FSD100MbP?h㈵>d dfffffr@`y}!added material template default initializing document Rwarning: at least one compound needs to be present for materials of type default inserted stream 1 $added property activityCoefficient +added property activityCoefficient.Dmoles 1added property activityCoefficient.DmolFraction .added property activityCoefficient.Dpressure 1added property activityCoefficient.Dtemperature added property density added property density.Dmoles %added property density.DmolFraction "added property density.Dpressure %added property density.Dtemperature added property enthalpy  added property enthalpy.Dmoles &added property enthalpy.DmolFraction #added property enthalpy.Dpressure &added property enthalpy.Dtemperature added property entropy added property entropy.Dmoles %added property entropy.DmolFraction "added property entropy.Dpressure %added property entropy.Dtemperature added property excessEnthalpy &added property excessEnthalpy.Dmoles ,added property excessEnthalpy.DmolFraction )added property excessEnthalpy.Dpressure ,added property excessEnthalpy.Dtemperature added property heatCapacity $added property heatCapacity.Dmoles *added property heatCapacity.DmolFraction 'added property heatCapacity.Dpressure *added property heatCapacity.Dtemperature #added property heatOfVaporization *added property heatOfVaporization.Dmoles 0added property heatOfVaporization.DmolFraction -added property heatOfVaporization.Dpressure 0added property heatOfVaporization.Dtemperature 'added property logFugacityCoefficient .added property logFugacityCoefficient.Dmoles 4added property logFugacityCoefficient.DmolFraction 1added property logFugacityCoefficient.Dpressure 4added property logFugacityCoefficient.Dtemperature added property surfaceTension &added property surfaceTension.Dmoles ,added property surfaceTension.DmolFraction )added property surfaceTension.Dpressure ,added property surfaceTension.Dtemperature $added property thermalConductivity +added property thermalConductivity.Dmoles 1added property thermalConductivity.DmolFraction .added property thermalConductivity.Dpressure 1added property thermalConductivity.Dtemperature added property vaporPressure +added property vaporPressure.Dtemperature added property viscosity !added property viscosity.Dmoles 'added property viscosity.DmolFraction $added property viscosity.Dpressure 'added property viscosity.Dtemperature added property volume added property volume.Dmoles $added property volume.DmolFraction !added property volume.Dpressure $added property volume.Dtemperature 'added property bubblePointTemperature $added property bubblePointPressure $added property dewPointTemperature !added property dewPointPressure Rwarning: at least one compound needs to be present for materials of type default !(last message repeated 2 times) Starting solve Solve finished in 31ms %inserted unit operation ChemSepUO_1 ?warning: no route found for stream 1; using most direct route  (last message repeated 1 time) ?warning: no route found for stream 1; using most direct route  (last message repeated 1 time) ?warning: no route found for stream 1; using most direct route  (last message repeated 1 time) ?warning: no route found for stream 1; using most direct route Fconnected stream 1 to unit ChemSepUO_1 as INLET at port Feed1_stage5 inserted stream 2 Econnected stream 2 to unit ChemSepUO_1 as OUTLET at port TopProduct inserted stream 3 Hconnected stream 3 to unit ChemSepUO_1 as OUTLET at port BottomProduct Starting solve solving ChemSepUO_1 Solve finished in 2s, 781ms Starting solve solving ChemSepUO_1 Solve finished in 313ms Starting solve solving ChemSepUO_1 Solve finished in 328ms Starting solve solving ChemSepUO_1 Solve finished in 1s, 844ms Starting solve solving ChemSepUO_1 Solve finished in 2s, 47ms Starting solve solving ChemSepUO_1 Solve finished in 391ms %inserted unit operation ChemSepUO_2 Fconnected stream 3 to