A kinetics manager for heterogeneous reaction mechanisms. More...

#include <InterfaceKinetics.h>

Inheritance diagram for InterfaceKinetics:

Detailed Description

A kinetics manager for heterogeneous reaction mechanisms.

The reactions are assumed to occur at a 2D interface between two 3D phases.

There are some important additions to the behavior of the kinetics class due to the presence of multiple phases and a heterogeneous interface. If a reactant phase doesn't exists, that is, has a mole number of zero, a heterogeneous reaction can not proceed from reactants to products. Note it could perhaps proceed from products to reactants if all of the product phases exist.

In order to make the determination of whether a phase exists or not actually involves the specification of additional information to the kinetics object., which heretofore has only had access to intrinsic field information about the phases (for example, temperature, pressure, and mole fraction).

The extrinsic specification of whether a phase exists or not must be specified on top of the intrinsic calculation of the reaction rate. This class carries a set of booleans indicating whether a phase in the heterogeneous mechanism exists or not.

Additionally, the class carries a set of booleans around indicating whether a product phase is stable or not. If a phase is not thermodynamically stable, it may be the case that a particular reaction in a heterogeneous mechanism will create a product species in the unstable phase. However, other reactions in the mechanism will destruct that species. This may cause oscillations in the formation of the unstable phase from time step to time step within a ODE solver, in practice. In order to avoid this situation, a set of booleans is tracked which sets the stability of a phase. If a phase is deemed to be unstable, then species in that phase will not be allowed to be birthed by the kinetics operator. Nonexistent phases are deemed to be unstable by default, but this can be changed.

Definition at line 54 of file InterfaceKinetics.h.

Public Member Functions
	InterfaceKinetics ()=default
	Constructor.

void	resizeReactions () override
	Finalize Kinetics object and associated objects.

string	kineticsType () const override
	Identifies the Kinetics manager type.

void	setElectricPotential (int n, double V)
	Set the electric potential in the nth phase.

void	updateROP () override
	Internal routine that updates the Rates of Progress of the reactions.

void	_update_rates_T ()
	Update properties that depend on temperature.

void	_update_rates_phi ()
	Update properties that depend on the electric potential.

void	_update_rates_C ()
	Update properties that depend on the species mole fractions and/or concentration,.

void	advanceCoverages (double tstep, double rtol=1.e-7, double atol=1.e-14, double maxStepSize=0, size_t maxSteps=20000, size_t maxErrTestFails=7)
	Advance the surface coverages in time.

void	solvePseudoSteadyStateProblem (int ifuncOverride=-1, double timeScaleOverride=1.0)
	Solve for the pseudo steady-state of the surface problem.

void	setIOFlag (int ioFlag)

virtual void	updateMu0 ()
	Update the standard state chemical potentials and species equilibrium constant entries.

void	updateKc ()
	Update the equilibrium constants and stored electrochemical potentials in molar units for all reversible reactions and for all species.

void	setPhaseExistence (const size_t iphase, const int exists)
	Set the existence of a phase in the reaction object.

void	setPhaseStability (const size_t iphase, const int isStable)
	Set the stability of a phase in the reaction object.

int	phaseExistence (const size_t iphase) const
	Gets the phase existence int for the ith phase.

int	phaseStability (const size_t iphase) const
	Gets the phase stability int for the ith phase.

double	interfaceCurrent (const size_t iphase)
	Gets the interface current for the ith phase.

void	setDerivativeSettings (const AnyMap &settings) override
	Set/modify derivative settings.

void	getDerivativeSettings (AnyMap &settings) const override
	Retrieve derivative settings.

Eigen::SparseMatrix< double >	fwdRatesOfProgress_ddCi () override
	Calculate derivatives for forward rates-of-progress with respect to species concentration at constant temperature, pressure and remaining species concentrations.

Eigen::SparseMatrix< double >	revRatesOfProgress_ddCi () override
	Calculate derivatives for forward rates-of-progress with respect to species concentration at constant temperature, pressure and remaining species concentrations.

