Uses of Class
neqsim.util.exception.TooManyIterationsException

Packages that use TooManyIterationsException
Package
Description
neqsim.thermo.phase
 
neqsim.thermodynamicoperations.flashops
 

  • Uses of TooManyIterationsException in neqsim.thermo.phase

    Methods in neqsim.thermo.phase that throw TooManyIterationsException
    Modifier and Type
    Method
    Description
    double
    PhaseCSPsrkEos.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseDefault.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseDesmukhMather.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseDuanSun.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseElectrolyteCPA.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseElectrolyteCPAOld.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseEos.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseGENRTL.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseGERG2004Eos.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseGERG2008Eos.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseGEUniquac.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseGEWilson.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseHydrate.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseIdealGas.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseInterface.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseLeachmanEos.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseModifiedFurstElectrolyteEos.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseModifiedFurstElectrolyteEosMod2004.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhasePCSAFT.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhasePCSAFTa.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhasePCSAFTRahmat.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhasePitzer.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseSAFTVRMie.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseSrkCPA.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseSrkCPAandersonMixing.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseSrkCPAandersonReduced.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseSrkCPABroydenImplicit.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseSrkCPAfullyImplicit.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseSrkCPAfullyImplicitReduced.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseSrkCPAreduced.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseUMRCPA.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseVegaEos.molarVolume(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume.
    double
    PhaseBWRSEos.molarVolume2(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume2.
    double
    PhaseElectrolyteCPA.molarVolume2(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume2.
    double
    PhaseElectrolyteCPAOld.molarVolume2(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume2.
    double
    PhaseEos.molarVolume2(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume2.
    double
    PhaseSrkCPA.molarVolume2(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume2.
    double
    PhaseUMRCPA.molarVolume2(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume2.
    double
    PhasePCSAFT.molarVolume22(double pressure, double temperature, double A, double B, int phaseNum)
    molarVolume22.
    double
    PhaseElectrolyteCPAOld.molarVolume3(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolume3.
    double
    PhaseElectrolyteCPA.molarVolumeChangePhase(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeChangePhase.
    double
    PhaseSrkCPA.molarVolumeChangePhase(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeChangePhase.
    double
    PhaseSrkCPAandersonMixing.molarVolumeChangePhase(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeChangePhase.
    double
    PhaseSrkCPAandersonReduced.molarVolumeChangePhase(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeChangePhase.
    double
    PhaseSrkCPABroydenImplicit.molarVolumeChangePhase(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeChangePhase.
    double
    PhaseSrkCPAfullyImplicit.molarVolumeChangePhase(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeChangePhase.
    double
    PhaseSrkCPAfullyImplicitReduced.molarVolumeChangePhase(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeChangePhase.
    double
    PhaseSrkCPAreduced.molarVolumeChangePhase(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeChangePhase.
    double
    PhaseUMRCPA.molarVolumeChangePhase(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeChangePhase.
    double
    PhaseSrkCPA.molarVolumeOld(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeOld.
    double
    PhaseUMRCPA.molarVolumeOld(double pressure, double temperature, double A, double B, PhaseType pt)
    molarVolumeOld.

  • Uses of TooManyIterationsException in neqsim.thermodynamicoperations.flashops

    Methods in neqsim.thermodynamicoperations.flashops that throw TooManyIterationsException
    Modifier and Type
    Method
    Description
    double
    RachfordRice.calcBeta(double[] K, double[] z)
    calcBeta.
    double
    RachfordRice.calcBetaMichelsen2001(double[] K, double[] z)
    calcBeta.
    double
    RachfordRice.calcBetaNielsen2023(double[] K, double[] z)
    calcBetaNielsen2023.
    final double
    RachfordRice.calcBetaS(SystemInterface system)
    calcBetaS.
    void
    Flash.stabilityAnalysis()
    stabilityAnalysis.