unit ChemSepUO_2 as INLET at port Feed1_stage5 inserted stream 4 Econnected stream 4 to unit ChemSepUO_2 as OUTLET at port TopProduct inserted stream 5 Hconnected stream 5 to unit ChemSepUO_2 as OUTLET at port BottomProduct Starting solve solving ChemSepUO_1 solving ChemSepUO_2 Solve finished in 2s, 766ms Starting solve solving ChemSepUO_1 solving ChemSepUO_2 Solve finished in 3s, 937ms Starting solve solving ChemSepUO_1 solving ChemSepUO_2 Solve finished in 1s, 63ms Starting solve solving ChemSepUO_1 solving ChemSepUO_2 Solve finished in 1s, 234ms Starting solve solving ChemSepUO_1 solving ChemSepUO_2 Solve finished in 906ms _Ex temperaturepressure compositionflow 0@V@B@fffffM@@Fpressure temperatureflow compositiondensityBTX-Antoine-UNIFACڐ@'t+,,BTX-Antoine-UNIFAC$Benzene / Toluene / p-Xylene exampleư>MbP?MbP?MbP?K2C:\Program Files\COCO\data\DefaultComponentLib.pcdABenzene-CHCHCHCHCHCH-C6H671-43-2c1ccccc13 `f@FRAMb?&?v@@jq@@jq@`8@KS@? ?`=C@Ǩ?A“A(AoAbbATS}Ar]@5*@6 8 8 8q@q@?@?`f@`? 8q@`f@i@V@`8C $@">@q@G@e@FA?п??q@`f@j@ '_)h@-2`*o?D@@3kq@d@6@@3$f6@ f`6f>@jq@@@ B@)@`)+`3j>i@p@h?)k2L@Qq@@h)8@ [@aվ@@jq@@e`>? @ A 8q@@@f-]?@ ?f`?;~o>q@y@H>:?zDc@@ 8@o@@@f@5^jTwx`IC>q@`f@@@@`I C?.Z@>I@@@d 8 8 8 8 8 8 8@35@B@D 8 8 u@`f@ `&5> 8 8@jq@@ |?5.[@@W;?Cl,f"-ܾ@@ @@33@@33@C?1L@ ? 8 8 8Y?h? 8j?@j>?Wʢ?pV@?&@ t@` A??PToluene (C6H5)CH3C7H8108-88-3 c1ccccc1(C)3 ~@pWOA X9?@`?w@Ef@Ef@U?  W@ [?@`?=@V9@x?ADA"AxAxPYAA@ #@`:? 8 8 8IW@Ef@U??~@.4? 8@3cd@`fn@i X@n&@i>@Ef@@3@eA@?෯?S@+0?Ef@ρ@j2Û@v^0 ?D@Ef@d@`H@%@@`?g|>@3Cf@@@ @̮E)@@)7>tUb@p@S:?dk`F@=o@@h@c @t6@.}@Ef@zw@e Z>_?=s@`f@ 8Ef@@@f +'7uqZ[`>Ef@}@`Xo> a?@ g@`@ 8zw@@@f43@mV 7|ϾEf@ρ@OV܂@ٿ \? 8i@p@ 8 8 8 8 8 8 8 /4@`f@N 8 85v@t@ N@]"? 8 8Ef@zw@ x#4@@33333ξ =DQOI?Zb#>@a@v@v@ ?w@>W? 8 8 8f?@? 84?f?E?`[@ [?"@-s@K\y?4?Z?XP-xylene CH3(C6H4)CH3C8H10106-42-3c1(C)ccc(C)cc1 A@lJA&1?t?zy@`q@`q@C@ Z@`๿?ज़?S=}@ ?bXA1qAA~A?QpA A`E$/@ ?S?A@ T? 8`q@A@i VX@ d&s>@ׯq@A@ew܊A/L? !?&kv?`q@A@jK̎@ @#MG? ~a)3@`q@d@vuA*@k`g>`fq@@w@L *@y>MRi@p@o@z d9@W`f.u@p@h7@3o@@@@Ͼ@`q@y@eOZ>`?`V"@ 8`fq@@fbE?)^@zn FY>`q@y@`>`C?@V|F@ 8t@@@f )l@5P@ `^?ټܾq@A@@p^@` l?.Vʢ>I@@@d 8 8 8 8 8 8 8 5@@`I 8 8@3#w@H@ kZa> 8 8`q@y@ e@ffffiFtϺF?J +6:vj$Ť@ף@Q @Q @h?„@v? 8 8 8@?? 8KP?ç??`@`๿?M@-ms@@ё?`I?activityCoefficientactivityCoefficientDdensitydensity enthalpyenthalpyentropyentropy:: excessEnthalpyexcessEnthalpy heatCapacityheatCapacityCpKK heatOfVaporizationheatOfVaporization logFugacityCoefficientlogFugacityCoefficientsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure))1 vaporPressure vaporPressure viscosity viscosity& viscosity (pure)viscosity (pure)" volumevolumeVapor Vapor phaseLiquid Liquid phase d`TR?Benzene/Toluene p282 1/7imported from NRTL.IPDjM?Benzene/pXylene p310 1/7imported from NRTL.IPDd`TR?Benzene/Toluene p282 1/7imported from NRTL.IPD7d?Toluene/pXylene p444 1/7imported from NRTL.IPDjM?Benzene/pXylene p310 1/7imported from NRTL.IPD7d?Toluene/pXylene p444 1/7imported from NRTL.IPDPkwBenzene/Toluene p285 1/7imported from VANLAAR.IPD cZBenzene/P-Xylene p310 1/7imported from VANLAAR.IPD rhBenzene/Toluene p285 1/7imported from VANLAAR.IPDj+Toluene/P-Xylene p444 1/7imported from VANLAAR.IPD'†WʢBenzene/P-Xylene p310 1/7imported from VANLAAR.IPDׁToluene/P-Xylene p444 1/7imported from VANLAAR.IPD 0*Benzene/Toluene p285 1/7imported from MARGULES.IPD/nBenzene/P-Xylene p310 1/7imported from MARGULES.IPD~jtBenzene/Toluene p285 1/7imported from MARGULES.IPD9#J?Toluene/P-Xylene p444 1/7imported from MARGULES.IPDZd;OBenzene/P-Xylene p310 1/7imported from MARGULES.IPD37ȿToluene/P-Xylene p444 1/7imported from MARGULES.IPD(g@Benzene/Toluene p301 1/7imported from WILSON.IPDp_3Benzene/P-Xylene p310 1/7imported from WILSON.IPDC)XfBenzene/Toluene p301 1/7imported from WILSON.IPDȬ*`NToluene/P-Xylene p444 1/7imported from WILSON.IPDC@Benzene/P-Xylene p310 1/7imported from WILSON.IPDm\M@Toluene/P-Xylene p444 1/7imported from WILSON.IPD"P>@Benzene/Toluene p282 1/7imported from NRTL.IPD"nzO9Benzene/pXylene p310 1/7imported from NRTL.IPD%D9Benzene/Toluene p282 1/7imported from NRTL.IPDB\@Toluene/pXylene p444 1/7imported from NRTL.IPDa@Benzene/pXylene p310 1/7imported from NRTL.IPD֨Cn^Toluene/pXylene p444 1/7imported from NRTL.IPD ?nkA@Benzene/Toluene p282 1/7imported from UNIQUAC.IPD1T?