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
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purebank
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