Uses of Interface neqsim.thermo.phase.PhaseInterface (NeqSim 3.2.1 API)

Uses of PhaseInterface in neqsim.blackoil

Methods in neqsim.blackoil that return PhaseInterface

Modifier and Type

Method

Description

private static PhaseInterface

BlackOilConverter.findGasPhase(SystemInterface s)

private static PhaseInterface

BlackOilConverter.findOilPhase(SystemInterface s)

private static PhaseInterface

BlackOilConverter.findWaterPhase(SystemInterface s)

Methods in neqsim.blackoil with parameters of type PhaseInterface

Modifier and Type

Method

Description

private static double

BlackOilConverter.hydrocarbonFraction(PhaseInterface p)

private static boolean

BlackOilConverter.isMostlyWater(PhaseInterface p)

private static SystemInterface

BlackOilConverter.phaseAsStandaloneSystem(SystemInterface base, PhaseInterface phase, double T, double P)

private static double

BlackOilConverter.phaseVolume(PhaseInterface p)

private static String

BlackOilConverter.safeTypeName(PhaseInterface p)
Uses of PhaseInterface in neqsim.chemicalreactions

Methods in neqsim.chemicalreactions with parameters of type PhaseInterface

Modifier and Type

Method

Description

double

ChemicalReactionOperations.solveKinetics(int phaseNum, PhaseInterface interPhase, int component)

solveKinetics.
Uses of PhaseInterface in neqsim.chemicalreactions.chemicalreaction

Methods in neqsim.chemicalreactions.chemicalreaction with parameters of type PhaseInterface

Modifier and Type

Method

Description

void

ChemicalReactionList.calcReacMatrix(PhaseInterface phase)

calcReacMatrix.

Jama.Matrix

ChemicalReactionList.calcReacRates(PhaseInterface phase, ComponentInterface[] components)

calcReacRates.

void

ChemicalReactionList.checkReactions(PhaseInterface phase)

checkReactions.

double[][]

ChemicalReactionList.createReactionMatrix(PhaseInterface phase, ComponentInterface[] components)

createReactionMatrix.

double

ChemicalReaction.getK(PhaseInterface phase)

getK.

double

ChemicalReaction.getRateFactor(PhaseInterface phase)

Getter for the field rateFactor.

double

ChemicalReaction.getReactionHeat(PhaseInterface phase)

Getter for property reactionHeat.

void

ChemicalReaction.init(PhaseInterface phase)

init.

void

ChemicalReaction.initMoleNumbers(PhaseInterface phase, ComponentInterface[] components, double[][] Amatrix, double[] chemRefPot)

Generaters initial estimates for the molenumbers.

void

ChemicalReactionList.initMoleNumbers(PhaseInterface phase, ComponentInterface[] components, double[][] Amatrix, double[] chemRefPot)

initMoleNumbers.

double

ChemicalReactionList.reacHeat(PhaseInterface phase, String comp)

reacHeat.

double[]

ChemicalReactionList.updateReferencePotentials(PhaseInterface phase, ComponentInterface[] components)

updateReferencePotentials.
Uses of PhaseInterface in neqsim.chemicalreactions.kinetics

Methods in neqsim.chemicalreactions.kinetics with parameters of type PhaseInterface

Modifier and Type

Method

Description

double

Kinetics.calcReacMatrix(PhaseInterface phase, PhaseInterface interPhase, int comp)

calcReacMatrix.

double

Kinetics.getPseudoFirstOrderCoef(PhaseInterface phase, PhaseInterface interPhase, int comp)

getPseudoFirstOrderCoef.
Uses of PhaseInterface in neqsim.mathlib.nonlinearsolver

Methods in neqsim.mathlib.nonlinearsolver with parameters of type PhaseInterface

Modifier and Type

Method

Description

static double

NumericalDerivative.fugcoefDiffPres(ComponentInterface component, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

fugcoefDiffPres.

static double

NumericalDerivative.fugcoefDiffTemp(ComponentInterface component, PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

fugcoefDiffTemp.
Uses of PhaseInterface in neqsim.physicalproperties

Methods in neqsim.physicalproperties with parameters of type PhaseInterface

Modifier and Type

Method

Description

PhysicalProperties

PhysicalPropertyHandler.getPhysicalProperties(PhaseInterface phase)

Get PhysicalProperties for a specific phase type.

void

PhysicalPropertyHandler.setPhysicalProperties(PhaseInterface phase, PhysicalPropertyModel ppm)

setPhysicalProperties.
Uses of PhaseInterface in neqsim.physicalproperties.methods.liquidphysicalproperties.diffusivity

Methods in neqsim.physicalproperties.methods.liquidphysicalproperties.diffusivity with parameters of type PhaseInterface

Modifier and Type

Method

Description

static String

DiffusivityModelSelector.getModelSelectionReason(PhaseInterface phase)

Get a description of why a particular model was selected.

private static boolean

DiffusivityModelSelector.hasAmineComponents(PhaseInterface phase)

Check if the phase contains amine components.

private static boolean

DiffusivityModelSelector.hasComponent(PhaseInterface phase, String componentName)

Check if the phase contains a specific component.

private static boolean

DiffusivityModelSelector.isAqueousPhase(PhaseInterface phase)

Check if the phase is predominantly aqueous.

static DiffusivityModelSelector.DiffusivityModelType

DiffusivityModelSelector.selectOptimalModel(PhaseInterface phase)

Select the optimal diffusivity model based on phase composition and conditions.
Uses of PhaseInterface in neqsim.physicalproperties.mixingrule

Methods in neqsim.physicalproperties.mixingrule with parameters of type PhaseInterface

Modifier and Type

Method

Description

void

PhysicalPropertyMixingRule.initMixingRules(PhaseInterface phase)

initMixingRules.

void

PhysicalPropertyMixingRuleInterface.initMixingRules(PhaseInterface phase)

initMixingRules.
Uses of PhaseInterface in neqsim.physicalproperties.system

Fields in neqsim.physicalproperties.system declared as PhaseInterface

Modifier and Type

Field

Description

protected PhaseInterface

PhysicalProperties.phase

Methods in neqsim.physicalproperties.system that return PhaseInterface

Modifier and Type

Method

Description

PhaseInterface

PhysicalProperties.getPhase()

Getter for property phase.

Methods in neqsim.physicalproperties.system with parameters of type PhaseInterface

Modifier and Type

Method

Description

void

PhysicalProperties.init(PhaseInterface phase)

Initialize / calculate all physical properties of phase.

void

PhysicalProperties.init(PhaseInterface phase, String name)

Initialize / calculate a specific physical property of phase.

void

PhysicalProperties.init(PhaseInterface phase, PhysicalPropertyType ppt)

Initialize / calculate a specific physical property of phase.

void

PhysicalProperties.setPhase(PhaseInterface phase)

Setter for property phase.

Constructors in neqsim.physicalproperties.system with parameters of type PhaseInterface

Modifier

Constructor

Description

PhysicalProperties(PhaseInterface phase)

Constructor for PhysicalProperties.

PhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for PhysicalProperties.
Uses of PhaseInterface in neqsim.physicalproperties.system.commonphasephysicalproperties

Constructors in neqsim.physicalproperties.system.commonphasephysicalproperties with parameters of type PhaseInterface

Modifier

Constructor

Description

DefaultPhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for DefaultPhysicalProperties.
Uses of PhaseInterface in neqsim.physicalproperties.system.gasphysicalproperties

Constructors in neqsim.physicalproperties.system.gasphysicalproperties with parameters of type PhaseInterface

Modifier

Constructor

Description

AirPhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for AirPhysicalProperties.

GasPhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for GasPhysicalProperties.

NaturalGasPhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for NaturalGasPhysicalProperties.
Uses of PhaseInterface in neqsim.physicalproperties.system.liquidphysicalproperties

Constructors in neqsim.physicalproperties.system.liquidphysicalproperties with parameters of type PhaseInterface

Modifier

Constructor

Description

AminePhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for AminePhysicalProperties.

CO2waterPhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for CO2waterPhysicalProperties.

GlycolPhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for GlycolPhysicalProperties.

LiquidPhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for LiquidPhysicalProperties.

SaltWaterPhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for WaterPhysicalProperties.

WaterPhysicalProperties(PhaseInterface phase, int binaryDiffusionCoefficientMethod, int multicomponentDiffusionMethod)

Constructor for WaterPhysicalProperties.
Uses of PhaseInterface in neqsim.physicalproperties.system.solidphysicalproperties

Constructors in neqsim.physicalproperties.system.solidphysicalproperties with parameters of type PhaseInterface

Modifier

Constructor

Description

SolidPhysicalProperties(PhaseInterface phase)

Constructor for SolidPhysicalProperties.
Uses of PhaseInterface in neqsim.thermo.component

Fields in neqsim.thermo.component declared as PhaseInterface

Modifier and Type

Field

Description

(package private) PhaseInterface

ComponentHydrate.refPhase

Reference phase containing only this single component, i.e., mixing rules are not relevant.

(package private) PhaseInterface

ComponentSolid.refPhase

Reference phase containing only this single component, i.e., mixing rules are not relevant.