@Benzene/pXylene p310 1/7imported from UNIQUAC.IPDw$j-[=Benzene/Toluene p282 1/7imported from UNIQUAC.IPD7WMHN@Toluene/pXylene p444 1/7imported from UNIQUAC.IPD]E]?Benzene/pXylene p310 1/7imported from UNIQUAC.IPD3;#NToluene/pXylene p444 1/7imported from UNIQUAC.IPD ?nkA@Benzene/Toluene p282 1/7imported from UNIQUAC.IPD1T?@Benzene/pXylene p310 1/7imported from UNIQUAC.IPDw$j-[=Benzene/Toluene p282 1/7imported from UNIQUAC.IPD7WMHN@Toluene/pXylene p444 1/7imported from UNIQUAC.IPD]E]?Benzene/pXylene p310 1/7imported from UNIQUAC.IPD3;#NToluene/pXylene p444 1/7imported from UNIQUAC.IPDACHACCH2ACHqh??K7 *@ACCH3B?`"?%C ;@d@YbACHACCH2ACHqh??K7 *@ACCH3B?`"?%C ;@d@Yb V瞯<BTX-Antoine-UNIFAC71-43-2BenzeneKS@BTX-Antoine-UNIFACBenzene108-88-3Toluene  W@BTX-Antoine-UNIFACToluene106-42-3P-xylene Z@BTX-Antoine-UNIFACP-xylene volume.Dmoles@@ logFugacityCoefficient.Dpressureenthalpy?volume.Dtemperature@@#logFugacityCoefficient.DtemperatureheatOfVaporization.Dmoles?excessEnthalpy.Dpressure?volume.DmolFraction@@thermalConductivity?#logFugacityCoefficient.DmolFractionheatOfVaporization.Dpressure?heatCapacity.Dtemperature?heatCapacity.DmolFraction? heatCapacity?entropy.Dmoles? activityCoefficient.DtemperaturesurfaceTension?logFugacityCoefficient.Dmoles / moldensity.Dpressure?@ activityCoefficient.DmolFractionthermalConductivity.Dpressure?density?@surfaceTension.Dtemperature?surfaceTension.DmolFraction?heatOfVaporization.Dtemperature?excessEnthalpy.Dmoles?activityCoefficient.Dpressureviscosity.Dtemperature??viscosity.Dpressure?surfaceTension.Dmoles? / molheatOfVaporization.DmolFraction?enthalpy.Dmoles?activityCoefficient.Dmoles / molviscosity.DmolFraction??thermalConductivity.Dmoles? / moldensity.Dmoles?@ / molvolume@@volume.Dpressure@@ viscosity??enthalpy.Dtemperature?surfaceTension.Dpressure?heatCapacity.Dmoles?excessEnthalpy.Dtemperature?enthalpy.DmolFraction?excessEnthalpy.DmolFraction?entropy.Dpressure?enthalpy.Dpressure?density.Dtemperature?@heatCapacity.Dpressure?entropy?density.DmolFraction?@activityCoefficientviscosity.Dmoles?? / molvaporPressure.Dtemperature? thermalConductivity.Dtemperature?excessEnthalpy?entropy.Dtemperature? thermalConductivity.DmolFraction?logFugacityCoefficientheatOfVaporization?entropy.DmolFraction?&{71F5AC07-65A1-4357-8F1B-A8CD58148763}Temperature profile?Pressure profile?Vapour Flow profile?Liquid Flow profile?TotalMassBalancePropertiesFraction? TotalFlowMass?BactivityCoefficientactivityCoefficient.Dmoles activityCoefficient.DmolFractionactivityCoefficient.Dpressure activityCoefficient.Dtemperaturedensitydensity.Dmolesdensity.DmolFractiondensity.Dpressuredensity.Dtemperatureenthalpyenthalpy.Dmolesenthalpy.DmolFractionenthalpy.Dpressureenthalpy.Dtemperatureentropyentropy.Dmolesentropy.DmolFractionentropy.Dpressureentropy.DtemperatureexcessEnthalpyexcessEnthalpy.DmolesexcessEnthalpy.DmolFractionexcessEnthalpy.DpressureexcessEnthalpy.Dtemperature heatCapacityheatCapacity.DmolesheatCapacity.DmolFractionheatCapacity.DpressureheatCapacity.DtemperatureheatOfVaporizationheatOfVaporization.DmolesheatOfVaporization.DmolFractionheatOfVaporization.DpressureheatOfVaporization.DtemperaturelogFugacityCoefficientlogFugacityCoefficient.Dmoles#logFugacityCoefficient.DmolFraction logFugacityCoefficient.Dpressure#logFugacityCoefficient.DtemperaturesurfaceTensionsurfaceTension.DmolessurfaceTension.DmolFractionsurfaceTension.DpressuresurfaceTension.DtemperaturethermalConductivitythermalConductivity.Dmoles thermalConductivity.DmolFractionthermalConductivity.Dpressure thermalConductivity.Dtemperature vaporPressurevaporPressure.Dtemperature viscosityviscosity.Dmolesviscosity.DmolFractionviscosity.Dpressureviscosity.Dtemperaturevolume volume.Dmolesvolume.DmolFractionvolume.Dpressurevolume.DtemperaturebubblePointTemperaturebubblePointPressuredewPointTemperaturedewPointPressureVaporBTX-Antoine-UNIFACVaporLiquidBTX-Antoine-UNIFACLiquid VaporLiquiddefaultdefault material templateBTX-Antoine-UNIFAC1 Gat least one compound needs to be present for materials of type default defaultм@fffffr@$@Kh/? 