Class ComponentPrCPA

java.lang.Object

neqsim.thermo.component.Component

neqsim.thermo.component.ComponentEos

neqsim.thermo.component.ComponentPR

neqsim.thermo.component.ComponentPrCPA

All Implemented Interfaces:

Serializable, Cloneable, ComponentCPAInterface, ComponentEosInterface, ComponentInterface, ThermodynamicConstantsInterface

public abstract class ComponentPrCPA
extends ComponentPR
implements ComponentCPAInterface

Abstract class ComponentPrCPA.

Author:

Even Solbraa

See Also:

• Serialized Form

Field Summary

Fields

Modifier and Type	Field	Description
(package private) int	cpaon
private static final long	serialVersionUID	Serialization version UID.
(package private) double[]	xsite

Fields inherited from class ComponentEos

a, aDern, aDerT, aDerTn, aDerTT, aDiffDiffT, aDiffT, Ai, Aij, AiT, alpha, aT, b, bDern, bDerTn, Bi, Bij, dAdndn, dBdndn, delta1, delta2, logger, m

Fields inherited from class Component

acentricFactor, aCPA, AntoineA, AntoineASolid, AntoineB, AntoineBSolid, AntoineC, AntoineCSolid, AntoineD, AntoineE, antoineLiqVapPresType, associationEnergy, associationScheme, associationVolume, attractiveTermNumber, bCPA, calcActivity, componentName, componentNumber, criticalPressure, criticalTemperature, criticalViscosity, criticalVolume, debyeDipoleMoment, dfugdn, dfugdp, dfugdt, dfugdx, dielectricParameter, dqPuredT, dqPuredTdT, elements, epsikSAFT, fugacityCoefficient, gibbsEnergyOfFormation, heatOfVaporizationCoefs, henryCoefParameter, Hsub, idealGasAbsoluteEntropy, idealGasGibbsEnergyOfFormation, index, ionicCharge, isIon, isNormalComponent, isPlusFraction, isTBPfraction, K, lennardJonesEnergyParameter, lennardJonesMolecularDiameter, liquidConductivityParameter, liquidDensityCoefs, liquidViscosityModel, liquidViscosityParameter, matiascopemanParams, matiascopemanParamsPR, matiascopemanParamsUMRPRU, matiascopemanSolidParams, mCPA, meltingPointTemperature, molarMass, mSAFTi, normalBoilingPoint, normalLiquidDensity, numberOfAssociationSites, numberOfMoles, numberOfMolesInPhase, parachorParameter, paulingAnionicDiameter, qPure, racketZ, referencePotential, referenceStateType, schwartzentruberParams, sigmaSAFTi, solidCheck, solidDensityCoefs, sphericalCoreRadius, srkacentricFactor, standardDensity, stokesCationicDiameter, surfTensInfluenceParam, triplePointDensity, triplePointPressure, TwuCoonParams, viscosityCorrectionFactor, viscosityFrictionK, voli, x, z

Fields inherited from interface ThermodynamicConstantsInterface

atm, avagadroNumber, boltzmannConstant, electronCharge, faradayConstant, gravity, molarMassAir, normalStateTemperature, pi, planckConstant, R, referencePressure, referenceTemperature, standardStateTemperature, vacumPermittivity

Constructor Summary

Constructors

Constructor	Description
ComponentPrCPA(int number, double TC, double PC, double M, double a, double moles)	Constructor for ComponentPrCPA.
ComponentPrCPA(String name, double moles, double molesInPhase, int compIndex)	Constructor for ComponentPrCPA.

Method Summary

Modifier and Type	Method	Description
double	calc_lngi(PhaseInterface phase)	calc_lngi.
double	calc_lngi2(PhaseInterface phase)	calc_lngi2.
double	calca()	calca.
double	calcb()	calcb.
ComponentPrCPA	clone()	clone.
double	dFCPAdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)	dFCPAdN.
double	dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)	dFdN.
double	dFdNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)	dFdNdN.
double	dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)	dFdNdT.
double	dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)	dFdNdV.
double	getVolumeCorrection()	getVolumeCorrection.
double[]	getXsite()	getXsite.
void	setAttractiveTerm(int i)	setAttractiveTerm.
void	setXsite(double[] xsite)	Setter for property xsite.
void	setXsite(int i, double xsite)	setXsite.

