Class PhaseGERG2004Eos
java.lang.Object
neqsim.thermo.phase.Phase
neqsim.thermo.phase.PhaseEos
neqsim.thermo.phase.PhaseGERG2004Eos
- All Implemented Interfaces:
Serializable, Cloneable, PhaseEosInterface, PhaseInterface, ThermodynamicConstantsInterface
PhaseGERG2004Eos class.
- Version:
- $Id: $Id
- Author:
- Even Solbraa
- See Also:
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Field Summary
FieldsModifier and TypeFieldDescription(package private) double(package private) double(package private) double(package private) doubleprivate GERG2004EOS(package private) double(package private) double(package private) int(package private) double(package private) booleanprivate static final longSerialization version UID.(package private) double[]Fields inherited from class Phase
beta, calcMolarVolume, chemSyst, componentArray, diElectricConstant, mixingRuleType, molarVolume, numberOfComponents, numberOfMolesInPhase, phaseVolume, physicalPropertyHandler, pressure, pt, refPhase, temperature, thermoPropertyModelName, useVolumeCorrection, ZFields inherited from interface ThermodynamicConstantsInterface
atm, avagadroNumber, boltzmannConstant, electronCharge, faradayConstant, gravity, molarMassAir, normalStateTemperature, pi, planckConstant, R, referencePressure, referenceTemperature, standardStateTemperature, vacumPermittivity -
Constructor Summary
Constructors -
Method Summary
Modifier and TypeMethodDescriptionvoidaddComponent(String name, double moles, double molesInPhase, int compNumber) Add component to component array and update moles variables.clone()clone.doublegetCp()method to return specific heat capacity (Cp).doublegetCv()method to return specific heat capacity (Cv).doublemethod to return enthalpy of a phase in unit Joule.doublemethod to return entropy of the phase.doublegetGibbsEnergy.doublegetInternalEnergy.doubleGet the Joule Thomson Coefficient of a phase.voidinit.doublemolarVolume(double pressure, double temperature, double A, double B, PhaseType pt) molarVolume.voidSetter for the fieldxFracGERG.Methods inherited from class PhaseEos
calcA, calcAi, calcAij, calcAiT, calcAT, calcATT, calcB, calcBi, calcBij, calcf, calcg, calcPressure, calcPressuredV, dFdN, dFdNdN, dFdNdT, dFdNdV, dFdT, dFdTdT, dFdTdV, dFdV, dFdVdV, dFdVdVdV, dFdxdxMatrix, dFdxdxMatrixSimple, dFdxMatrix, dFdxMatrixSimple, displayInteractionCoefficients, equals, F, fb, FB, fBB, FBB, FBD, FBT, fBV, FBV, FD, FDT, FDV, Fn, FnB, FnV, FT, FTT, FTV, fv, FV, fVV, FVV, fVVV, FVVV, gb, gBB, gBV, geta, geta, getA, getAresTV, getAT, getATT, getb, getb, getB, getCpres, getCvres, getdPdrho, getdPdTVn, getdPdVTn, getdrhodN, getdrhodP, getdrhodT, getdTVndSVnJaobiMatrix, getdUdSdSVn, getdUdSdVn, getdUdSVn, getdUdVdVSn, getdUdVSn, getdVdrho, getEosMixingRule, getF, getf_loc, getg, getGradientVector, getGresTP, getHresdP, getHresTP, getKappa, getMixingRule, getMixingRuleName, getPressureAttractive, getPressureRepulsive, getSoundSpeed, getSresTP, getSresTV, getUSVHessianMatrix, gV, gVV, gVVV, molarVolume2, resetMixingRule, setMixingRule, setMixingRuleGEModelMethods inherited from class Phase
addComponent, addMoles, addMolesChemReac, calcA, calcAT, calcDiElectricConstant, calcDiElectricConstantdT, calcDiElectricConstantdTdT, calcMolarVolume, calcR, getActivityCoefficient, getActivityCoefficient, getActivityCoefficient, getActivityCoefficientSymetric, getActivityCoefficientUnSymetric, getAiT, getAlpha0_EOSCG, getAlpha0_GERG2008, getAlpha0_Leachman, getAlpha0_Leachman, getAlpha0_Vega, getAlphares_EOSCG, getAlphares_GERG2008, getAlphares_Leachman, getAlphares_Leachman, getAlphares_Vega, getAntoineVaporPressure, getBeta, getBi, getComponent, getComponent, getcomponentArray, getComponentNames, getComponents, getComponentWithIndex, getComposition, getCompressibilityX, getCompressibilityY, getCorrectedVolume, getCp, getCp0, getCv, getDensity, getDensity, getDensity_AGA8, getDensity_EOSCG, getDensity_GERG2008, getDensity_Leachman, getDensity_Leachman, getDensity_Vega, getDiElectricConstant, getEnthalpy, getEnthalpydP, getEnthalpydT, getEntropy, getEntropydP, getEntropydT, getExcessGibbsEnergy, getExcessGibbsEnergySymetric, getFlowRate, getFugacity, getFugacity, getGamma, getHelmholtzEnergy, getHID, getInfiniteDiluteFugacity, getInfiniteDiluteFugacity, getInitType, getInternalEnergy, getIsobaricThermalExpansivity, getIsothermalCompressibility, getJouleThomsonCoefficient, getLogActivityCoefficient, getLogInfiniteDiluteFugacity, getLogInfiniteDiluteFugacity, getLogPureComponentFugacity, getLogPureComponentFugacity, getMass, getMeanIonicActivity, getMixGibbsEnergy, getMixingRuleType, getModelName, getMolalMeanIonicActivity, getMolarComposition, getMolarMass, getMolarMass, getMolarVolume, getMolarVolume, getMoleFraction, getNumberOfComponents, getNumberOfIonicComponents, getNumberOfMolecularComponents, getNumberOfMolesInPhase, getOsmoticCoefficient, getOsmoticCoefficientOfWater, getOsmoticCoefficientOfWaterMolality, getpH, getpH, getPhase, getPhysicalProperties, getPhysicalPropertyModel, getPressure, getPressure, getProperties_EOSCG, getProperties_GERG2008, getProperties_Leachman, getProperties_Leachman, getProperties_Vega, getPseudoCriticalPressure, getPseudoCriticalTemperature, getPureComponentFugacity, getPureComponentFugacity, getRefPhase, getRefPhase, getSoundSpeed, getTemperature, getTemperature, getThermalConductivity, getThermalConductivity, getThermoPropertyModelName, getTotalVolume, getType, getViscosity, getViscosity, getVolume, getVolume, getWaterDensity, getWtFrac, getWtFrac, getWtFraction, getWtFractionOfWaxFormingComponents, getZ, getZvolcorr, groupTBPfractions, hasComponent, hasPlusFraction, hasTBPFraction, initPhysicalProperties, initPhysicalProperties, initRefPhases, initRefPhases, isConstantPhaseVolume, isMixingRuleDefined, normalize, removeComponent, resetPhysicalProperties, setAttractiveTerm, setBeta, setComponentArray, setConstantPhaseVolume, setEmptyFluid, setInitType, setMolarVolume, setMoleFractions, setNumberOfComponents, setParams, setPhysicalProperties, setPhysicalPropertyModel, setPpm, setPressure, setProperties, setRefPhase, setRefPhase, setTemperature, setTotalVolume, setType, useVolumeCorrection, useVolumeCorrectionMethods inherited from class Object
finalize, getClass, hashCode, notify, notifyAll, toString, wait, wait, waitMethods inherited from interface PhaseEosInterface
getMolarVolumeMethods inherited from interface PhaseInterface
addMoles, addMolesChemReac, addMolesChemReac, calcAT, calcMolarVolume, calcR, getActivityCoefficient, getActivityCoefficient, getActivityCoefficient, getActivityCoefficientSymetric, getActivityCoefficientUnSymetric, getAlpha0_EOSCG, getAlpha0_GERG2008, getAlpha0_Leachman, getAlpha0_Leachman, getAlpha0_Vega, getAlphares_EOSCG, getAlphares_GERG2008, getAlphares_Leachman, getAlphares_Leachman, getAlphares_Vega, getAntoineVaporPressure, getBeta, getComponent, getComponent, getcomponentArray, getComponentNames, getComponents, getComponentWithIndex, getComposition, getCompressibilityX, getCompressibilityY, getCorrectedVolume, getCp, getCp0, getCv, getDensity, getDensity, getDensity_AGA8, getDensity_EOSCG, getDensity_GERG2008, getDensity_Leachman, getDensity_Leachman, getDensity_Vega, getEnthalpy, getEnthalpydP, getEnthalpydT, getEntropy, getEntropydP, getEntropydT, getExcessGibbsEnergy, getExcessGibbsEnergySymetric, getFlowRate, getFugacity, getFugacity, getGamma, getGamma2, getHelmholtzEnergy, getInfiniteDiluteFugacity, getInitType, getInternalEnergy, getIsobaricThermalExpansivity, getIsothermalCompressibility, getJouleThomsonCoefficient, getLogActivityCoefficient, getLogInfiniteDiluteFugacity, getLogInfiniteDiluteFugacity, getLogPureComponentFugacity, getMass, getMeanIonicActivity, getMixGibbsEnergy, getMixingRuleType, getModelName, getMolalMeanIonicActivity, getMolarComposition, getMolarMass, getMolarMass, getMolarVolume, getMoleFraction, getNumberOfComponents, getNumberOfIonicComponents, getNumberOfMolecularComponents, getNumberOfMolesInPhase, getOsmoticCoefficient, getOsmoticCoefficientOfWater, getOsmoticCoefficientOfWaterMolality, getpH, getpH, getPhase, getPhaseFraction, getPhaseTypeName, getPhysicalProperties, getPhysicalPropertyModel, getPressure, getPressure, getProperties_EOSCG, getProperties_GERG2008, getProperties_Leachman, getProperties_Leachman, getProperties_Vega, getPseudoCriticalPressure, getPseudoCriticalTemperature, getPureComponentFugacity, getPureComponentFugacity, getRefPhase, getRefPhase, getSoundSpeed, getTemperature, getTemperature, getThermalConductivity, getThermalConductivity, getTotalVolume, getType, getViscosity, getViscosity, getVolume, getVolume, getWaterDensity, getWtFrac, getWtFrac, getWtFraction, getWtFractionOfWaxFormingComponents, getZ, getZvolcorr, hasComponent, hasComponent, hasPlusFraction, hasTBPFraction, init, init, initPhysicalProperties, initPhysicalProperties, initPhysicalProperties, initRefPhases, isAsphalteneRich, isConstantPhaseVolume, isMixingRuleDefined, normalize, removeComponent, resetPhysicalProperties, setAttractiveTerm, setBeta, setComponentArray, setConstantPhaseVolume, setEmptyFluid, setInitType, setMixingRule, setMolarVolume, setMoleFractions, setNumberOfComponents, setParams, setPhaseTypeName, setPhysicalProperties, setPhysicalProperties, setPhysicalPropertyModel, setPpm, setPressure, setProperties, setRefPhase, setRefPhase, setTemperature, setTotalVolume, setType, useVolumeCorrection, useVolumeCorrection