1ZGU?I?1ZGU?)pGJU?KqU?nД??1ZGU?I?1ZGU?)pGJU?KqU?nД?1ZGU?I?1ZGU?)pGJU?KqU?nД?fffffr@м@$@Kh/?22*3.*3**3  =_=_defaultм@faɰv@^ώ! @/L?Li?uj? ~ ?˘?ߦ?ybq9>"O(oo>_X?=?E*2?j?fiko?a @r>({g>?Hi?uj? ~ ?˘?ۦ?ybq9>O(oo>23,92,9,229  defaultм@7"8x@$@%T>?yKq?Ky/l?^R~W?JK~?%??압|$?@ô<։? :?"?>h?rZ?>3M,??Kq?zy/l?R~W?|K~?%?]압|$?24ERKEREER  ԑ`defaultм@9'w@$ @db?+?gR8Y~?d8?|P?Q K?9e1>4O?U]?9?;?:]?],)u?|*R7?k:??+?4O?25GRLGRGR defaultм@Yy@$ @%?Ĥo=[7=AZPuJ?hF?jcb?FB?h2g=˱=EIA[?*)/eW? _?NM+??o=N7=AZPuJ?hF?jcb?FB?2 ChemSepUO_1ChemSep Unit OperationqeWCXclCSUOd[ChemSep] Version=6.10 Name=C:\DOCUME~1\Harry\LOCALS~1\Temp\CS1A8.sep Title=ChemSep CO Unit Operation "ChemSepUO_1" [Cape-Open] unitname=ChemSepUO_1 CO_ID=CS1A8 3 components Benzene 71-43-2 78.1139984131 Mw Toluene 108-88-3 92.1409988403 Mw P-xylene 106-42-3 106.166999817 Mw 0 thermo exe=C:\Program Files\ChemSepL\bin\co-col2.exe mode=Unknown NoWarnings=FALSE [Paths] Device drivers path=c:\progra~1\chemsepl\bin\ Help and Info path=c:\progra~1\chemsepl\help\ Component data path=c:\progra~1\chemsepl\pcd\ Property data path=c:\progra~1\chemsepl\ipd\ Section data path=c:\progra~1\chemsepl\ild\ Executables path=C:\PROGRA~1\ChemSepL\bin\ Temporary path=WINTMPDIR Scripts path=c:\progra~1\chemsepl\bin\ [Units] Temperature=C Flow=mol/s Mass flow=kg/s Pressure=bar Heat=MW Enthalpy=kJ/kmol Entropy=J/kmol/K Fraction= Length=m 1/Length=1/m Area=m Volume=m3 Mass=kg Angle=rad Velocity=m/s Surface tension=N/m Density=kg/m3 Molar density=kmol/m3 Viscosity=N/m2.s Molecular weight=kg/kmol Heat capacity=J/kmol/K Thermal conductivity=J/s/m2/K Diffusivity=1e-8 m/s Interaction parameter=J/mol Time=s [Components] 3 36 501 Library Offset, Index, CAS=71-43-2 CID=Benzene Name=Benzene Lib=c:\progra~1\chemsepl\pcd\lite.pcd 40 502 Library Offset, Index, CAS=108-88-3 CID=Toluene Name=Toluene Lib=c:\progra~1\chemsepl\pcd\lite.pcd 47 507 Library Offset, Index, CAS=106-42-3 CID=P-xylene Name=P-xylene Lib=c:\progra~1\chemsepl\pcd\lite.pcd [Operation] 2 Operation Column 1 Operation kind Simple Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 20 Stages 1 Feed stages 0 Sidestream stages F=10 S= 0 Pumparound stages P= [Properties] [Thermodynamics] * K model * * Activity coefficient * * Wilson model * * UNIQUAC model * * Equation of State * * Cubic EOS * * Virial EOS * * Vapour pressure * [Enthalpy] * Enthalpy * 1 Enthalpy reference state Vapour 298.15 Enthalpy reference temperature 1 Formation enthalpies Excluded 298.15 Exergy surroundings temperature [Physical property models] 0 No Check T range * Cubic EOS * * Virial EOS * * Vapour model * * Liquid mixture density * * Liquid component density * * Vapour mixture viscosity * * Vapour mixture viscosity pressure correction * * Vapour component viscosity * * Liquid mixture viscosity * * Liquid component viscosity * Vapour mixture Cp * Vapour component Cp * Liquid mixture Cp * Liquid component Cp * Vapour mixture conductivity * * Vapour component conductivity * * Liquid mixture conductivity * * Liquid component conductivity * Mixture surface tension * * Component surface tension * * Vignes MS D-model * * D mixture model * * Vapour Diffusion Coefficients * [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 0 Column duty Qcolumn 2 First stage 19 Last stage [Efficiencies] 1 Default efficiency 0 Number [Pressures] 1 Column pressure Constant pressure 101325 Condenser pressure 101325 Top pressure * Pressure Drop * Bottom pressure [Feeds] 1 