Methods in neqsim.thermo.component with parameters of type PhaseInterface

Modifier and Type

Method

Description

double

ComponentElectrolyteCPA.calc_lngi(PhaseInterface phase)

calc_lngi.

double

ComponentElectrolyteCPAOld.calc_lngi(PhaseInterface phase)

calc_lngi.

double

ComponentElectrolyteCPAstatoil.calc_lngi(PhaseInterface phase)

calc_lngi.

double

ComponentPCSAFTa.calc_lngi(PhaseInterface phase)

calc_lngi.

double

ComponentPrCPA.calc_lngi(PhaseInterface phase)

calc_lngi.

double

ComponentSrkCPA.calc_lngi(PhaseInterface phase)

calc_lngi.

double

ComponentSrkCPAs.calc_lngi(PhaseInterface phase)

calc_lngi.

double

ComponentUMRCPA.calc_lngi(PhaseInterface phase)

calc_lngi.

double

ComponentPrCPA.calc_lngi2(PhaseInterface phase)

calc_lngi2.

double

ComponentElectrolyteCPA.calc_lngidV(PhaseInterface phase)

calc_lngidV.

double

ComponentElectrolyteCPAOld.calc_lngidV(PhaseInterface phase)

calc_lngidV.

double

ComponentElectrolyteCPAstatoil.calc_lngidV(PhaseInterface phase)

calc_lngidV.

double

ComponentPCSAFTa.calc_lngidV(PhaseInterface phase)

calc_lngidV.

double

ComponentSrkCPA.calc_lngidV(PhaseInterface phase)

calc_lngidV.

double

ComponentSrkCPAs.calc_lngidV(PhaseInterface phase)

calc_lngidV.

double

ComponentUMRCPA.calc_lngidV(PhaseInterface phase)

calc_lngidV.

double

ComponentElectrolyteCPA.calc_lngij(int j, PhaseInterface phase)

calc_lngij.

double

ComponentElectrolyteCPAstatoil.calc_lngij(int j, PhaseInterface phase)

calc_lngij.

double

ComponentSrkCPA.calc_lngij(int j, PhaseInterface phase)

calc_lngij.

double

ComponentSrkCPAs.calc_lngij(int j, PhaseInterface phase)

calc_lngij.

double

ComponentUMRCPA.calc_lngij(int j, PhaseInterface phase)

calc_lngij.

double

ComponentGEUnifacPSRK.calcaij(PhaseInterface phase, int i, int j)

calcaij.

double

ComponentGEUnifacUMRPRU.calcaij(PhaseInterface phase, int i, int j)

calcaij.

double

ComponentGEUnifacPSRK.calcaijdT(PhaseInterface phase, int i, int j)

calcaijdT.

double

ComponentGEUnifacUMRPRU.calcaijdT(PhaseInterface phase, int i, int j)

calcaijdT.

double

ComponentGEUnifacUMRPRU.calcaijdTdT(PhaseInterface phase, int i, int j)

calcaijdTdT.

double

ComponentHydrate.calcChemPotEmpty(PhaseInterface phase, int numberOfComps, double temp, double pres, int hydrateStruct)

calcChemPotEmpty.

double

ComponentHydrate.calcChemPotIdealWater(PhaseInterface phase, int numberOfComps, double temp, double pres, int hydrateStruct)

calcChemPotIdealWater.

double

ComponentHydrate.calcCKI(int stucture, int cavityType, PhaseInterface phase)

calcCKI.

double

ComponentHydrateBallard.calcCKI(int stucture, int cavityType, PhaseInterface phase)

calcCKI.

double

ComponentHydrateGF.calcCKI(int stucture, int cavityType, PhaseInterface phase)

calcCKI.

double

ComponentHydrateKluda.calcCKI(int stucture, int cavityType, PhaseInterface phase)

calcCKI.

double

ComponentHydratePVTsim.calcCKI(int stucture, int cavityType, PhaseInterface phase)

calcCKI.

double

ComponentHydrateStatoil.calcCKI(int stucture, int cavityType, PhaseInterface phase)

calcCKI.

double

ComponentPCSAFT.calcdahsSAFTdi(PhaseInterface phase, int nuberOfComponents, double temp, double pres)

calcdahsSAFTdi.

double

ComponentHydratePVTsim.calcDeltaChemPot(PhaseInterface phase, int numberOfComps, double temp, double pres, int hydrateStruct)

calcDeltaChemPot.

double

ComponentPCSAFT.calcdghsSAFTdi(PhaseInterface phase, int nuberOfComponents, double temp, double pres)

calcdghsSAFTdi.

double

ComponentModifiedFurstElectrolyteEos.calcdiElectricdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcdiElectricdn.

double

ComponentModifiedFurstElectrolyteEosMod2004.calcdiElectricdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcdiElectricdn.

double

ComponentModifiedFurstElectrolyteEos.calcdiElectricdndn(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcdiElectricdndn.

double

ComponentModifiedFurstElectrolyteEosMod2004.calcdiElectricdndn(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcdiElectricdndn.

double

ComponentModifiedFurstElectrolyteEos.calcdiElectricdndT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcdiElectricdndT.

double

ComponentModifiedFurstElectrolyteEosMod2004.calcdiElectricdndT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcdiElectricdndT.

double

ComponentModifiedFurstElectrolyteEos.calcdiElectricdndV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcdiElectricdndV.

double

ComponentModifiedFurstElectrolyteEosMod2004.calcdiElectricdndV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcdiElectricdndV.

double

ComponentPCSAFT.calcdmSAFTdi(PhaseInterface phase, int nuberOfComponents, double temp, double pres)

calcdmSAFTdi.

double

ComponentPCSAFT.calcdnSAFTdi(PhaseInterface phase, int nuberOfComponents, double temp, double pres)

calcdnSAFTdi.

double

ComponentPCSAFT.calcF1dispSumTermdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcF1dispSumTermdn.

double

ComponentPCSAFT.calcF2dispSumTermdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcF2dispSumTermdn.

double

ComponentModifiedFurstElectrolyteEos.calcGammaLRdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcGammaLRdn.

double

ComponentModifiedFurstElectrolyteEosMod2004.calcGammaLRdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcGammaLRdn.

void

ComponentGEUnifacUMRPRU.calcGammaNumericalDerivatives(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

calcGammaNumericalDerivatives.

void

ComponentGEUnifac.calclnGammak(int k, PhaseInterface phase)

calclnGammak.

void

ComponentGEUnifacPSRK.calclnGammak(int k, PhaseInterface phase)

calclnGammak.

void

ComponentGEUnifacUMRPRU.calclnGammak(int k, PhaseInterface phase)

calclnGammak.

void

ComponentGEUnifacUMRPRU.calclnGammakdn(int k, PhaseInterface phase, int derCompNumb)

calclnGammakdn.

void

ComponentGEUnifacPSRK.calclnGammakdT(int k, PhaseInterface phase)

calclnGammakdT.

void

ComponentGEUnifacUMRPRU.calclnGammakdTdT(int k, PhaseInterface phase)

calclnGammakdTdT.

double

ComponentModifiedFurstElectrolyteEos.calcSolventdiElectricdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcSolventdiElectricdn.

double

ComponentModifiedFurstElectrolyteEosMod2004.calcSolventdiElectricdn(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcSolventdiElectricdn.

double

ComponentModifiedFurstElectrolyteEos.calcSolventdiElectricdndn(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcSolventdiElectricdndn.

double

ComponentModifiedFurstElectrolyteEosMod2004.calcSolventdiElectricdndn(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcSolventdiElectricdndn.

double

ComponentModifiedFurstElectrolyteEos.calcSolventdiElectricdndT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcSolventdiElectricdndT.

double

ComponentModifiedFurstElectrolyteEosMod2004.calcSolventdiElectricdndT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcSolventdiElectricdndT.

void

ComponentGEUnifacUMRPRU.calcSum2CompdTdT(PhaseInterface phase)

calcSum2CompdTdT.

void

ComponentGEUnifacUMRPRU.calcTempExpaij(PhaseInterface phase)

calcTempExpaij.

void

ComponentGEUnifacUMRPRU.calcUnifacGroupParams(PhaseInterface phase)

calcUnifacGroupParams.

void

ComponentGEUnifacUMRPRU.calcUnifacGroupParamsdT(PhaseInterface phase)

calcUnifacGroupParamsdT.

double

ComponentModifiedFurstElectrolyteEos.calcXLRdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcXLRdN.

double

ComponentModifiedFurstElectrolyteEosMod2004.calcXLRdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

calcXLRdN.

double

ComponentHydrate.calcYKI(int stucture, int cavityType, PhaseInterface phase)

calcYKI.

double

ComponentHydrateBallard.calcYKI(int stucture, int cavityType, PhaseInterface phase)

calcYKI.

double

ComponentHydrateGF.calcYKI(int stucture, int cavityType, PhaseInterface phase)

calcYKI.

double

ComponentHydrateKluda.calcYKI(int stucture, int cavityType, PhaseInterface phase)

calcYKI.

double

ComponentHydratePVTsim.calcYKI(int stucture, int cavityType, PhaseInterface phase)

calcYKI.

double

ComponentHydrateStatoil.calcYKI(int stucture, int cavityType, PhaseInterface phase)

calcYKI.

double

ComponentModifiedFurstElectrolyteEos.dAlphaLRdndn(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dAlphaLRdndn.

double

ComponentModifiedFurstElectrolyteEosMod2004.dAlphaLRdndn(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dAlphaLRdndn.

double

ComponentHydrateKluda.delt(int intnumb, double n, double radius, int struccture, int cavityType, PhaseInterface phase)

delt.

double

ComponentModifiedFurstElectrolyteEos.dEpsdNi(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dEpsdNi.

double

ComponentModifiedFurstElectrolyteEosMod2004.dEpsdNi(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dEpsdNi.

double

ComponentModifiedFurstElectrolyteEos.dEpsdNidV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dEpsdNidV.

double

ComponentModifiedFurstElectrolyteEosMod2004.dEpsdNidV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dEpsdNidV.

double

ComponentModifiedFurstElectrolyteEos.dEpsIonicdNi(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dEpsIonicdNi.

double

ComponentModifiedFurstElectrolyteEosMod2004.dEpsIonicdNi(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dEpsIonicdNi.

double

ComponentModifiedFurstElectrolyteEos.dEpsIonicdNidV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dEpsIonicdNidV.

double

ComponentModifiedFurstElectrolyteEosMod2004.dEpsIonicdNidV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dEpsIonicdNidV.

double

ComponentPCSAFT.dF_DISP1_SAFTdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dF_DISP1_SAFTdN.

double

ComponentPCSAFT.dF_DISP2_SAFTdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dF_DISP2_SAFTdN.

double

ComponentPCSAFT.dF_HC_SAFTdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dF_HC_SAFTdN.

double

ComponentModifiedFurstElectrolyteEos.dFBorndN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFBorndN.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFBorndN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFBorndN.

double

ComponentSrkCPAMM.dFBorndN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Born contribution to dF/dN_i.

double

ComponentModifiedFurstElectrolyteEos.dFBorndNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFBorndNdN.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFBorndNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFBorndNdN.

double

ComponentSrkCPAMM.dFBorndNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Composition derivative of Born contribution to dF/dN_i.

double

ComponentModifiedFurstElectrolyteEos.dFBorndNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFBorndNdT.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFBorndNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFBorndNdT.

