Class ComponentAmmoniaEos

java.lang.Object

neqsim.thermo.component.Component

neqsim.thermo.component.ComponentEos

neqsim.thermo.component.ComponentAmmoniaEos

All Implemented Interfaces:

Serializable, Cloneable, ComponentEosInterface, ComponentInterface, ThermodynamicConstantsInterface

public class ComponentAmmoniaEos
extends ComponentEos

Component implementation for the ammonia reference equation of state. The formulation mirrors the style of the Leachman hydrogen model where chemical potential derivatives are expressed through reduced Helmholtz-energy derivatives returned from PhaseAmmoniaEos.

Author:

esol

See Also:

• Serialized Form

Field Summary

Fields

Modifier and Type	Field	Description
private static final long	serialVersionUID

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

Method Summary

Modifier and Type	Method	Description
double	alpha(double temperature)	alpha.
double	calca()	calca.
double	calcb()	calcb.
ComponentAmmoniaEos	clone()	clone.
double	dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)	dFdN.
double	dFdNdN(int i, 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	diffaT(double temperature)	diffaT.
double	diffdiffaT(double temperature)	diffdiffaT.
void	Finit(PhaseInterface phase, double T, double p, double totalNumberOfMoles, double beta, int numberOfComponents, int initType)	Finit.
double	fugcoef(PhaseInterface phase)	Calculate, set and return fugacity coefficient.
double	getVolumeCorrection()	getVolumeCorrection.
double[]	logfugcoefdN(PhaseInterface phase)	logfugcoefdN.
double	logfugcoefdP(PhaseInterface phase)	logfugcoefdP.
double	logfugcoefdT(PhaseInterface phase)	logfugcoefdT.

Methods inherited from class ComponentEos

aT, diffalphaT, diffdiffalphaT, equals, 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, getSurfaceTenisionInfluenceParameter, init, logfugcoefdNi, seta, setAder, setAttractiveParameter, setAttractiveTerm, 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 ComponentInterface

addMoles, addMolesChemReac, 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, 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, getSurfTensInfluenceParam, getTC, getTC, getTotalFlowRate, getTriplePointDensity, getTriplePointPressure, getTriplePointTemperature, getTwuCoonParams, getViscosityCorrectionFactor, getViscosityFrictionK, getVoli, getVolumeCorrectionConst, getVolumeCorrectionT, getVolumeCorrectionT_CPA, getx, getz, insertComponentIntoDatabase, isHydrateFormer, isHydrocarbon, isInert, 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, 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

See Also:

• Constant Field Values

Constructor Details

ComponentAmmoniaEos

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

Constructor for ComponentAmmoniaEos.

Parameters:

name - a String object

moles - a double

molesInPhase - a double

compIndex - a int

ComponentAmmoniaEos

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

Constructor for ComponentAmmoniaEos.

Parameters:

number - a int

TC - a double

PC - a double

M - a double

a - a double

moles - a double

Method Details

clone

public ComponentAmmoniaEos clone()

clone.

Specified by:

clone in interface ComponentInterface

Overrides:

clone in class ComponentEos

Returns:

a ComponentInterface object

getVolumeCorrection

public double getVolumeCorrection()

getVolumeCorrection.

Specified by:

getVolumeCorrection in interface ComponentInterface

Overrides:

getVolumeCorrection in class Component

Returns:

a double

Finit

public void Finit(PhaseInterface phase,
 double T,
 double p,
 double totalNumberOfMoles,
 double beta,
 int numberOfComponents,
 int initType)

Finit.

Specified by:

Finit in interface ComponentInterface

Overrides:

Finit in class ComponentEos

Parameters:

phase - a PhaseInterface object

T - a double

p - a double

totalNumberOfMoles - a double

beta - a double

numberOfComponents - a int

initType - a int

calca

public double calca()

calca.

Specified by:

calca in interface ComponentEosInterface

Specified by:

calca in class ComponentEos

Returns:

a double

calcb

public double calcb()

calcb.

Specified by:

calcb in interface ComponentEosInterface

Specified by:

calcb in class ComponentEos

Returns:

a double

alpha

public double alpha(double temperature)

alpha.

Overrides:

alpha in class ComponentEos

Parameters:

temperature - a double

Returns:

a double

diffaT

public double diffaT(double temperature)

diffaT.

Specified by:

diffaT in interface ComponentEosInterface

Overrides:

diffaT in class ComponentEos

Parameters:

temperature - a double

Returns:

a double

diffdiffaT

public double diffdiffaT(double temperature)

diffdiffaT.

Specified by:

diffdiffaT in interface ComponentEosInterface

Overrides:

diffdiffaT in class ComponentEos

Parameters:

temperature - a double

Returns:

a double

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

dFdNdN

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

dFdNdN.

Specified by:

dFdNdN in interface ComponentEosInterface

Overrides:

dFdNdN in class ComponentEos

Parameters:

i - a int

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

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

fugcoef

public double fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

Specified by:

fugcoef in interface ComponentInterface

Overrides:

fugcoef in class ComponentEos

Parameters:

phase - a PhaseInterface object to get fugacity coefficient of.

Returns:

Fugacity coefficient

logfugcoefdP

public double logfugcoefdP(PhaseInterface phase)

logfugcoefdP.

Specified by:

logfugcoefdP in interface ComponentInterface

Overrides:

logfugcoefdP in class ComponentEos

Parameters:

phase - a PhaseInterface object

Returns:

a double

logfugcoefdT

public double logfugcoefdT(PhaseInterface phase)

logfugcoefdT.

Specified by:

logfugcoefdT in interface ComponentInterface

Overrides:

logfugcoefdT in class ComponentEos

Parameters:

phase - a PhaseInterface object

Returns:

a double

logfugcoefdN

public double[] logfugcoefdN(PhaseInterface phase)

logfugcoefdN.

Specified by:

logfugcoefdN in interface ComponentInterface

Overrides:

logfugcoefdN in class ComponentEos

Parameters:

phase - a PhaseInterface object

Returns:

an array of type double