FSD100MbP?h㈵>d{ +dfffffr@м@ )Restoring flowsheet from file +Loaded FlowsheetingWithCOCOandChemSep.fsd Qx temperaturepressure compositionflow 0@Z@H@fffff&P@@Fpressure temperatureflow compositionQhttp://www.cocosimulator.org/down.php?dl=FlowsheetingWithCOCOandChemsep_Notes.pdfSlides with notes1@@Q@gfffff,@@ MyPackageAUwNA\t 44 MyPackageFor use in my simulationư>MbP?MbP?MbP?K%c:\werk\CO\COCO\bin\data\ChemSep1.pcdEthanolCH3CH2OHC2H6O64-17-5CCON \@sWAA`?Q?u@c@c@ =@?G@ N ??@& =@#9pZ?@bA `!AnRA 8&g8@$ 8 8 8 \O@c@??G@fI? 8c@@3@ip^@ v- Գ>@c@"@e+xAs?Mb`@@Uc@@3@j`f@|`Ε?`24@c@d@@ 1?x]c@x@@@VN(@{>Pb@p@9@?IAa1pp@@@h`; @6@¤2@i@{@e࠻>(?-S@@3 8i@@@f`y;?^ ߿@^}p>c@`fv@?( 8`fq@@@fw*3@hF?`fq@`fr@@@?#Cw>I@@@d 8 8 8 8 8 8 8v6@@3N 8 8Hs@@3|@ l@ F`w? 8 8i@{@ vOjS)%寿#~j|4@kD>@G@?p?`I?@S@#??@ݲ˿`I?`? :ё? 8c]?`I@ N ?ެp=@z@,(2?Q?#?y Diethyl ether CH3CH2OCH2CH3C4H10O60-29-7CCOCCz=@3+}@`KA ??p9s@@3c@@3c@O?@߇R@`к?`? =@x9@5^?@xA@{ dpA|m[A 8 +-@V 8 8 8`^O@@3c@z1?[Z?@3+}@v2? 8@3c@@3+}@i?W@L@^%_>@@3c@+}@eA#?bb? HP`U?@3c@@3+}@j@3E@@@`e1$?9@pc@dPA`@ 2s?^hpc@|@@Q8)@5A&?`*si@p@z1?pM`n4h@@@3+m@@3+@h+G$@N gD@i@`fRw@e@W>@>w?? KJƾ@3c@`f{@ er?tsU@ 8i@@f=ՠQ@ *g?@3c@@3+}@@@ {s@ÿ@ ?E(oY@@@d 8 8 8 8 8 8 8`d4@̹@VD 8 8`fq@zz@ `d@l'> 8 8i@`fRw@ c]KXfffffv@1dn`8@ Q"?@` @(@(@@7?`&U@@ͺ? 8 8?)?!V?`?N@?3W@`к?@}@v@ز#ܻn??@ͺ?ZWaterHOHH2O 7732-18-5OT9@ uAz?@O?`fRw@`fq@`q@@2@ ??=^@ I9@qU?AӬ`@ AVA 8{J@` 8 8 8$m@`fq@ J{?x?`f:@?Qa@3o@Q:@iX@Y%@ó>@`frp@Q:@eFpAO?| :? :`fq@=:@j)hp࣐a@MоI =@33 @`fq@d0q@@a@eпf'?q@@3@@/@`0;@@`3c?I@@@4?`6l2vG)@`fq@@@h`f`@@Qx2@`T@q@@ 9@e@r>?`ff@ 8`q@Đ@f}@ K? R?sq@@3Ƀ@`1>P? /M@> 8`q@Đ@fJ@d@l v?ϧp@8@@fA`? k !@6l>I@@@d 8 8 8 8 8 8 8f7@&@B 8 8tx@@3@ ZWt l> 8 8q@@ 9@ :#J{#Q@\yf8TBfm?w-! b=@p?`ff???`X@B?`i?8? AN?έ?`? ?Q8*@ ?@1(@8@y ?(?B?activityactivityDactivityCoefficientactivityCoefficientDdensitydensity enthalpyenthalpy enthalpyF enthalpyFentropyentropy!entropyFentropyF excessEnthalpyexcessEnthalpyfugacityfugacity;fugacityCoefficientfugacityCoefficient;gibbsFreeEnergy gibbsEnergyGG heatCapacityheatCapacityCpKK heatOfVaporizationheatOfVaporizationOidealGasEnthalpyidealGasEnthalpy logFugacityCoefficientlogFugacityCoefficient;molecularWeightmolecularWeightHHHsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure)RS vaporPressure vaporPressureN viscosity viscosity& viscosity (pure)viscosity (pure)" volumevolumeVapor Vapor phaseLiquid Liquid phase  гY?DiethylEther/Ethanol p347 1/2cimported from NRTL.IPDs? Ethanol/Waterimported from NRTL.IPDгY?DiethylEther/Ethanol p347 1/2cimported from NRTL.IPD0*D?Diethylether/Water p344 1/1aimported from NRTL.IPDs? Ethanol/Waterimported from NRTL.IPD0*D?Diethylether/Water p344 1/1aimported from NRTL.IPD ffffff?Ethanol/ethanolimported from HAYDENO.IPD?Di-ethyl ether/ethanolimported from HAYDENO.IPD? Water/ethanolimported from HAYDENO.IPD?Di-ethyl ether/ethanolimported from HAYDENO.IPD?Water/di-ethyl etherimported from HAYDENO.IPD? Water/ethanolimported from HAYDENO.IPD?Water/di-ethyl etherimported from HAYDENO.IPD333333? Water/waterimported from HAYDENO.IPD&S? Ethanol/Waterimported from VANLAAR.IPD@@Diethylether/Water p344 1/1aimported from VANLAAR.IPD_L? Ethanol/Waterimported from VANLAAR.IPDa+e?Diethylether/Water p344 1/1aimported from VANLAAR.IPD'? Ethanol/Waterimported from MARGULES.IPD h"lx:@Diethylether/Water p344 1/1imported from MARGULES.IPD†W2? Ethanol/Waterimported from MARGULES.IPDs@Diethylether/Water p344 1/1imported from MARGULES.IPD\u<)@DiethylEther/Ethanol p347 1/2cimported from WILSON.IPD ^Kh@ Ethanol/Waterimported from WILSON.IPD~ƂUPDiethylEther/Ethanol p347 1/2cimported from WILSON.IPD8aBF@Diethylether/Water p344 1/1aimported from WILSON.IPD:h"~@ Ethanol/Waterimported from WILSON.IPD)@Diethylether/Water p344 1/1aimported from WILSON.IPD?A@DiethylEther/Ethanol p347 1/2cimported from NRTL.IPDb/= Ethanol/Waterimported from NRTL.IPD.x@DiethylEther/Ethanol p347 1/2cimported from NRTL.IPD@6L@Diethylether/Water p344 1/1aimported from NRTL.IPD~|HG@ Ethanol/Waterimported from NRTL.IPD7& j@Diethylether/Water p344 1/1aimported from NRTL.IPD GUDiethylEther/Ethanol p347 1/2cimported from UNIQUAC.IPD&BG.U@ Ethanol/Waterimported from UNIQUAC.IPDh%:t@DiethylEther/Ethanol p347 1/2cimported from UNIQUAC.IPD6݂@Diethylether/Water p344 1/1aimported from UNIQUAC.IPDƅ7K@ Ethanol/Waterimported from UNIQUAC.IPDPI@Diethylether/Water p344 1/1aimported from UNIQUAC.IPD q= ף`fDi-Ethyl Ether/Ethanolimported from UNIQUACP.IPDfffffL@ Ethanol/Waterimported from UNIQUACP.IPD(\@Di-Ethyl Ether/Ethanolimported from UNIQUACP.IPD33333CS@ Ethanol/Waterimported from UNIQUACP.IPD{CH2OHCH2OH2OCH3ͪ?A`"? rh.@CH2M O?HzG?Zd;O ,@OH?333333?5^I 1@CH3ORQ? rh?bX9?@H2Oq= ףp?ffffff?jt2@CH2OmV}b?(\?->@Ԏ@po@@̌c@(\<@v@ףp= T@fffffm@33333sr@33333l@CH2OHH2OCH3ͪ?A`"? rh.@CH2M O?HzG?Zd;O ,@OH?333333?5^I 1@H2Oq= ףp?ffffff?jt2@$@P@33333t@{G<@ffffffu@^ V瞯< MyPackage Ethanol2EthylbKrx-[W Ethanol2Ethyl7Reaction definitions for the ethanol conversion reactor%c:\werk\CO\COCO\bin\data\ChemSep1.pcdEthanol64-17-5EthanolC2H6OG@ Diethyl ether60-29-7 Diethyl etherC4H10O@߇R@Water 7732-18-5WaterH2O2@ conversionLiquid?? Ethanol2Ethyl64-17-5EthanolG@u@C2H6O MyPackageEthanol60-29-7 Diethyl ether@߇R@p9s@C4H10O MyPackage Diethyl ether 7732-18-5Water2@`fRw@H2O MyPackageWater ????????????excessEnthalpy.Dpressure??thermalConductivity.Dmoles?? / molenthalpyF.DmolFraction??gibbsFreeEnergy.Dpressure??viscosity.Dtemperature????activityCoefficiententhalpyF.Dpressure??thermalConductivity.Dpressure?? thermalConductivity.Dtemperature??heatCapacity.DmolFraction??entropyF.Dmoles??heatOfVaporization??density.Dpressure?@?@enthalpy.Dmoles??molecularWeight#logFugacityCoefficient.DmolFractionentropy.Dtemperature??viscosity.Dmoles???? / mol volume.Dmoles@@@@vaporPressure.Dtemperature??enthalpy?? enthalpyF??activity.DmolFractionfugacity.Dtemperature??excessEnthalpy.Dtemperature??volume.Dpressure@@@@surfaceTension.DmolFraction?? activityCoefficient.DtemperaturefugacityCoefficient.Dmoles / molgibbsFreeEnergy??activity.Dmoles / molactivityCoefficient.Dmoles / molgibbsFreeEnergy.DmolFraction??enthalpy.DmolFraction??enthalpy.Dpressure??logFugacityCoefficientactivitymolecularWeight.Dtemperaturefugacity.Dpressure fugacityCoefficient.DmolFractiondensity?@?@volume.DmolFraction@@@@activity.DtemperatureenthalpyF.Dtemperature??entropyF.DmolFraction??thermalConductivity??surfaceTension.Dtemperature??density.DmolFraction?@?@surfaceTension??heatCapacity.Dtemperature??#logFugacityCoefficient.DtemperatureexcessEnthalpy??fugacityCoefficient.Dpressureviscosity.DmolFraction????enthalpy.Dtemperature??entropy.Dpressure??surfaceTension.Dmoles?? / molgibbsFreeEnergy.Dmoles??density.Dmoles?@?