Using an external solver with Aspen

| categories: programming | tags: aspen | View Comments

One reason to interact with Aspen via python is to use external solvers to drive the simulations. Aspen has some built-in solvers, but it does not have everything. You may also want to integrate additional calculations, e.g. capital costs, water usage, etc… and integrate those results into a report.

Here is a simple example where we use fsolve to find the temperature of the flash tank that will give a vapor phase mole fraction of ethanol of 0.8. It is a simple example, but it illustrates the possibility.

import os
import win32com.client as win32
aspen = win32.Dispatch('Apwn.Document')

aspen.InitFromArchive2(os.path.abspath('data\Flash_Example.bkp'))

from scipy.optimize import fsolve

def func(flashT):
    flashT = float(flashT) # COM objects do not understand numpy types
    aspen.Tree.FindNode('\Data\Blocks\FLASH\Input\TEMP').Value = flashT
    aspen.Engine.Run2()
    y = aspen.Tree.FindNode('\Data\Streams\VAPOR\Output\MOLEFRAC\MIXED\ETHANOL').Value
    return y - 0.8

sol, = fsolve(func, 150.0)
print 'A flash temperature of {0:1.2f} degF will have y_ethanol = 0.8'.format(sol)
A flash temperature of 157.38 degF will have y_ethanol = 0.8

One unexpected detail was that the Aspen COM objects cannot be assigned numpy number types, so it was necessary to recast the argument as a float. Otherwise, this worked about as expected for an fsolve problem.

Copyright (C) 2013 by John Kitchin. See the License for information about copying.

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Aspen COM object introspection

| categories: programming | tags: aspen | View Comments

COM programming is a bit more difficult than normal python programming. The main reason is the functions on the objects are not easy to inspect, and they are not always well documented. Let us look at this for the Aspen COM interface.

import win32com.client as win32

aspen = win32.Dispatch('Apwn.Document')
print aspen
print dir(aspen)
Aspen Plus 27.0 OLE Services
['_ApplyTypes_', '_FlagAsMethod', '_LazyAddAttr_', '_NewEnum', '_Release_', '__AttrToID__', '__LazyMap__', '__call__', '__doc__', '__eq__', '__getattr__', '__getitem__', '__init__', '__int__', '__len__', '__module__', '__ne__', '__nonzero__', '__repr__', '__setattr__', '__setitem__', '__str__', '_builtMethods_', '_enum_', '_find_dispatch_type_', '_get_good_object_', '_get_good_single_object_', '_lazydata_', '_make_method_', '_mapCachedItems_', '_oleobj_', '_olerepr_', '_print_details_', '_proc_', '_unicode_to_string_', '_username_', '_wrap_dispatch_']

These are not that helpful. The COM object is so-called "late-bound" which means there is no information available about the methods. To get an "early-bound" object we have to do some work. We have to run the makepy.py utility which will generate a python interface with the methods. I found the makepy.py function like this:

import os
import win32com.client as win32
print os.path.split(win32.__file__)[0]
print os.path.exists(os.path.join(os.path.split(win32.__file__)[0], 'makepy.py'))
C:\Users\jkitchin\AppData\Local\Enthought\Canopy\System\lib\site-packages\win32com\client
True

So, change to the directory above, and run makepy.py. This will pop a window with a lot of libraries to select from. Select "Aspen Plus GUI 27.0 Type Library (10.0)" and click ok. You will see some output like this.

PS C:\Users\jkitchin\AppData\Local\Enthought\Canopy\System\lib\site-packages\win32com\client> python makepy.py
Generating to C:\Users\jkitchin\AppData\Local\Temp\gen_py\2.7\8E567520-F9BA-11CF-90B2-0000C0A810C4x409x16x0.py
Building definitions from type library...
Generating...
Importing module

That command created a new python module that contains the methods available. Luckily, you do not have to do anything special to use it. The new module will automatically be loaded. Let us see an example.

