MM "11.1" FLAVOR "NO" VERSION "11.1" DATETIME "Fri Nov 18 07:26:41 2016" 
MACHINE "WIN-NT/VC"  ; 
startlibrary
version1
NumLibs = 1
Built-In
NumCats = 9
Mixers/Splitters
active
Separators
active
Heat Exchangers
active
Columns
active
Reactors
active
Pressure Changers
active
Manipulators
active
Solids
active
User Models
active
endlibrary
; 
5
>VERSION 0
B1
Dupl
Built-In
DUPL
>VERSION 0
RSTOIC
RStoic
Built-In
RSTOIC
>VERSION 0
RGIBBS
RGibbs
Built-In
RGIBBS
>VERSION 0
RPLUG
RPlug
Built-In
RPLUG
>VERSION 0
RCSTR
RCSTR
Built-In
RCSTR
? SETUP MAIN ? \ TITLE TITLE = "REACTOR COMPARISON" \ \ SIMULATE INTERACTIVE
 = NO TFFFILE = "GEN_E" VISITED = 1 \ ? SETUP GLOBAL ? \ "IN-UNITS" INSET = 
ENG \ \ "STREAM-CLASS" SCLASS = CONVEN \ ? SETUP DIAGNOSTICS ? ? SETUP 
"SIM-OPTIONS" ? ; "ENG_MOLE" ; ? SETUP "UNITS-SET" METCBAR ? \ DESCRIPTION 
DESCRIPTION = "Metric Units with C, BAR, MMKCAL/HR, and CUM" \ \ MMLOCAL \ \ 
UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 7 7 3 3 5 3 3 3 5 3 4 3 3 3 3 1 
3 3 3 4 3 7 3 3 3 1 1 4 4 3 3 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3 3 3 3 3 3 4 3 3 
3 3 3 3 3 3 3 4 5 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 
3 3 3 3 3 3 3 3 3 3 3 3 3 ) \ ? SETUP "UNITS-SET" METCKGCM ? \ DESCRIPTION 
DESCRIPTION = "Metric Units with C, KG/SQCM, MMKCAL/HR, and CUM" \ \ MMLOCAL 
\ \ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 7 7 3 3 5 3 3 3 8 3 4 3 3 3 
3 1 3 3 3 4 3 7 3 3 3 3 3 4 4 3 3 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3 3 3 3 3 3 4 
3 3 3 3 3 3 3 3 3 4 8 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 
3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \ ? SETUP "UNITS-SET" "SI-CBAR" ? \ 
DESCRIPTION DESCRIPTION = "International System Units with C, BAR, and /HR" \ 
\ MMLOCAL \ \ UNITSET BASESET = SI ( 1 1 1 1 1 1 1 1 1 3 3 7 1 1 1 1 1 1 1 5 
1 4 1 1 1 1 1 1 1 1 4 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 
1 1 1 1 1 1 1 1 1 1 1 1 1 1 4 5 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 
1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 ) \ ? SETUP "ACCOUNT-INFO" ? \ 
ACCOUNT ACCOUNT = R PROJECT-ID = E PROJECT-NAME = "1" USER-NAME = "R" \ ? 
SETUP "RUN-CONTROL" ? ? SETUP DESCRIPTION ? \ DESCRIP DESCRIP = ( 
"General Simulation with English Units :" 
"F, psi, lb/hr, lbmol/hr, Btu/hr, cuft/hr." " " "Property Method: None" " " 
"Flow basis for input: Mole" " " "Stream report composition: Mole flow" ) \ ? 