@ / mol thermalConductivity.DmolFraction??idealGasEnthalpy.Dtemperature??logFugacityCoefficient.Dmoles / molheatOfVaporization.Dtemperature??enthalpyF.Dmoles??surfaceTension.Dpressure??entropy.DmolFraction??entropyF.Dtemperature??entropy??entropyF??volume@@@@heatCapacity.Dpressure??molecularWeight.DpressuregibbsFreeEnergy.Dtemperature??fugacityCoefficientidealGasEnthalpy?? logFugacityCoefficient.Dpressureviscosity.Dpressure??entropy.Dmoles??entropyF.Dpressure?? fugacityCoefficient.Dtemperature heatCapacity??activityCoefficient.Dpressure activityCoefficient.DmolFraction viscosity????excessEnthalpy.Dmoles??volume.Dtemperature@@@@density.Dtemperature?@?@fugacity.Dmoles?? / molheatCapacity.Dmoles??activity.DpressuremolecularWeight.DmolFractionexcessEnthalpy.DmolFraction??molecularWeight.Dmoles / mol@&{603DF4B9-4F88-475D-A458-85F56125DA70} Pressure drop?? Temperature?? Heat duty??TotalMassBalancePropertiesFraction?? TotalFlowMass??&{71F5AC07-65A1-4357-8F1B-A8CD58148763}RelativePerturbationTemperature??RelativePerturbationPressure??PerturbationComposition??Temperature profile??Pressure profile??Vapour Flow profile??Liquid Flow profile??Duties profile??Vapour Density profile@?@?Vapour Viscosity profile????Vapour Heat capacity profile??#Vapour Thermal conductivity profile??Liquid Density profile@?@?Liquid Viscosity profile????Liquid Heat capacity profile??Liquid Thermal cond. profile??Surface tension profile??dheatOfVaporizationheatOfVaporization.DtemperatureidealGasEnthalpyidealGasEnthalpy.Dtemperature vaporPressurevaporPressure.Dtemperatureactivityactivity.Dmolesactivity.DmolFractionactivity.Dpressureactivity.DtemperatureactivityCoefficientactivityCoefficient.Dmoles activityCoefficient.DmolFractionactivityCoefficient.Dpressure activityCoefficient.Dtemperaturedensitydensity.Dmolesdensity.DmolFractiondensity.Dpressuredensity.Dtemperatureenthalpyenthalpy.Dmolesenthalpy.DmolFractionenthalpy.Dpressureenthalpy.Dtemperature enthalpyFenthalpyF.DmolesenthalpyF.DmolFractionenthalpyF.DpressureenthalpyF.Dtemperatureentropyentropy.Dmolesentropy.DmolFractionentropy.Dpressureentropy.DtemperatureentropyFentropyF.DmolesentropyF.DmolFractionentropyF.DpressureentropyF.DtemperatureexcessEnthalpyexcessEnthalpy.DmolesexcessEnthalpy.DmolFractionexcessEnthalpy.DpressureexcessEnthalpy.Dtemperaturefugacityfugacity.Dmolesfugacity.DmolFractionfugacity.Dpressurefugacity.DtemperaturefugacityCoefficientfugacityCoefficient.Dmoles fugacityCoefficient.DmolFractionfugacityCoefficient.Dpressure fugacityCoefficient.DtemperaturegibbsFreeEnergygibbsFreeEnergy.DmolesgibbsFreeEnergy.DmolFractiongibbsFreeEnergy.DpressuregibbsFreeEnergy.Dtemperature heatCapacityheatCapacity.DmolesheatCapacity.DmolFractionheatCapacity.DpressureheatCapacity.DtemperaturelogFugacityCoefficientlogFugacityCoefficient.Dmoles#logFugacityCoefficient.DmolFraction logFugacityCoefficient.Dpressure#logFugacityCoefficient.DtemperaturemolecularWeightmolecularWeight.DmolesmolecularWeight.DmolFractionmolecularWeight.DpressuremolecularWeight.DtemperaturethermalConductivitythermalConductivity.Dmoles thermalConductivity.DmolFractionthermalConductivity.Dpressure thermalConductivity.Dtemperature viscosityviscosity.Dmolesviscosity.DmolFractionviscosity.Dpressureviscosity.Dtemperaturevolume volume.Dmolesvolume.DmolFractionvolume.Dpressurevolume.DtemperaturesurfaceTensionsurfaceTension.DmolessurfaceTension.DmolFractionsurfaceTension.DpressuresurfaceTension.DtemperaturebubblePointTemperaturebubblePointPressuredewPointTemperaturedewPointPressureVapor Vapor phase MyPackageVaporLiquid Liquid phase MyPackageLiquid VaporLiquiddefaultdefault material template MyPackage1!!! defaultм@fffffs@4@ rh}?333333?Эb.?433333?{ꌆ??333333?Эb.?433333?{ꌆ?333333?Эb.?433333?{ꌆ?fffffs@м@4@ rh}?22>NF>N>N defaultϼ@fffffs@(^SD@6:*?L7??/?AF?n{?ZfG%?yGo??L7??/?AF?n{?ZfG%?yGo?23]hb]h]h defaultм@8s@c&Nj @15?@O?0-C?W% ?6O#?oY>p U<>2V5@?~ӌ5?~?]\?vPˏE>W}>?@O?0-C?W% ?6O#?oY>p U<>24]+m+e+]+m+]+m+ "defaultм@87v@Yw(/@@3/Z?^Rݥ?[bD7#?h㈵>>0Sz?#Z?Ǚ(n?y%?MYX?6V^+?vQl?^K ??^Rݥ?[bD7#?h㈵>>0Sz?#Z?25|!!S !|!! ! defaultм@AW0~u@R4@?ĄX?mqvT?<`Ė1Z>S6>7`0*?ZsZ?Z?Ż?'?b*?1R֪? "??ĄX?mqvT?<`Ė1Z>S6>7`0*?ZsZ?26|@@@|@@|@@ 'defaultм@xm*w@ &'@Q?{Gz? ș?@;1vo=_0>B1Ը? D??L7??/?cC>=_0>B1Ը? D?2 Reactor 1GFixedConversionReactor - perform reactions using a specified conversion=`O]GXa%pHCOUSCOUS0002 Pressure dropPressure drop over the reactor?? _BHeat duty typeType of heat duty specification Isothermal Isothermal Isothermal Heat duty Energy inlet TemperatureReactor effluent temperature?fffffs@r@ _B Heat dutyReactor heat duty@?@#IV _ _B Enthalpy TypeEnthalpy calculation type Use EnthalpyF Use EnthalpyF Use EnthalpyF"Use Enthalpy (no heat of reaction)!Use Enthalpy and heat of reactionThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1 conversionEthanol?Last run+++ specifications +++ Using enthalpyF in enthalpy calculations Heat duty type: Isothermal Temperature: 313.15 K Pressure drop: 0 Pa +++ optional parameters +++ Heat duty: -207552.325334813 W +>! $not all material ports are connected Ethanol2EthylInletOutlet   $@@@@@@@@ @ @ @@ @@@@@ @@@@@@#@"@ ChemSepUO_2ChemSep Unit OperationqeWCXcCSUOf[ChemSep] Version=6.82 Compiled=2011-4-22 18:34 Name=C:\Users\jasper\AppData\Local\Temp\CS_7_A~1.sep Title=ChemSep CO Unit Operation "ChemSepUO_2" in COFE Flowsheet User=jasper Date=2011-05-23 Time=09:55:27 [Cape-Open] unitname=ChemSepUO_2 CO_ID=CS_7_A20_1CC191E_C6BF7090 3 components Ethanol 64-17-5 46.0690002441 Mw Diethyl ether 60-29-7 74.1230010986 Mw Water 7732-18-5 18.0149993896 Mw 0 thermo exe=C:\Program Files (x86)\ChemSepL6v70\bin\co-col2.exe mode=COFE NoWarnings=FALSE WilsonEstimate=TRUE Status= 0 only K-values and ethalpies 0 use only perturbed derivative 0 use only perturbed mole derivative 0.001 relative T perturbation 0.001 relative P perturbation 0.001 X perturbation 0 write all values to log 1 use initial guess 0 inlet reflash 0 outlet reflash 0 expose energy ports 0 clear log 0 update icon CO Thermo Version=Auto 2 number of run levels normal simplified 1 current run level [Paths] Device drivers path=c:\program files (x86)\chemsepl6v70\bin\ Help and Info path=c:\program files (x86)\chemsepl6v70\help\ Component data path=c:\program files (x86)\chemsepl6v70\pcd\ Property data path=c:\program files (x86)\chemsepl6v70\ipd\ Section data path=c:\program files (x86)\chemsepl6v70\ild\ Executables path=C:\Program Files (x86)\ChemSepL6v70\bin\ Temporary path=WINTMPDIR Scripts path=c:\program files (x86)\chemsepl6v70\bin\ [Units] Temperature=K Flow=kmol/s Mass flow=kg/s Pressure=N/m2 Heat=J/s Enthalpy=J/kmol Entropy=J/kmol/K Fraction=_ Length=m 1/Length=1/m Area=m2 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/m/K Diffusivity=m2/s Interaction parameter=J/mol Time=s [Components] 3 53 1102 Library Offset, Index DT=2010-09-20,09:33:26 CHK=41409 CAS=64-17-5 CID=Ethanol Name=Ethanol Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 98 1402 Library Offset, Index DT=2010-09-20,09:33:26 CHK=49315 CAS=60-29-7 CID=Diethyl ether Name=Diethyl ether Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 14 1921 Library Offset, Index DT=2010-09-20,09:33:26 CHK=32172 CAS=7732-18-5 CID=Water Name=Water Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.