FSD100MbP?h㈵>dk%*dfffffr@м@Harry Kooijmanwww.ChemSep.org(Pressure swing azeotropic distillation  Hx temperaturepressure compositionflowMethanol-Acetoneڐ@'t+((Methanol-Acetone& .>MbP?MbP?MbP?R%c:\werk\CO\COCO\bin\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?@?@֤? 8 8`?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:,?? ?activityactivityDactivityCoefficientactivityCoefficientDbubblePointPressurebubblePointPressurebubblePointTemperaturebubblePointTemperaturecompressibilityFactorcompressibilityFactordensitydensitydensity/volume (pure)density/volume (pure)dewPointPressuredewPointPressuredewPointTemperaturedewPointTemperature enthalpyenthalpyentropyentropy: excessEnthalpyexcessEnthalpyfugacityfugacityfugacityCoefficientfugacityCoefficientgibbsFreeEnergy gibbsEnergyGG heatCapacityheatCapacityCpKK heatOfVaporizationheatOfVaporizationOidealGasEnthalpyidealGasEnthalpy logFugacityCoefficientlogFugacityCoefficientsurfaceTensionsurfaceTensionsurfaceTension (pure)surfaceTension (pure)thermalConductivitythermalConductivity04thermalConductivity (pure)thermalConductivity (pure))1 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/Methanoimported from MARGULES.IPD q?Acetone/Methanoimported 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  QGw5EMethanol/Acetoneimported from UNIQUAC.IPDNʞMki@Methanol/Acetoneimported from UNIQUAC.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-Acetone67-56-1Methanolf@@u@CH4OMethanol-AcetoneMethanol67-64-1Acetone= M@̔t@C3H6OMethanol-AcetoneAcetone ????????????thermalConductivity.Dmoles?? / molexcessEnthalpy.Dpressure??gibbsFreeEnergy.Dpressure??viscosity.Dtemperature???? thermalConductivity.Dtemperature??activityCoefficientthermalConductivity.Dpressure??heatCapacity.DmolFraction??heatOfVaporization??enthalpy.Dmoles??density.Dpressure?@?@#logFugacityCoefficient.DmolFractionentropy.Dtemperature??viscosity.Dmoles???? / mol volume.Dmoles@@@@vaporPressure.Dtemperature??enthalpy??fugacity.Dtemperature??activity.DmolFractionexcessEnthalpy.Dtemperature??volume.Dpressure@@@@idealGasEnthalpy.DmolFraction??surfaceTension.DmolFraction??heatOfVaporization.DmolFraction?? activityCoefficient.DtemperaturefugacityCoefficient.Dmoles / molgibbsFreeEnergy??gibbsFreeEnergy.DmolFraction??activity.Dmoles / molactivityCoefficient.Dmoles / molcompressibilityFactor.Dpressure"compressibilityFactor.DtemperatureheatOfVaporization.Dpressure??enthalpy.DmolFraction??logFugacityCoefficiententhalpy.Dpressure??activity fugacityCoefficient.DmolFractionfugacity.Dpressuredensity?@?@volume.DmolFraction@@@@activity.DtemperaturesurfaceTension.Dtemperature??thermalConductivity??density.DmolFraction?@?@surfaceTension??heatCapacity.Dtemperature??#logFugacityCoefficient.DtemperatureexcessEnthalpy??fugacityCoefficient.Dpressureviscosity.DmolFraction????entropy.Dpressure??enthalpy.Dtemperature??surfaceTension.Dmoles?? / molgibbsFreeEnergy.Dmoles?? thermalConductivity.DmolFraction??density.Dmoles?@?@ / molidealGasEnthalpy.Dtemperature??logFugacityCoefficient.Dmoles / molsurfaceTension.Dpressure??heatOfVaporization.Dtemperature??entropy.DmolFraction??entropy??volume@@@@heatCapacity.Dpressure??compressibilityFactorgibbsFreeEnergy.Dtemperature??fugacityCoefficientidealGasEnthalpy??viscosity.Dpressure?? logFugacityCoefficient.Dpressure fugacityCoefficient.Dtemperature heatCapacity??entropy.Dmoles??activityCoefficient.Dpressure viscosity????"compressibilityFactor.DmolFraction activityCoefficient.DmolFractionexcessEnthalpy.Dmoles??heatOfVaporization.Dmoles??volume.Dtemperature@@@@density.Dtemperature?@?@fugacity.Dmoles?? / molheatCapacity.Dmoles??activity.DpressurecompressibilityFactor.Dmoles / molexcessEnthalpy.DmolFraction??@&{71F5AC07-65A1-4357-8F1B-A8CD58148763}RelativePerturbationTemperature??RelativePerturbationPressure??PerturbationComposition??Temperature profile??Pressure profile??Vapour Flow profile??Liquid Flow 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??Duties profile??TotalMassBalancePropertiesFraction?? TotalFlowMass??&{E813F646-A25E-4B14-8873-4853D1AA3252}Pressure increase??Pressure?? Energy demand??]activityactivity.Dtemperatureactivity.DmolFractionactivity.DpressureactivityCoefficient activityCoefficient.Dtemperature activityCoefficient.DmolFractionactivityCoefficient.DpressurebubblePointPressurebubblePointTemperaturecompressibilityFactor"compressibilityFactor.Dtemperature"compressibilityFactor.DmolFractioncompressibilityFactor.Dpressuredensitydensity.Dtemperaturedensity.DmolFractiondensity.DpressuredewPointPressuredewPointTemperatureenthalpyenthalpy.Dtemperatureenthalpy.DmolFractionenthalpy.DpressureexcessEnthalpyexcessEnthalpy.DtemperatureexcessEnthalpy.DmolFractionexcessEnthalpy.Dpressurefugacityfugacity.Dtemperaturefugacity.DmolFractionfugacity.DpressurefugacityCoefficient fugacityCoefficient.Dtemperature fugacityCoefficient.DmolFractionfugacityCoefficient.Dpressure heatCapacityheatCapacity.DtemperatureheatCapacity.DmolFractionheatCapacity.DpressureheatOfVaporizationheatOfVaporization.DtemperatureheatOfVaporization.DmolFractionheatOfVaporization.DpressureidealGasEnthalpyidealGasEnthalpy.DtemperaturelogFugacityCoefficient#logFugacityCoefficient.Dtemperature#logFugacityCoefficient.DmolFraction logFugacityCoefficient.DpressuresurfaceTensionsurfaceTension.DtemperaturesurfaceTension.DmolFractionsurfaceTension.DpressurethermalConductivity thermalConductivity.Dtemperature thermalConductivity.DmolFractionthermalConductivity.Dpressure vaporPressurevaporPressure.Dtemperature viscosityviscosity.Dtemperatureviscosity.DmolFractionviscosity.Dpressurevolumevolume.Dtemperaturevolume.DmolFractionvolume.Dpressureentropyentropy.Dtemperatureentropy.DmolFractionentropy.DpressuregibbsFreeEnergygibbsFreeEnergy.DtemperaturegibbsFreeEnergy.DmolFractiongibbsFreeEnergy.Dpressureactivity.DmolesactivityCoefficient.DmolescompressibilityFactor.Dmolesdensity.Dmolesenthalpy.Dmolesentropy.DmolesexcessEnthalpy.Dmolesfugacity.DmolesfugacityCoefficient.DmolesgibbsFreeEnergy.DmolesheatCapacity.DmolesheatOfVaporization.DmoleslogFugacityCoefficient.DmolessurfaceTension.DmolesthermalConductivity.Dmolesviscosity.Dmoles volume.DmolesVaporMethanol-AcetoneVaporLiquidMethanol-AcetoneLiquid VaporLiquiddefaultdefault material templateMethanol-AcetoneEquimolar Feed2'222'22'2 Gat least one compound needs to be present for materials of type defaultdefaulti@r@?-???)wi1??lDKg???)wi1??lDKg??)wi1??lDKg?r@i@?-??2Methanol3=I>=>3=I>3=3>I>  defaultj@nu@?ƻyh? r?(?@H?AJ9?ׯ ?sWV?ۡbw2l?$*MB?W'b??>(?@H?AJ9?ׯ ?2Pressured FeedF0V0N0F0V0F0V0 defaultO"A=3Yt@]Y* @E*?>(?@H?AJ9?ׯ ??>(?@H?AJ9?ׯ ?2Acetone Rich Productb=>p>b=>b=b>>  defaultO"Aux}x@8?x뎼? 3>P͂>D?^e?}o[ ?J>NA?k?? 3>P͂>D?ae?2Recycled High P Azeotropeb*',F"i,b*i*i"",',   defaultO"Aw""x@]Y*@ڲ2s?9?,1q?cr?W?^c1?P?R,:?,Ӕ??9?,1q?cr?W??)wi1??lDKg?(x@O"AzG?GC] ?2Methanol Column (1 bar)ChemSep Unit OperationqeWCXcCSUO[ChemSep] Version=6.82 Compiled=2011-4-22 18:34 Name=C:\Users\jasper\AppData\Local\Temp\CS_1B_~1.sep Title=ChemSep CO Unit Operation "Methanol Column (1 bar)" in COFE Flowsheet User=jasper Date=2011-05-23 Time=10:18:30 [Cape-Open] unitname=Methanol Column (1 bar) CO_ID=CS_1B_1AC0_1CC1921_FF9E4780 2 components Methanol 67-56-1 32.0419998169 Mw Acetone 67-64-1 58.0800018311 Mw 0 thermo exe=C:\Program Files (x86)\ChemSepL6v70\bin\co-col2.exe mode=COFE NoWarnings=FALSE WilsonEstimate=TRUE Status= 0 only K-values and ethalpies 0 use only perturbed derivative 0 use only perturbed mole derivative 0.001 relative T perturbation 0.001 relative P perturbation 0.001 X perturbation 0 write all values to log 1 use initial guess 0 inlet reflash 0 outlet reflash 0 expose energy ports 0 clear log 0 update icon CO Thermo Version=Auto 2 number of run levels normal simplified 1 current run level [Paths] Device drivers path=c:\program files (x86)\chemsepl6v70\bin\ Help and Info path=c:\program files (x86)\chemsepl6v70\help\ Component data path=c:\program files (x86)\chemsepl6v70\pcd\ Property data path=c:\program files (x86)\chemsepl6v70\ipd\ Section data path=c:\program files (x86)\chemsepl6v70\ild\ Executables path=C:\Program Files (x86)\ChemSepL6v70\bin\ Temporary path=WINTMPDIR Scripts path=c:\program files (x86)\chemsepl6v70\bin\ [Units] Temperature=K Flow=mol/s Mass flow=kg/s Pressure=bar 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=2010-09-20,09:33:26 CHK=28780 CAS=67-56-1 CID=Methanol Name=Methanol Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 62 1051 Library Offset, Index DT=2010-09-20,09:33:26 CHK=8776 CAS=67-64-1 CID=Acetone Name=Acetone Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd [Operation] 2 Operation Column 3 Operation kind Azeotropic Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 40 Stages 2 Feed stages 0 Sidestream stages F=1,16 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 39 Last stage 0 Qcolumn lost to surroundings [Efficiencies] 1 Default efficiency 0 Number [Pressures] 1 Column pressure Constant pressure 100000 Condenser pressure 100000 Top pressure * Pressure Drop * Bottom pressure [Feeds] 2 Number 1 Feed state T & p 1 Stage Feed2{split} 386.182166452 Temperature 600000 Pressure 7.80114227684e-014 Vapour fraction 2 componentflows 0.000665902185484 Component 1 flow 0.00197977723152 Component 2 flow 1 Feed state T & p 16 Stage Feed{split} 300 Temperature 100000 Pressure 0 Vapour fraction 2 componentflows 0.0005 Component 1 flow 0.0005 Component 2 flow [Condenser] 1 Type Reflux ratio 35 Value Qcondenser * Type * * Initialization guess [Reboiler] 4 Type Bottom product flow rate 0.0005 Value Qreboiler * Type * * Initialization guess [Solve options] 3 Initialization Old Results 1 Method Newton's method 0.5 Flow Step limit 10 Temperature Step limit 1 Composition Step limit 1 Flux Step limit 0.000001 Accuracy 30 Maximum iterations 1 Iteration count & function vector 0 T/V/L profiles 0 X/Y profiles 0 Variable and function vectors 0 Jacobian 1 History Screen History file= 1 Feeds type Stage below 1 Interactive 0 Log thermodynamics 0 Log enthalpy/entropy 0 Log physical properties 0 Log timing 0 CO numeric differencing 0 Log from iteration 0 CS K-value 0 CS enthalpy 0 CS entropy 0 CS flash 0 CS activity coefficient 0 CS vapor pressuure 0 CS density 0 CS viscosity 0 CS thermal conductivity 0 CS heat capacity 0 CS surface tension 0 CS diffusivity [Programs] Temporary file=SCRATCH.TMP User program= 8 DOS extender NT 1 Show windows Hidden [FlowSheet] [CoCo] [Settings] ComboBox=ComboBox14 -1 ComboBox=ComboBox20 -1 ComboBox=ComboBox21 -1 CheckBox=CheckBox3 0 Show settings CheckBox=CheckBox1 1 Auto colors CheckBox=CheckBox2 1 Auto points Edit=Edit9 0.2 StringGrid=StringGrid5 2 8 Title Labels Stages Axis color Commands Box Labels box Import data StringGrid=StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 y1 x2 y2 StringGrid=StringGrid3 1 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage CheckBox=CheckBox10 0 Show settings ComboBox=ComboBox22 -1 ComboBox=ComboBox23 -1 StringGrid=StringGrid7 16 2 StringGrid=StringGrid11 5 3 CheckBox=CheckBox45 0 Lumped ComboBox=ComboBox75 -1 ComboBox=ComboBox76 -1 ComboBox=ComboBox77 -1 Edit=Edit55 0.95 Edit=Edit56 0.95 Edit=Edit57 1.2 Edit=Edit1 1 CheckBox=CheckBox2 0 Use old results CheckBox=CheckBox3 1 Automatic CheckBox=CheckBox1 0 Keep sep-files CheckBox=CheckBox4 1 Restore original StringGrid=StringGrid1 1 6 StringGrid=StringGrid2 4 1 StringGrid=StringGrid3 1 1 None ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Binary Phase Diagram ComboBox=ComboBox4 0 ComboBox=ComboBox15 0 Edit=Edit17 Plot font CheckBox=CheckBox2 1 Color=Edit18 1635136 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 1635136 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 1635136 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 1635136 SpinEdit=SpinEdit3 1 ComboBox=ComboBox14 0 RadioButton=RadioButton3 TRUE DrawSetColors=BVLEcolors 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 ComboBox=ComboBox7 -1 ComboBox=ComboBox11 -1 ComboBox=ComboBox6 -1 Memo=Memo1 Memo1, ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox4 0 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Ternary Phase Diagram Edit=Edit4 T Edit=Edit6 0 Edit=Edit7 1 Edit=Edit8 1 Edit=Edit5 StringGrid=StringGrid1 3 5 0 0 ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 Edit=Edit3 21 Edit=Edit4 Binary Property Diagram Memo=Memo1 StringGrid=StringGrid1 13 4 Axis Left Right X/Y Property -click to select- -click to select- x Title x Units - Minimum 0 Maximum 1 Interval 0.2 Grid Off Off Off Log Off Off Off Color Blue Red Black Line Normal Normal Style Solid Solid Point None None Edit=Edit5 ComboBox=ComboBox7 -1 ComboBox=ComboBox6 -1 [End Settings] [End of Input] [Results] 1 Converged 2 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 328.0808222 1.000000000E+05 3.145679417E-03 1.095578923E-01 -3.435520631E+06 2 328.0808465 1.000000000E+05 1.100578923E-01 1.095536940E-01 0.000000000E+00 3 328.0808781 1.000000000E+05 1.100536940E-01 1.095484295E-01 0.000000000E+00 4 328.0809193 1.000000000E+05 1.100484295E-01 1.095418256E-01 0.000000000E+00 5 328.0809735 1.000000000E+05 1.100418256E-01 1.095335380E-01 0.000000000E+00 6 328.0810456 1.000000000E+05 1.100335380E-01 1.095231316E-01 0.000000000E+00 7 328.0811425 1.000000000E+05 1.100231316E-01 1.095100557E-01 0.000000000E+00 8 328.0812743 1.000000000E+05 1.100100557E-01 1.094936113E-01 0.000000000E+00 9 328.0814560 1.000000000E+05 1.099936113E-01 1.094729080E-01 0.000000000E+00 10 328.0817100 1.000000000E+05 1.099729080E-01 1.094468074E-01 0.000000000E+00 11 328.0820704 1.000000000E+05 1.099468074E-01 1.094138457E-01 0.000000000E+00 12 328.0825897 1.000000000E+05 1.099138457E-01 1.093721297E-01 0.000000000E+00 13 328.0833500 1.000000000E+05 1.098721297E-01 1.093191909E-01 0.000000000E+00 14 328.0844810 1.000000000E+05 1.098191909E-01 1.092517800E-01 0.000000000E+00 15 328.0861915 1.000000000E+05 1.097517800E-01 1.091655703E-01 0.000000000E+00 16 328.0888225 1.000000000E+05 1.096655703E-01 1.102398396E-01 0.000000000E+00 17 328.0905124 1.000000000E+05 1.097398396E-01 1.101769277E-01 0.000000000E+00 18 328.0929507 1.000000000E+05 1.096769277E-01 1.100946268E-01 0.000000000E+00 19 328.0965454 1.000000000E+05 1.095946268E-01 1.099864250E-01 0.000000000E+00 20 328.1019740 1.000000000E+05 1.094864250E-01 1.098432566E-01 0.000000000E+00 21 328.1103923 1.000000000E+05 1.093432566E-01 1.096522481E-01 0.000000000E+00 22 328.1238339 1.000000000E+05 1.091522481E-01 1.093946866E-01 0.000000000E+00 23 328.1460025 1.000000000E+05 1.088946866E-01 1.090426220E-01 0.000000000E+00 24 328.1839107 1.000000000E+05 1.085426220E-01 1.085530582E-01 0.000000000E+00 25 328.2514180 1.000000000E+05 1.080530582E-01 1.078580033E-01 0.000000000E+00 26 328.3771464 1.000000000E+05 1.073580033E-01 1.068485613E-01 0.000000000E+00 27 328.6221969 1.000000000E+05 1.063485613E-01 1.053575697E-01 0.000000000E+00 28 329.1152243 1.000000000E+05 1.048575697E-01 1.031846984E-01 0.000000000E+00 29 330.0854118 1.000000000E+05 1.026846984E-01 1.003190910E-01 0.000000000E+00 30 331.7315150 1.000000000E+05 9.981909104E-02 9.737088813E-02 0.000000000E+00 31 333.7706523 1.000000000E+05 9.687088813E-02 9.525388968E-02 0.000000000E+00 32 335.4715632 1.000000000E+05 9.475388968E-02 9.414860903E-02 0.000000000E+00 33 336.4911252 1.000000000E+05 9.364860903E-02 9.366386108E-02 0.000000000E+00 34 336.9902878 1.000000000E+05 9.316386108E-02 9.346336999E-02 0.000000000E+00 35 337.2111382 1.000000000E+05 9.296336999E-02 9.338141538E-02 0.000000000E+00 36 337.3045175 1.000000000E+05 9.288141538E-02 9.334793699E-02 0.000000000E+00 37 337.3432453 1.000000000E+05 9.284793699E-02 9.333425180E-02 0.000000000E+00 38 337.3591787 1.000000000E+05 9.283425180E-02 9.332865504E-02 0.000000000E+00 39 337.3657124 1.000000000E+05 9.282865504E-02 9.332636565E-02 0.000000000E+00 40 337.3683879 1.000000000E+05 9.282636565E-02 5.000000000E-04 3.416246636E+06 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2890473E+08 -0.2890473E+08 -0.8337587E+05 -0.8337587E+05 2 0.2107463E+07 -0.2890607E+08 0.1072345E+05 -0.8337818E+05 3 0.2107309E+07 -0.2890776E+08 0.1072478E+05 -0.8338107E+05 4 0.2107115E+07 -0.2890987E+08 0.1072644E+05 -0.8338469E+05 5 0.2106873E+07 -0.2891252E+08 0.1072852E+05 -0.8338925E+05 6 0.2106570E+07 -0.2891585E+08 0.1073112E+05 -0.8339498E+05 7 0.2106189E+07 -0.2892004E+08 0.1073439E+05 -0.8340218E+05 8 0.2105712E+07 -0.2892530E+08 