Class ComponentGEUnifacUMRPRU

java.lang.Object

neqsim.thermo.component.Component

neqsim.thermo.component.ComponentGE

neqsim.thermo.component.ComponentGEUniquac

neqsim.thermo.component.ComponentGEUnifac

neqsim.thermo.component.ComponentGEUnifacUMRPRU

All Implemented Interfaces:

Serializable, Cloneable, ComponentGEInterface, ComponentInterface, ThermodynamicConstantsInterface

public class ComponentGEUnifacUMRPRU
extends ComponentGEUnifac

ComponentGEUnifacUMRPRU class.

Version:

$Id: $Id

Author:

Even Solbraa

See Also:

• Serialized Form

Field Summary

Fields

Modifier and Type	Field	Description
(package private) double[][]	aij
(package private) double[][]	aijdT
(package private) double[][]	aijdTdT
(package private) static org.apache.logging.log4j.Logger	logger	Logger object for class.
(package private) int	numberOfUnifacSubGroups
(package private) double	old2Temperature
(package private) double	oldTemperature
private static final long	serialVersionUID	Serialization version UID.
(package private) double[]	sum2Comp
(package private) double[]	sum2CompdT
(package private) double[]	sum2CompdTdT
(package private) double[]	sum2Mix
(package private) double[]	sum2MixdT
(package private) double[]	sum2MixdTdT
(package private) double[][]	tempExpaij

Fields inherited from class ComponentGEUnifac

lnGammakComp, lnGammakMix, Q, R, unifacGroups, unifacGroupsArray

Fields inherited from class ComponentGEUniquac

q, r

Fields inherited from class ComponentGE

dlngammadn, dlngammadp, dlngammadt, dlngammadtdt, gamma, gammaRefCor, lngamma

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, referencePressure, referenceTemperature, standardStateTemperature, vacumPermittivity

Constructor Summary

Constructors

Constructor	Description
ComponentGEUnifacUMRPRU(String name, double moles, double molesInPhase, int compIndex)	Constructor for ComponentGEUnifacUMRPRU.

Method Summary

Modifier and Type	Method	Description
double	calcaij(PhaseInterface phase, int i, int j)	calcaij.
double	calcaijdT(PhaseInterface phase, int i, int j)	calcaijdT.
double	calcaijdTdT(PhaseInterface phase, int i, int j)	calcaijdTdT.
void	calcGammaNumericalDerivatives(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)	calcGammaNumericalDerivatives.
void	calclnGammak(int k, PhaseInterface phase)	calclnGammak.
void	calclnGammakdn(int k, PhaseInterface phase, int derCompNumb)	calclnGammakdn.
void	calclnGammakdTdT(int k, PhaseInterface phase)	calclnGammakdTdT.
void	calcSum2Comp()	calcSum2Comp.
void	calcSum2CompdTdT(PhaseInterface phase)	calcSum2CompdTdT.
void	calcTempExpaij(PhaseInterface phase)	calcTempExpaij.
void	calcUnifacGroupParams(PhaseInterface phase)	calcUnifacGroupParams.
void	calcUnifacGroupParamsdT(PhaseInterface phase)	calcUnifacGroupParamsdT.
double	getaij(int i, int j)	Getter for the field aij.
double	getaijdT(int i, int j)	Getter for the field aijdT.
double	getaijdTdT(int i, int j)	Getter for the field aijdTdT.
double	getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)	getGamma.

Methods inherited from class ComponentGEUnifac

addUNIFACgroup, fugcoef, fugcoefDiffPres, fugcoefDiffTemp, getNumberOfUNIFACgroups, getQ, getR, getUnifacGroup, getUnifacGroup2, getUnifacGroups, getUnifacGroups2, setQ, setR, setUnifacGroups

Methods inherited from class ComponentGEUniquac

getGamma, getlnGammadn, getlnGammadt, getq, getr

Methods inherited from class ComponentGE

fugcoef, fugcoefDiffPres, fugcoefDiffTemp, getGamma, getGammaRefCor, getlnGamma, getlnGammadtdt, setlnGammadn

Methods inherited from class Component

addMolesChemReac, calcActivity, clone, createComponent, doSolidCheck, equals, Finit, fugcoefDiffPresNumeric, fugcoefDiffTempNumeric, getAcentricFactor, getAntoineASolid, getAntoineBSolid, getAntoineCSolid, getAntoineVaporPressure, getAntoineVaporPressuredT, getAntoineVaporTemperature, getAssociationEnergy, getAssociationEnergySAFT, getAssociationScheme, getAssociationVolume, getAssociationVolumeSAFT, getAttractiveTerm, getAttractiveTermNumber, getCASnumber, getCCsolidVaporPressure, getCCsolidVaporPressuredT, getChemicalPotential, 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, getSurfaceTenisionInfluenceParameter, getSurfTensInfluenceParam, getTC, getTC, getTotalFlowRate, getTriplePointDensity, getTriplePointPressure, getTriplePointTemperature, getTwuCoonParams, getViscosityCorrectionFactor, getViscosityFrictionK, getVoli, getVolumeCorrection, getVolumeCorrectionConst, getVolumeCorrectionT, getVolumeCorrectionT_CPA, getx, getz, hasVolumeCorrection, init, insertComponentIntoDatabase, isHydrateFormer, isHydrocarbon, isInert, isIsHydrateFormer, isIsIon, isIsNormalComponent, isIsPlusFraction, isIsTBPfraction, isWaxFormer, logfugcoefdN, logfugcoefdNi, logfugcoefdP, logfugcoefdT, reducedPressure, reducedTemperature, seta, setAcentricFactor, setAntoineASolid, setAntoineBSolid, setAntoineCSolid, setAssociationEnergy, setAssociationEnergySAFT, setAssociationScheme, setAssociationVolume, setAssociationVolumeSAFT, setAttractiveTerm, setb, 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 ComponentInterface

