FSD100MbP?h㈵>dk /2dfffffr@м@Harry Kooijmanwww.ChemSep.org"Extractive azeotropic distillationRestoring flowsheet from file Loaded CScasebook_MCHT.fsd Saved CScasebook_MCHT.fsd jMx temperaturepressure compositionflowMCH-Tol Extractionڐ@'t+@0<0MCH-Tol Extraction:0yE>MbP?MbP?MbP?2C:\Program Files\COCO\data\DefaultComponentLib.pcdyPhenolC6H5OHC6H6O108-95-2 c1ccccc1(O)@TbWA@O??p|@̠s@s@Tg@`;W@Ķ?`I?d=`&@୊9?[̠s@z@i@h} A)@?ЯjY@p@/?`k@RVw %@`f2t@`f@h=w~@ K@> @`r@o|@e`|> #g?z@Ef@`f~@e@=܉A?V?@.4?Ef@`f~@j2Û@v^0 ?D@Ef@d@`H@%@@`?g|>@3Cf@@@ @̮E)@@)7>tUb@p@;k?u#9L@3@@f@@hv$|@¿좗>@g@zw@er\^>@??5/@h 8Ef@@@fVq<`GU>Ef@}@`Xo> a?@ g@`@ 8zw@@@f? c? 8 8 8Ef@`f~@j~@0_п͟? 8b@p@ 8 8 8 8 8 8 8;5@@ ݄F 8 8`fh@@3@ n?k^< ? 8 8g@zw@ x#4@@33333ξ =DQOI?Zb#>@a@v@v@ ?w@>W? 8 8f?@?4?f??`[@ H?"@s@yS&y?4?Z?Methylcyclohexane (C6H11)CH3C7H14108-87-2 C1CCCCC1(C)@|JAO?K7?aw@`Rb@`Rb@2#? X@`h?@?`=@ ?EoA@q@zAAYAY~A@33%@[C> 8 8 8`Rb@`c@&?@?@`? 8`Rb@ @i'W@̥@5^%`| >@`Rb@ @eaA@?6Y?ׁ`E ?`Rb@ @j@3@ W"v?|(@`Rb@d@@ d @`p"?`Rb@t@`=@$ d+@ X*<0}>i@p@ ?Ho@`E@@q@P@h` D@޿Q>@o@Gaw@e>? \kp@j@ 8Gaw@@fP?z4o ?@D{`a>`fq@Gaw@{?2?z.@Y@ 8Gaw@@f`R'?`? 8 8 8`Rb@ @jp@Kտ@^ ? 8i@p@ 8 8 8 8 8 8 84@@nrF 8 8 \e@ @ @? ⣿`? 8 8o@Gaw@ K7Ac@YU7i?">7G< @G@?5@?5@"?@!H@`"l? 8 8KY?`Ӽ?@Ď?ื?Eט?za@`h?@@جt@ F?rm?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 QI&?"MethylCycloHexane/Phenol p482 1/2dimported from NRTL.IPDQI&?"MethylCycloHexane/Phenol p482 1/2dimported from NRTL.IPDO {Gz? Phenol/phenolimported from HAYDENO.IPDZ&k"MethylCycloHexane/Phenol p482 1/2dimported from NRTL.IPDD7\@"MethylCycloHexane/Phenol p482 1/2dimported from NRTL.IPD7 4!=p"MethylCycloHexane/Phenol p482 1/2dimported from UNIQUAC.IPDGz`Methyl Cyclohexane/Tolueneimported from UNIQUACP.IPDa@"MethylCycloHexane/Phenol p482 1/2dimported from UNIQUAC.IPD33333Kj@Methyl Cyclohexane/Tolueneimported from UNIQUACP.IPD7 4!=p"MethylCycloHexane/Phenol p482 1/2dimported from UNIQUAC.IPDGz`Methyl Cyclohexane/Tolueneimported from UNIQUACP.IPDa@"MethylCycloHexane/Phenol p482 1/2dimported from UNIQUAC.IPD33333Kj@Methyl Cyclohexane/Tolueneimported from UNIQUACP.IPDACHACOHACCH2CH2ACHqh??K7 *@ACOHh"lxz?(\?S㥛=@ACCH3B?`"?%C ;@CH3ͪ?A`"? rh.@CH2M O?HzG?Zd;O ,@CH F%u?v/?K7 *@Ĕ@d@= ףp=&ףp= W9@fffffn@'9&D'9&9'D'   defaultм@ =!Mz@qKM@:/@9 ̮?j?̴yA?UQ6?,C6?p> q?&l'R?[\?M?&(?[3Q?9 Ml6R??9 ̮?j?ʹyA?WQ6?.C6?s> q?м@O@2TolueneP"Z"Y"P"Z"P"Z"  defaultм@ʏw@p=-'#@=c?2MbP?z"ջP? ?,CZ7a?pC?XUQxE?yS3?4d'4?-o%-?zl?gP?G6Q??2MbP?z"ջP? ?/CZ7a?pC?ZUQxE?_Recycle SolventP3 818 3P8P3P8 8  defaultм@ Ko|@a-I@g4@-W^?dg?)*?ǧly)?C/=U1=e~??5?|}75^?87u]?T<4!o >T >?-W^?dg?)*?ǧly)?C/=U1=EPhenol &defaultм@Pw@Zd;O?r9~Q????????Pw@м@Zd;O?r9~Q? Cold Solvent8.888 defaultм@Pw@a-I@g4@-W^?dg?)*?ǧly)?C/=U1=?-W^?dg?)*?ǧly)?C/=U1=??r@?zGI@Á@2Extractive ColumnChemSep Unit OperationqeWCXcCSUO[ChemSep] Version=6.92 Compiled=2012-9-1 00:06 a8532c7ec00c Name=C:\DOCUME~1\Harry\LOCALS~1\Temp\CS_1A_~2.sep Title=ChemSep CO Unit Operation "Extractive Column" in COFE Flowsheet User=Harry Date=2012-09-05 Time=02:48:14 [Cape-Open] unitname=Extractive Column CO_ID=CS_1A_16C8_1CD8B00_20C0A790 3 components Phenol 108-95-2 94.1129989624 Mw Toluene 108-88-3 92.1405029297 Mw Methylcyclohexane 108-87-2 98.1882019043 Mw 0 thermo exe=C:\Program Files\ChemSepL6v92\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\chemsepl6v92\bin\ Help and Info path=c:\program files\chemsepl6v92\help\ Component data path=c:\program files\chemsepl6v92\pcd\ Property data path=c:\program files\chemsepl6v92\ipd\ Section data path=c:\program files\chemsepl6v92\ild\ Executables path=C:\Program Files\ChemSepL6v92\bin\ Temporary path=C:\DOCUME~1\Harry\LOCALS~1\Temp\ Scripts path=c:\program files\chemsepl6v92\bin\ [Units] Temperature=K Flow=mol/s Mass flow=kg/s Pressure=N/m2 Heat=J/s Enthalpy=J/kmol Entropy=J/kmol/K Fraction=_ Length=m 1/Length=1/m Area=m2 Volume=m3 Mass=kg Angle=rad Velocity=m/s Surface tension=N/m Density=kg/m3 Molar density=kmol/m3 Viscosity=N/m2.s Molecular weight=kg/kmol Heat capacity=J/kmol/K Thermal conductivity=J/s/m/K Diffusivity=m2/s Interaction parameter=J/mol Time=s [Components] 3 126 1181 Library Offset, Index DT=2012-07-17,01:03:18 CHK=29002 CAS=108-95-2 CID=Phenol Name=Phenol Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd 140 502 Library Offset, Index DT=2012-07-17,01:03:18 CHK=10507 CAS=108-88-3 CID=Toluene Name=Toluene Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd 144 138 Library Offset, Index DT=2012-07-17,01:03:18 CHK=8682 CAS=108-87-2 CID=Methylcyclohexane Name=Methylcyclohexane Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd [Operation] 2 Operation Column 2 Operation kind Extractive Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 40 Stages 2 Feed stages 0 Sidestream stages F=10, 25 S= 0 Pumparound stages P= [Properties] 350 BIP estimation temperature [Thermodynamics] 4 K model DECHEMA 8 * Activity coefficient UNIFAC * Wilson model * * UNIQUAC model * 3 Equation of State Cubic 5 Cubic EOS Peng-Robinson 76 * 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 * 12 Default Liquid 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 101325 Condenser pressure 101325 Top pressure * Pressure Drop * Bottom pressure [Feeds] 2 Number 1 Feed state T & p 10 Stage Feed1{split} 373.000003298 Temperature 101325 Pressure 0 Vapour fraction 3 componentflows 0.0500185488624 Component 1 flow 9.9610950021e-006 Component 2 flow 1.56346481328e-012 Component 3 flow 1 Feed state T & p 25 Stage Feed2{split} 384 Temperature 101325 Pressure 1 Vapour fraction 3 componentflows 0 Component 1 flow 0.01 Component 2 flow 0.01 Component 3 flow [Condenser] 1 Type Reflux ratio 8 Value Qcondenser * Type * * Initialization guess [Reboiler] 7 Type Mole fraction of a component 0.0001 Value Qreboiler 3 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 0 Trace treshold [Programs] Temporary file=SCRATCH.TMP User program= 1 Compiler Gfortran 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 Title ComboBox=ComboBox4 0 ComboBox=ComboBox15 0 Edit=Edit17 Plot font CheckBox=CheckBox2 1 Color=Edit18 1241625 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 1241625 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 1241625 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 1241625 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=Edit5 0 0 ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 Edit=Edit3 21 Edit=Edit4 Binary Property Diagram Memo=Memo1 StringGrid=StringGrid1 13 4 Axis Left Right X/Y Property -click to select- -click to select- x Title x Units - Minimum 0 Maximum 1 Interval 0.2 Grid Off Off Off Log Off Off Off Color Blue Red Black Line Normal Normal Style Solid Solid Point None None Edit=Edit5 ComboBox=ComboBox7 -1 ComboBox=ComboBox6 -1 [End Settings] [End of Input] [Results] 1 Converged 0 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 374.1002737 1.013250000E+05 1.004460560E-02 8.035684479E-02 -2.770076101E+06 2 374.1038464 1.013250000E+05 9.040145039E-02 8.035023255E-02 0.000000000E+00 3 374.1104422 1.013250000E+05 9.039483815E-02 8.033757489E-02 0.000000000E+00 4 374.1227580 1.013250000E+05 9.038218048E-02 8.031334404E-02 0.000000000E+00 5 374.1461447 1.013250000E+05 9.035794964E-02 8.026608435E-02 0.000000000E+00 6 374.1918988 1.013250000E+05 9.031068994E-02 8.016966591E-02 0.000000000E+00 7 374.2866713 1.013250000E+05 9.021427151E-02 7.995317450E-02 0.000000000E+00 8 374.5073543 1.013250000E+05 8.999778010E-02 7.934782764E-02 0.000000000E+00 9 375.1818399 1.013250000E+05 8.939243324E-02 7.607580763E-02 0.000000000E+00 10 379.9420036 1.013250000E+05 8.612041323E-02 1.338657124E-01 0.000000000E+00 11 379.9506227 1.013250000E+05 9.388160306E-02 1.338515594E-01 0.000000000E+00 12 379.9620620 1.013250000E+05 9.386745007E-02 1.338329701E-01 0.000000000E+00 13 379.9773200 1.013250000E+05 9.384886076E-02 1.338085048E-01 0.000000000E+00 14 379.9977997 1.013250000E+05 9.382439549E-02 1.337762242E-01 0.000000000E+00 15 380.0255048 1.013250000E+05 9.379211482E-02 1.337334954E-01 0.000000000E+00 16 380.0633501 1.013250000E+05 9.374938608E-02 1.336767151E-01 0.000000000E+00 17 380.1156594 1.013250000E+05 9.369260574E-02 1.336009108E-01 0.000000000E+00 18 380.1889746 1.013250000E+05 9.361680141E-02 1.334991834E-01 0.000000000E+00 19 380.2933748 1.013250000E+05 9.351507406E-02 1.333619844E-01 0.000000000E+00 20 380.4445847 1.013250000E+05 9.337787503E-02 1.331764280E-01 0.000000000E+00 21 380.6670902 1.013250000E+05 9.319231865E-02 1.329269791E-01 0.000000000E+00 22 380.9971544 1.013250000E+05 9.294286970E-02 1.326069342E-01 0.000000000E+00 23 381.4727542 1.013250000E+05 9.262282488E-02 1.323191191E-01 0.000000000E+00 24 381.9902733 1.013250000E+05 9.233500978E-02 1.324836760E-01 0.000000000E+00 25 382.3040666 1.013250000E+05 7.249956666E-02 1.323088863E-01 0.000000000E+00 26 382.8014668 1.013250000E+05 7.232477692E-02 1.320657478E-01 0.000000000E+00 27 383.5738038 1.013250000E+05 