Number 1 Feed state T & p 10 Stage Feed1 298.15 Temperature 101325 Pressure 0 Vapour fraction 3 componentflows 0.0033496439031 Component 1 flow 0.0033496439031 Component 2 flow 0.00334974439342 Component 3 flow [Condenser] 1 Type Reflux ratio 2 Value Qcondenser * Type * * Initialization guess [Reboiler] 9 Type Fraction of combined feeds recovered 0.666667 Value Qreboiler * Type * * Initialization guess [Solve options] 3 Initialization Old Results 1 Method Newton's method 0.2 Flow Step limit 10 Temperature Step limit 1 Composition Step limit 0.000001 Accuracy 30 Maximum iterations 1 Iteration count & function vector 0 T/V/L profiles 0 X/Y profiles 0 Variable and function vectors 0 Jacobian 1 History Screen History file= 1 Feeds type Stage below 1 Interactive 0 Log thermodynamics 0 Log enthalpy/entropy 0 Log physical properties 0 Log timing 0 CO numeric differencing 0 Log from iteration 0 CS K-value 0 CS enthalpy 0 CS entropy 0 CS flash 0 CS activity coefficient 0 CS vapor pressuure 0 CS density 0 CS viscosity 0 CS thermal conductivity 0 CS heat capacity 0 CS surface tension 0 CS diffusivity [Programs] Temporary file=SCRATCH.TMP User program=CSW 8 DOS extender NT 1 Show windows Hidden [FlowSheet] 1 Dot Solid Dot Solid [CoCo] # Coco icon generated by ChemSep # Sizes WIDTH 14 HEIGHT 20 DEFHEIGHT 24 XGROW 4 YGROW 10 # column + Internals BODY 0 4 8 16 -1 4 LINE DASHED 0.5 8 7.5 8 LINE DASHED 0.5 12 7.5 12 # Total Condenser BODY 10 0 14 4 -1 -1 LINE 4 4 4 2 LINE ARROW 4 2 10 2 LINE 12 4 12 8 LINE ARROW 12 8 8 8 LINE THINLINE OARROW 14.2 -.2 9.8 4.2 LINE 12 8 14 8 CONNECTION 14 8 # Partial Reboiler BODY 10 16 14 20 -1 -1 LINE 4 16 4 18 LINE ARROW 4 18 10 18 LINE 12 16 12 12 LINE ARROW 12 12 8 12 LINE THINLINE OARROW 9.8 20.2 14.2 15.8 CONNECTION 12 20 CONNECTION 14 18 # Connections and free space for feeds and sidestreams VCONNECTION 0 8 12 VCONNECTION 8 9 11 FREESPACE 9 9 12 11 FREESPACE 13 9 14 11 [Settings] -1 -1 -1 0 Graph settings 1 Auto colors 1 Auto points 0.2 StringGrid5 2 8 Title Labels Stages Axis color Commands Box Labels box Import data StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 y1 x2 y2 StringGrid3 1 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage 0 Graph settings 0 1 StringGrid7 16 2 Title McCabe-Thiele diagram for Benzene - Toluene Xlabel X Benzene/(Benzene+Toluene) Ylabel Y Benzene/(Benzene+Toluene) X interval 0.2 Y interval 0.2 X min 0 X max 1 Y min 0 Y max 1 X tics 0 Y tics 0 Axis color Black Grid Off y Fractions Vertical Commands set label "ChemSep" at 1,0.02 right Stage numbers On StringGrid11 5 3 0 1 0 0.95 0.95 1.2 1 0 Use old results 1 Automatic 0 Keep sep-files 1 Restore original StringGrid1 1 6 StringGrid2 4 1 StringGrid3 1 1 None -1 -1 -1 21 Binary Phase Diagram T p x -1 -1 StringGrid1 3 5 -1 -1 -1 0 21 Ternary Phase Diagram T 0 1 1 StringGrid1 3 5 [End Settings] [End of Input] [Results] 1 Converged 0 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow 1 353.4806608 1.013250000E+05 3.349674050E-03 6.699348100E-03 2 353.7825487 1.013250000E+05 1.004902215E-02 6.678980694E-03 3 354.3033408 1.013250000E+05 1.002865474E-02 6.645534467E-03 4 355.1627101 1.013250000E+05 9.995208518E-03 6.594440418E-03 5 356.4879717 1.013250000E+05 9.944114468E-03 6.523761387E-03 6 358.3536945 1.013250000E+05 9.873435437E-03 6.436192997E-03 7 360.7321479 1.013250000E+05 9.785867047E-03 6.335150949E-03 8 363.5696808 1.013250000E+05 9.684824999E-03 6.214274676E-03 9 367.0138174 1.013250000E+05 9.563948726E-03 6.054906100E-03 10 371.4914514 1.013250000E+05 9.404580150E-03 2.008776237E-02 11 373.6685041 1.013250000E+05 1.338840422E-02 2.003320592E-02 12 376.3863910 1.013250000E+05 1.333384777E-02 1.999815719E-02 13 379.3386777 1.013250000E+05 1.329879904E-02 1.999523776E-02 14 382.1191756 1.013250000E+05 1.329587961E-02 2.002020397E-02 15 384.4356024 1.013250000E+05 1.332084582E-02 2.005517366E-02 16 386.2332372 1.013250000E+05 