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=8 S= 0 Pumparound stages P= [Properties] 350 BIP estimation temperature [Thermodynamics] * K model * * * Activity coefficient * * Wilson model * * UNIQUAC model * * Equation of State * * Cubic EOS * * Virial EOS * * Vapour pressure * 0 Henry's law * Henry's default * [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 0 Qcolumn lost to surroundings [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 8 Stage Feed1{split} 313.15 Temperature 101325 Pressure 0 Vapour fraction 3 componentflows 0.0168761682863 Component 1 flow 0.00843840619593 Component 2 flow 0.0153367365414 Component 3 flow [Condenser] 1 Type Reflux ratio 10 Value Qcondenser * Type * * Initialization guess [Reboiler] 7 Type Mole fraction of a component 0.00001 Value Qreboiler 2 1st comp. * Type * * Initialization guess [Solve options] 3 Initialization Old Results 1 Method Newton's method 0.5 Flow Step limit 10 Temperature Step limit 1 Composition Step limit 1 Flux 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= 8 DOS extender NT 1 Show windows Hidden [FlowSheet] [CoCo] [Settings] ComboBox=ComboBox14 -1 ComboBox=ComboBox20 -1 ComboBox=ComboBox21 -1 CheckBox=CheckBox3 0 Show settings CheckBox=CheckBox1 1 Auto colors CheckBox=CheckBox2 1 Auto points Edit=Edit9 0.2 StringGrid=StringGrid5 2 8 Title Labels Stages Axis color Commands Box Labels box Import data StringGrid=StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 y1 x2 y2 StringGrid=StringGrid3 1 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage CheckBox=CheckBox10 0 Show settings ComboBox=ComboBox22 1 ComboBox=ComboBox23 0 StringGrid=StringGrid7 16 2 Title McCabe-Thiele diagram - Ethanol Xlabel X Diethyl ether/(Diethyl ether+Ethanol) Ylabel Y Diethyl ether/(Diethyl ether+Ethanol) 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 StringGrid=StringGrid11 5 3 CheckBox=CheckBox45 0 Lumped ComboBox=ComboBox75 1 ComboBox=ComboBox76 0 ComboBox=ComboBox77 0 Edit=Edit55 0.95 Edit=Edit56 0.95 Edit=Edit57 1.2 Edit=Edit1 1 CheckBox=CheckBox2 0 Use old results CheckBox=CheckBox3 1 Automatic CheckBox=CheckBox1 0 Keep sep-files CheckBox=CheckBox4 1 Restore original StringGrid=StringGrid1 1 6 Name Variable Units Value Start/Valuelist End StringGrid=StringGrid2 4 1 Name Variable Units Current Value StringGrid=StringGrid3 1 1 None ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Binary Phase Diagram ComboBox=ComboBox4 0 ComboBox=ComboBox15 0 Edit=Edit17 Plot font CheckBox=CheckBox2 1 Color=Edit18 1635136 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 1635136 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 1635136 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 1635136 SpinEdit=SpinEdit3 1 ComboBox=ComboBox14 0 RadioButton=RadioButton3 TRUE DrawSetColors=BVLEcolors 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 ComboBox=ComboBox7 -1 ComboBox=ComboBox11 -1 ComboBox=ComboBox6 -1 Memo=Memo1 Memo1, ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox4 0 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Ternary Phase Diagram Edit=Edit4 T Edit=Edit6 0 Edit=Edit7 1 Edit=Edit8 1 Edit=Edit5 StringGrid=StringGrid1 3 5 0 0 ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 Edit=Edit3 21 Edit=Edit4 Binary Property Diagram Memo=Memo1 StringGrid=StringGrid1 13 4 Axis Left Right X/Y Property -click to select- -click to select- x Title x Units - Minimum 0 Maximum 1 Interval 0.2 Grid Off Off Off Log Off Off Off Color Blue Red Black Line Normal Normal Style Solid Solid Point None None Edit=Edit5 ComboBox=ComboBox7 -1 ComboBox=ComboBox6 -1 [End Settings] [End of Input] [Results] 1 Converged 0 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 307.5565966 1.013250000E+05 8.446123538E-03 8.446123538E-02 -2.473348953E+06 2 307.5683244 1.013250000E+05 9.290735892E-02 8.442547466E-02 0.000000000E+00 3 307.5894114 1.013250000E+05 9.287159820E-02 8.436033946E-02 0.000000000E+00 4 307.6294988 1.013250000E+05 9.280646299E-02 8.423303442E-02 0.000000000E+00 5 307.7145177 1.013250000E+05 9.267915796E-02 8.394712373E-02 0.000000000E+00 6 307.9337386 1.013250000E+05 9.239324726E-02 8.312630114E-02 0.000000000E+00 7 308.6992482 1.013250000E+05 9.157242468E-02 7.980256884E-02 0.000000000E+00 8 312.6362050 1.013250000E+05 8.824869238E-02 1.221003842E-01 0.000000000E+00 9 312.6380238 1.013250000E+05 8.989582004E-02 1.220903961E-01 0.000000000E+00 10 312.6492283 1.013250000E+05 8.988583194E-02 1.220294391E-01 0.000000000E+00 11 312.7185553 1.013250000E+05 8.982487488E-02 1.216571791E-01 0.000000000E+00 12 313.1509735 1.013250000E+05 8.945261490E-02 1.194593266E-01 0.000000000E+00 13 315.8390162 1.013250000E+05 8.725476241E-02 1.102916040E-01 0.000000000E+00 14 327.6322512 1.013250000E+05 7.808703979E-02 9.929785123E-02 0.000000000E+00 15 343.7562251 1.013250000E+05 6.709328703E-02 9.780391440E-02 0.000000000E+00 16 350.3139428 1.013250000E+05 6.559935020E-02 9.823833117E-02 0.000000000E+00 17 351.8513370 1.013250000E+05 6.603376697E-02 9.835618053E-02 0.000000000E+00 18 352.2269327 1.013250000E+05 6.615161633E-02 9.830129426E-02 0.000000000E+00 19 352.5065138 1.013250000E+05 6.609673006E-02 9.806491010E-02 0.000000000E+00 20 353.2836210 1.013250000E+05 6.586034590E-02 3.220456420E-02 2.629355557E+06 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2551945E+08 -0.2551945E+08 -0.8285307E+05 -0.8285307E+05 2 0.1102217E+07 -0.2552841E+08 0.3704175E+04 -0.8282894E+05 3 0.1104321E+07 -0.2554454E+08 0.3755449E+04 -0.8279363E+05 4 0.1108358E+07 -0.2557525E+08 0.3841354E+04 -0.8274150E+05 5 0.1117057E+07 -0.2564089E+08 0.3994231E+04 -0.8266510E+05 6 0.1140012E+07 -0.2581499E+08 0.4301188E+04 -0.8257556E+05 7 0.1222029E+07 -0.2647381E+08 0.5070475E+04 -0.8277440E+05 8 0.1644566E+07 -0.3015775E+08 0.7790067E+04 -0.8706927E+05 9 0.1644758E+07 -0.3015948E+08 0.7791263E+04 -0.8707170E+05 10 0.1645944E+07 -0.3016996E+08 0.7798544E+04 -0.8708649E+05 11 0.1653281E+07 -0.3023375E+08 0.7843023E+04 -0.8717694E+05 12 0.1698966E+07 -0.3061678E+08 0.8114590E+04 -0.8772929E+05 13 0.1978918E+07 -0.3256333E+08 0.9706060E+04 -0.9069998E+05 14 0.3056438E+07 -0.3607660E+08 0.1581890E+05 -0.9641620E+05 15 0.3693370E+07 -0.3685389E+08 0.1993300E+05 -0.9781244E+05 16 0.3440206E+07 -0.3675776E+08 0.1727400E+05 -0.9795635E+05 17 0.3318122E+07 -0.3673344E+08 