**********************************************LOG FORMAT************************************************** * Call on a given Object is indicated by 'Object<[Object Name]>: Call to [method name]'. * * Input arguments and returned values(if any) are then indicated. * * End of the call is indicated by 'Object<[Object Name]>: Return from [method name] - .' * ********************************************************************************************************** Log generated by C:\Program Files\PSE\gPROMS\bin\gSERVERcorba.exe Using configuration from C:\Program Files\CAPE-OPEN\COLTT\CAPE-OPENLogs.ini COLTT Version is 1.08.3 ClassFactory : Loading Aspen COMThermo (CAPE-OPEN 1.0) implemented by C:\Program Files\Fichiers communs\Hyprotech\CAPE-OPEN\HypCOTh.dll ClassFactory : Created instance of Aspen COMThermo (CAPE-OPEN 1.0) successfully ClassFactory : Logging enabled for Thermo System Aspen COMThermo (CAPE-OPEN 1.0) ThermoSystem : Call to ResolvePropertyPackage ThermoSystem : PropertyPackage to be resolved : EtOHWater EtOHWater is a valid package name ThermoSystem : Return from ResolvePropertyPackage - Succeeded ParameterCollection Parameter Collection Final Release... Simulation Context : Final Release ThermoSystem : Final Release PropertyPackage : Call to GetComponentList PropertyPackage : GetComponentList returns : Name CAS No Formula TBP MW Ethanol 64-17-5 C2H6O 351.398 46.0699 H2O 7732-18-5 H2O 373.148 18.0151 PropertyPackage : Return from GetComponentList - Succeeded PropertyPackage : Call to ICapeIdentification.get_ComponentName PropertyPackage : Return from ICapeIdentification.get_ComponentName - Succeeded PropertyPackage : Call to get_ComponentDescription PropertyPackage : Error returned from get_ComponentDescription - 0x80004001 PropertyPackage : Call to get_code PropertyPackage : Code: 0 PropertyPackage : Return from get_code - Succeeded PropertyPackage : Call to get_description PropertyPackage : Description: (null) PropertyPackage : Return from get_description - Succeeded PropertyPackage : Call to get_scope PropertyPackage : Scope: (null) PropertyPackage : Return from get_scope - Succeeded PropertyPackage : Call to get_interfaceName PropertyPackage : Interface Name: (null) PropertyPackage : Return from get_interfaceName - Succeeded PropertyPackage : Call to get_operation PropertyPackage : Operation: (null) PropertyPackage : Return from get_operation - Succeeded PropertyPackage : Call to get_moreInfo PropertyPackage : More Info: (null) PropertyPackage : Return from get_moreInfo - Succeeded PropertyPackage : Call to GetPhaseList PropertyPackage : GetPhaseList returns [Vapor Liquid L2 Overall VaporLiquid ] PropertyPackage : Return from GetPhaseList - Succeeded PropertyPackage : Call to GetComponentConstant requesting these constants : molecularweight MaterialObject : Call to get_ComponentIds get_ComponentIds returns : Ethanol H2O MaterialObject : Return from get_ComponentIds - Succeeded PropertyPackage : GetComponentConstant returns Compounds molecularweight Ethanol 46.069900 H2O 18.015100 PropertyPackage : Return from GetComponentConstant - Succeeded PropertyPackage : Call to GetPropList PropertyPackage : GetPropList Returns enthalpy entropy surfaceTension compressibilityFactor heatCapacity viscosity thermalConductivity volume kvalues fugacityCoefficient fugacity logFugacityCoefficient logFugacity logkvalues activityCoefficient heatCapacityCV gibbsFreeEnergy helmholtzFreeEnergy enthalpy.Dtemperature enthalpy.Dpressure entropy.Dtemperature entropy.Dpressure surfaceTension.Dtemperature surfaceTension.Dpressure compressibilityFactor.Dtemperature compressibilityFactor.Dpressure heatCapacity.Dtemperature heatCapacity.Dpressure viscosity.Dtemperature viscosity.Dpressure thermalConductivity.Dtemperature thermalConductivity.Dpressure volume.Dtemperature volume.Dpressure fugacityCoefficient.Dtemperature fugacityCoefficient.Dpressure fugacity.Dtemperature fugacity.Dpressure