1.335581551E-02 2.007955174E-02 17 387.6850130 1.013250000E+05 1.338019359E-02 2.007375925E-02 18 389.1602958 1.013250000E+05 1.337440110E-02 2.001433225E-02 19 391.2540025 1.013250000E+05 1.331497410E-02 1.987522286E-02 20 394.7638112 1.013250000E+05 1.317586471E-02 6.699358149E-03 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 0.0000000E+00 0.0000000E+00 0.1553204E+05 -0.7391114E+05 2 0.0000000E+00 0.0000000E+00 0.1587342E+05 -0.7332462E+05 3 0.0000000E+00 0.0000000E+00 0.1640389E+05 -0.7249062E+05 4 0.0000000E+00 0.0000000E+00 0.1720613E+05 -0.7135156E+05 5 0.0000000E+00 0.0000000E+00 0.1835314E+05 -0.6990097E+05 6 0.0000000E+00 0.0000000E+00 0.1986570E+05 -0.6819343E+05 7 0.0000000E+00 0.0000000E+00 0.2168715E+05 -0.6627645E+05 8 0.0000000E+00 0.0000000E+00 0.2374948E+05 -0.6405926E+05 9 0.0000000E+00 0.0000000E+00 0.2612326E+05 -0.6129677E+05 10 0.0000000E+00 0.0000000E+00 0.2903451E+05 -0.5791663E+05 11 0.0000000E+00 0.0000000E+00 0.3060593E+05 -0.5690618E+05 12 0.0000000E+00 0.0000000E+00 0.3245639E+05 -0.5579668E+05 13 0.0000000E+00 0.0000000E+00 0.3427062E+05 -0.5477041E+05 14 0.0000000E+00 0.0000000E+00 0.3570339E+05 -0.5397394E+05 15 0.0000000E+00 0.0000000E+00 0.3659499E+05 -0.5343737E+05 16 0.0000000E+00 0.0000000E+00 0.3704500E+05 -0.5306718E+05 17 0.0000000E+00 0.0000000E+00 0.3733216E+05 -0.5267263E+05 18 0.0000000E+00 0.0000000E+00 0.3784291E+05 -0.5196620E+05 19 0.0000000E+00 0.0000000E+00 0.3907843E+05 -0.5057258E+05 20 0.0000000E+00 0.0000000E+00 0.4156437E+05 -0.4824530E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.7815964E+02 0.2694628E+01 0.8958915E-05 0.9862694E+05 0.1509155E-01 2 0.7823659E+02 0.2694979E+01 0.8962486E-05 0.9885846E+05 0.1512252E-01 3 0.7837174E+02 0.2695667E+01 0.8968510E-05 0.9926275E+05 0.1517618E-01 4 0.7860131E+02 0.2697021E+01 0.8978072E-05 0.9994333E+05 0.1526534E-01 5 0.7897097E+02 0.2699632E+01 0.8991905E-05 0.1010250E+06 0.1540422E-01 6 0.7952128E+02 0.2704291E+01 0.9009557E-05 0.1026098E+06 0.1560191E-01 7 0.8026342E+02 0.2711532E+01 0.9029266E-05 0.1047158E+06 0.1585498E-01 8 0.8117469E+02 0.2720915E+01 0.9049727E-05 0.1072867E+06 0.1614976E-01 9 0.8225311E+02 0.2731189E+01 0.9072057E-05 0.1103576E+06 0.1647962E-01 10 0.8359914E+02 0.2742426E+01 0.9096682E-05 0.1142357E+06 0.1685505E-01 11 0.8461136E+02 0.2759460E+01 0.9094095E-05 0.1168546E+06 0.1710689E-01 12 0.8598207E+02 0.2783915E+01 0.9084944E-05 0.1203513E+06 0.1743123E-01 13 0.8761185E+02 0.2814606E+01 0.9067340E-05 0.1244506E+06 0.1779662E-01 14 0.8928538E+02 0.2847498E+01 0.9043338E-05 0.1286094E+06 0.1815328E-01 15 0.9077810E+02 0.2877659E+01 0.9018002E-05 0.1322874E+06 0.1845788E-01 16 0.9197490E+02 0.2902028E+01 0.8995729E-05 0.1352266E+06 0.1869261E-01 17 0.9290663E+02 0.2920449E+01 0.8977874E-05 0.1375282E+06 0.1886582E-01 18 0.9372991E+02 0.2935159E+01 0.8962557E-05 0.1396042E+06 0.1900313E-01 19 0.9472772E+02 0.2950531E+01 0.8944196E-05 0.1421828E+06 0.1914076E-01 20 0.9634319E+02 0.2974169E+01 0.8910219E-05 0.1463671E+06 0.1931763E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.7823659E+02 0.8146922E+03 0.3159873E-03 0.1571142E+06 0.1261256E+00 0.2110477E-01 2 0.7843952E+02 0.8142924E+03 0.3150550E-03 0.1576192E+06 0.1259297E+00 0.2107178E-01 3 0.7878515E+02 0.8136066E+03 0.3134590E-03 0.1584811E+06 0.1255957E+00 0.2101506E-01 4 0.7934400E+02 0.8124852E+03 0.3108596E-03 0.1598796E+06 0.1250549E+00 0.2092205E-01 5 0.8018091E+02 0.8107796E+03 0.3069332E-03 0.1619849E+06 0.1242452E+00 0.2078001E-01 6 0.8131828E+02 0.8084231E+03 0.3015770E-03 0.1648636E+06 0.1231515E+00 0.2058308E-01 7 0.8272819E+02 0.8054874E+03 0.2950701E-03 0.1684433E+06 0.1218296E+00 0.2033769E-01 8 0.8441813E+02 0.8020785E+03 0.2878988E-03 0.1726989E+06 0.1203499E+00 0.2005480E-01 9 0.8656579E+02 0.7980781E+03 0.2802542E-03 0.1779919E+06 0.1186830E+00 0.1972760E-01 10 0.8944102E+02 0.7931020E+03 0.2718488E-03 0.1849827E+06 