MM "37.0" FLAVOR "NO" VERSION "37.0" DATETIME "Wed Nov 18 19:26:06 2020"
MACHINE "WIN-NT/VC" ;
startlibrary
version1
NumLibs = 2
Built-In
ACM Built-In
NumCats = 12
Mixers/Splitters
active
Separators
active
Exchangers
active
Columns
active
Reactors
active
Pressure Changers
active
Manipulators
active
Solids
active
Solids Separators
active
User Models
active
Controllers
active
Batch Models
active
endlibrary
;
3
>VERSION 0
REACTOR
RStoic
Built-In
RSTOIC
>VERSION 0
COOL
Heater
Built-In
HEATER
>VERSION 0
SEP
Flash2
Built-In
FLASH2
? SETUP MAIN ? \ "RUN-CLASS" RUN-CLASS = FLOWSHEET \ \ SIMULATE INTERACTIVE
= NO MOLEFLOW = MOLEFLOW MOLEFRAC = MOLEFRAC INPUT-MODE = "STEADY-STATE"
VISITED = 1 \ ? SETUP GLOBAL ? \ "IN-UNITS" INSET = METCBAR \ \ "STREAM-CLASS"
SCLASS = CONVEN \ ? SETUP DIAGNOSTICS ? ? SETUP "SIM-OPTIONS" ? ;
"METCBAR_MOLE" ; ? SETUP "MODEL-OPTION" ? ; "METCBAR_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 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \
? SETUP "UNITS-SET" METCKGCM ? \ DESCRIPTION DESCRIPTION =
"Metric Units with C, KG/SQCM, MMKCAL/HR, and CUM" \ \ MMLOCAL \ \ UNITSET
BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 7 7 3 3 5 3 3 3 8 3 4 3 3 3 3 1 3 3 3 4
3 7 3 3 3 3 3 4 4 3 3 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3 3 3 3 3 3 4 3 3 3 3 3 3
3 3 3 4 8 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3
3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \
? SETUP "UNITS-SET" "SI-CBAR" ? \ DESCRIPTION DESCRIPTION =
"International System Units with C, BAR, and /HR" \ \ MMLOCAL \ \ UNITSET
BASESET = SI ( 1 1 1 1 1 1 1 1 1 3 3 7 1 1 1 1 1 1 1 5 1 4 1 1 1 1 1 1 1 1 4
1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
1 1 1 4 5 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1
1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 ) \
? SETUP "RUN-CONTROL" ? ? ODATABANKS ? \ ODATABANKS AUTO-PARAM = YES \ ?
"DATA-SERVICE" ? ? DATABANKS ? \ DATABANKS FILE-SYM-NAM = ( "APV110 PURE37"
"APV110 SOLIDS" "APV110 AQUEOUS" "APV110 INORGANIC" ) \ ? COMPONENTS MAIN ? \
COMPONENTS CID = BENZENE ANAME = C6H6 OUTNAME = BENZENE DBNAME1 = "BENZENE"
ANAME1 = "C6H6" / CID = PROPYLEN ANAME = C3H6-2 OUTNAME = PROPYLEN DBNAME1
= "PROPYLENE" ANAME1 = "C3H6-2" / CID = CUMENE ANAME = C9H12-2 OUTNAME =
CUMENE DBNAME1 = "ISOPROPYLBENZENE" ANAME1 = "C9H12-2" \ ? COMPONENTS
FORMULA ? \ FORMULA COMP = PROPYLEN NAME1 = C3H6-2 / COMP = CUMENE NAME1 =
C9H12-2 \ ? COMPONENTS "ADA/PCS" "LE-PROP-DATA" ? ; "METCBAR_MOLE" ; ?
COMPONENTS "COMP-LIST" GLOBAL ? ? COMPONENTS "UNIFAC-GROUP" ? ? SOLVE ? \
"RUN-MODE" MODE = SIM \ ? "INIT-VAR-ATT" ? ? "EO-ALIAS" ? ? SPECGROUPS ? ?
CONNECTIONS ? ? "EO-OPTIONS" ? ? SCRIPTMETHOD ? ? "DYN-OPTIONS" ? ? FLOWSHEET
GLOBAL ? \ BLOCK BLKID = REACTOR BLKTYPE = RSTOIC MDLTYPE = "RStoic" IN = (
FEED M0-1 RECYCLE M0-1 ) OUT = ( "REAC-OUT" M0-1 ) \ \ BLOCK BLKID = COOL
BLKTYPE = HEATER MDLTYPE = "Heater" IN = ( "REAC-OUT" M0-1 ) OUT = ( "COOL-OUT"
M0-1 ) \ \ BLOCK BLKID = SEP BLKTYPE = FLASH2 MDLTYPE = "Flash2" IN = (
"COOL-OUT" M0-1 ) OUT = ( RECYCLE M0-1 PRODUCT M1-2 ) \ \ "DEF-STREAM" SCLASS
= CONVEN \ ? PROPERTIES MAIN ? \ GPROPERTIES GBASEOPSET = SRK GOPSETNAME =
SRK GFREE-WATER = STEAMNBS PARCON = -2 \ ? PROPERTIES "OPTION-SETS" SRK ? \
PARAM BASE = SRK \ ? PROPERTIES "OPTION-SETS" STEAMNBS ? \ PARAM BASE =
STEAMNBS \ ? PROPERTIES "NC-PROPS" ? ? PROPERTIES "MOLEC-STRUCT" BENZENE ? ?
PROPERTIES "MOLEC-STRUCT" CUMENE ? ? PROPERTIES "MOLEC-STRUCT" PROPYLEN ? ?
PROPERTIES PARAMETERS SUMMARY ? ? PROPERTIES PARAMETERS BINARY SCALAR
"MLQKIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = MLQKIJ SETNO = 1 UNITROW
= 0 \ ? PROPERTIES PARAMETERS BINARY SCALAR "RKTKIJ-1" ? ; "ENG_MOLE" ; \
PROP-LIST PARAMNAME = RKTKIJ SETNO = 1 UNITROW = 0 \ ? PROPERTIES PARAMETERS
BINARY "T-DEPENDENT" "ANDKIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME =
ANDKIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F NEL = 2 \ ?
PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "ANDMIJ-1" ? ; "ENG_MOLE" ; \
PROP-LIST PARAMNAME = ANDMIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL
= F NEL = 2 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "MUKIJ-1" ? ;
"ENG_MOLE" ; \ PROP-LIST PARAMNAME = MUKIJ SETNO = 1 UNITROW = 0 TUNITROW = 22
TUNITLABEL = F NEL = 6 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT" "MULIJ-1"
? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = MULIJ SETNO = 1 UNITROW = 0 TUNITROW
= 22 TUNITLABEL = F NEL = 11 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT"
"SRKKIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = SRKKIJ SETNO = 1 UNITROW
= 0 TUNITROW = 22 TUNITLABEL = F BDBANK = ( "APV110 ETHYLENE"
"APV110 SRK-ASPEN" ) NEL = 5 \ ? PROPERTIES PARAMETERS BINARY "T-DEPENDENT"
"SRKLIJ-1" ? ; "ENG_MOLE" ; \ PROP-LIST PARAMNAME = SRKLIJ SETNO = 1 UNITROW
= 0 TUNITROW = 22 TUNITLABEL = F NEL = 8 \ ? PROPERTIES "ATTR-COMPS" ? ?
POLYMERS ? ? "ATTR-SCALING" ? ; "METCBAR_MOLE" ; ? "STREAM-CLASS" SUBSTREAMS
? \ DEF-SUBS-CLA SUBSTREAMS = MIXED \ \ DEF-SUBS-CLA SUBSTREAMS = CISOLID \ \
DEF-SUBS-CLA SUBSTREAMS = NC \ \ DEF-SUBS-CLA SUBSTREAMS = NCPSD \ \
DEF-SUBS-CLA SUBSTREAMS = CIPSD \ ? "STREAM-CLASS" "STREAM-CLASS" ? \
DEFINITION SCLASS = CONVEN \ \ DEFINITION SCLASS = MIXNC \ \ DEFINITION
SCLASS = MIXCISLD \ \ DEFINITION SCLASS = MIXNCPSD \ \ DEFINITION SCLASS =
MIXCIPSD \ \ DEFINITION SCLASS = MIXCINC \ \ DEFINITION SCLASS = MCINCPSD \ \
HEAT-DEFINE H-SCLASS = HEAT STREAM-ATTR = HEAT \ \ HEAT-DEFINE H-SCLASS =
LOAD STREAM-ATTR = LOAD \ ? "STREAM-CLASS" "DEF-STREAMS" ? ? "PROP-SET" MAIN
HXDESIGN ? ; "METCBAR_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 ) SYSPRES = YES \ \ DESCRIPTION DESCRIPTION =
"Thermal and Transport, for heat exchanger design" \ ? "PROP-SET" MAIN
THERMAL ? ; "METCBAR_MOLE" ; \ P1 ID = HMX UNITS = ( "Btu/lb" ) \ \ P1 ID =
CPMX UNITS = ( "Btu/lb-R" ) \ \ P1 ID = KMX \ \ P2 SUBSTREAM = MIXED PHASE =
( V L ) SYSPRES = YES \ \ DESCRIPTION DESCRIPTION =
"Enthalpy, heat capacity, and thermal conductivity" \ ? "PROP-SET" MAIN
TXPORT ? ; "METCBAR_MOLE" ; \ P1 ID = RHOMX UNITS = ( "lb/cuft" ) \ \ P1 ID
= MUMX \ \ P1 ID = SIGMAMX \ \ P2 SUBSTREAM = MIXED PHASE = ( V L ) SYSPRES
= YES \ \ DESCRIPTION DESCRIPTION = "Density, viscosity, and surface tension"
\ ? "PROP-SET" MAIN VLE ? ; "METCBAR_MOLE" ; \ P1 ID = PHIMX \ \ P1 ID =
GAMMA \ \ P1 ID = PL \ \ P2 SUBSTREAM = MIXED PHASE = ( V L ) SYSPRES = YES \
\ DESCRIPTION DESCRIPTION = "Fugacity, activity, and vapor pressure" \ ?
"PROP-SET" MAIN VLLE ? ; "METCBAR_MOLE" ; \ P1 ID = PHIMX \ \ P1 ID = GAMMA \
\ P1 ID = PL \ \ P2 SUBSTREAM = MIXED PHASE = ( V L1 L2 ) SYSPRES = YES \ \
DESCRIPTION DESCRIPTION = "Fugacity, activity, and vapor pressure" \ ?
"STREAM-NAMES" ? ? "STREAM-GROUP" All ? \ DESCRIPTION DESCRIPTION =
"All streams" \ ? "STREAM-GROUP" Boundary ? \ DESCRIPTION DESCRIPTION =
"Boundary streams" \ ? "STREAM-GROUP" Charge ? \ DESCRIPTION DESCRIPTION =
"Charge streams" \ ? "STREAM-GROUP" Feeds ? \ DESCRIPTION DESCRIPTION =
"Feed streams" \ ? "STREAM-GROUP" Initial ? \ DESCRIPTION DESCRIPTION =
"Streams with user-specified values entered" \ ? "STREAM-GROUP" Products ? \
DESCRIPTION DESCRIPTION = "Product streams" \ ? "STREAM-GROUP" "SG-1" ? \
"STREAM-GROUP" STREAM-LIST = ( PRODUCT "REAC-OUT" ) PRIORITY = 8 \ ?
