  Application | Class to hold global data |
| Application::Messages | Class to carry out messages |
| Application::ThreadMessages | Class that stores thread messages for each thread, and retrieves them based on the thread id |
 Array2D | A class for 2D arrays stored in column-major (Fortran-compatible) form |
  DenseMatrix | A class for full (non-sparse) matrices with Fortran-compatible data storage, which adds matrix operations to class Array2D |
  SquareMatrix | A class for full (non-sparse) matrices with Fortran-compatible data storage |
| Arrhenius | Arrhenius reaction rate type depends only on temperature |
| awData | |
| C1 | Handles one species in a reaction |
| C2 | Handles two species in a single reaction |
| C3 | Handles three species in a reaction |
| C_AnyN | Handles any number of species in a reaction, including fractional stoichiometric coefficients, and arbitrary reaction orders |
| CachedValue< T > | |
| ChebyshevRate | Pressure-dependent rate expression where the rate coefficient is expressed as a bivariate Chebyshev polynomial in temperature and pressure |
| ChemEquil | Class ChemEquil implements a chemical equilibrium solver for single-phase solutions |
| clockWC | The class provides the wall clock timer in seconds |
| CoverageDependency | Modifications to an InterfaceReaction rate based on a surface species coverage |
| DAE_Solver | Wrapper for DAE solvers |
| Domain1D | Base class for one-dimensional domains |
| Bdry1D | The base class for boundaries between one-dimensional spatial domains |
| Inlet1D | An inlet |
| Outlet1D | An outlet |
| OutletRes1D | An outlet with specified composition |
| ReactingSurf1D | A reacting surface |
| Surf1D | A non-reacting surface |
| Symm1D | A symmetry plane |
| Empty1D | A terminator that does nothing |
| StFlow | This class represents 1D flow domains that satisfy the one-dimensional similarity solution for chemically-reacting, axisymmetric, flows |
| AxiStagnFlow | A class for axisymmetric stagnation flows |
| FreeFlame | A class for freely-propagating premixed flames |
| Elements | Object containing the elements that make up species in a phase |
| Enhanced3BConc | Computes enhanced third-body concentrations |
| EquilOpt | Chemical equilibrium options |
| ExchangeCurrent | Arrhenius reaction rate type depends only on temperature |
| ExtraGlobalRxn | Class describing an extra global reaction, which is defined as a linear combination of actuals reactions, global or mass-action, creating a global stoichiometric result |
| FactoryBase | Base class for factories |
| FalloffFactory | Factory class to construct falloff function calculators |
| KineticsFactory | Factory for kinetics managers |
| SpeciesThermoFactory | Factory to build instances of classes that manage the standard-state thermodynamic properties of a set of species |
| ThermoFactory | Factory class for thermodynamic property managers |
| TransportFactory | Factory class for creating new instances of classes derived from Transport |
| VPSSMgrFactory | Factory to build instances of classes that manage the standard-state thermodynamic properties of a set of species |
| Falloff | Base class for falloff function calculators |
| SRI | The SRI falloff function |
| Troe | The 3- or 4-parameter Troe falloff parameterization |
| FalloffMgr | A falloff manager that implements any set of falloff functions |
| FlowDevice | Base class for 'flow devices' (valves, pressure regulators, etc.) connecting reactors |
| MassFlowController | A class for mass flow controllers |
| PressureController | 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 |
| Valve | Supply a mass flow rate that is a function of the pressure drop across the valve |
| Func1 | Base class for 'functor' classes that evaluate a function of one variable |
| Arrhenius1 | Sum of Arrhenius terms |
| Composite1 | Composite function |
| Const1 | Constant |
| Cos1 | Cos |
| Diff1 | Difference of two functions |
| Exp1 | Exp |
| Fourier1 | Fourier cosine/sine series |
| Gaussian | A Gaussian |
| Periodic1 | Periodic function |
| PlusConstant1 | A function plus a constant |
| Poly1 | Polynomial of degree n |
| Pow1 | Pow |
| Product1 | Product of two functions |
| Ratio1 | Ratio of two functions |
| Sin1 | Implements the sin() function |
| Sum1 | Sum of two functions |
| TimesConstant1 | Product of two functions |
| FuncEval | Virtual base class for ODE right-hand-side function evaluators |
| ImplicitSurfChem | Advances the surface coverages of the associated set of SurfacePhase objects in time |
| ReactorNet | A class representing a network of connected reactors |
| GeneralMatrix | Generic matrix |
| BandMatrix | A class for banded matrices, involving matrix inversion processes |
| MultiJac | Class MultiJac evaluates the Jacobian of a system of equations defined by a residual function supplied by an instance of class OneDim |
