neqsim.thermo.component.ComponentSpanWagnerEos

All Implemented Interfaces:: Serializable, Cloneable, ComponentEosInterface, ComponentInterface, ThermodynamicConstantsInterface

public class ComponentSpanWagnerEos extends ComponentEos

Component class for the Span-Wagner reference equation for CO2. The model is limited to pure CO2 and therefore many mixture related methods return simplified values.

Author:

esol

See Also:

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

ComponentSpanWagnerEos(int number, double TC, double PC, double M, double a, double moles)

Constructor for ComponentSpanWagnerEos.

ComponentSpanWagnerEos(String name, double moles, double molesInPhase, int compIndex)

Constructor for ComponentSpanWagnerEos.
Method Summary

Modifier and Type

Method

Description

double

alpha(double temperature)

alpha.

double

calca()

calca.

double

calcb()

calcb.

ComponentSpanWagnerEos

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.

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, logfugcoefdN, logfugcoefdNi, logfugcoefdP, logfugcoefdT, 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
- ComponentSpanWagnerEos
  
  public ComponentSpanWagnerEos(String name, double moles, double molesInPhase, int compIndex)
  
  Constructor for ComponentSpanWagnerEos.
  
  Parameters:
  
  name - a String object
  
  moles - a double
  
  molesInPhase - a double
  
  compIndex - a int
- ComponentSpanWagnerEos
  
  public ComponentSpanWagnerEos(int number, double TC, double PC, double M, double a, double moles)
  
  Constructor for ComponentSpanWagnerEos.
  
  Parameters:
  
  number - a int
  
  TC - a double
  
  PC - a double
  
  M - a double
  
  a - a double
  
  moles - a double
Method Details
- clone
  
  public ComponentSpanWagnerEos 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

Class ComponentSpanWagnerEos

Field Summary

Fields inherited from class ComponentEos

Fields inherited from class Component

Fields inherited from interface ThermodynamicConstantsInterface

Constructor Summary

Method Summary

Methods inherited from class ComponentEos

Methods inherited from class Component

Methods inherited from class Object

Methods inherited from interface ComponentInterface

Field Details

serialVersionUID

Constructor Details

ComponentSpanWagnerEos

ComponentSpanWagnerEos

Method Details

clone

getVolumeCorrection

Finit

calca

calcb

alpha

diffaT

diffdiffaT

dFdN

dFdNdN

dFdNdV

dFdNdT

fugcoef