0.1550010E+05 -0.9806920E+05 18 0.3282891E+07 -0.3677404E+08 0.1497133E+05 -0.9814442E+05 19 0.3255748E+07 -0.3690649E+08 0.1491444E+05 -0.9825924E+05 20 0.3202206E+07 -0.3728583E+08 0.1507501E+05 -0.9865685E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.7410844E+02 0.2936463E+01 0.7810358E-05 0.1182707E+06 0.1585974E-01 2 0.7409545E+02 0.2935836E+01 0.7811212E-05 0.1182499E+06 0.1586090E-01 3 0.7407267E+02 0.2934733E+01 0.7812722E-05 0.1182137E+06 0.1586300E-01 4 0.7403147E+02 0.2932718E+01 0.7815503E-05 0.1181493E+06 0.1586704E-01 5 0.7395213E+02 0.2928766E+01 0.7821057E-05 0.1180292E+06 0.1587577E-01 6 0.7377933E+02 0.2919842E+01 0.7834021E-05 0.1177836E+06 0.1589886E-01 7 0.7331295E+02 0.2894190E+01 0.7873527E-05 0.1171922E+06 0.1598057E-01 8 0.7158003E+02 0.2790195E+01 0.8050210E-05 0.1153332E+06 0.1639549E-01 9 0.7157936E+02 0.2790153E+01 0.8050286E-05 0.1153325E+06 0.1639566E-01 10 0.7157522E+02 0.2789891E+01 0.8050762E-05 0.1153278E+06 0.1639674E-01 11 0.7154923E+02 0.2788260E+01 0.8053716E-05 0.1152992E+06 0.1640351E-01 12 0.7138664E+02 0.2778082E+01 0.8072165E-05 0.1151228E+06 0.1644630E-01 13 0.7038102E+02 0.2715637E+01 0.8187130E-05 0.1140394E+06 0.1671535E-01 14 0.6479559E+02 0.2410132E+01 0.8759420E-05 0.1069610E+06 0.1795247E-01 15 0.5092476E+02 0.1805346E+01 0.9932736E-05 0.8480010E+05 0.1986704E-01 16 0.4217947E+02 0.1467323E+01 0.1063564E-04 0.6938681E+05 0.2074870E-01 17 0.3977389E+02 0.1377593E+01 0.1082734E-04 0.6506127E+05 0.2096955E-01 18 0.3910033E+02 0.1352819E+01 0.1087939E-04 0.6392275E+05 0.2103374E-01 19 0.3848632E+02 0.1330519E+01 0.1092424E-04 0.6304215E+05 0.2110106E-01 20 0.3703207E+02 0.1277428E+01 0.1103247E-04 0.6105913E+05 0.2127973E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.7409545E+02 0.6909653E+03 0.2057115E-03 0.1841458E+06 0.1249643E+00 0.1531547E-01 2 0.7407039E+02 0.6910556E+03 0.2059560E-03 0.1841058E+06 0.1250018E+00 0.1531999E-01 3 0.7402507E+02 0.6912149E+03 0.2063889E-03 0.1840335E+06 0.1250816E+00 0.1532942E-01 4 0.7393776E+02 0.6915060E+03 0.2071861E-03 0.1838943E+06 0.1252830E+00 0.1535260E-01 5 0.7374752E+02 0.6920786E+03 0.2087788E-03 0.1835920E+06 0.1259095E+00 0.1542272E-01 6 0.7323344E+02 0.6934012E+03 0.2125563E-03 0.1827817E+06 0.1283034E+00 0.1568559E-01 7 0.7131380E+02 0.6977005E+03 0.2252181E-03 0.1797938E+06 0.1395619E+00 0.1690798E-01 8 0.6132716E+02 0.7215724E+03 0.2971922E-03 0.1637904E+06 0.2026366E+00 0.2362974E-01 9 0.6132326E+02 0.7215857E+03 0.2972351E-03 0.1637842E+06 0.2026505E+00 0.2363122E-01 10 0.6129901E+02 0.7216653E+03 0.2974897E-03 0.1637455E+06 0.2027488E+00 0.2364163E-01 11 0.6114810E+02 0.7221432E+03 0.2990097E-03 0.1635031E+06 0.2034202E+00 0.2371244E-01 12 0.6022521E+02 0.7249965E+03 0.3080880E-03 0.1620131E+06 0.2077980E+00 0.2417140E-01 13 0.5542652E+02 0.7398842E+03 0.3564033E-03 0.1542619E+06 0.2310074E+00 0.2653667E-01 14 0.4501702E+02 0.7699409E+03 0.4424360E-03 0.1387409E+06 0.2808258E+00 0.3077334E-01 15 0.3906111E+02 0.7793630E+03 0.4295836E-03 0.1323090E+06 0.3102090E+00 0.3196570E-01 16 0.3745792E+02 0.7796655E+03 0.4115038E-03 0.1311636E+06 0.3188888E+00 0.3203475E-01 17 0.3700767E+02 0.7799117E+03 0.4064297E-03 0.1306708E+06 0.3229064E+00 0.3222021E-01 18 0.3659365E+02 0.7809396E+03 0.4040352E-03 0.1297447E+06 0.3296710E+00 0.3277792E-01 19 0.3561242E+02 0.7841043E+03 0.3997442E-03 0.1272535E+06 0.3474892E+00 0.3432475E-01 20 0.3270914E+02 0.7960147E+03 0.3871978E-03 0.1196794E+06 0.4007402E+00 0.3893475E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.517435663E-03 0.974738367E-03 0.176371372E-02 0.313837231E-02 0.557827711E-02 2 0.999481722E+00 0.999021556E+00 0.998221053E+00 0.996799511E+00 0.994165497E+00 3 0.842563073E-06 0.370602966E-05 0.152331329E-04 0.621163873E-04 0.256225966E-03 Component Mole fractions on stages: 6 to 10 1 0.100791876E-01 0.191999459E-01 0.432778053E-01 0.432993660E-01 0.434201441E-01 2 0.988835222E+00 0.975962693E+00 0.933038262E+00 0.933015676E+00 0.932881362E+00 3 0.108559035E-02 0.483736157E-02 0.236839326E-01 0.236849577E-01 0.236984941E-01 Component Mole fractions on stages: 11 to 15 1 0.441013383E-01 0.479724169E-01 0.701528930E-01 0.190038043E+00 0.495409083E+00 2 0.932077579E+00 0.927244236E+00 0.898231060E+00 0.738740720E+00 0.338838548E+00 3 0.238210830E-01 0.247833469E-01 0.316160472E-01 0.712212366E-01 0.165752369E+00 Component Mole fractions on stages: 16 to 20 1 0.690850031E+00 0.741101903E+00 0.744986960E+00 0.728483370E+00 0.677665206E+00 2 0.852528380E-01 0.172528309E-01 0.330542636E-02 0.613912268E-03 0.104319644E-03 3 0.223897131E+00 0.241645266E+00 0.251707613E+00 0.270902718E+00 0.322230474E+00 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.974738367E-03 0.184264467E-02 0.335499447E-02 0.603987816E-02 0.109952083E-01 2 0.999021556E+00 0.998140969E+00 0.996577041E+00 0.993678575E+00 0.987810350E+00 3 0.370602966E-05 0.163863315E-04 0.679644090E-04 0.281546372E-03 0.119444135E-02 Component Mole fractions on stages: 6 to 10 1 0.210517347E-01 0.477550663E-01 0.170023364E+00 0.170122651E+00 0.170687364E+00 2 0.973619776E+00 0.926054739E+00 0.686930937E+00 0.686811920E+00 0.686097343E+00 3 0.532848955E-02 0.261901942E-01 0.143045699E+00 0.143065429E+00 0.143215293E+00 Component Mole fractions on stages: 11 to 15 1 0.173921049E+00 0.192439224E+00 0.287483301E+00 0.504604171E+00 0.635831394E+00 2 0.681790785E+00 0.656083221E+00 0.523035262E+00 0.228948700E+00 0.571843454E-01 3 0.144288166E+00 0.151477555E+00 0.189481437E+00 0.266447129E+00 0.306984261E+00 Component Mole fractions on stages: 16 to 20 1 0.669852955E+00 0.672551306E+00 0.661414026E+00 0.627122902E+00 0.523760731E+00 2 0.116002730E-01 0.222641161E-02 0.416064096E-03 0.733450269E-04 0.100000000E-04 3 0.318546772E+00 0.325222282E+00 0.338169910E+00 0.372803753E+00 0.476229269E+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] -2.473348953E+06 [Reboiler Heat Duty] 2.629355557E+06 [K-values] Component K-values on stages: 1 to 5 1 0.530845693E+00 0.528988786E+00 0.525697950E+00 0.519608545E+00 0.507337101E+00 2 0.100046062E+01 0.100088223E+01 0.100164966E+01 0.100314079E+01 0.100643357E+01 3 0.227349253E+00 0.226165915E+00 0.224133972E+00 0.220625778E+00 0.214515319E+00 Component K-values on stages: 6 to 10 1 0.478781809E+00 0.402050451E+00 0.254540342E+00 0.254518523E+00 0.254384058E+00 2 0.101562771E+01 0.105389309E+01 0.135827084E+01 0.135847333E+01 0.135969243E+01 3 0.203733223E+00 0.184701249E+00 0.165568995E+00 0.165553326E+00 0.165474606E+00 Component K-values on stages: 11 to 15 1 0.253571023E+00 0.249286066E+00 0.244024237E+00 0.376608150E+00 0.779151654E+00 2 0.136710205E+01 0.141330277E+01 0.171734322E+01 0.322666484E+01 0.592537250E+01 3 