double

ComponentSrkCPAMM.dFBorndNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Temperature derivative of Born contribution to dF/dN_i.

double

ComponentSrkCPAMM.dFBorndNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Volume derivative of Born contribution to dF/dN_i.

double

ComponentElectrolyteCPA.dFCPAdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdN.

double

ComponentElectrolyteCPAOld.dFCPAdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdN.

double

ComponentPCSAFTa.dFCPAdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdN.

double

ComponentPrCPA.dFCPAdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdN.

double

ComponentSrkCPA.dFCPAdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdN.

double

ComponentUMRCPA.dFCPAdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdN.

double

ComponentElectrolyteCPA.dFCPAdNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdN.

double

ComponentSrkCPA.dFCPAdNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdN.

double

ComponentUMRCPA.dFCPAdNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdN.

double

ComponentElectrolyteCPA.dFCPAdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdT.

double

ComponentElectrolyteCPAOld.dFCPAdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdT.

double

ComponentSrkCPA.dFCPAdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdT.

double

ComponentUMRCPA.dFCPAdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdT.

double

ComponentElectrolyteCPA.dFCPAdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdV.

double

ComponentElectrolyteCPAOld.dFCPAdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdV.

double

ComponentPCSAFTa.dFCPAdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdV.

double

ComponentSrkCPA.dFCPAdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdV.

double

ComponentUMRCPA.dFCPAdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFCPAdNdV.

double

ComponentCPAInterface.dFCPAdNdXi(int site, PhaseInterface phase)

dFCPAdNdXi.

double

ComponentElectrolyteCPA.dFCPAdNdXi(int site, PhaseInterface phase)

dFCPAdNdXi.

double

ComponentElectrolyteCPAOld.dFCPAdNdXi(int site, PhaseInterface phase)

dFCPAdNdXi.

double

ComponentPCSAFTa.dFCPAdNdXi(int site, PhaseInterface phase)

dFCPAdNdXi.

double

ComponentSrkCPA.dFCPAdNdXi(int site, PhaseInterface phase)

dFCPAdNdXi.

double

ComponentUMRCPA.dFCPAdNdXi(int site, PhaseInterface phase)

dFCPAdNdXi.

double

ComponentElectrolyteCPA.dFCPAdNdXidXdV(PhaseInterface phase)

dFCPAdNdXidXdV.

double

ComponentElectrolyteCPAOld.dFCPAdNdXidXdV(PhaseInterface phase)

dFCPAdNdXidXdV.

double

ComponentPCSAFTa.dFCPAdNdXidXdV(PhaseInterface phase)

dFCPAdNdXidXdV.

double

ComponentSrkCPA.dFCPAdNdXidXdV(PhaseInterface phase)

dFCPAdNdXidXdV.

double

ComponentUMRCPA.dFCPAdNdXidXdV(PhaseInterface phase)

dFCPAdNdXidXdV.

double

ComponentCPAInterface.dFCPAdVdXi(int site, PhaseInterface phase)

dFCPAdVdXi.

double

ComponentElectrolyteCPA.dFCPAdVdXi(int site, PhaseInterface phase)

dFCPAdVdXi.

double

ComponentElectrolyteCPAOld.dFCPAdVdXi(int site, PhaseInterface phase)

dFCPAdVdXi.

double

ComponentPCSAFTa.dFCPAdVdXi(int site, PhaseInterface phase)

dFCPAdVdXi.

double

ComponentSrkCPA.dFCPAdVdXi(int site, PhaseInterface phase)

dFCPAdVdXi.

double

ComponentUMRCPA.dFCPAdVdXi(int site, PhaseInterface phase)

dFCPAdVdXi.

double

ComponentCPAInterface.dFCPAdXi(int site, PhaseInterface phase)

dFCPAdXi.

double

ComponentElectrolyteCPA.dFCPAdXi(int site, PhaseInterface phase)

dFCPAdXi.

double

ComponentElectrolyteCPAOld.dFCPAdXi(int site, PhaseInterface phase)

dFCPAdXi.

double

ComponentPCSAFTa.dFCPAdXi(int site, PhaseInterface phase)

dFCPAdXi.

double

ComponentSrkCPA.dFCPAdXi(int site, PhaseInterface phase)

dFCPAdXi.

double

ComponentUMRCPA.dFCPAdXi(int site, PhaseInterface phase)

dFCPAdXi.

double

ComponentElectrolyteCPA.dFCPAdXidni(int site, PhaseInterface phase)

dFCPAdXidni.

double

ComponentSrkCPA.dFCPAdXidni(int site, PhaseInterface phase)

dFCPAdXidni.

double

ComponentUMRCPA.dFCPAdXidni(int site, PhaseInterface phase)

dFCPAdXidni.

double

ComponentCPAInterface.dFCPAdXidXj(int sitei, int sitej, int compj, PhaseInterface phase)

dFCPAdXidXj.

double

ComponentElectrolyteCPA.dFCPAdXidXj(int sitei, int sitej, int compj, PhaseInterface phase)

dFCPAdXidXj.

double

ComponentElectrolyteCPAOld.dFCPAdXidXj(int sitei, int sitej, int compj, PhaseInterface phase)

dFCPAdXidXj.

double

ComponentPCSAFTa.dFCPAdXidXj(int sitei, int sitej, int compj, PhaseInterface phase)

dFCPAdXidXj.

double

ComponentSrkCPA.dFCPAdXidXj(int sitei, int sitej, int compj, PhaseInterface phase)

dFCPAdXidXj.

double

ComponentUMRCPA.dFCPAdXidXj(int sitei, int sitej, int compj, PhaseInterface phase)

dFCPAdXidXj.

double

ComponentSrkCPAMM.dFDebyeHuckeldN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Debye-Hückel contribution to dF/dN_i.

double

ComponentSrkCPAMM.dFDebyeHuckeldNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Composition derivative of Debye-Hückel contribution to dF/dN_i.

double

ComponentSrkCPAMM.dFDebyeHuckeldNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Temperature derivative of Debye-Hückel contribution to dF/dN_i.

double

ComponentSrkCPAMM.dFDebyeHuckeldNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Volume derivative of Debye-Hückel contribution to dF/dN_i.

double

ComponentAmmoniaEos.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentBWRS.dFdN(PhaseInterface phase, int numberOfComponentphases, double temperature, double pressure)

dFdN.

double

ComponentCSPsrk.dFdN(PhaseInterface phase, int numberOfComponentphases, double temperature, double pressure)

dFdN.

double

ComponentElectrolyteCPA.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentElectrolyteCPAOld.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentEos.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentEosInterface.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentGERG2008Eos.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentLeachmanEos.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentModifiedFurstElectrolyteEos.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentPCSAFT.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentPCSAFTa.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentPrCPA.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentPRvolcor.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentSpanWagnerEos.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentSrkCPA.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentSrkCPAMM.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentSrkvolcor.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentUMRCPA.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentVegaEos.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

ComponentWater.dFdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

ComponentGERG2008Eos.dFdNdN(int i, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFdNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

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

dFdNdN.

double

ComponentAmmoniaEos.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentElectrolyteCPA.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentElectrolyteCPAOld.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentEos.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentEosInterface.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentGERG2008Eos.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentLeachmanEos.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentModifiedFurstElectrolyteEos.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentPCSAFT.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentPCSAFTa.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentPrCPA.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentPRvolcor.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentSpanWagnerEos.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentSrkCPA.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentSrkCPAMM.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentSrkvolcor.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentUMRCPA.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentVegaEos.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentWater.dFdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdT.

double

ComponentAmmoniaEos.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentElectrolyteCPA.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentElectrolyteCPAOld.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentEos.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentEosInterface.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentGERG2008Eos.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentLeachmanEos.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentModifiedFurstElectrolyteEos.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentPCSAFTa.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentPrCPA.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentPRvolcor.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentSpanWagnerEos.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentSrkCPA.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentSrkCPAMM.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentSrkvolcor.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentUMRCPA.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentVegaEos.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentWater.dFdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFdNdV.

double

ComponentModifiedFurstElectrolyteEos.dFLRdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFLRdN.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFLRdN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFLRdN.

double

ComponentModifiedFurstElectrolyteEos.dFLRdNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFLRdNdN.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFLRdNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFLRdNdN.

double

ComponentModifiedFurstElectrolyteEos.dFLRdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFLRdNdT.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFLRdNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFLRdNdT.

double

ComponentModifiedFurstElectrolyteEos.dFLRdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFLRdNdV.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFLRdNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFLRdNdV.

double

ComponentSrkCPAMM.dFShortRangedN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Short-range ion-solvent contribution to dF/dN_i.

double

ComponentSrkCPAMM.dFShortRangedNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Composition derivative of short-range contribution to dF/dN_i using wij mixing rule.

double

ComponentSrkCPAMM.dFShortRangedNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Temperature derivative of short-range contribution to dF/dN_i using wij mixing rule.

double

ComponentSrkCPAMM.dFShortRangedNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

Volume derivative of short-range contribution to dF/dN_i using wij mixing rule.

double

ComponentModifiedFurstElectrolyteEos.dFSR2dN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFSR2dN.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFSR2dN(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFSR2dN.

double

ComponentModifiedFurstElectrolyteEos.dFSR2dNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFSR2dNdN.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFSR2dNdN(int j, PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFSR2dNdN.

double

ComponentModifiedFurstElectrolyteEos.dFSR2dNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFSR2dNdT.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFSR2dNdT(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFSR2dNdT.

double

ComponentModifiedFurstElectrolyteEos.dFSR2dNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFSR2dNdV.

double

ComponentModifiedFurstElectrolyteEosMod2004.dFSR2dNdV(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

dFSR2dNdV.

double

ComponentHydrateKluda.dfugdt(PhaseInterface phase, int numberOfComps, double temp, double pres)

dfugdt.