"STREAM-GROUP" Tears ? \ DESCRIPTION DESCRIPTION =
"Tear streams manipulated by the convergence algorithms" \ ? STREAM MATERIAL
"COOL-OUT" ? ; "METCBAR_MOLE" ; \ SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \
\ "SS-FLOWEMBED" SSXML = (
"DefaultFullfalsetruefalse"
"<srcSettings$StreamIds=""COOL-OUT""$TemplateName=""Full""><TFFTab"
"le><GeneralOptions>Description,SourceAndDestination,StreamCla"
"ss,MaximumErrorTolerance,CostFlow,PhaseLabel,ComponentAttributes,Parti"
"cleSizeDistributions,Temperature,Pressure,MolarVaporFraction,MolarLiqu"
"idFraction,MolarSolidFraction,MolarEnthalpy,MolarEntropy,MolarDensity,"
"MassVaporFraction,MassLiquidFraction,MassSolidFraction,MassEnthalpy,Ma"
"ssEntropy,MassDensity,EnthalpyFlow,AverageMolecularWeight,BatchPropert"
"ies</GeneralOptions><ScopeOptions>PhasesForMixedSubstream,"
"TotalStream,Substreams,MoleFlows,MassFlows,MoleFractions,MassFractions"
",VolumeFlows</ScopeOptions><Properties><Property$Type="""
"StateConditionProperty""$EngineName=""TEMP""$/><Property$Type=""Stat"
"eConditionProperty""$EngineName=""PRES""$/><Property$Type=""StateCon"
"ditionProperty""$EngineName=""VFRAC""$/><Property$Type=""StateCondit"
"ionProperty""$EngineName=""LFRAC""$/><Property$Type=""StateCondition"
"Property""$EngineName=""SFRAC""$/><Property$Type=""StateConditionPro"
"perty""$EngineName=""MASSVFRA""$/><Property$Type=""StateConditionPro"
"perty""$EngineName=""MASSLFRA""$/><Property$Type=""StateConditionPro"
"perty""$EngineName=""MASSSFRA""$/><Property$Type=""StateConditionPro"
"perty""$EngineName=""HMX""$/><Property$Type=""StateConditionProperty"
"""$EngineName=""MASSHMX""$/><Property$Type=""StateConditionProperty"""
"$EngineName=""SMX""$/><Property$Type=""StateConditionProperty""$Engi"
"neName=""MASSSMX""$/><Property$Type=""StateConditionProperty""$Engin"
"eName=""RHOMX""$/><Property$Type=""StateConditionProperty""$EngineNa"
"me=""MASSRHOM""$/><Property$Type=""StateConditionProperty""$EngineNa"
"me=""HFLMX""$/><Property$Type=""StateConditionProperty""$EngineName="
"""MWMX""$/><Property$Type=""StateConditionProperty""$EngineName=""MOL"
"EFLOW""$/><Property$Type=""StateConditionProperty""$EngineName=""MOL"
"EFRAC""$/><Property$Type=""StateConditionProperty""$EngineName=""MAS"
"SFLOW""$/><Property$Type=""StateConditionProperty""$EngineName=""MAS"
"SFRAC""$/><Property$Type=""StateConditionProperty""$EngineName=""VOL"
"FLMX""$/><Property$Type=""BatchProperty""$EngineName=""cmole_cycle""$"
"/><Property$Type=""BatchProperty""$EngineName=""cmole_time""$/>&l"
"t;Property$Type=""BatchProperty""$EngineName=""cmass_cycle""$/><Prop"
"erty$Type=""BatchProperty""$EngineName=""cmass_time""$/><Property$Ty"
"pe=""BatchProperty""$EngineName=""vol_cycle""$/><Property$Type=""Batc"
"hProperty""$EngineName=""vol_time""$/><Property$Type=""BatchProperty"
"""$EngineName=""enth_cycle""$/><Property$Type=""BatchProperty""$Engin"
"eName=""enth_time""$/><Property$Type=""BatchProperty""$EngineName=""c"
"ycle_time""$/><Property$Type=""BatchProperty""$EngineName=""oper_tim"
"e""$/><Property$Type=""BatchProperty""$EngineName=""ntrain""$/><"
";/Properties></TFFTable></srcSettings>" ) \ ? STREAM MATERIAL FEED ? ; "METCBAR_MOLE" ; \
SUBSTREAM SSID = MIXED TEMP = 100. <22> <4> PRES = 2.5 <20> <5> BASIS =
"MOLE-FLOW" MIXED-SPEC = TP TOTAL = 40. <-89> <0> JUNK = 2 \ \ MOLE-FLOW
SSID1 = MIXED CID = BENZENE FLOW = 20. <-89> <3> / SSID1 = MIXED CID =
PROPYLEN FLOW = 20. <-89> <3> \ \ "SS-FLOWEMBED" SSXML = (
"DefaultFullfalsetruefalse"
"<srcSettings$StreamIds=""FEED""$TemplateName=""Full""><TFFTable&g"
"t;<GeneralOptions>Description,SourceAndDestination,StreamClass,M"
"aximumErrorTolerance,CostFlow,PhaseLabel,ComponentAttributes,ParticleS"
"izeDistributions,Temperature,Pressure,MolarVaporFraction,MolarLiquidFr"
"action,MolarSolidFraction,MolarEnthalpy,MolarEntropy,MolarDensity,Mass"
"VaporFraction,MassLiquidFraction,MassSolidFraction,MassEnthalpy,MassEn"
"tropy,MassDensity,EnthalpyFlow,AverageMolecularWeight,BatchProperties&"
"lt;/GeneralOptions><ScopeOptions>PhasesForMixedSubstream,Tota"
"lStream,Substreams,MoleFlows,MassFlows,MoleFractions,MassFractions,Vol"
"umeFlows</ScopeOptions><Properties><Property$Type=""Stat"
"eConditionProperty""$EngineName=""TEMP""$/><Property$Type=""StateCon"
"ditionProperty""$EngineName=""PRES""$/><Property$Type=""StateConditi"
"onProperty""$EngineName=""VFRAC""$/><Property$Type=""StateConditionP"
"roperty""$EngineName=""LFRAC""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""SFRAC""$/><Property$Type=""StateConditionPropert"
"y""$EngineName=""MASSVFRA""$/><Property$Type=""StateConditionPropert"
"y""$EngineName=""MASSLFRA""$/><Property$Type=""StateConditionPropert"
"y""$EngineName=""MASSSFRA""$/><Property$Type=""StateConditionPropert"
"y""$EngineName=""HMX""$/><Property$Type=""StateConditionProperty""$En"
"gineName=""MASSHMX""$/><Property$Type=""StateConditionProperty""$Eng"
"ineName=""SMX""$/><Property$Type=""StateConditionProperty""$EngineNa"
"me=""MASSSMX""$/><Property$Type=""StateConditionProperty""$EngineNam"
"e=""RHOMX""$/><Property$Type=""StateConditionProperty""$EngineName="""
"MASSRHOM""$/><Property$Type=""StateConditionProperty""$EngineName="""
"HFLMX""$/><Property$Type=""StateConditionProperty""$EngineName=""MWM"
"X""$/><Property$Type=""StateConditionProperty""$EngineName=""MOLEFLO"
"W""$/><Property$Type=""StateConditionProperty""$EngineName=""MOLEFRA"
"C""$/><Property$Type=""StateConditionProperty""$EngineName=""MASSFLO"
"W""$/><Property$Type=""StateConditionProperty""$EngineName=""MASSFRA"
"C""$/><Property$Type=""StateConditionProperty""$EngineName=""VOLFLMX"
"""$/><Property$Type=""BatchProperty""$EngineName=""cmole_cycle""$/>"
";<Property$Type=""BatchProperty""$EngineName=""cmole_time""$/><Pr"
"operty$Type=""BatchProperty""$EngineName=""cmass_cycle""$/><Property"
"$Type=""BatchProperty""$EngineName=""cmass_time""$/><Property$Type="""
"BatchProperty""$EngineName=""vol_cycle""$/><Property$Type=""BatchPro"
"perty""$EngineName=""vol_time""$/><Property$Type=""BatchProperty""$En"
"gineName=""enth_cycle""$/><Property$Type=""BatchProperty""$EngineNam"
"e=""enth_time""$/><Property$Type=""BatchProperty""$EngineName=""cycle"
"_time""$/><Property$Type=""BatchProperty""$EngineName=""oper_time""$/"
"><Property$Type=""BatchProperty""$EngineName=""ntrain""$/></Pr"
"operties></TFFTable></srcSettings>" ) \ ? STREAM MATERIAL PRODUCT ? ; "METCBAR_MOLE" ; \
SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \ \ "SS-FLOWEMBED" SSXML = (
"DefaultFullfalsetruefalse"
"<srcSettings$StreamIds=""PRODUCT""$TemplateName=""Full""><TFFTabl"
"e><GeneralOptions>Description,SourceAndDestination,StreamClas"
"s,MaximumErrorTolerance,CostFlow,PhaseLabel,ComponentAttributes,Partic"
"leSizeDistributions,Temperature,Pressure,MolarVaporFraction,MolarLiqui"
"dFraction,MolarSolidFraction,MolarEnthalpy,MolarEntropy,MolarDensity,M"
"assVaporFraction,MassLiquidFraction,MassSolidFraction,MassEnthalpy,Mas"
"sEntropy,MassDensity,EnthalpyFlow,AverageMolecularWeight,BatchProperti"
"es</GeneralOptions><ScopeOptions>PhasesForMixedSubstream,T"