| SquareMatrix | A class for full (non-sparse) matrices with Fortran-compatible data storage |
| Group | Class Group is an internal class used by class ReactionPath |
| Integrator | Abstract base class for ODE system integrators |
| BEulerInt | |
| CVodeInt | Wrapper class for 'CVODE' integrator from LLNL |
| CVodesIntegrator | Wrapper class for 'cvodes' integrator from LLNL |
| Kinetics | Public interface for kinetics managers |
| BulkKinetics | Partial specialization of Kinetics for chemistry in a single bulk phase |
| AqueousKinetics | Kinetics manager for elementary aqueous-phase chemistry |
| GasKinetics | Kinetics manager for elementary gas-phase chemistry |
| IdealGasMix | Convenience class which inherits from both IdealGasPhase and GasKinetics |
| InterfaceKinetics | A kinetics manager for heterogeneous reaction mechanisms |
| EdgeKinetics | Heterogeneous reactions at one-dimensional interfaces between multiple adjacent two-dimensional surfaces |
| Edge | Convenience class which inherits from both EdgePhase and EdgeKinetics |
| ElectrodeKinetics | A kinetics manager for heterogeneous reaction mechanisms |
| Interface | An interface between multiple bulk phases |
| LiquidTranInteraction | Base class to handle transport property evaluation in a mixture |
| LTI_Log_MoleFracs | Mixing rule using logarithms of the mole fractions |
| LTI_MassFracs | Simple mass fraction weighting of transport properties |
| LTI_MoleFracs | Simple mole fraction weighting of transport properties |
| LTI_MoleFracs_ExpT | Simple mole fraction weighting of transport properties |
| LTI_Pairwise_Interaction | Transport properties that act like pairwise interactions as in binary diffusion coefficients |
| LTI_StefanMaxwell_PPN | Stefan Maxwell Diffusion Coefficients can be solved for given ion conductivity, mobility ratios, and self diffusion coeffs |
| LiquidTransportData | Class LiquidTransportData holds transport parameters for a specific liquid-phase species |
| Logger | Base class for 'loggers' that write text messages to log files |
| LTPspecies | Class LTPspecies holds transport parameterizations for a specific liquid-phase species |
| LTPspecies_Arrhenius | Class LTPspecies_Arrhenius holds transport parameters for a specific liquid-phase species (LTPspecies) when the transport property is expressed in Arrhenius form |
| LTPspecies_Const | Class LTPspecies_Const holds transport parameters for a specific liquid-phase species (LTPspecies) when the transport property is just a constant value |
| LTPspecies_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 |
| LTPspecies_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 |
| MMCollisionInt | Calculation of Collision integrals |
| MultiNewton | Newton iterator for multi-domain, one-dimensional problems |
| MultiPhase | A class for multiphase mixtures |
| MultiPhaseEquil | |
| NonlinearSolver | Class that calculates the solution to a nonlinear system |
| OneDim | Container class for multiple-domain 1D problems |
| Sim1D | One-dimensional simulations |
| PDSS | Virtual base class for a species with a pressure dependent standard state |
| PDSS_Molar | Base class for PDSS classes which compute molar properties directly |
| PDSS_HKFT | Class for pressure dependent standard states corresponding to ionic solutes in electrolyte water |
| PDSS_Water | Class for the liquid water pressure dependent standard state |
| PDSS_Nondimensional | Base class for PDSS classes which compute nondimensional properties directly |
| PDSS_ConstVol | Class for pressure dependent standard states that use a constant volume model |
| PDSS_IdealGas | Derived class for pressure dependent standard states of an ideal gas species |
| PDSS_IonsFromNeutral | Derived class for pressure dependent standard states of an ideal gas species |
| PDSS_SSVol | Class for pressure dependent standard states that uses a standard state volume model of some sort |
| Phase | 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 |
| ThermoPhase | Base class for a phase with thermodynamic properties |
| ConstDensityThermo | Overloads the virtual methods of class ThermoPhase to implement the incompressible equation of state |
| IncompressibleSolid | Wrapper for ConstDensityThermo with constructor from file |
| IdealGasPhase | Class IdealGasPhase represents low-density gases that obey the ideal gas equation of state |
| IdealGasMix | Convenience class which inherits from both IdealGasPhase and GasKinetics |
| IdealSolidSolnPhase | Class IdealSolidSolnPhase represents a condensed phase ideal solution compound |
| LatticePhase | A simple thermodynamic model for a bulk phase, assuming a lattice of solid atoms |
| LatticeSolidPhase | A phase that is comprised of a fixed additive combination of other lattice phases |
| MetalPhase | Class MetalPhase represents electrons in a metal |
| Metal | Wrapper for MetalPhase with constructor from file |
| MixtureFugacityTP | 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 |
