIATION = NORMAL OPTIMIZATION = NORMAL SKIP_INIT = None SMLSCL DEFAULT = 1e-08 SIMULATION = 1e-08 PARAMETER-ESTIMATION = 1e-08 RECONCILIATION = 1e-08 OPTIMIZATION = 1e-08 SOLVER = DMO SPDROP DEFAULT = 1e-15 SIMULATION = 1e-15 PARAMETER-ESTIMATION = 1e-15 RECONCILIATION = 1e-15 OPTIMIZATION = 1e-15 STEPFACTOR = 10.0 STEPMODE DEFAULT = NO SIMULATION = NO PARAMETER-ESTIMATION = NO RECONCILIATION = NO OPTIMIZATION = NO STEPSIZE DEFAULT = 0.1 SIMULATION = 0.1 PARAMETER-ESTIMATION = 0.1 RECONCILIATION = 0.1 OPTIMIZATION = 0.1 TARGET TAUHYB DEFAULT = 0.1 SIMULATION = 0.1 PARAMETER-ESTIMATION = 0.1 RECONCILIATION = 0.1 OPTIMIZATION = 0.1 TEMPBNDPERT DEFAULT = 0.01 SIMULATION = 0.01 PARAMETER-ESTIMATION = 0.01 RECONCILIATION = 0.01 OPTIMIZATION = 0.01 TOLANA DEFAULT = 0.1 SIMULATION = 0.1 PARAMETER-ESTIMATION = 0.1 RECONCILIATION = 0.1 OPTIMIZATION = 0.1 TOLBAS DEFAULT = 0.1 SIMULATION = 0.1 PARAMETER-ESTIMATION = 0.1 RECONCILIATION = 0.1 OPTIMIZATION = 0.1 TOLF DEFAULT = 1e-06 SIMULATION = 1e-06 PARAMETER-ESTIMATION = 1e-06 TOLFMX DEFAULT = 1e+30 SIMULATION = 1e+30 PARAMETER-ESTIMATION = 1e+30 TOLINI = None TOLV DEFAULT = 0.01 SIMULATION = 0.01 PARAMETER-ESTIMATION = 0.01 TRACELEVEL DEFAULT = LOW SIMULATION = LOW PARAMETER-ESTIMATION = LOW RECONCILIATION = LOW OPTIMIZATION = LOW TRUSTITER DEFAULT = 2 SIMULATION = 2 PARAMETER-ESTIMATION = 2 RECONCILIATION = 2 OPTIMIZATION = 2 TRUSTMARGIN DEFAULT = 1.0 SIMULATION = 1.0 PARAMETER-ESTIMATION = 1.0 RECONCILIATION = 1.0 OPTIMIZATION = 1.0 TRUSTMAXIT DEFAULT = 20 SIMULATION = 20 PARAMETER-ESTIMATION = 20 RECONCILIATION = 20 OPTIMIZATION = 20 TRUSTMODE DEFAULT = OFF SIMULATION = OFF PARAMETER-ESTIMATION = OFF RECONCILIATION = OFF OPTIMIZATION = OFF TRUSTMODE_X DEFAULT = GLOBAL SIMULATION = GLOBAL PARAMETER-ESTIMATION = GLOBAL RECONCILIATION = GLOBAL OPTIMIZATION = GLOBAL TRUSTRAMPIT DEFAULT = 2 SIMULATION = 2 PARAMETER-ESTIMATION = 2 RECONCILIATION = 2 OPTIMIZATION = 2 TRUSTSIZE DEFAULT = 0.1 SIMULATION = 0.1 PARAMETER-ESTIMATION = 0.1 RECONCILIATION = 0.1 OPTIMIZATION = 0.1 UOM USEDROPTOL DEFAULT = OFF SIMULATION = OFF PARAMETER-ESTIMATION = OFF RECONCILIATION = OFF OPTIMIZATION = OFF VARCNVGTOL DEFAULT = 100000000.0 SIMULATION = 100000000.0 PARAMETER-ESTIMATION = 100000000.0 RECONCILIATION = 100000000.0 OPTIMIZATION = 100000000.0 VARIABLE VARSCALE DEFAULT = ON SIMULATION = ON PARAMETER-ESTIMATION = ON RECONCILIATION = ON OPTIMIZATION = ON VMUFAC DEFAULT = 2.0 SIMULATION = 2.0 PARAMETER-ESTIMATION = 2.0 RECONCILIATION = 2.0 OPTIMIZATION = 2.0 VMUINI DEFAULT = 0.001 SIMULATION = 0.001 PARAMETER-ESTIMATION = 0.001 RECONCILIATION = 0.001 OPTIMIZATION = 0.001 VMUMIN DEFAULT = 1e-08 SIMULATION = 1e-08 PARAMETER-ESTIMATION = 1e-08 RECONCILIATION = 1e-08 OPTIMIZATION = 1e-08 WAIT = None WARMSTART DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 XPMIN DEFAULT = 0.01 SIMULATION = 0.01 PARAMETER-ESTIMATION = 0.01 RECONCILIATION = 0.01 OPTIMIZATION = 0.01 ZPERTF DEFAULT = 0.0001 SIMULATION = 0.0001 PARAMETER-ESTIMATION = 0.0001 RECONCILIATION = 0.0001 OPTIMIZATION = 0.0001 Output Unit Set = Prop Data User Table User Tree CC Nodes DMOBAS DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 DMOITER DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 ENTDMO1 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTDMO2 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTDMO3 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTDMO4 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTDMO5 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTDMO6 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTDMO7 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTDMO8 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTDMO9 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTHOMO = 0 ENTHOMP ENTLSQ1 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTLSQ10 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTLSQ11 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTLSQ2 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTLSQ3 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTLSQ4 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTLSQ5 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTLSQ6 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTLSQ7 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTLSQ8 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTLSQ9 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTNSL1 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 ENTNSL2 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 ENTNSL3 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 ENTSMI1 = 0 ENTSMI2 = 0 ENTSMI3 = 0 ENTSMI4 = 0 ENTXSLP1 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTXSLP2 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTXSLP3 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 