Log generated by C:\Program Files\AspenTech\Aspen HYSYS V7.2\hysys.exe Using configuration from C:\Program Files\CAPE-OPEN\COLTT\CAPE-OPENLogs.ini COLTT Version is 1.08.5 built on Aug 18 2010 at 23:05:38 ClassFactory : Loading Aspen Properties 24.0 implemented by C:\Program Files\AspenTech\APrSystem V7.2\Engine\Xeq\atcoproperties.dll ClassFactory : Created instance of Aspen Properties 24.0 successfully ClassFactory : Logging enabled for Thermo System Aspen Properties 24.0 ThermoSystem : Call to ResolvePropertyPackage ThermoSystem : PropertyPackage to be resolved : EtOHWaterNRTL EtOHWaterNRTL is a valid package name ThermoSystem : Return from ResolvePropertyPackage - Succeeded PropertyPackage : IPersistStorage is not supported in the logged component PropertyPackage : IPersistStreamInit is not supported in the logged component PropertyPackage : IPersistStream is not supported in the logged component PropertyPackage : Logging for unidentified interface with GUID {0000001B-0000-0000-C000-000000000046} is not supported by COLTT PropertyPackage : Logging for IMarshal with GUID {00000003-0000-0000-C000-000000000046} is not supported by COLTT ThermoSystem : Logging for unidentified interface with GUID {0000001B-0000-0000-C000-000000000046} is not supported by COLTT ThermoSystem : Logging for IMarshal with GUID {00000003-0000-0000-C000-000000000046} is not supported by COLTT PropertyPackage : Call to GetComponentList PropertyPackage : GetComponentList returns : Name CAS No Formula TBP MW ETHANOL 64-17-5 C2H6O-2 351.44 46.069 WATER 7732-18-5 H2O 373.15 18.0153 PropertyPackage : Return from GetComponentList - Succeeded PropertyPackage : Call to GetPhaseList PropertyPackage : GetPhaseList returns [Vapor Liquid Overall L2 VaporLiquid LiquidLiquid Solid ] PropertyPackage : Return from GetPhaseList - Succeeded PropertyPackage : Call to GetPropList PropertyPackage : GetPropList Returns fugacityCoefficient fugacityCoefficient.Dtemperature fugacityCoefficient.Dpressure fugacityCoefficient.Dmolfraction fugacityCoefficient.Dmoles logFugacityCoefficient logFugacityCoefficient.Dtemperature logFugacityCoefficient.Dpressure logFugacityCoefficient.Dmolfraction logFugacityCoefficient.Dmoles fugacity fugacity.Dtemperature fugacity.Dpressure fugacity.Dmolfraction fugacity.Dmoles enthalpy enthalpy.Dtemperature enthalpy.Dpressure enthalpy.Dmolfraction enthalpy.Dmoles entropy entropy.Dtemperature entropy.Dpressure entropy.Dmolfraction entropy.Dmoles gibbsFreeEnergy gibbsFreeEnergy.Dtemperature gibbsFreeEnergy.Dpressure gibbsFreeEnergy.Dmolfraction gibbsFreeEnergy.Dmoles volume volume.Dtemperature volume.Dpressure volume.Dmolfraction volume.Dmoles diffusionCoefficient diffusionCoefficient.Dtemperature diffusionCoefficient.Dmolfraction diffusionCoefficient.Dmoles viscosity viscosity.Dtemperature viscosity.Dpressure viscosity.Dmolfraction viscosity.Dmoles thermalConductivity thermalConductivity.Dtemperature thermalConductivity.Dmolfraction thermalConductivity.Dmoles surfaceTension surfaceTension.Dtemperature surfaceTension.Dmolfraction surfaceTension.Dmoles heatCapacity heatCapacityCv activityCoefficient kvalues density energy netHeatingValue grossHeatingValue molecularWeight vaporPressure normalBoilingPoint normalFreezingPoint criticalTemperature criticalPressure criticalCompressibilityFactor acentricFactor idealGasEnthalpyOfFormationAt25C gyrationRadius energyLennardJones lengthLennardJones pH solubilityIndex PropertyPackage : Return from GetPropList - Succeeded PropertyPackage : Call to put_simulationContext PropertyPackage put_simulationContext takes input argument: 0634B820 PropertyPackage : Return from put_simulationContext - Succeeded PropertyPackage : Call to GetComponentList PropertyPackage : GetComponentList returns : Name CAS No Formula TBP MW ETHANOL 64-17-5 C2H6O-2 351.44 46.069 WATER 7732-18-5 H2O 373.15 18.0153 