7.208163848E-02 1.317669138E-01 0.000000000E+00 28 384.7137401 1.013250000E+05 7.178280442E-02 1.314800287E-01 0.000000000E+00 29 386.2433096 1.013250000E+05 7.149591935E-02 1.313270987E-01 0.000000000E+00 30 388.0228425 1.013250000E+05 7.134298932E-02 1.314000354E-01 0.000000000E+00 31 389.7657716 1.013250000E+05 7.141592603E-02 1.316644491E-01 0.000000000E+00 32 391.2058206 1.013250000E+05 7.168033975E-02 1.319932847E-01 0.000000000E+00 33 392.2388687 1.013250000E+05 7.200917533E-02 1.322794308E-01 0.000000000E+00 34 392.9081936 1.013250000E+05 7.229532142E-02 1.324836761E-01 0.000000000E+00 35 393.3154121 1.013250000E+05 7.249956674E-02 1.326090520E-01 0.000000000E+00 36 393.5646393 1.013250000E+05 7.262494263E-02 1.326455484E-01 0.000000000E+00 37 393.7964906 1.013250000E+05 7.266143906E-02 1.323870250E-01 0.000000000E+00 38 394.5810916 1.013250000E+05 7.240291561E-02 1.303719614E-01 0.000000000E+00 39 399.4769419 1.013250000E+05 7.038785204E-02 1.219149857E-01 0.000000000E+00 40 420.8598548 1.013250000E+05 6.193087633E-02 5.998410936E-02 2.686808036E+06 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.1849680E+08 -0.1849680E+08 -0.4614643E+05 -0.4614643E+05 2 0.1214514E+08 -0.1849839E+08 0.3523029E+05 -0.4614011E+05 3 0.1214597E+08 -0.1850169E+08 0.3524095E+05 -0.4612817E+05 4 0.1214733E+08 -0.1850818E+08 0.3526139E+05 -0.4610742E+05 5 0.1214978E+08 -0.1852093E+08 0.3529879E+05 -0.4607299E+05 6 0.1215449E+08 -0.1854658E+08 0.3536655E+05 -0.4601783E+05 7 0.1216448E+08 -0.1860190E+08 0.3549181E+05 -0.4593341E+05 8 0.1218921E+08 -0.1874117E+08 0.3573954E+05 -0.4582339E+05 9 0.1227410E+08 -0.1925650E+08 0.3633032E+05 -0.4588969E+05 10 0.1299726E+08 -0.2583728E+08 0.3915401E+05 -0.5424453E+05 11 0.1299307E+08 -0.2584520E+08 0.3921901E+05 -0.5419493E+05 12 0.1298764E+08 -0.2585555E+08 0.3929753E+05 -0.5413601E+05 13 0.1298058E+08 -0.2586906E+08 0.3939221E+05 -0.5406634E+05 14 0.1297142E+08 -0.2588674E+08 0.3950601E+05 -0.5398451E+05 15 0.1295958E+08 -0.2590986E+08 0.3964221E+05 -0.5388930E+05 16 0.1294431E+08 -0.2594011E+08 0.3980427E+05 -0.5377990E+05 17 0.1292470E+08 -0.2597970E+08 0.3999576E+05 -0.5365637E+05 18 0.1289967E+08 -0.2603149E+08 0.4021996E+05 -0.5352028E+05 19 0.1286803E+08 -0.2609912E+08 0.4047945E+05 -0.5337571E+05 20 0.1282859E+08 -0.2618704E+08 0.4077514E+05 -0.5323065E+05 21 0.1278046E+08 -0.2630007E+08 0.4110490E+05 -0.5309865E+05 22 0.1272338E+08 -0.2644099E+08 0.4146047E+05 -0.5299821E+05 23 0.1265647E+08 -0.2659492E+08 0.4181694E+05 -0.5293168E+05 24 0.1255775E+08 -0.2660768E+08 0.4205972E+05 -0.5269386E+05 25 0.1253206E+08 -0.2667853E+08 0.4216199E+05 -0.5273490E+05 26 0.1249703E+08 -0.2677526E+08 0.4228160E+05 -0.5281332E+05 27 0.1245195E+08 -0.2689422E+08 0.4238592E+05 -0.5295010E+05 28 0.1239689E+08 -0.2701575E+08 0.4239588E+05 -0.5315814E+05 29 0.1233105E+08 -0.2710407E+08 0.4217713E+05 -0.5342492E+05 30 0.1225282E+08 -0.2712955E+08 0.4159395E+05 -0.5371445E+05 31 0.1216574E+08 -0.2709626E+08 0.4063588E+05 -0.5399382E+05 32 0.1208193E+08 -0.2703583E+08 0.3947734E+05 -0.5424640E+05 33 0.1201380E+08 -0.2697762E+08 0.3836057E+05 -0.5446286E+05 34 0.1196574E+08 -0.2693427E+08 0.3744520E+05 -0.5463692E+05 35 0.1193525E+08 -0.2690663E+08 0.3677348E+05 -0.5476837E+05 36 0.1191861E+08 -0.2689451E+08 0.3631977E+05 -0.5486532E+05 37 0.1192124E+08 -0.2692085E+08 0.3606543E+05 -0.5495611E+05 38 0.1201168E+08 -0.2716665E+08 0.3620866E+05 -0.5518559E+05 39 0.1267097E+08 -0.2843253E+08 0.3834475E+05 -0.5609319E+05 40 0.1561903E+08 -0.2912177E+08 0.4773934E+05 -0.5453879E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.9815799E+02 0.3324161E+01 0.8209105E-05 0.1751974E+06 0.2019122E-01 2 0.9815807E+02 0.3324130E+01 0.8209219E-05 0.1751979E+06 0.2019135E-01 3 0.9815779E+02 0.3324057E+01 0.8209466E-05 0.1751959E+06 0.2019145E-01 4 0.9815688E+02 0.3323908E+01 0.8209961E-05 0.1751893E+06 0.2019148E-01 5 0.9815482E+02 0.3323614E+01 0.8210925E-05 0.1751746E+06 0.2019145E-01 6 0.9815061E+02 0.3323031E+01 0.8212814E-05 0.1751449E+06 0.2019140E-01 7 0.9814206E+02 0.3321829E+01 0.8216651E-05 0.1750871E+06 0.2019168E-01 8 0.9812402E+02 0.3319090E+01 0.8225166E-05 0.1749756E+06 0.2019448E-01 9 0.9808131E+02 0.3311131E+01 0.8248611E-05 0.1747809E+06 0.2021600E-01 10 0.9794467E+02 0.3261001E+01 0.8380240E-05 0.1753122E+06 0.2053748E-01 11 0.9793371E+02 0.3260539E+01 0.8381381E-05 0.1752362E+06 0.2053430E-01 12 0.9791939E+02 0.3259933E+01 0.8382876E-05 0.1751369E+06 0.2053016E-01 13 0.9790066E+02 0.3259138E+01 0.8384839E-05 0.1750073E+06 0.2052477E-01 14 0.9787616E+02 0.3258094E+01 0.8387420E-05 0.1748379E+06 0.2051777E-01 15 0.9784409E+02 0.3256718E+01 0.8390822E-05 0.1746163E+06 0.2050868E-01 16 0.9780207E+02 0.3254902E+01 0.8395317E-05 0.1743266E+06 0.2049691E-01 17 0.9774695E+02 0.3252495E+01 0.8401281E-05 0.1739475E+06 0.2048169E-01 18 0.9767459E+02 0.3249293E+01 0.8409228E-05 0.1734513E+06 0.2046212E-01 19 0.9757950E+02 0.3245013E+01 0.8419873E-05 0.1728020E+06 0.2043710E-01 20 0.9745455E+02 0.3239262E+01 0.8434215E-05 0.1719533E+06 0.2040544E-01 21 0.9729061E+02 0.3231501E+01 0.8453644E-05 0.1708473E+06 0.2036595E-01 22 0.9707658E+02 0.3221019E+01 0.8480021E-05 0.1694152E+06 0.2031778E-01 23 0.9680057E+02 0.3207077E+01 0.8515349E-05 0.1675812E+06 0.2025986E-01 24 0.9645493E+02 0.3190392E+01 0.8557894E-05 0.1652518E+06 0.2018071E-01 25 0.9631204E+02 0.3182602E+01 0.8577960E-05 0.1643190E+06 0.2015633E-01 26 0.9609859E+02 0.3170735E+01 0.8608711E-05 0.1629311E+06 0.2012221E-01 27 0.9578982E+02 0.3153162E+01 0.8654667E-05 0.1609307E+06 0.2007698E-01 28 0.9536617E+02 0.3128481E+01 0.8720081E-05 0.1581910E+06 0.2002091E-01 29 0.9483136E+02 0.3096791E+01 0.8805612E-05 0.1547227E+06 0.1995616E-01 30 0.9423219E+02 0.3061086E+01 0.8904142E-05 0.1508025E+06 0.1988669E-01 31 0.9365326E+02 0.3026769E+01 0.9001101E-05 0.1469649E+06 0.1981884E-01 32 0.9317393E+02 0.2998664E+01 0.9082223E-05 0.1437443E+06 0.1976033E-01 33 0.9282735E+02 0.2978567E+01 0.9141209E-05 0.1413896E+06 0.1971616E-01 34 0.9260111E+02 0.2965559E+01 0.9179835E-05 0.1398405E+06 0.1968636E-01 35 0.9246325E+02 0.2957664E+01 0.9203453E-05 0.1388922E+06 0.1966794E-01 36 0.9238289E+02 0.2952975E+01 0.9217561E-05 0.1383402E+06 0.1965802E-01 37 0.9233816E+02 0.2949614E+01 0.9227836E-05 0.1380502E+06 0.1965952E-01 38 0.9232062E+02 0.2942698E+01 0.9249847E-05 0.1380668E+06 0.1971254E-01 39 0.9236569E+02 0.2905288E+01 0.9373363E-05 0.1392799E+06 0.2009275E-01 40 0.9274241E+02 0.2759299E+01 0.9931476E-05 0.1443454E+06 0.2156119E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.9815807E+02 0.7248514E+03 0.2976942E-03 0.2337870E+06 0.9352491E-01 0.1504628E-01 2 0.9815775E+02 0.7248961E+03 0.2977592E-03 0.2337837E+06 0.9353288E-01 0.1504884E-01 3 0.9815673E+02 0.7249837E+03 0.2978779E-03 0.2337743E+06 0.9354920E-01 0.1505388E-01 4 0.9815442E+02 0.7251517E+03 0.2980982E-03 0.2337543E+06 0.9358112E-01 0.1506360E-01 5 0.9814967E+02 0.7254751E+03 0.2985162E-03 0.2337145E+06 0.9364305E-01 0.1508235E-01 6 0.9814005E+02 0.7261130E+03 0.2993353E-03 0.2336376E+06 0.9376561E-01 0.1511932E-01 7 0.9811974E+02 0.7274457E+03 0.3010436E-03 0.2334885E+06 0.9402165E-01 0.1519645E-01 8 0.9807159E+02 0.7306075E+03 0.3051063E-03 0.2331891E+06 0.9462716E-01 0.1537868E-01 9 0.9791649E+02 0.7409661E+03 0.3185789E-03 0.2324710E+06 0.9658773E-01 0.1596854E-01 10 0.9648884E+02 0.8502832E+03 0.4753637E-03 0.2223934E+06 0.1152323E+00 0.2155303E-01 11 0.9647864E+02 0.8504232E+03 0.4752411E-03 0.2223188E+06 0.1152662E+00 0.2155922E-01 12 0.9646531E+02 0.8506065E+03 0.4750805E-03 0.2222214E+06 0.1153104E+00 0.2156731E-01 13 0.9644787E+02 0.8508466E+03 0.4748700E-03 0.2220940E+06 0.1153683E+00 0.2157788E-01 14 0.9642504E+02 0.8511616E+03 0.4745938E-03 0.2219275E+06 0.1154441E+00 0.2159170E-01 15 0.9639513E+02 0.8515756E+03 0.4742307E-03 0.2217098E+06 0.1155435E+00 0.2160979E-01 16 0.9635590E+02 0.8521205E+03 0.4737523E-03 0.2214249E+06 0.1156740E+00 0.2163347E-01 17 0.9630440E+02 0.8528394E+03 0.4731208E-03 0.2210521E+06 0.1158454E+00 0.2166449E-01 18 0.9623675E+02 0.8537900E+03 0.4722848E-03 0.2205643E+06 0.1160708E+00 0.2170510E-01 19 0.9614788E+02 0.8550493E+03 0.4711749E-03 0.2199270E+06 0.1163674E+00 0.2175819E-01 20 0.9603134E+02 0.8567186E+03 0.4696976E-03 0.2190972E+06 0.1167569E+00 0.2182734E-01 21 0.9587933E+02 0.8589235E+03 0.4677243E-03 0.2180251E+06 0.1172654E+00 0.2191648E-01 22 0.9568365E+02 0.8617820E+03 0.4650522E-03 0.2166634E+06 0.1179173E+00 0.2202808E-01 23 0.9544003E+02 0.8651357E+03 0.4610760E-03 0.2150043E+06 0.1186924E+00 0.2215124E-01 24 0.9516827E+02 0.8662797E+03 0.4517419E-03 0.2132618E+06 0.1192025E+00 0.2216751E-01 25 0.9505008E+02 0.8680140E+03 0.4497863E-03 0.2124851E+06 0.1195847E+00 0.2222532E-01 26 0.9487962E+02 0.8705248E+03 0.4468384E-03 0.2113809E+06 0.1201323E+00 0.2230512E-01 27 0.9464676E+02 0.8739438E+03 0.4425049E-03 0.2099063E+06 