ENTXSLP4 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 GENHOM = 0 HOMENB = 1 HOMOPT = 1 HOMPAR = 1 LSSBAS DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 LSSQPITER DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 METHD1 DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 METHD2 DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 METHD3 DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 SCALF DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 SMNSOLVE = 1 SMRUNMOD1 = 1 SMRUNMOD2 = 1 SMRUNMOD3 = 1 SMRUNMOD4 = 1 SOLVE = 1 UNIQVAR = 1 XSLP1 DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 XSLP2 DEFAULT = 0 SIMULATION = 0 PARAMETER-ESTIMATION = 0 RECONCILIATION = 0 OPTIMIZATION = 0 XSLP3 DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 XSLPBAS DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 XSLPITER DEFAULT = 1 SIMULATION = 1 PARAMETER-ESTIMATION = 1 RECONCILIATION = 1 OPTIMIZATION = 1 Comments Tear Input Unit Set = None User Table User Tree COMPS STATE TOL TRACE Output Unit Set = Prop Data User Table User Tree CC Nodes ISTEAR ROOT TEARS Comments Convergence Conv-Order Input Unit Set = None User Table User Tree CVBLOCK Output Unit Set = Prop Data User Table User Tree CC Nodes ROOT = 0 Comments Sequence Costing Cost-Options Input Unit Set = ENG User Table User Tree BASE_INDEX CENTROID CURRENT_INDE DESCRIPTION = None END = EQUIPMENT-COST ESCALATION EXCHANGE_RAT = 1.0 FILE_SYM_NAM = NO INDEX_MONTH INDEX_YEAR IN_EXCHANGE = 1.0 IN_SYMBOL = None MONTH = None MONTHS = None NAME1 PRF_YEAR PURCH_INDEX PUR_MONTH = None PUR_YEAR = None QUARTER RATE SOURCE ST_MONTH = None ST_YEAR = None SYMBOL = None YEAR = None Output Unit Set = Prop Data User Table User Tree CC Nodes DATE = 1 ECON1 = 1 IND IND1 Comments Equipment Labor-Cost Input Unit Set = ENG User Table User Tree ADJ_JOB_COND = None DESCRIPTION = None EXP_RATE = None INDEX = None INDEX_TYPE = LABOR LOCATION = None MONTH = None RATE = None UNADJ_JOB_CO = 1.0 YEAR = None Output Unit Set = Prop Data User Table User Tree CC Nodes LAB = 0 Comments Cost-Section Capital-Cost Input Unit Set = ENG User Table User Tree AMOUNT BA_AMOUNT = None BA_FACTOR = 0.1 COM_AMOUNT COM_HOURS COM_INDEX COM_JOB_COND COM_LAB_FAC COM_MAT_FAC COM_MONTH COM_WEIGHT COM_YEAR C_AMOUNT = None C_FACTOR = 0.12 C_INDEX_TYPE DESCRIPTION = None DE_AMOUNT = None DE_FACTOR = 0.2 D_AMOUNT = None D_FACTOR = 0.0 FIELD_AMOUNT = None FR_AMOUNT = None FR_FACTOR = 0.02 F_AMOUNT = None F_FACTOR = 0.08 HOURS INDEX INDEX_TYPE IND_HOURS = None IND_LAB_FAC = 0.73 IND_MAT_FAC = 0.27 JOB_COND LAB_FAC LA_AMOUNT = None LA_FACTOR = 0.02 MAT_FAC MONTH N_AMOUNT = None N_FACTOR = 0.0 O_AMOUNT = None O_FACTOR = 0.056 RO_AMOUNT = None RO_FACTOR = 0.0 SA_AMOUNT = None SA_FACTOR = 0.03 SITE_AMOUNT = None SITE_HOURS = None SITE_LAB_FAC = 0.02 SITE_MAT_FAC = 0.01 YEAR Output Unit Set = Prop Data User Table User Tree CC Nodes ADD1 = 1 CONT = 1 IND = 1 INST = 1 PLANT1 = 1 SERV SITE1 = 1 Comments Materials Operating-Cost Input Unit Set = ENG User Table User Tree ADD_FACTOR = 0.0 AMOUNT = None CAT_INDEX = None CAT_MONTH = None CAT_YEAR = None C_INDEX_TYPE = CHEMICAL DAYS = None DESCRIPTION = None EXP_PRICE = None EXP_RATE = None FACTOR = 0.9 FRINGE = 0.4 GEN_ADMIN = 0.6 INDEX = None INDEX_TYPE = OPER-LAB INSURANCE = 0.008 LABOR_REQ = None LAB_FACTOR = 0.0 LIFE = 15.0 MAINT = 0.024 MAINTENANCE = 0.036 MONTH = None NO = 1 NOPER = None NOPER1 = None OPERATING = 0.1 PRICE = None PROCESS_STEP = None PROD = 1.0 RATE = None SUPERVISION = 0.2 TAX = 0.02 USAGE = None YEAR = None Output Unit Set = Prop Data User Table User Tree CC Nodes MAIN = 0 OTH = 1 Comments Profit Input Unit Set = ENG User Table User Tree ADMIN = 0.09 AMOUNT BALANCE_TOL = 0.001 CAPACITY CASH_FLOW CASH_METH = 0 CONSTR_IRR = None CONSTR_RATE = None CREDIT = 0.1 DEP_BLD_FAC = 1.0 DEP_EQP_FAC = 0.95 DESCRIPTION = None DISCOUNT_RAT = 0.17 D_FRAC FRAC FRACTION = 0.0 IRR = None IRR_BOUND = 2.0 IRR_TOL = 0.1 LIFE = 15 MAXIT = 50 METHOD = IRS MODE = IRR MONTHS = None PLANT_FRAC = 0.0 PLANT_RATE = None P_CASH_FLOW RATE = 0.4 SALES = 0.03 SALV_AMT = None SALV_FAC = 0.07 STATE = 0.074 STEP_SIZE = 0.1 XAMOUNT XCAPACITY XD_FRAC XFRAC YEARS = None Output Unit Set = Prop Data User Table User Tree CC Nodes DEBT1 = 1 MAIN = 0 PROF = 1 TAX1 = 1 Comments Flowsheeting Options Design-Spec Calculator Transfer Stream-Lib Input Unit Set = ENG User Table User Tree CASE COMPS LIB_ID STATE STREAMS STR_OPT SUBSTREAMS TRANS1_C2 TRANS_C1 TRANS_C2 Output Unit Set = Prop Data User Table User Tree CC Nodes ENTDE ENTSP ONESTRM SAMECOMPS SPEC SPEC1 = 1 STRM STRM1 Comments Balance Pres-Relief Add-Input Add-Before Input Unit Set = None User Table User Tree ADDINPUT Output Unit Set = Prop Data User Table User Tree CC Nodes ENTBEFORE = 0 Comments Add-After Input Unit Set = None User Table User