Methods inherited from class ComponentPR

getdQpuredT, getdQpuredTdT, getQpure, getSurfaceTenisionInfluenceParameter

Methods inherited from class ComponentEos

alpha, aT, diffalphaT, diffaT, diffdiffalphaT, diffdiffaT, equals, Finit, fugcoef, geta, getAder, getaDiffDiffT, getaDiffT, getAi, getAij, getAiT, getAresnTV, getaT, getAttractiveParameter, getAttractiveTerm, getb, getBder, getBi, getBij, getChemicalPotential, getdAdndn, getdAdT, getdAdTdn, getdAdTdT, getdBdndn, getdBdndT, getdBdT, getDeltaEosParameters, getdUdndnSV, getdUdnSV, getdUdSdnV, getdUdVdnS, init, logfugcoefdN, logfugcoefdNi, logfugcoefdP, logfugcoefdT, seta, setAder, setAttractiveParameter, setb, setBder, setdAdndn, setdAdT, setdAdTdn, setdAdTdT, setdBdndn, setdBdndT, setdBdTdT

Methods inherited from class Component

addMolesChemReac, calcActivity, createComponent, doSolidCheck, fugcoefDiffPresNumeric, fugcoefDiffTempNumeric, getAcentricFactor, getAntoineASolid, getAntoineBSolid, getAntoineCSolid, getAntoineVaporPressure, getAntoineVaporPressuredT, getAntoineVaporTemperature, getAssociationEnergy, getAssociationEnergySAFT, getAssociationScheme, getAssociationVolume, getAssociationVolumeSAFT, getAttractiveTermNumber, getCASnumber, getCCsolidVaporPressure, getCCsolidVaporPressuredT, getChemicalPotential, getChemicalPotentialdN, getChemicalPotentialdNTV, getChemicalPotentialdP, getChemicalPotentialdP, getChemicalPotentialdT, getChemicalPotentialdV, getChemicalPotentialIdealReference, getComponentName, getComponentNumber, getComponentType, getCp0, getCpA, getCpB, getCpC, getCpD, getCpE, getCriticalCompressibilityFactor, getCriticalViscosity, getCriticalVolume, getCv0, getDebyeDipoleMoment, getdfugdn, getdfugdp, getdfugdt, getdfugdx, getDiElectricConstant, getDiElectricConstantdT, getDiElectricConstantdTdT, getdrhodN, getElements, getEnthalpy, getEntropy, getEpsikSAFT, getFlowRate, getFormulae, getFugacityCoefficient, getFugacitydN, getGibbsEnergy, getGibbsEnergyOfFormation, getGresTP, getHeatOfFusion, getHeatOfVapourization, getHenryCoef, getHenryCoefdT, getHenryCoefParameter, getHID, getHresTP, getHsub, getIdealGasAbsoluteEntropy, getIdealGasEnthalpyOfFormation, getIdealGasGibbsEnergyOfFormation, getIdEntropy, getIndex, getIonicCharge, getIonicDiameter, getK, getLennardJonesEnergyParameter, getLennardJonesMolecularDiameter, getLiquidConductivityParameter, getLiquidViscosityModel, getLiquidViscosityParameter, getMatiascopemanParams, getMatiascopemanParams, getMatiascopemanParamsPR, getMatiascopemanParamsUMRPRU, getMatiascopemanSolidParams, getMeltingPointTemperature, getMolality, getMolarity, getMolarMass, getMolarMass, getmSAFTi, getName, getNormalBoilingPoint, getNormalBoilingPoint, getNormalLiquidDensity, getNormalLiquidDensity, getNumberOfAssociationSites, getNumberOfmoles, getNumberOfMolesInPhase, getOrginalNumberOfAssociationSites, getParachorParameter, getPaulingAnionicDiameter, getPC, getPC, getPureComponentCpLiquid, getPureComponentCpSolid, getPureComponentHeatOfVaporization, getPureComponentLiquidDensity, getPureComponentSolidDensity, getRacketZ, getRacketZCPA, getRate, getReferenceEnthalpy, getReferencePotential, getReferenceStateType, getSchwartzentruberParams, getSigmaSAFTi, getSolidVaporPressure, getSolidVaporPressuredT, getSphericalCoreRadius, getSresTP, getStandardDensity, getStokesCationicDiameter, getSurfTensInfluenceParam, getTC, getTC, getTotalFlowRate, getTriplePointDensity, getTriplePointPressure, getTriplePointTemperature, getTwuCoonParams, getViscosityCorrectionFactor, getViscosityFrictionK, getVoli, getVolumeCorrectionConst, getVolumeCorrectionT, getVolumeCorrectionT_CPA, getx, getz, hasVolumeCorrection, insertComponentIntoDatabase, isHydrateFormer, isHydrocarbon, isInert, isIsHydrateFormer, isIsIon, isIsNormalComponent, isIsPlusFraction, isIsTBPfraction, isWaxFormer, reducedPressure, reducedTemperature, setAcentricFactor, setAntoineASolid, setAntoineBSolid, setAntoineCSolid, setAssociationEnergy, setAssociationEnergySAFT, setAssociationScheme, setAssociationVolume, setAssociationVolumeSAFT, setCASnumber, setComponentName, setComponentNumber, setComponentType, setCpA, setCpB, setCpC, setCpD, setCpE, setCriticalCompressibilityFactor, setCriticalViscosity, setCriticalVolume, setdfugdn, setdfugdp, setdfugdt, setdfugdx, setEpsikSAFT, setFormulae, setFugacityCoefficient, setHeatOfFusion, setHenryCoefParameter, setIdealGasEnthalpyOfFormation, setIsAllTypesFalse, setIsHydrateFormer, setIsIon, setIsNormalComponent, setIsPlusFraction, setIsTBPfraction, setK, setLennardJonesEnergyParameter, setLennardJonesMolecularDiameter, setLiquidConductivityParameter, setLiquidViscosityModel, setLiquidViscosityParameter, setMatiascopemanParams, setMatiascopemanParams, setMatiascopemanParamsPR, setMatiascopemanSolidParams, setMolarMass, setMolarMass, setmSAFTi, setNormalBoilingPoint, setNormalLiquidDensity, setNumberOfAssociationSites, setNumberOfmoles, setNumberOfMolesInPhase, setParachorParameter, setPaulingAnionicDiameter, setPC, setPC, setProperties, setRacketZ, setRacketZCPA, setReferenceEnthalpy, setReferencePotential, setSchwartzentruberParams, setSigmaSAFTi, setSolidCheck, setSphericalCoreRadius, setStandardDensity, setStokesCationicDiameter, setSurfTensInfluenceParam, setTC, setTC, setTriplePointTemperature, setTwuCoonParams, setViscosityAssociationFactor, setViscosityFrictionK, setVoli, setVolumeCorrection, setVolumeCorrectionConst, setVolumeCorrectionT, setVolumeCorrectionT_CPA, setWaxFormer, setx, setz