DATABANKS ? \ DATABANKS FILE-SYM-NAM = ( PURE11 AQUEOUS SOLIDS INORGANIC ) \ 
? COMPONENTS MAIN ? \ COMPONENTS CID = ETHANOL ANAME = C2H6O-2 OUTNAME = 
ETHANOL TYPE = CONV DBNAME1 = "ETHANOL" ANAME1 = "C2H6O-2" /  CID = ACID 
ANAME = C2H4O2-1 OUTNAME = ACID TYPE = CONV DBNAME1 = "ACETIC-ACID" ANAME1 = 
"C2H4O2-1" /  CID = ACETATE ANAME = C4H8O2-3 OUTNAME = ACETATE TYPE = CONV 
DBNAME1 = "ETHYL-ACETATE" ANAME1 = "C4H8O2-3" /  CID = WATER ANAME = H2O 
OUTNAME = WATER TYPE = CONV DBNAME1 = "WATER" ANAME1 = "H2O" \ ? COMPONENTS 
"COMP-LIST" GLOBAL ? ? SOLVE ? ? FLOWSHEET GLOBAL ? \ BLOCK BLKID = B1 
BLKTYPE = DUPL IN = ( 1 M0-1 ) OUT = ( "F-STOIC" M0-1 "F-GIBBS" M0-1 "F-PLUG" 
M0-1 "F-CSTR" M0-1 ) \ \ BLOCK BLKID = RSTOIC BLKTYPE = RSTOIC IN = ( "F-STOIC" 
M0-1 ) OUT = ( "P-STOIC" M0-1 ) \ \ BLOCK BLKID = RGIBBS BLKTYPE = RGIBBS 
IN = ( "F-GIBBS" M0-1 ) OUT = ( "P-GIBBS" M0-1 ) \ \ BLOCK BLKID = RPLUG 
BLKTYPE = RPLUG IN = ( "F-PLUG" M0-1 ) OUT = ( "P-PLUG" M0-1 ) \ \ BLOCK 
BLKID = RCSTR BLKTYPE = RCSTR IN = ( "F-CSTR" M0-1 ) OUT = ( "P-CSTR" M0-1 ) 
\ \ "DEF-STREAM" SCLASS = CONVEN \ ? PROPERTIES MAIN ? \ GPROPERTIES 
GBASEOPSET = "NRTL-HOC" GOPSETNAME = "NRTL-HOC" PARCON = -2 \ ? PROPERTIES 
"OPTION-SETS" NRTL ? \ PARAM BASE = NRTL \ ? PROPERTIES "OPTION-SETS" 
"NRTL-HOC" ? \ PARAM BASE = "NRTL-HOC" \ ? PROPERTIES "MOLEC-STRUCT" ACETATE 
? ? PROPERTIES "MOLEC-STRUCT" ACID ? ? PROPERTIES "MOLEC-STRUCT" ETHANOL ? ? 
PROPERTIES "MOLEC-STRUCT" WATER ? ? PROPERTIES PARAMETERS BINARY SCALAR 
"HOCETA-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = HOCETA SETNO = 1 BDBANK
 = ( "EOS-LIT" ) \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ETHANOL CID2 = ETHANOL 
VALUE = EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ETHANOL CID2 = ACID 
VALUE = EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ETHANOL CID2 = ACETATE 
VALUE = EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ETHANOL CID2 = WATER 
VALUE = EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ACID CID2 = ETHANOL 
VALUE = EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ACID CID2 = ACID VALUE = 
EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ACID CID2 = ACETATE VALUE = 
EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ACID CID2 = WATER VALUE = 
EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ACETATE CID2 = ETHANOL VALUE = 
EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ACETATE CID2 = ACID VALUE = 
EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ACETATE CID2 = ACETATE VALUE = 
EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = ACETATE CID2 = WATER VALUE = 
EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = WATER CID2 = ETHANOL VALUE = 
EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = WATER CID2 = ACID VALUE = 
EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = WATER CID2 = ACETATE VALUE = 
EOS-LIT \ \ BPVAL PARAMNAME2 = HOCETA CID1 = WATER CID2 = WATER VALUE = 
EOS-LIT \ ? PROPERTIES PARAMETERS BINARY SCALAR "RKTKIJ-1" ? ; "ENG_MOLE" ; \ 
PROP-LIST PARAMNAME = RKTKIJ SETNO = 1 UNITROW = 0 \ ? PROPERTIES PARAMETERS 
BINARY "T-DEPENDENT" "ANDKIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = 
ANDKIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F NEL = 2 \ ? 
PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "ANDMIJ-1" ? ; "ENG_MOLE" ; \ 
PROP-LIST PARAMNAME = ANDMIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL
 = F NEL = 2 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "HENRY-1" ? ; 
"ENG_MOLE" ; \ PROP-LIST PARAMNAME = HENRY SETNO = 1 UNITROW = 20 UNITLABEL
 = psi TUNITROW = 22 TUNITLABEL = F BDBANK = ( BINARY HENRY ) NEL = 6 \ ? 
PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "NRTL-1" ? ; "ENG_MOLE" ; \ 
PROP-LIST PARAMNAME = NRTL SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F 
BDBANK = ( "VLE-IG" "LLE-ASPEN" "VLE-LIT" ) NEL = 12 \ \ BPVAL PARAMNAME2 = 
NRTL CID1 = ETHANOL CID2 = ACETATE UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = 
F VAL1 = VLE-IG VAL2 = VLE-IG VAL3 = VLE-IG VAL4 = VLE-IG VAL5 = VLE-IG VAL6 
= VLE-IG VAL7 = VLE-IG VAL8 = VLE-IG VAL9 = VLE-IG VAL10 = VLE-IG VAL11 = 
VLE-IG VAL12 = VLE-IG /  PARAMNAME2 = NRTL CID1 = ETHANOL CID2 = WATER 
UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = F VAL1 = VLE-IG VAL2 = VLE-IG VAL3 
= VLE-IG VAL4 = VLE-IG VAL5 = VLE-IG VAL6 = VLE-IG VAL7 = VLE-IG VAL8 = 
VLE-IG VAL9 = VLE-IG VAL10 = VLE-IG VAL11 = VLE-IG VAL12 = VLE-IG /  
PARAMNAME2 = NRTL CID1 = ACETATE CID2 = WATER UNITROW2 = 0 TUNITROW2 = 22 
TUNITLABEL2 = F VAL1 = LLE-ASPEN VAL2 = LLE-ASPEN VAL3 = LLE-ASPEN VAL4 = 
LLE-ASPEN VAL5 = LLE-ASPEN VAL6 = LLE-ASPEN VAL7 = LLE-ASPEN VAL8 = LLE-ASPEN 
VAL9 = LLE-ASPEN VAL10 = LLE-ASPEN VAL11 = LLE-ASPEN VAL12 = LLE-ASPEN \ ? 