Tree ADDINPUT Output Unit Set = Prop Data User Table User Tree CC Nodes ENTAFTER = 0 Comments Measurement Model Analysis Tools Sensitivity Optimization Constraint Data-Fit Data-Set Regression EO Configuration Solve-Options Input Unit Set = None User Table User Tree METHOD = SM MODE = SIM OPTOBJ = None RECOBJ = None SEPSEQ = NO SM_STRATEGY = ALL Output Unit Set = Prop Data User Table User Tree CC Nodes MAIN = 1 SEQU = 1 SMNSOLVE = 1 SOLVE = 1 SOLVEENT = 1 Comments EO Input Input Unit Set = None User Table User Tree BOUND_TYPE DESCRIPTION = None EOVAR_TYPE IDESCRIPTION IVENABLED IVLOWER IVNAME IVSCALE IVSPEC IVSTEP IVUPPER IVVALUE PHYS_QTY RAMPED SBWEIGHT THRESHOLD UOM Output Unit Set = Prop Data User Table User Tree BLKSTAT = None PER_ERROR PROPSTAT = None CC Nodes IVENT IVSPEC IVUNIT Comments Aliases Input Unit Set = None User Table User Tree VAR Output Unit Set = Prop Data User Table User Tree BLKSTAT = None PER_ERROR PROPSTAT = None CC Nodes ENTN SPEC Comments Objective Spec Groups Input Unit Set = None User Table User Tree COMMENT DESCRIPTION = None ENABLED HIERARCHY SG_SPEC Output Unit Set = Prop Data User Table User Tree BLKSTAT = None PER_ERROR PROPSTAT = None ROWSTATSG CC Nodes SGENTS SGENTV SGSPEC SGVAR1 SGVAR2 SGVAR3 VAREXIST1 VAREXIST2 Comments Connection Input Unit Set = None User Table User Tree BIAS COMMENT DESCRIPTION = None DESTINATION DESTISPORT ENABLED SCALE SOURCE SOURCEISPORT Output Unit Set = Prop Data User Table User Tree BLKSTAT = None PER_ERROR PROPSTAT = None ROWSTAT CC Nodes ENTN PCCK SPEC Comments Ports Model Options Input Unit Set = None User Table User Tree ALWAYS_INST = NO AUTO_COMPS = None AUTO_COMPS_T = 0.0 AUTO_PHASE = YES AUTO_PHASE_T = 0.1 CHECK_FREE_W = YES CHEM_METHOD = YES COMP_TOL = 1e-15 DERIV_METHOD = None DUTY_TOL = 341.2141633 EO_COMPS = None EO_DEP_COMPS = None EO_FORM = None EO_HEAVY_KEY = None EO_LIGHT_KEY = None FLASH_FORM = PML FLOW_TOL = 0.7936641439 INIT_SCRIPT = None INLET_PHASE = None INTERACTIVE = NO L2_COMP = None L2_COMP_MODE = AUTO MIN_PRES = YES MO_ALWAYS_IN MO_AU_COMPS MO_AU_COMP_T MO_AU_PHASE MO_AU_PHAS_T MO_CHECK_FW MO_CHEM_METH MO_COMPS MO_COMP_TOL MO_DEP_COMPS MO_DERIV_MTH MO_DUTY_TOL MO_EO_FORM MO_FLASH_FO MO_FLOW_TOL MO_HEAVY_KEY MO_INIT_SCRI MO_INLET_PHA MO_L2_COMP MO_L2_COMP_M MO_LIGHT_KEY MO_MIN_PRES MO_NEG_COMP MO_NEG_FLOW MO_ON_SMEO_D MO_PASS_THRU MO_PRES_TOL MO_SFRAC_TOL MO_SOLVE_MTH MO_SPARSITY MO_TEMP_TOL MO_VFRACX_TO MO_VFRAC_TOL NEG_COMP_CHK = -1e-08 NEG_FLOW_CHK = 0.0 ON_SMEO_DIFF = USE-CLOSED PASS_THROUGH = NO PRES_TOL = 0.000145037738 SFRAC_TOL = 0.0001 SOLVE_METHOD = None SO_ALWAYS_IN SO_AU_COMPS SO_AU_COMP_T SO_AU_PHASE SO_AU_PHAS_T SO_CHECK_FW SO_CHEM_METH SO_COMPS SO_COMP_TOL SO_DEP_COMPS SO_DERIV_MTH SO_DUTY_TOL SO_EO_FORM SO_FLASH_FO SO_FLOW_TOL SO_HEAVY_KEY SO_INIT_SCRI SO_INLET_PHA SO_INTERACTI SO_L2_COMP SO_L2_COMP_M SO_LIGHT_KEY SO_MIN_PRES SO_NEG_COMP SO_NEG_FLOW SO_ON_SMEO_D SO_PASS_THRU SO_PRES_TOL SO_SFRAC_TOL SO_SOLVE_MTH SO_SPARSITY SO_TEMP_TOL SO_VFRACX_TO SO_VFRAC_TOL SPARSITY = None TEMP_TOL = 0.0018 VFRACX_TOL = 1e-05 VFRAC_TOL = 0.001 Output Unit Set = Prop Data User Table User Tree CC Nodes ENTMOD ENTPAR = 0 ENTSEC L2CP = 0 L2CP2 = 1 MOCP2 MOL2 MOSFRC OR SECP2 SEL2 SESFRC SFRC = 0 Comments Local Scripts Global Scripts Script Method Input Unit Set = None User Table User Tree FILE GLOBALSCRIPT LOCALSCRIPT SC_METHOD SC_TYPE USER_METHOD Output Unit Set = Prop Data User Table User Tree CC Nodes FILESC GLOBSC LOCASC SCMETH SMENT SMSPEC Comments EO-Sensitivity EO VarGrid Input Unit Set = None User Table User Tree Output Unit Set = Prop Data User Table User Tree CC Nodes Comments Results Summary Run-Status Input Unit Set = None User Table User Tree Output Unit Set = Prop Data User Table User Tree BLKSTAT = None CSSTAT = 2 CSSTAT2 = None CVSTAT = 2 CVSTAT2 = None DESCRIPTION = None FORSTAT = 2 INPUT = _1324gej.inm ITDATE = AUGUST 22, 2012 3:15:12 P.M. ITSTAT = 0 MACHINE = WIN32 NODENAME = PDS04V2 NODENAME2 = None NUMBER = None PAMB = 14.6959488 PCESSTAT = None PER_ERROR PPSTAT = 2 PROPSTAT = None RPTSTAT = 0 RSTAT = 0 RSTAT2 = None RUNID = _1324gej SENSSTAT = 2 SENSSTAT2 = None SITEID = SITEID2 = None SPDATE = AUGUST 22, 2012 3:15:12 P.M. SSTAT = 0 SSTAT2 = None TOTSTAT = 0 UOSSTAT = 0 UOSSTAT2 = 8 USER = jeslick USER2 = None VERNO = 25.0 CC Nodes Comments Stream-Sum Stream-Sum Display = ALLSTREAMS Units = TFF File = GEN_E Table Temperature F FEED = 100.0 Temperature F LIQUID = 150.0 Temperature F VAPOR = 150.0 Temperature F #3 = Pressure psia FEED = 50.00 Pressure psia LIQUID = 20.00 Pressure psia VAPOR = 20.00 Pressure psia #3 = Vapor Frac FEED = 0.000 Vapor Frac LIQUID = 0.000 Vapor Frac VAPOR = 1.000 Vapor Frac #3 = Mole Flow lbmol/hr FEED = 48.749 Mole Flow lbmol/hr LIQUID = 44.078 Mole Flow lbmol/hr VAPOR = 4.671 Mole Flow lbmol/hr #3 = Mass Flow lb/hr FEED = 1000.007 Mass Flow lb/hr LIQUID = 806.536 Mass Flow lb/hr VAPOR = 193.471 Mass Flow lb/hr #3 = Volume Flow cuft/hr FEED = 17.109 Volume Flow cuft/hr LIQUID = 13.632 Volume Flow cuft/hr VAPOR = 1481.434 Volume Flow cuft/hr #3 = Enthalpy MMBtu/hr FEED = -5.954 Enthalpy MMBtu/hr LIQUID = -5.383 Enthalpy MMBtu/hr VAPOR = -0.470 Enthalpy MMBtu/hr #3 = Mass Flow FEED = Mass Flow LIQUID = Mass Flow VAPOR = Mass Flow #3 = WATER FEED = 800.017 WATER LIQUID = 786.063 WATER VAPOR = 13.955 WATER #3 = ETHANOL FEED = 199.989 ETHANOL LIQUID = 20.473 ETHANOL VAPOR = 179.516 ETHANOL #3 = Mass Frac FEED = Mass Frac LIQUID = Mass Frac VAPOR = Mass Frac #3 = WATER FEED = 0.800 WATER LIQUID = 0.975 WATER VAPOR = 0.072 WATER #3 = ETHANOL FEED = 0.200 ETHANOL LIQUID = 0.025 ETHANOL VAPOR = 0.928 ETHANOL #3 = Mole Flow FEED = Mole Flow LIQUID = Mole Flow VAPOR = Mole Flow #3 = WATER FEED = 44.408 WATER LIQUID = 43.633 WATER VAPOR = 0.775 WATER #3 = ETHANOL FEED = 4.341 ETHANOL LIQUID = 0.444 ETHANOL VAPOR = 3.897 ETHANOL #3 = Mole Frac FEED = Mole Frac LIQUID = Mole Frac VAPOR = Mole Frac #3 = WATER FEED = 0.911 WATER LIQUID = 0.990 WATER VAPOR = 0.166 WATER #3 = ETHANOL FEED = 0.089 ETHANOL LIQUID = 0.010 ETHANOL VAPOR = 0.834 ETHANOL #3 = Conv-Sum Utility-Sum Input Unit Set = None User Table User Tree Output Unit Set = Prop Data User Table User Tree BLKCO2RATE BLKSTAT = None CO2TAX = 0.0 DEGSUB_IN DEGSUB_OUT DEGSUP_IN DEGSUP_OUT DUTY ELEC_PRICE EMDATASOURCE EMEFFICIENCY EMFACTOR EMFUELTYPE ENERGY_PRICE ENTH_IN ENTH_OUT FEEDCO2E = 0.0 FEEDSTR_COST = None FSTRMASSFLOW PLANT FEED = 1000.00692 FSTRMCO2E PLANT FEED = 0.0 HCO2TAX PLANT = 0.0 HCOOL HFEEDCO2E PLANT = 0.0 HNETSTRCO2E PLANT = 0.0 HPRODCO2E PLANT = 0.0 HTOTCO2E PLANT = 0.0 HUTILCO2E PLANT = 0.0 IN_PRES IN_TEMP IN_VF NETSTRCO2E = 0.0 NETSTR_COST = None NET_CO2RATE = None NET_COST = None NET_DUTY = None OUT_PRES OUT_TEMP PER_ERROR PPRICE PRODCO2E = 0.0 PRODSTR_COST = None PROPSTAT = None PSTRMASSFLOW PLANT VAPOR = 193.470961 LIQUID = 806.53595 PSTRMCO2E PLANT VAPOR = 0.0 LIQUID = 0.0 STRMCO2E = None TCOST TOTCO2E = 0.0 TOT_COOL_COST = None TOT_COOL_DUTY = None TOT_HEAT_COST = None TOT_HEAT_DUTY = None TRATE UTILCO2E = 0.0 UTIL_TYPE VFRAC CC Nodes Comments Dynamic Configuration Dynamic Options Input Unit Set = None User Table User Tree AUTO_PHASE = YES COMP OPT_COMP = INCLUDEALL Output Unit Set = Prop Data User Table User Tree CC Nodes CCDYN = 0 DYNOPTENT = 0 IDYNAMIC = 1 REMOVECOMPS = 0 Comments Unit Table AREA sqm = 1 sqft = 2 sqm = 3 sqcm = 4 sqin = 5 sqmile = 6 sqmm = 7 COMPOSITION mol-fr = 1 mol-fr = 2 mol-fr = 3 mass-fr = 4 DENSITY kg/cum = 1 lb/cuft = 2 gm/cc = 3 lb/gal = 4 gm/cum = 5 gm/ml = 6 lb/bbl = 7 DIFFUSIVITY sqm/sec = 1 sqft/hr = 2 sqcm/sec = 3 cs = 4 ENERGY J = 1 Btu = 2 cal = 3 kcal = 4 kWhr = 5 ft-lbf = 6 GJ = 7 kJ = 8 N-m = 9 MJ = 10 Mcal = 11 Gcal = 12 MBtu = 13 MMBtu = 14 hp-hr = 15 ENTHALPY J/kmol = 1 Btu/lbmol = 2 cal/mol = 3 J/kg = 4 Btu/lb = 5 cal/gm = 6 MBtu/lbmol = 7 ENTROPY J/kmol-K = 1 Btu/lbmol-R = 2 cal/mol-K = 3 J/kg-K = 4 Btu/lb-R = 5 cal/gm-K = 6 MJ/kmol-K = 7 kcal/kmol-K = 8 Gcal/kmol-K = 9 MBtu/lbmol-R = 10 FISCAL $ = 1 $ = 2 $ = 3 FLOW kg/sec = 1 lb/hr = 2 kg/hr = 3 lb/sec = 4 Mlb/hr = 5 tons/day = 6 Mcfh = 7 tonne/hr = 8 lb/day = 9 kg/day = 10 tons/hr = 11 kg/min = 12 kg/year = 13 gm/min = 14 gm/hr = 15 gm/day = 16 Mgm/hr = 17 Ggm/hr = 18 Mgm/day = 19 Ggm/day = 20 lb/min = 21 MMlb/hr = 22 Mlb/day = 23 MMlb/day = 24 lb/year = 25 Mlb/year = 26 MMlb/year = 27 tons/min = 28 Mtons/year = 29 MMtons/year = 30 L-tons/min = 31 L-tons/hr = 32 L-tons/day = 33 ML-tons/year = 34 MML-tons/year = 35 ktonne/year = 36 kg/oper-year = 37 lb/oper-year = 38 Mlb/oper-year = 39 MMlb/oper-year = 40 Mtons/oper-year = 41 MMtons/oper-year = 42 ML-tons/oper-year = 43 MML-tons/oper-year = 44 ktonne/oper-year = 45 MASS-FLOW kg/sec = 1 lb/hr = 2 kg/hr = 3 lb/sec = 4 Mlb/hr = 5 tons/day = 6 gm/sec = 7 tonne/hr = 8 lb/day = 9 kg/day = 10 tons/year = 11 tons/hr = 12 tonne/day = 13 tonne/year = 14 kg/min = 15 kg/year = 16 gm/min = 17 gm/hr = 18 gm/day = 19 Mgm/hr = 20 Ggm/hr = 21 Mgm/day = 22 Ggm/day = 23 lb/min = 24 MMlb/hr = 25 Mlb/day = 26 MMlb/day = 27 lb/year = 28 Mlb/year = 29 MMlb/year = 30 tons/min = 31 Mtons/year = 32 MMtons/year = 33 L-tons/min = 34 L-tons/hr = 35 L-tons/day = 36 ML-tons/year = 37 MML-tons/year = 38 ktonne/year = 39 tons/oper-year = 40 tonne/oper-year = 41 kg/oper-year = 42 lb/oper-year = 43 Mlb/oper-year = 44 MMlb/oper-year = 45 Mtons/oper-year = 46 MMtons/oper-year = 47 ML-tons/oper-year = 48 MML-tons/oper-year = 49 ktonne/oper-year = 50 MOLE-FLOW kmol/sec = 1 lbmol/hr = 2 kmol/hr = 3 MMscfh = 4 MMscmh = 5 mol/sec = 6 lbmol/sec = 7 scmh = 8 lbmol/day = 9 kmol/day = 10 MMscfd = 11 Mscfd = 12 scfm = 13 mol/min = 14 kmol/khr = 15 kmol/Mhr = 16 mol/hr = 17 Mmol/hr = 18 Mlbmol/hr = 19 lbmol/Mhr = 20 lbmol/MMhr = 21 Mscfm = 22 scfh = 23 Mscfh = 24 scfd = 25 ncmh = 26 ncmd = 27 kmol/min = 28 kmol/week = 29 kmol/month = 30 kmol/year = 31 kmol/oper-year = 32 VOLUME-FLOW cum/sec = 1 cuft/hr = 2 l/min = 3 gal/min = 4 gal/hr = 5 bbl/day = 6 cum/hr = 7 cuft/min = 8 bbl/hr = 9 cuft/sec = 10 cum/day = 11 cum/year = 12 l/hr = 13 kbbl/day = 14 MMcuft/hr = 15 MMcuft/day = 16 Mcuft/day = 17 l/sec = 18 l/day = 19 cum/min = 20 kcum/sec = 21 kcum/hr = 22 kcum/day = 23 Mcum/sec = 24 Mcum/hr = 25 Mcum/day = 26 ACFM = 27 cuft/day = 28 Mcuft/min = 29 Mcuft/hr = 30 MMcuft/hr = 31 Mgal/min = 32 MMgal/min = 33 Mgal/hr = 34 MMgal/hr = 35 Mbbl/hr = 36 MMbbl/hr = 37 Mbbl/day = 38 MMbbl/day = 39 cum/oper-year = 40 ENTHALPY-FLO Watt = 1 Btu/hr = 2 cal/sec = 3 J/sec = 4 GJ/hr = 5 kcal/hr = 6 MMkcal/hr = 7 MMBtu/hr = 8 MMkcal/day = 9 MMBtu/day = 10 Pcu/hr = 11 MMPcu/hr = 12 kJ/sec = 13 kW = 14 MW = 15 GW = 16 MJ/hr = 17 Gcal/hr = 18 MBtu/hr = 19 Gcal/day = 20 Mcal/hr = 21 kJ/hr = 22 FORCE Newton = 1 lbf = 2 dyne = 3 MOLE-HEAT-CA J/kmol-K = 1 Btu/lbmol-R = 2 cal/mol-K = 3 kcal/mol-K = 4 tcal/mol-K = 5 Pcu/lbmol-K = 6 kJ/kmol-K = 7 Btu/lbmol-F = 8 HEAT-TRANS-C Watt/sqm-K = 1 Btu/hr-sqft-R = 2 cal/sec-sqcm-K = 3 kcal/sec-sqm-K = 4 kcal/hr-sqm-K = 5 Pcu/hr-sqft-K = 6 kW/sqm-K = 7 J/sec-sqm-K = 8 kJ/sec-sqm-K = 9 MMBtu/hr-sqft-R = 10 kJ/sec-sqm-C = 11 MJ/sec-sqm-K = 12 MJ/sec-sqm-C = 13 GJ/hr-sqm-K = 14 GJ/hr-sqm-C = 15 kcal/hr-sqm-C = 16 Btu/hr-sqft-F = 17 MMBtu/hr-sqft-F = 18 LENGTH meter = 1 ft = 2 meter = 3 cm = 4 in = 5 mu = 6 mm = 7 mile = 8 km = 9 angstrom = 10 Mft = 11 micron = 12 MASS kg = 1 lb = 2 kg = 3 gm = 4 ton = 5 Mlb = 6 tonne = 7 L-ton = 8 MMlb = 9 POWER Watt = 1 hp = 2 kW = 3 Btu/hr = 4 cal/sec = 5 ft-lbf/sec = 6 MW = 7 GW = 8 MJ/hr = 9 kcal/hr = 10 Gcal/hr = 11 MMBtu/hr = 12 MBtu/hr = 13 Mhp = 14 PRESSURE N/sqm = 1 psia = 2 atm = 3 lbf/sqft = 4 bar = 5 torr = 6 in-water = 7 kg/sqcm = 8 mmHg = 9 kPa = 10 mm-water = 11 mbar = 12 psig = 13 atmg = 14 barg = 15 kg/sqcmg = 16 lb/ft-sqsec = 17 kg/m-sqsec = 18 Pa = 19 MPa = 20 Pag = 21 kPag = 22 MPag = 23 mbarg = 24 in-Hg = 25 mmHg-vac = 26 in-Hg-vac = 27 in-water-60F = 28 in-water-vac = 29 in-water-60F-vac = 30 in-water-g = 31 in-water-60F-g = 32 mm-water-g = 33 mm-water-60F-g = 34 psi = 35 mm-water-60F = 36 bara = 37 SURFACE-TENS N/m = 1 dyne/cm = 2 dyne/cm = 3 lbf/ft = 4 mN/m = 5 TEMPERATURE K = 1 F = 2 K = 3 C = 4 R = 5 THERMAL-COND Watt/m-K = 1 Btu-ft/hr-sqft-R = 2 kcal-m/hr-sqm-K = 3 Btu-in/hr-sqft-R = 4 c-cm/sec-sqcm-K = 5 cal-cm/sec-sqcm-K = 6 Btu/hr-ft-R = 7 kcal/hr-m-K = 8 J/sec-m-K = 9 kW/m-K = 10 Btu-ft/hr-sqft-F = 11 Btu-in/hr-sqft-F = 12 Btu/hr-ft-F = 13 TIME sec = 1 hr = 2 hr = 3 day = 4 min = 5 year = 6 month = 7 week = 8 nsec = 9 oper-year = 10 VELOCITY m/sec = 1 ft/sec = 2 m/sec = 3 mile/hr = 4 km/hr = 5 ft/min = 6 mm/day = 7 mm/hr = 8 mm/day30 = 9 in/day = 10 VISCOSITY N-sec/sqm = 1 cP = 2 cP = 3 lb/ft-hr = 4 mN-sec/sqm = 5 p = 6 gm/sec-cm = 7 dyn-sec/sqcm = 8 Pa-sec = 9 VOLUME cum = 1 cuft = 2 l = 3 cuin = 4 gal = 5 bbl = 6 cc = 7 kcum = 8 Mcum = 9 Mcuft = 10 MMcuft = 11 ml = 12 kl = 13 MMl = 14 Mgal = 15 MMgal = 16 UKgal = 17 MUKgal = 18 MMUKgal = 19 Mbbl = 20 MMbbl = 21 kbbl = 22 cuyd = 23 FREQUENCY Hz = 1 rpm = 2 rpm = 3 rad/sec = 4 rps = 5 krpm = 6 MMrpm = 7 rph = 8 UNIT-PRICE $/kg = 1 $/lb = 2 $/kg = 3 $/ton = 4 $/Mlb = 5 $/gm = 6 $/L-ton = 7 $/tonne = 8 $/MMlb = 9 ENERGY-PRICE $/J = 1 $/Btu = 2 $/cal = 3 $/kcal = 4 $/kWhr = 5 $/ft-lbf = 6 $/Gcal = 7 $/MMBtu = 8 $/hp-hr = 9 $/MBtu = 10 $/kJ = 11 $/MJ = 12 $/GJ = 13 $/N-m = 14 $/Mcal = 15 DELTA-T K = 1 F = 2 K = 3 C = 4 R = 5 DELTA-K = 6 DELTA-F = 7 DELTA-C = 8 DELTA-R = 9 ANGLE rad = 1 deg = 2 deg = 3 HEAD J/kg = 1 ft-lbf/lb = 2 m-kgf/kg = 3 sqm/sqsec = 4 inch = 5 ft = 6 meter = 7 kJ/kg = 8 km-kgf/kg = 9 Mft = 10 MJ/kg = 11 Mft-lbf/lb = 12 ft-head = 13 meter-head = 14 inch-head = 15 BOND-WORK-IN J/kg = 1 kWhr/ton = 2 kWhr/ton = 3 kJ/kg = 4 FILTER-RESIS 1/meter = 1 1/ft = 2 1/meter = 3 1/cm = 4 1/in = 5 SPEC-FLT-RES meter/kg = 1 ft/lb = 2 meter/kg = 3 cm/gm = 4 MOLE-DENSITY kmol/cum = 1 lbmol/cuft = 2 mol/cc = 3 lbmol/gal = 4 mol/l = 5 MASS-DENSITY kg/cum = 1 lb/cuft = 2 gm/cc = 3 lb/gal = 4 gm/cum = 5 gm/ml = 6 MOLE-ENTHALP J/kmol = 1 Btu/lbmol = 2 cal/mol = 3 kcal/mol = 4 tcal/mol = 5 MMkcal/mol = 6 MMBtu/lbmol = 7 Pcu/lbmol = 8 MMPcu/lbmol = 9 kJ/kmol = 10 GJ/kmol = 11 MJ/kmol = 12 kcal/kmol = 13 Gcal/kmol = 14 MBtu/lbmol = 15 Btu/scf = 16 Gcal/mol = 17 MASS-ENTHALP J/kg = 1 Btu/lb = 2 cal/gm = 3 kcal/kg = 4 MMkcal/kg = 5 MMBtu/lb = 6 Pcu/lb = 7 MMPcu/lb = 8 kJ/kg = 9 MJ/kg = 10 Gcal/kg = 11 MBtu/lb = 12 MOLE-ENTROPY J/kmol-K = 1 Btu/lbmol-R = 2 cal/mol-K = 3 kcal/mol-K = 4 kJ/kmol-K = 5 tcal/mol-K = 6 MJ/kmol-K = 7 kcal/kmol-K = 8 Gcal/kmol-K = 9 MBtu/lbmol-R = 10 MASS-ENTROPY J/kg-K = 1 Btu/lb-R = 2 cal/gm-K = 3 kcal/kg-K = 4 kJ/kg-K = 