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Functions7,525 in github.com/Cantera/cantera

↓ 1 callersMethodsetDensityPolynomial
src/thermo/PDSS_SSVol.cpp:28
↓ 1 callersMethodsetEmissivity
Set the emissivity.
include/cantera/zeroD/Wall.h:207
↓ 1 callersMethodsetExceptionType
include/cantera/cython/funcWrapper.h:49
↓ 1 callersMethodsetExceptionValue
include/cantera/cython/funcWrapper.h:58
↓ 1 callersMethodsetExpansionRateCoeff
Set the expansion rate coefficient.
include/cantera/zeroD/Wall.h:221
↓ 1 callersMethodsetExplicitThirdBodyDuplicateHandling
src/kinetics/Kinetics.cpp:92
↓ 1 callersMethodsetFixedTempProfile
Sometimes it is desired to carry out the simulation using a specified temperature profile, rather than computing it by solving the energy equation. Th
include/cantera/oneD/Flow1D.h:155
↓ 1 callersMethodsetFlatProfile
src/oneD/Sim1D.cpp:319
↓ 1 callersMethodsetFlow
include/cantera/kinetics/ReactionPath.h:129
↓ 1 callersMethodsetFont
Set name of the font used.
include/cantera/kinetics/ReactionPath.h:292
↓ 1 callersMethodsetGridCache
src/thermo/EEDFTwoTermApproximation.cpp:519
↓ 1 callersMethodsetHeader
src/base/YamlWriter.cpp:19
↓ 1 callersMethodsetHeatFlux
Specify the heat flux function @f$ q_0(t) @f$. @deprecated To be removed after %Cantera 3.2. Replaceable by version using shared pointer.
include/cantera/zeroD/Wall.h:165
↓ 1 callersMethodsetHeatTransferCoeff
Set the overall heat transfer coefficient [W/m^2/K].
include/cantera/zeroD/Wall.h:197
↓ 1 callersMethodsetID
Specify an identifying tag for this domain.
include/cantera/oneD/Domain1D.h:466
↓ 1 callersMethodsetIlutDropTol
Set drop tolerance for ILUT @param droptol double value used in setting solver drop tolerance
include/cantera/numerics/AdaptivePreconditioner.h:60
↓ 1 callersMethodsetIlutFillFactor
Set the fill factor for ILUT solver @param fillFactor fill in factor for ILUT solver
include/cantera/numerics/AdaptivePreconditioner.h:67
↓ 1 callersMethodsetInitialMixMoles
include/cantera/equil/MultiPhaseEquil.h:75
↓ 1 callersMethodsetJacAge
src/numerics/SteadyStateSystem.cpp:290
↓ 1 callersMethodsetLatticeStoichiometry
src/thermo/LatticeSolidPhase.cpp:383
↓ 1 callersMethodsetLeftControlPointCoordinate
src/oneD/Flow1D.cpp:1201
↓ 1 callersMethodsetLeftControlPointTemperature
src/oneD/Flow1D.cpp:1186
↓ 1 callersMethodsetLinearGrid
src/thermo/EEDFTwoTermApproximation.cpp:31
↓ 1 callersMethodsetLoc
src/base/SolutionArray.cpp:769
↓ 1 callersMethodsetMassFlowCoeff
Set the mass flow coefficient. ! * *m* has units of kg/s. The mass flow rate is computed as: * * where *g* is a function of time that i
include/cantera/zeroD/flowControllers.h:47
↓ 1 callersMethodsetMaxIonicStrength
include/cantera/thermo/HMWSoln.h:1126
↓ 1 callersMethodsetMaxStepSize
src/numerics/IdasIntegrator.cpp:151
↓ 1 callersMethodsetMaxTemp
include/cantera/thermo/ShomatePoly.h:258
↓ 1 callersMethodsetMaxTimeStep
src/zeroD/ReactorNet.cpp:54
↓ 1 callersMethodsetMaxTimeStepCount
Set the maximum number of timeteps allowed before successful steady-state solve
include/cantera/numerics/SteadyStateSystem.h:212
↓ 1 callersMethodsetMeanParticleDiameter
src/transport/DustyGasTransport.cpp:221
↓ 1 callersMethodsetMeanPoreRadius
src/transport/DustyGasTransport.cpp:215
↓ 1 callersMethodsetMinTemp
include/cantera/thermo/ShomatePoly.h:253
↓ 1 callersMethodsetMoleFractions
src/thermo/LatticeSolidPhase.cpp:171
↓ 1 callersMethodsetMolecularWeight
src/thermo/Phase.cpp:913
↓ 1 callersMethodsetMolecularWeight
src/thermo/PDSS.cpp:147
↓ 1 callersMethodsetMolesByName
src/equil/MultiPhase.cpp:359
↓ 1 callersMethodsetName
src/kinetics/Reaction.cpp:777
↓ 1 callersMethodsetNeedsReinit
Called to trigger integrator reinitialization before further integration.
