FSD100MbP?h㈵>dc 0dgffffr@м@Harry Kooijman and Ross TaylorPressure Swing MA iecr47p2696~1ChemsepAdapted from Luyben et al., Ind. Eng. Chem. Res. (2008) 47 pp. 2696-2707 Separation of Acetone and Methanol using two columns operating at two pressure. )Saved Pressure_Swing_MA_iecr47p2696.fsd Starting solve solving C1 Valve_6 C2 Pump_3 %Cutting self-recycle stream Recycle converged in 1 evaluation Solve finished in 10s, 328ms mUx temperaturepressure compositionflowMethanol and AcetoneAUwNA\t&&Methanol and Acetoneư>MbP?MbP?MbP?K-C:\Program Files (x86)\COCO\data\ChemSep1.pcdgMethanolCH3OHCH4O67-56-1COM@:^A?5?@?@ u@@ e@@ e@ {?@`@@ڤ?z?`T=@9`%;?VA3Y@H ALHA 8`•>@W 8 8 8dd@̔e@6??@? 8@ e@q@i`f^@@3.`U>@@ e@@e(A?-??@ e@@3 @j@3Ɍ@o2w?>9@@3c@d@̘@_?@@ e@y@ @3s-@ 1&@@qO?@הY@p@L0hC@?W@R`fq@p@h|@@ @vо@@ e@u@e Q> bJ?כi@M8@ 8n@@@f @O*@ڊ2`_b@z@K> C? [@@ 8q@b@f2@@@@qP?¾q@`fr@@#@@ M]h?58`U!>I@@@d 8 8 8 8 8 8 8Z7@ƫ@ ݔB 8 8`f>s@|@ @*? 8 8@ e@u@ 㥛 u@ X4?#~jL|sj1@G?G?Q?@?@֤?@?ۿ`?6?!S? k??@?@ڤ?D @z@)Տ?@?֤?wAcetoneCH3COCH3C3H6O67-64-1CC(=O)C@QA ?? t@`fNf@`fNf@@G@= M@`?`?=D@ ?]9 ?gA@@O AVA 8@O0@ > 8 8 8e@f@`}?n? \@? 8@f@@3@i`R@@>@`fNf@@3@eA @!$@`fNf@`f@jT@86 7? 9@`fNf@d'@`@~?`Ú?-`fNf@@ t@`@)f(@ ?@uob@p@q?TkXC[@LL@q@3o@@@h ,E@?@}z>@g@@ t@eA`>`fNf@`fru@:J?3֜$ 8`fq@@@fbӢj oT`"`fNf@p~@@A )@~?ໍCyq>i@@@d 8 8 8 8 8 8 8o5@`fE@+D 8 8s@|@ 7ԿBĽ ? 8 8g@@ t@ bX9dk ףp=p@ .V`¿x&1G@Y?@ @ @ @f?lD@ ? 8 8`R'??|? G? ?@P@`?<\@(@I:,?? ?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  sA?Acetone/Methanol p78 1/2cimported from NRTL.IPDsA?Acetone/Methanol p78 1/2cimported from NRTL.IPD Gz?Methanol/methanolimported from HAYDENO.IPD?Acetone/methanolimported from HAYDENO.IPD?Acetone/methanolimported from HAYDENO.IPD?Acetone/acetoneimported from HAYDENO.IPD(?Acetone/Methanolimported from VANLAAR.IPDw/?Acetone/Methanolimported from VANLAAR.IPDcZB>?Acetone/Methanolimported from MARGULES.IPD q?Acetone/Methanolimported from MARGULES.IPDgqZr@Acetone/Methanolimported from WILSON.IPDkٻ aTAcetone/Methanolimported from WILSON.IPDG>h\@Acetone/Methanol p78 1/2cimported from NRTL.IPDWr2W@Acetone/Methanol p78 1/2cimported from NRTL.IPD  QGw5EMethanol/Acetoneimported from UNIQUAC.IPDNʞMki@Methanol/Acetoneimported from UNIQUAC.IPD 9XAcetone/Methanolimported from UNIQUACP.IPDqv@Acetone/Methanolimported from UNIQUACP.IPDCH3OHCH2CH2COCH3OH?x?L7A`@@CH3ͪ?A`"? rh.@CH3CORI&?+?ʡE@(\0@p= c7@Ʌ@fffff}@,[@(\:@CH2OHCH2COCH3ͪ?A`"? rh.@OH?333333?5^I 1@CH3CORI&?+?ʡE@$@}@33333t@GzP@p= ףP@k@ V瞯<Methanol and Acetone67-56-1Methanol@`@@@ u@CH4OMethanol and AcetoneMethanol67-64-1Acetone= M@ t@C3H6OMethanol and AcetoneAcetone ????????????thermalConductivity.Dmoles?? / molexcessEnthalpy.Dpressure??gibbsFreeEnergy.Dpressure??enthalpyF.DmolFraction??viscosity.Dtemperature???? thermalConductivity.Dtemperature??thermalConductivity.Dpressure??enthalpyF.Dpressure??activityCoefficientheatCapacity.DmolFraction??entropyF.Dmoles??enthalpy.Dmoles??density.Dpressure?@?@heatOfVaporization??molecularWeight#logFugacityCoefficient.DmolFractionentropy.Dtemperature??viscosity.Dmoles???? / mol volume.Dmoles@@@@ enthalpyF??enthalpy??vaporPressure.Dtemperature??fugacity.Dtemperature??activity.DmolFractionvolume.Dpressure@@@@excessEnthalpy.Dtemperature??surfaceTension.DmolFraction?? activityCoefficient.DtemperaturefugacityCoefficient.Dmoles / molgibbsFreeEnergy??gibbsFreeEnergy.DmolFraction??activityCoefficient.Dmoles / molactivity.Dmoles / molenthalpy.DmolFraction??logFugacityCoefficiententhalpy.Dpressure??activitymolecularWeight.Dtemperature fugacityCoefficient.DmolFractionfugacity.Dpressurevolume.DmolFraction@@@@density?@?@activity.DtemperatureenthalpyF.Dtemperature??surfaceTension.Dtemperature??thermalConductivity??entropyF.DmolFraction??surfaceTension??density.DmolFraction?@?@heatCapacity.Dtemperature??#logFugacityCoefficient.DtemperatureexcessEnthalpy??viscosity.DmolFraction????fugacityCoefficient.DpressuresurfaceTension.Dmoles?? / molentropy.Dpressure??enthalpy.Dtemperature??gibbsFreeEnergy.Dmoles?? thermalConductivity.DmolFraction??density.Dmoles?@?@ / mollogFugacityCoefficient.Dmoles / molidealGasEnthalpy.Dtemperature??surfaceTension.Dpressure??enthalpyF.Dmoles??heatOfVaporization.Dtemperature??entropyF.Dtemperature??entropy.DmolFraction??volume@@@@entropyF??entropy??molecularWeight.DpressureheatCapacity.Dpressure??gibbsFreeEnergy.Dtemperature??fugacityCoefficientviscosity.Dpressure?? logFugacityCoefficient.DpressureidealGasEnthalpy?? heatCapacity?? fugacityCoefficient.DtemperatureentropyF.Dpressure??entropy.Dmoles??activityCoefficient.Dpressure viscosity???? activityCoefficient.DmolFractionexcessEnthalpy.Dmoles??volume.Dtemperature@@@@fugacity.Dmoles?? / moldensity.Dtemperature?@?@heatCapacity.Dmoles??molecularWeight.DmolFractionactivity.DpressuremolecularWeight.Dmoles / molexcessEnthalpy.DmolFraction??@&{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??Condenser duty ??Reboiler duty ?? Top pressure ??&{429DC999-9073-4549-8647-BA72D6BE7931}Pressure increase??Pressure?? Energy demand??Isentropic efficiency?TotalMassBalancePropertiesFraction? TotalFlowMass??&{E813F646-A25E-4B14-8873-4853D1AA3252}Pressure increase??Pressure?? Energy demand??Adiabatic efficiency?&{74475174-0CAC-48E0-93D5-90276104D854}Pressure difference??Pressure??COFE_ControllerdheatOfVaporizationheatOfVaporization.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 phaseMethanol and AcetoneVaporLiquid Liquid phaseMethanol and AcetoneLiquid VaporLiquiddefaultdefault material templateMethanol and AcetoneFeed0#000#00#0 defaultм@t@b@fff^ @?P+??j???P+??j??P+??j?t@м@b@fff^ @Methanol1D?D7D1D?D1D?D *defaultм@!<u@~i%R@ئH@أp= ?w4?{Gzt? CSUOz[ChemSep] Version=6.90 Compiled=2012-1-31 20:40 41769b34bc6e Name=C:\DOCUME~1\Harry\LOCALS~1\Temp\CS_46_~1.sep Title=ChemSep CO Unit Operation "Column" in COFE Flowsheet User=Harry Date=2012-02-02 Time=00:43:23 [Cape-Open] unitname=Column CO_ID=CS_48_1244_1CCE13B_4D7CDB10 2 components Methanol 67-56-1 32.0419998169 Mw Acetone 67-64-1 58.0800018311 Mw 1 thermo exe=C:\Program Files\ChemSepL6v90\bin\co-col2.exe mode=COFE NoWarnings=FALSE WilsonEstimate=TRUE Status= 1 Converged, 1 Iterations 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\chemsepl6v90\bin\ Help and Info path=c:\program files\chemsepl6v90\help\ Component data path=c:\program files\chemsepl6v90\pcd\ Property data path=c:\program files\chemsepl6v90\ipd\ Section data path=c:\program files\chemsepl6v90\ild\ Executables path=C:\Program Files\ChemSepL6v90\bin\ Temporary path=C:\DOCUME~1\Harry\LOCALS~1\Temp\ Scripts path=c:\program files\chemsepl6v90\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] 2 32 1101 Library Offset, Index DT=2012-01-31,09:17:24 CHK=37880 CAS=67-56-1 CID=Methanol Name=Methanol Lib=c:\program files\chemsepl6v90\pcd\chemsep1.pcd 62 1051 Library Offset, Index DT=2012-01-31,09:17:24 CHK=17876 CAS=67-64-1 CID=Acetone Name=Acetone Lib=c:\program files\chemsepl6v90\pcd\chemsep1.pcd [Operation] 2 Operation Column 1 Operation kind Simple Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 52 Stages 2 Feed stages 0 Sidestream stages F=37,42 S= 0 Pumparound stages P= [Properties] 350 BIP estimation temperature [Thermodynamics] 4 K model DECHEMA 8 * Activity coefficient UNIFAC * Wilson model * * UNIQUAC model * * Equation of State * * Cubic EOS * * Virial EOS * 1 Vapour pressure Antoine 0 Henry's law * Henry's default * [Enthalpy] 3 Enthalpy Excess 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 51 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] 2 Number 1 Feed state T & p 37 Stage Feed1{split} 320 Temperature 101325 Pressure 0 Vapour fraction 2 componentflows 0.075 Component 1 flow 0.075 Component 2 flow 1 Feed state T & p 42 Stage Feed2{split} 330.477551281 Temperature 101325 Pressure 0.334789971626 Vapour fraction 2 componentflows 0.0313180594662 Component 1 flow 0.0206801642431 Component 2 flow [Condenser] 7 Type Mole fraction of a component 0.75 Value Qcondenser 2 1st comp. * Type * * Initialization guess [Reboiler] 7 Type Mole fraction of a component 0.995 Value Qreboiler 1 1st comp. * Type * * Initialization guess [Monitored Variables] * [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 Liquid phase composition profiles On Vertical Black set label "ChemSep" at 1,2.02 right On Off StringGrid=StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 Liquid mole fraction 0 1 0.2 0 Off Off Off y1 Stage 52 1 10 0 Off Off Off x2 0 Off Off Off y2 0 Off Off Off StringGrid=StringGrid3 3 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage 1 Methanol X1 S x1 y1 _ Red Diamond Normal Solid 1 52 2 Acetone X2 S x1 y1 _ Green + Normal Solid 1 52 CheckBox=CheckBox10 0 Show settings ComboBox=ComboBox22 1 ComboBox=ComboBox23 0 StringGrid=StringGrid7 16 2 Title McCabe-Thiele diagram Acetone - Methanol Xlabel X Acetone/(Acetone+Methanol) Ylabel Y Acetone/(Acetone+Methanol) 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 -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 Title ComboBox=ComboBox4 0 ComboBox=ComboBox15 0 Edit=Edit17 Plot font CheckBox=CheckBox2 1 Color=Edit18 1241641 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 1241641 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 1241641 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 1241641 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 37,42 Edit=Edit6 Edit=Edit7 chemsep1.pcd Edit=Edit8 Edit=Edit5 StringGrid=StringGrid1 3 7 Identifier L# File Loc. CAS SMILES Name Methanol 1101 c:\program files\chemsepl6v90\pcd\chemsep1.pcd 32 67-56-1 CO Methanol Acetone 1051 c:\program files\chemsepl6v90\pcd\chemsep1.pcd 62 67-64-1 CC(=O)C Acetone 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 1 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 328.5377254 1.013250000E+05 1.270740579E-01 2.992409247E-01 -1.321188072E+07 2 328.5443679 1.013250000E+05 4.263149825E-01 2.987890442E-01 0.000000000E+00 3 328.5520974 1.013250000E+05 4.258631021E-01 2.983649569E-01 0.000000000E+00 4 328.5607193 1.013250000E+05 4.254390148E-01 2.979636953E-01 0.000000000E+00 5 328.5701018 1.013250000E+05 4.250377532E-01 2.975812234E-01 0.000000000E+00 6 328.5801569 1.013250000E+05 4.246552813E-01 2.972142087E-01 0.000000000E+00 7 328.5908287 1.013250000E+05 4.242882666E-01 2.968598586E-01 0.000000000E+00 8 328.6020850 1.013250000E+05 4.239339165E-01 2.965157918E-01 0.000000000E+00 9 328.6139112 1.013250000E+05 4.235898497E-01 2.961799601E-01 0.000000000E+00 10 328.6263072 1.013250000E+05 4.232540179E-01 2.958505685E-01 0.000000000E+00 11 328.6392843 1.013250000E+05 4.229246264E-01 2.955260293E-01 0.000000000E+00 12 328.6528632 1.013250000E+05 4.226000872E-01 2.952049190E-01 0.000000000E+00 13 328.6670730 1.013250000E+05 4.222789769E-01 2.948859467E-01 0.000000000E+00 14 328.6819505 1.013250000E+05 4.219600046E-01 2.945679291E-01 0.000000000E+00 15 328.6975388 1.013250000E+05 4.216419870E-01 2.942497676E-01 0.000000000E+00 16 328.7138878 1.013250000E+05 4.213238255E-01 2.939304393E-01 0.000000000E+00 17 