logFugacityCoefficient.Dtemperature logFugacityCoefficient.Dpressure logFugacity.Dtemperature logFugacity.Dpressure activityCoefficient.Dtemperature activityCoefficient.Dpressure heatCapacityCV.Dtemperature heatCapacityCV.Dpressure gibbsFreeEnergy.Dtemperature gibbsFreeEnergy.Dpressure helmholtzFreeEnergy.Dtemperature helmholtzFreeEnergy.Dpressure PropertyPackage : Return from GetPropList - Succeeded : Call to CalcEquilibrium requesting: Flashtype: TP Properties: enthalpy, volume MaterialObject : Call to GetNumComponents MaterialObject GetNumComponents returns 2 MaterialObject : Return from GetNumComponents - Succeeded MaterialObject : Call to get_ComponentIds get_ComponentIds returns : Ethanol H2O MaterialObject : Return from get_ComponentIds - Succeeded MaterialObject : Call to GetProp Property Phase--- Basis--- Calc---- Compounds Values returned fraction Overall mole (null) Ethanol 0.200000000 H2O 0.800000000 MaterialObject : Return from GetProp - Succeeded MaterialObject : Call to GetProp Property Phase--- Basis--- Calc---- Value returned temperature Overall (null) Mixture 358.150000000 MaterialObject : Return from GetProp - Succeeded MaterialObject : Call to GetProp Property Phase--- Basis--- Calc---- Value returned pressure Overall (null) Mixture 100000.000000000 MaterialObject : Return from GetProp - Succeeded MaterialObject : Call to SetProp : Property Phase--- Basis--- Calc---- Compounds New values fraction Vapor mole (null) Ethanol 0.463539263 H2O 0.536460737 MaterialObject : Return from SetProp - Succeeded MaterialObject : Call to SetProp : Property Phase--- Basis--- Calc---- New value phaseFraction Vapor mole (null) 0.257150069 MaterialObject : Return from SetProp - Succeeded MaterialObject : Call to SetProp : Property Phase--- Basis--- Calc---- Compounds New values fraction Liquid mole (null) Ethanol 0.108771426 H2O 0.891228574 MaterialObject : Return from SetProp - Succeeded MaterialObject : Call to SetProp : Property Phase--- Basis--- Calc---- New value phaseFraction Liquid mole (null) 0.742849931 MaterialObject : Return from SetProp - Succeeded MaterialObject : Call to GetNumComponents MaterialObject GetNumComponents returns 2 MaterialObject : Return from GetNumComponents - Succeeded MaterialObject : Call to GetProp Property Phase--- Basis--- Calc---- Value returned temperature Overall (null) Mixture 358.150000000 MaterialObject : Return from GetProp - Succeeded MaterialObject : Call to GetProp Property Phase--- Basis--- Calc---- Value returned pressure Overall (null) Mixture 100000.000000000 MaterialObject : Return from GetProp - Succeeded MaterialObject : Call to GetProp Property Phase--- Basis--- Calc---- Compounds Values returned fraction Vapor mole (null) Ethanol 0.463539263 H2O 0.536460737 MaterialObject : Return from GetProp - Succeeded MaterialObject : Call to SetProp : Property Phase--- Basis--- Calc---- New value enthalpy Vapor mole Mixture -235302.766082303 MaterialObject : Return from SetProp - Succeeded MaterialObject : Call to SetProp : Property Phase--- Basis--- Calc---- New value volume Vapor mole Mixture 0.029777737 MaterialObject : Return from SetProp - Succeeded MaterialObject : Call to GetProp Property Phase--- Basis--- Calc---- Compounds Values returned fraction Liquid mole (null) Ethanol 0.108771426 H2O 0.891228574 MaterialObject : Return from GetProp - Succeeded MaterialObject : Call to SetProp : Property Phase--- Basis--- Calc---- New value enthalpy Liquid mole Mixture -279075.311085926 MaterialObject : Return from SetProp - Succeeded MaterialObject : Call to SetProp : Property Phase--- Basis--- Calc---- New value volume Liquid mole Mixture 0.000022776 MaterialObject : Return from SetProp - Succeeded PropertyPackage : Return from CalcEquilibrium - Succeeded MaterialObject : Final Release ParameterCollection Parameter Collection Final Release... Simulation Context : Final Release PropertyPackage Property Package Final Release...