"otalStream,Substreams,MoleFlows,MassFlows,MoleFractions,MassFractions,"
"VolumeFlows</ScopeOptions><Properties><Property$Type=""S"
"tateConditionProperty""$EngineName=""TEMP""$/><Property$Type=""State"
"ConditionProperty""$EngineName=""PRES""$/><Property$Type=""StateCond"
"itionProperty""$EngineName=""VFRAC""$/><Property$Type=""StateConditi"
"onProperty""$EngineName=""LFRAC""$/><Property$Type=""StateConditionP"
"roperty""$EngineName=""SFRAC""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""MASSVFRA""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""MASSLFRA""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""MASSSFRA""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""HMX""$/><Property$Type=""StateConditionProperty"""
"$EngineName=""MASSHMX""$/><Property$Type=""StateConditionProperty""$"
"EngineName=""SMX""$/><Property$Type=""StateConditionProperty""$Engin"
"eName=""MASSSMX""$/><Property$Type=""StateConditionProperty""$Engine"
"Name=""RHOMX""$/><Property$Type=""StateConditionProperty""$EngineNam"
"e=""MASSRHOM""$/><Property$Type=""StateConditionProperty""$EngineNam"
"e=""HFLMX""$/><Property$Type=""StateConditionProperty""$EngineName="""
"MWMX""$/><Property$Type=""StateConditionProperty""$EngineName=""MOLE"
"FLOW""$/><Property$Type=""StateConditionProperty""$EngineName=""MOLE"
"FRAC""$/><Property$Type=""StateConditionProperty""$EngineName=""MASS"
"FLOW""$/><Property$Type=""StateConditionProperty""$EngineName=""MASS"
"FRAC""$/><Property$Type=""StateConditionProperty""$EngineName=""VOLF"
"LMX""$/><Property$Type=""BatchProperty""$EngineName=""cmole_cycle""$/"
"><Property$Type=""BatchProperty""$EngineName=""cmole_time""$/><"
";Property$Type=""BatchProperty""$EngineName=""cmass_cycle""$/><Prope"
"rty$Type=""BatchProperty""$EngineName=""cmass_time""$/><Property$Typ"
"e=""BatchProperty""$EngineName=""vol_cycle""$/><Property$Type=""Batch"
"Property""$EngineName=""vol_time""$/><Property$Type=""BatchProperty"""
"$EngineName=""enth_cycle""$/><Property$Type=""BatchProperty""$Engine"
"Name=""enth_time""$/><Property$Type=""BatchProperty""$EngineName=""cy"
"cle_time""$/><Property$Type=""BatchProperty""$EngineName=""oper_time"
"""$/><Property$Type=""BatchProperty""$EngineName=""ntrain""$/><"
"/Properties></TFFTable></srcSettings>" ) \ ? STREAM MATERIAL "REAC-OUT" ? ; "METCBAR_MOLE" ; \
SUBSTREAM SSID = MIXED TOTAL = 0. <0> <0> \ \ "SS-FLOWEMBED" SSXML = (
"DefaultFullfalsetruefalse" ) \ ? STREAM
MATERIAL RECYCLE ? ; "METCBAR_MOLE" ; \ SUBSTREAM SSID = MIXED TOTAL = 0. <0>
<0> \ \ "SS-FLOWEMBED" SSXML = (
"DefaultFullfalsetruefalse"
"<srcSettings$StreamIds=""RECYCLE""$TemplateName=""Full""><TFFTabl"
"e><GeneralOptions>Description,SourceAndDestination,StreamClas"
"s,MaximumErrorTolerance,CostFlow,PhaseLabel,ComponentAttributes,Partic"
"leSizeDistributions,Temperature,Pressure,MolarVaporFraction,MolarLiqui"
"dFraction,MolarSolidFraction,MolarEnthalpy,MolarEntropy,MolarDensity,M"
"assVaporFraction,MassLiquidFraction,MassSolidFraction,MassEnthalpy,Mas"
"sEntropy,MassDensity,EnthalpyFlow,AverageMolecularWeight,BatchProperti"
"es</GeneralOptions><ScopeOptions>PhasesForMixedSubstream,T"
"otalStream,Substreams,MoleFlows,MassFlows,MoleFractions,MassFractions,"
"VolumeFlows</ScopeOptions><Properties><Property$Type=""S"
"tateConditionProperty""$EngineName=""TEMP""$/><Property$Type=""State"
"ConditionProperty""$EngineName=""PRES""$/><Property$Type=""StateCond"
"itionProperty""$EngineName=""VFRAC""$/><Property$Type=""StateConditi"
"onProperty""$EngineName=""LFRAC""$/><Property$Type=""StateConditionP"
"roperty""$EngineName=""SFRAC""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""MASSVFRA""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""MASSLFRA""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""MASSSFRA""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""HMX""$/><Property$Type=""StateConditionProperty"""
"$EngineName=""MASSHMX""$/><Property$Type=""StateConditionProperty""$"
"EngineName=""SMX""$/><Property$Type=""StateConditionProperty""$Engin"
"eName=""MASSSMX""$/><Property$Type=""StateConditionProperty""$Engine"
"Name=""RHOMX""$/><Property$Type=""StateConditionProperty""$EngineNam"
"e=""MASSRHOM""$/><Property$Type=""StateConditionProperty""$EngineNam"
"e=""HFLMX""$/><Property$Type=""StateConditionProperty""$EngineName="""
"MWMX""$/><Property$Type=""StateConditionProperty""$EngineName=""MOLE"
"FLOW""$/><Property$Type=""StateConditionProperty""$EngineName=""MOLE"
"FRAC""$/><Property$Type=""StateConditionProperty""$EngineName=""MASS"
"FLOW""$/><Property$Type=""StateConditionProperty""$EngineName=""MASS"
"FRAC""$/><Property$Type=""StateConditionProperty""$EngineName=""VOLF"
"LMX""$/><Property$Type=""BatchProperty""$EngineName=""cmole_cycle""$/"
"><Property$Type=""BatchProperty""$EngineName=""cmole_time""$/><"
";Property$Type=""BatchProperty""$EngineName=""cmass_cycle""$/><Prope"
"rty$Type=""BatchProperty""$EngineName=""cmass_time""$/><Property$Typ"
"e=""BatchProperty""$EngineName=""vol_cycle""$/><Property$Type=""Batch"
"Property""$EngineName=""vol_time""$/><Property$Type=""BatchProperty"""
"$EngineName=""enth_cycle""$/><Property$Type=""BatchProperty""$Engine"
"Name=""enth_time""$/><Property$Type=""BatchProperty""$EngineName=""cy"
"cle_time""$/><Property$Type=""BatchProperty""$EngineName=""oper_time"
"""$/><Property$Type=""BatchProperty""$EngineName=""ntrain""$/><"
"/Properties></TFFTable></srcSettings>" ) \ ? "EO-VARS" ? \ "SS-FLOWEMBED" SSXML = (
"SG-1Chemicalsfalsefalsefalse" ) \ ?
BLOCK HEATER COOL ? ; "METCBAR_MOLE" ; ; HEATER ; \ PARAM TEMP = 50. <22> <4>
PRES = -0.005 <20> <5> DPPARM = 1E-009 <0> <0> SPEC-OPT = TP \ \ "SS-FLOWEMBED"
SSXML = (
"BoundaryFullfalsetruefalse<srcSettings$StreamIds=""REAC-OUT,COOL-OUT""$TemplateName=""Full"">"
"<TFFTable><GeneralOptions>Description,SourceAndDestination"
",StreamClass,MaximumErrorTolerance,CostFlow,PhaseLabel,ComponentAttrib"
"utes,ParticleSizeDistributions,Temperature,Pressure,MolarVaporFraction"
",MolarLiquidFraction,MolarSolidFraction,MolarEnthalpy,MolarEntropy,Mol"
"arDensity,MassVaporFraction,MassLiquidFraction,MassSolidFraction,MassE"
"nthalpy,MassEntropy,MassDensity,EnthalpyFlow,AverageMolecularWeight,Ba"
"tchProperties</GeneralOptions><ScopeOptions>PhasesForMixed"
"Substream,TotalStream,Substreams,MoleFlows,MassFlows,MoleFractions,Mas"
"sFractions,VolumeFlows</ScopeOptions><Properties><Prope"
"rty$Type=""StateConditionProperty""$EngineName=""TEMP""$/><Property$"
"Type=""StateConditionProperty""$EngineName=""PRES""$/><Property$Type"
"=""StateConditionProperty""$EngineName=""VFRAC""$/><Property$Type=""S"
"tateConditionProperty""$EngineName=""LFRAC""$/><Property$Type=""Stat"
"eConditionProperty""$EngineName=""SFRAC""$/><Property$Type=""StateCo"
"nditionProperty""$EngineName=""MASSVFRA""$/><Property$Type=""StateCo"
"nditionProperty""$EngineName=""MASSLFRA""$/><Property$Type=""StateCo"
"nditionProperty""$EngineName=""MASSSFRA""$/><Property$Type=""StateCo"
"nditionProperty""$EngineName=""HMX""$/><Property$Type=""StateConditi"
"onProperty""$EngineName=""MASSHMX""$/><Property$Type=""StateConditio"