Methods inherited from class Object

finalize, getClass, hashCode, notify, notifyAll, toString, wait, wait, wait

Methods inherited from interface ComponentCPAInterface

dFCPAdNdXi, dFCPAdVdXi, dFCPAdXi, dFCPAdXidXj, getXsitedT, getXsitedTdT, getXsitedV, getXsiteOld, setXsitedni, setXsitedT, setXsitedTdT, setXsitedV, setXsiteOld

Methods inherited from interface ComponentEosInterface

aT, diffaT, diffdiffaT, geta, getAder, getaDiffDiffT, getaDiffT, getAi, getAij, getAiT, getaT, getb, getBder, getBi, getBij, getdAdndn, getdAdT, getdAdTdn, getdBdndn, getdBdndT, getdBdT, getDeltaEosParameters, setAder, setBder, setdAdndn, setdAdT, setdAdTdn, setdAdTdT, setdBdndn, setdBdndT, setdBdTdT

Methods inherited from interface ComponentInterface

addMoles, addMolesChemReac, addMolesChemReac, calcActivity, createComponent, doSolidCheck, Finit, fugcoef, fugcoefDiffPresNumeric, fugcoefDiffTempNumeric, getAcentricFactor, getAntoineASolid, getAntoineBSolid, getAntoineCSolid, getAntoineVaporPressure, getAntoineVaporPressuredT, getAntoineVaporTemperature, getAssociationEnergy, getAssociationEnergySAFT, getAssociationScheme, getAssociationVolume, getAssociationVolumeSAFT, getAttractiveTerm, getAttractiveTermNumber, getCASnumber, getCCsolidVaporPressure, getCCsolidVaporPressuredT, getChemicalPotential, getChemicalPotential, getChemicalPotentialdN, getChemicalPotentialdNTV, getChemicalPotentialdP, getChemicalPotentialdT, getChemicalPotentialdV, getChemicalPotentialIdealReference, getComponentName, getComponentNumber, getComponentType, getCp0, getCpA, getCpB, getCpC, getCpD, getCpE, getCriticalCompressibilityFactor, getCriticalViscosity, getCriticalVolume, getCv0, getDebyeDipoleMoment, getdfugdn, getdfugdp, getdfugdt, getdfugdx, getDiElectricConstant, getDiElectricConstantdT, getDiElectricConstantdTdT, getdrhodN, getElements, getEnthalpy, getEntropy, getEpsikSAFT, getFlowRate, getFormulae, getFugacityCoefficient, getGibbsEnergy, getGibbsEnergyOfFormation, getGresTP, getHeatOfFusion, getHeatOfVapourization, getHenryCoef, getHenryCoefdT, getHenryCoefParameter, getHID, getHresTP, getHsub, getIdealGasAbsoluteEntropy, getIdealGasEnthalpyOfFormation, getIdealGasGibbsEnergyOfFormation, getIdEntropy, getIndex, getIonicCharge, getK, getLennardJonesEnergyParameter, getLennardJonesMolecularDiameter, getLiquidConductivityParameter, getLiquidViscosityModel, getLiquidViscosityParameter, getLogFugacityCoefficient, getMatiascopemanParams, getMatiascopemanSolidParams, getMeltingPointTemperature, getMolality, getMolarity, getMolarMass, getMolarMass, getmSAFTi, getName, getNormalBoilingPoint, getNormalBoilingPoint, getNormalLiquidDensity, getNormalLiquidDensity, getNumberOfAssociationSites, getNumberOfmoles, getNumberOfMolesInPhase, getOrginalNumberOfAssociationSites, getParachorParameter, getPaulingAnionicDiameter, getPC, getPC, getPureComponentCpLiquid, getPureComponentCpSolid, getPureComponentHeatOfVaporization, getPureComponentLiquidDensity, getPureComponentSolidDensity, getRacketZ, getRacketZCPA, getRate, getReferencePotential, getReferenceStateType, getSchwartzentruberParams, getSigmaSAFTi, getSolidVaporPressure, getSolidVaporPressuredT, getSphericalCoreRadius, getSresTP, getStokesCationicDiameter, getSurfaceTenisionInfluenceParameter, getSurfTensInfluenceParam, getTC, getTC, getTotalFlowRate, getTriplePointDensity, getTriplePointPressure, getTriplePointTemperature, getTwuCoonParams, getViscosityCorrectionFactor, getViscosityFrictionK, getVoli, getVolumeCorrectionConst, getVolumeCorrectionT, getVolumeCorrectionT_CPA, getx, getz, init, insertComponentIntoDatabase, isHydrateFormer, isHydrocarbon, isInert, isIsIon, isIsNormalComponent, isIsPlusFraction, isIsTBPfraction, isWaxFormer, logfugcoefdN, logfugcoefdNi, logfugcoefdP, logfugcoefdT, reducedPressure, reducedTemperature, seta, setAcentricFactor, setAntoineASolid, setAntoineBSolid, setAntoineCSolid, setAssociationEnergy, setAssociationEnergySAFT, setAssociationScheme, setAssociationVolume, setAssociationVolumeSAFT, setb, setCASnumber, setComponentName, setComponentNumber, setComponentType, setCpA, setCpB, setCpC, setCpD, setCpE, setCriticalCompressibilityFactor, setCriticalViscosity, setCriticalVolume, setdfugdn, setdfugdp, setdfugdt, setdfugdx, setEpsikSAFT, setFormulae, setFugacityCoefficient, setHeatOfFusion, setHenryCoefParameter, setIdealGasEnthalpyOfFormation, setIsHydrateFormer, setIsIon, setIsNormalComponent, setIsPlusFraction, setIsTBPfraction, setK, setLennardJonesEnergyParameter, setLennardJonesMolecularDiameter, setLiquidConductivityParameter, setLiquidViscosityModel, setLiquidViscosityParameter, setMatiascopemanParams, setMatiascopemanParams, setMolarMass, setMolarMass, setmSAFTi, setNormalBoilingPoint, setNormalLiquidDensity, setNumberOfAssociationSites, setNumberOfmoles, setNumberOfMolesInPhase, setParachorParameter, setPC, setPC, setProperties, setRacketZ, setRacketZCPA, setReferencePotential, setSchwartzentruberParams, setSigmaSAFTi, setSolidCheck, setSphericalCoreRadius, setStokesCationicDiameter, setSurfTensInfluenceParam, setTC, setTC, setTriplePointTemperature, setTwuCoonParams, setViscosityAssociationFactor, setViscosityFrictionK, setVolumeCorrection, setVolumeCorrectionConst, setVolumeCorrectionT, setVolumeCorrectionT_CPA, setWaxFormer, setx, setz

Field Details

serialVersionUID

private static final long serialVersionUID

Serialization version UID.