"PROP-SET" MAIN HXDESIGN ? ; "SI_MOLE" ; \ P1 ID = MASSVFRA \ \ P1 ID = 
MASSFLMX UNITS = ( "kg/sec" ) \ \ P1 ID = HMX UNITS = ( "J/kg" ) \ \ P1 ID = 
RHOMX UNITS = ( "kg/cum" ) \ \ P1 ID = CPMX UNITS = ( "J/kg-K" ) \ \ P1 ID = 
PCMX UNITS = ( "N/sqm" ) \ \ P1 ID = MUMX UNITS = ( "N-sec/sqm" ) \ \ P1 ID
 = KMX UNITS = ( "Watt/m-K" ) \ \ P1 ID = SIGMAMX UNITS = ( "N/m" ) \ \ P1 ID
 = MWMX \ \ P2 PHASE = ( T V L ) \ \ DESCRIPTION DESCRIPTION = 
"Thermal and Transport, for heat exchanger design" \ ? "PROP-SET" MAIN 
THERMAL ? ; "ENG_MOLE" ; \ P1 ID = HMX UNITS = ( "Btu/lb" ) \ \ P1 ID = CPMX 
UNITS = ( "Btu/lb-R" ) \ \ P1 ID = KMX \ \ P2 SUBSTREAM = MIXED PHASE = ( V L 
) \ \ DESCRIPTION DESCRIPTION = 
"Enthalpy, heat capacity, and thermal conductivity" \ ? "PROP-SET" MAIN 
TXPORT ? ; "ENG_MOLE" ; \ P1 ID = RHOMX UNITS = ( "lb/cuft" ) \ \ P1 ID = 
MUMX \ \ P1 ID = SIGMAMX \ \ P2 SUBSTREAM = MIXED PHASE = ( V L ) \ \ 
DESCRIPTION DESCRIPTION = "Density, viscosity, and surface tension" \ ? 
"PROP-SET" MAIN VLE ? ; "ENG_MOLE" ; \ P1 ID = PHIMX \ \ P1 ID = GAMMA \ \ P1 
ID = PL \ \ P2 SUBSTREAM = MIXED PHASE = ( V L ) \ \ DESCRIPTION DESCRIPTION
 = "Fugacity, activity, and vapor pressure" \ ? "PROP-SET" MAIN VLLE ? ; 
"ENG_MOLE" ; \ P1 ID = PHIMX \ \ P1 ID = GAMMA \ \ P1 ID = PL \ \ P2 
SUBSTREAM = MIXED PHASE = ( V L1 L2 ) \ \ DESCRIPTION DESCRIPTION = 
"Fugacity, activity, and vapor pressure" \ ? BLOCK RSTOIC RSTOIC ? ; "ENG_MOLE" 
; ; ICON1 ; ? BLOCK RGIBBS RGIBBS ? ; "ENG_MOLE" ; ; ICON2 ; ? BLOCK RCSTR 
RCSTR ? ; "ENG_MOLE" ; ; ICON1 ; ? BLOCK RPLUG RPLUG ? ; "ENG_MOLE" ; ; ICON1 
; ? BLOCK DUPL B1 ? ; "ENG_MOLE" ; ; BLOCK ; 

 GRAPHICS_BACKUP
PFS V 5.00
$CONFIG
paramdata ENRTL-RK
paramdata VLE-IG
paramdata VLE-RK
paramdata VLE-HOC
paramdata LLE-LIT
paramdata LLE-ASPEN
paramdata VLE-LIT
paramdata BINARY
paramdata EOS-LIT
paramdata HENRY
purebank PURE11
purebank AQUEOUS
purebank SOLIDS
purebank INORGANIC
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qwformat %.0f
tempformat %.0f
presformat %.0f
flowformat %.0f
strmqwformat %.0f
vflowformat %.0f
mflowformat %.0f
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