0.1208691E+00 0.2240546E-01 28 0.9435438E+02 0.8781547E+03 0.4364291E-03 0.2081174E+06 0.1217665E+00 0.2251300E-01 29 0.9402832E+02 0.8826387E+03 0.4286228E-03 0.2062182E+06 0.1227160E+00 0.2260167E-01 30 0.9371379E+02 0.8866352E+03 0.4198690E-03 0.2044991E+06 0.1235644E+00 0.2264779E-01 31 0.9345271E+02 0.8896165E+03 0.4115714E-03 0.2031712E+06 0.1242059E+00 0.2265028E-01 32 0.9326294E+02 0.8915449E+03 0.4049053E-03 0.2022705E+06 0.1246302E+00 0.2262833E-01 33 0.9313835E+02 0.8926843E+03 0.4002258E-03 0.2017119E+06 0.1248873E+00 0.2260182E-01 34 0.9306208E+02 0.8933292E+03 0.3972424E-03 0.2013835E+06 0.1250358E+00 0.2258057E-01 35 0.9301750E+02 0.8937016E+03 0.3954722E-03 0.2011969E+06 0.1251212E+00 0.2256677E-01 36 0.9299282E+02 0.8940178E+03 0.3945987E-03 0.2010970E+06 0.1251815E+00 0.2256211E-01 37 0.9298451E+02 0.8949984E+03 0.3951990E-03 0.2010778E+06 0.1253070E+00 0.2258715E-01 38 0.9301911E+02 0.9012050E+03 0.4032035E-03 0.2013262E+06 0.1260216E+00 0.2279421E-01 39 0.9325580E+02 0.9362273E+03 0.4483930E-03 0.2030402E+06 0.1299535E+00 0.2388350E-01 40 0.9378585E+02 0.1010640E+04 0.5020936E-03 0.2102076E+06 0.1384726E+00 0.2513685E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.830418967E-04 0.172293485E-03 0.337368440E-03 0.644025806E-03 0.121841177E-02 2 0.493934842E-02 0.486563559E-02 0.480132180E-02 0.474561438E-02 0.469811031E-02 3 0.994977610E+00 0.994962071E+00 0.994861310E+00 0.994610360E+00 0.994083478E+00 Component Mole fractions on stages: 6 to 10 1 0.231110078E-02 0.445247082E-02 0.890296347E-02 0.193784689E-01 0.528491104E-01 2 0.465901285E-02 0.462958690E-02 0.461315434E-02 0.461734661E-02 0.465661429E-02 3 0.993029886E+00 0.990917942E+00 0.986483882E+00 0.976004185E+00 0.942494275E+00 Component Mole fractions on stages: 11 to 15 1 0.528122390E-01 0.527646297E-01 0.527033672E-01 0.526249105E-01 0.525251031E-01 2 0.649381518E-02 0.889417930E-02 0.120317374E-01 0.161351535E-01 0.215053077E-01 3 0.940693946E+00 0.938341191E+00 0.935264895E+00 0.931239936E+00 0.925969589E+00 Component Mole fractions on stages: 16 to 20 1 0.523993468E-01 0.522431190E-01 0.520531841E-01 0.518301371E-01 0.515833695E-01 2 0.285386293E-01 0.377578459E-01 0.498517772E-01 0.657246857E-01 0.865515338E-01 3 0.919062024E+00 0.909999035E+00 0.898095039E+00 0.882445177E+00 0.861865097E+00 Component Mole fractions on stages: 21 to 25 1 0.513397926E-01 0.511537390E-01 0.510691958E-01 0.505276815E-01 0.507251500E-01 2 0.113823547E+00 0.149338919E+00 0.195035175E+00 0.252552605E+00 0.276046832E+00 3 0.834836660E+00 0.799507342E+00 0.753895629E+00 0.696919714E+00 0.673228018E+00 Component Mole fractions on stages: 26 to 30 1 0.511292246E-01 0.519245709E-01 0.533665214E-01 0.556573700E-01 0.587044876E-01 2 0.311067967E+00 0.361588200E+00 0.430668961E+00 0.517556007E+00 0.614576644E+00 3 0.637802809E+00 0.586487229E+00 0.515964518E+00 0.426786623E+00 0.326718868E+00 Component Mole fractions on stages: 31 to 35 1 0.620127202E-01 0.649606678E-01 0.671882362E-01 0.686811906E-01 0.696140047E-01 2 0.708075410E+00 0.785347306E+00 0.841154274E+00 0.877557805E+00 0.899723919E+00 3 0.229911870E+00 0.149692026E+00 0.916574896E-01 0.537610045E-01 0.306620763E-01 Component Mole fractions on stages: 36 to 40 1 0.702355232E-01 0.711236948E-01 0.755149144E-01 0.105999982E+00 0.301931633E+00 2 0.912592759E+00 0.919390719E+00 0.919332756E+00 0.891336977E+00 0.697018412E+00 3 0.171717178E-01 0.948558591E-02 0.515232977E-02 0.266304079E-02 0.104995540E-02 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.172293485E-03 0.358004507E-03 0.703006490E-03 0.134924739E-02 0.257875400E-02 2 0.486563559E-02 0.479328192E-02 0.473060813E-02 0.467715831E-02 0.463315580E-02 3 0.994962071E+00 0.994848714E+00 0.994566385E+00 0.993973594E+00 0.992788090E+00 Component Mole fractions on stages: 6 to 10 1 0.498874215E-02 0.999980718E-02 0.218097699E-01 0.598042499E-01 0.410673597E+00 2 0.460001192E-02 0.458143484E-02 0.458591582E-02 0.462901634E-02 0.426356194E-02 3 0.990411246E+00 0.985418758E+00 0.973604314E+00 0.935566734E+00 0.585062841E+00 Component Mole fractions on stages: 11 to 15 1 0.410678048E+00 0.410684803E+00 0.410695243E+00 0.410711670E+00 0.410737956E+00 2 0.594665395E-02 0.814642175E-02 0.110229614E-01 0.147868073E-01 0.197151351E-01 3 0.583375298E+00 0.581168776E+00 0.578281796E+00 0.574501523E+00 0.569546909E+00 Component Mole fractions on stages: 16 to 20 1 0.410780665E+00 0.410851006E+00 0.410968170E+00 0.411164858E+00 0.411495421E+00 2 0.261730393E-01 0.346409232E-01 0.457481739E-01 0.603102409E-01 0.793577040E-01 3 0.563046296E+00 0.554508071E+00 0.543283656E+00 0.528524901E+00 0.509146875E+00 Component Mole fractions on stages: 21 to 25 1 0.412041195E+00 0.412853140E+00 0.413262196E+00 0.405291950E+00 0.405981240E+00 2 0.104125462E+00 0.135934099E+00 0.175942389E+00 0.226249535E+00 0.245327560E+00 3 0.483833343E+00 0.451212761E+00 0.410795414E+00 0.368458515E+00 0.348691200E+00 Component Mole fractions on stages: 26 to 30 1 0.407068638E+00 0.408659602E+00 0.410680552E+00 0.412749312E+00 0.414350815E+00 2 0.272780532E+00 0.310212326E+00 0.357196739E+00 0.409716125E+00 0.460646421E+00 3 0.320150830E+00 0.281128072E+00 0.232122708E+00 0.177534563E+00 0.125002763E+00 Component Mole fractions on stages: 31 to 35 1 0.415248148E+00 0.415590729E+00 0.415653019E+00 0.415628572E+00 0.415641813E+00 2 0.503211438E+00 0.534359917E+00 0.554919371E+00 0.567546822E+00 0.574908655E+00 3 0.815404141E-01 0.500493541E-01 0.294276101E-01 0.168246060E-01 0.944953162E-02 Component Mole fractions on stages: 36 to 40 1 0.416033305E+00 0.419108413E+00 0.440877980E+00 0.563637901E+00 0.833837770E+00 2 0.578725397E+00 0.578028451E+00 0.557638233E+00 0.435779537E+00 0.166062230E+00 3 0.524129714E-02 0.286313639E-02 0.148378632E-02 0.582562253E-03 0.100000000E-03 [Reaction rates] Component reaction rates on stages: 1 to 5 1 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 2 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 3 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 Component reaction rates on stages: 6 to 10 1 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 2 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 3 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 Component reaction rates on stages: 11 to 15 1 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 2 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 3 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 Component reaction rates on stages: 16 to 20 1 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 2 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 3 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 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 3 -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 3 -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 3 -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 3 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 [Condenser Heat Duty] -2.770076101E+06 [Reboiler Heat Duty] 2.686808036E+06 [UA Column] 0.000000000E+00 [K-values] Component K-values on stages: 1 to 5 1 0.481979321E+00 0.481260659E+00 0.479893778E+00 0.477322256E+00 0.472480809E+00 2 0.101514965E+01 0.101509477E+01 0.101494808E+01 0.101463622E+01 0.101401946E+01 3 0.100001562E+01 0.100011394E+01 0.100029654E+01 0.100064063E+01 0.100130480E+01 Component K-values on stages: 6 to 10 1 0.463263226E+00 0.445255669E+00 0.408209876E+00 0.324031635E+00 0.128688844E+00 2 0.101282622E+01 0.101051022E+01 0.100593957E+01 0.997478972E+00 0.109218871E+01 3 0.100264399E+01 0.100558056E+01 0.101322875E+01 0.104322241E+01 0.161092828E+01 Component K-values on stages: 11 to 15 1 0.128597667E+00 0.128479626E+00 0.128327192E+00 0.128131033E+00 0.127879838E+00 2 0.109201160E+01 0.109178968E+01 0.109151587E+01 0.109118574E+01 0.109080194E+01 3 0.161250219E+01 0.161457606E+01 0.161731685E+01 0.162095295E+01 0.162580039E+01 Component K-values on stages: 16 to 20 1 0.127560402E+00 0.127158309E+00 0.126659893E+00 0.126056828E+00 0.125355880E+00 2 0.109038271E+01 0.108997810E+01 0.108969995E+01 0.108977679E+01 0.109065115E+01 3 0.163230275E+01 0.164109248E+01 0.165308676E+01 0.166963777E+01 0.169276305E+01 Component K-values on stages: 21 to 25 1 0.124598695E+00 0.123903006E+00 0.123575803E+00 0.124669859E+00 0.124944566E+00 2 0.109313921E+01 0.109861353E+01 0.110851763E+01 0.111625685E+01 0.112521737E+01 3 0.172546298E+01 0.177190729E+01 0.183520945E+01 0.189144706E+01 0.193072844E+01 Component K-values on stages: 26 to 30 1 0.125603448E+00 0.127060690E+00 0.129946551E+00 0.134845458E+00 0.141678224E+00 2 0.114035985E+01 0.116561519E+01 0.120569119E+01 0.126320634E+01 0.133416134E+01 3 0.199219477E+01 0.208619234E+01 0.222280931E+01 0.240396357E+01 0.261369317E+01 Component K-values on stages: 31 to 35 1 0.149338945E+00 0.156309232E+00 