"nProperty""$EngineName=""SMX""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""MASSSMX""$/><Property$Type=""StateConditionPrope"
"rty""$EngineName=""RHOMX""$/><Property$Type=""StateConditionProperty"
"""$EngineName=""MASSRHOM""$/><Property$Type=""StateConditionProperty"
"""$EngineName=""HFLMX""$/><Property$Type=""StateConditionProperty""$E"
"ngineName=""MWMX""$/><Property$Type=""StateConditionProperty""$Engin"
"eName=""MOLEFLOW""$/><Property$Type=""StateConditionProperty""$Engin"
"eName=""MOLEFRAC""$/><Property$Type=""StateConditionProperty""$Engin"
"eName=""MASSFLOW""$/><Property$Type=""StateConditionProperty""$Engin"
"eName=""MASSFRAC""$/><Property$Type=""StateConditionProperty""$Engin"
"eName=""VOLFLMX""$/><Property$Type=""BatchProperty""$EngineName=""cmo"
"le_cycle""$/><Property$Type=""BatchProperty""$EngineName=""cmole_tim"
"e""$/><Property$Type=""BatchProperty""$EngineName=""cmass_cycle""$/&g"
"t;<Property$Type=""BatchProperty""$EngineName=""cmass_time""$/><P"
"roperty$Type=""BatchProperty""$EngineName=""vol_cycle""$/><Property$"
"Type=""BatchProperty""$EngineName=""vol_time""$/><Property$Type=""Bat"
"chProperty""$EngineName=""enth_cycle""$/><Property$Type=""BatchPrope"
"rty""$EngineName=""enth_time""$/><Property$Type=""BatchProperty""$Eng"
"ineName=""cycle_time""$/><Property$Type=""BatchProperty""$EngineName"
"=""oper_time""$/><Property$Type=""BatchProperty""$EngineName=""ntrain"
"""$/></Properties></TFFTable></srcSettings>" ) \ ? BLOCK FLASH2 SEP ? ; "METCBAR_MOLE" ; ;
"V-DRUM1" ; \ PARAM PRES = 1. <20> <5> DUTY = 0.0 <13> <7> SPEC-OPT = PD \ \
FRAC SUBSTREAM = MIXED \ \ "SS-FLOWEMBED" SSXML = (
"BoundaryFullfalsetruefalse<srcSettings$StreamIds=""COOL-OUT,PRODUCT,RECYCLE""$TemplateName=""Fu"
"ll""><TFFTable><GeneralOptions>Description,SourceAndDest"
"ination,StreamClass,MaximumErrorTolerance,CostFlow,PhaseLabel,Componen"
"tAttributes,ParticleSizeDistributions,Temperature,Pressure,MolarVaporF"
"raction,MolarLiquidFraction,MolarSolidFraction,MolarEnthalpy,MolarEntr"
"opy,MolarDensity,MassVaporFraction,MassLiquidFraction,MassSolidFractio"
"n,MassEnthalpy,MassEntropy,MassDensity,EnthalpyFlow,AverageMolecularWe"
"ight,BatchProperties</GeneralOptions><ScopeOptions>PhasesF"
"orMixedSubstream,TotalStream,Substreams,MoleFlows,MassFlows,MoleFracti"
"ons,MassFractions,VolumeFlows</ScopeOptions><Properties>&l"
"t;Property$Type=""StateConditionProperty""$EngineName=""TEMP""$/><Pr"
"operty$Type=""StateConditionProperty""$EngineName=""PRES""$/><Proper"
"ty$Type=""StateConditionProperty""$EngineName=""VFRAC""$/><Property$"
"Type=""StateConditionProperty""$EngineName=""LFRAC""$/><Property$Typ"
"e=""StateConditionProperty""$EngineName=""SFRAC""$/><Property$Type="""
"StateConditionProperty""$EngineName=""MASSVFRA""$/><Property$Type="""
"StateConditionProperty""$EngineName=""MASSLFRA""$/><Property$Type="""
"StateConditionProperty""$EngineName=""MASSSFRA""$/><Property$Type="""
"StateConditionProperty""$EngineName=""HMX""$/><Property$Type=""State"
"ConditionProperty""$EngineName=""MASSHMX""$/><Property$Type=""StateC"
"onditionProperty""$EngineName=""SMX""$/><Property$Type=""StateCondit"
"ionProperty""$EngineName=""MASSSMX""$/><Property$Type=""StateConditi"
"onProperty""$EngineName=""RHOMX""$/><Property$Type=""StateConditionP"
"roperty""$EngineName=""MASSRHOM""$/><Property$Type=""StateConditionP"
"roperty""$EngineName=""HFLMX""$/><Property$Type=""StateConditionProp"
"erty""$EngineName=""MWMX""$/><Property$Type=""StateConditionProperty"
"""$EngineName=""MOLEFLOW""$/><Property$Type=""StateConditionProperty"
"""$EngineName=""MOLEFRAC""$/><Property$Type=""StateConditionProperty"
"""$EngineName=""MASSFLOW""$/><Property$Type=""StateConditionProperty"
"""$EngineName=""MASSFRAC""$/><Property$Type=""StateConditionProperty"
"""$EngineName=""VOLFLMX""$/><Property$Type=""BatchProperty""$EngineNa"
"me=""cmole_cycle""$/><Property$Type=""BatchProperty""$EngineName=""cm"
"ole_time""$/><Property$Type=""BatchProperty""$EngineName=""cmass_cyc"
"le""$/><Property$Type=""BatchProperty""$EngineName=""cmass_time""$/&g"
"t;<Property$Type=""BatchProperty""$EngineName=""vol_cycle""$/><Pr"
"operty$Type=""BatchProperty""$EngineName=""vol_time""$/><Property$Ty"
"pe=""BatchProperty""$EngineName=""enth_cycle""$/><Property$Type=""Bat"
"chProperty""$EngineName=""enth_time""$/><Property$Type=""BatchProper"
"ty""$EngineName=""cycle_time""$/><Property$Type=""BatchProperty""$Eng"
"ineName=""oper_time""$/><Property$Type=""BatchProperty""$EngineName="
"""ntrain""$/></Properties></TFFTable></srcSettings>"
"" ) \ ? BLOCK RSTOIC REACTOR ? ;
"METCBAR_MOLE" ; ; ICON1 ; \ PARAM PRES = 0.0 <20> <5> DUTY = 0.0 <13> <7>
SPEC-OPT = PD \ \ STOIC REACNO = 1 STOIC-CID = BENZENE STOIC-SSID = MIXED
COEF = -1 <0> <0> \ \ STOIC REACNO = 1 STOIC-CID = PROPYLEN STOIC-SSID =
MIXED COEF = -1 <0> <0> \ \ STOIC1 REACNO1 = 1 STOIC-CID1 = CUMENE
STOIC-SSID1 = MIXED COEF1 = 1 <0> <0> \ \ CONVEX EXT-REACNO = 1 KEY-SSID =
MIXED KEY-CID = PROPYLEN CONV = .9 <0> <0> \ \ PRODUCTS SID = "REAC-OUT" \ \
FORCONTROL FCVAR1 = CUMENE \ ? "DESIGN-SPEC" "DS-1" ? ; "METCBAR_MOLE" ; \
DEFINE FVN = PURITY FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM = PRODUCT FVN-SUBS
= MIXED FVN-COMPONEN = CUMENE \ \ SPEC EXPR1 = "PURITY" EXPR2 = ".98" \ \
"TOL-SPEC" TOL = ".00001" \ \ VARY VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK =
COOL VARYVARIABLE = TEMP VARYSENTENCE = PARAM VARYUOM = C \ \ LIMITS LOWER =
"30" UPPER = "150" \ ? "EO-CONV-OPTI" ? \ DMO-PARAMS MODE = DEFAULT \ \
DMO-PARAMS MODE = SIMULATION \ \ DMO-PARAMS MODE = "PARAMETER-ESTIMATION" \ \
DMO-PARAMS MODE = RECONCILIATION \ \ DMO-PARAMS MODE = OPTIMIZATION \ \
LSSQP-PARAMS MODE-L = DEFAULT \ \ LSSQP-PARAMS MODE-L = SIMULATION \ \
LSSQP-PARAMS MODE-L = "PARAMETER-ESTIMATION" \ \ LSSQP-PARAMS MODE-L =
RECONCILIATION \ \ LSSQP-PARAMS MODE-L = OPTIMIZATION \ \ NSOLVE-PARAM
NSOLVE-MODE = DEFAULT \ \ NSOLVE-PARAM NSOLVE-MODE = SIMULATION \ \
NSOLVE-PARAM NSOLVE-MODE = "PARAMETER-ESTIMATION" \ \ XSLP-PARAMS XSLP-MODE
= DEFAULT \ \ XSLP-PARAMS XSLP-MODE = SIMULATION \ \ XSLP-PARAMS XSLP-MODE
= "PARAMETER-ESTIMATION" \ \ XSLP-PARAMS XSLP-MODE = RECONCILIATION \ \
XSLP-PARAMS XSLP-MODE = OPTIMIZATION \ ? "BATCH-OPTS" ? ; "METCBAR_MOLE" ; ?
CALCULATOR "F-1" ? ; "METCBAR_MOLE" ; \ DEFINE FVN = DP FVN-VARTYPE =
"BLOCK-VAR" FVN-BLOCK = COOL FVN-VARIABLE = PRES FVN-SENTENCE = PARAM FVN-UOM
= psia \ \ DEFINE FVN = FLOW FVN-VARTYPE = "STREAM-VAR" FVN-STREAM =
"REAC-OUT" FVN-SUBS = MIXED FVN-VARIABLE = "MASS-FLOW" FVN-UOM = "lb/hr" \ \
DEFINE FVN = DENS FVN-VARTYPE = "STREAM-VAR" FVN-STREAM = "REAC-OUT" FVN-SUBS
= MIXED FVN-VARIABLE = "MASS-DENSITY" FVN-UOM = "lb/cuft" \ \ FORTRAN
FORTRAN-EXEC = ( "F VFLOW=FLOW/DENS" "F DP=-1E-9*VFLOW**2"
"C WRITE(NTERM,50) FLOW, DENS, VFLOW, DP"
"F 50 FORMAT(' FLOW=',F7.1,' DENS=',F7.4,"
"F 1 ' VFLOW=',F7.1,' DP=',F7.3)" ) \ \ "READ-VARS" READ-VAR
= ( FLOW DENS ) \ \ "WRITE-VARS" WRITE-VAR = ( DP ) \ ? SENSITIVITY "S-1" ?
; "METCBAR_MOLE" ; \ DEFINE FVN = PURITY FVN-VARTYPE = "MOLE-FRAC" FVN-STREAM
= PRODUCT FVN-SUBS = MIXED FVN-COMPONEN = CUMENE \ \ TABULATE COLNO = 1 EXPR
