teqp
0.22.0
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Class List
Here are the classes, structs, unions and interfaces with brief descriptions:
[detail level
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►
N
teqp
►
N
activity
►
N
activity_models
►
N
COSMOSAC
C
CombinatorialConstants
C
COSMO3
C
COSMO3Constants
C
FluidSigmaProfiles
C
SigmaProfile
C
BinaryInvariantResidualHelmholtzOverRT
C
NullResidualHelmholtzOverRT
C
WilsonResidualHelmholtzOverRT
►
N
algorithms
►
N
phase_equil
C
AbstractSpecification
C
BetaSpecification
Specification of molar phase fraction in given phase
C
CaloricPhaseDerivatives
►
C
GeneralizedPhaseEquilibrium
C
CallResult
C
UnpackedVariables
C
MolarEnthalpySpecification
Specification equation for molar enthalpy
C
MolarEntropySpecification
Specification equation for molar entropy
C
MolarInternalEnergySpecification
Specification equation for molar internal energy
C
MolarVolumeSpecification
Specification equation for molar volume
C
PSpecification
Specification equation for pressure
C
RequiredPhaseDerivatives
C
SpecificationSidecar
C
TSpecification
►
N
pure_param_optimization
C
PureParameterOptimizer
C
PVTNoniterativePoint
C
SatRhoLPoint
C
SatRhoLPPoint
C
SatRhoLPWPoint
C
SOSPoint
►
N
association
►
C
Association
C
IndexMapper
C
AssociationOptions
C
CanonicalData
C
DufalData
►
N
CPA
C
AssociationVariantWrapper
C
CPAAssociation
C
CPACubic
C
CPAEOS
►
N
cppinterface
►
N
adapter
►
N
internal
C
tag
C
ConstViewer
C
DerivativeAdapter
C
Owner
C
OwnershipSummer
A collection type that allows you to sum contributions from multiple EOS terms
C
AbstractModel
C
IterationMatrices
►
N
CubicSuperAncillary
C
Chebyshev
C
SuperAncillary
►
N
ECSHuberEly
C
ECSHuberEly1994
►
N
exp6
C
Kataoka1992
►
N
FEANN
C
ChaparroJCP2023
►
N
GERG2004
C
GERG2004IdealGasModel
C
GERG2004ResidualModel
►
N
GERG2008
C
GERG2008IdealGasModel
C
GERG2008ResidualModel
►
N
GERGGeneral
C
AlphaigCoeffs
C
BetasGammas
C
DepartureCoeffs
C
GERG200XAlphaig
C
GERG200XCorrespondingStatesTerm
C
GERG200XDepartureFunction
C
GERG200XDepartureTerm
C
GERG200XPureFluidEOS
►
C
GERG200XReducing
C
Matrices
C
TcVc
C
PureCoeffs
C
PureInfo
►
N
iteration
C
AlphaModel
C
MaxAbsErrorCondition
C
MinRelStepsizeCondition
C
NanXDXErrorCondition
C
NegativeXErrorCondition
C
NRIterator
C
NRIteratorResult
C
StepCountErrorCondition
C
StoppingCondition
C
StoppingData
►
N
LJChain
C
LJChain
►
N
LKP
C
LKPFluidParameters
C
LKPMix
►
N
Mie
C
Mie6Pohl2023
►
N
mie
►
N
lennardjones
►
N
Johnson
C
LJ126Johnson1993
►
N
Kolafa
C
LJ126KolafaNezbeda1994
►
N
multifluid
►
N
gasconstant
C
CODATA
C
MoleFractionWeighted
►
N
multifluid_activity
C
MultifluidPlusActivity
►
N
saft
►
N
genericsaft
C
GenericSAFT
►
N
PCSAFT
C
PCSAFTPureGrossSadowski2001
►
N
pcsaft
C
PCSAFTHardChainContribution
C
PCSAFTLibrary
Manager class for
PCSAFT
coefficients
C
PCSAFTMixture
C
SAFTCoeffs
Coefficients for one fluid
►
N
polar_terms
►
N
GrossVrabec
C
DipolarContributionGrossVrabec
C
DipolarQuadrupolarContributionVrabecGross
C
MultipolarContributionGrossVrabec
C
MultipolarContributionGrossVrabecTerms
C
QuadrupolarContributionGross
►
N
softsaft
C
SoftSAFT
►
N
SAFTpolar