import win32com.client as win32

aspen = win32.Dispatch('Apwn.Document')
print aspen
print dir(aspen)
print
print dir(aspen.Engine)
print
import inspect
print inspect.getargspec(aspen.InitFromArchive2)
Aspen Plus 27.0 OLE Services
['Activate', 'AdviseParent', 'CLSID', 'Choose', 'Close', 'CreateRouteTree', 'DeleteSelection', 'EditCompoundDocument', 'Export', 'Generate', 'GetNew', 'GetNew3', 'Import', 'InitFromArchive', 'InitFromArchive2', 'InitFromArchive3', 'InitFromFile', 'InitFromFile2', 'InitFromTemplate', 'InitFromTemplate2', 'InitFromXML', 'InitNew', 'InitNew2', 'LoadLink', 'NewSelection', 'Readback', 'Reconcile', 'Reinit', 'Restore', 'Restore2', 'RootModel', 'Run', 'Run2', 'RunScript', 'Save', 'Save2', 'SaveAs', 'SaveAs2', 'SaveLink', 'SaveSelection', 'Selection', 'SetCompat', 'SetParent', 'UIDisable', 'WriteArchive', 'WriteArchive2', '_ApplyTypes_', '__call__', '__doc__', '__eq__', '__getattr__', '__init__', '__int__', '__module__', '__ne__', '__repr__', '__setattr__', '__str__', '__unicode__', '_get_good_object_', '_get_good_single_object_', '_oleobj_', '_prop_map_get_', '_prop_map_put_', 'coclass_clsid']

['AddStopPoint', 'CLSID', 'ClearStopPoints', 'ConnectionDialog', 'DeleteStopPoint', 'EngineFilesSettings', 'ExportReport', 'GetStopPoint', 'Host', 'HostDescription', 'MoveTo', 'OptionSettings', 'ProcessInput', 'Reinit', 'ReinitializeEO', 'Run', 'Run2', 'RunSettings', 'SetEngineFilesSettings', 'SetOptionSettings', 'Step', 'Stop', 'StopPoints', 'SynchronizeEO', '_ApplyTypes_', '__doc__', '__eq__', '__getattr__', '__init__', '__module__', '__ne__', '__repr__', '__setattr__', '_get_good_object_', '_get_good_single_object_', '_oleobj_', '_prop_map_get_', '_prop_map_put_', 'coclass_clsid']

ArgSpec(args=['self', 'filename', 'host_type', 'node', 'username', 'password', 'working_directory', 'failmode'], varargs=None, keywords=None, defaults=(<PyOleEmpty object at 0x0000000001D36BB0>, <PyOleEmpty object at 0x0000000001D36BB0>, <PyOleEmpty object at 0x0000000001D36BB0>, <PyOleEmpty object at 0x0000000001D36BB0>, <PyOleEmpty object at 0x0000000001D36BB0>, <PyOleEmpty object at 0x0000000001D36BB0>, <PyOleEmpty object at 0x0000000001D36BB0>))

This is much more useful! We can see all the methods of a COM object! See this reference for more details: http://oreilly.com/catalog/pythonwin32/chapter/ch12.html#49339.

Copyright (C) 2013 by John Kitchin. See the License for information about copying.

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Aspen data introspection

| categories: programming | tags: aspen | View Comments

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

import os
import win32com.client as win32
aspen = win32.Dispatch('Apwn.Document')
aspen.InitFromArchive2(os.path.abspath('data\Flash_Example.bkp'))

def print_elements(obj, level=0):
    if hasattr(obj, 'Elements'):
        print ' '*level + obj.Name
        for o in obj.Elements:
            print_elements(o, level + 1)
    else:
        print ' '*level, obj.Name, ' = ', obj.Value

print_elements(aspen.Tree)

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

Copyright (C) 2013 by John Kitchin. See the License for information about copying.

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Running Aspen via Python

| categories: programming | tags: aspen | View Comments

Aspen is a process modeling tool that simulates industrial processes. It has a GUI for setting up the flowsheet, defining all the stream inputs and outputs, and for running the simulation. For single calculations it is pretty convenient. For many calculations, all the pointing and clicking to change properties can be tedious, and difficult to reproduce. Here we show how to use Python to automate Aspen using the COM interface.

We have an Aspen flowsheet setup for a flash operation. The feed consists of 91.095 mol% water and 8.905 mol% ethanol at 100 degF and 50 psia. 48.7488 lbmol/hr of the mixture is fed to the flash tank which is at 150 degF and 20 psia. We want to know the composition of the VAPOR and LIQUID streams. The simulation has been run once.