328.7310535 1.013250000E+05 4.210044971E-01 2.936089841E-01 0.000000000E+00 18 328.7490978 1.013250000E+05 4.206830420E-01 2.932844885E-01 0.000000000E+00 19 328.7680884 1.013250000E+05 4.203585464E-01 2.929560926E-01 0.000000000E+00 20 328.7880987 1.013250000E+05 4.200301505E-01 2.926229778E-01 0.000000000E+00 21 328.8092074 1.013250000E+05 4.196970357E-01 2.922843702E-01 0.000000000E+00 22 328.8314982 1.013250000E+05 4.193584281E-01 2.919395428E-01 0.000000000E+00 23 328.8550593 1.013250000E+05 4.190136007E-01 2.915878211E-01 0.000000000E+00 24 328.8799825 1.013250000E+05 4.186618789E-01 2.912285926E-01 0.000000000E+00 25 328.9063623 1.013250000E+05 4.183026504E-01 2.908613136E-01 0.000000000E+00 26 328.9342944 1.013250000E+05 4.179353715E-01 2.904855300E-01 0.000000000E+00 27 328.9638735 1.013250000E+05 4.175595879E-01 2.901008882E-01 0.000000000E+00 28 328.9951912 1.013250000E+05 4.171749461E-01 2.897071623E-01 0.000000000E+00 29 329.0283326 1.013250000E+05 4.167812202E-01 2.893042729E-01 0.000000000E+00 30 329.0633725 1.013250000E+05 4.163783308E-01 2.888923126E-01 0.000000000E+00 31 329.1003713 1.013250000E+05 4.159663705E-01 2.884715795E-01 0.000000000E+00 32 329.1393695 1.013250000E+05 4.155456374E-01 2.880425959E-01 0.000000000E+00 33 329.1803821 1.013250000E+05 4.151166537E-01 2.876061379E-01 0.000000000E+00 34 329.2233924 1.013250000E+05 4.146801958E-01 2.871632546E-01 0.000000000E+00 35 329.2683462 1.013250000E+05 4.142373125E-01 2.867152832E-01 0.000000000E+00 36 329.3151460 1.013250000E+05 4.137893411E-01 2.862638473E-01 0.000000000E+00 37 329.3636461 1.013250000E+05 4.133379052E-01 4.414030611E-01 0.000000000E+00 38 329.3996144 1.013250000E+05 4.184771190E-01 4.408983776E-01 0.000000000E+00 39 329.4557200 1.013250000E+05 4.179724355E-01 4.401327482E-01 0.000000000E+00 40 329.5438646 1.013250000E+05 4.172068060E-01 4.389790354E-01 0.000000000E+00 41 329.6834324 1.013250000E+05 4.160530933E-01 4.372607976E-01 0.000000000E+00 42 329.8796090 1.013250000E+05 3.969263634E-01 4.701366557E-01 0.000000000E+00 43 330.1266538 1.013250000E+05 3.952124899E-01 4.674149306E-01 0.000000000E+00 44 330.5541757 1.013250000E+05 3.924907647E-01 4.633203741E-01 0.000000000E+00 45 331.2699138 1.013250000E+05 3.883962083E-01 4.577764925E-01 0.000000000E+00 46 332.3607680 1.013250000E+05 3.828523267E-01 4.514812007E-01 0.000000000E+00 47 333.7530652 1.013250000E+05 3.765570349E-01 4.458408031E-01 0.000000000E+00 48 335.1486880 1.013250000E+05 3.709166373E-01 4.418773630E-01 0.000000000E+00 49 336.2433199 1.013250000E+05 3.669531972E-01 4.395630008E-01 0.000000000E+00 50 336.9503326 1.013250000E+05 3.646388350E-01 4.383465184E-01 0.000000000E+00 51 337.3524721 1.013250000E+05 3.634223526E-01 4.377360734E-01 0.000000000E+00 52 337.5650611 1.013250000E+05 3.628119076E-01 7.492416582E-02 1.283538437E+07 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2888789E+08 -0.2888789E+08 -0.8731252E+05 -0.8731252E+05 2 0.2103003E+07 -0.2894195E+08 0.1138878E+05 -0.8740623E+05 3 0.2097959E+07 -0.2899267E+08 0.1142451E+05 -0.8749637E+05 4 0.2093326E+07 -0.2904066E+08 0.1145698E+05 -0.8758356E+05 5 0.2089032E+07 -0.2908639E+08 0.1148676E+05 -0.8766837E+05 6 0.2085020E+07 -0.2913028E+08 0.1151431E+05 -0.8775127E+05 7 0.2081245E+07 -0.2917264E+08 0.1154000E+05 -0.8783270E+05 8 0.2077669E+07 -0.2921377E+08 0.1156412E+05 -0.8791306E+05 9 0.2074261E+07 -0.2925391E+08 0.1158689E+05 -0.8799269E+05 10 0.2070996E+07 -0.2929328E+08 0.1160853E+05 -0.8807194E+05 11 0.2067852E+07 -0.2933207E+08 0.1162919E+05 -0.8815110E+05 12 0.2064810E+07 -0.2937045E+08 0.1164900E+05 -0.8823048E+05 13 0.2061855E+07 -0.2940857E+08 0.1166808E+05 -0.8831035E+05 14 0.2058973E+07 -0.2944659E+08 0.1168653E+05 -0.8839099E+05 15 0.2056152E+07 -0.2948461E+08 0.1170442E+05 -0.8847266E+05 16 0.2053382E+07 -0.2952279E+08 0.1172183E+05 -0.8855561E+05 17 0.2050653E+07 -0.2956121E+08 0.1173881E+05 -0.8864010E+05 18 0.2047959E+07 -0.2960001E+08 0.1175542E+05 -0.8872639E+05 19 0.2045291E+07 -0.2963928E+08 0.1177169E+05 -0.8881473E+05 20 0.2042645E+07 -0.2967912E+08 0.1178766E+05 -0.8890537E+05 21 0.2040015E+07 -0.2971962E+08 0.1180334E+05 -0.8899857E+05 22 0.2037397E+07 -0.2976087E+08 0.1181877E+05 -0.8909457E+05 23 0.2034787E+07 -0.2980297E+08 0.1183394E+05 -0.8919361E+05 24 0.2032183E+07 -0.2984597E+08 0.1184887E+05 -0.8929594E+05 25 0.2029583E+07 -0.2988995E+08 0.1186354E+05 -0.8940177E+05 26 0.2026986E+07 -0.2993497E+08 0.1187796E+05 -0.8951132E+05 27 0.2024392E+07 -0.2998107E+08 0.1189209E+05 -0.8962477E+05 28 0.2021802E+07 -0.3002828E+08 0.1190592E+05 -0.8974228E+05 29 0.2019218E+07 -0.3007662E+08 0.1191942E+05 -0.8986397E+05 30 0.2016642E+07 -0.3012607E+08 0.1193253E+05 -0.8998991E+05 31 0.2014079E+07 -0.3017662E+08 0.1194523E+05 -0.9012011E+05 32 0.2011533E+07 -0.3022819E+08 0.1195745E+05 -0.9025450E+05 33 0.2009009E+07 -0.3028071E+08 0.1196913E+05 -0.9039294E+05 34 0.2006516E+07 -0.3033405E+08 0.1198022E+05 -0.9053518E+05 35 0.2004059E+07 -0.3038805E+08 0.1199066E+05 -0.9068087E+05 36 0.2001647E+07 -0.3044254E+08 0.1200037E+05 -0.9082955E+05 37 0.1999290E+07 -0.3049727E+08 0.1200930E+05 -0.9098063E+05 38 0.1997626E+07 -0.3053680E+08 0.1201524E+05 -0.9109082E+05 39 0.1995161E+07 -0.3059679E+08 0.1202342E+05 -0.9125975E+05 40 0.1991574E+07 -0.3068725E+08 0.1203382E+05 -0.9151839E+05 41 0.1986494E+07 -0.3082211E+08 0.1204492E+05 -0.9191275E+05 42 0.1980332E+07 -0.3099688E+08 0.1205101E+05 -0.9243963E+05 43 0.1973772E+07 -0.3119664E+08 0.1204542E+05 -0.9306428E+05 44 0.1964517E+07 -0.3150000E+08 0.1200680E+05 -0.9406112E+05 45 0.1952233E+07 -0.3191876E+08 0.1187347E+05 -0.9554386E+05 46 0.1935923E+07 -0.3240984E+08 0.1152253E+05 -0.9747977E+05 47 0.1913115E+07 -0.3286840E+08 0.1080805E+05 -0.9957054E+05 48 0.1883859E+07 -0.3320429E+08 0.9728674E+04 -0.1014042E+06 49 0.1854745E+07 -0.3340726E+08 0.8526155E+04 -0.1027533E+06 50 0.1832597E+07 -0.3351654E+08 0.7486822E+04 -0.1036316E+06 51 0.1818735E+07 -0.3357222E+08 0.6734814E+04 -0.1041614E+06 52 0.1811021E+07 -0.3359991E+08 0.6247253E+04 -0.1044671E+06 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.5173207E+02 0.1919027E+01 0.8781162E-05 0.7152513E+05 0.1466758E-01 2 0.5157050E+02 0.1912995E+01 0.8794520E-05 0.7131899E+05 0.1469746E-01 3 0.5142043E+02 0.1907384E+01 0.8807005E-05 0.7112773E+05 0.1472534E-01 4 0.5127976E+02 0.1902116E+01 0.8818775E-05 0.7094864E+05 0.1475159E-01 5 0.5114683E+02 0.1897131E+01 0.8829960E-05 0.7077956E+05 0.1477650E-01 6 0.5102027E+02 0.1892379E+01 0.8840663E-05 0.7061874E+05 0.1480032E-01 7 0.5089897E+02 0.1887818E+01 0.8850974E-05 0.7046473E+05 0.1482323E-01 8 0.5078199E+02 0.1883415E+01 0.8860965E-05 0.7031633E+05 0.1484540E-01 9 0.5066853E+02 0.1879139E+01 0.8870700E-05 0.7017252E+05 0.1486699E-01 10 0.5055791E+02 0.1874966E+01 0.8880235E-05 0.7003241E+05 0.1488811E-01 11 0.5044952E+02 0.1870873E+01 0.8889618E-05 0.6989525E+05 0.1490887E-01 12 0.5034286E+02 0.1866840E+01 0.8898894E-05 0.6976035E+05 0.1492938E-01 13 0.5023743E+02 0.1862849E+01 0.8908101E-05 0.6962711E+05 0.1494971E-01 14 0.5013281E+02 0.1858886E+01 0.8917276E-05 0.6949500E+05 0.1496995E-01 15 0.5002861E+02 0.1854935E+01 0.8926452E-05 0.6936351E+05 0.1499018E-01 16 0.4992448E+02 0.1850981E+01 0.8935662E-05 0.6923220E+05 0.1501047E-01 17 0.4982007E+02 0.1847014E+01 0.8944935E-05 0.6910063E+05 0.1503087E-01 18 0.4971507E+02 0.1843020E+01 0.8954300E-05 0.6896840E+05 0.1505146E-01 19 0.4960919E+02 0.1838989E+01 0.8963784E-05 0.6883516E+05 0.1507229E-01 20 0.4950214E+02 0.1834909E+01 0.8973414E-05 0.6870055E+05 0.1509342E-01 21 0.4939366E+02 0.1830770E+01 0.8983214E-05 0.6856423E+05 0.1511490E-01 22 0.4928351E+02 0.1826563E+01 0.8993210E-05 0.6842590E+05 0.1513679E-01 23 0.4917144E+02 0.1822279E+01 0.9003425E-05 0.6828526E+05 0.1515914E-01 24 0.4905723E+02 0.1817909E+01 0.9013881E-05 0.6814205E+05 0.1518200E-01 25 0.4894071E+02 0.1813446E+01 0.9024600E-05 0.6799603E+05 0.1520540E-01 26 0.4882168E+02 0.1808882E+01 0.9035599E-05 0.6784698E+05 0.1522940E-01 27 0.4870001E+02 0.1804211E+01 0.9046896E-05 0.6769473E+05 0.1525402E-01 28 0.4857558E+02 0.1799430E+01 0.9058506E-05 0.6753914E+05 0.1527929E-01 29 0.4844832E+02 0.1794535E+01 0.9070439E-05 0.6738012E+05 0.1530524E-01 30 0.4831820E+02 0.1789525E+01 0.9082700E-05 0.6721766E+05 0.1533187E-01 31 0.4818525E+02 0.1784400E+01 0.9095293E-05 0.6705177E+05 0.1535919E-01 32 0.4804956E+02 0.1779165E+01 0.9108211E-05 0.6688260E+05 0.1538718E-01 33 0.4791130E+02 0.1773824E+01 0.9121444E-05 0.6671034E+05 0.1541582E-01 34 0.4777071E+02 0.1768388E+01 0.9134971E-05 0.6653530E+05 0.1544506E-01 35 0.4762811E+02 0.1762869E+01 0.9148765E-05 0.6635788E+05 0.1547485E-01 36 0.4748392E+02 0.1757282E+01 0.9162787E-05 0.6617862E+05 0.1550508E-01 37 0.4733866E+02 0.1751648E+01 0.9176990E-05 0.6599813E+05 0.1553567E-01 38 0.4723343E+02 0.1747564E+01 0.9187327E-05 0.6586747E+05 0.1555790E-01 39 0.4707318E+02 0.1741338E+01 0.9203144E-05 0.6566859E+05 0.1559188E-01 40 0.4683002E+02 0.1731880E+01 0.9227321E-05 0.6536705E+05 0.1564373E-01 41 0.4646333E+02 0.1717591E+01 0.9264175E-05 0.6491288E+05 0.1572253E-01 42 0.4597861E+02 0.1698662E+01 0.9313614E-05 0.6431335E+05 0.1582782E-01 43 0.4540743E+02 0.1676305E+01 0.9372901E-05 0.6360790E+05 0.1595342E-01 44 0.4449269E+02 0.1640411E+01 0.9470094E-05 0.6247969E+05 0.1615775E-01 45 0.4309420E+02 0.1585417E+01 0.9623733E-05 0.6075631E+05 0.1647664E-01 46 0.4113529E+02 0.1508382E+01 0.9848366E-05 0.5833943E+05 0.1693351E-01 47 0.3876859E+02 0.1415668E+01 0.1013303E-04 0.5540612E+05 0.1749618E-01 48 0.3644036E+02 0.1325109E+01 0.1042609E-04 0.5249980E+05 0.1805652E-01 49 0.3460683E+02 0.1254338E+01 0.1066550E-04 0.5019436E+05 0.1850053E-01 50 0.3341004E+02 0.1208420E+01 0.1082576E-04 0.4868127E+05 0.1879113E-01 51 0.3272334E+02 0.1182171E+01 0.1091912E-04 0.4781010E+05 0.1895806E-01 52 0.3235833E+02 0.1168248E+01 0.1096916E-04 0.4734614E+05 0.1904683E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.5157050E+02 0.7571059E+03 0.2663104E-03 0.1214202E+06 0.1594524E+00 0.1940852E-01 2 0.5135661E+02 0.7574426E+03 0.2673198E-03 0.1210556E+06 0.1598268E+00 0.1941074E-01 3 0.5115594E+02 0.7577536E+03 0.2682667E-03 0.1207139E+06 0.1601775E+00 0.1941265E-01 4 0.5096614E+02 0.7580435E+03 0.2691623E-03 0.1203911E+06 0.1605088E+00 0.1941432E-01 5 0.5078531E+02 0.7583158E+03 0.2700156E-03 0.1200838E+06 0.1608240E+00 0.1941579E-01 6 0.5061185E+02 0.7585734E+03 0.2708342E-03 0.1197893E+06 0.1611260E+00 0.1941708E-01 7 0.5044445E+02 0.7588187E+03 0.2716241E-03 0.1195053E+06 0.1614172E+00 0.1941823E-01 8 0.5028198E+02 0.7590536E+03 0.2723909E-03 0.1192300E+06 0.1616994E+00 0.1941924E-01 9 0.5012346E+02 0.7592798E+03 0.2731389E-03 0.1189615E+06 0.1619746E+00 0.1942015E-01 10 0.4996804E+02 0.7594986E+03 0.2738724E-03 0.1186985E+06 0.1622440E+00 0.1942095E-01 11 0.4981498E+02 0.7597113E+03 0.2745947E-03 0.1184397E+06 0.1625092E+00 0.1942166E-01 12 0.4966359E+02 0.7599190E+03 0.2753090E-03 0.1181839E+06 0.1627711E+00 