5 MJ/kg-K = 6 Gcal/kg-K = 7 MBtu/lb-R = 8 MOLE-VOLUME cum/kmol = 1 cuft/lbmol = 2 cc/mol = 3 ml/mol = 4 bbl/mscf = 5 DIMENSIONLES Unitless = 1 Unitless = 2 Unitless = 3 Untless = 4 Unitles = 5 DIPOLEMOMENT (J*cum)**.5 = 1 (Btu*cuft)**.5 = 2 debye = 3 (kJ*cum)**.5 = 4 SOLUPARAM (J/cum)**.5 = 1 (Btu/cuft)**.5 = 2 (cal/cc)**.5 = 3 (kcal/cum)**.5 = 4 (kJ/cum)**.5 = 5 (cal/ml)**0.5 = 6 ELEC-POWER Watt = 1 kW = 2 kW = 3 ELEC-PRICE $/J = 1 $/kWhr = 2 $/kWhr = 3 MASS-HEAT-CA J/kg-K = 1 Btu/lb-R = 2 cal/gm-K = 3 kcal/gm-K = 4 Pcu/lb-K = 5 kJ/kg-K = 6 Btu/lb-F = 7 UA J/sec-K = 1 Btu/hr-R = 2 cal/sec-K = 3 kJ/sec-K = 4 kcal/sec-K = 5 kcal/hr-K = 6 Btu/hr-F = 7 MOLES kmol = 1 lbmol = 2 kmol = 3 scm = 4 MMscf = 5 Mscf = 6 MMscm = 7 mol = 8 scf = 9 WORK J = 1 hp-hr = 2 kW-hr = 3 ft-lbf = 4 kJ = 5 N-m = 6 MJ = 7 MBtu = 8 MMBtu = 9 Mcal = 10 Gcal = 11 HEAT J = 1 Btu = 2 cal = 3 kcal = 4 MMkcal = 5 MMBtu = 6 Pcu = 7 MMPcu = 8 kJ = 9 GJ = 10 N-m = 11 MJ = 12 Mcal = 13 Gcal = 14 MBtu = 15 kW-hr = 16 AREA-PRICE $/sqm = 1 $/sqft = 2 $/sqm = 3 $/sqcm = 4 $/sqin = 5 $/sqmile = 6 $/sqmm = 7 VOLUME-PRICE $/cum = 1 $/cuft = 2 $/l = 3 $/cc = 4 $/bbl = 5 $/cuyd = 6 $/kl = 7 $/cuin = 8 $/ml = 9 $/MMl = 10 $/gal = 11 $/Mgal = 12 $/MMgal = 13 $/UKgal = 14 $/MUKgal = 15 $/MMUKgal = 16 $/kbbl = 17 $/Mcuft = 18 $/MMcuft = 19 $/kcum = 20 $/Mcum = 21 $/Mbbl = 22 $/MMbbl = 23 ITEM-PRICE $/item = 1 $/item = 2 $/item = 3 NUM-CONC no/cum = 1 no/cuft = 2 no/l = 3 no/cc = 4 1e6/cc = 5 MASS-CONC kg/cum = 1 lb/cuft = 2 gm/l = 3 gm/cc = 4 mg/l = 5 mg/cc = 6 mg/cum = 7 INVERSE-TIME 1/sec = 1 1/hr = 2 1/hr = 3 1/min = 4 1/day = 5 1/year = 6 1/oper-year = 7 LN-INV-TIME ln(1/sec) = 1 ln(1/hr) = 2 ln(1/hr) = 3 ln(1/min) = 4 FLUX cum/sqm-sec = 1 cuft/sqft-sec = 2 l/sqm-sec = 3 l/sqm-hr = 4 gal/sqft-min = 5 AREA-USAGE sqm/sec = 1 sqft/hr = 2 sqm/hr = 3 sqm/day = 4 sqm/year = 5 sqm/oper-year = 6 VOLUME-USAGE cum/sec = 1 cuft/hr = 2 l/hr = 3 l/day = 4 l/year = 5 cum/hr = 6 cum/day = 7 cum/year = 8 l/oper-year = 9 cum/oper-year = 10 MOLE-CONC kmol/cum = 1 lbmol/cuft = 2 mol/cc = 3 mol/l = 4 mmol/cc = 5 mmol/l = 6 POWER-VOLUME Watt/cum = 1 hp/cuft = 2 kW/l = 3 kW/cum = 4 MASS-TRANS-C kg/s-sqm-kg/cum = 1 lb/hr-sqf-lb/cuf = 2 gm/s-sqcm-gm/cc = 3 SPECIFICAREA sqm/cum = 1 sqft/cuft = 2 sqcm/cc = 3 INVERSE-LENG 1/m = 1 1/ft = 2 1/cm = 3 1/in = 4 1/mm = 5 CHROM-VEL m/sec = 1 ft/sec = 2 cm/hr = 3 MASS-FLUX kg/sqm-s = 1 lb/sqft-hr = 2 kg/sqm-hr = 3 lb/sqft-s = 4 gm/sqcm-s = 5 kg/sqcm-s = 6 Mlb/sqft-hr = 7 tons/sqft-hr = 8 L-tons/sqft-hr = 9 tonne/sqft-hr = 10 SOLVENT-PERM kg/sqm-s-Pa = 1 lb/sqft-hr-atm = 2 kg/sqm-hr-atm = 3 gm/sqcm-s-atm = 4 gm/sqcm-s-Pa = 5 SOLUTE-PERM sqm/m-s = 1 sqft/ft-hr = 2 sqm/m-hr = 3 sqcm/cm-s = 4 sqft/ft-s = 5 WATER-RATE kg/J = 1 lb/hp-hr = 2 kg/kW-hr = 3 PDROP-PER-HT N/cum = 1 in-water/ft = 2 mm-water/m = 3 mbar/m = 4 mmHg/ft = 5 torr/m = 6 mmHg/m = 7 PDROP N/sqm = 1 psi = 2 atm = 3 lbf/sqft = 4 bar = 5 torr = 6 in-water = 7 kg/sqcm = 8 mmHg = 9 kPa = 10 mm-water = 11 mbar = 12 in-water-60F = 13 in-Hg = 14 lb/ft-sqsec = 15 kg/m-sqsec = 16 Pa = 17 MPa = 18 psia = 19 mm-water-60F = 20 PACK-FACTOR 1/m = 1 1/ft = 2 1/m = 3 1/cm = 4 1/in = 5 1/mm = 6 NUM-CON-RATE no/cum-sec = 1 no/cuft-sec = 2 no/l-sec = 3 no/cc-sec = 4 no/cum-sec = 5 no/cum-min = 6 no/cuft-min = 7 no/l-min = 8 no/cc-min = 9 no/cum-hr = 10 no/cuft-hr = 11 no/l-hr = 12 no/cc-hr = 13 INVERSE-AREA 1/sqm = 1 1/sqft = 2 1/sqm = 3 VOL-HEAT-CAP J/cum-K = 1 Btu/cuft-R = 2 cal/cc-K = 3 kcal/cum-K = 4 kJ/cum-K = 5 Btu/cuft-F = 6 HEAT-FLUX Watt/m = 1 Btu/hr-ft = 2 cal/sec-m = 3 J/sec-m = 4 MMBtu/hr-ft = 5 Gcal/hr-m = 6 GJ/hr-m = 7 kcal/hr-m = 8 kJ/hr-m = 9 INVERSE-TEMP 1/K = 1 1/R = 2 1/K = 3 INVERSE-PRES sqm/N = 1 1/psi = 2 1/atm = 3 sqft/lbf = 4 1/bar = 5 1/torr = 6 1/in-water = 7 sqcm/kg = 8 1/mmHg = 9 1/kPa = 10 1/mm-water = 11 TEMP-VOLUME cum-K/kmol = 1 cuft-R/lbmol = 2 cc-K/mol = 3 VFLOW-LENGTH sqm/sec = 1 gpm/ft = 2 sqcm/sec = 3 sqm/hr = 4 sqft/min = 5 CONTENTS fraction = 1 percent = 2 fraction = 3 ppm = 4 POP-DENSITY no/m/cum = 1 no/ft/cuft = 2 no/m/l = 3 no/mm/l = 4 no/mu/cc = 5 no/in/cuin = 6 INVERSE-HT-C sqm-K/Watt = 1 hr-sqft-R/Btu = 2 sec-sqcm-K/cal = 3 sec-sqm-K/kcal = 4 hr-sqm-K/kcal = 5 hr-sqft-K/Pcu = 6 sqm-K/kW = 7 sec-sqm-K/J = 8 sec-sqm-K/kJ = 9 VOL-ENTHALPY J/cum = 1 Btu/cuft = 2 cal/cc = 3 kcal/cum = 4 kJ/cum = 5 MMBtu/bbl = 6 MJ/cum = 7 MOL-FLOW-LEN kmol/sec-m = 1 lbmol/hr-ft = 2 kmol/hr-m = 3 mol/sec-m = 4 lbmol/sec-ft = 5 lbmol/day-ft = 6 kmol/day-m = 7 mol/min-m = 8 USR-DUMMY0 base-units = 1 USR-DUMMY1 base-units = 1 USR-DUMMY2 base-units = 1 USR-DUMMY3 base-units = 1 USR-DUMMY4 base-units = 1 USR-DUMMY5 base-units = 1 USR-DUMMY6 base-units = 1 USR-DUMMY7 base-units = 1 USR-DUMMY8 base-units = 1 USR-DUMMY9 base-units = 1 VFLOW-RPM cum/sec/rpm = 1 cuft/hr/rpm = 2 l/min/rpm = 3 gal/min/rpm = 4 gal/hr/rpm = 5 