void

Component.Finit(PhaseInterface phase, double temp, double pres, double totMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentAmmoniaEos.Finit(PhaseInterface phase, double T, double p, double totalNumberOfMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentEos.Finit(PhaseInterface phase, double temp, double pres, double totMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentGERG2008Eos.Finit(PhaseInterface phase, double T, double p, double totalNumberOfMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentInterface.Finit(PhaseInterface phase, double temperature, double pressure, double totalNumberOfMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentLeachmanEos.Finit(PhaseInterface phase, double T, double p, double totalNumberOfMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentModifiedFurstElectrolyteEos.Finit(PhaseInterface phase, double temp, double pres, double totMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentModifiedFurstElectrolyteEosMod2004.Finit(PhaseInterface phase, double temp, double pres, double totMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentPCSAFT.Finit(PhaseInterface phase, double temp, double pres, double totMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentPRvolcor.Finit(PhaseInterface phase, double temp, double pres, double totMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentSpanWagnerEos.Finit(PhaseInterface phase, double T, double p, double totalNumberOfMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentSrkvolcor.Finit(PhaseInterface phase, double temp, double pres, double totMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentVegaEos.Finit(PhaseInterface phase, double T, double p, double totalNumberOfMoles, double beta, int numberOfComponents, int initType)

Finit.

void

ComponentWater.Finit(PhaseInterface phase, double T, double p, double totalNumberOfMoles, double beta, int numberOfComponents, int initType)

Finit.

double

Component.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentAmmoniaEos.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentDesmukhMather.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentEos.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentGE.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentGeDuanSun.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentGePitzer.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentGERG2004.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentGERG2008Eos.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentGEUnifac.fugcoef(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

Calculate, set and return fugacity coefficient.

double

ComponentGEUniquac.fugcoef(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

Calculate, set and return fugacity coefficient.

double

ComponentGEWilson.fugcoef(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

Calculate, set and return fugacity coefficient.

double

ComponentHydrate.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentHydrate.fugcoef(PhaseInterface phase, int numberOfComps, double temp, double pres)

Calculate, set and return fugacity coefficient.

double

ComponentHydrateBallard.fugcoef(PhaseInterface phase, int numberOfComps, double temp, double pres)

Calculate, set and return fugacity coefficient.

double

ComponentHydrateGF.fugcoef(PhaseInterface phase, int numberOfComps, double temp, double pres)

Calculate, set and return fugacity coefficient.

double

ComponentHydrateKluda.fugcoef(PhaseInterface phase, int numberOfComps, double temp, double pres)

Calculate, set and return fugacity coefficient.

double

ComponentHydratePVTsim.fugcoef(PhaseInterface phase, int numberOfComps, double temp, double pres)

Calculate, set and return fugacity coefficient.

double

ComponentHydrateStatoil.fugcoef(PhaseInterface phase, int numberOfComps, double temp, double pres)

Calculate, set and return fugacity coefficient.

double

ComponentIdealGas.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentInterface.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentKentEisenberg.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentLeachmanEos.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentSolid.fugcoef(PhaseInterface phase1)

Calculate, set and return fugacity coefficient.

double

ComponentSpanWagnerEos.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentVegaEos.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentWater.fugcoef(PhaseInterface phase)

Calculate, set and return fugacity coefficient.

double

ComponentWax.fugcoef(PhaseInterface phase1)

Calculate, set and return fugacity coefficient.

double

ComponentWaxWilson.fugcoef(PhaseInterface phase1)

Calculate, set and return fugacity coefficient.

double

ComponentWonWax.fugcoef(PhaseInterface phase1)

Calculate, set and return fugacity coefficient.

double

ComponentHydrateGF.fugcoef2(PhaseInterface phase, int numberOfComps, double temp, double pres)

fugcoef2.

double

ComponentSolid.fugcoef2(PhaseInterface phase1)

Calculate, set and return fugacity coefficient.

double

ComponentWax.fugcoef2(PhaseInterface phase1)

Calculate, set and return fugacity coefficient.

double

ComponentWaxWilson.fugcoef2(PhaseInterface phase1)

Calculate, set and return fugacity coefficient.

double

ComponentWonWax.fugcoef2(PhaseInterface phase1)

Calculate, set and return fugacity coefficient.

double

ComponentGE.fugcoefDiffPres(PhaseInterface phase)

fugcoefDiffPres.

double

ComponentGEUnifac.fugcoefDiffPres(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

fugcoefDiffPres.

double

ComponentGEUniquac.fugcoefDiffPres(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

fugcoefDiffPres.

double

Component.fugcoefDiffPresNumeric(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

fugcoefDiffPresNumeric.

double

ComponentInterface.fugcoefDiffPresNumeric(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

fugcoefDiffPresNumeric.

double

ComponentGE.fugcoefDiffTemp(PhaseInterface phase)

fugcoefDiffTemp.

double

ComponentGEUnifac.fugcoefDiffTemp(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

fugcoefDiffTemp.

double

ComponentGEUniquac.fugcoefDiffTemp(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

fugcoefDiffTemp.

double

Component.fugcoefDiffTempNumeric(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

fugcoefDiffTempNumeric.

double

ComponentInterface.fugcoefDiffTempNumeric(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

fugcoefDiffTempNumeric.

double

ComponentEos.getAresnTV(PhaseInterface phase)

getAresnTV.

double

ComponentGEWilson.getCharEnergyParamter(PhaseInterface phase1, int comp1, int comp2)

getCharEnergyParamter.

double

ComponentWaxWilson.getCharEnergyParamter(PhaseInterface phase1, int comp1, int comp2)

getCharEnergyParamter.

double

Component.getChemicalPotential(PhaseInterface phase)

getChemicalPotential.

double

ComponentEos.getChemicalPotential(PhaseInterface phase)

getChemicalPotential.

double

ComponentInterface.getChemicalPotential(PhaseInterface phase)

getChemicalPotential.

final double

Component.getChemicalPotentialdN(int i, PhaseInterface phase)

getChemicalPotentialdN.

double

ComponentInterface.getChemicalPotentialdN(int i, PhaseInterface phase)

getChemicalPotentialdN.

final double

Component.getChemicalPotentialdNTV(int i, PhaseInterface phase)

getChemicalPotentialdNTV.

double

ComponentInterface.getChemicalPotentialdNTV(int i, PhaseInterface phase)

getChemicalPotentialdNTV.

final double

Component.getChemicalPotentialdP(int i, PhaseInterface phase)

getChemicalPotentialdP.

final double

Component.getChemicalPotentialdT(PhaseInterface phase)

getChemicalPotentialdT.

double

ComponentInterface.getChemicalPotentialdT(PhaseInterface phase)

getChemicalPotentialdT.

final double

Component.getChemicalPotentialdV(PhaseInterface phase)

getChemicalPotentialdV.

double

ComponentInterface.getChemicalPotentialdV(PhaseInterface phase)

getChemicalPotentialdV.

final double

Component.getChemicalPotentialIdealReference(PhaseInterface phase)

getChemicalPotentialIdealReference.

double

ComponentInterface.getChemicalPotentialIdealReference(PhaseInterface phase)

getChemicalPotentialIdealReference.

double

ComponentBWRS.getdRhodn(PhaseInterface phase, int numberOfComponentphases, double temperature, double pressure)

getdRhodn.

double

ComponentEos.getdUdndnSV(PhaseInterface phase, int compNumb1, int compNumb2)

getdUdndnSV.

double

ComponentEos.getdUdnSV(PhaseInterface phase)

getdUdnSV.

double

ComponentEos.getdUdSdnV(PhaseInterface phase)

getdUdSdnV.

double

ComponentEos.getdUdVdnS(PhaseInterface phase)

getdUdVdnS.

double

ComponentBWRS.getELdn(PhaseInterface phase, int numberOfComponentphases, double temperature, double pressure)

getELdn.

double

ComponentPRvolcor.getFC(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

getFC.

double

ComponentSrkvolcor.getFC(PhaseInterface phase, int numberOfComponents, double temperature, double pressure)

getFC.

double

ComponentBWRS.getFexpdn(PhaseInterface phase, int numberOfComponentphases, double temperature, double pressure)

getFexpdn.

double

ComponentBWRS.getFpoldn(PhaseInterface phase, int numberOfComponentphases, double temperature, double pressure)

getFpoldn.

final double

Component.getFugacitydN(int i, PhaseInterface phase)

getFugacitydN.

double

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

getGamma.

double

ComponentDesmukhMather.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij, double[][] intparam, String[][] mixRule)

getGamma.

double

ComponentGeDuanSun.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij)

getGamma.

double

ComponentGeDuanSun.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij, double[][] intparam, String[][] mixRule)

getGamma.

double

ComponentGEInterface.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij, double[][] intparam, String[][] mixRule)

getGamma.

double

ComponentGeNRTL.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij, double[][] intparam, String[][] mixRule)

getGamma.

double

ComponentGENRTLmodifiedHV.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij, double[][] HVgijT, double[][] intparam, String[][] mixRule)

getGamma.

double

ComponentGENRTLmodifiedHV.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij, double[][] intparam, String[][] mixRule)

getGamma.

double

ComponentGENRTLmodifiedWS.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] WSalpha, double[][] WSgij, double[][] WSgijT, double[][] intparam, String[][] mixRule)

getGamma.

double

ComponentGENRTLmodifiedWS.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] WSalpha, double[][] WSgij, double[][] intparam, String[][] mixRule)

getGamma.

double

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

Calculate activity coefficient using the Pitzer model.

double

ComponentGePitzer.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij, double[][] intparam, String[][] mixRule)

getGamma.

double

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

getGamma.

double

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

getGamma.

double

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

getGamma.

double

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

getGamma.

double

ComponentGEUniquac.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij, double[][] intparam, String[][] mixRule)

getGamma.

double

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

getGamma.

double

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

getGamma.

double

ComponentGEWilson.getGamma(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij, double[][] intparam, String[][] mixRule)

getGamma.

double

ComponentGeDuanSun.getGammaNRTL(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double[][] HValpha, double[][] HVgij)

getGammaNRTL.

double

ComponentGeDuanSun.getGammaPitzer(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt, double salinity)

getGammaPitzer.

private PhaseElectrolyteCPAMM

ComponentSrkCPAMM.getMMPhase(PhaseInterface phase)

Check if phase is an electrolyte MM phase.

double

Component.getMolality(PhaseInterface phase)

getMolality.

double

ComponentDesmukhMather.getMolality(PhaseInterface phase)

getMolality.

double

ComponentGePitzer.getMolality(PhaseInterface phase)

getMolality.

double

ComponentInterface.getMolality(PhaseInterface phase)

getMolality.

double

Component.getMolarity(PhaseInterface phase)

getMolarity.