0.1073848E+05 -0.8341126E+05 9 0.2105112E+07 -0.2893192E+08 0.1074361E+05 -0.8342271E+05 10 0.2104359E+07 -0.2894028E+08 0.1075005E+05 -0.8343718E+05 11 0.2103413E+07 -0.2895082E+08 0.1075813E+05 -0.8345552E+05 12 0.2102222E+07 -0.2896418E+08 0.1076828E+05 -0.8347882E+05 13 0.2100722E+07 -0.2898112E+08 0.1078103E+05 -0.8350854E+05 14 0.2098830E+07 -0.2900270E+08 0.1079706E+05 -0.8354662E+05 15 0.2096440E+07 -0.2903030E+08 0.1081724E+05 -0.8359573E+05 16 0.2093415E+07 -0.2906579E+08 0.1084267E+05 -0.8365951E+05 17 0.2091738E+07 -0.2908574E+08 0.1085671E+05 -0.8369566E+05 18 0.2089568E+07 -0.2911184E+08 0.1087480E+05 -0.8374330E+05 19 0.2086759E+07 -0.2914616E+08 0.1089814E+05 -0.8380650E+05 20 0.2083113E+07 -0.2919158E+08 0.1092824E+05 -0.8389110E+05 21 0.2078374E+07 -0.2925220E+08 0.1096710E+05 -0.8400570E+05 22 0.2072202E+07 -0.2933396E+08 0.1101723E+05 -0.8416325E+05 23 0.2064154E+07 -0.2944578E+08 0.1108181E+05 -0.8438410E+05 24 0.2053658E+07 -0.2960141E+08 0.1116465E+05 -0.8470138E+05 25 0.2040030E+07 -0.2982269E+08 0.1126983E+05 -0.8517133E+05 26 0.2022573E+07 -0.3014504E+08 0.1140002E+05 -0.8589299E+05 27 0.2000970E+07 -0.3062462E+08 0.1155103E+05 -0.8704172E+05 28 0.1976197E+07 -0.3133613E+08 0.1169410E+05 -0.8889914E+05 29 0.1951074E+07 -0.3231238E+08 0.1172507E+05 -0.9173867E+05 30 0.1925545E+07 -0.3338316E+08 0.1137780E+05 -0.9530715E+05 31 0.1891249E+07 -0.3420777E+08 0.1034112E+05 -0.9858040E+05 32 0.1850394E+07 -0.3466263E+08 0.8810736E+04 -0.1008186E+06 33 0.1818680E+07 -0.3486909E+08 0.7417267E+04 -0.1020923E+06 34 0.1800930E+07 -0.3495605E+08 0.6484797E+04 -0.1027500E+06 35 0.1792586E+07 -0.3499190E+08 0.5959619E+04 -0.1030719E+06 36 0.1788965E+07 -0.3500660E+08 0.5689946E+04 -0.1032243E+06 37 0.1787447E+07 -0.3501262E+08 0.5558407E+04 -0.1032950E+06 38 0.1786820E+07 -0.3501508E+08 0.5496203E+04 -0.1033272E+06 39 0.1786562E+07 -0.3501609E+08 0.5467383E+04 -0.1033418E+06 40 0.1786457E+07 -0.3501650E+08 0.5454223E+04 -0.1033483E+06 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.5259630E+02 0.1982354E+01 0.8698623E-05 0.7256665E+05 0.1447316E-01 2 0.5259290E+02 0.1982222E+01 0.8698896E-05 0.7256230E+05 0.1447378E-01 3 0.5258863E+02 0.1982058E+01 0.8699239E-05 0.7255684E+05 0.1447456E-01 4 0.5258329E+02 0.1981852E+01 0.8699668E-05 0.7255001E+05 0.1447553E-01 5 0.5257658E+02 0.1981593E+01 0.8700207E-05 0.7254143E+05 0.1447675E-01 6 0.5256816E+02 0.1981268E+01 0.8700883E-05 0.7253067E+05 0.1447828E-01 7 0.5255759E+02 0.1980861E+01 0.8701733E-05 0.7251715E+05 0.1448020E-01 8 0.5254431E+02 0.1980348E+01 0.8702801E-05 0.7250017E+05 0.1448262E-01 9 0.5252761E+02 0.1979704E+01 0.8704145E-05 0.7247882E+05 0.1448567E-01 10 0.5250658E+02 0.1978892E+01 0.8705838E-05 0.7245193E+05 0.1448950E-01 11 0.5248006E+02 0.1977869E+01 0.8707975E-05 0.7241805E+05 0.1449433E-01 12 0.5244658E+02 0.1976576E+01 0.8710677E-05 0.7237526E+05 0.1450045E-01 13 0.5240419E+02 0.1974938E+01 0.8714102E-05 0.7232111E+05 0.1450819E-01 14 0.5235040E+02 0.1972860E+01 0.8718458E-05 0.7225242E+05 0.1451803E-01 15 0.5228189E+02 0.1970210E+01 0.8724018E-05 0.7216497E+05 0.1453059E-01 16 0.5219426E+02 0.1966819E+01 0.8731152E-05 0.7205317E+05 0.1454669E-01 17 0.5214523E+02 0.1964921E+01 0.8735155E-05 0.7199066E+05 0.1455572E-01 18 0.5208133E+02 0.1962445E+01 0.8740382E-05 0.7190922E+05 0.1456750E-01 19 0.5199773E+02 0.1959204E+01 0.8747242E-05 0.7180271E+05 0.1458295E-01 20 0.5188780E+02 0.1954938E+01 0.8756297E-05 0.7166277E+05 0.1460332E-01 21 0.5174231E+02 0.1949285E+01 0.8768341E-05 0.7147772E+05 0.1463039E-01 22 0.5154816E+02 0.1941729E+01 0.8784524E-05 0.7123108E+05 0.1466670E-01 23 0.5128628E+02 0.1931515E+01 0.8806551E-05 0.7089892E+05 0.1471601E-01 24 0.5092817E+02 0.1917507E+01 0.8837049E-05 0.7044571E+05 0.1478408E-01 25 0.5042995E+02 0.1897940E+01 0.8880217E-05 0.6981704E+05 0.1488004E-01 26 0.4972202E+02 0.1869987E+01 0.8943055E-05 0.6892733E+05 0.1501897E-01 27 0.4869197E+02 0.1829020E+01 0.9037688E-05 0.6763976E+05 0.1522657E-01 28 0.4716234E+02 0.1767638E+01 0.9185228E-05 0.6574052E+05 0.1554649E-01 29 0.4489602E+02 0.1675925E+01 0.9418579E-05 0.6294467E+05 0.1604315E-01 30 0.4177117E+02 0.1549202E+01 0.9765967E-05 0.5909647E+05 0.1676026E-01 31 0.3824975E+02 0.1407611E+01 0.1018773E-04 0.5473301E+05 0.1759361E-01 32 0.3534995E+02 0.1292629E+01 0.1055648E-04 0.5110315E+05 0.1828927E-01 33 0.3358724E+02 0.1223528E+01 0.1078963E-04 0.4887835E+05 0.1871408E-01 34 0.3271312E+02 0.1189487E+01 0.1090773E-04 0.4776986E+05 0.1892505E-01 35 0.3232366E+02 0.1174367E+01 0.1096087E-04 0.4727487E+05 0.1901908E-01 36 0.3215846E+02 0.1167962E+01 0.1098351E-04 0.4706470E+05 0.1905898E-01 37 0.3208985E+02 0.1165304E+01 0.1099293E-04 0.4697737E+05 0.1907555E-01 38 0.3206160E+02 0.1164210E+01 0.1099681E-04 0.4694142E+05 0.1908237E-01 39 0.3205002E+02 0.1163761E+01 0.1099840E-04 0.4692667E+05 0.1908517E-01 40 0.3204527E+02 0.1163578E+01 0.1099905E-04 0.4692063E+05 0.1908632E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.5256786E+02 0.6623587E+03 0.2625789E-03 0.1397345E+06 0.1578635E+00 0.1944663E-01 2 0.5256358E+02 0.6623565E+03 0.2625991E-03 0.1397322E+06 0.1578710E+00 0.1944668E-01 3 0.5255820E+02 0.6623537E+03 0.2626244E-03 0.1397293E+06 0.1578805E+00 0.1944675E-01 4 0.5255147E+02 0.6623503E+03 0.2626562E-03 0.1397256E+06 0.1578923E+00 0.1944683E-01 5 0.5254301E+02 0.6623460E+03 0.2626960E-03 0.1397210E+06 0.1579072E+00 0.1944694E-01 6 0.5253239E+02 0.6623405E+03 0.2627461E-03 0.1397153E+06 0.1579258E+00 0.1944707E-01 7 0.5251904E+02 0.6623337E+03 0.2628090E-03 0.1397080E+06 0.1579493E+00 0.1944724E-01 8 0.5250226E+02 0.6623251E+03 0.2628881E-03 0.1396989E+06 0.1579788E+00 0.1944745E-01 9 0.5248113E+02 0.6623143E+03 0.2629878E-03 0.1396875E+06 0.1580159E+00 0.1944770E-01 10 0.5245449E+02 0.6623005E+03 0.2631134E-03 0.1396731E+06 0.1580627E+00 0.1944803E-01 11 0.5242084E+02 0.6622832E+03 0.2632720E-03 0.1396549E+06 0.1581217E+00 0.1944843E-01 12 0.5237825E+02 0.6622612E+03 0.2634727E-03 0.1396318E+06 0.1581965E+00 0.1944894E-01 13 0.5232420E+02 0.6622331E+03 0.2637275E-03 0.1396026E+06 0.1582913E+00 0.1944957E-01 14 0.5225536E+02 0.6621972E+03 0.2640521E-03 0.1395655E+06 0.1584120E+00 0.1945035E-01 15 0.5216731E+02 0.6621511E+03 0.2644671E-03 0.1395181E+06 0.1585663E+00 0.1945132E-01 16 0.5205406E+02 0.6620913E+03 0.2650010E-03 0.1394573E+06 0.1587646E+00 0.1945253E-01 17 0.5199040E+02 0.6620574E+03 0.2653010E-03 0.1394231E+06 0.1588760E+00 0.1945318E-01 18 0.5190711E+02 0.6620129E+03 0.2656937E-03 0.1393785E+06 0.1590217E+00 0.1945401E-01 19 0.5179759E+02 0.6619540E+03 0.2662099E-03 0.1393200E+06 0.1592131E+00 0.1945505E-01 20 0.5165264E+02 0.6618753E+03 0.2668931E-03 0.1392427E+06 0.1594662E+00 0.1945637E-01 21 0.5145922E+02 0.6617691E+03 0.2678049E-03 0.1391400E+06 0.1598035E+00 0.1945799E-01 22 0.5119833E+02 0.6616236E+03 0.2690347E-03 0.1390020E+06 0.1602577E+00 0.1945995E-01 23 0.5084158E+02 0.6614208E+03 0.2707164E-03 0.1388143E+06 0.1608775E+00 0.1946222E-01 24 0.5034526E+02 0.6611312E+03 0.2730561E-03 0.1385551E+06 0.1617374E+00 0.1946464E-01 25 0.4964007E+02 0.6607051E+03 0.2763808E-03 0.1381902E+06 0.1629547E+00 0.1946667E-01 26 0.4861406E+02 0.6600550E+03 0.2812171E-03 0.1376654E+06 0.1647169E+00 0.1946686E-01 27 0.4709059E+02 0.6590235E+03 0.2883892E-03 0.1368976E+06 0.1673161E+00 0.1946156E-01 28 0.4483374E+02 0.6573402E+03 0.2989491E-03 0.1357817E+06 0.1711301E+00 0.1944209E-01 29 0.4172268E+02 0.6546520E+03 0.3131547E-03 0.1342897E+06 0.1763142E+00 0.1939115E-01 30 0.3821788E+02 0.6509017E+03 0.3279385E-03 0.1327142E+06 0.1820249E+00 0.1929052E-01 31 0.3533260E+02 0.6469330E+03 0.3380247E-03 0.1315815E+06 0.1865734E+00 0.1915582E-01 32 0.3357904E+02 0.6439465E+03 0.3425346E-03 0.1310221E+06 0.1892376E+00 0.1903937E-01 33 0.3270954E+02 0.6422531E+03 0.3441208E-03 0.1307980E+06 0.1905210E+00 0.1896846E-01 34 0.3232216E+02 0.6414456E+03 0.3446595E-03 0.1307124E+06 0.1910832E+00 0.1893351E-01 35 0.3215784E+02 0.6410923E+03 0.3448537E-03 0.1306790E+06 0.1913198E+00 0.1891801E-01 36 0.3208960E+02 0.6409437E+03 0.3449282E-03 0.1306657E+06 0.1914177E+00 0.1891144E-01 37 0.3206151E+02 0.6408822E+03 0.3449578E-03 0.1306603E+06 0.1914579E+00 0.1890872E-01 38 