| ▼NCantera | Namespace for the Cantera kernel |
| CAdaptivePreconditioner | AdaptivePreconditioner a preconditioner designed for use with large mechanisms that leverages sparse solvers |
| CAnyBase | Base class defining common data possessed by both AnyMap and AnyValue objects |
| ▼CAnyMap | A map of string keys to values whose type can vary at runtime |
| CIterator | Defined to allow use with range-based for loops |
| COrderedIterator | Defined to allow the OrderedProxy class to be used with range-based for loops |
| COrderedProxy | Proxy for iterating over an AnyMap in the defined output ordering |
| CAnyValue | A wrapper for a variable whose type is determined at runtime |
| ▼CApplication | Class to hold global data |
| CMessages | Class to carry out messages |
| CThreadMessages | Class that stores thread messages for each thread, and retrieves them based on the thread id |
| CArray2D | A class for 2D arrays stored in column-major (Fortran-compatible) form |
| CArraySizeError | Array size error |
| CArrhenius1 | Implements a sum of Arrhenius terms |
| CArrheniusBase | Base class for Arrhenius-type Parameterizations |
| CArrheniusData | Data container holding shared data specific to ArrheniusRate |
| CArrheniusRate | Arrhenius reaction rate type depends only on temperature |
| CatomicWeightData | Database for atomic weights |
| ▼CBandMatrix | A class for banded matrices, involving matrix inversion processes |
| CPivData | |
| CBinarySolutionTabulatedThermo | Overloads the virtual methods of class IdealSolidSolnPhase to implement tabulated standard state thermodynamics for one species in a binary solution |
| CBlowersMaselData | Data container holding shared data specific to BlowersMaselRate |
| CBlowersMaselRate | Blowers Masel reaction rate type depends on the enthalpy of reaction |
| CBoundary1D | The base class for boundaries between one-dimensional spatial domains |
| CBulkKinetics | Specialization of Kinetics for chemistry in a single bulk phase |
| CC1 | Handles one species in a reaction |
| CC2 | Handles two species in a single reaction |
| CC3 | Handles three species in a reaction |
| CC_AnyN | Handles any number of species in a reaction, including fractional stoichiometric coefficients, and arbitrary reaction orders |
| CCachedValue | A cached property value and the state at which it was evaluated |
| CCanteraError | Base class for exceptions thrown by Cantera classes |
| CChebyshevData | Data container holding shared data specific to ChebyshevRate |
| CChebyshevRate | Pressure-dependent rate expression where the rate coefficient is expressed as a bivariate Chebyshev polynomial in temperature and pressure |
| CChemEquil | Class ChemEquil implements a chemical equilibrium solver for single-phase solutions |
| CclockWC | The class provides the wall clock timer in seconds |
| CComposite1 | Implements a composite function |
| CConst1 | Implements a constant |
| CConstCpPoly | A constant-heat capacity species thermodynamic property manager class |
| CConstPressureMoleReactor | ConstPressureMoleReactor is a class for constant-pressure reactors which use a state of moles |
| CConstPressureReactor | Class ConstPressureReactor is a class for constant-pressure reactors |
| CCos1 | Implements the cos() function |
| ▼CCoverageDependentSurfPhase | A thermodynamic model for a coverage-dependent surface phase, applying surface species lateral interaction correction factors to the ideal surface phase properties |
| CHeatCapacityDependency | A struct to store sets of parameters used in coverage-dependent heat capacity calculations by a log-quadratic equation in CoverageDependentSurfPhase |
| CInterpolativeDependency | A struct to store sets of parameters used in coverage-dependent enthalpy and entropy calculations by a interpolative equation or a piecewise-linear equation in CoverageDependentSurfPhase |
| CPolynomialDependency | A struct to store sets of parameters used in coverage-dependent enthalpy and entropy calculations by a polynomial equation or a linear equation in CoverageDependentSurfPhase |
| CCustomFunc1Rate | Custom reaction rate depending only on temperature |
| CCVodesIntegrator | Wrapper class for 'cvodes' integrator from LLNL |
| CDebyeHuckel | Class DebyeHuckel represents a dilute liquid electrolyte phase which obeys the Debye Huckel formulation for nonideality |
| CDelegator | Delegate member functions of a C++ class to externally-specified functions |
| CDenseMatrix | A class for full (non-sparse) matrices with Fortran-compatible data storage, which adds matrix operations to class Array2D |
| CDiff1 | Implements the difference of two functions |