include/cantera/zeroD/ReactorNet.h:336
↓ 1 callersMethodsetOmega
src/thermo/PDSS_HKFT.cpp:339
↓ 1 callersMethodsetParent
Set the parent VPStandardStateTP object of this PDSS object ! * This information is only used by certain PDSS subclasses * @param phase Po
include/cantera/thermo/PDSS.h:376
↓ 1 callersMethodsetPorosity
src/transport/DustyGasTransport.cpp:201
↓ 1 callersMethodsetPressure
src/thermo/LatticeSolidPhase.cpp:152
↓ 1 callersMethodsetPressureCoeff
Set the proportionality constant between pressure drop and mass flow rate.
include/cantera/zeroD/flowControllers.h:120
↓ 1 callersMethodsetPressureFunction
src/zeroD/FlowDevice.cpp:82
↓ 1 callersMethodsetProfile
src/oneD/Sim1D.cpp:75
↓ 1 callersMethodsetPtrThermoPhase
src/equil/vcs_VolPhase.cpp:551
↓ 1 callersFunctionsetPythonHome
src/extensions/pythonShim.cpp:39
↓ 1 callersMethodsetRateUnits
Set units of the reaction rate expression
include/cantera/kinetics/Arrhenius.h:126
↓ 1 callersMethodsetReactor
src/zeroD/ReactorSurface.cpp:74
↓ 1 callersMethodsetReferenceThermo
Set the SpeciesThermoInterpType object used to calculate reference state properties
include/cantera/thermo/PDSS.h:366
↓ 1 callersMethodsetRightControlPointCoordinate
src/oneD/Flow1D.cpp:1256
↓ 1 callersMethodsetRightControlPointTemperature
src/oneD/Flow1D.cpp:1241
↓ 1 callersMethodsetRoot
Set root Solution holding all phase information
include/cantera/kinetics/Kinetics.h:1401
↓ 1 callersMethodsetS0
src/thermo/PDSS_HKFT.cpp:323
↓ 1 callersMethodsetSensitivityParameters
src/zeroD/ReactorSurface.cpp:119
↓ 1 callersMethodsetSolution
src/oneD/Domain1D.cpp:31
↓ 1 callersMethodsetSpreadRate
set spreading rate
src/oneD/Boundary1D.cpp:96
↓ 1 callersMethodsetState_DP
Set the density (kg/m**3) and pressure (Pa) at constant composition ! * This method must be reimplemented in derived classes, where it may *
include/cantera/thermo/ThermoPhase.h:1404
↓ 1 callersMethodsetState_PV
src/thermo/PureFluidPhase.cpp:331
↓ 1 callersMethodsetState_SH
src/thermo/PureFluidPhase.cpp:355
↓ 1 callersMethodsetState_ST
src/thermo/PureFluidPhase.cpp:319
↓ 1 callersMethodsetState_TH
src/thermo/PureFluidPhase.cpp:349
↓ 1 callersMethodsetState_TP
src/thermo/VPStandardStateTP.cpp:207
↓ 1 callersMethodsetState_TV
src/thermo/PureFluidPhase.cpp:325
↓ 1 callersMethodsetState_UP
src/thermo/PureFluidPhase.cpp:337
↓ 1 callersMethodsetState_VH
src/thermo/PureFluidPhase.cpp:343
↓ 1 callersMethodsetStdState
src/tpx/Sub.cpp:24
↓ 1 callersMethodsetSubstance
Set the name of the TPX substance to use for the equation of state. This function should be called before initThermo().