0.3204998E+02 0.6408569E+03 0.3449697E-03 0.1306581E+06 0.1914744E+00 0.1890760E-01 39 0.3204526E+02 0.6408465E+03 0.3449746E-03 0.1306572E+06 0.1914811E+00 0.1890714E-01 40 0.3204333E+02 0.6408423E+03 0.3449765E-03 0.1306569E+06 0.1914839E+00 0.1890695E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.210603874E+00 0.210734492E+00 0.210898241E+00 0.211103579E+00 0.211361163E+00 2 0.789396126E+00 0.789265508E+00 0.789101759E+00 0.788896421E+00 0.788638837E+00 Component Mole fractions on stages: 6 to 10 1 0.211684429E+00 0.212090350E+00 0.212600416E+00 0.213241910E+00 0.214049580E+00 2 0.788315571E+00 0.787909650E+00 0.787399584E+00 0.786758090E+00 0.785950420E+00 Component Mole fractions on stages: 11 to 15 1 0.215067878E+00 0.216353954E+00 0.217981762E+00 0.220047749E+00 0.222678908E+00 2 0.784932122E+00 0.783646046E+00 0.782018238E+00 0.779952251E+00 0.777321092E+00 Component Mole fractions on stages: 16 to 20 1 0.226044419E+00 0.227927302E+00 0.230381299E+00 0.233592058E+00 0.237813999E+00 2 0.773955581E+00 0.772072698E+00 0.769618701E+00 0.766407942E+00 0.762186001E+00 Component Mole fractions on stages: 21 to 25 1 0.243401503E+00 0.250858006E+00 0.260915717E+00 0.274669002E+00 0.293803336E+00 2 0.756598497E+00 0.749141994E+00 0.739084283E+00 0.725330998E+00 0.706196664E+00 Component Mole fractions on stages: 26 to 30 1 0.320991655E+00 0.360551264E+00 0.419297348E+00 0.506336078E+00 0.626347469E+00 2 0.679008345E+00 0.639448736E+00 0.580702652E+00 0.493663922E+00 0.373652531E+00 Component Mole fractions on stages: 31 to 35 1 0.761588983E+00 0.872956678E+00 0.940654539E+00 0.974225485E+00 0.989182889E+00 2 0.238411017E+00 0.127043322E+00 0.593454606E-01 0.257745151E-01 0.108171110E-01 Component Mole fractions on stages: 36 to 40 1 0.995527483E+00 0.998162438E+00 0.999247136E+00 0.999692035E+00 0.999874242E+00 2 0.447251740E-02 0.183756204E-02 0.752864425E-03 0.307964884E-03 0.125757638E-03 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.211696008E+00 0.211860541E+00 0.212066863E+00 0.212325681E+00 0.212650495E+00 2 0.788303992E+00 0.788139459E+00 0.787933137E+00 0.787674319E+00 0.787349505E+00 Component Mole fractions on stages: 6 to 10 1 0.213058361E+00 0.213570872E+00 0.214215440E+00 0.215026984E+00 0.216050167E+00 2 0.786941639E+00 0.786429128E+00 0.785784560E+00 0.784973016E+00 0.783949833E+00 Component Mole fractions on stages: 11 to 15 1 0.217342416E+00 0.218978042E+00 0.221053961E+00 0.223697782E+00 0.227079513E+00 2 0.782657584E+00 0.781021958E+00 0.778946039E+00 0.776302218E+00 0.772920487E+00 Component Mole fractions on stages: 16 to 20 1 0.231428856E+00 0.233873716E+00 0.237072504E+00 0.241278676E+00 0.246845261E+00 2 0.768571144E+00 0.766126284E+00 0.762927496E+00 0.758721324E+00 0.753154739E+00 Component Mole fractions on stages: 21 to 25 1 0.254273763E+00 0.264293546E+00 0.277994673E+00 0.297055872E+00 0.324139114E+00 2 0.745726237E+00 0.735706454E+00 0.722005327E+00 0.702944128E+00 0.675860886E+00 Component Mole fractions on stages: 26 to 30 1 0.363543337E+00 0.422052971E+00 0.508727967E+00 0.628209534E+00 0.762812962E+00 2 0.636456663E+00 0.577947029E+00 0.491272033E+00 0.371790466E+00 0.237187038E+00 Component Mole fractions on stages: 31 to 35 1 0.873623276E+00 0.940969437E+00 0.974362802E+00 0.989240483E+00 0.995551156E+00 2 0.126376724E+00 0.590305633E-01 0.256371978E-01 0.107595166E-01 0.444884387E-02 Component Mole fractions on stages: 36 to 40 1 0.998172006E+00 0.999250895E+00 0.999693411E+00 0.999874642E+00 0.999948819E+00 2 0.182799364E-02 0.749105443E-03 0.306589187E-03 0.125358090E-03 0.511809336E-04 [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 [Condenser Heat Duty] -3.435520631E+06 [Reboiler Heat Duty] 3.416246636E+06 [K-values] Component K-values on stages: 1 to 5 1 0.994841024E+00 0.994684955E+00 0.994489369E+00 0.994244214E+00 0.993936852E+00 2 0.100138542E+01 0.100142874E+01 0.100148315E+01 0.100155153E+01 0.100163756E+01 Component K-values on stages: 6 to 10 1 0.993551382E+00 0.993067772E+00 0.992460750E+00 0.991698372E+00 0.990740178E+00 2 0.100174591E+01 0.100188259E+01 0.100205530E+01 0.100227406E+01 0.100255193E+01 Component K-values on stages: 11 to 15 1 0.989534772E+00 0.988016660E+00 0.986102043E+00 0.983683193E+00 0.980620864E+00 2 0.100290617E+01 0.100335981E+01 0.100394405E+01 0.100470182E+01 0.100569348E+01 Component K-values on stages: 16 to 20 1 0.976733943E+00 0.974574251E+00 0.971775704E+00 0.968142158E+00 0.963413264E+00 2 0.100700578E+01 0.100776166E+01 0.100877043E+01 0.101013102E+01 0.101199124E+01 Component K-values on stages: 21 to 25 1 0.957241911E+00 0.949164329E+00 0.938563727E+00 0.924637511E+00 0.906411240E+00 2 0.101457943E+01 0.101826209E+01 0.102365489E+01 0.103184730E+01 0.104488465E+01 Component K-values on stages: 26 to 30 1 0.882952931E+00 0.854279649E+00 0.824207386E+00 0.805998717E+00 0.821102288E+00 2 0.106685716E+01 0.110641409E+01 0.118203890E+01 0.132780146E+01 0.157534970E+01 Component K-values on stages: 31 to 35 1 0.871759039E+00 0.927720549E+00 0.965404815E+00 0.984821691E+00 0.993603275E+00 2 0.188651039E+01 0.215216160E+01 0.231481838E+01 0.239550857E+01 0.243144313E+01 Component K-values on stages: 36 to 40 1 0.997350633E+00 0.998910727E+00 0.999553588E+00 0.999817370E+00 0.999925419E+00 2 0.244668104E+01 0.245300852E+01 0.245561310E+01 0.245668137E+01 0.245711887E+01 [Molecular weights] 1 32.042 2 58.080 [Feed stream 1] 1 Stage Number 2.6456794170040E-03 Flow rate 3.8618216645200E+02 Temperature [K] 6.0000000000000E+05 Pressure [Pa] -2.0444173275015E+07 Enthalpy [J/kmol] -5.3702144144011E+04 Entropy [J/kmol/K] 4.2963069111917E-10 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.5169420799973E-01 Mole fraction of component 1 7.4830579200027E-01 Mole fraction of component 2 1.1366650764072E-12 Flow rate 3.1210213808568E-01 Mole fraction of component 1 6.8789786191432E-01 Mole fraction of component 2 2.6456794158673E-03 Flow rate 2.5169420797377E-01 Mole fraction of component 1 7.4830579202623E-01 Mole fraction of component 2 4.9953485730956E+01 Molar mass 1.0436993466414E+01 Density 1.0568508371965E-05 Viscosity 2.1520320112878E-02 Thermal conductivity 7.7142843055812E+04 Heat capacity 5.1526387536881E+01 Molar mass 5.9354607704263E+02 Density 1.7803082758180E-04 Viscosity 1.3992201507061E-01 Thermal conductivity 1.6529636407336E+05 Heat capacity 1.2971566305194E-02 Surface tension [Feed stream 2] 16 Stage Number 1.0000000000000E-03 Flow rate 3.0000000000000E+02 Temperature [K] 1.0000000000000E+05 Pressure [Pa] -3.5070547044808E+07 Enthalpy [J/kmol] -1.0030716855153E+05 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 1.0000000000000E-03 Flow rate 5.0000000000000E-01 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 4.5061000823975E+01 Molar mass 6.8358158999561E+02 Density 3.9993718326464E-04 Viscosity 1.8057598019588E-01 Thermal conductivity 1.2632928094219E+05 Heat capacity 2.2433383238054E-02 Surface tension [Reflashed Feed stream 1] 1 Stage Number 2.6456794170040E-03 Flow rate 3.2811102440520E+02 Temperature [K] 1.0000000000000E+05 Pressure [Pa] -2.0444173275015E+07 Enthalpy [J/kmol] -7.3043965974989E+04 Entropy [J/kmol/K] 2.8123116346101E-01 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.5169420799973E-01 Mole fraction of component 1 7.4830579200027E-01 Mole fraction of component 2 7.4404750058887E-04 Flow rate 2.4378654992641E-01 Mole fraction of component 1 7.5621345007359E-01 Mole fraction of component 2 1.9016319164151E-03 Flow rate 2.5478822066021E-01 Mole fraction of component 1 7.4521177933979E-01 Mole fraction of component 2 5.1732287153046E+01 Molar mass 1.9488951679376E+00 Density 8.7691737521506E-06 Viscosity 1.4632260258849E-02 Thermal conductivity 7.1464975518726E+04 Heat capacity 5.1445825628320E+01 Molar mass 6.6176165876623E+02 Density 2.6786799595984E-04 Viscosity 1.5982680029639E-01 Thermal conductivity 1.3913289498040E+05 Heat capacity 1.9458094809044E-02 Surface tension [Reflashed Feed stream 2] 16 Stage Number 1.0000000000000E-03 Flow rate 3.0000000000796E+02 Temperature [K] 1.0000000000000E+05 Pressure [Pa] -3.5070547044808E+07 Enthalpy [J/kmol] -1.0030716854830E+05 