C
GottschalkJIntegral
C
GottschalkKIntegral
C
GubbinsTwuJIntegral
C
GubbinsTwuKIntegral
C
LuckasJIntegral
C
LuckasKIntegral
C
MultipolarContributionGrayGubbins
C
MultipolarContributionGubbinsTwu
C
PolarizableArrays
►
N
SAFTVRMie
C
SAFTVRMieChainContributionTerms
Things that only depend on the components themselves, but not on composition, temperature, or density
C
SAFTVRMieCoeffs
Coefficients for one fluid
C
SAFTVRMieMixture
A class used to evaluate mixtures using the SAFT-VR-Mie model
C
SAFTVRMieNonpolarMixture
A class used to evaluate mixtures using the SAFT-VR-Mie model
►
N
squarewell
C
EspindolaHeredia2009
►
N
twocenterljf
C
AttractiveContribution
C
DipolarContribution
C
HardSphereContribution
C
ParameterContainer
C
QuadrupolarContribution
C
ReducingDensity
C
ReducingTemperature
C
Twocenterljf
►
N
VLLE
C
SelfIntersectionSolution
C
VLLEFinderOptions
C
VLLETracerOptions
C
AdvancedPRaEres
C
BasicAlphaFunction
The standard alpha function used by Peng-Robinson and SRK
C
Chebyshev2DEOSTerm
C
CorrespondingStatesContribution
►
C
CriticalTracing
C
psi1derivs
C
DepartureContribution
C
DerivativeHolderSquare
C
DoubleExponentialEOSTerm
C
EigenData
C
EOSTermContainer
C
ExponentialEOSTerm
C
Functor
C
GaoBEOSTerm
C
GaussianEOSTerm
C
GenericCubic
C
GenericCubicTerm
C
GERG2004EOSTerm
C
hybrj_functor__mix_VLE_Tp
C
IdealHelmholtz
Ideal-gas Helmholtz energy container
C
IdealHelmholtzConstant
C
IdealHelmholtzCp0Constant
C
IdealHelmholtzCp0PowerT
C
IdealHelmholtzGERG2004Cosh
C
IdealHelmholtzGERG2004Sinh
C
IdealHelmholtzLead
C
IdealHelmholtzLogT
C
IdealHelmholtzPlanckEinstein
C
IdealHelmholtzPlanckEinsteinGeneralized
C
IdealHelmholtzPowerT
C
InvalidArgument
C
InvalidValue
C
is_complex_t
C
is_complex_t< std::complex< T > >
C
is_container
C
is_container< std::valarray< Ts... > >
C
is_container< std::vector< Ts... > >
C
is_eigen_impl
C
is_eigen_impl< Eigen::Array< T, Is... > >
C
is_eigen_impl< Eigen::Matrix< T, Is... > >
C
is_mcx_t
C
IsochoricDerivatives
C
IsothermPureVLEResiduals
C
IterationFailure
C
JSONValidationError
Validation of a JSON schema failed
C
JSONValidator
C
JustPowerEOSTerm
C
Lemmon2005EOSTerm
C
MathiasCopemanAlphaFunction
The Mathias-Copeman alpha function used by Peng-Robinson and SRK
C
MixVLEpxFlags
C
MixVLEReturn
C
MixVLETpFlags
C
ModelContainer
C
MultiFluid
C
MultiFluidAdapter
C
MultiFluidAdapter_Ecs
C
MultiFluidInvariantReducingFunction
C
MultifluidPlusAssociation
C
MultiFluidReducingFunction
C
MultiFluidVLEAncillaries
C
NonAnalyticEOSTerm
C
NotImplementedError
C
NullEOSTerm
C
PCSAFTGrossSadowski2001Term
►
C
PowerEOSTerm
C
PowerEOSTermCoeffs
C
PureIdealHelmholtz
C
PVLEOptions
C
QuantumCorrectedPR
C
Reducing_ECS
C
ReducingTermContainer
C
RKPRCismondi2005
C
TCABOptions
C
TDXDerivatives
C
teqpcException
C
teqpException
C
Timer
C
TVLEOptions
C
TwuAlphaFunction
The Twu alpha function used by Peng-Robinson and SRK
C
vdWEOS
A slightly more involved implementation of van der Waals, this time with mixture properties
C
vdWEOS1
A (very) simple implementation of the van der Waals EOS
C
VirialDerivatives
C
VLEAncillary
C
wrt_helper
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