0.1942228E-01 13 0.4951327E+02 0.7601224E+03 0.2760184E-03 0.1179301E+06 0.1630310E+00 0.1942283E-01 14 0.4936345E+02 0.7603225E+03 0.2767253E-03 0.1176773E+06 0.1632898E+00 0.1942330E-01 15 0.4921363E+02 0.7605198E+03 0.2774322E-03 0.1174247E+06 0.1635484E+00 0.1942370E-01 16 0.4906331E+02 0.7607150E+03 0.2781414E-03 0.1171715E+06 0.1638076E+00 0.1942404E-01 17 0.4891204E+02 0.7609087E+03 0.2788551E-03 0.1169168E+06 0.1640682E+00 0.1942430E-01 18 0.4875939E+02 0.7611012E+03 0.2795751E-03 0.1166600E+06 0.1643310E+00 0.1942449E-01 19 0.4860496E+02 0.7612931E+03 0.2803035E-03 0.1164004E+06 0.1645966E+00 0.1942461E-01 20 0.4844835E+02 0.7614846E+03 0.2810421E-03 0.1161373E+06 0.1648657E+00 0.1942467E-01 21 0.4828921E+02 0.7616760E+03 0.2817925E-03 0.1158702E+06 0.1651390E+00 0.1942464E-01 22 0.4812718E+02 0.7618676E+03 0.2825563E-03 0.1155984E+06 0.1654169E+00 0.1942454E-01 23 0.4796195E+02 0.7620595E+03 0.2833351E-03 0.1153215E+06 0.1657001E+00 0.1942436E-01 24 0.4779323E+02 0.7622518E+03 0.2841301E-03 0.1150389E+06 0.1659890E+00 0.1942410E-01 25 0.4762075E+02 0.7624446E+03 0.2849426E-03 0.1147503E+06 0.1662841E+00 0.1942374E-01 26 0.4744430E+02 0.7626378E+03 0.2857735E-03 0.1144553E+06 0.1665857E+00 0.1942328E-01 27 0.4726370E+02 0.7628312E+03 0.2866236E-03 0.1141536E+06 0.1668941E+00 0.1942272E-01 28 0.4707883E+02 0.7630247E+03 0.2874933E-03 0.1138451E+06 0.1672095E+00 0.1942206E-01 29 0.4688965E+02 0.7632179E+03 0.2883829E-03 0.1135297E+06 0.1675319E+00 0.1942127E-01 30 0.4669619E+02 0.7634104E+03 0.2892922E-03 0.1132074E+06 0.1678613E+00 0.1942037E-01 31 0.4649856E+02 0.7636017E+03 0.2902203E-03 0.1128785E+06 0.1681975E+00 0.1941934E-01 32 0.4629699E+02 0.7637912E+03 0.2911663E-03 0.1125433E+06 0.1685400E+00 0.1941817E-01 33 0.4609183E+02 0.7639781E+03 0.2921283E-03 0.1122026E+06 0.1688883E+00 0.1941686E-01 34 0.4588354E+02 0.7641618E+03 0.2931040E-03 0.1118570E+06 0.1692414E+00 0.1941542E-01 35 0.4567273E+02 0.7643412E+03 0.2940905E-03 0.1115076E+06 0.1695985E+00 0.1941383E-01 36 0.4546012E+02 0.7645155E+03 0.2950842E-03 0.1111556E+06 0.1699583E+00 0.1941210E-01 37 0.4524660E+02 0.7646837E+03 0.2960808E-03 0.1108025E+06 0.1703191E+00 0.1941023E-01 38 0.4509241E+02 0.7648009E+03 0.2967997E-03 0.1105477E+06 0.1705795E+00 0.1940880E-01 39 0.4485846E+02 0.7649718E+03 0.2978888E-03 0.1101617E+06 0.1709741E+00 0.1940650E-01 40 0.4450575E+02 0.7652132E+03 0.2995271E-03 0.1095805E+06 0.1715681E+00 0.1940274E-01 41 0.4397993E+02 0.7655359E+03 0.3019593E-03 0.1087163E+06 0.1724516E+00 0.1939643E-01 42 0.4329817E+02 0.7658856E+03 0.3050915E-03 0.1075999E+06 0.1735932E+00 0.1938700E-01 43 0.4251777E+02 0.7661855E+03 0.3086403E-03 0.1063281E+06 0.1748944E+00 0.1937438E-01 44 0.4132798E+02 0.7664211E+03 0.3139528E-03 0.1044027E+06 0.1768659E+00 0.1935105E-01 45 0.3966830E+02 0.7662526E+03 0.3210872E-03 0.1017495E+06 0.1795879E+00 0.1930912E-01 46 0.3767391E+02 0.7651593E+03 0.3290227E-03 0.9862526E+05 0.1828059E+00 0.1924091E-01 47 0.3572309E+02 0.7629548E+03 0.3357540E-03 0.9566128E+05 0.1858807E+00 0.1914939E-01 48 0.3419401E+02 0.7602713E+03 0.3399840E-03 0.9342630E+05 0.1882239E+00 0.1905464E-01 49 0.3319905E+02 0.7579894E+03 0.3420724E-03 0.9202734E+05 0.1897081E+00 0.1897893E-01 50 0.3262914E+02 0.7564665E+03 0.3429812E-03 0.9125022E+05 0.1905411E+00 0.1892952E-01 51 0.3232647E+02 0.7555886E+03 0.3433681E-03 0.9084568E+05 0.1909777E+00 0.1890127E-01 52 0.3217219E+02 0.7551217E+03 0.3435380E-03 0.9064182E+05 0.1911986E+00 0.1888629E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.243794916E+00 0.250000000E+00 0.255763532E+00 0.261165913E+00 0.266271318E+00 2 0.756205084E+00 0.750000000E+00 0.744236468E+00 0.738834087E+00 0.733728682E+00 Component Mole fractions on stages: 6 to 10 1 0.271131851E+00 0.275790499E+00 0.280283256E+00 0.284640695E+00 0.288889143E+00 2 0.728868149E+00 0.724209501E+00 0.719716744E+00 0.715359305E+00 0.711110857E+00 Component Mole fractions on stages: 11 to 15 1 0.293051562E+00 0.297148242E+00 0.301197322E+00 0.305215210E+00 0.309216902E+00 2 0.706948438E+00 0.702851758E+00 0.698802678E+00 0.694784790E+00 0.690783098E+00 Component Mole fractions on stages: 16 to 20 1 0.313216242E+00 0.317226114E+00 0.321258593E+00 0.325325061E+00 0.329436270E+00 2 0.686783758E+00 0.682773886E+00 0.678741407E+00 0.674674939E+00 0.670563730E+00 Component Mole fractions on stages: 21 to 25 1 0.333602389E+00 0.337833009E+00 0.342137111E+00 0.346523013E+00 0.350998269E+00 2 0.666397611E+00 0.662166991E+00 0.657862889E+00 0.653476987E+00 0.649001731E+00 Component Mole fractions on stages: 26 to 30 1 0.355569540E+00 0.360242422E+00 0.365021236E+00 0.369908788E+00 0.374906086E+00 2 0.644430460E+00 0.639757578E+00 0.634978764E+00 0.630091212E+00 0.625093914E+00 Component Mole fractions on stages: 31 to 35 1 0.380012038E+00 0.385223126E+00 0.390533094E+00 0.395932644E+00 0.401409189E+00 2 0.619987962E+00 0.614776874E+00 0.609466906E+00 0.604067356E+00 0.598590811E+00 Component Mole fractions on stages: 36 to 40 1 0.406946690E+00 0.412525601E+00 0.416566867E+00 0.422721304E+00 0.432060197E+00 2 0.593053310E+00 0.587474399E+00 0.583433133E+00 0.577278696E+00 0.567939803E+00 Component Mole fractions on stages: 41 to 45 1 0.446142940E+00 0.464758925E+00 0.486695131E+00 0.521826365E+00 0.575535951E+00 2 0.553857060E+00 0.535241075E+00 0.513304869E+00 0.478173635E+00 0.424464049E+00 Component Mole fractions on stages: 46 to 50 1 0.650768438E+00 0.741662499E+00 0.831079312E+00 0.901496728E+00 0.947459692E+00 2 0.349231562E+00 0.258337501E+00 0.168920688E+00 0.985032724E-01 0.525403077E-01 Component Mole fractions on stages: 51 to 52 1 0.973832796E+00 0.987851251E+00 2 0.261672035E-01 0.121487495E-01 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.250000000E+00 0.258214744E+00 0.265921491E+00 0.273210628E+00 0.280155640E+00 2 0.750000000E+00 0.741785256E+00 0.734078509E+00 0.726789372E+00 0.719844360E+00 Component Mole fractions on stages: 6 to 10 1 0.286817237E+00 0.293246329E+00 0.299486224E+00 0.305574273E+00 0.311543116E+00 2 0.713182763E+00 0.706753671E+00 0.700513776E+00 0.694425727E+00 0.688456884E+00 Component Mole fractions on stages: 11 to 15 1 0.317421645E+00 0.323235747E+00 0.329008886E+00 0.334762562E+00 0.340516670E+00 2 0.682578355E+00 0.676764253E+00 0.670991114E+00 0.665237438E+00 0.659483330E+00 Component Mole fractions on stages: 16 to 20 1 0.346289776E+00 0.352099334E+00 0.357961840E+00 0.363892932E+00 0.369907450E+00 2 0.653710224E+00 0.647900666E+00 0.642038160E+00 0.636107068E+00 0.630092550E+00 Component Mole fractions on stages: 21 to 25 1 0.376019439E+00 0.382242115E+00 0.388587770E+00 0.395067637E+00 0.401691693E+00 2 0.623980561E+00 0.617757885E+00 0.611412230E+00 0.604932363E+00 0.598308307E+00 Component Mole fractions on stages: 26 to 30 1 0.408468410E+00 0.415404450E+00 0.422504299E+00 0.429769857E+00 0.437199981E+00 2 0.591531590E+00 0.584595550E+00 0.577495701E+00 0.570230143E+00 0.562800019E+00 Component Mole fractions on stages: 31 to 35 1 0.444790004E+00 0.452531253E+00 0.460410591E+00 0.468410032E+00 0.476506472E+00 2 0.555209996E+00 0.547468747E+00 0.539589409E+00 0.531589968E+00 0.523493528E+00 Component Mole fractions on stages: 36 to 40 1 0.484671587E+00 0.492871951E+00 0.498793712E+00 0.507778485E+00 0.521324750E+00 2 0.515328413E+00 0.507128049E+00 0.501206288E+00 0.492221515E+00 0.478675250E+00 Component Mole fractions on stages: 41 to 45 1 0.541518935E+00 0.567702042E+00 0.597673621E+00 0.643368051E+00 0.707108733E+00 2 0.458481065E+00 0.432297958E+00 0.402326379E+00 0.356631949E+00 0.292891267E+00 Component Mole fractions on stages: 46 to 50 1 0.783704340E+00 0.858626411E+00 0.917351024E+00 0.955563008E+00 0.977450790E+00 2 0.216295660E+00 0.141373589E+00 0.826489760E-01 0.444369917E-01 0.225492095E-01 Component Mole fractions on stages: 51 to 52 1 0.989074851E+00 0.995000000E+00 2 0.109251489E-01 0.500000000E-02 [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 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 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 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 Component reaction rates on stages: 21 to 25 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 Component reaction rates on stages: 26 to 30 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 Component reaction rates on stages: 31 to 35 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 Component reaction rates on stages: 36 to 40 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 Component reaction rates on stages: 41 to 45 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 Component reaction rates on stages: 46 to 50 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 Component reaction rates on stages: 51 to 52 1 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 [Condenser Heat Duty] -1.321188072E+07 [Reboiler Heat Duty] 1.283538437E+07 [UA Column] 0.000000000E+00 [K-values] Component K-values on stages: 1 to 5 1 0.975179663E+00 0.968186388E+00 0.961800907E+00 0.955914180E+00 0.950440682E+00 2 0.100827345E+01 0.101107429E+01 0.101383770E+01 0.101657250E+01 0.101928795E+01 Component K-values on stages: 6 to 10 1 0.945312261E+00 0.940473832E+00 0.935880294E+00 0.931494308E+00 0.927284629E+00 2 0.102199350E+01 0.102469861E+01 0.102741269E+01 0.103014516E+01 0.103290543E+01 Component K-values on stages: 11 to 15 1 0.923224886E+00 0.919292635E+00 0.915468653E+00 0.911736390E+00 0.908081542E+00 2 0.103570298E+01 0.103854740E+01 0.104144848E+01 0.104441625E+01 0.104746104E+01 Component K-values on stages: 16 to 20 1 0.904491741E+00 0.900956301E+00 0.897466035E+00 0.894013134E+00 0.890591066E+00 2 0.105059357E+01 0.105382495E+01 0.105716677E+01 0.106063110E+01 0.106423053E+01 Component K-values on stages: 21 to 25 1 0.887194529E+00 0.883819431E+00 0.880462889E+00 0.877123258E+00 0.873800169E+00 2 0.106797816E+01 0.107188756E+01 0.107597273E+01 0.108024802E+01 0.108472793E+01 Component K-values on stages: 26 to 30 1 0.870494588E+00 0.867208865E+00 0.863946797E+00 0.860713664E+00 0.857516246E+00 2 0.108942696E+01 0.109435930E+01 0.109953851E+01 0.110497703E+01 0.111068566E+01 Component K-values on stages: 31 to 35 1 0.854362809E+00 0.851263031E+00 0.848227869E+00 0.845269352E+00 0.842400288E+00 2 0.111667291E+01 0.112294424E+01 0.112950124E+01 0.113634077E+01 0.114345408E+01 Component K-values on stages: 36 to 40 1 0.839633888E+00 0.836983320E+00 0.835148593E+00 0.832491561E+00 0.828773613E+00 2 0.115082595E+01 0.115843405E+01 0.116405789E+01 0.117280265E+01 0.118648249E+01 Component K-values on stages: 41 to 45 1 0.823873205E+00 0.818666995E+00 0.814315897E+00 0.811085294E+00 0.813928501E+00 2 0.120802603E+01 0.123813001E+01 0.127584194E+01 0.134080426E+01 0.144922057E+01 Component K-values on stages: 46 to 50 1 0.830374931E+00 0.863777877E+00 0.905955616E+00 0.943419450E+00 0.969317025E+00 2 0.161460273E+01 0.182733920E+01 0.204383280E+01 0.221669534E+01 