See Also:

• Constant Field Values

cpaon

int cpaon

xsite

double[] xsite

Constructor Details

ComponentPrCPA

public ComponentPrCPA(String name,
 double moles,
 double molesInPhase,
 int compIndex)

Constructor for ComponentPrCPA.

Parameters:

name - Name of component.

moles - Total number of moles of component.

molesInPhase - Number of moles in phase.

compIndex - Index number of component in phase object component array.

ComponentPrCPA

public ComponentPrCPA(int number,
 double TC,
 double PC,
 double M,
 double a,
 double moles)

Constructor for ComponentPrCPA.

Parameters:

number - a int. Not used.

TC - Critical temperature [K]

PC - Critical pressure [bara]

M - Molar mass

a - Acentric factor

moles - Total number of moles of component.

Method Details

getVolumeCorrection

public double getVolumeCorrection()

getVolumeCorrection.

Specified by:

getVolumeCorrection in interface ComponentInterface

Overrides:

getVolumeCorrection in class ComponentPR

Returns:

a double

clone

public ComponentPrCPA clone()

clone.

Specified by:

clone in interface ComponentInterface

Overrides:

clone in class ComponentPR

Returns:

a ComponentInterface object

calca

public double calca()

calca.

Specified by:

calca in interface ComponentEosInterface

Overrides:

calca in class ComponentPR

Returns:

a double

calcb

public double calcb()

calcb.

Specified by:

calcb in interface ComponentEosInterface

Overrides:

calcb in class ComponentPR

Returns:

a double

setAttractiveTerm

public void setAttractiveTerm(int i)

setAttractiveTerm.

Specified by:

setAttractiveTerm in interface ComponentInterface

Overrides:

setAttractiveTerm in class ComponentEos

Parameters:

i - a int

dFdN

public double dFdN(PhaseInterface phase,
 int numberOfComponents,
 double temperature,
 double pressure)

dFdN.

Specified by:

dFdN in interface ComponentEosInterface

Overrides:

dFdN in class ComponentEos

Parameters:

phase - a PhaseInterface object

numberOfComponents - a int

temperature - a double

pressure - a double

Returns:

a double

dFdNdT

public double dFdNdT(PhaseInterface phase,
 int numberOfComponents,
 double temperature,
 double pressure)

dFdNdT.

Specified by:

dFdNdT in interface ComponentEosInterface

Overrides:

dFdNdT in class ComponentEos

Parameters:

phase - a PhaseInterface object

numberOfComponents - a int

temperature - a double

pressure - a double

Returns:

a double

dFdNdV

public double dFdNdV(PhaseInterface phase,
 int numberOfComponents,
 double temperature,
 double pressure)

dFdNdV.

Specified by:

dFdNdV in interface ComponentEosInterface

Overrides:

dFdNdV in class ComponentEos

Parameters:

phase - a PhaseInterface object

numberOfComponents - a int

temperature - a double

pressure - a double

Returns:

a double

dFdNdN

public double dFdNdN(int j,
 PhaseInterface phase,
 int numberOfComponents,
 double temperature,
 double pressure)

dFdNdN.

Specified by:

dFdNdN in interface ComponentEosInterface

Overrides:

dFdNdN in class ComponentEos

Parameters:

j - a int

phase - a PhaseInterface object

numberOfComponents - a int

temperature - a double

pressure - a double

Returns:

a double

dFCPAdN

public double dFCPAdN(PhaseInterface phase,
 int numberOfComponents,
 double temperature,
 double pressure)

dFCPAdN.

Parameters:

phase - a PhaseInterface object

numberOfComponents - a int

temperature - a double

pressure - a double

Returns:

a double

calc_lngi

public double calc_lngi(PhaseInterface phase)

calc_lngi.

Parameters:

phase - a PhaseInterface object

Returns:

a double

calc_lngi2

public double calc_lngi2(PhaseInterface phase)

calc_lngi2.

Parameters:

phase - a PhaseInterface object

Returns:

a double

getXsite

public double[] getXsite()

getXsite.

Specified by:

getXsite in interface ComponentCPAInterface

Returns:

an array of type double

setXsite

public void setXsite(double[] xsite)

Setter for property xsite.

Parameters:

xsite - New value of property xsite.

setXsite

public void setXsite(int i,
 double xsite)

setXsite.

Specified by:

setXsite in interface ComponentCPAInterface

Parameters:

i - a int

xsite - a double