Interface PhaseEosInterface

All Superinterfaces:

Cloneable, PhaseInterface, Serializable, ThermodynamicConstantsInterface

All Known Subinterfaces:

PhaseCPAInterface

All Known Implementing Classes:

PhaseAmmoniaEos, PhaseBNS, PhaseBWRSEos, PhaseCSPsrkEos, PhaseElectrolyteCPA, PhaseElectrolyteCPAMM, PhaseElectrolyteCPAOld, PhaseElectrolyteCPAstatoil, PhaseEos, PhaseEOSCGEos, PhaseGERG2004Eos, PhaseGERG2008Eos, PhaseLeachmanEos, PhaseModifiedFurstElectrolyteEos, PhaseModifiedFurstElectrolyteEosMod2004, PhasePCSAFT, PhasePCSAFTa, PhasePCSAFTRahmat, PhasePrCPA, PhasePrEos, PhasePrEosvolcor, PhasePureComponentSolid, PhaseRK, PhaseSolid, PhaseSolidComplex, PhaseSoreideWhitson, PhaseSpanWagnerEos, PhaseSrkCPA, PhaseSrkCPAs, PhaseSrkEos, PhaseSrkEosvolcor, PhaseSrkPenelouxEos, PhaseTSTEos, PhaseUMRCPA, PhaseVegaEos, PhaseWaterIAPWS, PhaseWax

public interface PhaseEosInterface
extends PhaseInterface

PhaseEosInterface interface.

Version:

$Id: $Id

Author:

Even Solbraa

Field Summary

Fields inherited from interface ThermodynamicConstantsInterface

atm, avagadroNumber, boltzmannConstant, electronCharge, faradayConstant, gravity, molarMassAir, normalStateTemperature, pi, planckConstant, R, referencePressure, referenceTemperature, standardStateTemperature, vacumPermittivity

Method Summary

Modifier and Type	Method	Description
double	calcPressure()	calcPressure.
double	calcPressuredV()	calcPressuredV.
double	dFdN(int i)	dFdN.
double	dFdNdN(int i, int j)	dFdNdN.
double	dFdNdT(int i)	dFdNdT.
double	dFdNdV(int i)	dFdNdV.
void	displayInteractionCoefficients(String intType)	displayInteractionCoefficients.
double	F()	F.
double	getAresTV()	getAresTV.
EosMixingRulesInterface	getEosMixingRule()	getEosMixingRule.
String	getMixingRuleName()	getMixingRuleName.
double	getMolarVolume()	method to return molar volume of the phase note: without Peneloux volume correction.
double	getPressureAttractive()	getPressureAttractive.
double	getPressureRepulsive()	getPressureRepulsive.
double	getSresTV()	getSresTV.