0.161645010E+00 0.165246557E+00 0.167485567E+00 2 0.140711311E+01 0.146969726E+01 0.151581350E+01 0.154622979E+01 0.156498586E+01 3 0.281960636E+01 0.299088827E+01 0.311467664E+01 0.319537970E+01 0.324482498E+01 Component K-values on stages: 36 to 40 1 0.168821876E+00 0.169702379E+00 0.171283026E+00 0.188063972E+00 0.362098773E+00 2 0.157690118E+01 0.159056309E+01 0.164861859E+01 0.204538511E+01 0.419733259E+01 3 0.327623436E+01 0.331300526E+01 0.347242033E+01 0.457125531E+01 0.104995540E+02 [Molecular weights] 1 94.113 2 92.141 3 98.188 [Feed stream 1] 10 Stage Number 5.0028509958966E-02 Flow rate 3.7300000329800E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -4.1861036242027E+07 Enthalpy [J/kmol] -8.5719196117210E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9980089160013E-01 Mole fraction of component 1 1.9910836861362E-04 Mole fraction of component 2 3.1251476699234E-11 Mole fraction of component 3 5.0028509958966E-02 Flow rate 9.9980089160013E-01 Mole fraction of component 1 1.9910836861362E-04 Mole fraction of component 2 3.1251476699234E-11 Mole fraction of component 3 9.4112606222063E+01 Molar mass 1.1183230559764E+03 Density 1.1145891620510E-03 Viscosity 1.4883461037979E-01 Thermal conductivity 1.8926484926683E+05 Heat capacity 3.2489279286796E-02 Surface tension [Feed stream 2] 25 Stage Number 2.0000000000000E-02 Flow rate 3.8400000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] 1.2244258987705E+07 Enthalpy [J/kmol] 4.0596962627597E+04 Entropy [J/kmol/K] 1.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 0.0000000000000E+00 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 5.0000000000000E-01 Mole fraction of component 3 2.0000000000000E-02 Flow rate 0.0000000000000E+00 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 5.0000000000000E-01 Mole fraction of component 3 9.5164352416992E+01 Molar mass 3.1272844887241E+00 Density 8.6958338767964E-06 Viscosity 2.0032063277787E-02 Thermal conductivity 1.5745502083969E+05 Heat capacity [Reflashed Feed stream 1] 10 Stage Number 5.0028509958966E-02 Flow rate 3.7300000494721E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -4.1861036242027E+07 Enthalpy [J/kmol] -8.5719195301698E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9980089160013E-01 Mole fraction of component 1 1.9910836861362E-04 Mole fraction of component 2 3.1251476699234E-11 Mole fraction of component 3 5.0028509958966E-02 Flow rate 9.9980089160013E-01 Mole fraction of component 1 1.9910836861362E-04 Mole fraction of component 2 3.1251476699234E-11 Mole fraction of component 3 9.4112606222063E+01 Molar mass 1.1183230546376E+03 Density 1.1145891322698E-03 Viscosity 1.4883461021003E-01 Thermal conductivity 1.8926484991354E+05 Heat capacity 3.2489279107169E-02 Surface tension [Reflashed Feed stream 2] 25 Stage Number 2.0000000000000E-02 Flow rate 3.8400000000000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] 1.2244258987705E+07 Enthalpy [J/kmol] 4.0596962627597E+04 Entropy [J/kmol/K] 1.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 0.0000000000000E+00 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 5.0000000000000E-01 Mole fraction of component 3 2.0000000000000E-02 Flow rate 0.0000000000000E+00 Mole fraction of component 1 5.0000000000000E-01 Mole fraction of component 2 5.0000000000000E-01 Mole fraction of component 3 9.5164352416992E+01 Molar mass 3.1272844887241E+00 Density 8.6958338767964E-06 Viscosity 2.0032063277787E-02 Thermal conductivity 1.5745502083969E+05 Heat capacity [Top product] 1 Stage Number 1.0044605600000E-02 Flow rate 3.7410027370000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -1.8496800662327E+07 Enthalpy [J/kmol] -4.6146431059246E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.7229348500000E-04 Mole fraction of component 1 4.8656355900000E-03 Mole fraction of component 2 9.9496207100000E-01 Mole fraction of component 3 1.0044605600000E-02 Flow rate 1.7229348500000E-04 Mole fraction of component 1 4.8656355900000E-03 Mole fraction of component 2 9.9496207100000E-01 Mole fraction of component 3 9.8158073881376E+01 Molar mass 7.2485135447811E+02 Density 2.9769423330199E-04 Viscosity 9.3524910776134E-02 Thermal conductivity 2.3378696726152E+05 Heat capacity 1.5046284562214E-02 Surface tension [Bottom product] 40 Stage Number 5.9984109360000E-02 Flow rate 4.2085985480000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.9121771590818E+07 Enthalpy [J/kmol] -5.4538792289634E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 8.3383777000000E-01 Mole fraction of component 1 1.6606223000000E-01 Mole fraction of component 2 1.0000000000000E-04 Mole fraction of component 3 5.9984109360000E-02 Flow rate 8.3383777000000E-01 Mole fraction of component 1 1.6606223000000E-01 Mole fraction of component 2 1.0000000000000E-04 Mole fraction of component 3 9.3785849392838E+01 Molar mass 1.0106397917575E+03 Density 5.0209360914954E-04 Viscosity 1.3847263999723E-01 Thermal conductivity 2.1020757523846E+05 Heat capacity 2.5136852968831E-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(bbaw@Zaw@Q _aw@(aw@/ӛVbw@Dycw@;#4dw@ߊhw@yrw@n]rw@]%5w@dw@Kw@Vww@Bwhw@,d{w@ǫw@e: w@7Ʃw@լw@fw@,Xw@@fw@(w@ltw@Gw@!L.w@5zk x@l#x@X]@x@J@\x@} Ksx@hg҃x@&x@4 x@7x@%ilx@&Lx@yiԍx@TMz@"Pressure profile.Pressure at each stage(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 stage(o$@ \V@];EV@AuV@ZV@XV@ٟV@`V@tNYV@6ٴU@:=/lxW@dLMwW@SvW@F!MtW@[rW@^koW@SlW@ygW@0`W@/XW@K NLW@x'WS@}곻`@>?`@xA鰧`@UuE߹`@+"ָ`@XXx`@l`@:I:`@6wO`@0N``@)CUL`@kЩ`@^zEl`@@B96`@;Fz`@וe`@Y!`@<;ώx`@%e\o`@ bwj`@ l`@iK*Cu`@`@o`@kLFz`@Z}`@?U`@@b`@ K`@s. z^@qKM@Duties profile*Duties at each stage(h N"E㥛DA4Vapour Moleweight profile@Vapour Moleweight at each stage(X@X@h:;X@`YiR X@1%X@ X@wӂX@2X@.4X@(yu|X@|{X@?'IzX@/4iyX@dxX@\8vX@hUsX@o_oX@Z {,kX@ +eX@eX]X@xZRX@̯DX@( <3X@ X@žvX@mnLOX@n/iW@KToW@̒5W@Tr3܎W@=iW@rK!KW@jM4W@x&W@SW@EW@/4iW@c W@ZwgW@L;/W@.Vapour Density profile:Vapour Density at each stage( @G8-xї @QH2 @YM] @8– @F @.W[@9Ϙ@p ?@>@Z @2Vapour Viscosity profile>Vapour Viscosity at each stage(.:7>;wJ7>ejl7>r7>d48>[ 89>G;>*R 5?>-٣vpL>Zj>{;>A[>WG>3%:>waɘ>!3>Dg>~>"b>GS֮>J>Qc/6>Ҩ>{>2gA>{; >tn`p&>({ΎI>7zw> B_>d m>l9 >M;2+>1Zb@>ͤM>ɺT>uf(Z>BޜJe>L3I>>:Vapour Heat capacity profileFVapour Heat capacity at each stage(_Qe@|a2Ue@*De@@߾e@6'IX@ X@ X@X@z3X@VIX@_)X@9#J{X@x&X@v X@|yX@VFW@DW@Жs)W@xW@4W@:KW@dW@іs)W@tρW@@mW@$]3\W@3KPW@YHW@odCW@QAW@$\?W@p%;6?W@A&9AW@F_PW@c]KrW@.Liquid Density profile:Liquid Density at each stage(ͪϦ@z6+@ާ@mV}6@:ͫ@Cl簆@^)ː@(Ԇ@S'@ё\C@V}b@1ڔ@Y8Ŗ@EJ@<,Ԛ@X9@X@Q@ed@?W[Ŋ@Sc׊@K7A@ @Z<@'1 @W24@O@ZLiquid Viscosity at each stage(kz3?1b3?~֏3? }B3?PE3?_-R3?]j3?AƎ3?4?]G'??Prr8%??/5"??ז??\??dXE??> ??S\??8ş>?K%D>? 7>?q>?E=lGz>?IW7>?=ͯ=?Er)z=?BmPH=?=?AZ&}~?lBZ?H8[?OÞ?es?R?uu"?0Ku ?'?X#P7/?)9?piG?HY?;_Fq?Ql?vЮ?\i?+,;–?C'ז?#t?{ڥ ?e$?Pu0?Ya1?'@+?™v$?Z=f\?bL? P?`H=!?5]W?t?ry? Unit is validF ChemSep (TM) - COL2 6.92 Copyright (c) 1988-2012 Harry Kooijman and Ross Taylor License: 2100- 6 LITE free license Build: edd84037473c Checking data file C:\DOCUME~1\Harry\LOCALS~1\Temp\CS_1A_~2.SEP Cape Open unit name: Extractive Column Cape-Open unit id: CS_1A_16C8_1CD8B00_20C0A790 Cape-Open run level: normal Cape open Initialized Cape Open Thermodynamic-properties enabled Reading configuration Reading component property libraries Reading thermodynamic property options Reading specifications Reading reaction data Checking Component Data 108-95-2 Phenol 108-88-3 Toluene 108-87-2 Methylcyclohexane Determining feed conditions Possible trivial solution Run level: Initialization Reading initial temperature profiles Reading initial composition profiles Init 46 milliseconds Run level: Complete model Iteration log(Err/Tol) 0 -0.3816 Run level: Report Convergence obtained in 0 iterations Time 297 milliseconds FixMem driver done run time: 0.36 seconds Using: C:\Program Files\ChemSepL6v92\bin\co-col2.exe Using CAPE-OPEN version 1.0 thermodynamics CAPE-OPEN thermo-properties were enabled CAPE-OPEN diffusion coefficients were disabled CAPE-OPEN supplied derivatives were enabled CAPE-OPEN supplied molar derivatives were enabled Inlet re-flash: <none> Outlet flash: Auto Flash used for TopProduct: PVF Flash used for BottomProduct: PVF CAPE-OPEN supplied d H / d T have been used CAPE-OPEN supplied d H / d x have been used CAPE-OPEN supplied d K / d T have been used CAPE-OPEN supplied d K / d x and d K / d y have been used Relative perturbation of pressure: 0.001 Relative perturbation of temperature: 0.001 Perturbation of composition: 0.001+-;& not all ports are connectedFeed2{split}_stage25Feed1{split}_stage10 TopProduct BottomProduct @ @0@@$@,@@$@0@,@4@@@@@@@$@@@(@@(@ @(@ @ @ @ffffff,@ɿ#@@ ɿ#@@ɿ#@@ ɿ#@@@0@@2@@2@$@2@(@0@(@(@(@(@ @(@#@3333334@ffffff,@/@ 3333334@ffffff,@/@3333334@ffffff,@/@ 3333334@ffffff,@/@ 334@ffffff,@/@ 334@ffffff,@/@ ffffff,@/@  ffffff,@/@? @@ @?