include/cantera/thermo/PureFluidPhase.h:59
↓ 1 callersMethodsetThermalResistance
Set the thermal resistance of the wall [K*m^2/W].
include/cantera/zeroD/Wall.h:192
↓ 1 callersMethodsetThreshold
Set the threshold value to compare elements against @param threshold double value used in setting by threshold
include/cantera/numerics/AdaptivePreconditioner.h:53
↓ 1 callersMethodsetTimeStep
src/numerics/SteadyStateSystem.cpp:226
↓ 1 callersMethodsetTortuosity
src/transport/DustyGasTransport.cpp:208
↓ 1 callersMethodsetTransientTolerances
src/oneD/Domain1D.cpp:87
↓ 1 callersMethodsetTransport
src/base/Solution.cpp:73
↓ 1 callersMethodsetType
Set the type of the ReactionData class. This should match the corresponding ReactionRate class's type
include/cantera/kinetics/ReactionRateDelegator.h:35
↓ 1 callersMethodsetUnitSystem
src/base/YamlWriter.cpp:203
↓ 1 callersMethodsetUnits
src/base/YamlWriter.cpp:197
↓ 1 callersMethodsetUnstrainedFlow
Set flow configuration for burner-stabilized flames, using specified inlet mass fluxes.
include/cantera/oneD/Flow1D.h:206
↓ 1 callersMethodsetValid
Set validity flag of reaction
include/cantera/kinetics/Reaction.h:89
↓ 1 callersMethodsetVelocity
Set the wall velocity to a specified function of time, @f$ v(t) @f$. @deprecated To be removed after %Cantera 3.2. Replaceable by version using share
include/cantera/zeroD/Wall.h:127
↓ 1 callersMethodsetViscosityFlag
Specify if the viscosity term should be included in the momentum equation
include/cantera/oneD/Flow1D.h:384
↓ 1 callersMethodsetWrapper
Set the external language wrapper for this ReactionData object
include/cantera/kinetics/ReactionRateDelegator.h:45
↓ 1 callersMethodset_a
src/thermo/PDSS_HKFT.cpp:327
↓ 1 callersMethodset_c
src/thermo/PDSS_HKFT.cpp:334
↓ 1 callersMethodset_initial_guess
Set the initial guess for the solution. By default, the adiabatic flame temperature and equilibrium composition are computed for the
interfaces/cython/cantera/onedim.py:629
↓ 1 callersMethodset_initial_guess
Set the initial guess for the solution. By default, the adiabatic flame temperature and equilibrium composition are computed for the
interfaces/cython/cantera/onedim.py:836
↓ 1 callersFunctionsetupConstCp
src/thermo/SpeciesThermoFactory.cpp:128
↓ 1 callersFunctionsetupGasTransportData
src/transport/TransportData.cpp:161
↓ 1 callersFunctionsetupMu0
src/thermo/SpeciesThermoFactory.cpp:163
↓ 1 callersFunctionsetupNasa9Poly
src/thermo/SpeciesThermoFactory.cpp:144
↓ 1 callersFunctionsetupNasaPoly
src/thermo/SpeciesThermoFactory.cpp:88
↓ 1 callersFunctionsetupShomatePoly
src/thermo/SpeciesThermoFactory.cpp:108
↓ 1 callersMethodsetupUniformGrid
src/oneD/Domain1D.cpp:240
↓ 1 callersFunctionshow_coverages
Print the coverages for surface s.
samples/python/kinetics/sofc.py:55
↓ 1 callersMethodshow_duplicate_reactions
(self, error_message)
interfaces/cython/cantera/ck2yaml.py:2224
↓ 1 callersFunctionsimple_demo
The actual code is put into a function that can be called from the main program.
doc/sphinx/userguide/demo1a.cpp:7
↓ 1 callersFunctionsimple_demo2
doc/sphinx/userguide/kinetics_transport.cpp:7
↓ 1 callersMethodsize
Size of SolutionArray (number of entries).
include/cantera/base/SolutionArray.h:74
↓ 1 callersFunctionsoln_adjacent
src/clib/ct.cpp:212
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