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Field Details
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serialVersionUID
private static final long serialVersionUIDSerialization version UID.- See Also:
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gergEOS
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xFracGERG
double[] xFracGERG -
IPHASE
int IPHASE -
okVolume
boolean okVolume -
enthalpy
double enthalpy -
entropy
double entropy -
gibbsEnergy
double gibbsEnergy -
CpGERG
double CpGERG -
CvGERG
double CvGERG -
internalEnery
double internalEnery -
JTcoef
double JTcoef
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Constructor Details
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PhaseGERG2004Eos
public PhaseGERG2004Eos()Constructor for PhaseGERG2004Eos.
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Method Details
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clone
clone.
- Specified by:
clonein interfacePhaseInterface- Overrides:
clonein classPhaseEos- Returns:
- a
PhaseInterfaceobject
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addComponent
Add component to component array and update moles variables.
- Parameters:
name- Name of component.moles- Total number of moles of component.molesInPhase- Number of moles in phase.compNumber- Index number of component in phase object component array.
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setxFracGERG
public void setxFracGERG()Setter for the field
xFracGERG. -
init
public void init(double totalNumberOfMoles, int numberOfComponents, int initType, PhaseType pt, double beta) init.
initType used in component.init()
Calls component.init(initType)
- Specified by:
initin interfacePhaseInterface- Overrides:
initin classPhaseEos- Parameters:
totalNumberOfMoles- Total number of moles in all phases of Stream.numberOfComponents- Number of components in system.initType- a int. Use 0 to init, and 1 to reset.pt- Type of phase.beta- Mole fraction of this phase in system.
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getGibbsEnergy
public double getGibbsEnergy()getGibbsEnergy.
- Specified by:
getGibbsEnergyin interfacePhaseInterface- Overrides:
getGibbsEnergyin classPhase- Returns:
- a double
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getJouleThomsonCoefficient
public double getJouleThomsonCoefficient()Get the Joule Thomson Coefficient of a phase.- Specified by:
getJouleThomsonCoefficientin interfacePhaseInterface- Overrides:
getJouleThomsonCoefficientin classPhaseEos- Returns:
- Joule Thomson coefficient in K/bar
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getEnthalpy
public double getEnthalpy()method to return enthalpy of a phase in unit Joule.- Specified by:
getEnthalpyin interfacePhaseInterface- Overrides:
getEnthalpyin classPhase- Returns:
- a double
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getEntropy
public double getEntropy()method to return entropy of the phase.- Specified by:
getEntropyin interfacePhaseInterface- Overrides:
getEntropyin classPhase- Returns:
- a double
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getInternalEnergy
public double getInternalEnergy()getInternalEnergy.
- Specified by:
getInternalEnergyin interfacePhaseInterface- Overrides:
getInternalEnergyin classPhase- Returns:
- a double
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getCp
public double getCp()method to return specific heat capacity (Cp).- Specified by:
getCpin interfacePhaseInterface- Overrides:
getCpin classPhase- Returns:
- Cp in unit J/K
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getCv
public double getCv()method to return specific heat capacity (Cv).- Specified by:
getCvin interfacePhaseInterface- Overrides:
getCvin classPhase- Returns:
- Cv in unit J/K
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molarVolume
public double molarVolume(double pressure, double temperature, double A, double B, PhaseType pt) throws IsNaNException, TooManyIterationsException molarVolume.
- Specified by:
molarVolumein interfacePhaseInterface- Overrides:
molarVolumein classPhaseEos- Parameters:
pressure- a doubletemperature- a doubleA- a doubleB- a doublept- the PhaseType of the phase- Returns:
- a double
- Throws:
IsNaNException- if any.TooManyIterationsException- if any.
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