(@@(@0@+@message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.10 K, range = [383.78 - 1000.00] K)  (last message repeated 1 time) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.11 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.12 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.15 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.19 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.29 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.51 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 375.18 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 379.94 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 379.95 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 379.96 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 379.98 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.00 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.03 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.06 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.12 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.19 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.29 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.44 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 380.67 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 381.00 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 381.47 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 381.99 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 382.30 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 382.80 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 383.57 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 374.10 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.10 K, range = [273.15 - 374.08] K) #(last 2 messages repeated 1 time) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 374.11 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.11 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 374.12 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.12 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 374.15 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.15 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 374.19 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.19 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 374.29 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.29 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 374.51 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.51 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 375.18 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 375.18 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 379.94 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 379.94 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 379.95 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 379.95 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 379.96 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 379.96 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 379.98 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 379.98 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 380.00 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.00 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 380.03 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.03 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 380.06 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.06 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 380.12 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.12 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 380.19 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.19 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 380.29 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.29 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 380.44 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.44 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 380.67 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 380.67 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 381.00 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 381.00 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 381.47 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 381.47 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 381.99 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 381.99 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 382.30 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 382.30 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 382.80 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 382.80 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 383.57 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 383.57 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 384.71 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 384.71 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 384.71 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 386.24 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 386.24 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 386.24 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 388.02 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 388.02 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 388.02 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 389.77 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 389.77 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 389.77 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 391.21 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 391.21 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 391.21 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 392.24 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 392.24 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 392.24 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 392.91 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 392.91 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 392.91 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 393.32 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 393.32 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 393.32 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 393.56 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 393.56 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 393.56 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 393.80 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 393.80 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 393.80 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 394.58 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 394.58 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 394.58 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 399.48 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 399.48 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 399.48 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 420.86 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 420.86 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 420.86 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for vapor thermal conductivity for compound Toluene (T = 374.10 K, range = [383.78 - 1000.00] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 374.10 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 374.10 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 420.86 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 420.86 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 420.86 K, range = [273.15 - 374.08] K) Solvent RecoveryChemSep Unit OperationqeWCXcoCSUOie[ChemSep] Version=6.92 Compiled=2012-9-1 00:06 a8532c7ec00c Name=C:\DOCUME~1\Harry\LOCALS~1\Temp\CS_1B_~1.sep Title=ChemSep CO Unit Operation "Solvent Recovery" in COFE Flowsheet User=Harry Date=2012-09-05 Time=02:48:16 [Cape-Open] unitname=Solvent Recovery CO_ID=CS_1B_16C8_1CD8B00_20C0A790 3 components Phenol 108-95-2 94.1129989624 Mw Toluene 108-88-3 92.1405029297 Mw Methylcyclohexane 108-87-2 98.1882019043 Mw 0 thermo exe=C:\Program Files\ChemSepL6v92\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\chemsepl6v92\bin\ Help and Info path=c:\program files\chemsepl6v92\help\ Component data path=c:\program files\chemsepl6v92\pcd\ Property data path=c:\program files\chemsepl6v92\ipd\ Section data path=c:\program files\chemsepl6v92\ild\ Executables path=C:\Program Files\ChemSepL6v92\bin\ Temporary path=C:\DOCUME~1\Harry\LOCALS~1\Temp\ Scripts path=c:\program files\chemsepl6v92\bin\ [Units] Temperature=K Flow=mol/s Mass flow=kg/s Pressure=N/m2 Heat=J/s Enthalpy=J/kmol Entropy=J/kmol/K Fraction=_ Length=m 1/Length=1/m Area=m2 Volume=m3 Mass=kg Angle=rad Velocity=m/s Surface tension=N/m Density=kg/m3 Molar density=kmol/m3 Viscosity=N/m2.s Molecular weight=kg/kmol Heat capacity=J/kmol/K