| RedlichKwongMFTP | This class can handle either an ideal solution or an ideal gas approximation of a phase |
| PureFluidPhase | 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 |
| PureFluid | Wrapper for PureFluidPhase with constructor from file |
| SemiconductorPhase | Class SemiconductorPhase represents electrons and holes in a semiconductor |
| SingleSpeciesTP | Filter class for ThermoPhase |
| FixedChemPotSSTP | Class FixedChemPotSSTP represents a stoichiometric (fixed composition) incompressible substance |
| MetalSHEelectrons | Class MetalSHEelectrons represents electrons within a metal, adjacent to an aqueous electrolyte, that are consistent with the SHE reference electrode |
| StoichSubstanceSSTP | Class StoichSubstanceSSTP represents a stoichiometric (fixed composition) incompressible substance |
| electrodeElectron | Class electrodeElectron represents an electron in a metal using the Standard hydrogen reference electrode |
| MineralEQ3 | Class MineralEQ3 represents a stoichiometric (fixed composition) incompressible substance based on EQ3's parameterization |
| WaterSSTP | Class for single-component water |
| StoichSubstance | Class StoichSubstance represents a stoichiometric (fixed composition) incompressible substance |
| SurfPhase | A simple thermodynamic model for a surface phase, assuming an ideal solution model |
| EdgePhase | A thermodynamic phase representing a one dimensional edge between two surfaces |
| Edge | Convenience class which inherits from both EdgePhase and EdgeKinetics |
| Interface | An interface between multiple bulk phases |
| VPStandardStateTP | This is a filter class for ThermoPhase that implements some prepatory steps for efficiently handling a variable pressure standard state for species |
| GibbsExcessVPSSTP | |
| IonsFromNeutralVPSSTP | |
| MargulesVPSSTP | MargulesVPSSTP is a derived class of GibbsExcessVPSSTP that employs the Margules approximation for the excess Gibbs free energy |
| MolarityIonicVPSSTP | |
| MixedSolventElectrolyte | MixedSolventElectrolyte is a derived class of GibbsExcessVPSSTP that employs the DH and local Marguless approximations for the excess Gibbs free energy |
| PhaseCombo_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 |
| PseudoBinaryVPSSTP | |
| RedlichKisterVPSSTP | RedlichKisterVPSSTP is a derived class of GibbsExcessVPSSTP that employs the Redlich-Kister approximation for the excess Gibbs free energy |
| IdealSolnGasVPSS | An ideal solution or an ideal gas approximation of a phase |
| MaskellSolidSolnPhase | 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 |
| MolalityVPSSTP | |
| DebyeHuckel | Class DebyeHuckel represents a dilute liquid electrolyte phase which obeys the Debye Huckel formulation for nonideality |
| HMWSoln | Class HMWSoln represents a dilute or concentrated liquid electrolyte phase which obeys the Pitzer formulation for nonideality |
| IdealMolalSoln | This phase is based upon the mixing-rule assumption that all molality-based activity coefficients are equal to one |
| Plog | Pressure-dependent reaction rate expressed by logarithmically interpolating between Arrhenius rate expressions at various pressures |
| PropertyCalculator< M > | Classes used by ChemEquil |
| Rate1< R > | This rate coefficient manager supports one parameterization of the rate constant of any type |
| Reaction | Intermediate class which stores data about a reaction and its rate parameterization so that it can be added to a Kinetics object |
| ChebyshevReaction | A pressure-dependent reaction parameterized by a bi-variate Chebyshev polynomial in temperature and pressure |
| ElementaryReaction | A reaction which follows mass-action kinetics with a modified Arrhenius reaction rate |
| InterfaceReaction | A reaction occurring on an interface (i.e. a SurfPhase or an EdgePhase) |
| ElectrochemicalReaction | An interface reaction which involves charged species |
| ThreeBodyReaction | A reaction with a non-reacting third body "M" that acts to add or remove energy from the reacting species |
| FalloffReaction | A reaction that is first-order in [M] at low pressure, like a third-body reaction, but zeroth-order in [M] as pressure increases |
| ChemicallyActivatedReaction | A reaction where the rate decreases as pressure increases due to collisional stabilization of a reaction intermediate |
| PlogReaction | A pressure-dependent reaction parameterized by logarithmically interpolating between Arrhenius rate expressions at various pressures |
| ReactionData | Intermediate class which stores data about a reaction and its rate parameterization before adding the reaction to a Kinetics object |
| ReactionPathDiagram | Reaction path diagrams (graphs) |
| ReactionRules | Rules for parsing and installing reactions |
| ReactionStoichMgr | Reaction mechanism stoichiometry manager |
| ReactorBase | Base class for stirred reactors |