| CDomain1D | Base class for one-dimensional domains |
| CDomainFactory | Factory class to create domain objects |
| CDustyGasTransport | Class DustyGasTransport implements the Dusty Gas model for transport in porous media |
| CEdgeKinetics | Heterogeneous reactions at one-dimensional interfaces between multiple adjacent two-dimensional surfaces |
| CEdgePhase | A thermodynamic phase representing a one dimensional edge between two surfaces |
| CElectronCollisionPlasmaData | Data container holding shared data specific to ElectronCollisionPlasmaRate |
| CElectronCollisionPlasmaRate | Electron collision plasma reaction rate type |
| CEmpty1D | A terminator that does nothing |
| CEquilOpt | Chemical equilibrium options |
| CExp1 | Implements the exp() (exponential) function |
| CExtensionManager | Base class for managing user-defined Cantera extensions written in other languages |
| CExtensionManagerFactory | A factory class for creating ExtensionManager objects |
| CExternalHandle | A base class for managing the lifetime of an external object, such as a Python object used by a Delegator |
| CExternalLogger | Logger that delegates to an external source via a callback to produce log output |
| CFactory | Factory class that supports registering functions to create objects |
| CFactoryBase | Base class for factories |
| CFalloffData | Data container holding shared data specific to Falloff rates |
| CFalloffRate | Base class for falloff rate calculators |
| CFlow1D | This class represents 1D flow domains that satisfy the one-dimensional similarity solution for chemically-reacting, axisymmetric flows |
| CFlowDevice | Base class for 'flow devices' (valves, pressure regulators, etc.) connecting reactors |
| CFlowDeviceFactory | Factory class to create FlowDevice objects |
| CFlowReactor | Adiabatic flow in a constant-area duct with homogeneous and heterogeneous reactions |
| CFourier1 | Implements a Fourier cosine/sine series |
| CFunc1 | Base class for 'functor' classes that evaluate a function of one variable |
| CFunc1Factory | Factory class to create Func1 objects |
| CFuncEval | Virtual base class for ODE/DAE right-hand-side function evaluators |
| CGasTransport | Class GasTransport implements some functions and properties that are shared by the MixTransport and MultiTransport classes |
| CGasTransportData | Transport data for a single gas-phase species which can be used in mixture-averaged or multicomponent transport models |
| CGaussian1 | Implements a Gaussian function |
| CGeneralMatrix | Generic matrix |
| CGibbsExcessVPSSTP | GibbsExcessVPSSTP is a derived class of ThermoPhase that handles variable pressure standard state methods for calculating thermodynamic properties that are further based on expressing the Excess Gibbs free energy as a function of the mole fractions (or pseudo mole fractions) of constituents |
| CGroup | Class Group is an internal class used by class ReactionPath |
| CHighPressureGasTransport | Class MultiTransport implements transport properties for high pressure gas mixtures |
| CHMWSoln | Class HMWSoln represents a dilute or concentrated liquid electrolyte phase which obeys the Pitzer formulation for nonideality |
| CIdasIntegrator | Wrapper for Sundials IDAS solver |
| CIdealGasConstPressureMoleReactor | IdealGasConstPressureMoleReactor is a class for ideal gas constant-pressure reactors which use a state of moles |
| CIdealGasConstPressureReactor | Class ConstPressureReactor is a class for constant-pressure reactors |
| CIdealGasMoleReactor | IdealGasMoleReactor is a class for ideal gas constant-volume reactors which use a state of moles |
| CIdealGasPhase | Class IdealGasPhase represents low-density gases that obey the ideal gas equation of state |
| CIdealGasReactor | Class IdealGasReactor is a class for stirred reactors that is specifically optimized for ideal gases |
| CIdealMolalSoln | This phase is based upon the mixing-rule assumption that all molality-based activity coefficients are equal to one |
| CIdealSolidSolnPhase | Class IdealSolidSolnPhase represents a condensed phase ideal solution compound |
| CIdealSolnGasVPSS | An ideal solution approximation of a phase |
| CImplicitSurfChem | Advances the surface coverages of the associated set of SurfacePhase objects in time |
| CIndexError | An array index is out of range |
| CInlet1D | An inlet |
| CInputFileError | Error thrown for problems processing information contained in an AnyMap or AnyValue |
| CIntegrator | Abstract base class for ODE system integrators |
| CInterface | A container class for chemically-reacting interfaces |
| CInterfaceData | Data container holding shared data for reaction rate specification with interfaces |