= "PURITY" LINE1 = "CUMENE" LINE2 = "PRODUCT " LINE3 = "PURITY" \ \ VARY
VARY-VARTYPE = "BLOCK-VAR" VARYBLOCK = COOL VARYVARIABLE = TEMP VARYSENTENCE
= PARAM VARYUOM = C LOWER = "30" UPPER = "130" NPOINT = "11" INCR =
"10.000000" OPT-LIST = RANGE DISABLE = NO OPT-RANGE = INCR \ ? "CONV-OPTIONS"
? ? TEAR ? ? "CONV-ORDER" ? ? REPORT "BLOCK-REPORT" ? ? REPORT "STREAM-REPOR"
? \ OPTIONS MOLEFLOW = MOLEFLOW MOLEFRAC = MOLEFRAC \ ? REPORT "BATCH-OPERAT"
? ; "METCBAR_MOLE" ; ? "PROP-TABLE" BINARY "BINRY-1" ? ; "METCBAR_MOLE" ; \
PROPERTIES OPSETNAME = SRK FRWATEROPSET = STEAMNBS SOLU-WATER = 3 TRUE-COMPS
= YES \ \ "MASS-FLOW" COMP1 = BENZENE COMP2 = PROPYLEN \ \ STATE VFRAC = 0.0
<0> <0> PRES = 1.013250000 <20> <5> GUNITLABEL = "kcal/mol" \ \ ANALTYP
ANALTYPE = TXY \ \ TVARY TVARNAME = TEMP TUNITLABEL = C TVARVALUE = LIST
TLIST = ( 25.00000000 <0> <0> ) \ \ PVARY PVARNAME = PRES PUNITLABEL = bar
PVARVALUE = LIST PLIST = ( 2.5 <0> <0> ) \ \ CVARY CVARNAME = MOLEFRAC CCOMP
= BENZENE VARVALUE = RANGE CLOWER = 0.0 <0> <0> CUPPER = 1.0 <0> <0> CINCR
= 0.1 <0> <0> CNPOINT = 10 OPT-CPTINCR = INCR \ \ PARAM NPHASE = 3 TAGID =
"BINRY-1" \ \ PROPTY LOCALPROP = SRK \ \ P2 PCOMPS1 = BENZENE PCOMPS2 =
PROPYLEN \ ? "PROP-TABLE" PURE "PURE-1" ? ; "METCBAR_MOLE" ; \ PROPERTIES
OPSETNAME = SRK FRWATEROPSET = STEAMNBS SOLU-WATER = 3 TRUE-COMPS = YES \ \
TVARY TVARNAME = TEMP TUNITLABEL = C VARVALUE = RANGE TLOWER = 95. <0> <0>
TUPPER = 105. <0> <0> TINCR = 5. <0> <0> TNPOINT = 2 OPT-TPTINCR = INCR \ \
PVARY PVARNAME = PRES PUNITLABEL = bar PVARVALUE = LIST PLIST = ( 1.013250000
<0> <0> ) \ \ PARAM TAGID = "PURE-1" \ \ PROPTY PROPTYPE = THERMODYNAMIC
LOCALPROP = SRK \ \ P1 ID = PL UNITS = ( bar ) \ \ P2 COMPS = ( BENZENE )
VAPOR-PHASE = NO LIQUID-PHASE = YES SOLID-PHASE = NO \ ? "STREAM-LIB" ? ;
"METCBAR_MOLE" ; ? DISABLE ? \ SENSITIVITY LIST = ( "S-1" ) \ \ CALCULATOR
LIST = ( "F-1" ) \ \ DESIGN-SPEC LIST = ( "DS-1" ) \
GRAPHICS_BACKUP
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paramdata APV110 ENRTL-RK
paramdata APV110 VLE-IG
paramdata APV110 VLE-RK
paramdata APV110 VLE-HOC
paramdata APV110 LLE-LIT
paramdata APV110 LLE-ASPEN
paramdata APV110 VLE-LIT
paramdata APV110 BINARY
paramdata APV110 EOS-LIT
paramdata APV110 HENRY-AP
paramdata APV110 SRK-ASPEN
paramdata APV110 PC-SAFT
paramdata APV110 POLYPCSF
purebank APV110 PURE25
purebank APV110 AQUEOUS
purebank APV110 SOLIDS
purebank APV110 INORGANIC
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browsertreewidth 3360
polyplusenabled 1
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heat_color 0
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work_color 0
work_style 1
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work_termid W
connections_color 9
connections_style 3
connections_width 1
connections_termid C
measurements_color 4
measurements_style 3
measurements_width 1
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displayeoconn 1
displaycalcs 0
displaytransfers 0
displaymeas 0
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displaymeascons 0
displayothercons 0
displayeomeas 1
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showeoviews 1
eoautosave 1
lockflowsheet 0
allow_system_userprops 0
copy_estimation 1
copy_retrieved 1
purge_incomp_params 0
set_default_biparams 0
set_default_dataset1 0
set_default_dataset0 1
bestinput 0
autosmrun 0
genallpropset 0
strmresformdefault 0
roottype 0
exchangerfile 1
streamformat 1
runsettingfile 1
usermodelfile 1
fortranfile 0
timeout 1000
auto_evaluate 0
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
ignoreEOVarNameFixupsOnImport 1
tpsaupgrade 1
#
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IDSET IDPH_L1 (PHASE) (LIQUID_1)
IDSET IDPH_T (PHASE) (TOTAL)
IDSET IDPH_L2 (PHASE) (LIQUID_2)
IDSET IDWET (BASIS) (WET)
IDSET IDDRY (BASIS) (DRY)
IDSET SP (PROPERTIES) (118 *6)
LSET SP (%SP)
IDSET SPSTAT (SPSTAT) (116 *1)
LSET SPSTAT ( %SPSTAT)
IDSET ID_SENS (PROPERTIES) (105 *2)
IDSET IDERR (PROPERTIES) (131 *1)
DSET RUN-STATUS SP @SP ( "NOVEMBER 18, 2020 7:25:20 P.M." )
IDSET FOR (PROPERTIES) (737 *1)
LSET FOR (%FOR)
IDSET FORSTAT (PROPERTIES) (738 *1)
LSET FORSTAT (%FORSTAT)
IDSET MW (PROPERTIES) (269 *2)
LSET MW (%MW & %ID_NCCNS)
DSET MW MW @MW (7.81136400D+01 4.20806400D+01 1.20194280D+02)
IDSET VST (PROPERTIES) (270 *2 <43> )
LSET VST (%VST & %ID_NCCNS)
DSET VST VST @VST (8.85091000D+01 <3> 8.08566000D+01 <3> 1.39057000D+02 <3> )
IDSET TB (PROPERTIES) (271 *2 <22> )
LSET TB (%TB & %ID_NCC)
DSET TB TB @TB (8.00900000D+01 <4> -4.77000000D+01 <4> 1.52410000D+02 <4> )
IDSET CASN (PROPERTIES) (37100 *6)
LSET CASN (%ID_NCC & %CASN)
DSET CASN CASN @CASN ( "71-43-2" "115-07-1" "98-82-8" )
IDSET PAMB (PROPERTIES) (32 *2)
LSET PAMB (%PAMB)
DSET PAMB PAMB @PAMB (1.01325000D+05)
IDSET PAMB2 (PROPERTIES) (32 *2 <20> )
LSET PAMB2 (%PAMB2)
DSET RUN-STATUS PAMB @PAMB2 (1.01325000D+00 <5> )
IDSET ISODES (PROPERTIES) (123 *5 124 *5 132 *5 1269 *5)
IDSET ISODESHW (PROPERTIES) (123 *5 124 *5 132 *5)
IDSET ISTRCV (PROPERTIES) (1251 *2)
IDSET ID_WORK (PROPERTIES) (112 *2 <19> 195 *2 <28> )
LSET L_WORK (%ISODESHW %ID_WORK)
IDSET ID_HEAT (PROPERTIES) (1 *2 <13> 815 *2 <22> 816 *2 <22> )
LSET L_HEAT (%ISODESHW %ID_HEAT)
IDSET ID_LTVC (PROPERTIES) (817 *2 <22> )
IDSET ID_LQVC (PROPERTIES) (818 *2 <13> )
IDSET ID_TPQV (PROPERTIES) (1 *2 <13> 31 *2 <22> 32 *2 <20> 2 *2 3 *2)
IDSET ID_QTP (PROPERTIES) (1 *2 <13> 31 *2 <22> 32 *2 <20> 3 *2)
IDSET TOTAL (PROPERTIES) (524 *2 <10> 525 *2 <10> 526 *2 <10> )
IDSET ENERGY (PROPERTIES) (504 *2 <13> 505 *2 <13> 506 *2 <13> 1 *2 <13> )
IDSET TOTAX (PROPERTIES) (524 *2 <18> 525 *2 <18> 526 *2 <18> )
IDSET ENERGX (PROPERTIES) (504 *2 <5> 505 *2 <5> 506 *2 <5> 1 *2 <5> )
LSET BPSBAL3 ( %TOTAL %ENERGY)
LSET BPBATCH ( %TOTAX %ENERGX)
IDSET ID_1 (NPOINT) (#1)
IDSET ID_2 (PROPERTIES) (263 *5 241 *2 41151 *2 256 *2 257 *6 126 *6 258 *5 )
LSET L_1 (%ID_2 & %ID_1)
DSET CONV-SUM TEAR-SUMMARY CNV_TEAR @L_1 ("RECYCLE" 9.96111321D-11
-1.68093985D-05 1.68093985D-01 "BENZENE MOLEFLOW" "#" "$OLVER01" )
DSET CONV-SUM TEAR-SUMMARY COMPSTAT @L_1 (0)
DSET RUN-STATUS FORSTAT @FORSTAT (2)
IDSET ID_3 (PROPERTIES) (131 *6 265 *1 266 *1 )
LSET L_2 (%ID_3)
DSET CONVERGENCE WEGSTEIN $OLVER01 OPT_STAT @L_2 ("OK" 8 * )
IDSET ID_4 (NPOINT) (#6)
IDSET ID_5 (PROPERTIES) (257 *6 262 *6 260 *2 261 *2 256 *2 126 *6 850 *1 263
*6 133 *5 339 *5 253 *5 347 *5 )
LSET L_3 (%ID_5 & %ID_4)
DSET CONVERGENCE WEGSTEIN $OLVER01 CONV_PLT @L_3 ("TOTAL MOLEFLOW" "KMOL/HR"
1.08438004D+00 1.08437204D+00 7.37848518D-02 "" 1 "RECYCLE" "MIXED" "" "" ""
"MOLE-FLOW" "KMOL/HR" 2.13329494D-02 2.13333080D-02 -1.68093985D-01 "" 2
"RECYCLE" "MIXED" "BENZENE" "" "" "MOLE-FLOW" "KMOL/HR" 1.03752875D+00
1.03752014D+00 8.30594594D-02 "" 3 "RECYCLE" "MIXED" "PROPYLEN" "" ""
"MOLE-FLOW" "KMOL/HR" 2.55183327D-02 2.55185906D-02 -1.01088303D-01 "" 4
"RECYCLE" "MIXED" "CUMENE" "" "" "PRESSURE" "BAR" 1.00000000D+00
1.00000000D+00 0.D0 "" 5 "RECYCLE" "MIXED" "" "" "" "MASS ENTHALPY" "KCAL/KG"
1.21589555D+02 1.21589822D+02 -2.20085618D-02 "" 6 "RECYCLE" "MIXED" "" "" ""
)
DSET CONVERGENCE WEGSTEIN $OLVER01 COMPSTAT @L_1 (0)