Thermal conductivity=J/s/m/K Diffusivity=m2/s Interaction parameter=J/mol Time=s [Components] 3 126 1181 Library Offset, Index DT=2012-07-17,01:03:18 CHK=29002 CAS=108-95-2 CID=Phenol Name=Phenol Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd 140 502 Library Offset, Index DT=2012-07-17,01:03:18 CHK=10507 CAS=108-88-3 CID=Toluene Name=Toluene Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd 144 138 Library Offset, Index DT=2012-07-17,01:03:18 CHK=8682 CAS=108-87-2 CID=Methylcyclohexane Name=Methylcyclohexane Lib=c:\program files\chemsepl6v92\pcd\chemsep1.pcd [Operation] 2 Operation Column 2 Operation kind Extractive Distillation 1 Condenser Total (Liquid product) 1 Reboiler Partial (Liquid product) 20 Stages 1 Feed stages 0 Sidestream stages F=12 S= 0 Pumparound stages P= [Properties] 350 BIP estimation temperature [Thermodynamics] 4 K model DECHEMA 8 * Activity coefficient UNIFAC * Wilson model * * UNIQUAC model * 3 Equation of State Cubic 5 Cubic EOS Peng-Robinson 76 * 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 * 12 Default Liquid Diffusion Coefficients * [Reaction data] 0 Number of reactions [Specifications] Top Bottom [Heaters/Coolers] 0 Number 0 Column duty Qcolumn 2 First stage 19 Last stage 0 Qcolumn lost to surroundings [Efficiencies] 1 Default efficiency 0 Number [Pressures] 1 Column pressure Constant pressure 101325 Condenser pressure 101325 Top pressure * Pressure Drop * Bottom pressure [Feeds] 1 Number 1 Feed state T & p 12 Stage Feed1{split} 420.859854822 Temperature 101325 Pressure 0 Vapour fraction 3 componentflows 0.0500170159842 Component 1 flow 0.00996109496489 Component 2 flow 5.998410936e-006 Component 3 flow [Condenser] 7 Type Mole fraction of a component 0.001 Value Qcondenser 1 1st comp. * Type * * Initialization guess [Reboiler] 8 Type Component recovery 0.001 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 0 Trace treshold [Programs] Temporary file=SCRATCH.TMP User program= 1 Compiler Gfortran 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 Title ComboBox=ComboBox4 0 ComboBox=ComboBox15 0 Edit=Edit17 Plot font CheckBox=CheckBox2 1 Color=Edit18 -16777208 SpinEdit=SpinEdit1 1 CheckBox=CheckBox2 1 Color=Edit19 -16777211 Edit=Edit5 StringGrid=StringGrid2 7 2 StringGrid=StringGrid3 7 2 StringGrid=StringGrid4 7 2 Color=BVLEbplineColor 0 SpinEdit=SpinEdit2 1 ComboBox=ComboBox13 0 Color=BVLEdplineColor 0 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=Edit5 0 0 ComboBox=ComboBox1 -1 ComboBox=ComboBox2 -1 ComboBox=ComboBox3 -1 Edit=Edit1 Edit=Edit2 Edit=Edit3 21 Edit=Edit4 Binary Property Diagram Memo=Memo1 StringGrid=StringGrid1 13 4 Axis Left Right X/Y Property -click to select- -click to select- x Title x Units - Minimum 0 Maximum 1 Interval 0.2 Grid Off Off Off Log Off Off Off Color Blue Red Black Line Normal Normal Style Solid Solid Point None None Edit=Edit5 ComboBox=ComboBox7 -1 ComboBox=ComboBox6 -1 [End Settings] [End of Input] [Results] 1 Converged 0 Iterations [Profiles] Stage Temperature Pressure Vapour Flow Liquid Flow Duties 1 383.8100555 1.013250000E+05 9.967099404E-03 1.077536612E-02 -6.774479029E+05 2 383.8752781 1.013250000E+05 2.074246552E-02 1.076084504E-02 0.000000000E+00 3 383.9825155 1.013250000E+05 2.072794444E-02 1.073402850E-02 0.000000000E+00 4 384.1789622 1.013250000E+05 2.070112790E-02 1.068088213E-02 0.000000000E+00 5 384.5715371 1.013250000E+05 2.064798153E-02 1.056133045E-02 0.000000000E+00 6 385.4759234 1.013250000E+05 2.052842986E-02 1.022489838E-02 0.000000000E+00 7 388.1663177 1.013250000E+05 2.019199779E-02 9.121957783E-03 0.000000000E+00 8 397.5945885 1.013250000E+05 1.908905719E-02 7.311585774E-03 0.000000000E+00 9 413.5590341 1.013250000E+05 1.727868518E-02 6.665536968E-03 0.000000000E+00 10 421.4317205 1.013250000E+05 1.663263637E-02 6.613169317E-03 0.000000000E+00 11 423.4222819 1.013250000E+05 1.658026872E-02 6.612483345E-03 0.000000000E+00 12 423.8464924 1.013250000E+05 1.657958275E-02 6.661149416E-02 0.000000000E+00 13 429.2670981 1.013250000E+05 1.659448421E-02 6.691601769E-02 0.000000000E+00 14 437.3666769 1.013250000E+05 1.689900773E-02 6.783980811E-02 0.000000000E+00 15 445.4543311 1.013250000E+05 1.782279816E-02 6.915827573E-02 0.000000000E+00 16 450.7723712 1.013250000E+05 1.914126577E-02 7.019704697E-02 0.000000000E+00 17 453.3421452 1.013250000E+05 2.018003702E-02 7.074288989E-02 0.000000000E+00 18 454.3928837 1.013250000E+05 2.072587993E-02 7.097398492E-02 0.000000000E+00 19 454.7921789 1.013250000E+05 2.095697497E-02 7.106299083E-02 0.000000000E+00 20 454.9396207 1.013250000E+05 2.104598087E-02 5.001700995E-02 9.531711785E+05 [Enthalpies/Entropies] Stage Vap.Enthalpy Liq.Enthalpy Vap.Entropy Liq.Entropy 1 -0.2210492E+08 -0.2210492E+08 -0.5456276E+05 -0.5456276E+05 2 0.1055503E+08 -0.2212256E+08 0.3006065E+05 -0.5447961E+05 3 0.1056875E+08 -0.2215444E+08 0.3015393E+05 -0.5434141E+05 4 0.1059457E+08 -0.2221704E+08 0.3032315E+05 -0.5412837E+05 5 0.1064648E+08 -0.2235566E+08 0.3063077E+05 -0.5380591E+05 6 0.1076656E+08 -0.2273507E+08 0.3124824E+05 -0.5336726E+05 7 0.1112630E+08 -0.2415476E+08 0.3277639E+05 -0.5336142E+05 8 0.1240434E+08 -0.2800950E+08 0.3732349E+05 -0.5584355E+05 9 0.1460366E+08 -0.2941683E+08 0.4456127E+05 -0.5573295E+05 10 0.1569486E+08 -0.2908289E+08 0.4792773E+05 -0.5442820E+05 11 0.1597054E+08 -0.2894035E+08 0.4873858E+05 -0.5402454E+05 12 0.1602926E+08 -0.2890748E+08 0.4890864E+05 -0.5393540E+05 13 0.1677659E+08 -0.2841969E+08 0.5095999E+05 -0.5271432E+05 14 0.1788490E+08 -0.2750364E+08 0.5353416E+05 -0.5067630E+05 15 0.1897163E+08 -0.2642440E+08 0.5503347E+05 -0.4850154E+05 16 0.1966971E+08 -0.2564707E+08 0.5489007E+05 -0.4706773E+05 17 0.2000100E+08 -0.2525554E+08 0.5414996E+05 -0.4640891E+05 18 0.2013518E+08 -0.2509276E+08 0.5355872E+05 -0.4616213E+05 19 0.2018596E+08 -0.2503050E+08 0.5322307E+05 -0.4607875E+05 20 0.2020468E+08 -0.2500746E+08 0.5305581E+05 -0.4605237E+05 [Vapour Properties] Stage Moleweight Density Viscosity Heat capacity Thermal conductivity 1 0.9214727E+02 0.3026177E+01 0.8981917E-05 0.1349145E+06 0.1886397E-01 2 0.9214612E+02 0.3025584E+01 0.8983883E-05 0.1349128E+06 0.1886759E-01 3 0.9214775E+02 0.3024730E+01 0.8986808E-05 0.1349347E+06 0.1887467E-01 4 0.9215183E+02 0.3023203E+01 0.8992034E-05 0.1349839E+06 0.1888818E-01 5 0.9215988E+02 0.3020151E+01 0.9002348E-05 0.1350862E+06 0.1891589E-01 6 0.9217638E+02 0.3013062E+01 0.9025730E-05 0.1353279E+06 0.1898208E-01 7 0.9221533E+02 0.2991789E+01 0.9093570E-05 0.1360676E+06 0.1918981E-01 8 0.9232777E+02 0.2918870E+01 0.9327639E-05 0.1386683E+06 0.1994055E-01 9 0.9257787E+02 0.2806020E+01 0.9736155E-05 0.1427048E+06 0.2110954E-01 10 0.9275237E+02 0.2755630E+01 0.9947531E-05 0.1444299E+06 0.2159181E-01 11 0.9280328E+02 0.2743447E+01 0.1000228E-04 0.1448307E+06 0.2170001E-01 12 0.9281451E+02 0.2740880E+01 0.1001402E-04 0.1449141E+06 0.2172226E-01 13 0.9296922E+02 0.2708945E+01 0.1016657E-04 0.1459010E+06 0.2197868E-01 14 0.9325054E+02 0.2664457E+01 0.1040341E-04 0.1471284E+06 0.2225207E-01 15 0.9359915E+02 0.2623920E+01 0.1065211E-04 0.1479845E+06 0.2236003E-01 16 0.9387061E+02 0.2599427E+01 0.1082303E-04 0.1483079E+06 0.2232039E-01 17 0.9401501E+02 0.2588218E+01 0.1090787E-04 0.1483873E+06 0.2226485E-01 18 0.9407666E+02 0.2583754E+01 0.1094299E-04 0.1484044E+06 0.2223475E-01 19 0.9410050E+02 0.2582076E+01 0.1095641E-04 0.1484084E+06 0.2222214E-01 20 0.9410936E+02 0.2581459E+01 0.1096137E-04 0.1484096E+06 0.2221732E-01 [Liquid Properties] Stage Moleweight Density Viscosity Heat capacity Thermal cond. Surface tension 1 0.9214612E+02 0.7844353E+03 0.2494763E-03 0.1946586E+06 0.1120624E+00 0.1818205E-01 2 0.9214926E+02 0.7850188E+03 0.2501360E-03 0.1946715E+06 0.1121367E+00 0.1820693E-01 3 0.9215714E+02 0.7860500E+03 0.2513525E-03 0.1947112E+06 0.1122650E+00 0.1825122E-01 4 0.9217272E+02 0.7879941E+03 0.2536705E-03 0.1948023E+06 0.1125061E+00 0.1833480E-01 5 0.9220495E+02 0.7920136E+03 0.2585034E-03 0.1950298E+06 0.1130042E+00 0.1850746E-01 6 0.9228280E+02 0.8018593E+03 0.2705415E-03 0.1956981E+06 0.1142229E+00 0.1892865E-01 7 0.9252626E+02 0.8337966E+03 0.3113861E-03 0.1978789E+06 0.1181314E+00 0.2026104E-01 8 0.9316642E+02 0.9237060E+03 0.4324870E-03 0.2023723E+06 0.1285622E+00 0.2351233E-01 9 0.9365892E+02 0.9941471E+03 0.5003551E-03 0.2077006E+06 0.1364508E+00 0.2507802E-01 10 0.9379372E+02 0.1011652E+04 0.5017388E-03 0.2104044E+06 0.1386056E+00 0.2513073E-01 11 0.9382198E+02 0.1015069E+04 0.5003736E-03 0.2111008E+06 0.1390619E+00 0.2510534E-01 12 0.9382776E+02 0.1015754E+04 0.5000134E-03 0.2112499E+06 0.1391555E+00 0.2509831E-01 13 0.9389490E+02 0.1023317E+04 0.4936068E-03 0.2131717E+06 0.1402558E+00 0.2496458E-01 14 0.9397771E+02 0.1031336E+04 0.4795554E-03 0.2160997E+06 0.1416540E+00 0.2464725E-01 15 0.9404563E+02 0.1036467E+04 0.4622701E-03 0.2190776E+06 0.1428609E+00 0.2423181E-01 16 0.9408455E+02 