Eigen::SparseMatrix< double >	netRatesOfProgress_ddCi () override
	Calculate derivatives for net rates-of-progress with respect to species concentration at constant temperature, pressure, and remaining species concentrations.

Reaction Rates Of Progress
void	getEquilibriumConstants (double *kc) override
	Equilibrium constant for all reactions including the voltage term.

void	getDeltaGibbs (double *deltaG) override
	Return the vector of values for the reaction Gibbs free energy change.

void	getDeltaElectrochemPotentials (double *deltaM) override
	Return the vector of values for the reaction electrochemical free energy change.

void	getDeltaEnthalpy (double *deltaH) override
	Return the vector of values for the reactions change in enthalpy.

void	getDeltaEntropy (double *deltaS) override
	Return the vector of values for the reactions change in entropy.

void	getDeltaSSGibbs (double *deltaG) override
	Return the vector of values for the reaction standard state Gibbs free energy change.

void	getDeltaSSEnthalpy (double *deltaH) override
	Return the vector of values for the change in the standard state enthalpies of reaction.

void	getDeltaSSEntropy (double *deltaS) override
	Return the vector of values for the change in the standard state entropies for each reaction.

Reaction Mechanism Informational Query Routines
void	getActivityConcentrations (double *const conc) override
	Get the vector of activity concentrations used in the kinetics object.

void	getFwdRateConstants (double *kfwd) override
	Return the forward rate constants.

void	getRevRateConstants (double *krev, bool doIrreversible=false) override
	Return the reverse rate constants.

Reaction Mechanism Construction
void	addThermo (shared_ptr< ThermoPhase > thermo) override
	Add a thermo phase to the kinetics manager object.

void	init () override
	Prepare the class for the addition of reactions, after all phases have been added.

void	resizeSpecies () override
	Resize arrays with sizes that depend on the total number of species.

bool	addReaction (shared_ptr< Reaction > r, bool resize=true) override
	Add a single reaction to the mechanism.

void	modifyReaction (size_t i, shared_ptr< Reaction > rNew) override
	Modify the rate expression associated with a reaction.

void	setMultiplier (size_t i, double f) override
	Set the multiplier for reaction i to f.

Public Member Functions inherited from Kinetics
virtual pair< size_t, size_t >	checkDuplicates (bool throw_err=true, bool fix=false)
	Check for unmarked duplicate reactions and unmatched marked duplicates.

virtual void	setRoot (shared_ptr< Solution > root)
	Set root Solution holding all phase information.

shared_ptr< Solution >	root () const
	Get the Solution object containing this Kinetics object and associated ThermoPhase objects.

void	registerReactionAddedCallback (void *id, const function< void()> &callback)
	Register a function to be called if reaction is added.

void	removeReactionAddedCallback (void *id)
	Remove the reaction-changed callback function associated with the specified object.

	Kinetics ()=default
	Default constructor.

	Kinetics (const Kinetics &)=delete
	Kinetics objects are not copyable or assignable.

Kinetics &	operator= (const Kinetics &)=delete

size_t	nReactions () const
	Number of reactions in the reaction mechanism.

void	checkReactionIndex (size_t m) const
	Check that the specified reaction index is in range Throws an exception if i is greater than nReactions()

void	checkReactionArraySize (size_t ii) const
	Check that an array size is at least nReactions() Throws an exception if ii is less than nReactions().

void	checkSpeciesIndex (size_t k) const
	Check that the specified species index is in range Throws an exception if k is greater than nSpecies()-1.

void	checkSpeciesArraySize (size_t mm) const
	Check that an array size is at least nSpecies() Throws an exception if kk is less than nSpecies().

size_t	nPhases () const
	The number of phases participating in the reaction mechanism.

void	checkPhaseIndex (size_t m) const
	Check that the specified phase index is in range Throws an exception if m is greater than nPhases()

void	checkPhaseArraySize (size_t mm) const
	Check that an array size is at least nPhases() Throws an exception if mm is less than nPhases().

size_t	phaseIndex (const string &ph) const
	Return the phase index of a phase in the list of phases defined within the object.

shared_ptr< ThermoPhase >	reactionPhase () const
	Return pointer to phase where the reactions occur.

shared_ptr< ThermoPhase >	phase (size_t n=0) const
	Return pointer to phase associated with Kinetics by index.