DSET CONVERGENCE WEGSTEIN $OLVER01 BLKSTAT @BLKSTAT (0 0)
IDSET ID_6 (NPOINT) (#8)
IDSET ID_7 (PROPERTIES) (222 *1 256 *2 263 *6 257 *6 850 *1 133 *5 339 *5
41140 *5 41141 *5 )
LSET L_4 (%ID_7 & %ID_6)
DSET CONVERGENCE WEGSTEIN $OLVER01 CONV_HIS_TS @L_4 (1 1.00000000D+06
"RECYCLE" "PRESSURE" 5 "MIXED" "" "" "" 2 4.59981924D+03 "RECYCLE" "MOLE-FLOW"
4 "MIXED" "CUMENE" "" "" 3 -1.96678018D+03 "RECYCLE" "MOLE-FLOW" 4 "MIXED"
"CUMENE" "" "" 4 3.22998108D+03 "RECYCLE" "MOLE-FLOW" 2 "MIXED" "BENZENE" ""
"" 5 4.09314728D+01 "RECYCLE" "MOLE-FLOW" 2 "MIXED" "BENZENE" "" "" 6
-1.72715627D+00 "RECYCLE" "MOLE-FLOW" 4 "MIXED" "CUMENE" "" "" 7
8.44167716D+00 "RECYCLE" "MOLE-FLOW" 4 "MIXED" "CUMENE" "" "" 8
-1.68093985D-01 "RECYCLE" "MOLE-FLOW" 2 "MIXED" "BENZENE" "" "" )
IDSET ID_8 (NPOINT) (#8)
IDSET ID_9 (NCOL) (#1)
IDSET ID_10 (PROPERTIES) (106 *6 107 *6 108 *6 109 *6 110 *6 111 *6 )
IDSET ID_11 (PROPERTIES) (260 *2)
IDSET ID_12 (PROPERTIES) (131 *1 )
LSET L_5 ((%ID_12 & %ID_8) (%ID_10 & %ID_9) (%ID_11 & %ID_9 & %ID_8) )
DSET CONVERGENCE WEGSTEIN $OLVER01 IHMXET @L_5 ( 1 1 1 1 1 1 1 1 "MAXIMUM"
"ERR/TOL" * * * * 1.00000000D+04 4.59981924D+03 -1.96678018D+03 3.22998108D+03
4.09314728D+01 -1.72715627D+00 8.44167716D+00 -1.68093985D-01 )
DSET FLWBAL @FLWBAL (1.89337678D+01 <3> 1.89337767D+01 <3> -1.89337684D+01 <3>
9.46688388D-01 9.46688837D-01 -1.00000000D+00 1.89337761D+01 <3>
2.00025575D-07 3.03616295D-04 <3> 1.26302306D-07 6.93648058D-01 <7>
1.26479575D+00)
DSET ALIAS @ALIAS ( "C6H6" "C3H6-2" "C9H12-2" )
IDSET ID_13 (NPOINT) (#3)
IDSET ID_14 (PROPERTIES) (339 *6 132 *5 1196 *6 1197 *6 1198 *6)
LSET L_6 (%ID_14 & %ID_13)
DSET COMPONENTS MAIN COMPS @L_6 ("BENZENE" C "C6H6" "C6H6" "BENZENE"
"PROPYLEN" C "C3H6-2" "C3H6-2" "PROPYLEN" "CUMENE" C "C9H12-2" "C9H12-2"
"CUMENE" )
IDSET ID_15 (PROPERTIES) (837 *1 182 *2 <22> 183 *2 <20> 184 *2 836 *2 1052 *2
<13> 173 *2 <31> 1165 *2 <31> 1166 *2 <31> )
IDSET ID_16 (PROPERTIES) (298 *2 <75> )
LSET L_7 (%ID_RXBAL %ID_TPQV %ID_15 %ID_KODE %ID_16)
DSET BLOCK HEATER COOL BLKSTAT @BLKSTAT (0 0)
DSET BLOCK HEATER COOL COMPSTAT @L1 (0)
DSET BLOCK HEATER COOL SYNCSTAT @L1 (0)
DSET BLOCK HEATER COOL BLKIN @BLKIN (1 REAC-OUT
"2bd01b45-48e2-4038-b191-ad81df689a13" * )
DSET BLOCK HEATER COOL TYPIN @TYPIN (1 MATERIAL)
DSET BLOCK HEATER COOL BLKOUT @BLKOUT (1 COOL-OUT
"2bd01b45-48e2-4038-b191-ad81df689a13" * )
DSET BLOCK HEATER COOL TYPOUT @TYPOUT (1 MATERIAL)
DSET BLOCK HEATER COOL RES_Q @L_7 (2.21506039D+01 <3> 2.21506039D+01 <3> 0.D0
<3> 0.D0 2.45227872D+03 <3> 2.45227872D+03 <3> * <3> 0.D0 * <3> * <3> * <3> *
2.21506039D+01 <3> 2.21506039D+01 <3> 0.D0 <3> 0.D0 2.45227872D+03 <3>
2.45227872D+03 <3> * <3> 0.D0 5.54311049D-01 <7> -1.39336927D-01 <7> * <7>
1.25136956D+00 0.D0 <3> 0.D0 <3> 0.D0 <3> 0.D0 <3> 0.D0 <3> -6.93647976D-01 <7>
5.00000000D+01 <4> 9.95000000D-01 <5> 4.92152714D-02 1.00000000D+00 1 * <4>
1.00000000D+00 <5> * * -6.93647976D-01 <7> * <4> * <4> * <4> 11 5.00000000D-03
<5> )
IDSET ID_17 (PROPERTIES) (1051 *2 )
LSET L_8 (%ID_17 )
DSET BLOCK HEATER COOL HTR_RES @L_8 ( *)
DSET BLOCK HEATER COOL VLE @VLE ( 4.90986697D-02 5.06176645D-02 1.97533660D-02
3.90246492D-01 9.49749281D-02 5.03736346D-02 9.56622697D-01 1.89905435D+01
8.55926402D-01 8.99008701D-01 2.36239370D-02 2.62777623D-02 )
IDSET ID_18 (PROPERTIES) (1052 *2 <13> )
LSET L_9 (%ID_RXBAL %ID_TPQV %ID_18 %ID_KODE )
DSET BLOCK RSTOIC REACTOR BLKSTAT @BLKSTAT (0 0)
DSET BLOCK RSTOIC REACTOR COMPSTAT @L1 (0)
DSET BLOCK RSTOIC REACTOR SYNCSTAT @L1 (0)
DSET BLOCK RSTOIC REACTOR BLKIN @BLKIN (2 FEED RECYCLE
"4c3721c9-8f73-43a8-ac60-5a4d8305e677" * * )
DSET BLOCK RSTOIC REACTOR TYPIN @TYPIN (2 MATERIAL MATERIAL)
DSET BLOCK RSTOIC REACTOR BLKOUT @BLKOUT (1 REAC-OUT
"4c3721c9-8f73-43a8-ac60-5a4d8305e677" * )
DSET BLOCK RSTOIC REACTOR TYPOUT @TYPOUT (1 MATERIAL)
DSET BLOCK RSTOIC REACTOR RES_Q @L_9 (4.10843720D+01 <3> 2.21506039D+01 <3>
-1.89337681D+01 <3> -1.72947206D-16 2.45227872D+03 <3> 2.45227872D+03 <3> * <3>
1.85438689D-16 * <3> * <3> * <3> * 4.10843720D+01 <3> 2.21506039D+01 <3>
-1.89337681D+01 <3> -1.72947206D-16 2.45227872D+03 <3> 2.45227872D+03 <3> * <3>
1.85438689D-16 5.54311049D-01 <7> 5.54311049D-01 <7> * <7> 0.D0 0.D0 <3> 0.D0
<3> 0.D0 <3> 0.D0 <3> 0.D0 <3> 0.D0 <7> 4.55447707D+02 <4> 1.00000000D+00 <5>
1.00000000D+00 * 0.D0 <7> 10)
IDSET ID_19 (NPOINTS) ( #1)
IDSET ID_20 (PROPERTIES) (602 *5)
LSET L_10 ( %ID_20 & %ID_19)
DSET BLOCK RSTOIC REACTOR REAC_IDS @L_10 ( 1 )
IDSET ID_21 (PROPERTIES) (1060 *2 <11> )
LSET L_11 ( %ID_21 & %ID_19)
DSET BLOCK RSTOIC REACTOR REAC_PRF @L_11 ( 1.89337681D+01 <3> )
IDSET ID_22 (PROPERTIES) (131 *6 )
LSET L_12 ( %ID_22 & %ID_19)
DSET BLOCK RSTOIC REACTOR RXN_STOI @L_12 (
"BENZENE + PROPYLEN --> CUMENE"
)
IDSET ID_23 (CONV_NO) (1 )
IDSET ID_24 (RSUBSTRM) (MIXED )
IDSET ID_25 (RXN_NO) (1 )
IDSET ID_26 (PROPERTIES) (7001 *2 <22> 7002 *2 <20> 7003 *2 62 *2 <13> 31 *2
<22> 32 *2 <20> 298 *2 <75> )
IDSET ID_27 (PROPERTIES) (14005 *2 <6> )
IDSET ID_28 (PROPERTIES) (537 *2)
IDSET ID_29 (PROPERTIES) (549 *2)
LSET L_13 ( %ID_26 (%ID_29 & %ID_23) (%ID_28 & %ID_24 & %ID_NCC & %ID_25)
)
DSET BLOCK RSTOIC REACTOR RST_INPT @L_13 ( * 0.D0 <5> * 0.D0 <7> * * 0.D0 <1>
9.00000000D-01 -1.00000000D+00 -1.00000000D+00 1.00000000D+00 )
IDSET ID_30 (PROPERTIES) (88 *2 <39> 61 *2 <39> 89 *2 <39> 90 *2 <39> 991 *2
<7> 992 *2 <7> 993 *2 <7> 994 *2 <7> 926 *2 <37> 925 *2 <37> 995 *2 <37> 996
*2 <37> 928 *2 927 *2 997 *2 998 *2 2 *2 3 *2 31 *2 <22> )
IDSET ID_31 (PROPERTIES) (39 *2 36 *2 37 *2 38 *2 )
LSET L_14 ( %ID_30 %ID_NCCNS & %ID_31 )
DSET BLOCK RSTOIC REACTOR R1_DPLS @L_14 ( 1.34920178D+01 <4> * <4> * <4> * <4>
-3.01501220D+01 <3> * <3> * <3> * <3> 3.29861157D-02 <1> * <1> * <1> * <1>
5.96888452D+01 * * * 1.00000000D+00 1.00000000D+00 9.67825185D+01 <4>
4.87322364D-01 5.12056509D-01 6.21126462D-04 9.65814036D-01 1.98171219D-02
1.43688424D-02 9.65814036D-01 1.98171219D-02 1.43688424D-02 4.87322364D-01
5.12056509D-01 6.21126462D-04 )
DSET BLOCK RSTOIC REACTOR VLE @VLE ( 4.90986697D-02 4.90986697D-02
4.90986697D-02 * 9.49749281D-02 9.49749281D-02 9.49749281D-02 * 8.55926402D-01
8.55926402D-01 8.55926402D-01 * )
IDSET ID_32 (PROPERTIES) (1052 *2 <13> )
IDSET ID_33 (PROPERTIES) (298 *2 <75> )
IDSET ID_34 (PROPERTIES) (7007 *2 )
LSET L_15 (%ID_RXBAL %ID_TPQV %ID_32 %ID_KODE %ID_33 %ID_34)
DSET BLOCK FLASH2 SEP BLKSTAT @BLKSTAT (0 0)
DSET BLOCK FLASH2 SEP COMPSTAT @L1 (0)
DSET BLOCK FLASH2 SEP SYNCSTAT @L1 (0)
DSET BLOCK FLASH2 SEP BLKIN @BLKIN (1 COOL-OUT
"58f6ee0b-42ef-4893-b720-3a49ad9c3bca" * )
DSET BLOCK FLASH2 SEP TYPIN @TYPIN (1 MATERIAL)
DSET BLOCK FLASH2 SEP BLKOUT @BLKOUT (2 RECYCLE PRODUCT
"58f6ee0b-42ef-4893-b720-3a49ad9c3bca" * * )
DSET BLOCK FLASH2 SEP TYPOUT @TYPOUT (2 MATERIAL MATERIAL)
DSET BLOCK FLASH2 SEP RES_Q @L_15 (2.21506039D+01 <3> 2.21505959D+01 <3> 0.D0
<3> 3.61210151D-07 2.45227872D+03 <3> 2.45227842D+03 <3> * <3> 1.23809864D-07
* <3> * <3> * <3> * 2.21506039D+01 <3> 2.21505959D+01 <3> 0.D0 <3>
3.61210151D-07 2.45227872D+03 <3> 2.45227842D+03 <3> * <3> 1.23809864D-07
-1.39336927D-01 <7> -1.39337009D-01 <7> * <7> 5.88498349D-07 0.D0 <3> 0.D0 <3>