| CInterfaceKinetics | A kinetics manager for heterogeneous reaction mechanisms |
| CInterfaceRate | A class template for interface reaction rate specifications |
| CInterfaceRateBase | Base class for rate parameterizations that involve interfaces |
| CIonFlow | This class models the ion transportation in a flame |
| CIonGasTransport | Class IonGasTransport implements Stockmayer-(n,6,4) model for transport of ions |
| CisotopeWeightData | Database for named isotopic weights |
| CKinetics | Public interface for kinetics managers |
| CKineticsFactory | Factory for kinetics managers |
| CLatticePhase | A simple thermodynamic model for a bulk phase, assuming a lattice of solid atoms |
| CLatticeSolidPhase | A phase that is comprised of a fixed additive combination of other lattice phases |
| CLindemannRate | The Lindemann falloff parameterization |
| CLinearBurkeData | Data container holding shared data specific to LinearBurkeRate |
| CLinearBurkeRate | Pressure-dependent and composition-dependent reaction rate calculated according to the reduced-pressure linear mixture rule (LMR-R) |
| CLog1 | Implements the log() (natural logarithm) function |
| CLogger | Base class for 'loggers' that write text messages to log files |
| CMargulesVPSSTP | MargulesVPSSTP is a derived class of GibbsExcessVPSSTP that employs the Margules approximation for the excess Gibbs free energy |
| CMassFlowController | A class for mass flow controllers |
| CMath1FactoryA | Factory class to create Func1 compound objects - version A |
| CMath1FactoryB | Factory class to create Func1 compound objects - version B |
| CMetalPhase | Class MetalPhase represents electrons in a metal |
| CMixTransport | Class MixTransport implements mixture-averaged transport properties for ideal gas mixtures |
| CMixtureFugacityTP | This is a filter class for ThermoPhase that implements some preparatory steps for efficiently handling mixture of gases that whose standard states are defined as ideal gases, but which describe also non-ideal solutions |
| CMMCollisionInt | Calculation of Collision integrals |
| CMolalityVPSSTP | MolalityVPSSTP is a derived class of ThermoPhase that handles variable pressure standard state methods for calculating thermodynamic properties that are further based on molality-scaled activities |
| CMoleReactor | MoleReactor is meant to serve the same purpose as the reactor class but with a state vector composed of moles |
| CMu0Poly | Implements an interpolation of the Gibbs free energy based on a piecewise constant heat capacity approximation |
| CMultiJac | Class MultiJac evaluates the Jacobian of a system of equations defined by a residual function supplied by an instance of class OneDim |
| CMultiNewton | Newton iterator for multi-domain, one-dimensional problems |
| CMultiPhase | A class for multiphase mixtures |
| CMultiPhaseEquil | Multiphase chemical equilibrium solver |
| CMultiRate | A class template handling ReactionRate specializations |
| CMultiRateBase | An abstract base class for evaluating all reactions of a particular type |
| CMultiSpeciesThermo | A species thermodynamic property manager for a phase |
| CMultiTransport | Class MultiTransport implements multicomponent transport properties for ideal gas mixtures |
| CNasa9Poly1 | The NASA 9 polynomial parameterization for one temperature range |
| CNasa9PolyMultiTempRegion | The NASA 9 polynomial parameterization for a single species encompassing multiple temperature regions |
| CNasaPoly1 | The NASA polynomial parameterization for one temperature range |
| CNasaPoly2 | The NASA polynomial parameterization for two temperature ranges |
| CNoExitLogger | Logger that doesn't exit when an error is thrown |
| CNotImplementedError | An error indicating that an unimplemented function has been called |
| COneDim | Container class for multiple-domain 1D problems |
| COutlet1D | An outlet |
| COutletRes1D | An outlet with specified composition |
| CPath | |
| CPDSS | Virtual base class for a species with a pressure dependent standard state |
| CPDSS_ConstVol | Class for pressure dependent standard states that use a constant volume model |
| CPDSS_HKFT | Class for pressure dependent standard states corresponding to ionic solutes in electrolyte water |
| CPDSS_Molar | Base class for PDSS classes which compute molar properties directly |
| CPDSS_Nondimensional | Base class for PDSS classes which compute nondimensional properties directly |
| CPDSS_SSVol | Class for pressure dependent standard states that uses a standard state volume model of some sort |
| CPDSS_Water | Class for the liquid water pressure dependent standard state |