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 1.0000000000000E-03 Flow rate 5.0000000000000E-01 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 4.5061000823975E+01 Molar mass 6.8358158998903E+02 Density 3.9993718322878E-04 Viscosity 1.8057598019313E-01 Thermal conductivity 1.2632928094461E+05 Heat capacity 2.2433383237241E-02 Surface tension [Top product] 1 Stage Number 3.1456794170041E-03 Flow rate 3.2808082216932E+02 Temperature [K] 1.0000000000000E+05 Pressure [Pa] -2.8904731285310E+07 Enthalpy [J/kmol] -8.3375873938891E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.1169600829352E-01 Mole fraction of component 1 7.8830399170647E-01 Mole fraction of component 2 3.1456794170041E-03 Flow rate 2.1169600829352E-01 Mole fraction of component 1 7.8830399170647E-01 Mole fraction of component 2 5.2567860740718E+01 Molar mass 6.6235866159547E+02 Density 2.6257887005133E-04 Viscosity 1.5786350175569E-01 Thermal conductivity 1.3973452602007E+05 Heat capacity 1.9446628009259E-02 Surface tension [Bottom product] 40 Stage Number 5.0000000000000E-04 Flow rate 3.3736838794714E+02 Temperature [K] 1.0000000000000E+05 Pressure [Pa] -3.5016504360889E+07 Enthalpy [J/kmol] -1.0334828605047E+05 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9994881906634E-01 Mole fraction of component 1 5.1180933648804E-05 Mole fraction of component 2 5.0000000000000E-04 Flow rate 9.9994881906634E-01 Mole fraction of component 1 5.1180933648804E-05 Mole fraction of component 2 3.2043332466148E+01 Molar mass 6.4084229070168E+02 Density 3.4497654695547E-04 Viscosity 1.9148390256898E-01 Thermal conductivity 1.3065685320233E+05 Heat capacity 1.8906951806361E-02 Surface tension [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlash AutoDUseOnlyKValuesAndEnthalpyFromCOSE*RestartDataAvailable,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts UseInitialGuess(Temperature profile4Temperature at each stage(8 Kt@%Kt@gFKt@1 rKt@|eުKt@xKt@ \Lt@GLt@ΤMt@%Nt@? )Pt@ǓIRt@AfUt@"¿Zt@V at@bJ$kt@^!rt@?߹|t@Ey0st@0}t@c*āt@.jA9t@&Vt@'XLt@zt@ܩt@Òt@Foבt@{]t@It@eTt@څt@u@ *8u@r`u@Mu@}u@*2u@>u@u@"Pressure profile.Pressure at each stage(j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@j@(Vapour Flow profile4Vapour Flow at each stage(]Y* @-灴[@so[@X x[@HE[@K|%[@D`z[@ۨ[@S[@D~[@~|[@Ŭr|z[@w[@+mt[@\r)p[@+j[@I1Yo[@jPRk[@Ԑ]f[@,J@㈵$J@uJ@2J@}i J@yܝI@ı.nI@4I@|\*I@ۿҤI@mIFvI@%u7I@j&kH@yXH@jǔG@GȰrF@ԲD@C@^)ˬA@s)*@@#G[@@ݰm)@@jH@@m4 @@@@@,g@@Hh@@.Vapour Density profile:Vapour Density at each stage(<Ӹ?_vj.?g s?1Xq?oܚ? F?M?#/kb?*ެ?xe?[Y?'? X?bՐ??H?ǘ?[]N ?s֧?i ?8؛?AF@#?( 5?3?$^?:?õÞ?{?2Vapour Viscosity profile>Vapour Viscosity at each stage(sJ >>D)/>> M^>>C>> ~VX>>F0@@?>?>[G@>T(eA>~CA>MC>TD>#0YF>4PH>okK>*ndO> ƏQ>4|tT>ipG#X>װK]>σXwc> 'l> 4'w>.Z>V(>D>~.ja>9HC>>9H{>~]>-Dw#>Yt>| >P>p>~kw >>>W>>:Vapour Heat capacity profileFVapour Heat capacity at each stage(ё\C$R@##R@F=D#R@E$]3#R@ʦ"R@M!R@HP!R@. R@*R@3kR@TR@߄BR@R@67'R@Tގ R@6$#gR@%]3fQ@70Q@Ù_Q@GjQ@J)Q@Q@n燹Q@`Lm?(2J)?u9F.?#"l?jL)?La?jhfڼy?o3.2?}?|R,T?S?@]?4Liquid Moleweight profile@Liquid Moleweight at each stage(qZHJ@Wc#HJ@HPsGJ@\FJ@SZEJ@[[%DJ@moBJ@c AJ@J@=J@-s,:J@l5J@#~j0J@}b)J@qZ J@%jjJ@&pJ@\mI@3.I@mI@ I@ՐǺI@hbI@{kI@Nz1,I@KRH@䠄NH@sG@jF@:ǀD@9}C@&SA@@@4Z@@( <)@@4@@]Fx @@@0G@@e@@e@@wb֋@@.Liquid Density profile:Liquid Density at each stage(޲@1ڲ@d`Բ@OjͲ@T㥛IJ@NbX@gj@p_Ι@鷯@Clg@ё\C@@ecݱ@+ݓ@hs5@~@S!u@Pk@ʡ@QI@Ԛ'@I.!@Ac]@镲 @Gx @= ףp@ 0@Ǻ@K7u@mV}6W@X9v7@Pn@JY@Ș @^K@镲@@߾@c@ʡ@^K@2Liquid Viscosity profile>Liquid Viscosity at each stage(5W51?>䋮51?g561?ʣ61?N71?P%81?Yb491?4ʇ:1?/4<1?BrO>1?]D@1?d@VD1?uH1?ZI"N1?<U1?Lߠ]1?RP\c1?i1?dzBr1?"}1?I1?<1?P1޽1?31?EK2?b#a? n2?Ϛ.^2?+3?U1݅4?!}5?a '6?r6?c6?9Gm6?d]6?7٥V6?(1xn6?aa6?6??9ɾ6?:Liquid Heat capacity profileFLiquid Heat capacity at each stage(/$wa@3ı.nwa@!lVwa@I}8wa@Pnwa@ZӼva@-va@ec]va@va@ ua@Dta@37ta@:Hsa@ktra@؁sFpa@3na@ ma@'1la@ ףp=ja@W2ga@Gzda@Mb`a@@߾Za@O@aQa@`vOFa@EJ5a@x#a@鷯`@48E`@Yږ`@S㥛r`@' ``@K7Y`@tV`@}?5^U`@OjMU`@1w-!U`@/'U`@]KU`@&SU`@:Liquid Thermal cond. profileFLiquid Thermal cond. at each stage(R4?O5?]m5?%e5?sM6?6?5®7? 98?_q9?՛f;?$T=?l??^B?8+F?r_K?OaeR?E| V?vZmZ?!Ha?hpci?$pt?Q7S?HĔH?!ťϳ?_?Lq?,j?_?GA]?Cq \?Y\?sׯd\?&W\? 1 Converged 2 Iterations 1ChemSep (TM) - COL2 6.81 Copyright (c) 1988-2011 Harry Kooijman and Ross Taylor 2100 6 LITE free license Checking data file C:\Users\jasper\AppData\Local\Temp\CS_1B_~1.SEP Cape Open unit name: Methanol Column (1 bar) Cape-Open unit id: CS_1B_1AC0_1CC1921_FF9E4780 Cape-Open run level: normal Cape open Initialized Cape Open Thermodynamic-properties enabled Reading configuration Reading component property libraries Reading thermodynamic property options Reading specifications Reading reaction data Checking Component Data 67-56-1 Methanol 67-64-1 Acetone * No class Determining feed conditions Run level: Initialization Reading initial temperature profiles Reading initial composition profiles Init 47 milliseconds Run level: Complete model Iteration Error 0 0.9184 1 2.0708 2 -1.7247 Run level: Report Convergence obtained in 2 iterations Time 172 milliseconds FixMem driver done run time: 0.33 seconds Using: C:\Program Files (x86)\ChemSepL6v70\bin\co-col2.exe Using CAPE-OPEN version 1.0 thermodynamics CAPE-OPEN thermo-properties were enabled CAPE-OPEN diffusion coefficients were disabled CAPE-OPEN supplied derivatives were enabled CAPE-OPEN supplied molar derivatives were enabled Inlet re-flash: <none> Outlet flash: Auto Flash used for TopProduct: PVF Flash used for BottomProduct: PVF CAPE-OPEN supplied d H / d T have been used CAPE-OPEN supplied d H / d x have been used CAPE-OPEN supplied d K / d T have been used CAPE-OPEN supplied d K / d x and d K / d y have been used Relative perturbation of pressure: 0.001 Relative perturbation of temperature: 0.001 Perturbation of composition: 0.001"'!5=not all ports are connectedFeed{split}_stage16Feed2{split}_stage1 TopProduct BottomProduct @ @0@@$@,@@$@0@,@4@@@@@@@$@@@(@@(@ @(@ @ @ @ffffff,@ɿ#@@ ɿ#@@ɿ#@@ ɿ#@@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@#@3333334@ffffff,@/@ 3333334@ffffff,@/@3333334@ffffff,@/@ 3333334@ffffff,@/@ 334@ffffff,@/@ 334@ffffff,@/@ ffffff,@/@  ffffff,@/@? @@ @?(@@(@@>@message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 330.09 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 331.73 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 333.77 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 335.47 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 336.49 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 336.99 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 337.21 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 337.30 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 337.34 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 337.36 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 337.37 K, range = [190.00 - 329.44] K)  (last message repeated 1 time) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 386.18 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 386.18 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 386.18 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 337.37 K, range = [190.00 - 329.44] K) Acetone Column (6 bar)ChemSep Unit OperationqeWCXcDžCSUO\[ChemSep] Version=6.82 Compiled=2011-4-22 18:34 Name=C:\Users\jasper\AppData\Local\Temp\CS_1C_~1.sep Title=ChemSep CO Unit Operation "Acetone Column (6 bar)" in COFE Flowsheet User=jasper Date=2011-05-23 Time=10:18:32 [Cape-Open] unitname=Acetone Column (6 bar) CO_ID=CS_1C_1AC0_1CC1921_FF9EBCB0 2 components Methanol 67-56-1 32.0419998169 Mw Acetone 67-64-1 58.0800018311 Mw 0 thermo exe=C:\Program Files (x86)\ChemSepL6v70\bin\co-col2.exe mode=COFE NoWarnings=FALSE WilsonEstimate=TRUE Status= 0 only K-values and ethalpies 0 use only perturbed derivative 0 use only perturbed mole derivative 0.001 relative T perturbation 0.001 relative P perturbation 0.001 X perturbation 0 write all values to log 1 use initial guess 0 inlet reflash 0 outlet reflash 0 expose energy ports 0 clear log 0 update icon CO Thermo Version=Auto 2 number of run levels normal simplified 1 current run level [Paths] Device drivers path=c:\program files (x86)\chemsepl6v70\bin\ Help and Info path=c:\program files (x86)\chemsepl6v70\help\ Component data path=c:\program files (x86)\chemsepl6v70\pcd\ Property data path=c:\program files (x86)\chemsepl6v70\ipd\ Section data path=c:\program files (x86)\chemsepl6v70\ild\ Executables path=C:\Program Files (x86)\ChemSepL6v70\bin\ Temporary path=WINTMPDIR Scripts path=c:\program files (x86)\chemsepl6v70\bin\ [Units] Temperature=K Flow=mol/s Mass flow=kg/s Pressure=bar 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=2010-09-20,09:33:26 CHK=28780 CAS=67-56-1 CID=Methanol Name=Methanol Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd 62 1051 Library Offset, Index DT=2010-09-20,09:33:26 CHK=8776 CAS=67-64-1 CID=Acetone Name=Acetone Lib=c:\program files (x86)\chemsepl6v70\pcd\chemsep1.pcd [Operation] 2 Operation Column 3 Operation kind Azeotropic Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 20 Stages 1 Feed stages 0 Sidestream stages F=10 S= 0 Pumparound stages P= [Properties] 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 19 Last stage 0 Qcolumn lost to surroundings [Efficiencies] 1 Default efficiency 0 Number [Pressures] 1 Column pressure Constant pressure 600000 Condenser pressure 600000 Top pressure * Pressure Drop * Bottom pressure [Feeds] 1 Number 1 Feed state T & p 10 Stage Feed1{split} 328.459277973 Temperature 600000 Pressure 0 Vapour fraction 2 componentflows 0.000665927775951 Component 1 flow 0.00247975164105 Component 2 flow [Condenser] 1 Type Reflux ratio 50 Value Qcondenser * Type * * Initialization guess [Reboiler] 4 Type Bottom product flow rate 0.0005 Value Qreboiler * Type * * Initialization guess [Solve options] 3 Initialization Old Results 1 Method Newton's method 0.5 Flow Step limit 10 Temperature Step limit 1 Composition Step limit 1 Flux Step limit 0.000001 Accuracy 30 Maximum iterations 1 Iteration count & function vector 0 T/V/L profiles 0 X/Y profiles 0 Variable and function vectors 0 Jacobian 1 History Screen History file= 1 Feeds type Stage below 1 Interactive 0 Log thermodynamics 0 Log enthalpy/entropy 0 Log physical properties 0 Log timing 0 CO numeric differencing 0 Log from iteration 0 CS K-value 0 CS enthalpy 0 CS entropy 0 CS flash 0 CS activity coefficient 0 CS vapor pressuure 0 CS density 0 CS viscosity 0 CS thermal conductivity 0 CS heat capacity 0 CS surface tension 0 CS diffusivity [Programs] Temporary file=SCRATCH.TMP User program= 8 DOS extender NT 1 Show windows Hidden [FlowSheet] [CoCo] [Settings] ComboBox=ComboBox14 -1 ComboBox=ComboBox20 -1 ComboBox=ComboBox21 -1 CheckBox=CheckBox3 0 Show settings CheckBox=CheckBox1 1 Auto colors CheckBox=CheckBox2 1 Auto points Edit=Edit9 0.2 StringGrid=StringGrid5 2 8 Title Labels Stages Axis color Commands Box Labels box Import data StringGrid=StringGrid4 5 9 Title Start End Tic interval Small tics Grid Logarithmic Scientific notation x1 y1 x2 y2 StringGrid=StringGrid3 1 14 Label Plot X Plot Y X axis Y axis Units X Units Y Color Points Thickness Style 1st stage Last stage CheckBox=CheckBox10 0 Show settings ComboBox=ComboBox22 -1 ComboBox=ComboBox23 -1 StringGrid=StringGrid7 16 2 StringGrid=StringGrid11 5 3 CheckBox=CheckBox45 0 Lumped ComboBox=ComboBox75 -1 ComboBox=ComboBox76 -1 ComboBox=ComboBox77 -1 Edit=Edit55 0.95 Edit=Edit56 0.95 Edit=Edit57 1.2 Edit=Edit1 1 CheckBox=CheckBox2 0 Use old results CheckBox=CheckBox3 1 Automatic CheckBox=CheckBox1 0 Keep sep-files CheckBox=CheckBox4 1 Restore original StringGrid=StringGrid1 1 6 StringGrid=StringGrid2 4 1 StringGrid=StringGrid3 1 1 None ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Binary Phase Diagram ComboBox=ComboBox4 0 ComboBox=ComboBox15 0 Edit=Edit17 Plot font CheckBox=CheckBox2 1 Color=Edit18 1635136 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 1635136 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 1635136 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 1635136 SpinEdit=SpinEdit3 1 ComboBox=ComboBox14 0 RadioButton=RadioButton3 TRUE DrawSetColors=BVLEcolors 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 ComboBox=ComboBox7 -1 ComboBox=ComboBox11 -1 ComboBox=ComboBox6 -1 Memo=Memo1 Memo1, ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox4 0 Edit=Edit1 Edit=Edit2 21 Edit=Edit3 Ternary Phase Diagram Edit=Edit4 T Edit=Edit6 0 Edit=Edit7 1 Edit=Edit8 1 Edit=Edit5 StringGrid=StringGrid1 3 5 0 0 ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 Edit=Edit3 21 Edit=Edit4 Binary Property Diagram Memo=Memo1 StringGrid=StringGrid1 13 4 Axis Left Right X/Y Property -click to select- -click to select- x Title x Units - Minimum 0 Maximum 1 Interval 0.2 Grid Off Off Off Log Off Off Off Color Blue Red Black Line Normal Normal Style Solid Solid Point None None Edit=Edit5 ComboBox=ComboBox7 -1 ComboBox=ComboBox6 -1 [End Settings] [End of Input] [Results] 1 Converged 1 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 386.1821214 6.000000000E+05 2.645679417E-03 1.322839709E-01 -3.637222495E+06 2 387.0289041 6.000000000E+05 1.349296503E-01 1.344494236E-01 0.000000000E+00 3 388.0431182 6.000000000E+05 1.370951030E-01 1.365532386E-01 0.000000000E+00 4 389.0593321 6.000000000E+05 1.391989181E-01 1.383768366E-01 0.000000000E+00 5 389.9196109 6.000000000E+05 1.410225160E-01 1.397873491E-01 0.000000000E+00 6 390.5541169 6.000000000E+05 1.424330285E-01 1.407746163E-01 0.000000000E+00 7 390.9775552 6.000000000E+05 1.434202957E-01 1.414144388E-01 0.000000000E+00 8 391.2419913 6.000000000E+05 1.440601182E-01 1.418075696E-01 0.000000000E+00 9 391.4004353 6.000000000E+05 1.444532490E-01 1.420410110E-01 0.000000000E+00 10 391.4930455 6.000000000E+05 1.446866904E-01 1.466251001E-01 0.000000000E+00 11 391.6418558 6.000000000E+05 1.461251001E-01 1.468487133E-01 0.000000000E+00 12 391.7284032 6.000000000E+05 1.463487133E-01 1.469782055E-01 0.000000000E+00 13 391.7780689 6.000000000E+05 1.464782055E-01 1.470523363E-01 0.000000000E+00 14 391.8063516 6.000000000E+05 1.465523363E-01 1.470944938E-01 0.000000000E+00 15 391.8223870 6.000000000E+05 1.465944938E-01 1.471183776E-01 0.000000000E+00 16 391.8314561 6.000000000E+05 1.466183776E-01 1.471318797E-01 0.000000000E+00 17 391.8365780 6.000000000E+05 1.466318797E-01 1.471395034E-01 0.000000000E+00 18 391.8394684 6.000000000E+05 1.466395034E-01 1.471438050E-01 0.000000000E+00 19 391.8410988 6.000000000E+05 1.466438050E-01 1.471462313E-01 0.000000000E+00 20 391.8420182 6.000000000E+05 1.466462313E-01 5.000000000E-04 3.665255220E+06 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2044422E+08 -0.2044422E+08 -0.6066652E+05 -0.6066652E+05 2 0.6512219E+07 -0.1973173E+08 0.7178963E+04 -0.5926396E+05 3 0.6785169E+07 -0.1905997E+08 0.7274670E+04 -0.5808449E+05 4 0.7043392E+07 -0.1849979E+08 0.7220051E+04 -0.5722637E+05 5 0.7255519E+07 -0.1808280E+08 0.7044973E+04 -0.5668267E+05 6 0.7409710E+07 -0.1779989E+08 0.6818054E+04 -0.5637829E+05 7 0.7511910E+07 -0.1762056E+08 0.6601438E+04 -0.5622524E+05 8 0.7575528E+07 -0.1751194E+08 0.6427746E+04 -0.5615509E+05 9 0.7613587E+07 -0.1744801E+08 0.6303483E+04 -0.5612541E+05 10 0.7635814E+07 -0.1741102E+08 0.6221333E+04 -0.5611366E+05 11 0.7671507E+07 -0.1735215E+08 0.6068456E+04 -0.5610673E+05 12 0.7692253E+07 -0.1731822E+08 0.5961406E+04 -0.5611292E+05 13 0.7704155E+07 -0.1729886E+08 0.5889411E+04 -0.5612238E+05 14 0.7710932E+07 -0.1728786E+08 0.5842342E+04 -0.5613115E+05 15 0.7714773E+07 -0.1728164E+08 0.5812192E+04 -0.5613806E+05 16 0.7716946E+07 -0.1727812E+08 0.5793175E+04 -0.5614307E+05 17 0.7718173E+07 -0.1727613E+08 0.5781323E+04 -0.5614652E+05 18 0.7718866E+07 -0.1727501E+08 0.5774005E+04 -0.5614882E+05 19 0.7719256E+07 -0.1727438E+08 0.5769522E+04 -0.5615031E+05 20 0.7719476E+07 -0.1727403E+08 0.5766794E+04 -0.5615127E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.4995339E+02 0.1043697E+02 0.1056852E-04 0.7714270E+05 0.2152034E-01 2 0.5152629E+02 0.1076800E+02 0.1043580E-04 0.7960010E+05 0.2123708E-01 3 0.5312972E+02 0.1109999E+02 0.1030828E-04 0.8213710E+05 0.2096090E-01 4 0.5456917E+02 0.1139388E+02 0.1019960E-04 0.8444039E+05 0.2072125E-01 5 0.5570606E+02 0.1162355E+02 0.1011714E-04 0.8627572E+05 0.2053618E-01 6 0.5651048E+02 0.1178488E+02 0.1006044E-04 0.8758248E+05 0.2040698E-01 7 0.5703453E+02 0.1188950E+02 0.1002417E-04 0.8843730E+05 0.2032345E-01 8 0.5735732E+02 