0.233002880E+01 Component K-values on stages: 51 to 52 1 0.984589584E+00 0.992815327E+00 2 0.239513472E+01 0.242974989E+01 [Molecular weights] 1 32.042 2 58.080 [Feed stream 1] 37 Stage Number 1.5000000000000E-01 Flow rate 3.2000000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.1710458484833E+07 Enthalpy [J/kmol] -9.3780181307306E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 5.0000000000000E-01 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 1.5000000000000E-01 Flow rate 5.0000000000000E-01 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 4.5061000823975E+01 Molar mass 7.7643118573676E+02 Density 3.2442594711447E-04 Viscosity 1.7376930861498E-01 Thermal conductivity 1.0818250825980E+05 Heat capacity 2.0381466192264E-02 Surface tension [Feed stream 2] 42 Stage Number 5.1998223709300E-02 Flow rate 3.3054999842009E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.0294560516474E+07 Enthalpy [J/kmol] -8.2044495796183E+04 Entropy [J/kmol/K] 3.3478997162600E-01 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 6.0229094826943E-01 Mole fraction of component 1 3.9770905173057E-01 Mole fraction of component 2 1.7408483840239E-02 Flow rate 5.2149669042811E-01 Mole fraction of component 1 4.7850330957189E-01 Mole fraction of component 2 3.4589739869061E-02 Flow rate 6.4295345518997E-01 Mole fraction of component 1 3.5704654481003E-01 Mole fraction of component 2 4.4501269955310E+01 Molar mass 1.6407478266621E+00 Density 9.4691690528050E-06 Viscosity 1.6155818219242E-02 Thermal conductivity 6.2490271203196E+04 Heat capacity 4.1338778469807E+01 Molar mass 7.6642022861756E+02 Density 3.1390518660812E-04 Viscosity 1.7684808892347E-01 Thermal conductivity 1.0442008029412E+05 Heat capacity 1.9351285837365E-02 Surface tension [Reflashed Feed stream 1] 37 Stage Number 1.5000000000000E-01 Flow rate 3.2000000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.1710458484833E+07 Enthalpy [J/kmol] -9.3780181307306E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 5.0000000000000E-01 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 1.5000000000000E-01 Flow rate 5.0000000000000E-01 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 4.5061000823975E+01 Molar mass 7.7643118573676E+02 Density 3.2442594711447E-04 Viscosity 1.7376930861498E-01 Thermal conductivity 1.0818250825980E+05 Heat capacity 2.0381466192264E-02 Surface tension [Reflashed Feed stream 2] 42 Stage Number 5.1998223709300E-02 Flow rate 3.3054998015895E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.0294560516474E+07 Enthalpy [J/kmol] -8.2044517154318E+04 Entropy [J/kmol/K] 3.3479013009849E-01 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 6.0229094826943E-01 Mole fraction of component 1 3.9770905173057E-01 Mole fraction of component 2 1.7408492080527E-02 Flow rate 5.2149524876397E-01 Mole fraction of component 1 4.7850475123603E-01 Mole fraction of component 2 3.4589731628773E-02 Flow rate 6.4295420955424E-01 Mole fraction of component 1 3.5704579044576E-01 Mole fraction of component 2 4.4501307493363E+01 Molar mass 1.6407493013211E+00 Density 9.4691650102576E-06 Viscosity 1.6155809761041E-02 Thermal conductivity 6.2490317474451E+04 Heat capacity 4.1338758827669E+01 Molar mass 7.6642026278628E+02 Density 3.1390535033597E-04 Viscosity 1.7684812943061E-01 Thermal conductivity 1.0442004191975E+05 Heat capacity 1.9351287968209E-02 Surface tension [Top product] 1 Stage Number 1.2707405788529E-01 Flow rate 3.2853772541232E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.8887887229572E+07 Enthalpy [J/kmol] -8.7312516771893E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.5000000000001E-01 Mole fraction of component 1 7.5000000000002E-01 Mole fraction of component 2 1.2707405788529E-01 Flow rate 2.5000000000001E-01 Mole fraction of component 1 7.5000000000002E-01 Mole fraction of component 2 5.1570501327516E+01 Molar mass 7.5710588442053E+02 Density 2.6631044074663E-04 Viscosity 1.5945235388795E-01 Thermal conductivity 1.2142017437923E+05 Heat capacity 1.9408520081000E-02 Surface tension [Bottom product] 52 Stage Number 7.4924165824011E-02 Flow rate 3.3756506109397E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -3.3599909082589E+07 Enthalpy [J/kmol] -1.0446707452715E+05 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9499999999996E-01 Mole fraction of component 1 4.9999999999998E-03 Mole fraction of component 2 7.4924165824011E-02 Flow rate 9.9499999999996E-01 Mole fraction of component 1 4.9999999999998E-03 Mole fraction of component 2 3.2172189826964E+01 Molar mass 7.5512174715948E+02 Density 3.4353801657585E-04 Viscosity 1.9119861477082E-01 Thermal conductivity 9.0641817245977E+04 Heat capacity 1.8886293281003E-02 Surface tension [Equilibrium Data at 1.01325E+05 Pa] Temperature X(1) Y(1) 329.401 0.0000000 0.0000000 329.190 0.0250000 0.0316930 329.015 0.0500000 0.0611298 328.872 0.0750000 0.0886090 328.758 0.1000000 0.1143853 328.669 0.1250000 0.1386777 328.604 0.1500000 0.1616763 328.560 0.1750000 0.1835477 328.535 0.2000000 0.2044392 328.528 0.2250000 0.2244822 328.538 0.2500000 0.2437949 328.563 0.2750000 0.2624852 328.603 0.3000000 0.2806520 328.657 0.3250000 0.2983876 328.725 0.3500000 0.3157788 328.806 0.3750000 0.3329083 328.900 0.4000000 0.3498561 329.006 0.4250000 0.3667003 329.126 0.4500000 0.3835187 329.260 0.4750000 0.4003892 329.407 0.5000000 0.4173915 329.569 0.5250000 0.4346079 329.745 0.5500000 0.4521245 329.937 0.5750000 0.4700328 330.147 0.6000000 0.4884306 330.375 0.6250000 0.5074243 330.622 0.6500000 0.5271304 330.890 0.6750000 0.5476779 331.182 0.7000000 0.5692110 331.500 0.7250000 0.5918921 331.845 0.7500000 0.6159058 332.222 0.7750000 0.6414637 332.633 0.8000000 0.6688100 333.081 0.8250000 0.6982290 333.573 0.8500000 0.7300536 334.112 0.8750000 0.7646774 334.703 0.9000000 0.8025685 335.355 0.9250000 0.8442886 336.073 0.9500000 0.8905168 336.868 0.9750000 0.9420811 337.749 1.0000000 1.0000000 [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlash AutoDUseOnlyKValuesAndEnthalpyFromCOSE*RestartDataAvailable,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts UseInitialGuess(Temperature profile4Temperature at each stage4򅚈t@wt@NSdՈt@̴t@@#t@RHt@tt@#t@_ꌔ҉t@ӲZt@,:t@1̮ rt@Tt@oDt@q)t@7 lt@'et@Mt@Jt@Ra t@jut@zMt@@Rt@֨ht@=Mut@`Mt@lt@FMt@f tt@tt@Pt@H:t@DWt@t@b%Kt@r7 t@~ѕt@,dt@!Jt@<]t@nVt@Gt@"t@λVݨt@!Qt@t@\ t@at@uOhu@*4u@ ȹu@ } u@"Pressure profile.Pressure at each stage4м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@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 stage4X]_@+ z@%Dϝz@\b4z@uz@>|z@x8pz@mR~z@0=pyz@utz@KP Enz@+ iz@n]{vdz@'-\_z@P)EZz@c.Uz@kPz@rJz@a&Ez@T7{@z@P';z@{w5z@>^70z@VT*z@!$z@!Hz@qz@!Hz@ z@ј z@@vy@GHy@R'Ey@y@&1y@8"$y@`rHhy@TG'z@߆z@Oz@02\xz@ambx@3[fx@,ڇx@vVFx@ `R!w@cmw@ߋ.w@9 K@v@ 8v@v@Ғv@(Liquid Flow profile4Liquid Flow at each stage4Ǵڳr@쟬r@1 ֥r@LKkr@jLr@Lfmr@br@@r@[r@ (}r@jxr@D5%YGsr@gr,nr@&<ir@O cr@Q^r@fYr@i9CTr@)'LOr@%ґIr@OOnjDr@^?r@ag9r@ѶP3r@-r@'r@e%R@Duties profile*Duties at each stage4q= 3i= G{hA4Vapour Moleweight profile@Vapour Moleweight at each stage40BxI@/$I@ vеI@O],ϣI@- PS˒I@5I@ rsI@G?dI@2dUI@AJiGI@r߉9I@#+I@n2dI@wJI@V+~I@.R\UH@"7 H@,iH@nH@FH@&lscH@c AJH@H@, PSH@n/ixH@~k,iH@o|YH@IH@Eb9H@)Ǻ(H@ʡEH@JiWH@"lxzG@YG@1%eG@.G@O;5YG@G@S\U]G@Qi>jG@eN;G@ĬCF@c&F@{Fw?F@@߾E@.QD@.9(abC@;k]8B@MA@0|@@g\@@}-@@.Vapour Density profile:Vapour Density at each stage4AҧU?&?^?b,/o? Z?13/G?Sͬ4?û\w"?5Z?}1Y?߆?խ?M.:?H??JRЭ?,G@?T^?}?B˺l?Q-"[?{{J?V9?XS(??a'??N+@.?UZ ?|w?pUj?e?鷯?euw?+MFa?8*7QK?4?p?3 ?ͫ:?EVapour Viscosity at each stage4(.Yj>q> 9x>~4~>d+v>*xK>*ԏ>8I1>}k>y4>8p˓>Ѭ>[0> m>8Z>tL>YF>.M>ue>JH>>^1>FO>$_J>UZ >>BE>U>MD?>@Ȥ>8 _< >?@+>E9>2 !>GL(>鯴/>-;7>>>8vhD>zL>trWY>FKm>ʾw\5> U > 7>!mʳ.>՝M>D !@>v>p(]>= >nml(>|">:Vapour Heat capacity profileFVapour Heat capacity at each stage4 ܺQ@pUjQ@-s,Q@[닄Q@DQOQ@.oQ@"Q@//>Q@yS Q@dQ@KyQ@ pQ@?"hQ@Hz_Q@6qrCWQ@ec]NQ@ǿϸpFQ@\C=Q@ZBs5Q@ͪ,Q@[%X$Q@sAQ@ض(AQ@eX Q@oP@n4P@4ctvP@EP@#SP@oi5$P@~:3PP@ܵ|P@B5vP@ cZBP@P@VnP@ʦ\P@䠄wP@-jP@H}WP@ KW[G@1PNG@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stage4xJC ?c.F?ǭQ(?+y6?A$C? rRO?@[?Cg?rW?ȥÄ?h}?,٬@Gz‡@(ć@QŇ@oELJ@Aȇ@DXʇ@"uˇ@ rh͇@D·@"yЇ@鷯҇@jqӇ@6Շ@{/Lև@2؇@cZBه@:Hۇ@H܇@d`Tއ@&߇@c]K@)Ǻ@v@47x@ZB>h@?@3@ioI@s@Dl{@Bi^@&S@?F@ı.nׇ@=U+‡@MJꯇ@Zd@hs@c=@2Liquid Viscosity profile>Liquid Viscosity at each stage44eus1?Lo1?Ĕ1?Fˣ1?+1?rؿ1?U1?ӱ1?2F1?S1?^A1?;& 2?iG2?ҿ "2?;9.2?Dw7p:2?%iF2?aI}R2?Uj]^2?6ؠk2?ϼ^w2?Y2?2?K|2?%2?){2?q2?:ARV2?^@C2?2?uw3?mw3?~%3?%x53??S^F3?V3?x\Zig3?:Eys3?]b3?صH;3?wQ 3?~3?Jx:4?>,A4? 5?s5?us6?A)G6?[Wk6?^1 Ez6?€6?9y6?:Liquid Heat capacity profileFLiquid Heat capacity at each stage4qZ^@jMC^@R'-^@]K^@٬\^@%]@ΪV]@Q]@K7]@bX9]@Gx $]@oŋ]@&†{]@,eXk]@H.[]@"J]@C>٬:]@ ףp=*]@`TR']@jo]@>W[\@J{/L\@jt\@lV}\@J\@w#\@*ԉ\@`vOv\@=,Ԛa\@/L FM\@NbX98\@\m"\@ۊe \@+[@ܵ|[@}гY[@(\[@;M [@JY[@x&e[@-[@7dZ@Tt$Z@Y8Z@oY@߄BX@_YiRW@;H[W@wEW@3V@gV@z1V@:Liquid Thermal cond. profileFLiquid Thermal cond. at each stage4eh?V_4u? B?/\g?E4~?DƟ?Q?3dᐲ?.l?qPi?I??{&3?כb?j'?: k?#/?h\W?2[?ݺQ?%VF#?uTڇa,?8/5?t? ??2"!H?*"R?.\?8N g?oq?8z|?Hm~??$!?hó?yUg?X1?+1*??Dz?D?I? lgNM8?t b?#?~?A /f?8S?li?fZH?cc?Sq??2y?0Surface tension profile<Surface tension at each stage44ߓ?eh?wȃ?tX?M?U.?P/[_?J"?ɝ4?Bm?"E?\%o?D?W ?q?g9B?.?{y*u?M ?؊?s% ?(?mȻ?UI?YC ?42A?_&̬?sb`?s]+?J?>ة??n6o?PBb?IZ?2wV?Number of stagesNSi Feed1 stageF1Ni Reflux ratioRRoCondenser duty QCo?@@J/sReboiler duty QRo?@@J/s Feed2 stageF2Ni Top pressure PPTi?N/m2 1 Converged 1 Iterations ChemSep (TM) - COL2 6.90 Copyright (c) 1988-2012 Harry Kooijman and Ross Taylor License: 2100- 6 LITE free license Build: 6494e2b69d23 Checking data file C:\DOCUME~1\Harry\LOCALS~1\Temp\CS_46_~1.SEP Cape Open unit name: C1 Cape-Open unit id: CS_46_4F4_1CCE13B_454128C0 Cape-Open run level: normal Cape open Initialized Cape Open Thermodynamic-properties disabled Reading configuration Reading component property libraries Reading thermodynamic property options Reading physical property options Reading thermodynamic property data Reading specifications Reading reaction data Checking Component Data 67-56-1 Methanol 67-64-1 Acetone * No class Determining feed conditions Solving TP flash Possible trivial solution Solving PV flash Run level: Initialization Reading initial temperature profiles Reading initial composition profiles Init 110 milliseconds Run level: Complete model Iteration log(Err/Tol) 0 0.9163 1 -2.5926 Run level: Report Convergence obtained in 1 iterations Generating equilibrium data Time 46 milliseconds FixMem driver done run time: 0.27 seconds Using: C:\Program Files\ChemSepL6v90\bin\co-col2.exe CAPE-OPEN thermo-properties were disabled. All calculation methods have been determined by ChemSep. See output report or graphical user interface for more information. #1F not all ports are connectedFeed2{split}_stage42Feed1{split}_stage37 TopProduct BottomProduct @ @0@@ @ @ @(@ @(@$@,@@@@@@@@$@@(@@(@ @(@ @ @ @,@$@@@$@@(@ @,@ @ @,@ @$@0@,@4@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@$@4@,@0@@ 4@,@0@ 4@,@0@4@,@0@ 4@,@0@ 4@,@0@ ,@0@  ,@0@@-@Pump_3>Pump - unit increasing the pressure due to the work performed.F^KsHSѪ2RhCOUSCOUS0002Pressure spec.