bbl/day/rpm = 6 cum/hr/rpm = 7 cuft/min/rpm = 8 bbl/hr/rpm = 9 cuft/sec/rpm = 10 cum/day/rpm = 11 cum/year/rpm = 12 l/hr/rpm = 13 kbbl/day/rpm = 14 MMcuft/hr/rpm = 15 MMcuft/day/rpm = 16 Mcuft/day/rpm = 17 l/sec/rpm = 18 l/day/rpm = 19 cum/min/rpm = 20 F-FACTOR (kg-cum)**.5/sec = 1 (lb-cuft)**.5/hr = 2 (gm-l)**.5/min = 3 (lb-gal)**.5/min = 4 MASS-CYCL kg/cycle = 1 lb/cycle = 2 kg/cycle = 3 lb/cycle = 4 Mlb/cycle = 5 tons/cycle = 6 gm/cycle = 7 tonne/cycle = 8 lb/cycle = 9 kg/cycle = 10 tons/cycle = 11 tons/cycle = 12 MOLE-CYCL kmol/cycle = 1 lbmol/cycle = 2 kmol/cycle = 3 MMscfh/cycle = 4 MMscmh/cycle = 5 mol/cycle = 6 lbmol/cycle = 7 scmh/cycle = 8 lbmol/cycle = 9 kmol/cycle = 10 MMscfd/cycle = 11 scfm/cycle = 12 VOLUME-CYCL cum/cycle = 1 cuft/cycle = 2 l/cycle = 3 gal/cycle = 4 gal/cycle = 5 bbl/cycle = 6 cum/cycle = 7 cuft/cycle = 8 bbl/cycle = 9 cuft/cycle = 10 cum/cycle = 11 cum/cycle = 12 l/cycle = 13 kbbl/cycle = 14 MMcuft/cycle = 15 ENTHALPY-CYC Watt/cycle = 1 Btu/cycle = 2 cal/cycle = 3 J/cycle = 4 GJ/cycle = 5 kcal/cycle = 6 MMkcal/cycle = 7 MMBtu/cycle = 8 MMkcal/cycle = 9 MMBtu/cycle = 10 Pcu/cycle = 11 MMPcu/cycle = 12 kJ/cycle = 13 kW/cycle = 14 Gcal/cycle = 15 MASS-OPER kg/op-sec = 1 lb/op-hr = 2 kg/op-hr = 3 lb/op-sec = 4 Mlb/op-hr = 5 tons/op-day = 6 gm/op-sec = 7 tonne/op-hr = 8 lb/op-day = 9 kg/op-day = 10 tons/op-year = 11 tons/op-hr = 12 MOLE-OPER kmol/op-sec = 1 lbmol/op-hr = 2 kmol/op-hr = 3 MMscf/cycle-hr = 4 MMscm/cycle-hr = 5 mol/op-sec = 6 lbmol/op-sec = 7 scm/cycle-hr = 8 lbmol/op-day = 9 kmol/op-day = 10 MMscf/cycle-day = 11 scf/cycle-min = 12 VOLUME-OPER cum/op-sec = 1 cuft/op-hr = 2 l/op-min = 3 gal/op-min = 4 gal/op-hr = 5 bbl/op-day = 6 cum/op-hr = 7 cuft/op-min = 8 bbl/op-hr = 9 cuft/op-sec = 10 cum/op-day = 11 cum/op-year = 12 l/op-hr = 13 kbbl/op-day = 14 MMcuft/op-hr = 15 ENTHALPY-OPR Watt/cycle = 1 Btu/op-hr = 2 cal/op-sec = 3 J/op-sec = 4 GJ/op-hr = 5 kcal/op-hr = 6 MMkcal/op-hr = 7 MMBtu/op-hr = 8 MMkcal/op-day = 9 MMBtu/op-day = 10 Pcu/op-hr = 11 MMPcu/op-hr = 12 kJ/op-sec = 13 kW/cycle = 14 Gcal/op-hr = 15 Gcal/op-day = 16 RHO-VSQRD kg/m-sqsec = 1 lb/ft-sqsec = 2 kg/m-sqsec = 3 SOUND-LEVEL decibels = 1 decibels = 2 decibels = 3 MOM-INERTIA kg-sqm = 1 lb-sqft = 2 kg-sqm = 3 gm-sqcm = 4 lb-sqin = 5 VOLTAGE volt = 1 kvolt = 2 volt = 3 CURRENT amp = 1 mamp = 2 amp = 3 MASS-VOLUME cum/kg = 1 cuft/lb = 2 cc/g = 3 BPD/MLBPH = 4 cc/kg = 5 MASS-PER-LEN kg/m = 1 lb/ft = 2 kg/m = 3 ENERGY-VOL cum/J = 1 bbl/Btu = 2 bbl/MMBtu = 3 SIEMENS-M Siemens/m = 1 Siemens/ft = 2 Siemens/m = 3 Siemens/cm = 4 COST-RATE $/sec = 1 $/hr = 2 $/hr = 3 $/min = 4 $/day = 5 $/year = 6 k$/hr = 7 k$/day = 8 k$/year = 9 MM$/day = 10 MM$/year = 11 $/week = 12 $/nsec = 13 $/oper-year = 14 k$/oper-year = 15 MM$/oper-year = 16 FLUX-HEAT-AR Watt/sqm = 1 Btu/hr-sqft = 2 cal/sec-sqm = 3 J/sec-sqm = 4 MMBtu/hr-sqft = 5 kW/sqm = 6 FLUX-MOLE kmol/sqm-s = 1 lbmol/sqft-hr = 2 kmol/sqm-hr = 3 lbmol/sqft-s = 4 mol/sqcm-s = 5 HEAT-RATE-V Watt/cum = 1 Btu/hr-cuft = 2 cal/sec-cum = 3 J/sec-cum = 4 MMBtu/hr-cuft = 5 GJ/hr-cum = 6 MOLE-RXN-RAT kmol/cum-s = 1 lbmol/cuft-hr = 2 kmol/cum-hr = 3 mol/cc-s = 4 MOL-RXN-RATW kmol/kg-s = 1 lbmol/lb-hr = 2 kmol/kg-hr = 3 mol/gm-s = 4 MOLE-PRICE $/kmol = 1 $/lbmol = 2 $/mol = 3 VOL-HTR-COEF Watt/cum-K = 1 Btu/hr-cuft-R = 2 cal/sec-cc-K = 3 Watt/cum-C = 4 Watt/cum-F = 5 kW/cum-K = 6 kW/cum-C = 7 Btu/hr-cuft-F = 8 POWER-AREA Watt/sqm = 1 hp/sqft = 2 kW/sqm = 3 W/sqcm = 4 kW/sqcm = 5 POWER-MASS Watt/kg = 1 hp/lb = 2 kW/kg = 3 W/g = 4 kW/g = 5 MASS-EMISSIO kg/J = 1 lb/Btu = 2 kg/cal = 3 tonne/GJ = 4 tonne/MMBtu = 5 kg/kcal = 6 kg/GJ = 7 kg/kJ = 8 kg/MJ = 9 kg/MMkcal = 10 tonne/MMkcal = 11 kg/MMBtu = 12 g/MJ = 13 lb/MMBtu = 14 tonne/TJ = 15 INVERSE-VEL sec/m = 1 sec/ft = 2 sec/cm = 3 sec/in = 4 sec/mm = 5 SPEC-MAT-RES kg/J-m = 1 lb/Btu-ft = 2 gm/cal-cm = 3 ACCELERATION m/sqsec = 1 ft/sqsec = 2 m/sqsec = 3 MASS-CONTENT kg/kg_dry = 1 lb/lb_dry = 2 kg/kg_dry = 3 AREA-SQTIME sqm/sqsec = 1 sqft/sqsec = 2 sqm/sqsec = 3 sqmm/sqsec = 4 sqin/sqsec = 5 Settings paramdata #0 = APV80 ENRTL-RK #1 = APV80 VLE-IG #2 = APV80 VLE-RK #3 = APV80 VLE-HOC #4 = APV80 LLE-LIT #5 = APV80 LLE-ASPEN #6 = APV80 VLE-LIT #7 = APV80 BINARY #8 = APV80 EOS-LIT #9 = APV80 HENRY-AP #10 = APV80 SRK-ASPEN #11 = APV80 PC-SAFT #12 = APV80 POLYPCSF #13 = APV80 HYSYS purebank #0 = APV80 PURE25 #1 = APV80 AQUEOUS #2 = APV80 SOLIDS #3 = APV80 INORGANIC regdbank = 1 ftn_check = 1 autoblockid = 1 autostreamid = 1 showblockid = 1 showstreamid = 1 autoplacement = 1 grid = 2 placement = 2.5 gridresolution = 0.1 scale = 0 streamprefix = blockprefix = B labelscale = 1.0 plotmarkersize = 4 plottitlefont = 9 pt. Segoe UI Bold plotlegendfont = 8 pt. Segoe UI plotlabelfont = 8 pt. Segoe UI plotscalefont = 8 pt. Segoe UI plottextfont = 8 pt. Segoe UI tablefont = 8 pt. Courier 3DOn = 0 