| ▶NCantera | Namespace for the Cantera kernel |
| CAdsorbate | An adsorbed surface species |
| ▶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 |
| CAqueousKinetics | Kinetics manager for elementary aqueous-phase chemistry |
| CArray2D | A class for 2D arrays stored in column-major (Fortran-compatible) form |
| CArraySizeError | Array size error |
| CArrhenius | Arrhenius reaction rate type depends only on temperature |
| CArrhenius1 | Sum of Arrhenius terms |
| CatomicWeightData | |
| CAxiStagnFlow | A class for axisymmetric stagnation flows |
| CBandMatrix | A class for banded matrices, involving matrix inversion processes |
| CBdry1D | The base class for boundaries between one-dimensional spatial domains |
| CBulkKinetics | Partial 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 | |
| CCanteraError | Base class for exceptions thrown by Cantera classes |
| CCELapackError | Exception thrown when an LAPACK error is encountered associated with inverting or solving a matrix |
| CChebyshevRate | Pressure-dependent rate expression where the rate coefficient is expressed as a bivariate Chebyshev polynomial in temperature and pressure |
| CChebyshevReaction | A pressure-dependent reaction parameterized by a bi-variate Chebyshev polynomial in temperature and pressure |
| CChemEquil | Class ChemEquil implements a chemical equilibrium solver for single-phase solutions |
| CChemicallyActivatedReaction | A reaction where the rate decreases as pressure increases due to collisional stabilization of a reaction intermediate |
| CclockWC | The class provides the wall clock timer in seconds |
| CComposite1 | Composite function |
| CConst1 | Constant |
| CConstCpPoly | A constant-heat capacity species thermodynamic property manager class |
| CConstDensityThermo | Overloads the virtual methods of class ThermoPhase to implement the incompressible equation of state |
| CConstPressureReactor | Class ConstPressureReactor is a class for constant-pressure reactors |
| CCos1 | Cos |
| CCoverageDependency | Modifications to an InterfaceReaction rate based on a surface species coverage |
| CCVodesErr | Exception thrown when a CVODES error is encountered |
| CCVodesIntegrator | Wrapper class for 'cvodes' integrator from LLNL |
| CDAE_Solver | Wrapper for DAE solvers |
| CDebyeHuckel | Class DebyeHuckel represents a dilute liquid electrolyte phase which obeys the Debye Huckel formulation for nonideality |
| CDenseMatrix | A class for full (non-sparse) matrices with Fortran-compatible data storage, which adds matrix operations to class Array2D |
| CDiff1 | Difference of two functions |
| CDomain1D | Base class for one-dimensional domains |
| CDustyGasTransport | Class DustyGasTransport implements the Dusty Gas model for transport in porous media |
| CEdge | Convenience class which inherits from both EdgePhase and EdgeKinetics |
| 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 |
| CElectrochemicalReaction | An interface reaction which involves charged species |
| CElementaryReaction | A reaction which follows mass-action kinetics with a modified Arrhenius reaction rate |
| CEmpty1D | A terminator that does nothing |
| CEquilOpt | Chemical equilibrium options |
| CExp1 | Exp |
| CFactory | Factory class that supports registering functions to create objects |
| CFactoryBase | Base class for factories |
| CFalloff | Base class for falloff function calculators |
| CFalloffFactory | Factory class to construct falloff function calculators |
| CFalloffMgr | A falloff manager that implements any set of falloff functions |
| CFalloffReaction | A reaction that is first-order in [M] at low pressure, like a third-body reaction, but zeroth-order in [M] as pressure increases |
| CFixedChemPotSSTP | Class FixedChemPotSSTP represents a stoichiometric (fixed composition) incompressible substance |
| CFlowDevice | Base class for 'flow devices' (valves, pressure regulators, etc.) connecting reactors |
| CFlowReactor | Adiabatic flow in a constant-area duct |
| CFourier1 | Fourier cosine/sine series |
| CFreeFlame | A class for freely-propagating premixed flames |
| CFunc1 | Base class for 'functor' classes that evaluate a function of one variable |
| CFuncEval | Virtual base class for ODE right-hand-side function evaluators |
| CGasKinetics | Kinetics manager for elementary gas-phase chemistry |