| CPDSSFactory | |
| CPengRobinson | Implementation of a multi-species Peng-Robinson equation of state |
| CPeriodic1 | Implements a periodic function |
| ▼CPhase | Class Phase is the base class for phases of matter, managing the species and elements in a phase, as well as the independent variables of temperature, mass density (compressible substances) or pressure (incompressible substances), species mass/mole fraction, and other generalized forces and intrinsic properties (such as electric potential) that define the thermodynamic state |
| CUndefElement | |
| CPlasmaPhase | Base class for a phase with plasma properties |
| CPlogData | Data container holding shared data specific to PlogRate |
| CPlogRate | Pressure-dependent reaction rate expressed by logarithmically interpolating between Arrhenius rate expressions at various pressures |
| CPlusConstant1 | Implements the sum of a function and a constant |
| CPoly13 | Implements a polynomial of degree n |
| CPow1 | Implements the pow() (power) function |
| CPreconditionerBase | PreconditionerBase serves as an abstract type to extend different preconditioners |
| CPreconditionerFactory | Factory class to create preconditioner objects |
| CPressureController | A class for flow controllers where the flow rate is equal to the flow rate of a primary mass flow controller plus a correction proportional to the pressure difference between the inlet and outlet |
| CProduct1 | Implements the product of two functions |
| CPureFluidPhase | This phase object consists of a single component that can be a gas, a liquid, a mixed gas-liquid fluid, or a fluid beyond its critical point |
| CPythonExtensionManager | Class for managing user-defined Cantera extensions written in Python |
| CPythonHandle | Class that holds an owned or weak (borrowed) reference to a Python object |
| CRatio1 | Implements the ratio of two functions |
| CReactingSurf1D | A reacting surface |
| CReaction | Abstract base class which stores data about a reaction and its rate parameterization so that it can be added to a Kinetics object |
| CReactionData | Data container holding shared data used for ReactionRate calculation |
| CReactionDataDelegator | Delegate methods of the ReactionData class to external functions |
| CReactionPathBuilder | |
| CReactionPathDiagram | Reaction path diagrams (graphs) |
| CReactionRate | Abstract base class for reaction rate definitions; this base class is used by user-facing APIs to access reaction rate objects |
| CReactionRateDelegator | Delegate methods of the ReactionRate class to external functions |
| CReactionRateFactory | Factory class to construct reaction rate calculators |
| CReactor | Class Reactor is a general-purpose class for stirred reactors |
| CReactorAccessor | An abstract base class for providing access to protected capabilities Reactor objects from delegate methods, which would normally only be able to access public Reactor members |
| CReactorBase | Base class for stirred reactors |
| CReactorDelegator | Delegate methods of the Reactor class to external functions |
| CReactorFactory | Factory class to create reactor objects |
| CReactorNet | A class representing a network of connected reactors |
| CReactorSurface | A surface where reactions can occur that is in contact with the bulk fluid of a Reactor |
| CRedlichKisterVPSSTP | RedlichKisterVPSSTP is a derived class of GibbsExcessVPSSTP that employs the Redlich-Kister approximation for the excess Gibbs free energy |
| CRedlichKwongMFTP | Implementation of a multi-species Redlich-Kwong equation of state |
| CRefiner | Refine Domain1D grids so that profiles satisfy adaptation tolerances |
| CReservoir | A source or sink whose state remains constant regardless of any flows or other interactions with other Reactor objects |
| CSensitivityParameter | |
| CShomatePoly | The Shomate polynomial parameterization for one temperature range for one species |
| CShomatePoly2 | The Shomate polynomial parameterization for two temperature ranges for one species |
| CSim1D | One-dimensional simulations |
| CSin1 | Implements the sin() function |
| CSingleSpeciesTP | Filter class for ThermoPhase |
| CSolution | A container class for chemically-reacting solutions |
| CSolutionArray | A container class holding arrays of state information |
| CsolveSP | Method to solve a pseudo steady state surface problem |
| CSpecies | Contains data about a single chemical species |
| CSpeciesNode | Nodes in reaction path graphs |
| CSpeciesThermoInterpType | Abstract Base class for the thermodynamic manager for an individual species' reference state |