0.1195376E+02 0.1000208E-04 0.8896516E+05 0.2027221E-01 9 0.5754922E+02 0.1199190E+02 0.9989038E-05 0.8927947E+05 0.2024182E-01 10 0.5766089E+02 0.1201408E+02 0.9981478E-05 0.8946252E+05 0.2022415E-01 11 0.5783959E+02 0.1204953E+02 0.9969426E-05 0.8975572E+05 0.2019592E-01 12 0.5794312E+02 0.1207006E+02 0.9962469E-05 0.8992571E+05 0.2017959E-01 13 0.5800240E+02 0.1208180E+02 0.9958493E-05 0.9002310E+05 0.2017024E-01 14 0.5803612E+02 0.1208848E+02 0.9956235E-05 0.9007850E+05 0.2016492E-01 15 0.5805522E+02 0.1209226E+02 0.9954956E-05 0.9010989E+05 0.2016191E-01 16 0.5806602E+02 0.1209440E+02 0.9954233E-05 0.9012764E+05 0.2016021E-01 17 0.5807212E+02 0.1209561E+02 0.9953826E-05 0.9013767E+05 0.2015925E-01 18 0.5807556E+02 0.1209629E+02 0.9953595E-05 0.9014332E+05 0.2015870E-01 19 0.5807750E+02 0.1209668E+02 0.9953466E-05 0.9014651E+05 0.2015840E-01 20 0.5807859E+02 0.1209689E+02 0.9953392E-05 0.9014831E+05 0.2015822E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.5152629E+02 0.5935461E+03 0.1780311E-03 0.1652963E+06 0.1399222E+00 0.1297158E-01 2 0.5316127E+02 0.5930547E+03 0.1737123E-03 0.1667819E+06 0.1364294E+00 0.1276593E-01 3 0.5462812E+02 0.5922882E+03 0.1697294E-03 0.1682622E+06 0.1332088E+00 0.1255162E-01 4 0.5578598E+02 0.5913948E+03 0.1664936E-03 0.1695601E+06 0.1305926E+00 0.1235709E-01 5 0.5660481E+02 0.5905671E+03 0.1641450E-03 0.1705656E+06 0.1286939E+00 0.1220284E-01 6 0.5713805E+02 0.5899228E+03 0.1625840E-03 0.1712671E+06 0.1274320E+00 0.1209365E-01 7 0.5746641E+02 0.5894790E+03 0.1616090E-03 0.1717201E+06 0.1266438E+00 0.1202257E-01 8 0.5766159E+02 0.5891967E+03 0.1610240E-03 0.1719975E+06 0.1261709E+00 0.1197881E-01 9 0.5777515E+02 0.5890257E+03 0.1606817E-03 0.1721619E+06 0.1258942E+00 0.1195282E-01 10 0.5784041E+02 0.5889252E+03 0.1604844E-03 0.1722574E+06 0.1257347E+00 0.1193770E-01 11 0.5794358E+02 0.5887627E+03 0.1601714E-03 0.1724099E+06 0.1254817E+00 0.1191351E-01 12 0.5800266E+02 0.5886677E+03 0.1599916E-03 0.1724981E+06 0.1253363E+00 0.1189950E-01 13 0.5803626E+02 0.5886130E+03 0.1598892E-03 0.1725486E+06 0.1252535E+00 0.1189148E-01 14 0.5805530E+02 0.5885818E+03 0.1598311E-03 0.1725773E+06 0.1252065E+00 0.1188692E-01 15 0.5806606E+02 0.5885641E+03 0.1597982E-03 0.1725935E+06 0.1251800E+00 0.1188434E-01 16 0.5807214E+02 0.5885541E+03 0.1597796E-03 0.1726027E+06 0.1251650E+00 0.1188288E-01 17 0.5807557E+02 0.5885484E+03 0.1597692E-03 0.1726079E+06 0.1251565E+00 0.1188205E-01 18 0.5807750E+02 0.5885452E+03 0.1597633E-03 0.1726108E+06 0.1251517E+00 0.1188159E-01 19 0.5807860E+02 0.5885434E+03 0.1597599E-03 0.1726124E+06 0.1251490E+00 0.1188133E-01 20 0.5807921E+02 0.5885424E+03 0.1597580E-03 0.1726134E+06 0.1251475E+00 0.1188118E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.312105702E+00 0.251698137E+00 0.190117718E+00 0.134835085E+00 0.911720322E-01 2 0.687894298E+00 0.748301863E+00 0.809882282E+00 0.865164915E+00 0.908827968E+00 Component Mole fractions on stages: 6 to 10 1 0.602780522E-01 0.401518871E-01 0.277550714E-01 0.203850326E-01 0.160962792E-01 2 0.939721948E+00 0.959848113E+00 0.972244929E+00 0.979614967E+00 0.983903721E+00 Component Mole fractions on stages: 11 to 15 1 0.923313020E-02 0.525702929E-02 0.298031237E-02 0.168541470E-02 0.951757520E-03 2 0.990766870E+00 0.994742971E+00 0.997019688E+00 0.998314585E+00 0.999048242E+00 Component Mole fractions on stages: 16 to 20 1 0.536990831E-03 0.302795273E-03 0.170650291E-03 0.961167396E-04 0.540870147E-04 2 0.999463009E+00 0.999697205E+00 0.999829350E+00 0.999903883E+00 0.999945913E+00 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.251698137E+00 0.188905946E+00 0.132570897E+00 0.881028725E-01 0.566551479E-01 2 0.748301863E+00 0.811094054E+00 0.867429103E+00 0.911897128E+00 0.943344852E+00 Component Mole fractions on stages: 6 to 10 1 0.361761451E-01 0.235653892E-01 0.160694638E-01 0.117079199E-01 0.920174833E-02 2 0.963823855E+00 0.976434611E+00 0.983930536E+00 0.988292080E+00 0.990798252E+00 Component Mole fractions on stages: 11 to 15 1 0.523923329E-02 0.297027713E-02 0.167978737E-02 0.948625627E-03 0.535269083E-03 2 0.994760767E+00 0.997029723E+00 0.998320213E+00 0.999051374E+00 0.999464731E+00 Component Mole fractions on stages: 16 to 20 1 0.301869552E-03 0.170173665E-03 0.958933953E-04 0.540064902E-04 0.303892755E-04 2 0.999698130E+00 0.999829826E+00 0.999904107E+00 0.999945994E+00 0.999969611E+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 [Condenser Heat Duty] -3.637222495E+06 [Reboiler Heat Duty] 3.665255220E+06 [K-values] Component K-values on stages: 1 to 5 1 0.124000005E+01 0.133239923E+01 0.143408336E+01 0.153042780E+01 0.160924533E+01 2 0.919273802E+00 0.922583342E+00 0.933658185E+00 0.948752758E+00 0.963410110E+00 Component K-values on stages: 6 to 10 1 0.166623757E+01 0.170384994E+01 0.172719337E+01 0.174113188E+01 0.174926314E+01 2 0.974993452E+00 0.983013202E+00 0.988123544E+00 0.991220093E+00 0.993041438E+00 Component K-values on stages: 11 to 15 1 0.176230561E+01 0.176987839E+01 0.177422001E+01 0.177669109E+01 0.177809171E+01 2 0.995985068E+00 0.997706435E+00 0.998697287E+00 0.999262511E+00 0.999583289E+00 Component K-values on stages: 16 to 20 1 0.177888372E+01 0.177933098E+01 0.177958336E+01 0.177972572E+01 0.177980600E+01 2 0.999764808E+00 0.999867356E+00 0.999925236E+00 0.999957887E+00 0.999976302E+00 [Molecular weights] 1 32.042 2 58.080 [Feed stream 1] 10 Stage Number 3.1456794170010E-03 Flow rate 3.2845927797300E+02 Temperature [K] 6.0000000000000E+05 Pressure [Pa] -2.8851821521340E+07 Enthalpy [J/kmol] -8.3221507179380E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.1169600829377E-01 Mole fraction of component 1 7.8830399170623E-01 Mole fraction of component 2 3.1456794170010E-03 Flow rate 2.1169600829377E-01 Mole fraction of component 1 7.8830399170623E-01 Mole fraction of component 2 5.2567860740712E+01 Molar mass 6.6256247327049E+02 Density 2.6175594594190E-04 Viscosity 1.5772412188263E-01 Thermal conductivity 1.3987427750248E+05 Heat capacity 1.9403624665658E-02 Surface tension [Reflashed Feed stream 1] 10 Stage Number 3.1456794170010E-03 Flow rate 3.2845927797300E+02 Temperature [K] 6.0000000000000E+05 Pressure [Pa] -2.8851821521340E+07 Enthalpy [J/kmol] -8.3221507179379E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.1169600829377E-01 Mole fraction of component 1 7.8830399170623E-01 Mole fraction of component 2 3.1456794170010E-03 Flow rate 2.1169600829377E-01 Mole fraction of component 1 7.8830399170623E-01 Mole fraction of component 2 5.2567860740712E+01 Molar mass 6.6256247327049E+02 Density 2.6175594594190E-04 Viscosity 1.5772412188263E-01 Thermal conductivity 1.3987427750248E+05 Heat capacity 1.9403624665658E-02 Surface tension [Top product] 1 Stage Number 2.6456794170010E-03 Flow rate 3.8618212140471E+02 Temperature [K] 6.0000000000000E+05 Pressure [Pa] -2.0444216925298E+07 Enthalpy [J/kmol] -6.0666516530240E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 2.5169813736000E-01 Mole fraction of component 1 7.4830186263991E-01 Mole fraction of component 2 2.6456794170010E-03 Flow rate 2.5169813736000E-01 Mole fraction of component 1 7.4830186263991E-01 Mole fraction of component 2 5.1526285223510E+01 Molar mass 5.9354609798633E+02 Density 1.7803109447408E-04 Viscosity 1.3992223094168E-01 Thermal conductivity 1.6529627556226E+05 Heat capacity 1.2971578248139E-02 Surface tension [Bottom product] 20 Stage Number 5.0000000000000E-04 Flow rate 3.9184201823437E+02 Temperature [K] 6.0000000000000E+05 Pressure [Pa] -1.7274025207500E+07 Enthalpy [J/kmol] -5.6151270129740E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 3.0389275480326E-05 Mole fraction of component 1 9.9996961072493E-01 Mole fraction of component 2 5.0000000000000E-04 Flow rate 3.0389275480326E-05 Mole fraction of component 1 9.9996961072493E-01 Mole fraction of component 2 5.8079210555063E+01 Molar mass 5.8854239464538E+02 Density 1.5975804465518E-04 Viscosity 1.2514749770887E-01 Thermal conductivity 1.7261337883993E+05 Heat capacity 1.1881179323917E-02 Surface tension [End of Results] GUIArguments /kpldUseCOSEThermo:UseCOSEDiffusionCoefficients8UsePerturbedDerivativesOnly"UsePerturbed_ddX"SuppressWarnings@RelativePerturbationTemperatureMbP?:RelativePerturbationPressureMbP?0PerturbationCompositionMbP?InletReflash<none>OutletFlash AutoDUseOnlyKValuesAndEnthalpyFromCOSE*RestartDataAvailable,OmitStageFromPortNameWilsonEstimate"LogPropertyCallsEnergyPorts UseInitialGuess(Temperature profile4Temperature at each stagen!"x@C%dv0x@̭@x@Q7Px@H빶^x@hx@ox@D2sx@Z.hvx@ wx@[ Ezx@${x@_r|x@=q|x@}ZE(}x@XM}x@蜟b}x@hjvn}x@G$u}x@0zx}x@"Pressure profile.Pressure at each stageO"AO"AO"AO"AO"AO"AO"AO"AO"AO"AO"AO"AO"AO"AO"AO"AO"AO"AO"AO"A(Vapour Flow profile4Vapour Flow at each stage]Y*@f`@ Xr #a@}]fa@`tysa@^a@sa@}b@; b@EO%^b@>Db@e˨(Kb@uMOb@-Qb@Sb@ҿSb@3[8Tb@ʕvTb@ Tb@dCTb@(Liquid Flow profile4Liquid Flow at each stage$J`@a`@Po!a@ La@a1ya@Znɘa@1(Ca@ͧ3׹a@LOa@>Tb@e˨([b@uM_b@-ab@cb@ҿcb@3[8db@ʕvdb@ db@dCdb@?Duties profile*Duties at each stage(\?K(KA4Vapour Moleweight profile@Vapour Moleweight at each stage*H@x]I@:J@HK@Á,`K@hWAL@]zkL@viL@'ILL@q $ L@:dwL@ 'L@UNM@]M@ rM@pWsM@h:; M@aq8 M@R M@u< M@.Vapour Density profile:Vapour Density at each stage&$@K7%@ڧ13&@&@sA?'