0.1038669E+04 0.4498468E-03 0.2210596E+06 0.1435899E+00 0.2392034E-01 17 0.9410208E+02 0.1039461E+04 0.4436403E-03 0.2220231E+06 0.1439295E+00 0.2376125E-01 18 0.9410903E+02 0.1039739E+04 0.4410719E-03 0.2224180E+06 0.1440665E+00 0.2369479E-01 19 0.9411165E+02 0.1039838E+04 0.4400916E-03 0.2225682E+06 0.1441183E+00 0.2366933E-01 20 0.9411261E+02 0.1039874E+04 0.4397291E-03 0.2226237E+06 0.1441374E+00 0.2365990E-01 [Vapour phase compositions] Component Mole fractions on stages: 1 to 5 1 0.301121480E-03 0.100000000E-02 0.222222973E-02 0.441545990E-02 0.853339859E-02 2 0.998678754E+00 0.998398179E+00 0.997304659E+00 0.995151303E+00 0.991046360E+00 3 0.102012456E-02 0.601820964E-03 0.473111150E-03 0.433237046E-03 0.420241584E-03 Component Mole fractions on stages: 6 to 10 1 0.169194481E-01 0.366782486E-01 0.937084604E-01 0.220539828E+00 0.309038124E+00 2 0.982665845E+00 0.962911911E+00 0.905889790E+00 0.779071861E+00 0.690582433E+00 3 0.414707005E-03 0.409840362E-03 0.401749415E-03 0.388310955E-03 0.379442566E-03 Component Mole fractions on stages: 11 to 15 1 0.334854542E+00 0.340551208E+00 0.419735777E+00 0.562635708E+00 0.739467231E+00 2 0.664769508E+00 0.659073760E+00 0.580132937E+00 0.437325244E+00 0.260523646E+00 3 0.375949280E-03 0.375032407E-03 0.131285336E-03 0.390481433E-04 0.912302545E-05 Component Mole fractions on stages: 16 to 20 1 0.877110364E+00 0.950319879E+00 0.981579130E+00 0.993664510E+00 0.998156103E+00 2 0.122887948E+00 0.496798524E-01 0.184208296E-01 0.633548457E-02 0.184389596E-02 3 0.168743465E-05 0.269032692E-06 0.399267689E-07 0.569619792E-08 0.740229746E-09 [Liquid phase compositions] Component Mole fractions on stages: 1 to 5 1 0.100000000E-02 0.335430488E-02 0.758689068E-02 0.155633547E-01 0.319431919E-01 2 0.998398179E+00 0.996291800E+00 0.992136411E+00 0.984185848E+00 0.967818687E+00 3 0.601820964E-03 0.353895280E-03 0.276698178E-03 0.250796804E-03 0.238120973E-03 Component Mole fractions on stages: 6 to 10 1 0.714569464E-01 0.195006281E+00 0.519814891E+00 0.769653168E+00 0.838026509E+00 2 0.928320353E+00 0.804810578E+00 0.480087854E+00 0.230299915E+00 0.161937966E+00 3 0.222700141E-03 0.183141407E-03 0.972556965E-04 0.469160770E-04 0.355246783E-04 Component Mole fractions on stages: 11 to 15 1 0.852362046E+00 0.855293044E+00 0.889398923E+00 0.931406291E+00 0.965843216E+00 2 0.147604764E+00 0.144674250E+00 0.110591216E+00 0.685913122E-01 0.341563168E-01 3 0.331904728E-04 0.327062774E-04 0.986126284E-05 0.239681404E-05 0.467061943E-06 Component Mole fractions on stages: 16 to 20 1 0.985576205E+00 0.994462343E+00 0.997988928E+00 0.999313740E+00 0.999800846E+00 2 0.144237172E-01 0.553764483E-02 0.201107049E-02 0.686260086E-03 0.199154148E-03 3 0.773629859E-07 0.117196355E-07 0.170398410E-08 0.241227194E-09 0.312586621E-10 [Reaction rates] Component reaction rates on stages: 1 to 5 1 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 2 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 3 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 Component reaction rates on stages: 6 to 10 1 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 2 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 3 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 Component reaction rates on stages: 11 to 15 1 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 2 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 3 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 Component reaction rates on stages: 16 to 20 1 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 2 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 3 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 -0.000000000E+00 [Condenser Heat Duty] -6.774479029E+05 [Reboiler Heat Duty] 9.531711785E+05 [UA Column] 0.000000000E+00 [K-values] Component K-values on stages: 1 to 5 1 0.301121479E+00 0.298124362E+00 0.292903882E+00 0.283708749E+00 0.267142953E+00 2 0.100028102E+01 0.100211422E+01 0.100520921E+01 0.101114165E+01 0.102400003E+01 3 0.169506318E+01 0.170056228E+01 0.170984556E+01 0.172744245E+01 0.176482390E+01 Component K-values on stages: 6 to 10 1 0.236778214E+00 0.188087524E+00 0.180272751E+00 0.286544430E+00 0.368768912E+00 2 0.105854174E+01 0.119644540E+01 0.188692503E+01 0.338285779E+01 0.426448750E+01 3 0.186217665E+01 0.223783561E+01 0.413085741E+01 0.827671408E+01 0.106810979E+02 Component K-values on stages: 11 to 15 1 0.392854825E+00 0.398169038E+00 0.471931960E+00 0.604071192E+00 0.765618289E+00 2 0.450371310E+01 0.455557060E+01 0.524574155E+01 0.637581101E+01 0.762739283E+01 3 0.113270239E+02 0.114666797E+02 0.133132377E+02 0.162916866E+02 0.195327956E+02 Component K-values on stages: 16 to 20 1 0.889946773E+00 0.955611729E+00 0.983557135E+00 0.994346890E+00 0.998354930E+00 2 0.851985285E+01 0.897129627E+01 0.915971357E+01 0.923190013E+01 0.925863702E+01 3 0.218119121E+02 0.229557218E+02 0.234314210E+02 0.236134153E+02 0.236807879E+02 [Molecular weights] 1 94.113 2 92.141 3 98.188 [Feed stream 1] 12 Stage Number 5.9984109360026E-02 Flow rate 4.2085985482200E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.9121771586193E+07 Enthalpy [J/kmol] -5.4538792278961E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 8.3383777000000E-01 Mole fraction of component 1 1.6606223000000E-01 Mole fraction of component 2 9.9999999999957E-05 Mole fraction of component 3 5.9984109360026E-02 Flow rate 8.3383777000000E-01 Mole fraction of component 1 1.6606223000000E-01 Mole fraction of component 2 9.9999999999957E-05 Mole fraction of component 3 9.3785849392838E+01 Molar mass 1.0106397917352E+03 Density 5.0209360904420E-04 Viscosity 1.3847263999555E-01 Thermal conductivity 2.1020757524785E+05 Heat capacity 2.5136852966478E-02 Surface tension [Reflashed Feed stream 1] 12 Stage Number 5.9984109360026E-02 Flow rate 4.2085985482539E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.9121771586193E+07 Enthalpy [J/kmol] -5.4538792277318E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 8.3383777000000E-01 Mole fraction of component 1 1.6606223000000E-01 Mole fraction of component 2 9.9999999999957E-05 Mole fraction of component 3 5.9984109360026E-02 Flow rate 8.3383777000000E-01 Mole fraction of component 1 1.6606223000000E-01 Mole fraction of component 2 9.9999999999957E-05 Mole fraction of component 3 9.3785849392838E+01 Molar mass 1.0106397917318E+03 Density 5.0209360902800E-04 Viscosity 1.3847263999529E-01 Thermal conductivity 2.1020757524929E+05 Heat capacity 2.5136852966116E-02 Surface tension [Top product] 1 Stage Number 9.9670994040000E-03 Flow rate 3.8381005550000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.2104923727565E+07 Enthalpy [J/kmol] -5.4562762519393E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 1.0000000000000E-03 Mole fraction of component 1 9.9839817900000E-01 Mole fraction of component 2 6.0182096400000E-04 Mole fraction of component 3 9.9670994040000E-03 Flow rate 1.0000000000000E-03 Mole fraction of component 1 9.9839817900000E-01 Mole fraction of component 2 6.0182096400000E-04 Mole fraction of component 3 9.2146115054430E+01 Molar mass 7.8443534888450E+02 Density 2.4947625874963E-04 Viscosity 1.1206237714107E-01 Thermal conductivity 1.9465856874436E+05 Heat capacity 1.8182054962293E-02 Surface tension [Bottom product] 20 Stage Number 5.0017009950000E-02 Flow rate 4.5493962070000E+02 Temperature [K] 1.0132500000000E+05 Pressure [Pa] -2.5007458181469E+07 Enthalpy [J/kmol] -4.6052370896892E+04 Entropy [J/kmol/K] 0.0000000000000E+00 Vapour fraction [-] 1.0000000000000E+00 Liquid phase split ratio [-] 9.9980084600000E-01 Mole fraction of component 1 1.9915414800000E-04 Mole fraction of component 2 3.1258662100000E-11 Mole fraction of component 3 5.0017009950000E-02 Flow rate 9.9980084600000E-01 Mole fraction of component 1 1.9915414800000E-04 Mole fraction of component 2 3.1258662100000E-11 Mole fraction of component 3 9.4112606148633E+01 Molar mass 1.0398737175000E+03 Density 4.3972905198230E-04 Viscosity 1.4413738568758E-01 Thermal conductivity 2.2262369472335E+05 Heat capacity 2.3659902505349E-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 stagew@{#w@E,bw@wx@6% x@kax@!;ox@y@4HSVz@cvz@e;}z@.EFz@.ۘU{@D{@E[,|@>myU|@*k@If|@MAìl|@Po|@"Pressure profile.Pressure at each stageм@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@м@(Vapour Flow profile4Vapour Flow at each stage{R0'#@f84@Z4@,8}4@4@ -G4@Kd&14@s3@uWG1@iu0@J}0@d_0@;00@3^%0@ht1@1V)$3@$.4@;,`Dӹ4@=O4@Bf 5@(Liquid Flow profile4Liquid Flow at each stage%@d?({%@cw%@Ǐ!\%@xif%@ f%s$@"@q>"@WTW?@#[߅@Ms@z.s@Hf"P@FP@e׃jP@o0!JQ@BjQ@ Q@UQ@ Q@rza-I@Duties profile*Duties at each stageHΏ$Zd[-A4Vapour Moleweight profile@Vapour Moleweight at each stagek&l W@RZ W@~jt W@O#- W@5Ry; W@VI W@@z W@ /W@s$W@u&0W@ah3W@ 4W@DR>W@PW@=yXfW@dwW@;ǀW@T:XW@OnW@eW@.Vapour Density profile:Vapour Density at each stageWBwI5@+hZbe4@4i2@KZ /@oD)@?