$Pressure increase specification typePressurePressure increasePressure increasePressure Energy spec. Energy demand specification type Efficiency Efficiency Energy demand EfficiencyEnergy specification streamPressure increasePressure increase??j+A _BPressureOutlet pressure?.Aj@ _B Energy demandEnergy consumed by the pump@?@gϘ@@xDAdiabatic efficiencyPump adiabatic efficiency???Thermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last run+++ specifications +++ Pressure: 1013250 Pa Adiabatic efficiency: 0.75 +++ optional parameters +++ Pressure increase: 911925 Pa Energy demand: 10519.1938295363 W Adiabatic efficiency: 0.75 ;2?6 $not all material ports are connectedInletOutlet@@?K(^&?@@@@?:t= @@?:t= @@?:t= @@?:t= @@?:t= @@@C2ChemSep Unit OperationqeWCXcCSUO[ChemSep] Version=6.90 Compiled=2012-1-31 20:40 41769b34bc6e Name=C:\DOCUME~1\Harry\LOCALS~1\Temp\CS_47_~1.sep Title=ChemSep CO Unit Operation "Column" in COFE Flowsheet User=Harry Date=2012-02-02 Time=00:43:28 [Cape-Open] unitname=Column CO_ID=CS_49_1244_1CCE13B_4E5A90E0 2 components Methanol 67-56-1 32.0419998169 Mw Acetone 67-64-1 58.0800018311 Mw 1 thermo exe=C:\Program Files\ChemSepL6v90\bin\co-col2.exe mode=COFE NoWarnings=FALSE WilsonEstimate=TRUE Status= 1 Converged, 1 Iterations 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\chemsepl6v90\bin\ Help and Info path=c:\program files\chemsepl6v90\help\ Component data path=c:\program files\chemsepl6v90\pcd\ Property data path=c:\program files\chemsepl6v90\ipd\ Section data path=c:\program files\chemsepl6v90\ild\ Executables path=C:\Program Files\ChemSepL6v90\bin\ Temporary path=C:\DOCUME~1\Harry\LOCALS~1\Temp\ Scripts path=c:\program files\chemsepl6v90\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] 2 32 1101 Library Offset, Index DT=2012-01-31,09:17:24 CHK=37880 CAS=67-56-1 CID=Methanol Name=Methanol Lib=c:\program files\chemsepl6v90\pcd\chemsep1.pcd 62 1051 Library Offset, Index DT=2012-01-31,09:17:24 CHK=17876 CAS=67-64-1 CID=Acetone Name=Acetone Lib=c:\program files\chemsepl6v90\pcd\chemsep1.pcd [Operation] 2 Operation Column 1 Operation kind Simple Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 62 Stages 1 Feed stages 0 Sidestream stages F=41 S= 0 Pumparound stages P= [Properties] 350 BIP estimation temperature [Thermodynamics] 4 K model DECHEMA 8 * Activity coefficient UNIFAC * Wilson model * * UNIQUAC model * * Equation of State * * Cubic EOS * * Virial EOS * 1 Vapour pressure Antoine 0 Henry's law * Henry's default * [Enthalpy] 3 Enthalpy Excess 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 61 Last stage 0 Qcolumn lost to surroundings [Efficiencies] 1 Default efficiency 0 Number [Pressures] 1 Column pressure Constant pressure 1013200 Condenser pressure 1013200 Top pressure * Pressure Drop * Bottom pressure [Feeds] 1 Number 1 Feed state T & p 41 Stage Feed1{split} 328.87255374 Temperature 1013250 Pressure 0 Vapour fraction 2 componentflows 0.0317685144713 Component 1 flow 0.095305543414 Component 2 flow [Condenser] 1 Type Reflux ratio 3.11 Value Qcondenser * Type * * Initialization guess [Reboiler] 7 Type Mole fraction of a component 0.994 Value Qreboiler 2 1st comp. * Type * * Initialization guess [Monitored Variables] * [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 Temperature profile On Vertical Black set label "ChemSep" at 418.0459,2.22 right On Off StringGrid=StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 Temperature (K) 405.4396 418.0459 2 0 Off Off Off y1 Stage 62 1 10 0 Off Off Off x2 0 Off Off Off y2 0 Off Off Off StringGrid=StringGrid3 2 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage 1 T T S x1 y1 K Red Diamond Normal Solid 1 62 CheckBox=CheckBox10 0 Show settings ComboBox=ComboBox22 0 ComboBox=ComboBox23 1 StringGrid=StringGrid7 16 2 Title McCabe-Thiele diagram Methanol - Acetone Xlabel X Methanol/(Methanol+Acetone) Ylabel Y Methanol/(Methanol+Acetone) 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 0 ComboBox=ComboBox76 1 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 Title ComboBox=ComboBox4 0 ComboBox=ComboBox15 0 Edit=Edit17 Plot font CheckBox=CheckBox2 1 Color=Edit18 1241641 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 1241641 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 1241641 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 1241641 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 41 Edit=Edit6 Edit=Edit7 chemsep1.pcd Edit=Edit8 Edit=Edit5 StringGrid=StringGrid1 3 7 Identifier L# File Loc. CAS SMILES Name Methanol 1101 c:\program files\chemsepl6v90\pcd\chemsep1.pcd 32 67-56-1 CO Methanol Acetone 1051 c:\program files\chemsepl6v90\pcd\chemsep1.pcd 62 67-64-1 CC(=O)C Acetone 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 1 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 407.2405061 1.013200000E+06 5.199822371E-02 1.617144757E-01 -5.796322471E+06 2 407.2431643 1.013200000E+06 2.137126994E-01 1.618986750E-01 0.000000000E+00 3 407.2466875 1.013200000E+06 2.138968987E-01 1.620874333E-01 0.000000000E+00 4 407.2511440 1.013200000E+06 2.140856570E-01 1.622813466E-01 0.000000000E+00 5 407.2566139 1.013200000E+06 2.142795703E-01 1.624810319E-01 0.000000000E+00 6 407.2631913 1.013200000E+06 2.144792556E-01 1.626871319E-01 0.000000000E+00 7 407.2709849 1.013200000E+06 2.146853556E-01 1.629003134E-01 0.000000000E+00 8 407.2801196 1.013200000E+06 2.148985371E-01 1.631212691E-01 0.000000000E+00 9 407.2907384 1.013200000E+06 2.151194928E-01 1.633507148E-01 0.000000000E+00 10 407.3030038 1.013200000E+06 2.153489385E-01 1.635893879E-01 0.000000000E+00 11 407.3170994 1.013200000E+06 2.155876116E-01 1.638380432E-01 0.000000000E+00 12 407.3332316 1.013200000E+06 2.158362669E-01 1.640974437E-01 0.000000000E+00 13 407.3516304 1.013200000E+06 2.160956675E-01 1.643683495E-01 0.000000000E+00 14 407.3725507 1.013200000E+06 2.163665732E-01 1.646515034E-01 0.000000000E+00 15 407.3962716 1.013200000E+06 2.166497271E-01 1.649476129E-01 0.000000000E+00 16 407.4230957 1.013200000E+06 2.169458366E-01 1.652573202E-01 0.000000000E+00 17 407.4533456 1.013200000E+06 2.172555439E-01 1.655811736E-01 0.000000000E+00 18 407.4873591 1.013200000E+06 2.175793973E-01 1.659195860E-01 0.000000000E+00 19 407.5254812 1.013200000E+06 2.179178097E-01 1.662727950E-01 0.000000000E+00 20 407.5680528 1.013200000E+06 2.182710187E-01 1.666408035E-01 0.000000000E+00 21 407.6153950 1.013200000E+06 2.186390272E-01 1.670233302E-01 0.000000000E+00 22 407.6677896 1.013200000E+06 2.190215539E-01 1.674197465E-01 0.000000000E+00 23 407.7254553 1.013200000E+06 2.194179702E-01 1.678290253E-01 0.000000000E+00 24 407.7885200 1.013200000E+06 2.198272490E-01 1.682496937E-01 0.000000000E+00 25 407.8569917 1.013200000E+06 2.202479174E-01 1.686797975E-01 0.000000000E+00 26 407.9307296 1.013200000E+06 2.206780212E-01 1.691168992E-01 0.000000000E+00 27 408.0094196 1.013200000E+06 2.211151229E-01 1.695580935E-01 0.000000000E+00 28 408.0925578 1.013200000E+06 2.215563172E-01 1.700000688E-01 0.000000000E+00 29 408.1794462 1.013200000E+06 2.219982925E-01 1.704392020E-01 0.000000000E+00 30 408.2692041 1.013200000E+06 2.224374257E-01 1.708716822E-01 0.000000000E+00 31 408.3607969 1.013200000E+06 2.228699059E-01 1.712936754E-01 0.000000000E+00 32 408.4530805 1.013200000E+06 2.232918991E-01 1.717014892E-01 0.000000000E+00 33 408.5448591 1.013200000E+06 2.236997129E-01 1.720917436E-01 0.000000000E+00 34 408.6349490 1.013200000E+06 2.240899673E-01 1.724615212E-01 0.000000000E+00 35 408.7222418 1.013200000E+06 2.244597449E-01 1.728084791E-01 0.000000000E+00 36 408.8057598 1.013200000E+06 2.248067028E-01 1.731309264E-01 0.000000000E+00 37 408.8846978 1.013200000E+06 2.251291502E-01 1.734278487E-01 0.000000000E+00 38 408.9584475 1.013200000E+06 2.254260724E-01 1.736988819E-01 0.000000000E+00 39 409.0266050 1.013200000E+06 2.256971056E-01 1.739442568E-01 0.000000000E+00 40 409.0889629 1.013200000E+06 2.259424805E-01 1.741647145E-01 0.000000000E+00 41 409.1454898 1.013200000E+06 2.261629382E-01 3.624248767E-01 0.000000000E+00 42 409.1579848 1.013200000E+06 2.873490425E-01 3.625145982E-01 0.000000000E+00 43 409.1761624 1.013200000E+06 2.874387640E-01 3.626445557E-01 0.000000000E+00 44 409.2025919 1.013200000E+06 2.875687215E-01 3.628323174E-01 0.000000000E+00 45 409.2409842 1.013200000E+06 2.877564833E-01 3.631026224E-01 0.000000000E+00 46 409.2966734 1.013200000E+06 2.880267882E-01 3.634897313E-01 0.000000000E+00 47 409.3772622 1.013200000E+06 2.884138971E-01 3.640399823E-01 0.000000000E+00 48 409.4934284 1.013200000E+06 2.889641481E-01 3.648138252E-01 0.000000000E+00 49 409.6597838 1.013200000E+06 2.897379910E-01 3.658858319E-01 0.000000000E+00 50 409.8954086 1.013200000E+06 2.908099978E-01 3.673400761E-01 0.000000000E+00 51 410.2231469 1.013200000E+06 2.922642419E-01 3.692572513E-01 0.000000000E+00 52 410.6660059 1.013200000E+06 2.941814171E-01 3.716906319E-01 0.000000000E+00 53 411.2388180 1.013200000E+06 2.966147977E-01 3.746324239E-01 0.000000000E+00 54 411.9356092 1.013200000E+06 2.995565897E-01 3.779814575E-01 0.000000000E+00 55 412.7190583 1.013200000E+06 3.029056233E-01 3.815335357E-01 0.000000000E+00 56 413.5231591 1.013200000E+06 3.064577015E-01 3.850154442E-01 0.000000000E+00 57 414.2735621 1.013200000E+06 3.099396100E-01 3.881604908E-01 0.000000000E+00 58 414.9138038 1.013200000E+06 3.130846566E-01 3.907873877E-01 0.000000000E+00 59 415.4195314 1.013200000E+06 3.157115535E-01 3.928355232E-01 0.000000000E+00 60 415.7952452 1.013200000E+06 3.177596891E-01 3.943454339E-01 0.000000000E+00 61 416.0618594 1.013200000E+06 3.192695998E-01 3.954120764E-01 0.000000000E+00 62 416.2449648 1.013200000E+06 3.203362422E-01 7.507583418E-02 7.417289951E+06 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2033255E+08 -0.2033255E+08 -0.7503142E+05 -0.7503142E+05 2 0.6789479E+07 -0.2028256E+08 0.5752966E+04 -0.7488007E+05 3 0.6803963E+07 -0.2023136E+08 0.5806393E+04 -0.7472590E+05 4 0.6818844E+07 -0.2017879E+08 0.5860733E+04 -0.7456845E+05 5 0.6834176E+07 -0.2012469E+08 0.5916134E+04 -0.7440731E+05 6 0.6850010E+07 -0.2006889E+08 0.5972741E+04 -0.7424204E+05 7 0.6866403E+07 -0.2001120E+08 0.6030703E+04 -0.7407218E+05 8 0.6883414E+07 -0.1995144E+08 0.6090167E+04 -0.7389728E+05 9 0.6901105E+07 -0.1988941E+08 0.6151283E+04 -0.7371690E+05 10 0.6919542E+07 -0.1982493E+08 0.6214198E+04 -0.7353059E+05 11 0.6938792E+07 -0.1975779E+08 0.6279058E+04 -0.7333789E+05 12 0.6958927E+07 -0.1968778E+08 0.6346004E+04 -0.7313839E+05 13 0.6980018E+07 -0.1961470E+08 0.6415170E+04 -0.7293168E+05 14 0.7002141E+07 -0.1953837E+08 0.6486680E+04 -0.7271740E+05 15 0.7025370E+07 -0.1945858E+08 0.6560642E+04 -0.7249522E+05 16 0.7049778E+07 -0.1937517E+08 0.6637144E+04 -0.7226492E+05 17 0.7075435E+07 -0.1928800E+08 0.6716246E+04 -0.7202636E+05 18 0.7102403E+07 -0.1919696E+08 0.6797970E+04 -0.7177952E+05 19 0.7130736E+07 -0.1910200E+08 0.6882296E+04 -0.7152453E+05 20 0.7160473E+07 -0.1900311E+08 0.6969149E+04 -0.7126172E+05 21 0.7191634E+07 -0.1890040E+08 0.7058387E+04 -0.7099163E+05 22 0.7224213E+07 -0.1879403E+08 0.7149795E+04 -0.7071505E+05 23 0.7258174E+07 -0.1868430E+08 0.7243070E+04 -0.7043305E+05 24 0.7293444E+07 -0.1857162E+08 0.7337824E+04 -0.7014695E+05 25 0.7329906E+07 -0.1845653E+08 0.7433571E+04 -0.6985839E+05 26 0.7367397E+07 -0.1833970E+08 0.7529737E+04 -0.6956925E+05 27 0.7405705E+07 -0.1822192E+08 0.7625666E+04 -0.6928165E+05 28 0.7444569E+07 -0.1810412E+08 0.7720638E+04 -0.6899783E+05 29 0.7483684E+07 -0.1798725E+08 0.7813892E+04 -0.6872016E+05 30 0.7522712E+07 -0.1787237E+08 0.7904658E+04 -0.6845093E+05 31 0.7561289E+07 -0.1776049E+08 0.7992190E+04 -0.6819232E+05 32 0.7599048E+07 -0.1765260E+08 0.8075799E+04 -0.6794629E+05 33 0.7635630E+07 -0.1754958E+08 0.8154891E+04 -0.6771447E+05 34 0.7670704E+07 -0.1745219E+08 0.8228989E+04 -0.6749812E+05 35 0.7703984E+07 -0.1736103E+08 0.8297748E+04 -0.6729806E+05 36 0.7735237E+07 -0.1727650E+08 0.8360970E+04 -0.6711471E+05 37 0.7764296E+07 -0.1719884E+08 0.8418591E+04 -0.6694810E+05 38 0.7791057E+07 -0.1712812E+08 0.8470677E+04 -0.6679788E+05 39 0.7815480E+07 -0.1706422E+08 0.8517401E+04 -0.6666343E+05 40 0.7837581E+07 -0.1700693E+08 0.8559021E+04 -0.6654390E+05 41 0.7857427E+07 -0.1695591E+08 0.8595862E+04 -0.6643827E+05 42 0.7861790E+07 -0.1694475E+08 0.8603895E+04 -0.6641526E+05 43 0.7868124E+07 -0.1692858E+08 0.8615511E+04 -0.6638199E+05 44 0.7877302E+07 -0.1690522E+08 0.8632255E+04 -0.6633407E+05 45 0.7890571E+07 -0.1687159E+08 0.8656274E+04 -0.6626538E+05 46 0.7909692E+07 -0.1682345E+08 0.8690495E+04 -0.6616761E+05 47 0.7937108E+07 -0.1675504E+08 0.8738764E+04 -0.6602990E+05 48 0.7976135E+07 -0.1665892E+08 0.8805862E+04 -0.6583876E+05 49 0.8031109E+07 -0.1652598E+08 0.8897185E+04 -0.6557900E+05 50 0.8107361E+07 -0.1634617E+08 0.9017735E+04 -0.6523627E+05 51 0.8210788E+07 -0.1611041E+08 0.9169983E+04 -0.6480212E+05 52 0.8346673E+07 -0.1581401E+08 0.9350374E+04 -0.6428135E+05 53 0.8517458E+07 -0.1546114E+08 0.9545242E+04 -0.6369901E+05 54 0.8719818E+07 -0.1506837E+08 0.9728838E+04 -0.6310135E+05 55 0.8942579E+07 -0.1466388E+08 0.9867628E+04 -0.6254572E+05 56 0.9167860E+07 -0.1428059E+08 0.9932356E+04 -0.6208181E+05 57 0.9376263E+07 -0.1394610E+08 0.9911740E+04 -0.6173546E+05 58 0.9553313E+07 -0.1367533E+08 0.9817304E+04 -0.6150503E+05 59 0.9692950E+07 -0.1346959E+08 0.9675768E+04 -0.6136993E+05 60 0.9796672E+07 -0.1332090E+08 0.9516167E+04 -0.6130292E+05 61 0.9870302E+07 -0.1321735E+08 0.9360626E+04 -0.6127918E+05 62 0.9920893E+07 -0.1314713E+08 0.9221613E+04 -0.6128017E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.4230397E+02 0.1265946E+02 0.1203698E-04 0.6814001E+05 0.2613716E-01 2 0.4239755E+02 0.1268738E+02 0.1202564E-04 0.6828598E+05 0.2611348E-01 3 0.4249307E+02 0.1271586E+02 0.1201412E-04 0.6843507E+05 0.2608940E-01 4 0.4259083E+02 0.1274497E+02 0.1200237E-04 0.6858775E+05 0.2606484E-01 5 0.4269113E+02 0.1277481E+02 0.1199036E-04 0.6874449E+05 0.2603974E-01 6 0.4279427E+02 0.1280547E+02 0.1197807E-04 0.6890580E+05 0.2601404E-01 7 0.4290058E+02 0.1283704E+02 0.1196545E-04 0.6907220E+05 0.2598765E-01 8 0.4301040E+02 0.1286961E+02 0.1195247E-04 0.6924420E+05 0.2596050E-01 9 0.4312407E+02 0.1290329E+02 0.1193911E-04 0.6942238E+05 0.2593252E-01 10 0.4324194E+02 0.1293817E+02 0.1192531E-04 0.6960729E+05 0.2590365E-01 11 0.4336438E+02 0.1297435E+02 0.1191105E-04 0.6979953E+05 0.2587380E-01 12 0.4349175E+02 0.1301194E+02 0.1189629E-04 0.6999971E+05 0.2584289E-01 13 0.4362442E+02 0.1305105E+02 0.1188100E-04 0.7020842E+05 0.2581087E-01 14 0.4376276E+02 0.1309176E+02 0.1186515E-04 0.7042626E+05 0.2577767E-01 15 0.4390712E+02 0.1313418E+02 0.1184870E-04 0.7065383E+05 0.2574321E-01 16 0.4405783E+02 0.1317840E+02 0.1183164E-04 0.7089167E+05 0.2570745E-01 17 0.4421518E+02 0.1322448E+02 0.1181395E-04 0.7114029E+05 0.2567035E-01 18 0.4437941E+02 0.1327249E+02 0.1179560E-04 0.7140010E+05 0.2563188E-01 19 0.4455068E+02 0.1332247E+02 0.1177661E-04 0.7167141E+05 0.2559203E-01 20 0.4472906E+02 0.1337441E+02 0.1175697E-04 0.7195436E+05 0.2555082E-01 21 0.4491448E+02 0.1342830E+02 0.1173671E-04 0.7224893E+05 0.2550829E-01 22 0.4510674E+02 0.1348405E+02 0.1171588E-04 0.7255482E+05 0.2546454E-01 23 0.4530546E+02 0.1354153E+02 0.1169452E-04 0.7287148E+05 0.2541967E-01 24 0.4551002E+02 0.1360057E+02 0.1167272E-04 0.7319799E+05 0.2537385E-01 25 0.4571961E+02 0.1366091E+02 0.1165059E-04 0.7353309E+05 0.2532730E-01 26 0.4593316E+02 0.1372224E+02 0.1162823E-04 0.7387512E+05 0.2528026E-01 27 0.4614937E+02 0.1378417E+02 0.1160580E-04 0.7422202E+05 0.2523305E-01 28 0.4636671E+02 0.1384627E+02 0.1158345E-04 0.7457135E+05 0.2518598E-01 29 0.4658348E+02 0.1390804E+02 0.1156137E-04 0.7492039E+05 0.2513943E-01 30 0.4679783E+02 0.1396897E+02 0.1153973E-04 0.7526615E+05 0.2509377E-01 31 0.4700787E+02 0.1402852E+02 0.1151870E-04 0.7560555E+05 0.2504939E-01 32 0.4721174E+02 0.1408617E+02 0.1149846E-04 0.7593553E+05 0.2500664E-01 33 0.4740768E+02 0.1414146E+02 0.1147917E-04 0.7625320E+05 0.2496586E-01 34 0.4759414E+02 0.1419394E+02 0.1146096E-04 0.7655595E+05 0.2492731E-01 35 0.4776980E+02 0.1424329E+02 0.1144392E-04 0.7684160E+05 0.2489123E-01 36 0.4793369E+02 0.1428924E+02 0.1142813E-04 0.7710848E+05 0.2485776E-01 37 0.4808517E+02 0.1433162E+02 0.1141363E-04 0.7735544E+05 0.2482700E-01 38 0.4822390E+02 0.1437038E+02 0.1140042E-04 0.7758189E+05 0.2479896E-01 39 0.4834988E+02 0.1440552E+02 0.1138849E-04 0.7778775E+05 0.2477362E-01 40 0.4846339E+02 0.1443714E+02 0.1137779E-04 0.7797340E+05 0.2475087E-01 41 0.4856491E+02 0.1446538E+02 0.1136826E-04 0.7813958E+05 0.2473059E-01 42 0.4858718E+02 0.1447158E+02 0.1136617E-04 0.7817606E+05 0.2472615E-01 43 0.4861947E+02 0.1448055E+02 0.1136315E-04 0.7822896E+05 0.2471972E-01 44 0.4866621E+02 0.1449353E+02 0.1135878E-04 0.7830553E+05 0.2471043E-01 45 0.4873363E+02 0.1451225E+02 0.1135250E-04 0.7841606E+05 0.2469704E-01 46 0.4883050E+02 0.1453912E+02 0.1134350E-04 0.7857496E+05 0.2467786E-01 47 0.4896882E+02 0.1457743E+02 0.1133070E-04 0.7880206E+05 0.2465057E-01 48 0.4916456E+02 0.1463155E+02 0.1131270E-04 0.7912386E+05 0.2461214E-01 49 0.4943806E+02 0.1470697E+02 0.1128777E-04 0.7957428E+05 0.2455883E-01 50 0.4981328E+02 0.1481007E+02 0.1125397E-04 0.8019374E+05 0.2448636E-01 51 0.5031498E+02 0.1494728E+02 0.1120948E-04 0.8102470E+05 0.2439062E-01 52 0.5096238E+02 0.1512328E+02 0.1115319E-04 0.8210141E+05 0.2426884E-01 53 0.5175889E+02 0.1533826E+02 0.1108557E-04 0.8343274E+05 0.2412144E-01 54 0.5268059E+02 0.1558499E+02 0.1100940E-04 0.8498210E+05 0.2395372E-01 55 0.5367085E+02 0.1584781E+02 0.1092985E-04 0.8665668E+05 0.2377629E-01 56 0.5464954E+02 0.1610541E+02 0.1085335E-04 0.8832130E+05 0.2360317E-01 57 0.5553686E+02 0.1633726E+02 0.1078566E-04 0.8983837E+05 0.2344767E-01 58 0.5627847E+02 0.1652987E+02 0.1073021E-04 0.9111174E+05 0.2331851E-01 59 0.5685610E+02 0.1667920E+02 0.1068769E-04 0.9210686E+05 0.2321828E-01 60 0.5728127E+02 0.1678875E+02 0.1065675E-04 0.9284112E+05 0.2314466E-01 61 0.5758117E+02 0.1686583E+02 0.1063510E-04 0.9335994E+05 0.2309280E-01 62 0.5778635E+02 0.1691848E+02 0.1062037E-04 0.9371530E+05 0.2305735E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.4239755E+02 0.6588386E+03 0.1010917E-03 0.1289910E+06 0.1508824E+00 0.1133021E-01 2 0.4252375E+02 0.6587636E+03 0.1010473E-03 0.1291802E+06 0.1506170E+00 0.1132039E-01 3 0.4265284E+02 0.6586841E+03 0.1009996E-03 0.1293740E+06 0.1503453E+00 0.1131025E-01 4 0.4278519E+02 0.6585998E+03 0.1009486E-03 0.1295729E+06 0.1500665E+00 0.1129976E-01 5 0.4292123E+02 0.6585101E+03 0.1008938E-03 0.1297777E+06 0.1497795E+00 0.1128888E-01 6 0.4306137E+02 0.6584146E+03 0.1008348E-03 0.1299889E+06 0.1494837E+00 0.1127758E-01 7 0.4320603E+02 0.6583127E+03 0.1007715E-03 0.1302073E+06 0.1491779E+00 0.1126580E-01 8 0.4335567E+02 0.6582038E+03 0.1007032E-03 0.1304335E+06 0.1488613E+00 0.1125349E-01 9 0.4351073E+02 0.6580871E+03 0.1006295E-03 0.1306682E+06 0.1485328E+00 0.1124062E-01 10 0.4367169E+02 0.6579620E+03 0.1005500E-03 0.1309122E+06 0.1481915E+00 0.1122712E-01 11 0.4383902E+02 0.6578276E+03 0.1004641E-03 0.1311663E+06 0.1478361E+00 0.1121294E-01 12 0.4401319E+02 0.6576830E+03 0.1003711E-03 0.1314312E+06 0.1474658E+00 0.1119802E-01 13 0.4419465E+02 0.6575273E+03 0.1002704E-03 0.1317077E+06 0.1470794E+00 0.1118229E-01 14 0.4438386E+02 0.6573595E+03 0.1001613E-03 0.1319964E+06 0.1466759E+00 0.1116571E-01 15 0.4458122E+02 0.6571786E+03 0.1000431E-03 0.1322982E+06 0.1462544E+00 0.1114821E-01 16 0.4478710E+02 0.6569834E+03 0.9991508E-04 0.1326136E+06 0.1458140E+00 0.1112972E-01 17 0.4500178E+02 0.6567730E+03 0.9977647E-04 0.1329431E+06 0.1453539E+00 0.1111018E-01 18 0.4522546E+02 0.6565462E+03 0.9962654E-04 0.1332871E+06 0.1448737E+00 0.1108956E-01 19 0.4545818E+02 0.6563022E+03 0.9946460E-04 0.1336458E+06 0.1443731E+00 0.1106780E-01 20 0.4569986E+02 0.6560400E+03 0.9929007E-04 0.1340191E+06 0.1438523E+00 0.1104487E-01 21 0.4595018E+02 0.6557590E+03 0.9910249E-04 0.1344066E+06 0.1433116E+00 0.1102076E-01 22 0.4620861E+02 0.6554589E+03 0.9890160E-04 0.1348077E+06 0.1427521E+00 0.1099549E-01 23 0.4647435E+02 0.6551397E+03 0.9868739E-04 0.1352211E+06 0.1421754E+00 0.1096907E-01 24 0.4674631E+02 0.6548019E+03 0.9846017E-04 0.1356453E+06 0.1415838E+00 0.1094159E-01 25 0.4702307E+02 0.6544465E+03 0.9822061E-04 0.1360781E+06 0.1409801E+00 0.1091315E-01 26 0.4730294E+02 0.6540751E+03 0.9796982E-04 0.1365170E+06 0.1403680E+00 0.1088389E-01 27 0.4758393E+02 0.6536900E+03 0.9770935E-04 0.1369588E+06 0.1397517E+00 0.1085399E-01 28 0.4786383E+02 0.6532942E+03 0.9744122E-04 0.1374001E+06 0.1391360E+00 0.1082368E-01 29 0.4814028E+02 0.6528912E+03 0.9716784E-04 0.1378371E+06 0.1385261E+00 0.1079320E-01 30 0.4841085E+02 0.6524851E+03 0.9689198E-04 0.1382661E+06 0.1379274E+00 0.1076285E-01 31 0.4867315E+02 0.6520802E+03 0.9661665E-04 0.1386831E+06 0.1373452E+00 0.1073292E-01 32 0.4892496E+02 0.6516811E+03 0.9634494E-04 0.1390845E+06 0.1367847E+00 0.1070369E-01 33 0.4916431E+02 0.6512921E+03 0.9607989E-04 0.1394670E+06 0.1362503E+00 0.1067546E-01 34 0.4938957E+02 0.6509174E+03 0.9582433E-04 0.1398279E+06 0.1357459E+00 0.1064847E-01 35 0.4959953E+02 0.6505604E+03 0.9558074E-04 0.1401651E+06 0.1352745E+00 0.1062295E-01 36 0.4979339E+02 0.6502242E+03 0.9535116E-04 0.1404771E+06 0.1348381E+00 0.1059905E-01 37 0.4997079E+02 0.6499110E+03 0.9513709E-04 0.1407633E+06 0.1344377E+00 0.1057690E-01 38 0.5013176E+02 0.6496220E+03 0.9493952E-04 0.1410235E+06 0.1340736E+00 0.1055657E-01 39 0.5027669E+02 0.6493579E+03 0.9475892E-04 0.1412581E+06 0.1337451E+00 0.1053806E-01 40 0.5040622E+02 0.6491187E+03 0.9459528E-04 0.1414682E+06 0.1334509E+00 0.1052136E-01 41 0.5052124E+02 0.6489039E+03 0.9444821E-04 0.1416550E+06 0.1331892E+00 0.1050640E-01 42 0.5054637E+02 0.6488566E+03 0.9441586E-04 0.1416958E+06 0.1331320E+00 0.1050312E-01 43 0.5058274E+02 0.6487880E+03 0.9436889E-04 0.1417549E+06 