Methods inherited from interface PhaseInterface

addComponent, addMoles, addMolesChemReac, addMolesChemReac, calcA, calcAi, calcAij, calcAiT, calcAT, calcB, calcBi, calcBij, calcMolarVolume, calcR, clone, dFdT, dFdTdT, dFdTdV, dFdV, dFdVdV, fb, FB, fBB, FBB, FBD, FBT, fBV, FBV, FD, FDT, FDV, Fn, FnB, FnV, FT, FTT, FTV, fv, FV, fVV, FVV, gb, gBB, gBV, geta, getA, getActivityCoefficient, getActivityCoefficient, getActivityCoefficient, getActivityCoefficientSymetric, getActivityCoefficientUnSymetric, getAlpha0_EOSCG, getAlpha0_GERG2008, getAlpha0_Leachman, getAlpha0_Leachman, getAlpha0_Vega, getAlphares_EOSCG, getAlphares_GERG2008, getAlphares_Leachman, getAlphares_Leachman, getAlphares_Vega, getAntoineVaporPressure, getAT, getATT, getb, getB, getBeta, getComponent, getComponent, getcomponentArray, getComponentNames, getComponents, getComponentWithIndex, getComposition, getCompressibilityX, getCompressibilityY, getCorrectedVolume, getCp, getCp, getCp0, getCpres, getCv, getCv, getDensity, getDensity, getDensity_AGA8, getDensity_EOSCG, getDensity_GERG2008, getDensity_Leachman, getDensity_Leachman, getDensity_Vega, getdPdrho, getdPdTVn, getdPdVTn, getdrhodN, getdrhodP, getdrhodT, getEnthalpy, getEnthalpy, getEnthalpydP, getEnthalpydT, getEntropy, getEntropy, getEntropydP, getEntropydT, getExcessGibbsEnergy, getExcessGibbsEnergySymetric, getFlowRate, getFugacity, getFugacity, getg, getGamma, getGamma2, getGibbsEnergy, getGresTP, getHelmholtzEnergy, getHresTP, getInfiniteDiluteFugacity, getInitType, getInternalEnergy, getInternalEnergy, getIsobaricThermalExpansivity, getIsothermalCompressibility, getJouleThomsonCoefficient, getJouleThomsonCoefficient, getKappa, getLogActivityCoefficient, getLogInfiniteDiluteFugacity, getLogInfiniteDiluteFugacity, getLogPureComponentFugacity, getMass, getMeanIonicActivity, getMixGibbsEnergy, getMixingRule, getMixingRuleType, getModelName, getMolalMeanIonicActivity, getMolarComposition, getMolarMass, getMolarMass, getMolarVolume, getMoleFraction, getNumberOfComponents, getNumberOfIonicComponents, getNumberOfMolecularComponents, getNumberOfMolesInPhase, getOsmoticCoefficient, getOsmoticCoefficientOfWater, getOsmoticCoefficientOfWaterMolality, getpH, getpH, getPhase, getPhaseFraction, getPhaseTypeName, getPhysicalProperties, getPhysicalPropertyModel, getPressure, getPressure, getProperties_EOSCG, getProperties_GERG2008, getProperties_Leachman, getProperties_Leachman, getProperties_Vega, getPseudoCriticalPressure, getPseudoCriticalTemperature, getPureComponentFugacity, getPureComponentFugacity, getRefPhase, getRefPhase, getSoundSpeed, getSoundSpeed, getSresTP, getTemperature, getTemperature, getThermalConductivity, getThermalConductivity, getTotalVolume, getType, getViscosity, getViscosity, getVolume, getVolume, getWaterDensity, getWtFrac, getWtFrac, getWtFraction, getWtFractionOfWaxFormingComponents, getZ, getZvolcorr, gV, gVV, hasComponent, hasComponent, hasPlusFraction, hasTBPFraction, init, init, init, initPhysicalProperties, initPhysicalProperties, initPhysicalProperties, initRefPhases, isAsphalteneRich, isConstantPhaseVolume, isMixingRuleDefined, molarVolume, normalize, removeComponent, resetMixingRule, resetPhysicalProperties, setAttractiveTerm, setBeta, setComponentArray, setConstantPhaseVolume, setEmptyFluid, setInitType, setMixingRule, setMixingRule, setMixingRuleGEModel, setMolarVolume, setMoleFractions, setNumberOfComponents, setParams, setPhaseTypeName, setPhysicalProperties, setPhysicalProperties, setPhysicalPropertyModel, setPpm, setPressure, setProperties, setRefPhase, setRefPhase, setTemperature, setTotalVolume, setType, useVolumeCorrection, useVolumeCorrection

Method Details

getMolarVolume

double getMolarVolume()

method to return molar volume of the phase note: without Peneloux volume correction.

Specified by:

getMolarVolume in interface PhaseInterface

Returns:

molar volume volume in unit m3/mol*1e5

getEosMixingRule

EosMixingRulesInterface getEosMixingRule()

getEosMixingRule.

Returns:

a EosMixingRulesInterface object

getMixingRuleName

String getMixingRuleName()

getMixingRuleName.

Returns:

a String object

calcPressure

double calcPressure()

calcPressure.

Returns:

a double

calcPressuredV

double calcPressuredV()

calcPressuredV.

Returns:

a double

getPressureRepulsive

double getPressureRepulsive()

getPressureRepulsive.

Returns:

a double

getPressureAttractive

double getPressureAttractive()

getPressureAttractive.

Returns:

a double

displayInteractionCoefficients

void displayInteractionCoefficients(String intType)

displayInteractionCoefficients.

Parameters:

intType - a String object

F

double F()

F.

Returns:

a double

dFdN

double dFdN(int i)

dFdN.

Parameters:

i - a int

Returns:

a double

dFdNdN

double dFdNdN(int i,
 int j)

dFdNdN.

Parameters:

i - a int

j - a int

Returns:

a double

dFdNdV

double dFdNdV(int i)

dFdNdV.

Parameters:

i - a int

Returns:

a double

dFdNdT

double dFdNdT(int i)

dFdNdT.

Parameters:

i - a int

Returns:

a double

getAresTV

double getAresTV()

getAresTV.

Returns:

a double

getSresTV

double getSresTV()

getSresTV.

Returns:

a double