0.D0 <3> 0.D0 <3> 0.D0 <3> 0.D0 <7> 5.00228560D+01 <4> 1.00000000D+00 <5>
4.89548746D-02 1.00000000D+00 0.D0 <7> 10 -5.00000000D-03 <5> 1.97340643D-02)
IDSET ID_35 (PROPERTIES) (1 *2 <13> 31 *2 <22> 32 *2 <20> 2 *2 7001 *2 <22>
7002 *2 <20> 899 *2 )
LSET L_16 ( %ID_35 )
DSET BLOCK FLASH2 SEP FLS2_INR @L_16 ( 0.D0 <1> * <1> 1.00000000D+05 <1> * *
<1> * <1> 0.D0 )
DSET BLOCK FLASH2 SEP VLE @VLE ( 4.90986697D-02 5.06133535D-02 1.96729455D-02
3.88689311D-01 9.49749281D-02 5.06129274D-02 9.56794407D-01 1.89040776D+01
8.55926402D-01 8.98773719D-01 2.35326471D-02 2.61829597D-02 )
IDSET ID_36 (PROPERTIES) (7001 *2 <22> 7002 *2 <20> 8103 *2 <10> 204 *2 <12>
8101 *2 <11> 7003 *2 )
LSET L_17 ( %ID_36 )
IDSET ID_37 (PROPERTIES) (253 *2)
IDSET ID_38 (PROPERTIES) (253 *2 <11> )
IDSET ID_39 (PROPERTIES) (253 *2 <12> )
IDSET ID_40 (PROPERTIES) (253 *2 <17> )
IDSET ID_41 (PROPERTIES) (253 *2 <27> )
IDSET ID_42 (PROPERTIES) (253 *2 <59> )
IDSET ID_43 (PROPERTIES) (253 *2 <10> )
IDSET ID_44 (PROPERTIES) (8101 *2 <11> 8002 *2 8103 *2 <10> 8004 *2 )
IDSET ID_45 (PROPERTIES) (8001 *2 <11> 8003 *2 <10> 8010 *2 <12> 7001 *2 <22>
7002 *2 <20> 7003 *2 7004 *2 7006 *2 2002 *2 <39> 41142 *2 <40> 41143 *2 <13>
2003 *2 <41> 41144 *2 <42> 11006 *2 <37> 41145 *2 <38> 11007 *2 8005 *2 <12> )
LSET L_18 ( %ISODES (( %ID_NCCNS & %ID_44 %ID_45) & %IDS_1) )
DSET STREAM MATERIAL COOL-OUT BLKSTAT @BLKSTAT (0 0)
DSET STREAM MATERIAL COOL-OUT COMPSTAT @L1 (0)
DSET STREAM MATERIAL COOL-OUT STR_MAIN @L_18 (COOL SEP MIXED SRK
1.08756518D+00 <3> 2.10375201D+00 <3> 1.89592867D+01 <3> 4.90986697D-02
9.49749281D-02 8.55926402D-01 8.49536753D+01 <3> 8.85272311D+01 <3>
2.27879782D+03 <3> 3.46427486D-02 3.60999875D-02 9.29257264D-01 2.21506039D+01
<3> 2.45227872D+03 <3> 3.19634195D+01 <7> 5.00000000D+01 <4> 9.95000000D-01 <5>
4.92152714D-02 9.50784729D-01 0.D0 -6.29043467D+00 <4> -5.68193679D+01 <4>
-1.39336927D-01 <7> -1.16311889D+02 <3> -1.05060593D+00 <3> 6.92998568D-01 <1>
7.67214135D+01 <1> 1.10709339D+02 2.90278318D+00 <7> )
DSET STREAM MATERIAL COOL-OUT RES_STR @L_17 (5.00000000D+01 <4> 9.95000000D-01
<5> 2.45227872D+03 <3> 3.19634195D+01 <7> 2.21506039D+01 <3> 4.92152714D-02 )
DSET STREAM MATERIAL FEED BLKSTAT @BLKSTAT (0 0)
DSET STREAM MATERIAL FEED COMPSTAT @L1 (0)
DSET STREAM MATERIAL FEED STR_MAIN @L_18 (* REACTOR VAPOR SRK 2.00000000D+01
<3> 2.00000000D+01 <3> 0.D0 <3> 5.00000000D-01 5.00000000D-01 0.D0
1.56227280D+03 <3> 8.41612800D+02 <3> 0.D0 <3> 6.49894820D-01 3.50105180D-01
0.D0 4.00000000D+01 <3> 2.40388560D+03 <3> 4.78469460D+02 <7> 1.00000000D+02
<4> 2.50000000D+00 <5> 1.00000000D+00 0.D0 0.D0 1.37106735D+01 <4>
2.28141863D+02 <4> 5.48426938D-01 <7> -3.18607013D+01 <3> -5.30153371D-01 <3>
8.35999021D-02 <1> 5.02411502D+00 <1> 6.00971400D+01 3.38731400D+00 <7> )
DSET STREAM MATERIAL FEED RES_STR @L_17 (1.00000000D+02 <4> 2.50000000D+00 <5>
2.40388560D+03 <3> 4.78469460D+02 <7> 4.00000000D+01 <3> 1.00000000D+00 )
DSET STREAM MATERIAL PRODUCT BLKSTAT @BLKSTAT (0 0)
DSET STREAM MATERIAL PRODUCT COMPSTAT @L1 (0)
DSET STREAM MATERIAL PRODUCT STR_MAIN @L_18 (SEP * LIQUID SRK 1.06623224D+00
<3> 1.06622326D+00 <3> 1.89337684D+01 <3> 5.06133535D-02 5.06129274D-02
8.98773719D-01 8.32872810D+01 <3> 4.48673571D+01 <3> 2.27573066D+03 <3>
3.46469447D-02 1.86645166D-02 9.46688539D-01 2.10662239D+01 <3> 2.40388530D+03
<3> 2.88001436D+00 <7> 5.00228560D+01 <4> 1.00000000D+00 <5> 0.D0
1.00000000D+00 0.D0 -6.89355249D+00 <4> -6.04110023D+01 <4> -1.45221120D-01 <7>
-1.20547288D+02 <3> -1.05640488D+00 <3> 7.31462458D+00 <1> 8.34678231D+02 <1>
1.14110878D+02 2.81345547D+00 <7> )
DSET STREAM MATERIAL PRODUCT RES_STR @L_17 (5.00228560D+01 <4> 1.00000000D+00
<5> 2.40388530D+03 <3> 2.88001436D+00 <7> 2.10662239D+01 <3> 0.D0 )
DSET STREAM MATERIAL REAC-OUT BLKSTAT @BLKSTAT (0 0)
DSET STREAM MATERIAL REAC-OUT COMPSTAT @L1 (0)
DSET STREAM MATERIAL REAC-OUT STR_MAIN @L_18 (REACTOR COOL VAPOR SRK
1.08756518D+00 <3> 2.10375201D+00 <3> 1.89592867D+01 <3> 4.90986697D-02
9.49749281D-02 8.55926402D-01 8.49536753D+01 <3> 8.85272311D+01 <3>
2.27879782D+03 <3> 3.46427486D-02 3.60999875D-02 9.29257264D-01 2.21506039D+01
<3> 2.45227872D+03 <3> 1.33486238D+03 <7> 4.55447707D+02 <4> 1.00000000D+00 <5>
1.00000000D+00 0.D0 0.D0 2.50246472D+01 <4> 2.26039171D+02 <4> 5.54311049D-01
<7> -5.09356528D+01 <3> -4.60084517D-01 <3> 1.65939233D-02 <1> 1.83710229D+00
<1> 1.10709339D+02 2.90278318D+00 <7> )
DSET STREAM MATERIAL REAC-OUT RES_STR @L_17 (4.55447707D+02 <4> 1.00000000D+00
<5> 2.45227872D+03 <3> 1.33486238D+03 <7> 2.21506039D+01 <3> 1.00000000D+00 )
DSET STREAM MATERIAL RECYCLE BLKSTAT @BLKSTAT (0 0)
DSET STREAM MATERIAL RECYCLE COMPSTAT @L1 (0)
DSET STREAM MATERIAL RECYCLE STR_MAIN @L_18 (SEP REACTOR VAPOR SRK
2.13333080D-02 <3> 1.03752014D+00 <3> 2.55185906D-02 <3> 1.96734214D-02
9.56793520D-01 2.35330586D-02 1.66642234D+00 <3> 4.36595114D+01 <3>
3.06718863D+00 <3> 3.44351069D-02 9.02184221D-01 6.33806723D-02 1.08437204D+00
<3> 4.83931223D+01 <3> 2.87857177D+01 <7> 5.00228560D+01 <4> 1.00000000D+00 <5>
1.00000000D+00 0.D0 0.D0 5.42628448D+00 <4> 1.21589822D+02 <4> 5.88411115D-03
<7> -3.40420822D+01 <3> -7.62800171D-01 <3> 3.76704880D-02 <1> 1.68115045D+00
<1> 4.46277853D+01 8.93270812D-02 <7> )
DSET STREAM MATERIAL RECYCLE RES_STR @L_17 (5.00228560D+01 <4> 1.00000000D+00
<5> 4.83931223D+01 <3> 2.87857177D+01 <7> 1.08437204D+00 <3> 1.00000000D+00 )
IDSET ID_46 (PROPERTIES) (757 *1)
IDSET ID_47 (PROPERTIES) (36 *2 37 *2 38 *2 39 *2 8103 *2 <10> )
LSET L_19 ( %ID_NCCNS & %ID_47 %ID_46)
DSET STREAM MATERIAL COOL-OUT STRM_XY @L_19 ( 5.06176645D-02 5.03736346D-02
8.99008701D-01 5.06176645D-02 5.03736346D-02 8.99008701D-01 4.90986697D-02
9.49749281D-02 8.55926402D-01 1.97533660D-02 9.56622697D-01 2.36239370D-02
8.49536753D+01 <3> 8.85272311D+01 <3> 2.27879782D+03 <3> * )
DSET STREAM MATERIAL FEED STRM_XY @L_19 ( 9.61723089D-01 3.82769106D-02 0.D0
9.61723089D-01 3.82769106D-02 0.D0 5.00000000D-01 5.00000000D-01 0.D0
5.00000000D-01 5.00000000D-01 0.D0 1.56227280D+03 <3> 8.41612800D+02 <3> 0.D0
<3> 0 )
DSET STREAM MATERIAL PRODUCT STRM_XY @L_19 ( 5.06133535D-02 5.06129274D-02
8.98773719D-01 5.06133535D-02 5.06129274D-02 8.98773719D-01 0.D0 0.D0 0.D0
0.D0 0.D0 0.D0 8.32872810D+01 <3> 4.48673571D+01 <3> 2.27573066D+03 <3> * )
DSET STREAM MATERIAL REAC-OUT STRM_XY @L_19 ( 4.90986697D-02 9.49749281D-02
8.55926402D-01 4.90986697D-02 9.49749281D-02 8.55926402D-01 4.90986697D-02
9.49749281D-02 8.55926402D-01 4.90986697D-02 9.49749281D-02 8.55926402D-01
8.49536753D+01 <3> 8.85272311D+01 <3> 2.27879782D+03 <3> * )
DSET STREAM MATERIAL RECYCLE STRM_XY @L_19 ( 5.06133535D-02 5.06129274D-02
8.98773719D-01 5.06133535D-02 5.06129274D-02 8.98773719D-01 1.96729455D-02
9.56794407D-01 2.35326471D-02 1.96734214D-02 9.56793520D-01 2.35330586D-02
1.66642234D+00 <3> 4.36595114D+01 <3> 3.06718863D+00 <3> * )
IDSET ID_48 (PROPERTIES) (64 *2 <11> 63 *2 <11> 94 *2 <11> 95 *2 <11> 88 *2
<39> 61 *2 <39> 89 *2 <39> 90 *2 <39> 991 *2 <7> 992 *2 <7> 993 *2 <7> 994 *2
<7> 926 *2 <37> 925 *2 <37> 995 *2 <37> 996 *2 <37> 928 *2 927 *2 997 *2 998