0.1330491E+00 0.1049835E-01 44 0.5063522E+02 0.6486886E+03 0.9430082E-04 0.1418403E+06 0.1329295E+00 0.1049146E-01 45 0.5071064E+02 0.6485449E+03 0.9420238E-04 0.1419631E+06 0.1327574E+00 0.1048150E-01 46 0.5081839E+02 0.6483377E+03 0.9406048E-04 0.1421387E+06 0.1325111E+00 0.1046718E-01 47 0.5097097E+02 0.6480407E+03 0.9385696E-04 0.1423878E+06 0.1321618E+00 0.1044670E-01 48 0.5118435E+02 0.6476181E+03 0.9356722E-04 0.1427370E+06 0.1316718E+00 0.1041768E-01 49 0.5147746E+02 0.6470234E+03 0.9315931E-04 0.1432182E+06 0.1309960E+00 0.1037706E-01 50 0.5187004E+02 0.6462007E+03 0.9259457E-04 0.1438656E+06 0.1300858E+00 0.1032120E-01 51 0.5237774E+02 0.6450904E+03 0.9183183E-04 0.1447082E+06 0.1288993E+00 0.1024639E-01 52 0.5300410E+02 0.6436448E+03 0.9083802E-04 0.1457562E+06 0.1274198E+00 0.1014976E-01 53 0.5373132E+02 0.6418540E+03 0.8960632E-04 0.1469861E+06 0.1256780E+00 0.1003100E-01 54 0.5451558E+02 0.6397749E+03 0.8817674E-04 0.1483297E+06 0.1237668E+00 0.9894064E-02 55 0.5529382E+02 0.6375433E+03 0.8664476E-04 0.1496828E+06 0.1218321E+00 0.9747886E-02 56 0.5600230E+02 0.6353486E+03 0.8514252E-04 0.1509341E+06 0.1200327E+00 0.9604669E-02 57 0.5659669E+02 0.6333729E+03 0.8379591E-04 0.1519999E+06 0.1184912E+00 0.9476078E-02 58 0.5706121E+02 0.6317342E+03 0.8268453E-04 0.1528441E+06 0.1172638E+00 0.9369612E-02 59 0.5740406E+02 0.6304667E+03 0.8182901E-04 0.1534741E+06 0.1163438E+00 0.9287358E-02 60 0.5764640E+02 0.6295388E+03 0.8120545E-04 0.1539232E+06 0.1156857E+00 0.9227202E-02 61 0.5781244E+02 0.6288871E+03 0.8076891E-04 0.1542328E+06 0.1152310E+00 0.9184971E-02 62 0.5792377E+02 0.6284425E+03 0.8047189E-04 0.1544413E+06 0.1149242E+00 0.9156177E-02 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.605884965E+00 0.602290948E+00 0.598622357E+00 0.594867917E+00 0.591016031E+00 2 0.394115035E+00 0.397709052E+00 0.401377643E+00 0.405132083E+00 0.408983969E+00 Component Mole fractions on stages: 6 to 10 1 0.587054731E+00 0.582971646E+00 0.578753977E+00 0.574388511E+00 0.569861641E+00 2 0.412945269E+00 0.417028354E+00 0.421246023E+00 0.425611489E+00 0.430138359E+00 Component Mole fractions on stages: 11 to 15 1 0.565159438E+00 0.560267758E+00 0.555172407E+00 0.549859370E+00 0.544315127E+00 2 0.434840562E+00 0.439732242E+00 0.444827593E+00 0.450140630E+00 0.455684873E+00 Component Mole fractions on stages: 16 to 20 1 0.538527059E+00 0.532483974E+00 0.526176749E+00 0.519599105E+00 0.512748507E+00 2 0.461472941E+00 0.467516026E+00 0.473823251E+00 0.480400895E+00 0.487251493E+00 Component Mole fractions on stages: 21 to 25 1 0.505627182E+00 0.498243194E+00 0.490611547E+00 0.482755187E+00 0.474705808E+00 2 0.494372818E+00 0.501756806E+00 0.509388453E+00 0.517244813E+00 0.525294192E+00 Component Mole fractions on stages: 26 to 30 1 0.466504314E+00 0.458200762E+00 0.449853695E+00 0.441528731E+00 0.433296437E+00 2 0.533495686E+00 0.541799238E+00 0.550146305E+00 0.558471269E+00 0.566703563E+00 Component Mole fractions on stages: 31 to 35 1 0.425229565E+00 0.417399850E+00 0.409874678E+00 0.402713943E+00 0.395967437E+00 2 0.574770435E+00 0.582600150E+00 0.590125322E+00 0.597286057E+00 0.604032563E+00 Component Mole fractions on stages: 36 to 40 1 0.389673019E+00 0.383855704E+00 0.378527684E+00 0.373689177E+00 0.369329901E+00 2 0.610326981E+00 0.616144296E+00 0.621472316E+00 0.626310823E+00 0.630670099E+00 Component Mole fractions on stages: 41 to 45 1 0.365430951E+00 0.364575610E+00 0.363335366E+00 0.361540640E+00 0.358951153E+00 2 0.634569049E+00 0.635424390E+00 0.636664634E+00 0.638459360E+00 0.641048847E+00 Component Mole fractions on stages: 46 to 50 1 0.355230839E+00 0.349918737E+00 0.342401039E+00 0.331897287E+00 0.317486879E+00 2 0.644769161E+00 0.650081263E+00 0.657598961E+00 0.668102713E+00 0.682513121E+00 Component Mole fractions on stages: 51 to 55 1 0.298218776E+00 0.273355069E+00 0.242764891E+00 0.207366495E+00 0.169335095E+00 2 0.701781224E+00 0.726644931E+00 0.757235109E+00 0.792633505E+00 0.830664905E+00 Component Mole fractions on stages: 56 to 60 1 0.131748361E+00 0.976702140E-01 0.691886118E-01 0.470045919E-01 0.306756333E-01 2 0.868251639E+00 0.902329786E+00 0.930811388E+00 0.952995408E+00 0.969324367E+00 Component Mole fractions on stages: 61 to 62 1 0.191576597E-01 0.112778545E-01 2 0.980842340E+00 0.988722146E+00 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.602290948E+00 0.597444088E+00 0.592486582E+00 0.587403319E+00 0.582178739E+00 2 0.397709052E+00 0.402555912E+00 0.407513418E+00 0.412596681E+00 0.417821261E+00 Component Mole fractions on stages: 6 to 10 1 0.576796791E+00 0.571240912E+00 0.565494041E+00 0.559538659E+00 0.553356884E+00 2 0.423203209E+00 0.428759088E+00 0.434505959E+00 0.440461341E+00 0.446643116E+00 Component Mole fractions on stages: 11 to 15 1 0.546930616E+00 0.540241764E+00 0.533272546E+00 0.526005912E+00 0.518426077E+00 2 0.453069384E+00 0.459758236E+00 0.466727454E+00 0.473994088E+00 0.481573923E+00 Component Mole fractions on stages: 16 to 20 1 0.510519206E+00 0.502274254E+00 0.493683967E+00 0.484746044E+00 0.475464436E+00 2 0.489480794E+00 0.497725746E+00 0.506316033E+00 0.515253956E+00 0.524535564E+00 Component Mole fractions on stages: 21 to 25 1 0.465850723E+00 0.455925492E+00 0.445719595E+00 0.435275124E+00 0.424645929E+00 2 0.534149277E+00 0.544074508E+00 0.554280405E+00 0.564724876E+00 0.575354071E+00 Component Mole fractions on stages: 26 to 30 1 0.413897480E+00 0.403105903E+00 0.392356105E+00 0.381738965E+00 0.371347744E+00 2 0.586102520E+00 0.596894097E+00 0.607643895E+00 0.618261035E+00 0.628652256E+00 Component Mole fractions on stages: 31 to 35 1 0.361273968E+00 0.351603173E+00 0.342410935E+00 0.333759612E+00 0.325696096E+00 2 0.638726032E+00 0.648396827E+00 0.657589065E+00 0.666240388E+00 0.674303904E+00 Component Mole fractions on stages: 36 to 40 1 0.318250760E+00 0.311437580E+00 0.305255310E+00 0.299689427E+00 0.294714565E+00 2 0.681749240E+00 0.688562420E+00 0.694744690E+00 0.700310573E+00 0.705285435E+00 Component Mole fractions on stages: 41 to 45 1 0.290297147E+00 0.289332137E+00 0.287935481E+00 0.285919890E+00 0.283023163E+00 2 0.709702853E+00 0.710667863E+00 0.712064519E+00 0.714080110E+00 0.716976837E+00 Component Mole fractions on stages: 46 to 50 1 0.278885132E+00 0.273025175E+00 0.264830173E+00 0.253573124E+00 0.238496002E+00 2 0.721114868E+00 0.726974825E+00 0.735169827E+00 0.746426876E+00 0.761503998E+00 Component Mole fractions on stages: 51 to 55 1 0.218997558E+00 0.194941997E+00 0.167012920E+00 0.136892978E+00 0.107004368E+00 2 0.781002442E+00 0.805058003E+00 0.832987080E+00 0.863107022E+00 0.892995632E+00 Component Mole fractions on stages: 56 to 60 1 0.797950407E-01 0.569670235E-01 0.391270246E-01 0.259598078E-01 0.166526927E-01 2 0.920204959E+00 0.943032977E+00 0.960872975E+00 0.974040192E+00 0.983347307E+00 Component Mole fractions on stages: 61 to 62 1 0.102757623E-01 0.600000000E-02 2 0.989724238E+00 0.994000000E+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 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 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 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 Component reaction rates on stages: 21 to 25 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 Component reaction rates on stages: 26 to 30 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 Component reaction rates on stages: 31 to 35 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 Component reaction rates on stages: 36 to 40 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 Component reaction rates on stages: 41 to 45 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 Component reaction rates on stages: 46 to 50 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 Component reaction rates on stages: 51 to 55 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 Component reaction rates on stages: 56 to 60 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 Component reaction rates on stages: 61 to 62 1 0.000000000E+00 0.000000000E+00 2 0.000000000E+00 0.000000000E+00 [Condenser Heat Duty] -5.796322471E+06 [Reboiler Heat Duty] 7.417289951E+06 [UA Column] 0.000000000E+00 [K-values] Component K-values on stages: 1 to 5 1 0.100596724E+01 0.100811266E+01 0.101035597E+01 0.101270779E+01 0.101517969E+01 2 0.990963201E+00 0.987959783E+00 0.984943379E+00 0.981908246E+00 0.978849110E+00 Component K-values on stages: 6 to 10 1 0.101778432E+01 0.102053553E+01 0.102344841E+01 0.102653946E+01 0.102982660E+01 2 0.975761194E+00 0.972640269E+00 0.969482729E+00 0.966285687E+00 0.963047103E+00 Component K-values on stages: 11 to 15 1 0.103332931E+01 0.103706858E+01 0.104106692E+01 0.104534827E+01 0.104993778E+01 2 0.959765938E+00 0.956442336E+00 0.953077838E+00 0.949675620E+00 0.946240756E+00 Component K-values on stages: 16 to 20 1 0.105486151E+01 0.106014587E+01 0.106581697E+01 0.107189963E+01 0.107841611E+01 2 0.942780487E+00 0.939304486E+00 0.935825096E+00 0.932357509E+00 0.928919841E+00 Component K-values on stages: 21 to 25 1 0.108538456E+01 0.109281714E+01 0.110071792E+01 0.110908058E+01 0.111788616E+01 2 0.925533067E+00 0.922220759E+00 0.919008588E+00 0.915923550E+00 0.912992917E+00 Component K-values on stages: 26 to 30 1 0.112710112E+01 0.113667589E+01 0.114654440E+01 0.115662474E+01 0.116682125E+01 2 0.910242949E+00 0.907697430E+00 0.905376174E+00 0.903293654E+00 0.901457932E+00 Component K-values on stages: 31 to 35 1 0.117702797E+01 0.118713335E+01 0.119702567E+01 0.120659879E+01 0.121575739E+01 2 0.899870064E+00 0.898524059E+00 0.897407443E+00 0.896502326E+00 0.895786841E+00 Component K-values on stages: 36 to 40 1 0.122442133E+01 0.123252853E+01 0.124003636E+01 0.124692146E+01 0.125317831E+01 2 0.895236760E+00 0.894827076E+00 0.894533382E+00 0.894332953E+00 0.894205477E+00 Component K-values on stages: 41 to 45 1 0.125881689E+01 0.126005916E+01 0.126186382E+01 0.126448230E+01 0.126827483E+01 2 0.894133433E+00 0.894122871E+00 0.894110881E+00 0.894100468E+00 0.894099800E+00 Component K-values on stages: 46 to 50 1 0.127375323E+01 0.128163543E+01 0.129290797E+01 0.130888196E+01 0.133120420E+01 2 0.894128231E+00 0.894228026E+00 0.894485786E+00 0.895067868E+00 0.896269912E+00 Component K-values on stages: 51 to 55 1 0.136174475E+01 0.140223796E+01 0.145356952E+01 0.151480739E+01 0.158250637E+01 2 0.898564699E+00 0.902599475E+00 0.909059850E+00 0.918349040E+00 0.930200413E+00 Component K-values on stages: 56 to 60 1 0.165108458E+01 0.171450443E+01 0.176830752E+01 0.181066794E+01 0.184208246E+01 2 0.943541577E+00 0.956837999E+00 0.968714296E+00 0.978394337E+00 0.985739585E+00 Component K-values on stages: 61 to 62 1 0.186435410E+01 0.187964241E+01 2 0.991025887E+00 0.994690287E+00 [Molecular weights] 1 32.042 2 58.080 [Feed stream 1] 41 Stage Number 1.2707405788530E-01 Flow rate 3.2887255374000E+02 Temperature [K] 1.0132500000000E+06 Pressure [Pa] -2.8843464834748E+07 Enthalpy [J/kmol] -8.7211247984024E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.4999999999980E-01 Mole fraction of component 1 7.5000000000020E-01 Mole fraction of component 2 1.2707405788530E-01 Flow rate 2.4999999999980E-01 Mole fraction of component 1 7.5000000000020E-01 Mole fraction of component 2 5.1570501327520E+01 Molar mass 7.5747049505375E+02 Density 2.6556371427811E-04 Viscosity 1.5933077922127E-01 Thermal conductivity 1.2150478447076E+05 Heat capacity 1.9370920555266E-02 Surface tension [Reflashed Feed stream 1] 41 Stage Number 1.2707405788530E-01 Flow rate 3.2887255374000E+02 Temperature [K] 1.0132000000000E+06 Pressure [Pa] -2.8843464834748E+07 Enthalpy [J/kmol] -8.7211247984024E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.4999999999980E-01 Mole fraction of component 1 7.5000000000020E-01 Mole fraction of component 2 1.2707405788530E-01 Flow rate 2.4999999999980E-01 Mole fraction of component 1 7.5000000000020E-01 Mole fraction of component 2 5.1570501327520E+01 Molar mass 7.5747045294873E+02 Density 2.6556371427811E-04 Viscosity 1.5933077922127E-01 Thermal conductivity 1.2150478447076E+05 Heat capacity 1.9370920555266E-02 Surface tension [Top product] 1 Stage Number 5.1998223709330E-02 Flow rate 4.0724050610938E+02 Temperature [K] 1.0132000000000E+06 Pressure [Pa] -2.0332551740427E+07 Enthalpy [J/kmol] -7.5031416257316E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 6.0229094826990E-01 Mole fraction of component 1 3.9770905173011E-01 Mole fraction of component 2 5.1998223709330E-02 Flow rate 6.0229094826990E-01 Mole fraction of component 1 3.9770905173011E-01 Mole fraction of component 2 4.2397548906893E+01 Molar mass 6.5883861815120E+02 Density 1.0109173009695E-04 Viscosity 1.5088244109530E-01 Thermal conductivity 1.2899098709592E+05 Heat capacity 1.1330212448569E-02 Surface tension [Bottom product] 62 Stage Number 7.5075834175970E-02 Flow rate 4.1624496482522E+02 Temperature [K] 1.0132000000000E+06 Pressure [Pa] -1.3147134147607E+07 Enthalpy [J/kmol] -6.1280173995053E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 5.9999999999999E-03 Mole fraction of component 1 9.9399999999999E-01 Mole fraction of component 2 7.5075834175970E-02 Flow rate 5.9999999999999E-03 Mole fraction of component 1 9.9399999999999E-01 Mole fraction of component 2 5.7923773818969E+01 Molar mass 6.2844250662994E+02 Density 8.0471892560826E-05 Viscosity 1.1492418968061E-01 Thermal conductivity 1.5444125083432E+05 Heat capacity 9.1561771104641E-03 Surface tension [Equilibrium Data at 1.01320E+06 Pa] Temperature X(1) Y(1) 416.508 0.0000000 0.0000000 415.458 0.0250000 0.0453462 414.518 0.0500000 0.0867524 413.675 0.0750000 0.1247951 412.917 0.1000000 0.1599486 412.236 0.1250000 0.1926076 411.622 0.1500000 0.2231034 411.068 0.1750000 0.2517174 410.569 0.2000000 0.2786903 410.119 0.2250000 0.3042302 409.714 0.2500000 0.3285186 409.350 0.2750000 0.3517147 409.023 0.3000000 0.3739602 408.730 0.3250000 0.3953816 408.469 0.3500000 0.4160934 408.237 0.3750000 0.4361998 408.033 0.4000000 0.4557971 407.855 0.4250000 0.4749749 407.701 0.4500000 0.4938174 407.570 0.4750000 0.5124052 407.462 0.5000000 0.5308155 407.376 0.5250000 0.5491238 407.310 0.5500000 0.5674050 407.266 0.5750000 0.5857336 407.242 0.6000000 0.6041853 407.238 0.6250000 0.6228374 407.256 0.6500000 0.6417704 407.295 0.6750000 0.6610684 407.357 0.7000000 0.6808207 407.441 0.7250000 0.7011228 407.549 0.7500000 0.7220779 407.683 0.7750000 0.7437984 407.843 0.8000000 0.7664083 408.033 0.8250000 0.7900444 408.254 0.8500000 0.8148599 408.508 0.8750000 0.8410266 408.800 0.9000000 0.8687389 409.131 0.9250000 0.8982185 409.507 0.9500000 0.9297189 409.931 0.9750000 0.9635330 410.408 1.0000000 1.0000000 [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>џsy@?sy@Pnsy@c)ty@/C-ty@x6ty@[3CUty@^{ty@Nݦty@9ty@M uy@Tuy@x2Guy@ uy@V Wvy@@)vy@P@wy@>9wy@^hxy@kfyy@qmyy@%Dzy@\Cw{y@%ǝ|y@<}y@D~y@*&y@?{y@C߂y@0WNy@_Ņy@IV?y@,y@ ZH(y@jMy@Vcdy@~]'y@ Uy@N]ly@\dly@mSy@>y@,ђy@=y@?ۓy@}i,y@FD y@-y@6uyy@Sy@C{y@wy@#2ҳy@c=ZAy@FCy@^y@`y@^y@Rfy@Sy@4?H`z@5`z@"Pressure profile.Pressure at each stage>.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A.A(Vapour Flow profile4Vapour Flow at each stage>YEfI@ nζj@f dj@j@i=j@ Vj@,nj@Wj@qj@*j@׶j@FGͲj@IIk@2 k@f|k@ KDk@'fj-(k@4l2k@sr^=k@Xh/Hk@%+rTk@=͑`k@|v `mk@xzk@xk@Yk@P8k@yYͱk@k@}.dk@Dk@kl@,6El@q@jf-q@0{q@;q@vmr@ƐRr@&mr@r@P@,r@U:Dr@br@6։r@r@n}r@HξR's@~_s@@Zs@=bs@ 's@"@GPs@H?at@(Liquid Flow profile4Liquid Flow at each stage>-$6d@s9kd@eDrd@T?zd@q@Bd@ɋd@tٔd@IRd@5s;d@`d@{?md@epd@2uWvd@Jd@C6nd@`d@p}e@̯e@d#e@S1e@H@e@JZ Ne@,[e@yeie@zrve@3Fe@$Ďe@ߙe@ŏ0e@[ﰭe@=]e@` Z7e@WWEe@RK̦v@IyR;v@4?Pv@D ,Qv@ebWv@>|շv@zģv@mv@^,v@lpv@w@1 ;w@Whjw@ w@\w@jB?x@^Bx@]L#lx@0M^x@v冥x@AWlݗx@7wR@Duties profile*Duties at each stage>/$xV/|rK\A4Vapour Moleweight profile@Vapour Moleweight at each stage>{,}&E@-C2E@Q?E@rCQKE@jvXE@eE@A4FsE@oTE@5E@E@E@mE@{E@6YE@E@%]3fF@k`F@?0F@G|FF@/iQ]F@Ll> uF@hF@:3PF@('UHF@3.F@pqF@s`G@ގpZ.G@_xJG@CKfG@LOXG@KG@ܝ.G@k G@:pΈG@Mg'G@L H@TH@"*,H@]P;H@xNHH@nض(KH@3mJOH@S"^FUH@|]H@MjH@3K|H@iUMH@מYH@>H@qrCQ(I@)D/{I@wN#I@ WJ@BiJ@иp $SK@CԷK@du#L@ OmL@GŧL@JOcL@ԚL@.Vapour Density profile:Vapour Density at each stage>R Q)@UwE_)@t3n)@5l})@?:u峌)@xWf)@?)@=)@|)@8-xW)@)@J*@9#*@t)*.*@=D*@z6>W[*@P6 r*@],σ*@*@9⪲*@9#J*@Af*@kC+@9}3+@2bR+@pq+@6~+@++MJ+@pn+@9+@Xf,,@gy,,@cbqmH,@ŊLc,@?|,@cC,@'fʩ,@Z/r,@rCQ,@g,@lIF,@6 r,@/L ,@0,@ʡE-@2=a-@du'-@ޓZC-@i-@~-@LOX-@s`?.@+j0.@],σ+/@q&/@ޫV&0@?ޫVV0@!q0@vq 0@R0@K0@Z!0@2Vapour Viscosity profile>Vapour Viscosity at each stage> U%M>>]`78>m^f2>* ,+>F%>E>gP>NE >(P Z>.+?>.֥>4>c} >L8>].8>> 9i붼>`/> >t#>DI>r>kz>Jn> b>JV>]T>J>>>jX3>Ǖ(>KO0> >ǝ"Y >Poc>K3:n>\>?ˍ>%&>zg>I>iB*>q>S2>vr#>'>ӌ>!u>K>>>3 >c> a#?>>%j>KnF%>rq>ҁ>6;ռ>i>ALY>M>͉E>:Vapour Heat capacity profileFVapour Heat capacity at each stage>:ǀQ@MQ@!^/Q@V-%Q@b/Q@-9Q@[DQ@k OQ@F[Q@LfQ@+sQ@ަ?Q@EVQ@GQ@2YةQ@4 Q@,}Q@L=Q@F aQ@';Q@?xR@ʾ+#R@ T7R@ػ?ޫLR@%bR@QxR@_5R@u$R@0duR@%uR@TR@R8R@8m4S@ O#S@?5S@IVFS@-iVS@=eS@#~jrS@J{/L~S@?S@)DS@GS@|͍S@KS@ %̤S@[wTS@R~RS@ͯS@UtU@ U@ -V@ڧuV@i&V@ PSW@5W@m!A WW@ ymW@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stage>*Ú?V}?-?{ͽ?&^)?K%l?Jf?c?|"6 ?[c|?KS~?.Xv? **n?w&ve?-m\?j S?QTI?Q WY>??4?$)?N]?FZ`?>L-?Ʊ??1Tf?Pͼ?FR֙?1Zʙ?–&?-C2E@ףp= CE@BSE@dE@ YuE@NzڇE@X0_E@5E@Ù_E@nE@OXeE@/Q5F@MJF@ S"1F@jeJF@?W[dF@S:F@0GۜF@4iF@1F@F@-σG@m4L@.Liquid Density profile:Liquid Density at each stage>hs@Q@k y@ Ac̔@ O@_Q@h@fa@|a@V-@[잎@X9v@r7@L7A@8m@އ@w/@^@fj@Q@Pn~@aӫ{@y@MJjv@Pns@p_Ιp@Qm@ޓZj@1w-!g@Q|c@?`@rr]@KY8VZ@ΪVW@m{T@^)Q@?5^IO@"L@٬J@HPH@V/;G@QF@MF@4@E@[D@B@ZS@@Ci<@V/8@u1@x#(@(@F@]m2@VX@ڃ@mʃ@?߽@X5ͻ@_vO@A@ףp=@2Liquid Viscosity profile>Liquid Viscosity at each stage>|.&?ݲ8e+}?m$gy?v?Ir?~Vn?8d/j?jf?c!a?[?/V?+^O?ZI?r<A?P?^9?_,01?Ƴ'? ?#?ei>?@bЧ?"Ҍ,?Gs?|&׌?!;y?~c ?B)?i+?Xx?"̗Of?HrrhS?:wA?s/?AʡE`@W2%`@+`@|a2U2`@-C8`@v?`@3F`@Zd;M`@eaU`@) 0]`@d`TRe`@!Acm`@#lxzv`@@`@Zڊ`@lw`@r -`@V/`@7d`@Qkw`@`@V`@N@`@{/L`@*:a@Ca@lV}a@&䃞,a@jo:a@%Ha@Ua@bX9ba@mna@x $(~za@:Ha@~8gDa@-!la@na@ cZBa@~a@)\a@ё\Ca@x $(a@ZӼa@XѾa@~:pa@qha@$a@~a@]ma@ b@W28b@R!_b@猊b@bٵb@2%b@H.b@c@a+/c@Zڊ=c@HPsGc@1w-!Nc@:Liquid Thermal cond. profileFLiquid Thermal cond. at each stage>_NP?p^jG?KMɃ>? a5?<+?X}d)H"?IB? ?C1o?g?UK?!#(?(un?AAΠF?|rv?C|?Kl?Hwƭ8?vWz?&)i?mX?whE?ڥ2?[Rj?qˢ ?Գ ?K:b?\5?;&9?t䚧?2! ? :)?H[p?u$`?ʽP?_B?l*A5?R)?.@7? I?tW ?)x ?ߐ?9w?1?m?0c?g?z?EVȦ??9rJO?y7?kTV.?P^uc0?)Yv?!tpU?3?8Ƚ?g?A|`?ڄ k?0Surface tension profile<Surface tension at each stage>&A K4?X%/?m)?8T$?Dӟ?{d9*?D?|  ?JKzR?}Ӊ>?oT?p?iN?J: ކ?jԆ? O-ˆ?y?a[7?1O?1[?m7^ ? ̈́?qWv?_ܺYh?*O2Y?zJJ?:?*?K'Ⱦ?EF ?#$??Q܎݅?08s΅?C6|?h?|W?GsC׮?x?l#9?0#a?i?稂?K(?;Ʋ|?ESw?1@o?Ve?3WU?j@?/ФH#?cҝ/?eɄ?đ"?oVC? ?zٜ?ը1h?`0?3@?&?hHzς?'+Fy?Number of stagesNSi Feed1 stageF1Ni Reflux ratioRRoCondenser duty QCo?@@J/sReboiler duty QRo?@@J/s Top pressure PPTi?N/m2 1 Converged 1 Iterations ChemSep (TM) - COL2 6.90 Copyright (c) 1988-2012 Harry Kooijman and Ross Taylor License: 2100- 6 LITE free license Build: 6494e2b69d23 Checking data file C:\DOCUME~1\Harry\LOCALS~1\Temp\CS_47_~1.SEP Cape Open unit name: C2 Cape-Open unit id: CS_47_4F4_1CCE13B_46535C10 Cape-Open run level: normal Cape open Initialized Cape Open Thermodynamic-properties disabled Reading configuration Reading component property libraries Reading thermodynamic property options Reading physical property options Reading thermodynamic property data Reading specifications Reading reaction data Checking Component Data 67-56-1 Methanol 67-64-1 Acetone * No class Determining feed conditions Solving TP flash Possible trivial solution Run level: Initialization Reading initial temperature profiles Reading initial composition profiles Init 109 milliseconds Run level: Complete model Iteration log(Err/Tol) 0 0.9310 1 -2.8327 Run level: Report Convergence obtained in 1 iterations Generating equilibrium data Time 47 milliseconds FixMem driver done run time: 0.23 seconds Using: C:\Program Files\ChemSepL6v90\bin\co-col2.exe CAPE-OPEN thermo-properties were disabled. All calculation methods have been determined by ChemSep. See output report or graphical user interface for more information. HVH not all ports are connectedFeed1{split}_stage41 TopProduct BottomProduct @ @0@@ @ @ @(@ @(@$@,@@@@@@@@$@@(@@(@ @(@ @ @ @,@$@@@$@@(@ @,@ @ @,@ @$@0@,@4@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@$@4@,@0@@ 4@,@0@ 4@,@0@4@,@0@ 4@,@0@ 4@,@0@ ,@0@  ,@0@jffff@533331@Valve_61Valve - generates power from pressure difference.tQGt HՐ'aTJCOUSCOUS0002Pressure spec. Pressure drop specification typePressurePressure differencePressure differencePressurePressure differencePressure drop along the valve??+A _BPressureValve outlet pressure?м@j@ _BThermo Version*Thermodynamics CAPE-OPEN Interface version1.11.01.01.1Last runp+++ specifications +++ Pressure: 101325 Pa +++ optional parameters +++ Pressure difference: 911875 Pa <? $not all material ports are connectedInletOutlet0@@@@@?@MS Sans/C6?/C6?h㈵>/C6?,~{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 1 bar \par } I@;@C@F@`9@`<@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 37\b0 \par } ;@;@B@|D@F@33333cH@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 41\b0 \par } ;@;@\ʥ\B@ 0 `D@`aI@~~J@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Script;}} \viewkind4\uc1\pard\b\f0\fs27 x\sub A\nosupersub =0.75\b0 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W@;@@D@I@3@̬6@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Script;}} \viewkind4\uc1\pard\b\f0\fs27 x\sub A\nosupersub =0.75\b0 \par } R@;@V@33333[X@9@̌<@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 RR=3.11 \par } S@;@T@V@@@pB@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\b\f0\fs27 x\sub A\nosupersub =0.994\b0 \par } T@;@V@0X@Q@33333R@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\i\f0\fs27 Ind.Eng.Chem.Res.\i0 (2008) \b 47\b0 pp. 2696-2707 \par } v@<@D@S@&@,@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs42 Pressure Swing Distillation of Acetone-Methanol \par } @C@=@@V@ @'@_=@@@E@F@@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\f0\fs27 43\f1\fs29 \par } 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