double

ComponentInterface.getMolarity(PhaseInterface phase)

getMolarity.

double

ComponentHydrate.getPot(double radius, int struccture, int cavityType, PhaseInterface phase)

getPot.

double

ComponentHydrateBallard.getPot(double radius, int struccture, int cavityType, PhaseInterface phase)

getPot.

double

ComponentHydrateKluda.getPot(int intnumb, double radius, int struccture, int cavityType, PhaseInterface phase)

getPot.

double

ComponentHydrateStatoil.getPot(double radius, int struccture, int cavityType, PhaseInterface phase)

getPot.

double

ComponentGEWilson.getWilsonActivityCoefficient(PhaseInterface phase1)

getWilsonActivityCoefficient.

double

ComponentWaxWilson.getWilsonActivityCoefficient(PhaseInterface phase1)

getWilsonActivityCoefficient.

double

ComponentGEWilson.getWilsonInteractionEnergy(PhaseInterface phase1)

getWilsonInteractionEnergy.

double

ComponentWaxWilson.getWilsonInteractionEnergy(PhaseInterface phase1)

getWilsonInteractionEnergy.

double

ComponentWonWax.getWonActivityCoefficient(PhaseInterface phase1)

getWonActivityCoefficient.

double

ComponentWonWax.getWonParam(PhaseInterface phase1)

getWonParam.

double

ComponentWonWax.getWonVolume(PhaseInterface phase1)

getWonVolume.

double[]

Component.logfugcoefdN(PhaseInterface phase)

logfugcoefdN.

double[]

ComponentAmmoniaEos.logfugcoefdN(PhaseInterface phase)

logfugcoefdN.

double[]

ComponentEos.logfugcoefdN(PhaseInterface phase)

logfugcoefdN.

double[]

ComponentGERG2008Eos.logfugcoefdN(PhaseInterface phase)

logfugcoefdN.

double[]

ComponentIdealGas.logfugcoefdN(PhaseInterface phase)

logfugcoefdN.

double[]

ComponentInterface.logfugcoefdN(PhaseInterface phase)

logfugcoefdN.

double

Component.logfugcoefdNi(PhaseInterface phase, int k)

logfugcoefdNi.

double

ComponentEos.logfugcoefdNi(PhaseInterface phase, int k)

logfugcoefdNi.

double

ComponentGERG2008Eos.logfugcoefdNi(PhaseInterface phase, int k)

logfugcoefdNi.

double

ComponentIdealGas.logfugcoefdNi(PhaseInterface phase, int k)

logfugcoefdNi.

double

ComponentInterface.logfugcoefdNi(PhaseInterface phase, int k)

logfugcoefdNi.

double

Component.logfugcoefdP(PhaseInterface phase)

logfugcoefdP.

double

ComponentAmmoniaEos.logfugcoefdP(PhaseInterface phase)

logfugcoefdP.

double

ComponentEos.logfugcoefdP(PhaseInterface phase)

logfugcoefdP.

double

ComponentGERG2008Eos.logfugcoefdP(PhaseInterface phase)

logfugcoefdP.

double

ComponentIdealGas.logfugcoefdP(PhaseInterface phase)

logfugcoefdP.

double

ComponentInterface.logfugcoefdP(PhaseInterface phase)

logfugcoefdP.

double

Component.logfugcoefdT(PhaseInterface phase)

logfugcoefdT.

double

ComponentAmmoniaEos.logfugcoefdT(PhaseInterface phase)

logfugcoefdT.

double

ComponentEos.logfugcoefdT(PhaseInterface phase)

logfugcoefdT.

double

ComponentGERG2008Eos.logfugcoefdT(PhaseInterface phase)

logfugcoefdT.

double

ComponentIdealGas.logfugcoefdT(PhaseInterface phase)

logfugcoefdT.

double

ComponentInterface.logfugcoefdT(PhaseInterface phase)

logfugcoefdT.

double

ComponentHydrate.potIntegral(int stucture, int cavityType, PhaseInterface phase)

potIntegral.

double

ComponentHydrateBallard.potIntegral(int stucture, int cavityType, PhaseInterface phase)

potIntegral.

double

ComponentHydrateKluda.potIntegral(int intnumb, int stucture, int cavityType, PhaseInterface phase)

potIntegral.

double

ComponentHydrateStatoil.potIntegral(int stucture, int cavityType, PhaseInterface phase)

potIntegral.

void

ComponentHydrate.setSolidRefFluidPhase(PhaseInterface phase)

setSolidRefFluidPhase.

void

ComponentSolid.setSolidRefFluidPhase(PhaseInterface phase)

setSolidRefFluidPhase.

Constructors in neqsim.thermo.component with parameters of type PhaseInterface

Modifier

Constructor

Description

ComponentSrkCPA(int number, double TC, double PC, double M, double a, double moles, PhaseInterface phase)

Constructor for ComponentSrkCPA.

ComponentSrkCPA(String name, double moles, double molesInPhase, int compIndex, PhaseInterface phase)

Constructor for ComponentSrkCPA.

ComponentSrkCPAMM(String name, double moles, double molesInPhase, int compIndex, PhaseInterface phase)

Constructor for ComponentSrkCPAMM.

ComponentSrkCPAs(int number, double TC, double PC, double M, double a, double moles, PhaseInterface phase)

Constructor for ComponentSrkCPAs.

ComponentSrkCPAs(String name, double moles, double molesInPhase, int compIndex, PhaseInterface phase)

Constructor for ComponentSrkCPAs.
Uses of PhaseInterface in neqsim.thermo.mixingrule

Fields in neqsim.thermo.mixingrule declared as PhaseInterface

Modifier and Type

Field

Description

(package private) PhaseInterface

EosMixingRuleHandler.SRKHuronVidal.orgPhase

(package private) PhaseInterface

EosMixingRuleHandler.SRKHuronVidal2.orgPhase

Methods in neqsim.thermo.mixingrule that return PhaseInterface

Modifier and Type

Method

Description

PhaseInterface

EosMixingRuleHandler.ClassicVdW.getGEPhase()

getGEPhase.

PhaseInterface

EosMixingRuleHandler.SRKHuronVidal2.getGEPhase()

getGEPhase.

PhaseInterface

EosMixingRulesInterface.getGEPhase()

getGEPhase.

Methods in neqsim.thermo.mixingrule with parameters of type PhaseInterface

Modifier and Type

Method

Description

double

EosMixingRuleHandler.ClassicSRK.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

EosMixingRuleHandler.ClassicSRKT2x.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

EosMixingRuleHandler.ClassicVdW.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

EosMixingRuleHandler.SRKHuronVidal.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

EosMixingRuleHandler.SRKHuronVidal2.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

EosMixingRuleHandler.WhitsonSoreideMixingRule.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

EosMixingRuleHandler.WongSandlerMixingRule.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

EosMixingRulesInterface.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

EosMixingRuleHandler.ClassicSRK.calcAi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

EosMixingRuleHandler.ClassicSRKT2x.calcAi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAi.

double

EosMixingRuleHandler.ClassicVdW.calcAi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAi.

double

EosMixingRuleHandler.SRKHuronVidal.calcAi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAi.

double

EosMixingRuleHandler.SRKHuronVidal2.calcAi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAi.

double

EosMixingRuleHandler.WhitsonSoreideMixingRule.calcAi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

EosMixingRuleHandler.WongSandlerMixingRule.calcAi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAi.

double

EosMixingRulesInterface.calcAi(int compnumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAi.

double

EosMixingRuleHandler.ClassicSRK.calcAij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

EosMixingRuleHandler.ClassicSRKT2x.calcAij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

EosMixingRuleHandler.ClassicVdW.calcAij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

EosMixingRuleHandler.SRKHuronVidal.calcAij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

EosMixingRuleHandler.SRKHuronVidal2.calcAij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

EosMixingRuleHandler.WhitsonSoreideMixingRule.calcAij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

EosMixingRuleHandler.WongSandlerMixingRule.calcAij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

EosMixingRulesInterface.calcAij(int compnumb, int j, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

EosMixingRuleHandler.ClassicSRK.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

EosMixingRuleHandler.ClassicSRKT.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

EosMixingRuleHandler.ClassicSRKT2x.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

EosMixingRuleHandler.ClassicVdW.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

EosMixingRuleHandler.SRKHuronVidal.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

EosMixingRuleHandler.SRKHuronVidal2.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

EosMixingRuleHandler.WhitsonSoreideMixingRule.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

EosMixingRuleHandler.WongSandlerMixingRule.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

EosMixingRulesInterface.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

EosMixingRuleHandler.ClassicSRKT.calcAiTT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

EosMixingRuleHandler.ClassicSRK.calcAT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAT.

double

EosMixingRuleHandler.ClassicVdW.calcAT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAT.

double

EosMixingRuleHandler.SRKHuronVidal.calcAT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAT.

double

EosMixingRuleHandler.SRKHuronVidal2.calcAT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAT.

double

EosMixingRuleHandler.WhitsonSoreideMixingRule.calcAT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAT.

double

EosMixingRuleHandler.WongSandlerMixingRule.calcAT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAT.

double

EosMixingRulesInterface.calcAT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAT.

double

EosMixingRuleHandler.ClassicSRK.calcATT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcATT.

double

EosMixingRuleHandler.ClassicSRKT.calcATT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

EosMixingRuleHandler.ClassicVdW.calcATT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcATT.

double

EosMixingRuleHandler.SRKHuronVidal2.calcATT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcATT.

double

EosMixingRuleHandler.WhitsonSoreideMixingRule.calcATT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcATT.

double

EosMixingRuleHandler.WongSandlerMixingRule.calcATT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcATT.

double

EosMixingRulesInterface.calcATT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcATT.

double

EosMixingRuleHandler.ClassicVdW.calcB(PhaseInterface phase, double T, double P, int n)

calcB.

double

EosMixingRuleHandler.WongSandlerMixingRule.calcB(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcB.

double

EosMixingRulesInterface.calcB(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcB.

double

EosMixingRuleHandler.ClassicVdW.calcBFull(PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

EosMixingRuleHandler.ClassicVdW.calcBi(int i, PhaseInterface phase, double T, double P, int n)

calcBi.

double

EosMixingRuleHandler.WongSandlerMixingRule.calcBi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBi.

