© 2024 Jasper van Baten, AmsterCHEM

Supported calculations

REFROP CAPE-OPEN supplies the following compound constants: casRegistryNumber, chemicalFormula, acentricFactor, charge, criticalDensity, criticalPressure, criticalTemperature, criticalVolume, dipoleMoment, molecularWeight and normalBoilingPoint.

The following temperature dependent properties are supported: vaporPressure, vaporPressure.Dtemperature, fugacityCoefficientOfVapor, heatCapacityOfLiquid, heatOfVaporization, surfaceTensionSatLiquid, thermalConductivityOfLiquid, thermalConductivityOfVapor, virialCoefficient, virialCoefficient.Dtemperature, idealGasEnthalpy, idealGasEnthalpy.Dtemperature, idealGasEntropy, idealGasHeatCapacity, viscosityOfLiquid, viscosityOfVapor, volumeChangeUponVaporization and volumeOfLiquid.

The supported phases are Vapor and Liquid.

The following single phase mixture properties are supported: compressibility, compressibility.Dtemperature, compressibility.Dpressure, compressibility.Dmoles, compressibility.DmolFraction, compressibilityFactor, compressibilityFactor.Dtemperature, compressibilityFactor.Dpressure, compressibilityFactor.Dmoles, compressibilityFactor.DmolFraction, density, density.Dtemperature, density.Dpressure, density.Dmoles, density.DmolFraction, enthalpy, enthalpy.Dtemperature, enthalpy.Dpressure, enthalpy.Dmoles, enthalpy.DmolFraction, entropy, entropy.Dtemperature, entropy.Dpressure, entropy.Dmoles, entropy.DmolFraction, fugacity, fugacity.Dtemperature, fugacity.Dpressure, fugacity.Dmoles, fugacity.DmolFraction, fugacityCoefficient, fugacityCoefficient.Dtemperature, fugacityCoefficient.Dpressure, fugacityCoefficient.Dmoles, fugacityCoefficient.DmolFraction, gibbsEnergy, gibbsEnergy.Dtemperature, gibbsEnergy.Dpressure, gibbsEnergy.Dmoles, gibbsEnergy.DmolFraction, heatCapacityCp, heatCapacityCp.Dtemperature, heatCapacityCp.Dpressure, heatCapacityCp.Dmoles, heatCapacityCp.DmolFraction, heatCapacityCv, heatCapacityCv.Dtemperature, heatCapacityCv.Dpressure, heatCapacityCv.Dmoles, heatCapacityCv.DmolFraction, helmholtzEnergy, helmholtzEnergy.Dtemperature, helmholtzEnergy.Dpressure, helmholtzEnergy.Dmoles, helmholtzEnergy.DmolFraction, internalEnergy, internalEnergy.Dtemperature, internalEnergy.Dpressure, internalEnergy.Dmoles, internalEnergy.DmolFraction, jouleThomsonCoefficient, jouleThomsonCoefficient.Dtemperature, jouleThomsonCoefficient.Dpressure, jouleThomsonCoefficient.Dmoles, jouleThomsonCoefficient.DmolFraction, logFugacityCoefficient, logFugacityCoefficient.Dtemperature, logFugacityCoefficient.Dpressure, logFugacityCoefficient.Dmoles, logFugacityCoefficient.DmolFraction, speedOfSound, speedOfSound.Dtemperature, speedOfSound.Dpressure, speedOfSound.Dmoles, speedOfSound.DmolFraction, thermalConductivity, thermalConductivity.Dtemperature, thermalConductivity.Dpressure, thermalConductivity.Dmoles, thermalConductivity.DmolFraction, viscosity, viscosity.Dtemperature, viscosity.Dpressure, viscosity.Dmoles, viscosity.DmolFraction, volume, volume.Dtemperature, volume.Dpressure, volume.Dmoles, volume.DmolFraction and molecularWeight.

The following two-phase mixture properties are supported: kvalue, kvalue.Dtemperature, kvalue.Dpressure, kvalue.Dmoles, kvalue.DmolFraction, logKvalue, logKvalue.Dtemperature, logKvalue.Dpressure, logKvalue.Dmoles, logKvalue.DmolFraction, surfaceTension, surfaceTension.Dtemperature, surfaceTension.Dpressure, surfaceTension.Dmoles, and surfaceTension.DmolFraction.

Most temperature derivatives and all pressure- and composition derivatives are done by perturbation as they are not supplied by refprop.dll. Composition derivatives for two-phase properties are not available in CAPE-OPEN version 1.0.

The following flash calculations are supported: temperature-pressure, volume-enthalpy(1.1), volume-entropy(1.1), volume-internal energy(1.1), temperature-enthalpy, temperature-entropy, pressure-volume(1.1), temperature-volume(1.1), pressure-enthalpy, pressure-entropy, enthalpy-entropy, pressure-internal(1.1) energy, temperature-vapor fraction and pressure-vapor fraction.

The flash calculations marked with (1.1) are only available when using the CAPE-OPEN version 1.1 standard.

Calculations are only supported within the range of validity defined by REFPROP.

INDEX
Calculation methods
CAPE-OPEN
COM registration
Compound constants
Configuring Property Packages
Copyright
Disclaimer
Editing Property Packages
Flash calculations
Fluid files
Getting started
License
Mixture coefficients
Mixture properties
Property derivatives
Property Package files
Single-phase properties
Supported properties
Temperature dependent properties
Two-phase properties
User data
Version
Welcome
CONTENT
 Welcome
 Getting started
 Configuring Property Packages
 Supported calculations
 License