@B</@D4Y@`r@Ͻ @yy:W@wR~R@@M-[@CP@@ b@%Y@F7@J>v@ Ӧ@2Vapour Viscosity profile>Vapour Viscosity at each stageE!>GFz/>|>g>ᄴI>P~>_~>KI> <k>@>A>m<>E"R>nI>HkV> ꑲ><>\>2->8>:Vapour Heat capacity profileFVapour Heat capacity at each stage%C`@>yX5`@Hr`@Q|`@J&`@x $(~`@y)a@V}bUa@Ǻa@ b@1*b@¨N@b@F)?l8?BK.1\>?ث!W@YJW@ʾ+jW@NrW@}RtW@;tW@0L FyW@8̒~W@mW@8gDiW@dzW@XW@L F%W@̒5W@.Liquid Density profile:Liquid Density at each stage~{@RI&@fffff@g@Q@@o_@S݌@B-@K7@d;O@y&1@K7@MbX@|?51@V:@Mb=@~j>@1Z?@"~?@2Liquid Viscosity profile>Liquid Viscosity at each stageR\Y0?$d0?Hkx0?3_0?0? 1?1h4?W\W?\QK-{=?hf =?9bk@46 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,DR3 not all ports are connectedFeed1{split}_stage12 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,@/@? @@ @?(@@(@`0@-@message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 383.81 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 383.81 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 383.81 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 383.88 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 383.88 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 383.88 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 383.98 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 383.98 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 383.98 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 384.18 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 384.18 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 384.18 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 384.57 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 384.57 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 384.57 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 385.48 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 385.48 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 385.48 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 388.17 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 388.17 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 388.17 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 397.59 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 397.59 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 397.59 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 413.56 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 413.56 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 413.56 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 421.43 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 421.43 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 421.43 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 423.42 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 423.42 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 423.42 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 423.85 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 423.85 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 423.85 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 429.27 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 429.27 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 429.27 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 437.37 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 437.37 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 437.37 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 445.45 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 445.45 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 445.45 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 450.77 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 450.77 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 450.77 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 453.34 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 453.34 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 453.34 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 454.39 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 454.39 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 454.39 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 454.79 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 454.79 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 454.79 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 454.94 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 454.94 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 454.94 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 420.86 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 420.86 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 420.86 K, range = [273.15 - 374.08] K) #(last 3 messages repeated 1 time) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 383.81 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 383.81 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 383.81 K, range = [273.15 - 374.08] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Toluene (T = 454.94 K, range = [190.00 - 383.78] K) message: Warning: temperature out of range for liquid viscosity correlation for compound Methylcyclohexane (T = 454.94 K, range = [248.15 - 374.08] K) message: Warning: temperature out of range for liquid thermal conductivity for compound Methylcyclohexane (T = 454.94 K, range = [273.15 - 374.08] K) Solvent Makeup6Mixer - mix 2 or more inlet streams to a single outletk!^/E a-COUSCOUS0002Number of inletsNumber of inlet ports Pressure drop Pressure drop? _BThermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Last runD+++ specifications +++ Number of inlets: 2 Pressure drop: 0 Pa - $not all material ports are connectedInlet 1Inlet 2Outlet0@@@@@@@CoolerMHeaterCooler - heat or cool stream specifying heat duty or outlet temperaturez,wKJEKBCOUSCOUS0002TypeOperation type Temperature Heat duty Heat duty Temperature Energy inletOutlet temperatureOutlet temperature?Pw@r@ _B Heat duty Heat duty@?@c#)@x@xD Pressure drop Pressure drop? _BThermo Version*Thermodynamics CAPE OPEN Interface version1.01.01.01.1Last run+++ specifications +++ Heat duty: -842965.569115568 W Pressure drop: 0 Pa +++ optional parameters +++ Outlet temperature: 373 K .6 : $not all material ports are connectedInletOutlet HmUd n?TTHmUd n?TTHmUd n?TTHmUd n?TT@@ ɿ@????@@@@@ɿ@@@MS Sans -C6?-C6?h㈵>-C6?http://www.chemsep.com/Copyright (c) 2012 ChemSep.orgVUUUUeB@ P@<@@-http://pubs.acs.org/doi/pdf/10.1021/ie990654kEExtractive Distillation of Toluene and MethylCycloHexane using PhenolXUUUU5@TUUUUU @43333sM@@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\f0\fs27 20 kmol/s\f1\fs29 \par } T@;@@)@=@fffff&@@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 110.85\super o\nosupersub C \par } T@;@$I$IRB@xF@7@L:@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\f0\fs27 x\sub Tol\nosupersub = 0.5\f1\fs29 \par } S@;@@)@;@L>@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 1 atm\f1\fs29 \par } K@;@gffffFD@hffffI@"@433333(@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 RR = 8\f1\fs29 \par } P@;@K@tP@0@fffff3@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 x\sub MCH\nosupersub = 0.9999\b0\f1\fs29 \par } ^@;@L@43333Q@433333*@/@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 1 atm\f1\fs29 \par } K@;@43333#P@43333R@L<@?@@J@*:@ݍF@*:@ݍF@J@*:@*:@ @ @@J@*2@ݍF@*2@ݍF@J@*2@*2@ @ @@S@UUUUUC@Q@UUUUUC@Q@S@UUUUUC@UUUUUC@ @ @{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 2\f1\fs29 \par } 1@;@IH@I@+@0@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 2\f1\fs29 \par } 1@;@Q@R@DDDDD?@HA@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 10\f1\fs29 \par } ;@;@G@0I@/@2@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 25\f1\fs29 \par } ;@;@H@ffffffI@DDDDD7@:@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 39\f1\fs29 \par } ;@;@IH@I@DDDDD;@>@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 12\f1\fs29 \par } ;@;@Q@R@"""""bB@C@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 19\f1\fs29 \par } ;@;@Q@R@"""""bD@E@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 x\sub Tol\nosupersub = 0.999\b0\f1\fs29 \par } @Y@;@T@43333X@ B@43333sC@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}{\f1\fnil MS Sans;}} \viewkind4\uc1\pard\b\f0\fs27 Rec\sub Tol\nosupersub = 0.001\b0\f1\fs29 \par } _@;@|T@̜W@ J@43333sK@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 100\super o\nosupersub C \par } L@;@$I$IRC@xG@/@L2@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 147.7\super o\nosupersub C \par } R@;@$I$IRM@W|WP@C@hffff&E@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 181.8\super o\nosupersub C \par } R@;@$I$Q@W|WS@@L@hffffM@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 110.6\super o\nosupersub C \par } R@;@$I$)U@W|W@hffff@@{\rtf1\ansi\ansicpg1252\deff0\deflang1033{\fonttbl{\f0\fnil\fcharset0 Roman;}} \viewkind4\uc1\pard\f0\fs27 101\super o\nosupersub C \par } L@;@$I$iT@W|W|V@0@L3@ׁ?ׁ?ׁ?ׁ??,:Pn}