Class ComponentPCSAFT
java.lang.Object
neqsim.thermo.component.Component
neqsim.thermo.component.ComponentEos
neqsim.thermo.component.ComponentSrk
neqsim.thermo.component.ComponentPCSAFT
- All Implemented Interfaces:
Serializable, Cloneable, ComponentEosInterface, ComponentInterface, ThermodynamicConstantsInterface
- Direct Known Subclasses:
ComponentPCSAFTa
ComponentPCSAFT 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) doubleprivate double(package private) doubleprivate doubleprivate doubleprivate doubleprivate doubleprivate doubleprivate doubleprivate doubleprivate doubleprivate static final longSerialization version UID.(package private) int(package private) int(package private) intFields 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, mFields 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, zFields inherited from interface ThermodynamicConstantsInterface
atm, avagadroNumber, boltzmannConstant, electronCharge, faradayConstant, gravity, molarMassAir, normalStateTemperature, pi, planckConstant, R, referencePressure, referenceTemperature, standardStateTemperature, vacumPermittivity -
Constructor Summary
ConstructorsConstructorDescriptionComponentPCSAFT(int number, double TC, double PC, double M, double a, double moles) Constructor for ComponentPCSAFT.ComponentPCSAFT(String name, double moles, double molesInPhase, int compIndex) Constructor for ComponentPCSAFT. -
Method Summary
Modifier and TypeMethodDescriptiondoublecalcdahsSAFTdi(PhaseInterface phase, int nuberOfComponents, double temp, double pres) calcdahsSAFTdi.doublecalcdghsSAFTdi(PhaseInterface phase, int nuberOfComponents, double temp, double pres) calcdghsSAFTdi.doublecalcdmSAFTdi(PhaseInterface phase, int nuberOfComponents, double temp, double pres) calcdmSAFTdi.doublecalcdnSAFTdi(PhaseInterface phase, int nuberOfComponents, double temp, double pres) calcdnSAFTdi.doublecalcF1dispSumTermdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) calcF1dispSumTermdn.doublecalcF2dispSumTermdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) calcF2dispSumTermdn.clone()clone.doubledF_DISP1_SAFTdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) dF_DISP1_SAFTdN.doubledF_DISP2_SAFTdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) dF_DISP2_SAFTdN.doubledF_HC_SAFTdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) dF_HC_SAFTdN.doubledFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) dFdN.doubledFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) dFdNdT.voidFinit(PhaseInterface phase, double temp, double pres, double totMoles, double beta, int numberOfComponents, int initType) Finit.doubleGetter for the fielddahsSAFTdi.doubleGetter for the fielddghsSAFTdi.doubleGetter for the fielddlogghsSAFTdi.doubleGetter for the fielddmSAFTdi.doubleGetter for the fielddnSAFTdi.doubleGetter for the fielddSAFTi.voidinit(double temperature, double pressure, double totalNumberOfMoles, double beta, int initType) Initialize component.voidsetdahsSAFTdi(double dahsSAFTdi) Setter for the fielddahsSAFTdi.voidsetDghsSAFTdi(double dghsSAFTdi) Setter for the fielddghsSAFTdi.voidsetDlogghsSAFTdi(double dlogghsSAFTdi) Setter for the fielddlogghsSAFTdi.voidsetDmSAFTdi(double dmSAFTdi) Setter for the fielddmSAFTdi.voidsetDnSAFTdi(double dnSAFTdi) Setter for the fielddnSAFTdi.voidsetdSAFTi(double di) Setter for the fielddSAFTi.Methods inherited from class ComponentSrk
calca, calcb, getdQpuredT, getdQpuredTdT, getQpure, getSurfaceTenisionInfluenceParameter, getVolumeCorrectionMethods inherited from class ComponentEos
alpha, aT, dFdNdN, dFdNdV, diffalphaT, diffaT, diffdiffalphaT, diffdiffaT, equals, 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, logfugcoefdN, logfugcoefdNi, logfugcoefdP, logfugcoefdT, seta, setAder, setAttractiveParameter, setAttractiveTerm, setb, setBder, setdAdndn, setdAdT, setdAdTdn, setdAdTdT, setdBdndn, setdBdndT, setdBdTdTMethods 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, setzMethods inherited from class Object
finalize, getClass, hashCode, notify, notifyAll, toString, wait, wait, waitMethods 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
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Field Details
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serialVersionUID
private static final long serialVersionUIDSerialization version UID.- See Also:
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dSAFTi
private double dSAFTi -
dmSAFTdi
private double dmSAFTdi -
dghsSAFTdi
double dghsSAFTdi -
dnSAFTdi
double dnSAFTdi -
dahsSAFTdi
double dahsSAFTdi -
dlogghsSAFTdi
double dlogghsSAFTdi -
F1dispVolTermdn
private double F1dispVolTermdn -
F1dispSumTermdn
private double F1dispSumTermdn -
F1dispI1dn
private double F1dispI1dn -
F2dispI2dn
private double F2dispI2dn -
F2dispZHCdn
private double F2dispZHCdn -
F2dispVolTermdn
private double F2dispVolTermdn -
F2dispSumTermdn
private double F2dispSumTermdn -
useHS
int useHS -
useDISP1
int useDISP1 -
useDISP2
int useDISP2
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Constructor Details
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ComponentPCSAFT
Constructor for ComponentPCSAFT.
- 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.
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ComponentPCSAFT
public ComponentPCSAFT(int number, double TC, double PC, double M, double a, double moles) Constructor for ComponentPCSAFT.
- Parameters:
number- a int. Not used.TC- Critical temperature [K]PC- Critical pressure [bara]M- Molar massa- Acentric factormoles- Total number of moles of component.