| CSriRate | The SRI falloff function |
| CStFlow | This class represents 1D flow domains that satisfy the one-dimensional similarity solution for chemically-reacting, axisymmetric flows |
| CStickingCoverage | Base class for rate parameterizations that implement sticking coefficients |
| CStickingRate | A class template for interface sticking rate specifications |
| CStoichManagerN | This class handles operations involving the stoichiometric coefficients on one side of a reaction (reactant or product) for a set of reactions comprising a reaction mechanism |
| CStoichSubstance | Class StoichSubstance represents a stoichiometric (fixed composition) incompressible substance |
| CStorage | A wrapper class handling storage to HDF |
| CSum1 | Implements the sum of two functions |
| CSundialsContext | A wrapper for managing a SUNContext object, need for Sundials >= 6.0 |
| CSurf1D | A non-reacting surface |
| CSurfPhase | A simple thermodynamic model for a surface phase, assuming an ideal solution model |
| CSymm1D | A symmetry plane |
| CTabulated1 | Implements a tabulated function |
| CThermoFactory | Factory class for thermodynamic property managers |
| CThermoPhase | Base class for a phase with thermodynamic properties |
| CThirdBody | A class for managing third-body efficiencies, including default values |
| CThirdBodyCalc | Calculate and apply third-body effects on reaction rates, including non- unity third-body efficiencies |
| CTimesConstant1 | Implements the product of a function and a constant |
| CTransport | Base class for transport property managers |
| CTransportData | Base class for transport data for a single species |
| CTransportFactory | Factory class for creating new instances of classes derived from Transport |
| CTroeRate | The 3- or 4-parameter Troe falloff parameterization |
| CTsangRate | The 1- or 2-parameter Tsang falloff parameterization |
| CTwoTempPlasmaData | Data container holding shared data specific to TwoTempPlasmaRate |
| CTwoTempPlasmaRate | Two temperature plasma reaction rate type depends on both gas temperature and electron temperature |
| CUnits | A representation of the units associated with a dimensional quantity |
| CUnitStack | Unit aggregation utility |
| CUnitSystem | Unit conversion utility |
| CUnityLewisTransport | Class UnityLewisTransport implements the unity Lewis number approximation for the mixture-averaged species diffusion coefficients |
| CValueCache | Storage for cached values |
| CValve | Supply a mass flow rate that is a function of the pressure drop across the valve |
| CVCS_COUNTERS | Class to keep track of time and iterations |
| Cvcs_MultiPhaseEquil | Cantera's Interface to the Multiphase chemical equilibrium solver |
| CVCS_SOLVE | This is the main structure used to hold the internal data used in vcs_solve_TP(), and to solve TP systems |
| CVCS_SPECIES_THERMO | Identifies the thermo model for the species |
| Cvcs_SpeciesProperties | Properties of a single species |
| Cvcs_VolPhase | Phase information and Phase calculations for vcs |
| CVPStandardStateTP | This is a filter class for ThermoPhase that implements some preparatory steps for efficiently handling a variable pressure standard state for species |
| CWall | Represents a wall between between two ReactorBase objects |
| CWallBase | Base class for 'walls' (walls, pistons, etc.) connecting reactors |
| CWallFactory | Factory class to create WallBase objects |
| CWaterProps | Used to house several approximation routines for properties of water |
| CWaterPropsIAPWS | Class for calculating the equation of state of water |
| CWaterPropsIAPWSphi | Low level class for the real description of water |
| CWaterSSTP | Class for single-component water |
| CWaterTransport | Transport Parameters for pure water |
| CYamlWriter | A class for generating full YAML input files from multiple data sources |
| ▼Ntpx | |
| CCarbonDioxide | Pure species representation of carbon dioxide |
| CHeptane | Pure species representation of heptane |
| CHFC134a | Equation of state for HFC-134a |
| Chydrogen | Pure species representation of hydrogen |
| Cmethane | Pure species representation of methane |
| Cnitrogen | Pure species representation of nitrogen |
| Coxygen | Pure species representation of oxygen |
| CSubstance | Base class from which all pure substances are derived |
| Cwater | Pure species representation of water |
| ▼NYAML | |
| Cconvert< Cantera::AnyMap > | |
| Cconvert< Cantera::AnyValue > | |
| CCallbackError | |
| CFunc1Py | |
| CPyFuncInfo | A class to hold information needed to call Python functions from delegated methods (see class Delegator) |
| CPythonLogger | |
1.9.7