0.1166922E+00 0.1932342E-01 11 0.9036650E+02 0.7907025E+03 0.2666760E-03 0.1876107E+06 0.1157573E+00 0.1911667E-01 12 0.9145799E+02 0.7877440E+03 0.2603047E-03 0.1907847E+06 0.1146355E+00 0.1886179E-01 13 0.9257137E+02 0.7845710E+03 0.2534763E-03 0.1941131E+06 0.1134682E+00 0.1858875E-01 14 0.9356048E+02 0.7816162E+03 0.2471276E-03 0.1971507E+06 0.1124126E+00 0.1833509E-01 15 0.9435265E+02 0.7791780E+03 0.2419254E-03 0.1996302E+06 0.1115629E+00 0.1812643E-01 16 0.9497062E+02 0.7773043E+03 0.2380344E-03 0.2015618E+06 0.1109213E+00 0.1796680E-01 17 0.9551974E+02 0.7758147E+03 0.2352032E-03 0.2032076E+06 0.1104157E+00 0.1784083E-01 18 0.9618887E+02 0.7743411E+03 0.2329377E-03 0.2050704E+06 0.1099156E+00 0.1771754E-01 19 0.9727004E+02 0.7723104E+03 0.2306021E-03 0.2079456E+06 0.1092253E+00 0.1754836E-01 20 0.9909290E+02 0.7689806E+03 0.2275774E-03 0.2128148E+06 0.1081020E+00 0.1726832E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.996746379E+00 0.991261701E+00 0.981632708E+00 0.965292489E+00 0.939054190E+00 2 0.325341941E-02 0.873685548E-02 0.183600280E-01 0.346737735E-01 0.607971896E-01 3 0.201877157E-06 0.144388615E-05 0.726409564E-05 0.337370665E-04 0.148620595E-03 Component Mole fractions on stages: 6 to 10 1 0.900286980E+00 0.849087754E+00 0.789714129E+00 0.728781057E+00 0.671201474E+00 2 0.990996202E-01 0.148589434E+00 0.202371113E+00 0.247354670E+00 0.266551008E+00 3 0.613399869E-03 0.232281189E-02 0.791475784E-02 0.238642730E-01 0.622475177E-01 Component Mole fractions on stages: 11 to 15 1 0.606159942E+00 0.517975400E+00 0.413057113E+00 0.305460597E+00 0.210188788E+00 2 0.324471107E+00 0.403120138E+00 0.496767304E+00 0.592651942E+00 0.676777200E+00 3 0.693689511E-01 0.789044622E-01 0.901755826E-01 0.101887461E+00 0.113034012E+00 Component Mole fractions on stages: 16 to 20 1 0.135876659E+00 0.832729952E-01 0.484422361E-01 0.263189279E-01 0.126156562E-01 2 0.740078996E+00 0.778861404E+00 0.789828638E+00 0.762936985E+00 0.675167955E+00 3 0.124044345E+00 0.137865601E+00 0.161729126E+00 0.210744087E+00 0.312216389E+00 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.991261701E+00 0.976803530E+00 0.952202738E+00 0.912535163E+00 0.853575330E+00 2 0.873685548E-02 0.231862872E-01 0.477472474E-01 0.872414576E-01 0.145497057E+00 3 0.144388615E-05 0.101830747E-04 0.500144071E-04 0.223379630E-03 0.927613243E-03 Component Mole fractions on stages: 6 to 10 1 0.775094264E+00 0.683147029E+00 0.587296388E+00 0.494138871E+00 0.405458532E+00 2 0.221374784E+00 0.304754095E+00 0.375976583E+00 0.409178055E+00 0.381552135E+00 3 0.353095251E-02 0.120988764E-01 0.367270291E-01 0.966830737E-01 0.212989333E+00 Component Mole fractions on stages: 11 to 15 1 0.346217448E+00 0.276145637E+00 0.204579094E+00 0.141313882E+00 0.919455462E-01 2 0.434055381E+00 0.496385079E+00 0.560143735E+00 0.616158709E+00 0.658420467E+00 3 0.219727170E+00 0.227469285E+00 0.235277171E+00 0.242527409E+00 0.249633986E+00 Component Mole fractions on stages: 16 to 20 1 0.569459477E-01 0.337319081E-01 0.189702132E-01 0.983448023E-02 0.436464313E-02 2 0.684362621E+00 0.691642413E+00 0.673460614E+00 0.614649707E+00 0.495626329E+00 3 0.258691432E+00 0.274625678E+00 0.307569173E+00 0.375515812E+00 0.500009028E+00 [Reaction rates] Component reaction rates on stages: 1 to 5 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 6 to 10 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 11 to 15 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 Component reaction rates on stages: 16 to 20 1 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 3 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 0.000000000E+00 [Condenser Heat Duty] 0.000000000E+00 [Reboiler Heat Duty] 0.000000000E+00 [K-values] Component K-values on stages: 1 to 5 1 0.100553303E+01 0.101480151E+01 0.103090725E+01 0.105781402E+01 0.110014214E+01 2 0.372378760E+00 0.376811321E+00 0.384525371E+00 