| Cantera 3.0.0

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Here is a list of all documented class members with links to the class documentation for each member:

### - t -

- T_Basis_Opts : VCS_COUNTERS
- T_Calls_Inest : VCS_COUNTERS
- T_Calls_vcs_TP : VCS_COUNTERS
- T_fixed() : StFlow
- T_Its : VCS_COUNTERS
- T_Time_basopt : VCS_COUNTERS
- T_Time_inest : VCS_COUNTERS
- T_Time_vcs : VCS_COUNTERS
- T_Time_vcs_TP : VCS_COUNTERS
- Tabulated1() : Tabulated1
- tau : WaterPropsIAPWS
- TAUp : WaterPropsIAPWSphi
- TAUsave : WaterPropsIAPWSphi
- TAUsqrt : WaterPropsIAPWSphi
- TCoeff_ : PDSS_SSVol
- Tcrit() : WaterPropsIAPWS, CarbonDioxide, Heptane, HFC134a, hydrogen, methane, nitrogen, oxygen, Substance, water
- tdpolycalc() : WaterPropsIAPWSphi
- Temp() : Substance
- Temp_ : vcs_VolPhase
- temperature() : Boundary1D, MultiPhase, PDSS, Phase, ReactionData, ReactorBase, WaterPropsIAPWS
- temperatureExponent() : ArrheniusBase
- temperaturePolySize() : Nasa9Poly1, Nasa9PolyMultiTempRegion, NasaPoly1, NasaPoly2, ShomatePoly2, ShomatePoly, SpeciesThermoInterpType
- tempOK() : MultiPhase
- thermalConductivity() : HighPressureGasTransport, IonGasTransport, MixTransport, MultiTransport, Transport, WaterTransport
- thermalExpansionCoeff() : IdealGasPhase, IdealMolalSoln, PDSS, PDSS_Water, PengRobinson, PureFluidPhase, RedlichKwongMFTP, StoichSubstance, ThermoPhase, WaterSSTP
- thermo() : Interface, Kinetics, ReactorSurface, Solution, SolutionArray, Species, Transport
- thermo_mutex : ThermoFactory
- thermo_warnings_suppressed() : Application
- ThermoFactory() : ThermoFactory
- ThermoPhase() : ThermoPhase
- theta_ : LatticeSolidPhase
- thirdBody() : Reaction
- ThirdBody() : ThirdBody
- thirdBodyConcentrations() : BulkKinetics, Kinetics
- thread_complete() : Application
- ThreadMessages() : Application::ThreadMessages
- threadMsgMap_t : Application::ThreadMessages
- threshold() : AdaptivePreconditioner
- throwUndefinedElements() : Phase
- time() : ReactorNet
- Time_basopt : VCS_COUNTERS
- Time_vcs_TP : VCS_COUNTERS
- timeIsIndependent() : FlowReactor, Reactor
- timeStep() : OneDim
- timeStepStats() : OneDim
- Tmax() : ChebyshevRate, CarbonDioxide, Heptane, HFC134a, hydrogen, methane, nitrogen, oxygen, Substance, water
- Tmax_ : ChebyshevRate
- Tmin() : ChebyshevRate, CarbonDioxide, Heptane, HFC134a, hydrogen, methane, nitrogen, oxygen, Substance, water
- tmpNM : PDSS_IonsFromNeutral
- tmpV_ : LatticeSolidPhase
- toArray() : Domain1D
- totalMoles() : vcs_VolPhase
- totalMolesInert() : vcs_VolPhase
- toYamlFile() : YamlWriter
- toYamlString() : YamlWriter
- TP_ptr : vcs_VolPhase
- TPhInertMoles : VCS_SOLVE
- TPX_Substance() : PureFluidPhase
- transferElementsFM() : vcs_VolPhase
- transient() : Domain1D, OneDim
- transient_atol() : Domain1D
- transient_rtol() : Domain1D
- transport() : Solution
- Transport() : Transport
- transport_mutex : TransportFactory
- TransportFactory : DustyGasTransport, TransportFactory
- transportModel() : DustyGasTransport, HighPressureGasTransport, IonGasTransport, MixTransport, MultiTransport, StFlow, Transport, UnityLewisTransport, WaterTransport
- transportType() : Transport
- TrDen_ : ChebyshevRate
- TroeRate() : TroeRate
- TsangRate() : TsangRate
- Tsat() : Substance
- tstar : MMCollisionInt
- TwoPhase() : Substance
- TwoTempPlasmaRate() : TwoTempPlasmaRate
- type() : AnyValue, Arrhenius1, ArrheniusRate, BinarySolutionTabulatedThermo, BlowersMaselRate, Boundary1D, ChebyshevRate, Composite1, Const1, ConstPressureMoleReactor, ConstPressureReactor, Cos1, CoverageDependentSurfPhase, CustomFunc1Rate, DebyeHuckel, Diff1, Domain1D, EdgePhase, Empty1D, Exp1, FalloffRate, FlowDevice, FlowReactor, Fourier1, Func1, Gaussian1, HMWSoln, IdealGasConstPressureMoleReactor, IdealGasConstPressureReactor, IdealGasMoleReactor, IdealGasPhase, IdealGasReactor, IdealMolalSoln, IdealSolidSolnPhase, IdealSolnGasVPSS, Inlet1D, InterfaceRate< RateType, DataType >, IonFlow, IonsFromNeutralVPSSTP, LatticePhase, LatticeSolidPhase, Log1, MargulesVPSSTP, MaskellSolidSolnPhase, MassFlowController, MetalPhase, MixtureFugacityTP, MoleReactor, MultiRate< RateType, DataType >, MultiRateBase, Outlet1D, OutletRes1D, PengRobinson, Periodic1, Phase, PlasmaPhase, PlogRate, PlusConstant1, Poly1, Pow1, PressureController, Product1, PureFluidPhase, Ratio1, ReactingSurf1D, Reaction, ReactionRate, ReactionRateDelegator, Reactor, ReactorBase, RedlichKisterVPSSTP, RedlichKwongMFTP, Reservoir, Sin1, SingleSpeciesTP, StFlow, StickingRate< RateType, DataType >, StoichSubstance, Sum1, Surf1D, SurfPhase, Symm1D, Tabulated1, ThermoPhase, TimesConstant1, TwoTempPlasmaRate, Valve, Wall, WallBase, WaterSSTP
- type_str() : AnyValue
- typeName() : Func1