| 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 |
| CGaussian | A Gaussian |
| CGeneralMatrix | Generic matrix |
| CGeneralSpeciesThermo | |
| CGibbsExcessVPSSTP | |
| 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 |
| CIDA_Err | Exception thrown when a IDA error is encountered |
| CIDA_Solver | Wrapper for Sundials IDA solver |
| CIdealGasConstPressureReactor | Class ConstPressureReactor is a class for constant-pressure reactors |
| CIdealGasMix | Convenience class which inherits from both IdealGasPhase and GasKinetics |
| 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 or an ideal gas approximation of a phase |
| CImplicitSurfChem | Advances the surface coverages of the associated set of SurfacePhase objects in time |
| CIncompressibleSolid | Wrapper for ConstDensityThermo with constructor from file |
| CIndexError | An array index is out of range |
| CInlet1D | An inlet |
| CIntegrator | Abstract base class for ODE system integrators |
| CInterface | An interface between multiple bulk phases |
| ▶CInterfaceKinetics | A kinetics manager for heterogeneous reaction mechanisms |
| CStickData | Values used for converting sticking coefficients into rate constants |
| CInterfaceReaction | A reaction occurring on an interface (i.e. a SurfPhase or an EdgePhase) |
| CIonsFromNeutralVPSSTP | |
| CisotopeWeightData | |
| 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 |
| CLiquidTranInteraction | Base class to handle transport property evaluation in a mixture |
| CLiquidTransport | Class LiquidTransport implements models for transport properties for liquid phases |
| CLiquidTransportData | Class LiquidTransportData holds transport parameters for a specific liquid-phase species |
| CLiquidTransportParams | Class LiquidTransportParams holds transport model parameters relevant to transport in mixtures |
| CLogger | Base class for 'loggers' that write text messages to log files |
| CLTI_Log_MoleFracs | Mixing rule using logarithms of the mole fractions |
| CLTI_MassFracs | Simple mass fraction weighting of transport properties |
| CLTI_MoleFracs | Simple mole fraction weighting of transport properties |
| CLTI_MoleFracs_ExpT | Simple mole fraction weighting of transport properties |
| CLTI_Pairwise_Interaction | Transport properties that act like pairwise interactions as in binary diffusion coefficients |
| CLTI_StefanMaxwell_PPN | Stefan Maxwell Diffusion Coefficients can be solved for given ion conductivity, mobility ratios, and self diffusion coeffs |
| CLTPError | Exception thrown if an error is encountered while reading the transport database |
| CLTPmodelError | Exception thrown if an error is encountered while reading the transport database |
| CLTPspecies | Class LTPspecies holds transport parameterizations for a specific liquid- phase species |
| CLTPspecies_Arrhenius | Class LTPspecies_Arrhenius holds transport parameters for a specific liquid- phase species (LTPspecies) when the transport property is expressed in Arrhenius form |
| CLTPspecies_Const | Class LTPspecies_Const holds transport parameters for a specific liquid- phase species (LTPspecies) when the transport property is just a constant value |
| CLTPspecies_ExpT | Class LTPspecies_ExpT holds transport parameters for a specific liquid- phase species (LTPspecies) when the transport property is expressed as an exponential in temperature |
| CLTPspecies_Poly | Class LTPspecies_Poly holds transport parameters for a specific liquid-phase species (LTPspecies) when the transport property is expressed as a polynomial in temperature |
| CMargulesVPSSTP | MargulesVPSSTP is a derived class of GibbsExcessVPSSTP that employs the Margules approximation for the excess Gibbs free energy |
| CMaskellSolidSolnPhase | Class MaskellSolidSolnPhase represents a condensed phase non-ideal solution with 2 species following the thermodynamic model described in Maskell, Shaw, and Tye, Manganese Dioxide Electrode – IX, Electrochimica Acta 28(2) pp 231-235, 1983 |
| CMassFlowController | A class for mass flow controllers |
| CMetal | Wrapper for MetalPhase with constructor from file |
| CMetalPhase | Class MetalPhase represents electrons in a metal |
| CMetalSHEelectrons | Class MetalSHEelectrons represents electrons within a metal, adjacent to an aqueous electrolyte, that are consistent with the SHE reference electrode |