0.165093809E+00 0.163610687E+00 0.166855644E+00 0.267299697E+00 0.539937679E+00 Component K-values on stages: 16 to 20 1 0.103134580E+01 0.110192620E+01 0.112635495E+01 0.116162776E+01 0.129384500E+01 2 0.734920962E+01 0.774916501E+01 0.794451237E+01 0.837019625E+01 0.104319644E+02 3 0.702870506E+00 0.743015715E+00 0.744322914E+00 0.726663065E+00 0.676628874E+00 [Molecular weights] 1 46.069 2 74.123 3 18.015 [Feed stream 1] 8 Stage Number 4.0651311023630E-02 Flow rate 3.1315000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.8678778761576E+07 Enthalpy [J/kmol] -1.0332913369027E+05 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 4.1514450238739E-01 Mole fraction of component 1 2.0758017351580E-01 Mole fraction of component 2 3.7727532409680E-01 Mole fraction of component 3 4.0651311023630E-02 Flow rate 4.1514450238739E-01 Mole fraction of component 1 2.0758017351580E-01 Mole fraction of component 2 3.7727532409680E-01 Mole fraction of component 3 4.1308372344738E+01 Molar mass 7.9668043790367E+02 Density 5.5759096878778E-04 Viscosity 3.3192103776202E-01 Thermal conductivity 1.2619814750925E+05 Heat capacity 3.7975761864533E-02 Surface tension [Reflashed Feed stream 1] 8 Stage Number 4.0651311023630E-02 Flow rate 3.1314999998371E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.8678778761576E+07 Enthalpy [J/kmol] -1.0332913369651E+05 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 4.1514450238739E-01 Mole fraction of component 1 2.0758017351580E-01 Mole fraction of component 2 3.7727532409680E-01 Mole fraction of component 3 4.0651311023630E-02 Flow rate 4.1514450238739E-01 Mole fraction of component 1 2.0758017351580E-01 Mole fraction of component 2 3.7727532409680E-01 Mole fraction of component 3 4.1308372344738E+01 Molar mass 7.9668043792208E+02 Density 5.5759096893935E-04 Viscosity 3.3192103775718E-01 Thermal conductivity 1.2619814750449E+05 Heat capacity 3.7975761866510E-02 Surface tension [Top product] 1 Stage Number 8.4461235380000E-03 Flow rate 3.0755659660000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.5519452018459E+07 Enthalpy [J/kmol] -8.2853073293743E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.7473836700000E-04 Mole fraction of component 1 9.9902155600000E-01 Mole fraction of component 2 3.7060296600000E-06 Mole fraction of component 3 8.4461235380000E-03 Flow rate 9.7473836700000E-04 Mole fraction of component 1 9.9902155600000E-01 Mole fraction of component 2 3.7060296600000E-06 Mole fraction of component 3 7.4095447879135E+01 Molar mass 6.9096529169770E+02 Density 2.0571150927873E-04 Viscosity 1.2496431881954E-01 Thermal conductivity 1.8414576215525E+05 Heat capacity 1.5315471549734E-02 Surface tension [Bottom product] 20 Stage Number 3.2204564200000E-02 Flow rate 3.5328362100000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.7285833512019E+07 Enthalpy [J/kmol] -9.8656847026173E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 5.2376073100000E-01 Mole fraction of component 1 1.0000000000000E-05 Mole fraction of component 2 4.7622926900000E-01 Mole fraction of component 3 3.2204564200000E-02 Flow rate 5.2376073100000E-01 Mole fraction of component 1 1.0000000000000E-05 Mole fraction of component 2 4.7622926900000E-01 Mole fraction of component 3 3.2709144464689E+01 Molar mass 7.9601467404499E+02 Density 3.8719780862477E-04 Viscosity 4.0074022497211E-01 Thermal conductivity 1.1967942761275E+05 Heat capacity 3.8934745092848E-02 Surface tension [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlash AutoDUseOnlyKValuesAndEnthalpyFromCOSE*RestartDataAvailable,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts UseInitialGuess(Temperature profile4Temperature at each stage !8s@MxS9s@<:n9s@mUm:s@n;s@5>s@l0Ks@HK-s@qX5s@46=cs@3s@Q0cjs@=@ls@-ozt@}|u@ u@͋u@J.v@6v@Ww,v@"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 stage#_Mj @%+:W@)C7W@3W@(Rw+W@D<*W@} V@RqV@UyV@WsxxV@9tV@K|\V@NU@ VS@l)jP@x[fP@q<)P@P@^G0P@?wP@(Liquid Flow profile4Liquid Flow at each stage6fU@~:U@" =U@/3 U@eg٬T@o`QT@%I]S@?ڱl^@K Ʌ^@QT^@W8j^@Kee]@ң[@X@$2bUssX@1a@X@k˖X@ KgHX@+|'X@Yw(/@@Duties profile*Duties at each stagemyBKuDA4Vapour Moleweight profile@Vapour Moleweight at each stageeSR@QR@YR@3R@⪲|R@qR@ o_TR@,&6Q@';Q@TgQ@&Q@ԲQ@ǵbQ@Q2P@S"^vI@{NzE@YC@bg ׌C@׻?>C@cB@.Vapour Density profile:Vapour Density at each stageO7P}@ [|@KUz@4v@ ]n@[[@,H3M'@QR@n;R@WXp?2Vapour Viscosity profile>Vapour Viscosity at each stage@n'a>y͜a>Ulb>c>ӯf>FХm>EO>,p>ߦ >BM8>yqL>u%>wBn+>^>1Hט>);M>JG>_ >>!#>:Vapour Heat capacity profileFVapour Heat capacity at each stage&S]@Nё\]@B]@R!]@Biށ]@RI&r]@:ML]@&S\@zG\@?٬\@&\@\@ݓ\@/$Z@a43U@~XQ@uCP@'1O@a+eO@2dN@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stage=~"=?-#=?c>?0s??A?nG?5]?,Whɐ?V?ʐ?z>Nʐ? \̐?ّLא?a]&?3!!b?E|X?%??ح y?weމ?q*?1Zʕ?4Liquid Moleweight profile@Liquid Moleweight at each stageQR@ER@3R@߄B|R@F ^oR@eSNR@_LQ@G`N@o l`N@EN@DN@]hN@5K@`-F@s҇C@`B@TB@#KB@JOcA@$zZ@@.Liquid Density profile:Liquid Density at each stage4︗@Ciq@H}@5^I @k @>yX5@vͅ@؁sF@#J{@;pΈR@L F%@@s@tF@ClZ@R]@^)K_@:Mg@=Հ@@2Liquid Viscosity profile>Liquid Viscosity at each stagem:oT*?֞*?&C +? (+?[wl?sA"*?B?fOs?Ц4?~B,Q ?sL?&?߷ ?0{v?BÑh?q?"dT?mWC=?QL9?0Surface tension profile<Surface tension at each stage.]?K3@`?~e?#D/q?wp?F ?АTSP?mK e2?!BT2?O5?P;H?1c?t-m,?e ?/]?`+f?p*?~|DȠ?.c}?mkA? Unit is validCChemSep (TM) - COL2 6.81 Copyright (c) 1988-2011 Harry Kooijman and Ross Taylor 2100 6 LITE free license Checking data file C:\Users\jasper\AppData\Local\Temp\CS_7_A~1.SEP Cape Open unit name: ChemSepUO_2 Cape-Open unit id: CS_7_A20_1CC191E_C6BF7090 Cape-Open run level: normal Cape open Initialized Cape Open Thermodynamic-properties enabled Reading configuration Reading component property libraries Reading thermodynamic property options Reading specifications Reading reaction data Checking Component Data 64-17-5 Ethanol 60-29-7 Diethyl ether 7732-18-5 Water * No class Determining feed conditions Possible trivial solution Run level: Initialization Reading initial temperature profiles Reading initial composition profiles Init 110 milliseconds Run level: Complete model Iteration Error 0 -0.0799 Run level: Report Convergence obtained in 0 iterations Time 405 milliseconds FixMem driver done run time: 0.66 seconds Using: C:\Program Files (x86)\ChemSepL6v70\bin\co-col2.exe Using CAPE-OPEN version 1.1 thermodynamics CAPE-OPEN thermo-properties were enabled CAPE-OPEN diffusion coefficients were disabled CAPE-OPEN supplied derivatives were enabled CAPE-OPEN supplied molar derivatives were enabled Inlet re-flash: <none> Outlet flash: Auto Flash used for TopProduct: PVF Flash used for BottomProduct: PVF CAPE-OPEN supplied d H / d T have been used CAPE-OPEN supplied d H / d x have been used CAPE-OPEN supplied