qwformat = %.0f tempformat = %.0f presformat = %.0f flowformat = %.0f strmqwformat = %.0f vflowformat = %.0f mflowformat = %.0f vfracformat = %.2f pseudobatch = 0 partial = 1 animation = 1 runanyway = 0 template = General with English Units econtemplate = US_IP runtype = FLOWSHEET editor = notepad component = 1 account-info = 0 psfont = Helvetica alwayssavebkp = 1 defsaveasbkp = 2 timestamp = &[VERSION] Run:&[RUNID] &[DATE] &[TIME] plottimestamp = 0 zoomfactor = 2.0 scrollstep = 2 copyvalue = 1 copylabel = 0 copyunits = 0 copybasis = 0 globalqw = 0 globaltemp = 0 globalpres = 0 globalflow = 0 globalstrmqw = 0 globalvflow = 0 globalmflow = 0 globalvfrac = 0 globalshowcalcerror = 1 globalshowcalcwarning = 1 globalshowdisabled = 1 lockblock = 0 startupdir = C:\ProgramData\AspenTech\Aspen Plus V8.0\ printcommand = print cpontop = 0 servertype = Local PC servername = None username = None workingdir = None tffdir = editinput = 0 showlegend = 1 gridstyle = 3 linestyle = 2 polyplus = 1 dynaplus = 0 bfrac = 1 rtf = 1 rsp = 1 plotheight = 5000 plotwidth = 5000 plotleft = 0 plottop = 0 frameheight = 725 framewidth = 800 frametop = 0 frameleft = 0 framemaximized = 0 listviewdefault = 3 wallpaperview = 1 worksheetmode = 0 statusbarview = 1 modellibraryview = 1 toolstdvisible = 1 tooldatavisible = 1 toolpfsvisible = 1 tooldrawvisible = 0 toolrunvisible = 1 tooldynvisible = 1 toolsectionsvisible = 0 toolstddock = 1 tooldatadock = 1 toolpfsdock = 1 tooldrawdock = 1 toolrundock = 1 tooldyndock = 1 toolsectionsdock = None pfsheight = 0 pfswidth = 0 pfstop = 0 pfsleft = 0 browserheight = 7575 browserwidth = 12345 browserleft = 0 browsertop = 0 browsertreewidth = 3645 browsertreeview = 1 browserstatusbar = 1 browserdescription = 1 mdichildstate = 0 papersize = 1 papersource = 1 paperwidth = 11000 paperheight = 8500 orientation = 1 marginleft = None margintop = None marginright = None marginbottom = None polyplusenabled = 1 dynaplusenabled = 1 bfracenabled = 1 rtfenabled = 1 rspenabled = 1 pdbenabled = 0 drawcolor = 0 drawlinestyle = 0 drawfont = 10 pt. Times New Roman solids = 1 petroleum = 1 rtopt = 1 initializeicarus = 0 eodghidden = 15524 eoexplorerhidden = 15524 eovariablefilter = *;*.STR.*, *.BLK.*, *.SPC.*, *.PROP.* eovarindex = 0 eoblocksorting = 0 eovarnamesonly = 0 rtexecprogid = None lockprops = None pinchenabled = 0 saveasapw = 0 ignoreexportwarnmsg = 0 ignoreexporterrmsg = 0 timestampastext = 0 linethickness = 1 dcomconnect = 1 templatedir = simulations linklimit = 5000 material_color = 0 material_style = 0 material_width = 1 material_termid = heat_color = 0 heat_style = 2 heat_width = 1 heat_termid = Q work_color = 0 work_style = 1 work_width = 1 work_termid = W connections_color = 9 connections_style = 3 connections_width = 1 connections_termid = measurements_color = 4 measurements_style = 3 measurements_width = 1 measurements_termid = displayeoconn = 0 displaycalcs = 0 displaytransfers = 0 displaymeas = 0 displaydesignspecs = 0 displaycalccons = 0 displaymeascons = 0 displayothercons = 0 displayeomeas = 1 displayeomeastype = 2 displayothermanipconn = 0 UseExcelCOMAddin = 1 wpfformsenabled = 0 showeoviews = 0 eoautosave = 1 ercrashreport = 1 dontshow_upwardcompDB = 0 new_pure_com = 1 new_prop_opt = 0 new_bin_par = 0 new_ada = 1 new_mwcalc = 1 checkseq = 1 pro2blockdata = 0 fileopendir = 0 dontask_buildchk = 0 lockflowsheet = None allow_system_userprops = 0 dontask_chgdir = 0 proppkgsel = PropertyMethodAssistant placesbartype = None place0 = None place1 = None place2 = None place3 = None place4 = None enablethemes = 1 commentlinewrap = 80 copy_estimation = 1 copy_retrieved = 1 savebkpformat = 0 userdefinedexports = 0 purge_incomp_params = 0 set_default_biparams = 0 set_default_dataset1 = 0 set_default_dataset0 = 1 bestinput = 0 autosmrun = 0 labelfont = 8 pt. Arial genallpropset = 0 strmresformdefault = 0 roottype = 0 exchangerfile = 1 streamformat = 1 runsettingfile = 1 usermodelfile = 1 fortranfile = 0 allow_system_autoparam = 1 timeout = 1000 auto_evaluate = 0 distdontshow = 0 econdontshow = 0 myrssnewsalias = My News mynewsurl = http://www.aspentech.com/rss/aspenplus.xml RSSRefeshRate = 60 UserSpecRSSRefRate = 0 showstartpageonstartup = 1 showcalculatorblocks = 1 showdesignspecblocks = 1 showtransferblocks = 1 showmeasurementblocks = 1 showcalculatorconns = 1 showstartpageonstartup = 1 ignoreapwnshellsettings = 0 activeuserpropglobdata = None customglobaldatapropset1 = 0 | Custom1 | * | %.2f | 0 | 6 customglobaldatapropset2 = 0 | Custom2 | * | %.2f | 1 | 7 customglobaldatapropset3 = 0 | Custom3 | * | %.2f | 2 | 8 customglobaldatapropset4 = 0 | Custom4 | * | %.2f | 4 | 9 customglobaldatapropset5 = 0 | Custom5 | * | %.2f | 5 | 10 customglobaldatapropset6 = 0 | Custom6 | * | %.2f | 6 | 11 economics_active = 0

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