| CMineralEQ3 | Class MineralEQ3 represents a stoichiometric (fixed composition) incompressible substance based on EQ3's parameterization |
| CMixedSolventElectrolyte | MixedSolventElectrolyte is a derived class of GibbsExcessVPSSTP that employs the DH and local Margules approximations for the excess Gibbs free energy |
| 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 | |
| CMolarityIonicVPSSTP | |
| 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 | |
| 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 |
| 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 |
| 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_IdealGas | Derived class for pressure dependent standard states of an ideal gas species |
| CPDSS_IonsFromNeutral | Derived class for pressure dependent standard states of an ideal gas species |
| 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 |
| CPeriodic1 | 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, species mass/mole fraction, and other generalized forces and intrinsic properties (such as electric potential) that define the thermodynamic state |
| CPhaseCombo_Interaction | PhaseCombo_Interaction is a derived class of GibbsExcessVPSSTP that employs the Margules approximation for the excess Gibbs free energy while eliminating the entropy of mixing term |
| CPlog | Pressure-dependent reaction rate expressed by logarithmically interpolating between Arrhenius rate expressions at various pressures |
| CPlogReaction | A pressure-dependent reaction parameterized by logarithmically interpolating between Arrhenius rate expressions at various pressures |
| CPlusConstant1 | A function plus a constant |
| CPoly1 | Polynomial of degree n |
| CPow1 | Pow |
| CPressureController | A class for flow controllers where the flow rate is equal to the flow rate of a "master" mass flow controller plus a correction proportional to the pressure difference between the inlet and outlet |
| CProduct1 | Product of two functions |
| CPureFluid | Wrapper for PureFluidPhase with constructor from file |
| 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 |
| CRate1 | This rate coefficient manager supports one parameterization of the rate constant of any type |
| CRatio1 | Ratio of two functions |
| CReactingSurf1D | A reacting surface |
| CReaction | Intermediate class which stores data about a reaction and its rate parameterization so that it can be added to a Kinetics object |
| CReactionPathDiagram | Reaction path diagrams (graphs) |
| CReactor | Class Reactor is a general-purpose class for stirred reactors |
| CReactorBase | Base class for stirred reactors |
| CReactorNet | A class representing a network of connected reactors |
| 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 |
| CResidData | A simple class to hold an array of parameter values and a pointer to an instance of a subclass of ResidEval |
| CResidEval | Virtual base class for DAE residual function evaluators |
| CResidJacEval | Wrappers for the function evaluators for Nonlinear solvers and Time steppers |
| ▶CRootFind | Root finder for 1D problems |
| CrfTable | Structure containing the iteration history |
| CSemiconductorPhase | Class SemiconductorPhase represents electrons and holes in a semiconductor |
| 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 |
| CSimpleTransport | Class SimpleTransport implements mixture-averaged transport properties for liquid phases |
| CSin1 | Implements the sin() function |
| CSingleSpeciesTP | Filter class for ThermoPhase |
| CSolidTransport | Class SolidTransport implements transport properties for solids |
| CSolidTransportData | Class SolidTransportData holds transport parameters for a specific solid- phase species |
| CsolveSP | Method to solve a pseudo steady state surface problem |
| CSpecies | Contains data about a single chemical species |
| CSpeciesNode | Nodes in reaction path graphs |
| CSpeciesThermo | |
| CSpeciesThermoInterpType | Abstract Base class for the thermodynamic manager for an individual species' reference state |
| CSquareMatrix | A class for full (non-sparse) matrices with Fortran-compatible data storage |
| CSRI | The SRI falloff function |
| CStFlow | This class represents 1D flow domains that satisfy the one-dimensional similarity solution for chemically-reacting, axisymmetric flows |