d K / d T have been used CAPE-OPEN supplied d K / d x and d K / d y have been used Relative perturbation of pressure: 0.001 Relative perturbation of temperature: 0.001 Perturbation of composition: 0.001N ]-not all ports are connectedFeed1{split}_stage8 TopProduct BottomProduct @ @0@@ @ @ @(@ @(@$@,@@@@@@@@$@@(@@(@ @(@ @ @ @,@$@@@$@@(@ @,@ @ @,@ @$@0@,@4@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@$@4@,@0@@ 4@,@0@ 4@,@0@4@,@0@ 4@,@0@ 4@,@0@ ,@0@  ,@0@@C@message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Ethanol (T = 353.28 K, range = [159.05 - 353.15] K)  (last message repeated 1 time) ChemSepUO_3ChemSep Unit OperationqeWCXcCSUOEY[ChemSep] Version=6.82 Compiled=2011-4-22 18:34 Name=C:\Users\jasper\AppData\Local\Temp\CS_8_A~1.sep Title=ChemSep CO Unit Operation "ChemSepUO_3" in COFE Flowsheet User=jasper Date=2011-05-23 Time=09:55:29 [Cape-Open] unitname=ChemSepUO_3 CO_ID=CS_8_A20_1CC191E_C6BFBEB0 3 components Ethanol 64-17-5 46.0690002441 Mw Diethyl ether 60-29-7 74.1230010986 Mw Water 7732-18-5 18.0149993896 Mw 0 thermo exe=C:\Program Files (x86)\ChemSepL6v70\bin\co-col2.exe mode=COFE NoWarnings=FALSE WilsonEstimate=TRUE Status= 0 only K-values and ethalpies 0 use only perturbed derivative 0 use only perturbed mole derivative 0.001 relative T perturbation 0.001 relative P perturbation 0.001 X perturbation 0 write all values to log 1 use initial guess 0 inlet reflash 0 outlet reflash 0 expose energy ports 0 clear log 0 update icon CO Thermo Version=Auto 2 number of run levels normal simplified 1 current run level [Paths] Device drivers path=c:\program files (x86)\chemsepl6v70\bin\ Help and Info path=c:\program files (x86)\chemsepl6v70\help\ Component data path=c:\program files (x86)\chemsepl6v70\pcd\ Property data path=c:\program files (x86)\chemsepl6v70\ipd\ Section data path=c:\program files (x86)\chemsepl6v70\ild\ Executables path=C:\Program Files (x86)\ChemSepL6v70\bin\ Temporary path=WINTMPDIR Scripts path=c:\program files (x86)\chemsepl6v70\bin\ [Units] Temperature=K Flow=kmol/s Mass flow=kg/s Pressure=N/m2 Heat=J/s Enthalpy=J/kmol Entropy=J/kmol/K Fraction=_ Length=m 1/Length=1/m Area=m2 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/m/K Diffusivity=m2/s Interaction parameter=J/mol Time=s [Components] 3 53 1102 Library Offset, Index DT=2010-09-20,09:33:26 CHK=41409 CAS=64-17-5 CID=Ethanol Name=Ethanol Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 98 1402 Library Offset, Index DT=2010-09-20,09:33:26 CHK=49315 CAS=60-29-7 CID=Diethyl ether Name=Diethyl ether Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 14 1921 Library Offset, Index DT=2010-09-20,09:33:26 CHK=32172 CAS=7732-18-5 CID=Water Name=Water Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd [Operation] 2 Operation Column 1 Operation kind Simple Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 15 Stages 1 Feed stages 0 Sidestream stages F=4 S= 0 Pumparound stages P= [Properties] 350 BIP estimation temperature [Thermodynamics] * K model * * * Activity coefficient * * Wilson model * * UNIQUAC model * * Equation of State * * Cubic EOS * * Virial EOS * * Vapour pressure * 0 Henry's law * Henry's default * [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 14 Last stage 0 Qcolumn lost to surroundings [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 4 Stage Feed1{split} 353.283621042 Temperature 101325 Pressure 0 Vapour fraction 3 componentflows 0.0168674860869 Component 1 flow 3.22045642e-007 Component 2 flow 0.0153367560674 Component 3 flow [Condenser] 1 Type Reflux ratio 3 Value Qcondenser * Type * * Initialization guess [Reboiler] 7 Type Mole fraction of a component 0.99 Value Qreboiler 3 1st comp. * Type * * Initialization guess [Solve options] 3 Initialization Old Results 1 Method Newton's method 0.5 Flow Step limit 10 Temperature Step limit 1 Composition Step limit 1 Flux 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= 8 DOS extender NT 1 Show windows Hidden [FlowSheet] [CoCo] [Settings] ComboBox=ComboBox14 -1 ComboBox=ComboBox20 -1 ComboBox=ComboBox21 -1 CheckBox=CheckBox3 0 Show settings CheckBox=CheckBox1 1 Auto colors CheckBox=CheckBox2 1 Auto points Edit=Edit9 0.2 StringGrid=StringGrid5 2 8 Title Labels Stages Axis color Commands Box Labels box Import data StringGrid=StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 y1 x2 y2 StringGrid=StringGrid3 1 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage CheckBox=CheckBox10 0 Show settings ComboBox=ComboBox22 -1 ComboBox=ComboBox23 -1 StringGrid=StringGrid7 16 2 StringGrid=StringGrid11 5 3 CheckBox=CheckBox45 0 Lumped ComboBox=ComboBox75 -1 ComboBox=ComboBox76 -1 ComboBox=ComboBox77 -1 Edit=Edit55 0.95 Edit=Edit56 0.95 Edit=Edit57 1.2 Edit=Edit1 1 CheckBox=CheckBox2 0 Use old results CheckBox=CheckBox3 1 Automatic CheckBox=CheckBox1 0 Keep sep-files CheckBox=CheckBox4 1 Restore original StringGrid=StringGrid1 1 6 Name Variable Units Value Start/Valuelist End StringGrid=StringGrid2 4 1 Name Variable Units Current Value StringGrid=StringGrid3 1 1 None ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Binary Phase Diagram ComboBox=ComboBox4 0 ComboBox=ComboBox15 0 Edit=Edit17 Plot font CheckBox=CheckBox2 1 Color=Edit18 1635136 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 1635136 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 1635136 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 1635136 SpinEdit=SpinEdit3 1 ComboBox=ComboBox14 0 RadioButton=RadioButton3 TRUE DrawSetColors=BVLEcolors 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 ComboBox=ComboBox7 -1 ComboBox=ComboBox11 -1 ComboBox=ComboBox6 -1 Memo=Memo1 Memo1, ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox4 0 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Ternary Phase Diagram Edit=Edit4 T Edit=Edit6 0 Edit=Edit7 1 Edit=Edit8 1 Edit=Edit5 StringGrid=StringGrid1 3 5 0 0 ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 Edit=Edit3 21 Edit=Edit4 Binary Property Diagram Memo=Memo1 StringGrid=StringGrid1 13 4 Axis Left Right X/Y Property -click to select- -click to select- x Title x Units - Minimum 0 Maximum 1 Interval 0.2 Grid Off Off Off Log Off Off Off Color Blue Red Black Line Normal Normal Style Solid Solid Point None None Edit=Edit5 ComboBox=ComboBox7 -1 ComboBox=ComboBox6 -1 [End Settings] [End of Input] [Results] 1 Converged 0 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 351.5684797 1.013250000E+05 2.065131110E-02 6.195393331E-02 -3.262442176E+06 2 351.7302933 1.013250000E+05 8.260524442E-02 6.175055181E-02 0.000000000E+00 3 351.9722318 1.013250000E+05 8.240186291E-02 6.151094840E-02 0.000000000E+00 4 352.3606129 1.013250000E+05 8.216225950E-02 9.368076345E-02 0.000000000E+00 5 352.3623552 