*2 2 *2 3 *2 606 *2 <11> 103 *2 <12> 269 *2 1246 *2 <10> 1247 *2 <10> 1248 *2
<12> 1249 *2 <12> 8010 *2 <12> 7007 *2 7008 *2 )
LSET L_20 ( %ID_48)
DSET STREAM MATERIAL COOL-OUT STR_PHAS @L_20 ( 1.09014798D+00 <3>
2.10604559D+01 <3> 2.10604559D+01 <3> 0.D0 <3> 5.42688730D+00 <4>
-6.89695597D+00 <4> -6.89695597D+00 <4> * <4> -3.40385781D+01 <3>
-1.20570585D+02 <3> -1.20570585D+02 <3> * <3> 3.74828087D-02 <1>
7.31399535D+00 <1> 7.31399535D+00 <1> * <1> 4.46377647D+01 1.14129388D+02
1.14129388D+02 * 4.92152714D-02 1.00000000D+00 2.21506039D+01 <3>
2.90278318D+00 <7> 1.10709339D+02 4.86617692D+01 <3> 2.40361695D+03 <3>
2.90839460D+01 <7> 2.87947352D+00 <7> 3.19634195D+01 <7> 1.98434904D-02 0.D0 )
DSET STREAM MATERIAL FEED STR_PHAS @L_20 ( 4.00000000D+01 <3> 0.D0 <3> 0.D0 <3>
0.D0 <3> 1.37106735D+01 <4> * <4> * <4> * <4> -3.18607013D+01 <3> * <3> * <3>
* <3> 8.35999021D-02 <1> * <1> * <1> * <1> 6.00971400D+01 * * * 1.00000000D+00
1.00000000D+00 4.00000000D+01 <3> 3.38731400D+00 <7> 6.00971400D+01
2.40388560D+03 <3> 0.D0 <3> 4.78469460D+02 <7> * <7> 4.78469460D+02 <7>
1.00000000D+00 0.D0 )
DSET STREAM MATERIAL PRODUCT STR_PHAS @L_20 ( 0.D0 <3> 2.10662239D+01 <3>
2.10662239D+01 <3> 0.D0 <3> * <4> -6.89355249D+00 <4> -6.89355249D+00 <4> * <4>
* <3> -1.20547288D+02 <3> -1.20547288D+02 <3> * <3> * <1> 7.31462458D+00 <1>
7.31462458D+00 <1> * <1> * 1.14110878D+02 1.14110878D+02 * 0.D0 1.00000000D+00
2.10662239D+01 <3> 2.81345547D+00 <7> 1.14110878D+02 0.D0 <3> 2.40388530D+03
<3> * <7> 2.88001436D+00 <7> 2.88001436D+00 <7> 0.D0 0.D0 )
DSET STREAM MATERIAL REAC-OUT STR_PHAS @L_20 ( 2.21506039D+01 <3> 0.D0 <3>
0.D0 <3> 0.D0 <3> 2.50246474D+01 <4> * <4> * <4> * <4> -5.09356528D+01 <3> *
<3> * <3> * <3> 1.65939233D-02 <1> * <1> * <1> * <1> 1.10709339D+02 * * *
1.00000000D+00 1.00000000D+00 2.21506039D+01 <3> 2.90278318D+00 <7>
1.10709339D+02 2.45227872D+03 <3> 0.D0 <3> 1.33486238D+03 <7> * <7>
1.33486238D+03 <7> 1.00000000D+00 0.D0 )
DSET STREAM MATERIAL RECYCLE STR_PHAS @L_20 ( 1.08437204D+00 <3> 0.D0 <3> 0.D0
<3> 0.D0 <3> 5.42626654D+00 <4> * <4> * <4> * <4> -3.40420446D+01 <3> * <3> *
<3> * <3> 3.76705296D-02 <1> * <1> * <1> * <1> 4.46277360D+01 * * *
1.00000000D+00 1.00000000D+00 1.08437204D+00 <3> 8.93270812D-02 <7>
4.46277853D+01 4.83930689D+01 <3> 0.D0 <3> 2.87856860D+01 <7> * <7>
2.87857177D+01 <7> 9.99998895D-01 0.D0 )
IDSET ID_49 (PROPERTIES) (8103 *2 <10> 1265 *2 <10> )
IDSET ID_50 (HIER-ID) ( PLANT )
IDSET ID_51 (STREAM-ID) ( FEED )
LSET L_21 ( %ID_50 & %ID_49 & %ID_51)
DSET UTIL-SUMMARY FEEDSUM @L_21 ( 2.40388560D+03 <3> 0.D0 <3> )
IDSET ID_52 (HIER-ID) ( PLANT )
IDSET ID_53 (STREAM-ID) ( PRODUCT )
LSET L_22 ( %ID_52 & %ID_49 & %ID_53)
DSET UTIL-SUMMARY PRODSUM @L_22 ( 2.40388530D+03 <3> 0.D0 <3> )
IDSET ID_54 (PROPERTIES) ( 1266 *2 <10> 1267 *2 <10> 1262 *2 <10> 1263 *2 <10>
1264 *2 <10> 1268 *2 <119> )
LSET L_23 ( %ID_54)
DSET UTIL-SUMMARY PLANTSUM @L_23 ( 0.D0 <3> 0.D0 <3> 0.D0 <3> 0.D0 <3> 0.D0 <3>
0.D0 <3> )
IDSET ID_55 (HIER-ID) ( PLANT )
LSET L_24 ( %ID_55 & %ID_54)
DSET UTIL-SUMMARY HIERSUM @L_24 ( 0.D0 <3> 0.D0 <3> 0.D0 <3> 0.D0 <3> 0.D0 <3>
0.D0 <3> )
IDSET RSTAT (PROPERTIES) (739 *1)
LSET RSTAT ( %RSTAT)
DSET RUN-STATUS RPTSTAT @RSTAT (0)
IDSET ID_56 (PROPERTIES) (7002 *2 <20> )
IDSET ID_57 ( PROPERTIES, COMPONENTS) (8002 *2 , "BENZENE" )
IDSET ID_58 ( PROPERTIES, PHASE) (7001 *2 <22> , TOTAL )
IDSET ID_59 ( PROPERTIES, PHASE, COMPONENTS) (6001 *2 , TOTAL , "BENZENE"
6001 *2 , TOTAL , "PROPYLEN" 2010 *2 , LIQUID1 , "BENZENE" 2010 *2 , LIQUID1 ,
"PROPYLEN" 2010 *2 , LIQUID2 , "BENZENE" 2010 *2 , LIQUID2 , "PROPYLEN" 6002
*2 , TOTAL , "BENZENE" 6002 *2 , TOTAL , "PROPYLEN" )
IDSET ID_60 ( PROPERTIES, PHASE) (7005 *2 , TOTAL )
IDSET ID_61 ( PROPERTIES, PHASE, COMPONENTS) (8002 *2 , VAPOR , "BENZENE"
8002 *2 , VAPOR , "PROPYLEN" 8002 *2 , LIQUID1 , "BENZENE" 8002 *2 , LIQUID1 ,
"PROPYLEN" 8002 *2 , LIQUID2 , "BENZENE" 8002 *2 , LIQUID2 , "PROPYLEN" )
IDSET ID_62 (NPOINT) ( #11)
LSET L_25 ((%IDERR %ID_56 %ID_57 %ID_58 %ID_59 %ID_60 %ID_61) & %ID_62)
DSET PROP-TABLE FLASHCURVE BINRY-1 PROPTAB @L_25 (0 2.50000000D+00 <5> 0.D0
-2.58174037D+01 <4> 5.97226227D-03 9.99999987D-01 1.74853404D+00
1.00000000D+00 * * * * 1.00000000D+00 0.D0 1.00000000D+00 0.D0 1.00000000D+00
* * 0 2.50000000D+00 <5> 1.00000000D-01 -2.29812342D+01 <4> 6.17436399D-03
1.11042507D+00 1.49363825D+00 1.00816212D+00 * * * * 1.00000000D+00
6.17436393D-04 9.99382564D-01 1.00000000D-01 9.00000000D-01 * * 0
2.50000000D+00 <5> 2.00000000D-01 -2.00723837D+01 <4> 6.64255741D-03
1.24833936D+00 1.32786316D+00 1.02938628D+00 * * * * 1.00000000D+00
1.32851148D-03 9.98671489D-01 2.00000000D-01 8.00000000D-01 * * 0
2.50000000D+00 <5> 3.00000000D-01 -1.68609136D+01 <4> 7.46708324D-03
1.42537125D+00 1.21612199D+00 1.06032127D+00 * * * * 1.00000000D+00
2.24012498D-03 9.97759875D-01 3.00000000D-01 7.00000000D-01 * * 0
2.50000000D+00 <5> 4.00000000D-01 -1.30796184D+01 <4> 8.83892060D-03
1.66077404D+00 1.13926255D+00 1.09892872D+00 * * * * 1.00000000D+00
3.53556769D-03 9.96464432D-01 4.00000000D-01 6.00000000D-01 * * 0
2.50000000D+00 <5> 5.00000000D-01 -8.35904588D+00 <4> 1.11652741D-02
1.98883472D+00 1.08607868D+00 1.14400040D+00 * * * * 1.00000000D+00
5.58263634D-03 9.94417364D-01 5.00000000D-01 5.00000000D-01 * * 0
2.50000000D+00 <5> 6.00000000D-01 -2.10011628D+00 <4> 1.54052276D-02
2.47689215D+00 1.04963362D+00 1.19504302D+00 * * * * 1.00000000D+00
9.24313522D-03 9.90756865D-01 6.00000000D-01 4.00000000D-01 * * 0
2.50000000D+00 <5> 7.00000000D-01 6.83799097D+00 <4> 2.42501019D-02
3.27674974D+00 1.02542637D+00 1.25266670D+00 * * * * 1.00000000D+00
1.69750677D-02 9.83024932D-01 7.00000000D-01 3.00000000D-01 * * 0
2.50000000D+00 <5> 8.00000000D-01 2.10957064D+01 <4> 4.77581581D-02
4.80896733D+00 1.01041393D+00 1.32085143D+00 * * * * 1.00000000D+00
3.82065124D-02 9.61793488D-01 8.00000000D-01 2.00000000D-01 * * 0
2.50000000D+00 <5> 9.00000000D-01 4.86355773D+01 <4> 1.47878791D-01
8.66909088D+00 1.00245545D+00 1.42562812D+00 * * * * 1.00000000D+00
1.33090912D-01 8.66909088D-01 9.00000000D-01 1.00000000D-01 * * 0
2.50000000D+00 <5> 1.00000000D+00 1.12767466D+02 <4> 9.99999798D-01
2.11287127D+01 1.00000000D+00 1.60207613D+00 * * * * 1.00000000D+00
1.00000000D+00 0.D0 1.00000000D+00 0.D0 * * )
DSET PROP-TABLE FLASHCURVE BINRY-1 COMPSTAT @L_1 (0)
IDSET ID_63 (PROPERTIES) (7001 *2 <22> 7002 *2 <20> )
IDSET ID_64 ( PROPERTIES, PHASE, COMPONENTS) (1013 *2 <20> , LIQUID ,
"BENZENE" )
IDSET ID_65 (NPOINT) ( #3)
LSET L_26 ((%IDERR %ID_63 %ID_64) & %ID_65)
DSET PROP-TABLE PROPS PURE-1 PROPTAB @L_26 (0 9.50000000D+01 <4>
1.01325000D+00 <5> 1.55965952D+00 <5> 0 1.00000000D+02 <4> 1.01325000D+00 <5>
1.79027565D+00 <5> 0 1.05000000D+02 <4> 1.01325000D+00 <5> 2.04656128D+00 <5>
)
DSET PROP-TABLE PROPS PURE-1 COMPSTAT @L_1 (0)
DSET RUN-STATUS PPSTAT @PPSTAT (0)
DSET RUN-STATUS OLDSTAT @STATUS ( 0 0 0 2 0 0 )
DSET RUN-STATUS STATUS @STATUS ( 8 * * * * * )
DSET RUN-STATUS COMPSTAT @L_1 (0)
IDSET TSTAT (PROPERTIES) (741 *1)
LSET TSTAT ( %TSTAT)
DSET RUN-STATUS TOTSTAT @TSTAT (0)
DSET SPSTAT @SPSTAT (0)
$_ADS_FILE
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