This is an example that just illustrates it is possible to access data from a simulation that has been run. You have to know quite a bit about the Aspen flowsheet before writing this code. Particularly, you need to open the Variable Explorer to find the "path" to the variables that you want, and to know what the units are of those variables are.

import os
import win32com.client as win32
aspen = win32.Dispatch('Apwn.Document')

aspen.InitFromArchive2(os.path.abspath('data\Flash_Example.bkp'))

## Input variables
feed_temp = aspen.Tree.FindNode('\Data\Streams\FEED\Input\TEMP\MIXED').Value
print 'Feed temperature was {0} degF'.format(feed_temp)

ftemp = aspen.Tree.FindNode('\Data\Blocks\FLASH\Input\TEMP').Value
print 'Flash temperature = {0}'.format(ftemp)

## Output variables
eL_out = aspen.Tree.FindNode("\Data\Streams\LIQUID\Output\MOLEFLOW\MIXED\ETHANOL").Value
wL_out = aspen.Tree.FindNode("\Data\Streams\LIQUID\Output\MOLEFLOW\MIXED\WATER").Value

eV_out = aspen.Tree.FindNode("\Data\Streams\VAPOR\Output\MOLEFLOW\MIXED\ETHANOL").Value
wV_out = aspen.Tree.FindNode("\Data\Streams\VAPOR\Output\MOLEFLOW\MIXED\WATER").Value

tot = aspen.Tree.FindNode("\Data\Streams\FEED\Input\TOTFLOW\MIXED").Value

print 'Ethanol vapor mol flow: {0} lbmol/hr'.format(eV_out)
print 'Ethanol liquid mol flow: {0} lbmol/hr'.format(eL_out)

print 'Water vapor mol flow: {0} lbmol/hr'.format(wV_out)
print 'Water liquid mol flow: {0} lbmol/hr'.format(wL_out)

print 'Total = {0}. Total in = {1}'.format(eV_out + eL_out + wV_out + wL_out,
                                           tot)

aspen.Close()
Feed temperature was 100.0 degF
Flash temperature = 150.0
Ethanol vapor mol flow: 3.89668323 lbmol/hr
Ethanol liquid mol flow: 0.444397241 lbmol/hr
Water vapor mol flow: 0.774592763 lbmol/hr
Water liquid mol flow: 43.6331268 lbmol/hr
Total = 48.748800034. Total in = 48.7488

It is nice that we can read data from a simulation, but it would be helpful if we could change variable values and to rerun the simulations. That is possible. We simply set the value of the variable, and tell Aspen to rerun. Here, we will change the temperature of the Flash tank and plot the composition of the outlet streams as a function of that temperature.

import os
import numpy as np
import matplotlib.pyplot as plt
import win32com.client as win32

aspen = win32.Dispatch('Apwn.Document')
aspen.InitFromArchive2(os.path.abspath('data\Flash_Example.bkp'))

T = np.linspace(150, 200, 10)

x_ethanol, y_ethanol = [], []

for temperature in T:
    aspen.Tree.FindNode('\Data\Blocks\FLASH\Input\TEMP').Value = temperature
    aspen.Engine.Run2()

    x_ethanol.append(aspen.Tree.FindNode('\Data\Streams\LIQUID\Output\MOLEFRAC\MIXED\ETHANOL').Value)
    y_ethanol.append(aspen.Tree.FindNode('\Data\Streams\VAPOR\Output\MOLEFRAC\MIXED\ETHANOL').Value)

plt.plot(T, y_ethanol, T, x_ethanol)
plt.legend(['vapor', 'liquid'])
plt.xlabel('Flash Temperature (degF)')
plt.ylabel('Ethanol mole fraction')
plt.savefig('images/aspen-water-ethanol-flash.png')
aspen.Close()

It takes about 30 seconds to run the previous example. Unfortunately, the way it is written, if you want to change anything, you have to run all of the calculations over again. How to avoid that is moderately tricky, and will be the subject of another example.

In summary, it seems possible to do a lot with Aspen automation via python. This can also be done with Matlab, Excel, and other programming languages where COM automation is possible. The COM interface is not especially well documented, and you have to do a lot of digging to figure out some things. It is not clear how committed Aspen is to maintaining or improving the COM interface (http://www.chejunkie.com/aspen-plus/aspen-plus-activex-automation-server/). Hopefully they can keep it alive for power users who do not want to program in Excel!

Copyright (C) 2013 by John Kitchin. See the License for information about copying.

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