1.013250000E+05 8.212679526E-02 9.367909853E-02 0.000000000E+00 6 352.3658421 1.013250000E+05 8.212513034E-02 9.367560064E-02 0.000000000E+00 7 352.3731325 1.013250000E+05 8.212163245E-02 9.366827610E-02 0.000000000E+00 8 352.3884873 1.013250000E+05 8.211430791E-02 9.365290586E-02 0.000000000E+00 9 352.4211349 1.013250000E+05 8.209893767E-02 9.362048519E-02 0.000000000E+00 10 352.4919097 1.013250000E+05 8.206651700E-02 9.355132432E-02 0.000000000E+00 11 352.6516707 1.013250000E+05 8.199735613E-02 9.339992771E-02 0.000000000E+00 12 353.0442942 1.013250000E+05 8.184595952E-02 9.304557767E-02 0.000000000E+00 13 354.2055302 1.013250000E+05 8.149160948E-02 9.206376936E-02 0.000000000E+00 14 359.0842978 1.013250000E+05 8.050980117E-02 9.048686985E-02 0.000000000E+00 15 370.6326728 1.013250000E+05 7.893290166E-02 1.155396819E-02 3.274258582E+06 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.3613261E+08 -0.3613261E+08 -0.9793185E+05 -0.9793185E+05 2 0.3361764E+07 -0.3632108E+08 0.1438328E+05 -0.9795399E+05 3 0.3318002E+07 -0.3653997E+08 0.1459657E+05 -0.9802804E+05 4 0.3269728E+07 -0.3681161E+08 0.1480899E+05 -0.9818908E+05 5 0.3269551E+07 -0.3681263E+08 0.1480927E+05 -0.9818988E+05 6 0.3269195E+07 -0.3681478E+08 0.1481067E+05 -0.9819146E+05 7 0.3268454E+07 -0.3681926E+08 0.1481373E+05 -0.9819478E+05 8 0.3266910E+07 -0.3682866E+08 0.1482010E+05 -0.9820179E+05 9 0.3263693E+07 -0.3684840E+08 0.1483330E+05 -0.9821681E+05 10 0.3257015E+07 -0.3689010E+08 0.1486035E+05 -0.9824988E+05 11 0.3243265E+07 -0.3697936E+08 0.1491459E+05 -0.9832686E+05 12 0.3215639E+07 -0.3717637E+08 0.1501776E+05 -0.9852733E+05 13 0.3165484E+07 -0.3764978E+08 0.1518682E+05 -0.9919206E+05 14 0.3116093E+07 -0.3863667E+08 0.1525056E+05 -0.1015077E+06 15 0.2799162E+07 -0.3832436E+08 0.1155617E+05 -0.1013619E+06 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.4154251E+02 0.1440007E+01 0.1071273E-04 0.6723605E+05 0.2078843E-01 2 0.4077327E+02 0.1412693E+01 0.1076437E-04 0.6617009E+05 0.2085969E-01 3 0.3989861E+02 0.1381438E+01 0.1082432E-04 0.6496528E+05 0.2094644E-01 4 0.3883133E+02 0.1343002E+01 0.1089954E-04 0.6350323E+05 0.2106116E-01 5 0.3882720E+02 0.1342853E+01 0.1089984E-04 0.6349753E+05 0.2106162E-01 6 0.3881883E+02 0.1342550E+01 0.1090044E-04 0.6348608E+05 0.2106256E-01 7 0.3880136E+02 0.1341918E+01 0.1090169E-04 0.6346223E+05 0.2106453E-01 8 0.3876481E+02 0.1340596E+01 0.1090431E-04 0.6341232E+05 0.2106865E-01 9 0.3868814E+02 0.1337821E+01 0.1090982E-04 0.6330766E+05 0.2107734E-01 10 0.3852657E+02 0.1331966E+01 0.1092148E-04 0.6308723E+05 0.2109583E-01 11 0.3818266E+02 0.1319478E+01 0.1094650E-04 0.6261869E+05 0.2113604E-01 12 0.3743502E+02 0.1292203E+01 0.1100194E-04 0.6160308E+05 0.2122765E-01 13 0.3573195E+02 0.1229372E+01 0.1113470E-04 0.5930491E+05 0.2146082E-01 14 0.3140223E+02 0.1065727E+01 0.1152025E-04 0.5351808E+05 0.2222469E-01 15 0.2156871E+02 0.7091897E+00 0.1223782E-04 0.3955837E+05 0.2389988E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.4077327E+02 0.7711188E+03 0.4208710E-03 0.1401755E+06 0.2530913E+00 0.2603979E-01 2 0.3960610E+02 0.7732650E+03 0.4162838E-03 0.1373275E+06 0.2744003E+00 0.2792085E-01 3 0.3817935E+02 0.7764806E+03 0.4104944E-03 0.1337842E+06 0.3004743E+00 0.3021403E-01 4 0.3629496E+02 0.7818236E+03 0.4026161E-03 0.1290113E+06 0.3349544E+00 0.3323099E-01 5 0.3628757E+02 0.7818471E+03 0.4025847E-03 0.1289924E+06 0.3350894E+00 0.3324275E-01 6 0.3627217E+02 0.7818963E+03 0.4025194E-03 0.1289530E+06 0.3353715E+00 0.3326736E-01 7 0.3623993E+02 0.7819997E+03 0.4023827E-03 0.1288705E+06 0.3359618E+00 0.3331885E-01 8 0.3617231E+02 0.7822178E+03 0.4020960E-03 0.1286973E+06 0.3372003E+00 0.3342685E-01 9 0.3602980E+02 0.7826834E+03 0.4014911E-03 0.1283319E+06 0.3398104E+00 0.3365439E-01 10 0.3572652E+02 0.7837014E+03 0.4002005E-03 0.1275527E+06 0.3453662E+00 0.3413837E-01 11 0.3506739E+02 0.7860445E+03 0.3973824E-03 0.1258511E+06 0.3574467E+00 0.3518901E-01 12 0.3356678E+02 0.7920856E+03 0.3909129E-03 0.1219388E+06 0.3849798E+00 0.3757461E-01 13 0.2975734E+02 0.8125548E+03 0.3743250E-03 0.1117915E+06 0.4550905E+00 0.4359016E-01 14 0.2115077E+02 0.8996719E+03 0.3313019E-03 0.8813069E+05 0.6156641E+00 0.5668532E-01 15 0.1829554E+02 0.9435579E+03 0.2857593E-03 0.8124905E+05 0.6745589E+00 0.5911236E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.838422158E+00 0.811199664E+00 0.780042133E+00 0.742000278E+00 0.741860756E+00 2 0.114303833E-03 0.155947868E-04 0.550285768E-05 0.446809653E-05 0.631451563E-06 3 0.161463538E+00 0.188784741E+00 0.219952365E+00 0.257995253E+00 0.258138613E+00 Component Mole fractions on stages: 6 to 10 1 0.741563442E+00 0.740941023E+00 0.739638209E+00 0.736905357E+00 0.731145894E+00 2 0.892069753E-07 0.125929373E-07 0.177484220E-08 0.249296318E-09 0.347601574E-10 3 0.258436469E+00 0.259058964E+00 0.260361789E+00 0.263094642E+00 0.268854106E+00 Component Mole fractions on stages: 11 to 15 1 0.718887200E+00 0.692237146E+00 0.631530405E+00 0.477195025E+00 0.126674011E+00 2 0.476763985E-11 0.628534915E-12 0.742260734E-13 0.578774289E-14 0.534971965E-16 3 0.281112800E+00 0.307762854E+00 0.368469595E+00 0.522804975E+00 0.873325989E+00 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.811199664E+00 0.769622082E+00 0.718767698E+00 0.651597872E+00 0.651335623E+00 2 0.155947868E-04 0.212780174E-05 0.732489339E-06 0.553572488E-06 0.782045791E-07 3 0.188784741E+00 0.230375790E+00 0.281231569E+00 0.348401575E+00 0.348664299E+00 Component Mole fractions on stages: 6 to 10 1 0.650786605E+00 0.649637443E+00 0.647226972E+00 0.642147245E+00 0.631336754E+00 2 0.110397218E-07 0.155591567E-08 0.218540607E-09 0.304703083E-10 0.417881699E-11 3 0.349213384E+00 0.350362556E+00 0.352773028E+00 0.357852755E+00 0.368663246E+00 Component Mole fractions on stages: 11 to 15 1 0.607841510E+00 0.554351642E+00 0.418562226E+00 0.111776294E+00 0.100000000E-01 2 0.550782483E-12 0.650090341E-13 0.506139366E-14 0.466768095E-16 0.821736175E-19 3 0.392158490E+00 0.445648358E+00 0.581437774E+00 0.888223706E+00 0.990000000E+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 [Condenser Heat Duty] -3.262442176E+06 [Reboiler Heat Duty] 3.274258582E+06 [K-values] Component K-values on stages: 1 to 5 1 0.103355832E+01 0.105402338E+01 0.108524929E+01 0.113873957E+01 0.113898385E+01 2 0.732961820E+01 0.732906008E+01 0.751254302E+01 0.807138475E+01 0.807435537E+01 3 0.855278539E+00 0.819464324E+00 0.782104103E+00 0.740511158E+00 0.740364338E+00 Component K-values on stages: 6 to 10 1 0.113948787E+01 0.114054544E+01 0.114278026E+01 0.114756446E+01 0.115809176E+01 2 0.808054559E+01 0.809358599E+01 0.812133828E+01 0.818161457E+01 0.831818131E+01 3 0.740053160E+00 0.739402539E+00 0.738043356E+00 