| CSTITbyPDSS | Class for the thermodynamic manager for an individual species' reference state which uses the PDSS base class to satisfy the requests |
| CStoichSubstance | Class StoichSubstance represents a stoichiometric (fixed composition) incompressible substance |
| CSum1 | Sum of two functions |
| CSurf1D | A non-reacting surface |
| CSurfaceArrhenius | An Arrhenius rate with coverage-dependent terms |
| CSurfPhase | A simple thermodynamic model for a surface phase, assuming an ideal solution model |
| CSymm1D | A symmetry plane |
| 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 |
| CThreeBodyReaction | A reaction with a non-reacting third body "M" that acts to add or remove energy from the reacting species |
| CtimesConstant | Unary operator to multiply the argument by a constant |
| CTimesConstant1 | Product of two functions |
| CTortuosity | Specific Class to handle tortuosity corrections for diffusive transport in porous media using the Bruggeman exponent |
| CTortuosityMaxwell | This class implements transport coefficient corrections appropriate for porous media with a dispersed phase |
| CTortuosityPercolation | This class implements transport coefficient corrections appropriate for porous media where percolation theory applies |
| CTransport | Base class for transport property managers |
| CTransportData | Base class for transport data for a single species |
| CTransportDBError | Exception thrown if an error is encountered while reading the transport database |
| CTransportFactory | Factory class for creating new instances of classes derived from Transport |
| CTransportParams | Base structure to hold transport model parameters |
| CTroe | The 3- or 4-parameter Troe falloff parameterization |
| CUnit | Unit conversion utility |
| CUnknownThermoPhaseModel | Specific error to be thrown if the type of Thermo manager is unrecognized |
| CUnknownVPSSMgrModel | Throw a named error for an unknown or missing vpss species thermo model |
| CValueCache | |
| 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_PROB | Interface class for the vcs thermo equilibrium solver package, which generally describes the problem to be solved |
| 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 | |
| Cvcs_SpeciesProperties | Properties of a single species |
| Cvcs_VolPhase | Phase information and Phase calculations for vcs |
| CVPSSMgr | Virtual base class for the classes that manage the calculation of standard state properties for all the species in a phase |
| CVPSSMgr_ConstVol | Constant Molar Volume e VPSS species thermo manager class |
| CVPSSMgr_General | Class that handles the calculation of standard state thermo properties for a set of species belonging to a single phase in a completely general but slow way |
| CVPSSMgr_IdealGas | A VPSSMgr where all species in the phase obey an ideal gas equation of state |
| CVPSSMgr_Water_ConstVol | Handles the calculation of standard state thermo properties for real water and a set of species which have a constant molar volume pressure dependence |
| CVPSSMgr_Water_HKFT | Manages standard state thermo properties for real water and a set of species which have the HKFT equation of state |
| CVPSSMgrFactory | Factory to build instances of classes that manage the standard-state thermodynamic properties of a set of species |
| CVPStandardStateTP | This is a filter class for ThermoPhase that implements some prepatory steps for efficiently handling a variable pressure standard state for species |
| CWall | Represents a wall between between two ReactorBase 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 |
| CXML_Error | Classs representing a generic XML error condition |
| CXML_NoChild | Class representing a specific type of XML file formatting error |
| CXML_Node | Class XML_Node is a tree-based representation of the contents of an XML file |
| CXML_Reader | Class XML_Reader reads an XML file into an XML_Node object |
| CXML_TagMismatch | Class representing a specific type of XML file formatting error |
| ▶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 |
| Cleekesler | |
| Cmethane | Pure species representation of methane |
| Cnitrogen | Pure species representation of nitrogen |
| Coxygen | Pure species representation of oxygen |
| CRedlichKwong | |
| CSubstance | |
| Cwater | Pure species representation of water |