PropertyPackage : Return from GetComponentList - Succeeded PropertyPackage : Call to GetPhaseList PropertyPackage : GetPhaseList returns [Vapor Liquid Overall L2 VaporLiquid LiquidLiquid Solid ] PropertyPackage : Return from GetPhaseList - Succeeded PropertyPackage : Call to GetPropList PropertyPackage : GetPropList Returns fugacityCoefficient fugacityCoefficient.Dtemperature fugacityCoefficient.Dpressure fugacityCoefficient.Dmolfraction fugacityCoefficient.Dmoles logFugacityCoefficient logFugacityCoefficient.Dtemperature logFugacityCoefficient.Dpressure logFugacityCoefficient.Dmolfraction logFugacityCoefficient.Dmoles fugacity fugacity.Dtemperature fugacity.Dpressure fugacity.Dmolfraction fugacity.Dmoles enthalpy enthalpy.Dtemperature enthalpy.Dpressure enthalpy.Dmolfraction enthalpy.Dmoles entropy entropy.Dtemperature entropy.Dpressure entropy.Dmolfraction entropy.Dmoles gibbsFreeEnergy gibbsFreeEnergy.Dtemperature gibbsFreeEnergy.Dpressure gibbsFreeEnergy.Dmolfraction gibbsFreeEnergy.Dmoles volume volume.Dtemperature volume.Dpressure volume.Dmolfraction volume.Dmoles diffusionCoefficient diffusionCoefficient.Dtemperature diffusionCoefficient.Dmolfraction diffusionCoefficient.Dmoles viscosity viscosity.Dtemperature viscosity.Dpressure viscosity.Dmolfraction viscosity.Dmoles thermalConductivity thermalConductivity.Dtemperature thermalConductivity.Dmolfraction thermalConductivity.Dmoles surfaceTension surfaceTension.Dtemperature surfaceTension.Dmolfraction surfaceTension.Dmoles heatCapacity heatCapacityCv activityCoefficient kvalues density energy netHeatingValue grossHeatingValue molecularWeight vaporPressure normalBoilingPoint normalFreezingPoint criticalTemperature criticalPressure criticalCompressibilityFactor acentricFactor idealGasEnthalpyOfFormationAt25C gyrationRadius energyLennardJones lengthLennardJones pH solubilityIndex PropertyPackage : Return from GetPropList - Succeeded PropertyPackage : Logging for unidentified interface with GUID {0000001B-0000-0000-C000-000000000046} is not supported by COLTT PropertyPackage : Logging for IMarshal with GUID {00000003-0000-0000-C000-000000000046} is not supported by COLTT PropertyPackage : Call to GetPropList PropertyPackage : GetPropList Returns fugacityCoefficient fugacityCoefficient.Dtemperature fugacityCoefficient.Dpressure fugacityCoefficient.Dmolfraction fugacityCoefficient.Dmoles logFugacityCoefficient logFugacityCoefficient.Dtemperature logFugacityCoefficient.Dpressure logFugacityCoefficient.Dmolfraction logFugacityCoefficient.Dmoles fugacity fugacity.Dtemperature fugacity.Dpressure fugacity.Dmolfraction fugacity.Dmoles enthalpy enthalpy.Dtemperature enthalpy.Dpressure enthalpy.Dmolfraction enthalpy.Dmoles entropy entropy.Dtemperature entropy.Dpressure entropy.Dmolfraction entropy.Dmoles gibbsFreeEnergy gibbsFreeEnergy.Dtemperature gibbsFreeEnergy.Dpressure gibbsFreeEnergy.Dmolfraction gibbsFreeEnergy.Dmoles volume volume.Dtemperature volume.Dpressure volume.Dmolfraction volume.Dmoles diffusionCoefficient diffusionCoefficient.Dtemperature diffusionCoefficient.Dmolfraction diffusionCoefficient.Dmoles viscosity viscosity.Dtemperature viscosity.Dpressure viscosity.Dmolfraction viscosity.Dmoles thermalConductivity thermalConductivity.Dtemperature thermalConductivity.Dmolfraction thermalConductivity.Dmoles surfaceTension surfaceTension.Dtemperature surfaceTension.Dmolfraction surfaceTension.Dmoles heatCapacity heatCapacityCv activityCoefficient kvalues density energy netHeatingValue grossHeatingValue molecularWeight vaporPressure normalBoilingPoint normalFreezingPoint criticalTemperature criticalPressure criticalCompressibilityFactor acentricFactor idealGasEnthalpyOfFormationAt25C gyrationRadius energyLennardJones lengthLennardJones pH solubilityIndex PropertyPackage : Return from GetPropList - Succeeded PropertyPackage : Call to GetPhaseList PropertyPackage : GetPhaseList returns [Vapor Liquid Overall L2 VaporLiquid LiquidLiquid Solid ] PropertyPackage : Return from GetPhaseList - Succeeded PropertyPackage : Call to GetComponentList PropertyPackage : GetComponentList returns : Name CAS No Formula TBP MW ETHANOL 64-17-5 C2H6O-2 351.44 46.069 WATER 7732-18-5 H2O 373.15 18.0153 PropertyPackage : Return from GetComponentList - Succeeded PropertyPackage : Call to GetComponentConstant requesting these constants : criticalTemperature MaterialObject : Call to get_ComponentIds get_ComponentIds returns : ETHANOL WATER MaterialObject : Return from get_ComponentIds - Succeeded PropertyPackage : GetComponentConstant returns Compounds criticalTemperature ETHANOL 514.000000 WATER 647.096000 PropertyPackage : Return from GetComponentConstant - Succeeded PropertyPackage : Call to GetComponentConstant requesting these constants : criticalPressure MaterialObject : Call to get_ComponentIds get_ComponentIds returns : ETHANOL WATER MaterialObject : Return from get_ComponentIds - Succeeded PropertyPackage : GetComponentConstant returns Compounds criticalPressure ETHANOL 6137000.000000 WATER 22064000.000000 PropertyPackage : Return from GetComponentConstant - Succeeded PropertyPackage : Call to GetComponentConstant requesting these constants : criticalVolume MaterialObject : Call to get_ComponentIds get_ComponentIds returns : ETHANOL WATER MaterialObject : Return from get_ComponentIds - Succeeded PropertyPackage : GetComponentConstant returns Compounds criticalVolume ETHANOL 0.000168 WATER 0.000056 PropertyPackage : Return from GetComponentConstant - Succeeded PropertyPackage : Call to GetComponentConstant requesting these constants : acentricFactor MaterialObject : Call to get_ComponentIds get_ComponentIds returns : ETHANOL WATER MaterialObject : Return from get_ComponentIds - Succeeded PropertyPackage : GetComponentConstant returns Compounds acentricFactor ETHANOL 0.643558 WATER 0.344861 PropertyPackage : Return from GetComponentConstant - Succeeded PropertyPackage : Call to GetComponentConstant requesting these constants : liquidDensityAt25C MaterialObject : Call to get_ComponentIds get_ComponentIds returns : ETHANOL WATER MaterialObject : Return from get_ComponentIds - Succeeded CAPE-OPEN error: Error Name : ECapeLimitedImplHR Error Code : 0x8004050a Object Name : Anonymous Interface : (null) Method : (null) Description : (null) PropertyPackage : Error returned from GetComponentConstant - 0x8004050a PropertyPackage : Call to GetPhaseList PropertyPackage : GetPhaseList returns [Vapor Liquid Overall L2 VaporLiquid LiquidLiquid Solid ] PropertyPackage : Return from GetPhaseList - Succeeded PropertyPackage : Call to CalcEquilibrium requesting: Flashtype: TP Properties: MaterialObject : Logging for ICOMaterialObject with GUID {3C860BB3-8AF4-4D93-A4BB-F9D068804365} is not supported by COLTT MaterialObject : Call to GetNumComponents MaterialObject GetNumComponents returns 2 MaterialObject : Return from GetNumComponents - Succeeded MaterialObject : Call to get_ComponentIds get_ComponentIds returns : ETHANOL WATER MaterialObject : Return from get_ComponentIds - Succeeded MaterialObject : Call to GetProp Property temperature Overall (null) mixture 300.000000000 MaterialObject : Return from GetProp - Succeeded MaterialObject : Call to GetProp Property pressure Overall (null) mixture 100000.000000000 MaterialObject : Return from GetProp - Succeeded MaterialObject : Call to GetProp Property fraction Overall mole (null) ETHANOL 0.500000000 WATER 0.500000000 MaterialObject : Return from GetProp - Succeeded MaterialObject : Logging for ICOMaterialObject with GUID {3C860BB3-8AF4-4D93-A4BB-F9D068804365} is not supported by COLTT MaterialObject : Call to SetProp : Property PhaseFraction Vapor mole (null) -179769313486231570000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000.000000000