0.735203625E+00 0.729267451E+00 Component K-values on stages: 11 to 15 1 0.118268856E+01 0.124873292E+01 0.150880888E+01 0.426919705E+01 0.126674011E+02 2 0.865612105E+01 0.966842415E+01 0.146651454E+02 0.123996050E+03 0.651031154E+03 3 0.716834668E+00 0.690595734E+00 0.633721460E+00 0.588596061E+00 0.882147465E+00 [Molecular weights] 1 46.069 2 74.123 3 18.015 [Feed stream 1] 4 Stage Number 3.2204564199942E-02 Flow rate 3.5328362104200E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.7285833506992E+07 Enthalpy [J/kmol] -9.8656847012583E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 5.2376073100006E-01 Mole fraction of component 1 1.0000000000018E-05 Mole fraction of component 2 4.7622926899994E-01 Mole fraction of component 3 3.2204564199942E-02 Flow rate 5.2376073100006E-01 Mole fraction of component 1 1.0000000000018E-05 Mole fraction of component 2 4.7622926899994E-01 Mole fraction of component 3 3.2709144464691E+01 Molar mass 7.9601467399712E+02 Density 3.8719780840105E-04 Viscosity 4.0074022498143E-01 Thermal conductivity 1.1967942762823E+05 Heat capacity 3.8934745087151E-02 Surface tension [Reflashed Feed stream 1] 4 Stage Number 3.2204564199942E-02 Flow rate 3.5328362764278E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.7285833506992E+07 Enthalpy [J/kmol] -9.8656844876810E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 5.2376073100006E-01 Mole fraction of component 1 1.0000000000018E-05 Mole fraction of component 2 4.7622926899994E-01 Mole fraction of component 3 3.2204564199942E-02 Flow rate 5.2376073100006E-01 Mole fraction of component 1 1.0000000000018E-05 Mole fraction of component 2 4.7622926899994E-01 Mole fraction of component 3 3.2709144464691E+01 Molar mass 7.9601466647485E+02 Density 3.8719777324028E-04 Viscosity 4.0074022645136E-01 Thermal conductivity 1.1967943005951E+05 Heat capacity 3.8934744192163E-02 Surface tension [Top product] 1 Stage Number 2.0651311100000E-02 Flow rate 3.5156847970000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.6132607385074E+07 Enthalpy [J/kmol] -9.7931854530849E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 8.1119966400000E-01 Mole fraction of component 1 1.5594786800000E-05 Mole fraction of component 2 1.8878474100000E-01 Mole fraction of component 3 2.0651311100000E-02 Flow rate 8.1119966400000E-01 Mole fraction of component 1 1.5594786800000E-05 Mole fraction of component 2 1.8878474100000E-01 Mole fraction of component 3 4.0773270445152E+01 Molar mass 7.7111878054871E+02 Density 4.2087103490698E-04 Viscosity 2.5309132355607E-01 Thermal conductivity 1.4017551697375E+05 Heat capacity 2.6039785968426E-02 Surface tension [Bottom product] 15 Stage Number 1.1553968190000E-02 Flow rate 3.7063267280000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.8324363650270E+07 Enthalpy [J/kmol] -1.0136193671546E+05 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.0000000000000E-02 Mole fraction of component 1 8.2173617500000E-20 Mole fraction of component 2 9.9000000000000E-01 Mole fraction of component 3 1.1553968190000E-02 Flow rate 1.0000000000000E-02 Mole fraction of component 1 8.2173617500000E-20 Mole fraction of component 2 9.9000000000000E-01 Mole fraction of component 3 1.8295539398193E+01 Molar mass 9.4355793396847E+02 Density 2.8575934057249E-04 Viscosity 6.7455887666134E-01 Thermal conductivity 8.1249047294787E+04 Heat capacity 5.9112362837064E-02 Surface tension [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlash AutoDUseOnlyKValuesAndEnthalpyFromCOSE*RestartDataAvailable,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts UseInitialGuess(Temperature profile4Temperature at each stage +~u@Hu@Bu@@@v@X4v@>}v@2Yv@u>7v@Ev@]v@/A>m v@qmv@rI#v@aHYqv@m*w@"Pressure profile.Pressure at each stageм@м@м@м@м@м@м@м@м@м@м@м@м@м@м@(Vapour Flow profile4Vapour Flow at each stageS4@#ST@95T@}ubT@8iT@d"T@xxȇT@PT@?TT@2AT@+4ήT@f3$vT@;v_T@4' T@b*S@(Liquid Flow profile4Liquid Flow at each stage큘|N@N@fN@ܠkW@&GYvkW@:}w =kW@ jW@E5iW@gW@HcW@djYW@BW@W@$((V@ &'@Duties profile*Duties at each stage+H~J HA4Vapour Moleweight profile@Vapour Moleweight at each stageapD@,}bD@C@}ijC@'iC@}khC@J)fC@HKaC@㈵XC@PfCC@$#gaC@@B@R'A@Wxf?@}5@.Vapour Density profile:Vapour Density at each stageZ-D ?,c?9w^?fG|?)^emS|?s{?>x?_s?n.g?$O?臭?} ݬ?i?Um77 ?$?2Vapour Viscosity profile>Vapour Viscosity at each stage=hfZw>a>}6C>^>D>QY!>j[>vi4>[M>*>-l>>>Y>n(>o,!>:Vapour Heat capacity profileFVapour Heat capacity at each stage"uqP@*P@%=P@.4iO@c#O@7O@tFZ*O@MƴO@$#gaO@tFZ*O@^.;1OO@o1N@wJM@[rPJ@ xC@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stageiI?6k>\? r?ͩ?2gd-?.zyl?ҭ?+*?PZWL?W/%?D?oz?Rn.@?2ڲ–?5y?4Liquid Moleweight profile@Liquid Moleweight at each stage,}bD@ OC@DC@h?%B@Ƨ$B@ypw"B@&B@ c AB@ݵ|B@{A@ K?@@=@7ܘ&5@jK2@.Liquid Density profile:Liquid Density at each stagejM@Q*@DC@ǘn@c]n@=U+o@}bo@( q@Pkwu@Qkw}@`"[@M O@~:pd@vq `@sFv|@2Liquid Viscosity profile>Liquid Viscosity at each stage0K. ;?NH;?:?zb:?@b:?T'a:?XEw^:?r{+ Z:?! $O:?1@::?9yi :?en9?`7!8?2ZR5?vZ>2?:Liquid Heat capacity profileFLiquid Heat capacity at each stageV-a@Gz*a@0*`@K?K8 Outlet flash: Auto Flash used for TopProduct: PVF Flash used for BottomProduct: PVF CAPE-OPEN supplied d H / d T have been used CAPE-OPEN supplied d H / d x have been used CAPE-OPEN supplied d K / d T have been used CAPE-OPEN supplied d K / d x and d K / d y have been used Relative perturbation of pressure: 0.001 Relative perturbation of temperature: 0.001 Perturbation of composition: 0.001m|Bnot all ports are connectedFeed1{split}_stage4 TopProduct BottomProduct @ @0@@ @ @ @(@ @(@$@,@@@@@@@@$@@(@@(@ @(@ @ @ @,@$@@@$@@(@ @,@ @ @,@ @$@0@,@4@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@$@4@,@0@@ 4@,@0@ 4@,@0@4@,@0@ 4@,@0@ 4@,@0@ ,@0@  ,@0@@E@message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Ethanol (T = 354.21 K, range = [159.05 - 353.15] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Ethanol (T = 359.08 K, range = [159.05 - 353.15] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Ethanol (T = 370.63 K, range = [159.05 - 353.15] K) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Ethanol (T = 353.28 K, range = [159.05 - 353.15] K)  (last message repeated 1 time) message: Warning: temperature out of range for liquid thermal conductivity correlation for compound Ethanol (T = 370.63 K, range = [159.05 - 353.15] K) Mixer_46Mixer - mix 2 or more inlet streams to a single outletk!^/E a-COUSCOUS0002Number of inletsNumber of inlet ports Pressure dropPressure drop along the mixer?? _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last runD+++ specifications +++ Number of inlets: 2 Pressure drop: 0 Pa !' $not all material ports are connectedInlet 1Inlet 2Outlet0@@@@@@@ @MS Sans-C6?-C6?h㈵>-C6?t,,