@ۑ'@Cl'@Gw;S'@Q'@,g~5(@~W[(@#(@')(@>$@M-(@:u0(@AL1(@Z| 1(@oꐛ1(@2Vapour Viscosity profile>Vapour Viscosity at each stageT)>D>n>V77>Yc>;<"7>]VX(>e)o>ah>->I>=eyK>$.8P>'l>؄6>->B]#>m>a>1JQ>ǯ>:Vapour Heat capacity profileFVapour Heat capacity at each stageH.!IS@ hS@?ƈT@߉Y/U@eU@1ZGU@#V@r.=V@#QV@o|]V@;k]pV@"'>{V@i"lxzV@/$V@ pV@Uj@+V@ԕψV@77',V@]zk`V@9}V@HVapour Thermal conductivity profileTVapour Thermal conductivity at each stagem ?Z @P,?/v?6T7?\go?K+>?^ϔ?<”?*eE?A[??=?Yc\?^!䁧??_LR?औ?+]?hdt{?ZpRg?>[?4Liquid Moleweight profile@Liquid Moleweight at each stagex]I@~J@UtLiquid Viscosity at each stageU'?yK&?,:q,?&?QL"%?]WHʃ%? iO%?vN.%?%?@ K%?%?$myu$?am$?"$?Fܱ $?;$?)PP$?)R$?boL$?g$?BŖ$?:Liquid Heat capacity profileFLiquid Heat capacity at each stage9#J{d@&Sd@\ Ace@V1e@+eRe@_Lhe@0' we@Re@H.e@f?õ^?ڹmZ?s3e+X?$V?)' V?͆FU?`U?C=U?M(U? 1 Converged 1 Iterations )ChemSep (TM) - COL2 6.81 Copyright (c) 1988-2011 Harry Kooijman and Ross Taylor 2100 6 LITE free license Checking data file C:\Users\jasper\AppData\Local\Temp\CS_1C_~1.SEP Cape Open unit name: Acetone Column (6 bar) Cape-Open unit id: CS_1C_1AC0_1CC1921_FF9EBCB0 Cape-Open run level: normal Cape open Initialized Cape Open Thermodynamic-properties enabled Reading configuration Reading component property libraries Reading thermodynamic property options Reading specifications Reading reaction data Checking Component Data 67-56-1 Methanol 67-64-1 Acetone * No class Determining feed conditions Possible trivial solution Run level: Initialization Reading initial temperature profiles Reading initial composition profiles Init 31 milliseconds Run level: Complete model Iteration Error 0 0.6542 1 -4.3628 Run level: Report Convergence obtained in 1 iterations Time 78 milliseconds FixMem driver done run time: 0.22 seconds Using: C:\Program Files (x86)\ChemSepL6v70\bin\co-col2.exe Using CAPE-OPEN version 1.0 thermodynamics CAPE-OPEN thermo-properties were enabled CAPE-OPEN diffusion coefficients were disabled CAPE-OPEN supplied derivatives were enabled CAPE-OPEN supplied molar derivatives were enabled Inlet re-flash: <none> Outlet flash: Auto Flash used for TopProduct: PVF Flash used for BottomProduct: PVF CAPE-OPEN supplied d H / d T have been used CAPE-OPEN supplied d H / d x have been used CAPE-OPEN supplied d K / d T have been used CAPE-OPEN supplied d K / d x and d K / d y have been used Relative perturbation of pressure: 0.001 Relative perturbation of temperature: 0.001 Perturbation of composition: 0.001#V"d=not all ports are connectedFeed1{split}_stage10 TopProduct BottomProduct @ @0@@$@,@@$@0@,@4@@@@@@@$@@@(@@(@ @(@ @ @ @ffffff,@ɿ#@@ ɿ#@@ɿ#@@ ɿ#@@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@#@3333334@ffffff,@/@ 3333334@ffffff,@/@3333334@ffffff,@/@ 3333334@ffffff,@/@ 334@ffffff,@/@ 334@ffffff,@/@ ffffff,@/@  ffffff,@/@? @@ @?(@@(@@=@message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 386.18 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 386.18 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 386.18 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 387.03 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 387.03 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 387.03 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 388.04 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 388.04 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 388.04 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 389.06 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 389.06 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 389.06 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 389.92 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 389.92 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 389.92 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 390.55 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 390.55 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 390.55 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 390.98 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 390.98 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 390.98 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.24 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.24 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.24 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.40 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.40 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.40 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.49 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.49 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.49 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.64 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.64 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.64 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.73 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.73 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.73 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.78 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.78 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.78 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.81 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.81 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.81 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.82 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.82 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.82 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.83 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.83 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.83 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.84 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.84 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.84 K, range = [178.45 - 343.15] K) $(last 3 messages repeated 3 times) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 386.18 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 386.18 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 386.18 K, range = [178.45 - 343.15] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methanol (T = 391.84 K, range = [175.47 - 337.85] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Acetone (T = 391.84 K, range = [190.00 - 329.44] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Acetone (T = 391.84 K, range = [178.45 - 343.15] K) Pump>Pump - unit increasing the pressure due to the work performed.F^KsHSѪ2RCOUSCOUS0002Pressure spec.Operation typePressurePressure increasePressure increasePressure Energy spec.Operation type Efficiency Efficiency Energy demand EfficiencyPressure increasePressure increase?A _BPressurePressure?O"Aj@ _B Energy demand Energy demand@?@C6-d@@xDAdiabatic efficiencyAdiabatic efficiency???Thermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Last run+++ specifications +++ Pressure: 600000 Pa Adiabatic efficiency: 0.75 +++ optional parameters +++ Pressure increase: 500000 Pa Energy demand: 166.437155694164 W Adiabatic efficiency: 0.75 $B.F2 $not all material ports are connectedInletOutlet@@?K(^&?@@@@?:t= @@?:t= @@?:t= @@@MS Sans -C6?-C6?h㈵>-C6?Xt|