| Reactor | Class Reactor is a general-purpose class for stirred reactors |
| ConstPressureReactor | Class ConstPressureReactor is a class for constant-pressure reactors |
| IdealGasConstPressureReactor | Class ConstPressureReactor is a class for constant-pressure reactors |
| FlowReactor | Adiabatic flow in a constant-area duct |
| IdealGasReactor | Class IdealGasReactor is a class for stirred reactors that is specifically optimized for ideal gases |
| Refiner | Refine Domain1D grids so that profiles satisfy adaptation tolerances |
| ResidData | A simple class to hold an array of parameter values and a pointer to an instance of a subclass of ResidEval |
| ResidEval | Virtual base class for DAE residual function evaluators |
| ResidJacEval | Wrappers for the function evaluators for Nonlinear solvers and Time steppers |
| RootFind | Root finder for 1D problems |
| RootFind::rfTable | Structure containing the iteration history |
| RxnMolChange | Class that includes some bookeeping entries for a reaction or a global reaction defined on a surface |
| RxnOrders | Forward orders |
| solveProb | Method to solve a pseudo steady state of a nonlinear problem |
| solveSP | Method to solve a pseudo steady state surface problem |
| Species | Contains data about a single chemical species |
| SpeciesNode | Nodes in reaction path graphs |
| SpeciesThermo | Pure Virtual base class for the species thermo manager classes |
| GeneralSpeciesThermo | A species thermodynamic property manager for a phase |
| NasaThermo | A species thermodynamic property manager for the NASA polynomial parameterization with two temperature ranges |
| ShomateThermo | A species thermodynamic property manager for the Shomate polynomial parameterization |
| SimpleThermo | |
| SpeciesThermoDuo< T1, T2 > | This species thermo manager requires that all species have one of two parameterizations |
| SpeciesThermoInterpType | Pure Virtual Base class for the thermodynamic manager for an individual species' reference state |
| Adsorbate | An adsorbed surface species |
| ConstCpPoly | A constant-heat capacity species thermodynamic property manager class |
| Mu0Poly | Implements an interpolation of the Gibbs free energy based on a piecewise constant heat capacity approximation |
| Nasa9Poly1 | The NASA 9 polynomial parameterization for one temperature range |
| Nasa9PolyMultiTempRegion | The NASA 9 polynomial parameterization for a single species encompassing multiple temperature regions |
| NasaPoly1 | The NASA polynomial parameterization for one temperature range |
| NasaPoly2 | The NASA polynomial parameterization for two temperature ranges |
| ShomatePoly | The Shomate polynomial parameterization for one temperature range for one species |
| ShomatePoly2 | The Shomate polynomial parameterization for two temperature ranges for one species |
| StatMech | Statistical mechanics |
| STITbyPDSS | Class for the thermodynamic manager for an individual species' reference state which uses the PDSS base class to satisfy the requests |
| SurfaceArrhenius | An Arrhenius rate with coverage-dependent terms |
| ThirdBody | A class for managing third-body efficiencies, including default values |
| ThirdBodyCalc | Calculate and apply third-body effects on reaction rates, including non- unity third-body efficiencies |
| ThirdBodyMgr< _E > | |
| timesConstant< T > | Unary operator to multiply the argument by a constant |
| Tortuosity | Specific Class to handle tortuosity corrections for diffusive transport in porous media using the Bruggeman exponent |
| TortuosityMaxwell | This class implements transport coefficient corrections appropriate for porous media with a dispersed phase |
| TortuosityPercolation | This class implements transport coefficient corrections appropriate for porous media where percolation theory applies |
| Transport | Base class for transport property managers |
| AqueousTransport | Class AqueousTransport implements mixture-averaged transport properties for brine phases |
| DustyGasTransport | Class DustyGasTransport implements the Dusty Gas model for transport in porous media |
| GasTransport | Class GasTransport implements some functions and properties that are shared by the MixTransport and MultiTransport classes |
| MixTransport | Class MixTransport implements mixture-averaged transport properties for ideal gas mixtures |
| MultiTransport | Class MultiTransport implements multicomponent transport properties for ideal gas mixtures |
| HighPressureGasTransport | Class MultiTransport implements transport properties for high pressure gas mixtures |
| LiquidTransport | Class LiquidTransport implements models for transport properties for liquid phases |
| PecosTransport | Class PecosTransport implements mixture-averaged transport properties for ideal gas mixtures |
| SimpleTransport | Class SimpleTransport implements mixture-averaged transport properties for liquid phases |