double

EosMixingRulesInterface.calcBi(int compnumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBi.

double

EosMixingRuleHandler.ClassicVdW.calcBi2(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

EosMixingRuleHandler.ClassicVdW.calcBiFull(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

EosMixingRuleHandler.ClassicVdW.calcBij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBij.

double

EosMixingRuleHandler.WongSandlerMixingRule.calcBij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBij.

double

EosMixingRulesInterface.calcBij(int compnumb, int j, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBij.

double

EosMixingRuleHandler.WongSandlerMixingRule.calcBiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

EosMixingRuleHandler.WongSandlerMixingRule.calcBT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

EosMixingRuleHandler.WongSandlerMixingRule.calcBTT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

CPAMixingRuleHandler.CPA_Radoch_base.calcDelta(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDelta.

double

CPAMixingRuleHandler.CPA_Radoch.calcDelta(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDelta.

double

CPAMixingRuleHandler.CPA_Radoch.calcDelta(int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

CPAMixingRuleHandler.PCSAFTa_Radoch.calcDelta(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDelta.

double

CPAMixingRulesInterface.calcDelta(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDelta.

double

CPAMixingRuleHandler.CPA_Radoch_base.calcDeltadN(int derivativeComp, int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadN.

double

CPAMixingRuleHandler.CPA_Radoch.calcDeltadN(int derivativeComp, int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadN.

double

CPAMixingRulesInterface.calcDeltadN(int derivativeComp, int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadN.

double

CPAMixingRuleHandler.CPA_Radoch_base.calcDeltadT(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadT.

double

CPAMixingRuleHandler.CPA_Radoch.calcDeltadT(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadT.

double

CPAMixingRulesInterface.calcDeltadT(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadT.

double

CPAMixingRuleHandler.CPA_Radoch_base.calcDeltadTdT(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadTdT.

double

CPAMixingRuleHandler.CPA_Radoch.calcDeltadTdT(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadTdT.

double

CPAMixingRulesInterface.calcDeltadTdT(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadTdT.

double

CPAMixingRuleHandler.CPA_Radoch_base.calcDeltadTdV(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadTdV.

double

CPAMixingRuleHandler.CPA_Radoch.calcDeltadTdV(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadTdV.

double

CPAMixingRulesInterface.calcDeltadTdV(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadTdV.

double

CPAMixingRuleHandler.CPA_Radoch_base.calcDeltadV(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadV.

double

CPAMixingRuleHandler.CPA_Radoch.calcDeltadV(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadV.

double

CPAMixingRulesInterface.calcDeltadV(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltadV.

double

CPAMixingRuleHandler.CPA_Radoch_base.calcDeltaNog(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltaNog.

double

CPAMixingRuleHandler.CPA_Radoch.calcDeltaNog(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltaNog.

double

CPAMixingRulesInterface.calcDeltaNog(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcDeltaNog.

double

ElectrolyteMixingRulesInterface.calcW(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcW.

double

EosMixingRuleHandler.ElectrolyteMixRule.calcW(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcW.

double

ElectrolyteMixingRulesInterface.calcWi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWi.

double

EosMixingRuleHandler.ElectrolyteMixRule.calcWi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWi.

double

ElectrolyteMixingRulesInterface.calcWij(int compNumbi, int compNumj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWij.

void

ElectrolyteMixingRulesInterface.calcWij(PhaseInterface phase)

calcWij.

double

EosMixingRuleHandler.ElectrolyteMixRule.calcWij(int compNumbi, int compNumj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWij.

void

EosMixingRuleHandler.ElectrolyteMixRule.calcWij(PhaseInterface phase)

calcWij.

double

ElectrolyteMixingRulesInterface.calcWiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWiT.

double

EosMixingRuleHandler.ElectrolyteMixRule.calcWiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWiT.

double

ElectrolyteMixingRulesInterface.calcWT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWT.

double

EosMixingRuleHandler.ElectrolyteMixRule.calcWT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWT.

double

ElectrolyteMixingRulesInterface.calcWTT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWTT.

double

EosMixingRuleHandler.ElectrolyteMixRule.calcWTT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWTT.

double

CPAMixingRuleHandler.CPA_Radoch_base.calcXi(int[][][] assosScheme, int[][][][] assosScheme2, int siteNumber, int compnumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcXi.

double

CPAMixingRuleHandler.CPA_Radoch_base.calcXi(int siteNumber, int compnumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

CPAMixingRulesInterface.calcXi(int[][][] assosScheme, int[][][][] assosScheme2, int siteNumber, int compnumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcXi.

void

EosMixingRuleHandler.displayInteractionCoefficients(String intType, PhaseInterface phase)

displayInteractionCoefficients.

double

CPAMixingRuleHandler.CPA_Radoch.getCrossAssociationEnergy(int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

CPAMixingRuleHandler.PCSAFTa_Radoch.getCrossAssociationEnergy(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

CPAMixingRuleHandler.CPA_Radoch.getCrossAssociationVolume(int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

double

CPAMixingRuleHandler.PCSAFTa_Radoch.getCrossAssociationVolume(int siteNumber1, int siteNumber2, int compnumb1, int compnumb2, PhaseInterface phase, double temperature, double pressure, int numbcomp)

ElectrolyteMixingRulesInterface

EosMixingRuleHandler.getElectrolyteMixingRule(PhaseInterface phase)

getElectrolyteMixingRule.

double

EosMixingRuleHandler.ClassicSRKT2x.getkij(PhaseInterface phase, double temperature, int i, int j)

double

EosMixingRuleHandler.ClassicSRKT2x.getkijdn(int k, PhaseInterface phase, double temperature, int i, int j)

double

EosMixingRuleHandler.ClassicSRKT2x.getkijdndn(int k, int l, PhaseInterface phase, double temperature, int i, int j)

CPAMixingRulesInterface

CPAMixingRuleHandler.getMixingRule(int mr, PhaseInterface phase)

getMixingRule.

EosMixingRulesInterface

EosMixingRuleHandler.getMixingRule(int mr, PhaseInterface phase)

getMixingRule.

void

EosMixingRuleHandler.SRKHuronVidal2.init(PhaseInterface phase, double temperature, double pressure, int numbcomp)

init.

void

EosMixingRuleHandler.WongSandlerMixingRule.init(PhaseInterface phase, double temperature, double pressure, int numbcomp)

init.

MixingRulesInterface

CPAMixingRuleHandler.resetMixingRule(int i, PhaseInterface phase)

resetMixingRule.

EosMixingRulesInterface

EosMixingRuleHandler.resetMixingRule(int i, PhaseInterface phase)

resetMixingRule.

int[][]

CPAMixingRuleHandler.setAssociationScheme(int compnumb, PhaseInterface phase)

setAssociationScheme.

int[][]

CPAMixingRuleHandler.setCrossAssociationScheme(int compnumb, int compnumb2, PhaseInterface phase)

setCrossAssociationScheme.

Constructors in neqsim.thermo.mixingrule with parameters of type PhaseInterface

Modifier

Constructor

Description

ElectrolyteMixRule(PhaseInterface phase)

SRKHuronVidal(PhaseInterface phase, double[][] HValpha, double[][] HVDij, double[][] HVDijT, String[][] mixRule)

SRKHuronVidal(PhaseInterface phase, double[][] HValpha, double[][] HVDij, String[][] mixRule)

SRKHuronVidal2(PhaseInterface phase, double[][] HValpha, double[][] HVDij, double[][] HVDijT, String[][] mixRule)

SRKHuronVidal2(PhaseInterface phase, double[][] HValpha, double[][] HVDij, String[][] mixRule)

Constructor for SRKHuronVidal2.

WongSandlerMixingRule(PhaseInterface phase, double[][] WSalpha, double[][] WSDij, double[][] WSDijT, String[][] mixRule)

WongSandlerMixingRule(PhaseInterface phase, double[][] WSalpha, double[][] WSDij, String[][] mixRule)
Uses of PhaseInterface in neqsim.thermo.phase

Subinterfaces of PhaseInterface in neqsim.thermo.phase

Modifier and Type

Interface

Description

interface

PhaseCPAInterface

PhaseCPAInterface interface.

interface

PhaseEosInterface

PhaseEosInterface interface.

Classes in neqsim.thermo.phase that implement PhaseInterface

Modifier and Type

Class

Description

class

Phase

Abstract Phase class.

class

PhaseAmmoniaEos

Phase implementation for the Ammonia2023 reference equation of state based on a multiparameter Helmholtz energy formulation.

class

PhaseBNS

Phase implementation using the Burgoyne–Nielsen–Stanko PR correlation.

class

PhaseBWRSEos

PhaseBWRSEos class.

class

PhaseCSPsrkEos

PhaseCSPsrkEos class.

class

PhaseDefault

PhaseDefault class.

class

PhaseDesmukhMather

PhaseDesmukhMather class.

class

PhaseDuanSun

PhaseDuanSun class.

class

PhaseElectrolyteCPA

PhaseElectrolyteCPA class.

class

PhaseElectrolyteCPAMM

Electrolyte CPA (e-CPA) phase class implementing the Maribo-Mogensen model.

class

PhaseElectrolyteCPAOld

PhaseElectrolyteCPAOld class.

class

PhaseElectrolyteCPAstatoil

PhaseElectrolyteCPAstatoil class.

class

PhaseEos

Abstract class PhaseEos.

class

PhaseEOSCGEos

Phase implementation using the EOS-CG mixture model.

class

PhaseGE

Abstract class PhaseGE.

class

PhaseGENRTL

PhaseGENRTL class.

class

PhaseGENRTLmodifiedHV

PhaseGENRTLmodifiedHV class.

class

PhaseGENRTLmodifiedWS

PhaseGENRTLmodifiedWS class.

class

PhaseGERG2004Eos

PhaseGERG2004Eos class.

class

PhaseGERG2008Eos

PhaseGERG2008Eos class.

class

PhaseGEUnifac

PhaseGEUnifac class.

class

PhaseGEUnifacPSRK

PhaseGEUnifacPSRK class.

class

PhaseGEUnifacUMRPRU

PhaseGEUnifacUMRPRU class.

class

PhaseGEUniquac

PhaseGEUniquac class.