addMoles, addMolesChemReac, addMolesChemReac, calcActivity, clone, createComponent, doSolidCheck, Finit, 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, getVolumeCorrection, 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, setAttractiveTerm, 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

logger

static org.apache.logging.log4j.Logger logger

Logger object for class.

numberOfUnifacSubGroups

int numberOfUnifacSubGroups

aij

double[][] aij

aijdT

double[][] aijdT

aijdTdT

double[][] aijdTdT

tempExpaij

double[][] tempExpaij

oldTemperature

double oldTemperature

old2Temperature

double old2Temperature

sum2Comp

double[] sum2Comp

sum2Mix

double[] sum2Mix

sum2CompdT

double[] sum2CompdT

sum2CompdTdT

double[] sum2CompdTdT

sum2MixdT

double[] sum2MixdT

sum2MixdTdT

double[] sum2MixdTdT

Constructor Details

ComponentGEUnifacUMRPRU

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

Constructor for ComponentGEUnifacUMRPRU.

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.

Method Details

calcTempExpaij

public void calcTempExpaij(PhaseInterface phase)

calcTempExpaij.

Parameters:

phase - a PhaseInterface object

calcSum2Comp

public void calcSum2Comp()

calcSum2Comp.

calcSum2CompdTdT

public void calcSum2CompdTdT(PhaseInterface phase)

calcSum2CompdTdT.

Parameters:

phase - a PhaseInterface object

calclnGammak

public void calclnGammak(int k,
 PhaseInterface phase)

calclnGammak.

Overrides:

calclnGammak in class ComponentGEUnifac

Parameters:

k - a int

phase - a PhaseInterface object

calclnGammakdn

public void calclnGammakdn(int k,
 PhaseInterface phase,
 int derCompNumb)

calclnGammakdn.

Parameters:

k - a int

phase - a PhaseInterface object

derCompNumb - a int

calclnGammakdTdT

public void calclnGammakdTdT(int k,
 PhaseInterface phase)

calclnGammakdTdT.

Parameters:

k - a int

phase - a PhaseInterface object

getGamma

public double getGamma(PhaseInterface phase,
 int numberOfComponents,
 double temperature,
 double pressure,
 PhaseType pt)

getGamma.

Overrides:

getGamma in class ComponentGEUnifac

Parameters:

phase - a PhaseInterface object

numberOfComponents - a int

temperature - a double

pressure - a double

pt - the PhaseType of the phase

Returns:

a double

calcUnifacGroupParams

public void calcUnifacGroupParams(PhaseInterface phase)

calcUnifacGroupParams.

Parameters:

phase - a PhaseInterface object

calcUnifacGroupParamsdT

public void calcUnifacGroupParamsdT(PhaseInterface phase)

calcUnifacGroupParamsdT.

Parameters:

phase - a PhaseInterface object

calcGammaNumericalDerivatives

public void calcGammaNumericalDerivatives(PhaseInterface phase,
 int numberOfComponents,
 double temperature,
 double pressure,
 PhaseType pt)

calcGammaNumericalDerivatives.

Parameters:

phase - a PhaseInterface object

numberOfComponents - a int

temperature - a double

pressure - a double

pt - the PhaseType of the phase

getaij

public double getaij(int i,
 int j)

Getter for the field aij.

Parameters:

i - a int

j - a int

Returns:

a double

getaijdT

public double getaijdT(int i,
 int j)

Getter for the field aijdT.

Parameters:

i - a int

j - a int

Returns:

a double

getaijdTdT

public double getaijdTdT(int i,
 int j)

Getter for the field aijdTdT.

Parameters:

i - a int

j - a int

Returns:

a double

calcaij

public double calcaij(PhaseInterface phase,
 int i,
 int j)

calcaij.

Parameters:

phase - a PhaseInterface object

i - a int

j - a int

Returns:

a double

calcaijdT

public double calcaijdT(PhaseInterface phase,
 int i,
 int j)

calcaijdT.

Parameters:

phase - a PhaseInterface object

i - a int

j - a int

Returns:

a double

calcaijdTdT

public double calcaijdTdT(PhaseInterface phase,
 int i,
 int j)

calcaijdTdT.

Parameters:

phase - a PhaseInterface object

i - a int

j - a int

Returns:

a double