| SolidTransport | Class SolidTransport implements transport properties for solids |
| WaterTransport | Transport Parameters for pure water |
| TransportData | Base class for transport data for a single species |
| GasTransportData | Transport data for a single gas-phase species which can be used in mixture-averaged or multicomponent transport models |
| TransportParams | Base structure to hold transport model parameters |
| GasTransportParams | This structure holds transport model parameters relevant to transport in ideal gases with a kinetic theory of gases derived transport model |
| LiquidTransportParams | Class LiquidTransportParams holds transport model parameters relevant to transport in mixtures |
| SolidTransportData | Class SolidTransportData holds transport parameters for a specific solid-phase species |
| Unit | Unit conversion utility |
| ValueCache | |
| VCS_COUNTERS | Class to keep track of time and iterations |
| vcs_MultiPhaseEquil | Cantera's Interface to the Multiphase chemical equilibrium solver |
| VCS_PROB | Interface class for the vcs thermo equilibrium solver package, which generally describes the problem to be solved |
| VCS_SOLVE | This is the main structure used to hold the internal data used in vcs_solve_TP(), and to solve TP systems |
| VCS_SPECIES_THERMO | |
| vcs_SpeciesProperties | Properties of a single species |
| vcs_VolPhase | Phase information and Phase calculations for vcs |
| VPSSMgr | Virtual base class for the classes that manage the calculation of standard state properties for all the species in a phase |
| VPSSMgr_ConstVol | Constant Molar Volume e VPSS species thermo manager class |
| VPSSMgr_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 |
| VPSSMgr_IdealGas | A VPSSMgr where all species in the phase obey an ideal gas equation of state |
| VPSSMgr_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 |
| VPSSMgr_Water_HKFT | Manages standard state thermo properties for real water and a set of species which have the HKFT equation of state |
| Wall | Represents a wall between between two ReactorBase objects |
| WaterProps | Used to house several approximation routines for properties of water |
| WaterPropsIAPWS | Class for calculating the equation of state of water |
| WaterPropsIAPWSphi | Low level class for the real description of water |
| XML_Node | Class XML_Node is a tree-based representation of the contents of an XML file |
| XML_Reader | Class XML_Reader reads an XML file into an XML_Node object |
| Rate1< Cantera::Arrhenius > | |
| Rate1< Cantera::ChebyshevRate > | |
| Rate1< Cantera::Plog > | |
| Rate1< Cantera::SurfaceArrhenius > | |
| exception | STL class |
| CanteraError | Base class for exceptions thrown by Cantera classes |
| ArraySizeError | Array size error |
| BEulerErr | Exception class thrown when a BEuler error is encountered |
| CELapackError | Exception thrown when an LAPACK error is encountered associated with inverting or solving a matrix |
| CVodeErr | Exception thrown when a CVODE error is encountered |
| CVodesErr | Exception thrown when a CVODES error is encountered |
| ElementsFrozen | Exception class to indicate a fixed set of elements |
| IDA_Err | Exception thrown when a IDA error is encountered |
| IndexError | An array index is out of range |
| LTPError | Exception thrown if an error is encountered while reading the transport database |
| LTPError | Exception thrown if an error is encountered while reading the transport database |
| LTPmodelError | Exception thrown if an error is encountered while reading the transport database |
| LTPmodelError | Exception thrown if an error is encountered while reading the transport database |
| NotImplementedError | An error indicating that an unimplemented function has been called |
| TransportDBError | Exception thrown if an error is encountered while reading the transport database |
| UnknownSpeciesThermo | Unknown species thermo manager string error |
| UnknownSpeciesThermoModel | Throw a named error for an unknown or missing species thermo model |
| UnknownThermoPhaseModel | Specific error to be thrown if the type of Thermo manager is unrecognized |
| UnknownVPSSMgrModel | Throw a named error for an unknown or missing vpss species thermo model |
| XML_Error | Classs representing a generic XML error condition |
| XML_NoChild | Class representing a specific type of XML file formatting error |
| XML_TagMismatch | Class representing a specific type of XML file formatting error |
| Substance | |
| CarbonDioxide | Pure species representation of carbon dioxide |
| Heptane | Pure species representation of heptane |
| HFC134a | Equation of state for HFC-134a |
| hydrogen | Pure species representation of hydrogen |
| methane | Pure species representation of methane |
| nitrogen | Pure species representation of nitrogen |
| oxygen | Pure species representation of oxygen |
| water | Pure species representation of water |
1.8.6