class

PhaseGEUniquacmodifiedHV

PhaseGEUniquacmodifiedHV class.

class

PhaseGEWilson

PhaseGEWilson class.

class

PhaseHydrate

PhaseHydrate class.

class

PhaseIdealGas

Phase model for an ideal gas.

class

PhaseKentEisenberg

PhaseKentEisenberg class.

class

PhaseLeachmanEos

PhaseLeachmanEos class.

class

PhaseModifiedFurstElectrolyteEos

PhaseModifiedFurstElectrolyteEos class.

class

PhaseModifiedFurstElectrolyteEosMod2004

PhaseModifiedFurstElectrolyteEosMod2004 class.

class

PhasePCSAFT

PhasePCSAFT class.

class

PhasePCSAFTa

PhasePCSAFTa class.

class

PhasePCSAFTRahmat

PhasePCSAFTRahmat class.

class

PhasePitzer

Phase implementation for the Pitzer activity coefficient model.

class

PhasePrCPA

PhasePrCPA class.

class

PhasePrEos

PhasePrEos class.

class

PhasePrEosvolcor

PhasePrEosvolcor class.

class

PhasePureComponentSolid

PhasePureComponentSolid class.

class

PhaseRK

PhaseRK class.

class

PhaseSolid

Abstract PhaseSolid class.

class

PhaseSolidComplex

PhaseSolidComplex class.

class

PhaseSoreideWhitson

PhaseSoreideWhitson implements the Søreide-Whitson Peng-Robinson EoS with modified alpha and mixing rule.

class

PhaseSpanWagnerEos

Phase implementation using the Span-Wagner reference equation for CO2.

class

PhaseSrkCPA

PhaseSrkCPA class.

class

PhaseSrkCPAs

PhaseSrkCPAs class.

class

PhaseSrkEos

PhaseSrkEos class.

class

PhaseSrkEosvolcor

PhasePrEosvolcor class.

class

PhaseSrkPenelouxEos

PhaseSrkPenelouxEos class.

class

PhaseTSTEos

PhaseTSTEos class.

class

PhaseUMRCPA

PhaseSrkCPA class.

class

PhaseVegaEos

PhaseVegaEos class.

class

PhaseWaterIAPWS

Phase implementation using the IAPWS-IF97 reference equations for pure water.

class

PhaseWax

PhaseWax class.

Fields in neqsim.thermo.phase declared as PhaseInterface

Modifier and Type

Field

Description

protected PhaseInterface[]

Phase.refPhase

Reference phase per component.

Methods in neqsim.thermo.phase that return PhaseInterface

Modifier and Type

Method

Description

PhaseInterface

PhaseInterface.clone()

clone.

PhaseInterface

Phase.getPhase()

getPhase.

PhaseInterface

PhaseInterface.getPhase()

getPhase.

PhaseInterface[]

Phase.getRefPhase()

Getter for property refPhase.

PhaseInterface

Phase.getRefPhase(int index)

Indexed getter for property refPhase.

PhaseInterface[]

PhaseInterface.getRefPhase()

Getter for property refPhase.

PhaseInterface

PhaseInterface.getRefPhase(int index)

Indexed getter for property refPhase.

Methods in neqsim.thermo.phase with parameters of type PhaseInterface

Modifier and Type

Method

Description

double

Phase.calcA(int comp, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

Phase.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

PhaseEos.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

PhaseInterface.calcA(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcA.

double

Phase.calcAi(int comp, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAi.

double

PhaseEos.calcAi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAi.

double

PhaseInterface.calcAi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAi.

double

Phase.calcAij(int compNumb, int j, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

PhaseEos.calcAij(int compNumb, int j, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

PhaseInterface.calcAij(int compNumb, int j, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAij.

double

Phase.calcAiT(int comp, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

PhaseEos.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

PhaseInterface.calcAiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAiT.

double

Phase.calcAT(int comp, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAT.

double

PhaseEos.calcAT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAT.

double

PhaseInterface.calcAT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcAT.

double

PhaseEos.calcATT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcATT.

double

Phase.calcB(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcB.

double

PhaseEos.calcB(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcB.

double

PhaseInterface.calcB(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcB.

double

Phase.calcBi(int comp, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBi.

double

PhaseEos.calcBi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBi.

double

PhaseInterface.calcBi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBi.

double

Phase.calcBij(int compNumb, int j, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBij.

double

PhaseEos.calcBij(int compNumb, int j, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBij.

double

PhaseInterface.calcBij(int compNumb, int j, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcBij.

double

PhasePrEosvolcor.calcC(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcC.

double

PhaseSrkEosvolcor.calcC(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcC.

double

PhasePrEosvolcor.calcCi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcCi.

double

PhaseSrkEosvolcor.calcCi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcCi.

double

PhasePrEosvolcor.calcCij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcCij.

double

PhaseSrkEosvolcor.calcCij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcCij.

double

PhasePrEosvolcor.calcCiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcCiT.

double

PhaseSrkEosvolcor.calcCiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcCiT.

void

PhaseGEUnifacUMRPRU.calcCommontemp(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

Calculate common temp.

double

PhasePrEosvolcor.calcCT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcCT.

double

PhaseSrkEosvolcor.calcCT(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcCT.

double

PhaseModifiedFurstElectrolyteEos.calcW(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcW.

double

PhaseModifiedFurstElectrolyteEosMod2004.calcW(PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcW.

double

PhaseModifiedFurstElectrolyteEos.calcWi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWi.

double

PhaseModifiedFurstElectrolyteEosMod2004.calcWi(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWi.

double

PhaseModifiedFurstElectrolyteEos.calcWij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWij.

double

PhaseModifiedFurstElectrolyteEosMod2004.calcWij(int compNumb, int compNumbj, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWij.

double

PhaseModifiedFurstElectrolyteEos.calcWiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWiT.

double

PhaseModifiedFurstElectrolyteEosMod2004.calcWiT(int compNumb, PhaseInterface phase, double temperature, double pressure, int numbcomp)

calcWiT.

double

Phase.geta(PhaseInterface phase, double temperature, double pressure, int numbcomp)

geta.

double

PhaseEos.geta(PhaseInterface phase, double temperature, double pressure, int numbcomp)

geta.

double

PhaseInterface.geta(PhaseInterface phase, double temperature, double pressure, int numbcomp)

geta.

double

Phase.getb(PhaseInterface phase, double temperature, double pressure, int numbcomp)

getb.

double

PhaseEos.getb(PhaseInterface phase, double temperature, double pressure, int numbcomp)

getb.

double

PhaseInterface.getb(PhaseInterface phase, double temperature, double pressure, int numbcomp)

getb.

double

PhaseEos.getdUdSdVn(PhaseInterface phase)

getdUdSdVn.

double

PhaseEos.getdUdVdVSn(PhaseInterface phase)

getdUdVdVSn.

double

PhaseDesmukhMather.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseDuanSun.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseGEInterface.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseGENRTL.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseGENRTLmodifiedHV.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseGENRTLmodifiedWS.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseGEUnifac.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseGEUnifacPSRK.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseGEUnifacUMRPRU.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseGEUniquac.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseGEUniquacmodifiedHV.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhaseGEWilson.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

double

PhasePitzer.getExcessGibbsEnergy(PhaseInterface phase, int numberOfComponents, double temperature, double pressure, PhaseType pt)

getExcessGibbsEnergy.

void

Phase.setParams(PhaseInterface phase, double[][] alpha, double[][] Dij, double[][] DijT, String[][] mixRule, double[][] intparam)

setParams.

void

PhaseGENRTLmodifiedHV.setParams(PhaseInterface phase, double[][] alpha, double[][] Dij, double[][] DijT, String[][] mixRule, double[][] intparam)

setParams.

void

PhaseInterface.setParams(PhaseInterface phase, double[][] alpha, double[][] Dij, double[][] DijT, String[][] mixRule, double[][] intparam)

setParams.

void

Phase.setProperties(PhaseInterface phase)

setProperties.

void

PhaseInterface.setProperties(PhaseInterface phase)

setProperties.

void

Phase.setRefPhase(int index, PhaseInterface refPhase)

Indexed setter for property refPhase.

void

Phase.setRefPhase(PhaseInterface[] refPhase)

Setter for property refPhase.

void

PhaseInterface.setRefPhase(int index, PhaseInterface refPhase)

Indexed setter for property refPhase.

void

PhaseInterface.setRefPhase(PhaseInterface[] refPhase)

Setter for property refPhase.

void

PhaseHydrate.setSolidRefFluidPhase(PhaseInterface refPhase)

setSolidRefFluidPhase.

void

PhaseSolid.setSolidRefFluidPhase(PhaseInterface refPhase)

setSolidRefFluidPhase.

Constructors in neqsim.thermo.phase with parameters of type PhaseInterface

Modifier

Constructor

Description

PhaseGENRTL(PhaseInterface phase, double[][] alpha, double[][] Dij, String[][] mixRule, double[][] intparam)

Constructor for PhaseGENRTL.

PhaseGENRTLmodifiedHV(PhaseInterface phase, double[][] alpha, double[][] Dij, double[][] DijT, String[][] mixRule, double[][] intparam)

Constructor for PhaseGENRTLmodifiedHV.

PhaseGENRTLmodifiedHV(PhaseInterface phase, double[][] alpha, double[][] Dij, String[][] mixRule, double[][] intparam)

Constructor for PhaseGENRTLmodifiedHV.

PhaseGENRTLmodifiedWS(PhaseInterface phase, double[][] alpha, double[][] Dij, double[][] DijT, String[][] mixRule, double[][] intparam)

Constructor for PhaseGENRTLmodifiedWS.

PhaseGENRTLmodifiedWS(PhaseInterface phase, double[][] alpha, double[][] Dij, String[][] mixRule, double[][] intparam)

Constructor for PhaseGENRTLmodifiedWS.

PhaseGEUnifac(PhaseInterface phase, double[][] alpha, double[][] Dij, String[][] mixRule, double[][] intparam)

Constructor for PhaseGEUnifac.

PhaseGEUnifacPSRK(PhaseInterface phase, double[][] alpha, double[][] Dij, String[][] mixRule, double[][] intparam)

Constructor for PhaseGEUnifacPSRK.