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Method Details
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clone
clone.
- Specified by:
clonein interfaceComponentInterface- Overrides:
clonein classComponentSrk- Returns:
- a
ComponentInterfaceobject
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init
public void init(double temperature, double pressure, double totalNumberOfMoles, double beta, int initType) Initialize component.
- Specified by:
initin interfaceComponentInterface- Overrides:
initin classComponentEos- Parameters:
temperature- Temperature in unit ?. Used to calculateK.pressure- Pressure in unit ?. Used to calculateK.totalNumberOfMoles- Total number of moles of component.beta- Beta value, i.e.,initType- Init type. CalculateK,z,xif type == 0.
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Finit
public void Finit(PhaseInterface phase, double temp, double pres, double totMoles, double beta, int numberOfComponents, int initType) Finit.
- Specified by:
Finitin interfaceComponentInterface- Overrides:
Finitin classComponentEos- Parameters:
phase- aPhaseInterfaceobjecttemp- a doublepres- a doubletotMoles- a doublebeta- a doublenumberOfComponents- a intinitType- a int
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dFdN
public double dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) dFdN.
- Specified by:
dFdNin interfaceComponentEosInterface- Overrides:
dFdNin classComponentEos- Parameters:
phase- aPhaseInterfaceobjectnumberOfComponents- a inttemperature- a doublepressure- a double- Returns:
- a double
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dF_HC_SAFTdN
public double dF_HC_SAFTdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) dF_HC_SAFTdN.
- Parameters:
phase- aPhaseInterfaceobjectnumberOfComponents- a inttemperature- a doublepressure- a double- Returns:
- a double
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dF_DISP1_SAFTdN
public double dF_DISP1_SAFTdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) dF_DISP1_SAFTdN.
- Parameters:
phase- aPhaseInterfaceobjectnumberOfComponents- a inttemperature- a doublepressure- a double- Returns:
- a double
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calcdmSAFTdi
calcdmSAFTdi.
- Parameters:
phase- aPhaseInterfaceobjectnuberOfComponents- a inttemp- a doublepres- a double- Returns:
- a double
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dF_DISP2_SAFTdN
public double dF_DISP2_SAFTdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) dF_DISP2_SAFTdN.
- Parameters:
phase- aPhaseInterfaceobjectnumberOfComponents- a inttemperature- a doublepressure- a double- Returns:
- a double
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dFdNdT
public double dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) dFdNdT.
- Specified by:
dFdNdTin interfaceComponentEosInterface- Overrides:
dFdNdTin classComponentEos- Parameters:
phase- aPhaseInterfaceobjectnumberOfComponents- a inttemperature- a doublepressure- a double- Returns:
- a double
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calcF1dispSumTermdn
public double calcF1dispSumTermdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) calcF1dispSumTermdn.
- Parameters:
phase- aPhaseInterfaceobjectnumberOfComponents- a inttemperature- a doublepressure- a double- Returns:
- a double
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calcF2dispSumTermdn
public double calcF2dispSumTermdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure) calcF2dispSumTermdn.
- Parameters:
phase- aPhaseInterfaceobjectnumberOfComponents- a inttemperature- a doublepressure- a double- Returns:
- a double
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calcdghsSAFTdi
calcdghsSAFTdi.
- Parameters:
phase- aPhaseInterfaceobjectnuberOfComponents- a inttemp- a doublepres- a double- Returns:
- a double
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calcdahsSAFTdi
calcdahsSAFTdi.
- Parameters:
phase- aPhaseInterfaceobjectnuberOfComponents- a inttemp- a doublepres- a double- Returns:
- a double
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calcdnSAFTdi
calcdnSAFTdi.
- Parameters:
phase- aPhaseInterfaceobjectnuberOfComponents- a inttemp- a doublepres- a double- Returns:
- a double
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getdSAFTi
public double getdSAFTi()Getter for the field
dSAFTi.- Returns:
- a double
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setdSAFTi
public void setdSAFTi(double di) Setter for the field
dSAFTi.- Parameters:
di- a double
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getDghsSAFTdi
public double getDghsSAFTdi()Getter for the field
dghsSAFTdi.- Returns:
- a double
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setDghsSAFTdi
public void setDghsSAFTdi(double dghsSAFTdi) Setter for the field
dghsSAFTdi.- Parameters:
dghsSAFTdi- a double
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getDnSAFTdi
public double getDnSAFTdi()Getter for the field
dnSAFTdi.- Returns:
- a double
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setDnSAFTdi
public void setDnSAFTdi(double dnSAFTdi) Setter for the field
dnSAFTdi.- Parameters:
dnSAFTdi- a double
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getdahsSAFTdi
public double getdahsSAFTdi()Getter for the field
dahsSAFTdi.- Returns:
- a double
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setdahsSAFTdi
public void setdahsSAFTdi(double dahsSAFTdi) Setter for the field
dahsSAFTdi.- Parameters:
dahsSAFTdi- a double
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getDmSAFTdi
public double getDmSAFTdi()Getter for the field
dmSAFTdi.- Returns:
- a double
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setDmSAFTdi
public void setDmSAFTdi(double dmSAFTdi) Setter for the field
dmSAFTdi.- Parameters:
dmSAFTdi- a double
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getDlogghsSAFTdi
public double getDlogghsSAFTdi()Getter for the field
dlogghsSAFTdi.- Returns:
- a double
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setDlogghsSAFTdi
public void setDlogghsSAFTdi(double dlogghsSAFTdi) Setter for the field
dlogghsSAFTdi.- Parameters:
dlogghsSAFTdi- a double
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