0.397446060E+00 0.417858552E+00 3 0.139815149E+00 0.141792749E+00 0.145240063E+00 0.151030184E+00 0.160218276E+00 Component K-values on stages: 6 to 10 1 0.116151934E+01 0.124290631E+01 0.134466029E+01 0.147485069E+01 0.165541337E+01 2 0.447655414E+00 0.487571577E+00 0.538254566E+00 0.604515971E+00 0.698596558E+00 3 0.173720793E+00 0.191985754E+00 0.215502261E+00 0.246829896E+00 0.292256503E+00 Component K-values on stages: 11 to 15 1 0.175080703E+01 0.187573270E+01 0.201905828E+01 0.216157529E+01 0.228601381E+01 2 0.747533886E+00 0.812111716E+00 0.886856843E+00 0.961849493E+00 0.102787996E+01 3 0.315704931E+00 0.346879634E+00 0.383273831E+00 0.420106995E+00 0.452798971E+00 Component K-values on stages: 16 to 20 1 0.238606370E+01 0.246867135E+01 0.255359471E+01 0.267618901E+01 0.289042099E+01 2 0.108141353E+01 0.112610417E+01 0.117279114E+01 0.124125494E+01 0.136225199E+01 3 0.479506972E+00 0.502012782E+00 0.525830090E+00 0.561212285E+00 0.624421502E+00 [Molecular weights] 1 78.114 2 92.141 3 106.167 [Feed stream 1] 10 Stage Number 1.0049032199620E-02 Flow rate 2.9815000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.8149898142423E+07 Enthalpy [J/kmol] -9.2154472164390E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 3.3333000000007E-01 Mole fraction of component 1 3.3333000000007E-01 Mole fraction of component 2 3.3333999999987E-01 Mole fraction of component 3 1.0049032199620E-02 Flow rate 3.3333000000007E-01 Mole fraction of component 1 3.3333000000007E-01 Mole fraction of component 2 3.3333999999987E-01 Mole fraction of component 3 9.2140805953443E+01 Molar mass 8.6452131801025E+02 Density 5.8636921825020E-04 Viscosity 1.3565310206886E-01 Thermal conductivity 1.5799446679648E+05 Heat capacity 2.7981923535284E-02 Surface tension [Top product] 1 Stage Number 3.3496740501959E-03 Flow rate 3.5348066080002E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] 0.0000000000000E+00 Enthalpy [J/kmol] -7.3911142178922E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9126170062963E-01 Mole fraction of component 1 8.7368554842207E-03 Mole fraction of component 2 1.4438861497889E-06 Mole fraction of component 3 3.3496740501959E-03 Flow rate 9.9126170062963E-01 Mole fraction of component 1 8.7368554842207E-03 Mole fraction of component 2 1.4438861497889E-06 Mole fraction of component 3 7.8236590794036E+01 Molar mass 8.1469222292582E+02 Density 3.1598731161590E-04 Viscosity 1.2612556848001E-01 Thermal conductivity 1.5711421237048E+05 Heat capacity 2.1104768530562E-02 Surface tension [Bottom product] 20 Stage Number 6.6993581494241E-03 Flow rate 3.9476381123892E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] 0.0000000000000E+00 Enthalpy [J/kmol] -4.8245301786307E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 4.3646431338139E-03 Mole fraction of component 1 4.9562632881325E-01 Mole fraction of component 2 5.0000902805293E-01 Mole fraction of component 3 6.6993581494241E-03 Flow rate 4.3646431338139E-03 Mole fraction of component 1 4.9562632881325E-01 Mole fraction of component 2 5.0000902805293E-01 Mole fraction of component 3 9.9092903104990E+01 Molar mass 7.6898058009068E+02 Density 2.2757737305462E-04 Viscosity 1.0810195035182E-01 Thermal conductivity 2.1281480439413E+05 Heat capacity 1.7268320153923E-02 Surface tension [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlash AutoDUseOnlyKValuesAndEnthalpyFromCOSE(TryUsingRestartData,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts(Temperature profile4Temperature at each stageaɰv@p Qv@{$v@u2v@iGv@gdev@\eඋv@Riv@8v@-$7w@Z1Zw@GT.w@'N9kw@$w@8:x@_#V#x@\1:x@*TRx@dtx@8x@"Pressure profile.Pressure at each stageм@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@(Vapour Flow profile4Vapour Flow at each stage7! @(fn$@Yի$@q#@{b#@9*2#@c*]#@``a^#@- #@!!%"@*@-K*@0*@A}*@?E*@Us-*@e*@@,@*@,ID*@s Z*@(Liquid Flow profile4Liquid Flow at each stage7!@a F@@*`@XJT@o`@t1W@j@TgM98@.