PhaseGEUnifacUMRPRU(PhaseInterface phase, double[][] alpha, double[][] Dij, String[][] mixRule, double[][] intparam)

Constructor for PhaseGEUnifacUMRPRU.

PhaseGEUniquac(PhaseInterface phase, double[][] alpha, double[][] Dij, String[][] mixRule, double[][] intparam)

Constructor for PhaseGEUniquac.

PhaseGEWilson(PhaseInterface phase, double[][] alpha, double[][] Dij, String[][] mixRule, double[][] intparam)

Constructor for PhaseGEWilson.
Uses of PhaseInterface in neqsim.thermo.system

Fields in neqsim.thermo.system declared as PhaseInterface

Modifier and Type

Field

Description

protected PhaseInterface[]

SystemThermo.phaseArray

Array containing all phases of System.

Methods in neqsim.thermo.system that return PhaseInterface

Modifier and Type

Method

Description

PhaseInterface

SystemInterface.getGasPhase()

getGasPhase.

final PhaseInterface

SystemThermo.getGasPhase()

getGasPhase.

default PhaseInterface

SystemInterface.getHydratePhase()

Get the hydrate phase if it exists.

PhaseInterface

SystemInterface.getLiquidPhase()

getLiquidPhase.

final PhaseInterface

SystemThermo.getLiquidPhase()

getLiquidPhase.

PhaseInterface

SystemInterface.getLowestGibbsEnergyPhase()

getLowestGibbsEnergyPhase.

PhaseInterface

SystemThermo.getLowestGibbsEnergyPhase()

getLowestGibbsEnergyPhase.

PhaseInterface

SystemInterface.getPhase(int i)

Get phase number i from SystemInterface object.

PhaseInterface

SystemInterface.getPhase(String phaseTypeName)

getPhase.

PhaseInterface

SystemInterface.getPhase(PhaseType pt)

getPhase.

final PhaseInterface

SystemThermo.getPhase(int i)

Get phase number i from SystemInterface object.

PhaseInterface

SystemThermo.getPhase(String phaseTypeName)

getPhase.

PhaseInterface

SystemThermo.getPhase(PhaseType pt)

getPhase.

PhaseInterface

SystemInterface.getPhaseOfType(String phaseTypeName)

return the phase of to specified type if the phase does not exist, the method will return null.

PhaseInterface

SystemThermo.getPhaseOfType(String phaseTypeName)

return the phase of to specified type if the phase does not exist, the method will return null.

PhaseInterface[]

SystemInterface.getPhases()

getPhases.

final PhaseInterface[]

SystemThermo.getPhases()

getPhases.

Methods in neqsim.thermo.system with parameters of type PhaseInterface

Modifier and Type

Method

Description

int

SystemInterface.getPhaseIndex(PhaseInterface phase)

Get property phaseIndex corresponding to a phase.

int

SystemThermo.getPhaseIndex(PhaseInterface phase)

Get property phaseIndex corresponding to a phase.

SystemInterface

SystemInterface.phaseToSystem(PhaseInterface newPhase)

phaseToSystem.

SystemInterface

SystemThermo.phaseToSystem(PhaseInterface newPhase)

phaseToSystem.

void

SystemInterface.replacePhase(int repPhase, PhaseInterface newPhase)

replacePhase.

void

SystemThermo.replacePhase(int repPhase, PhaseInterface newPhase)

replacePhase.

void

SystemInterface.setPhase(PhaseInterface phase, int index)

Set phaseArray[phaseIndex] = phase.

void

SystemThermo.setPhase(PhaseInterface phase, int index)

Set phaseArray[phaseIndex] = phase.
Uses of PhaseInterface in neqsim.thermo.util.gerg

Fields in neqsim.thermo.util.gerg declared as PhaseInterface

Modifier and Type

Field

Description

(package private) PhaseInterface

NeqSimAGA8Detail.phase

(package private) PhaseInterface

NeqSimEOSCG.phase

(package private) PhaseInterface

NeqSimGERG2008.phase

Methods in neqsim.thermo.util.gerg with parameters of type PhaseInterface

Modifier and Type

Method

Description

double

NeqSimAGA8Detail.getDensity(PhaseInterface phase)

getDensity.

double

NeqSimEOSCG.getDensity(PhaseInterface phase)

double

NeqSimGERG2008.getDensity(PhaseInterface phase)

getDensity.

double

NeqSimAGA8Detail.getMolarDensity(PhaseInterface phase)

getMolarDensity.

double

NeqSimEOSCG.getMolarDensity(PhaseInterface phase)

double

NeqSimGERG2008.getMolarDensity(PhaseInterface phase)

getMolarDensity.

double[]

NeqSimAGA8Detail.getProperties(PhaseInterface phase, String[] properties)

getProperties.

double[]

NeqSimEOSCG.getProperties(PhaseInterface phase, String[] properties)

double[]

NeqSimGERG2008.getProperties(PhaseInterface phase, String[] properties)

getProperties.

double[]

NeqSimAGA8Detail.propertiesDetail(PhaseInterface phase)

propertiesDetail.

double[]

NeqSimGERG2008.propertiesGERG(PhaseInterface phase)

propertiesGERG.

void

NeqSimAGA8Detail.setPhase(PhaseInterface phase)

Setter for the field phase.

void

NeqSimEOSCG.setPhase(PhaseInterface phase)

void

NeqSimGERG2008.setPhase(PhaseInterface phase)

Setter for the field phase.

Constructors in neqsim.thermo.util.gerg with parameters of type PhaseInterface

Modifier

Constructor

Description

NeqSimAGA8Detail(PhaseInterface phase)

Constructor for NeqSimAGA8Detail.

NeqSimEOSCG(PhaseInterface phase)

NeqSimGERG2008(PhaseInterface phase)

Constructor for NeqSimGERG2008.

NeqSimGERG2008(PhaseInterface phase, GERG2008Type modelType)

Constructor for NeqSimGERG2008 with specified model type.
Uses of PhaseInterface in neqsim.thermo.util.leachman

Fields in neqsim.thermo.util.leachman declared as PhaseInterface

Modifier and Type

Field

Description

(package private) PhaseInterface

NeqSimLeachman.phase

Methods in neqsim.thermo.util.leachman with parameters of type PhaseInterface

Modifier and Type

Method

Description

double

NeqSimLeachman.getDensity(PhaseInterface phase)

Get the density of the specified phase.

double

NeqSimLeachman.getMolarDensity(PhaseInterface phase)

Get the molar density of the specified phase.

double[]

NeqSimLeachman.getProperties(PhaseInterface phase, String[] properties)

Get specific thermodynamic properties of the specified phase.

double[]

NeqSimLeachman.propertiesLeachman(PhaseInterface phase)

Get various thermodynamic properties of the specified phase.

void

NeqSimLeachman.setPhase(PhaseInterface phase)

Setter for the field phase.

Constructors in neqsim.thermo.util.leachman with parameters of type PhaseInterface

Modifier

Constructor

Description

NeqSimLeachman(PhaseInterface phase, String hydrogenType)

Constructor for NeqSimLeachman.
Uses of PhaseInterface in neqsim.thermo.util.referenceequations

Fields in neqsim.thermo.util.referenceequations declared as PhaseInterface

Modifier and Type

Field

Description

private PhaseInterface

Ammonia2023.phase

Methods in neqsim.thermo.util.referenceequations with parameters of type PhaseInterface

Modifier and Type

Method

Description

void

Ammonia2023.setPhase(PhaseInterface phase)

Setter for the field phase.

Constructors in neqsim.thermo.util.referenceequations with parameters of type PhaseInterface

Modifier

Constructor

Description

Ammonia2023(PhaseInterface phase)

Constructor for Ammonia2023.
Uses of PhaseInterface in neqsim.thermo.util.Vega

Fields in neqsim.thermo.util.Vega declared as PhaseInterface

Modifier and Type

Field

Description

(package private) PhaseInterface

NeqSimVega.phase

Methods in neqsim.thermo.util.Vega with parameters of type PhaseInterface

Modifier and Type

Method

Description

double

NeqSimVega.getDensity(PhaseInterface phase)

getDensity.

double

NeqSimVega.getMolarDensity(PhaseInterface phase)

getMolarDensity.

double[]

NeqSimVega.getProperties(PhaseInterface phase, String[] properties)

getProperties.

double[]

NeqSimVega.propertiesVega(PhaseInterface phase)

propertiesGERG.

void

NeqSimVega.setPhase(PhaseInterface phase)

Setter for the field phase.

Constructors in neqsim.thermo.util.Vega with parameters of type PhaseInterface

Modifier

Constructor

Description

NeqSimVega(PhaseInterface phase)

Constructor for NeqSimGERG2008.

Uses of Interfaceneqsim.thermo.phase.PhaseInterface

Uses of PhaseInterface in neqsim.blackoil

Uses of PhaseInterface in neqsim.chemicalreactions

Uses of PhaseInterface in neqsim.chemicalreactions.chemicalreaction

Uses of PhaseInterface in neqsim.chemicalreactions.kinetics

Uses of PhaseInterface in neqsim.mathlib.nonlinearsolver

Uses of PhaseInterface in neqsim.physicalproperties

Uses of PhaseInterface in neqsim.physicalproperties.methods.liquidphysicalproperties.diffusivity

Uses of PhaseInterface in neqsim.physicalproperties.mixingrule

Uses of PhaseInterface in neqsim.physicalproperties.system

Uses of PhaseInterface in neqsim.physicalproperties.system.commonphasephysicalproperties

Uses of PhaseInterface in neqsim.physicalproperties.system.gasphysicalproperties

Uses of PhaseInterface in neqsim.physicalproperties.system.liquidphysicalproperties

Uses of PhaseInterface in neqsim.physicalproperties.system.solidphysicalproperties

Uses of PhaseInterface in neqsim.thermo.component

Uses of PhaseInterface in neqsim.thermo.mixingrule

Uses of PhaseInterface in neqsim.thermo.phase

Uses of PhaseInterface in neqsim.thermo.system

Uses of PhaseInterface in neqsim.thermo.util.gerg

Uses of PhaseInterface in neqsim.thermo.util.leachman

Uses of PhaseInterface in neqsim.thermo.util.referenceequations

Uses of PhaseInterface in neqsim.thermo.util.Vega

Uses of Interface
neqsim.thermo.phase.PhaseInterface