ThermoPhase &	thermo (size_t n=0)
	This method returns a reference to the nth ThermoPhase object defined in this kinetics mechanism.

const ThermoPhase &	thermo (size_t n=0) const

size_t	nTotalSpecies () const
	The total number of species in all phases participating in the kinetics mechanism.

size_t	kineticsSpeciesIndex (size_t k, size_t n) const
	The location of species k of phase n in species arrays.

string	kineticsSpeciesName (size_t k) const
	Return the name of the kth species in the kinetics manager.

size_t	kineticsSpeciesIndex (const string &nm) const
	This routine will look up a species number based on the input string nm.

ThermoPhase &	speciesPhase (const string &nm)
	This function looks up the name of a species and returns a reference to the ThermoPhase object of the phase where the species resides.

const ThermoPhase &	speciesPhase (const string &nm) const

ThermoPhase &	speciesPhase (size_t k)
	This function takes as an argument the kineticsSpecies index (that is, the list index in the list of species in the kinetics manager) and returns the species' owning ThermoPhase object.

size_t	speciesPhaseIndex (size_t k) const
	This function takes as an argument the kineticsSpecies index (that is, the list index in the list of species in the kinetics manager) and returns the index of the phase owning the species.

virtual void	getFwdRatesOfProgress (double *fwdROP)
	Return the forward rates of progress of the reactions.

virtual void	getRevRatesOfProgress (double *revROP)
	Return the Reverse rates of progress of the reactions.

virtual void	getNetRatesOfProgress (double *netROP)
	Net rates of progress.

virtual void	getReactionDelta (const double property, double deltaProperty) const
	Change in species properties.

virtual void	getRevReactionDelta (const double g, double dg) const
	Given an array of species properties 'g', return in array 'dg' the change in this quantity in the reversible reactions.

virtual void	getThirdBodyConcentrations (double *concm)
	Return a vector of values of effective concentrations of third-body collision partners of any reaction.

virtual const vector< double > &	thirdBodyConcentrations () const
	Provide direct access to current third-body concentration values.

virtual void	getCreationRates (double *cdot)
	Species creation rates [kmol/m^3/s or kmol/m^2/s].

virtual void	getDestructionRates (double *ddot)
	Species destruction rates [kmol/m^3/s or kmol/m^2/s].

virtual void	getNetProductionRates (double *wdot)
	Species net production rates [kmol/m^3/s or kmol/m^2/s].

virtual void	getFwdRateConstants_ddT (double *dkfwd)
	Calculate derivatives for forward rate constants with respect to temperature at constant pressure, molar concentration and mole fractions.

virtual void	getFwdRateConstants_ddP (double *dkfwd)
	Calculate derivatives for forward rate constants with respect to pressure at constant temperature, molar concentration and mole fractions.

virtual void	getFwdRateConstants_ddC (double *dkfwd)
	Calculate derivatives for forward rate constants with respect to molar concentration at constant temperature, pressure and mole fractions.

virtual void	getFwdRatesOfProgress_ddT (double *drop)
	Calculate derivatives for forward rates-of-progress with respect to temperature at constant pressure, molar concentration and mole fractions.

virtual void	getFwdRatesOfProgress_ddP (double *drop)
	Calculate derivatives for forward rates-of-progress with respect to pressure at constant temperature, molar concentration and mole fractions.

virtual void	getFwdRatesOfProgress_ddC (double *drop)
	Calculate derivatives for forward rates-of-progress with respect to molar concentration at constant temperature, pressure and mole fractions.

virtual Eigen::SparseMatrix< double >	fwdRatesOfProgress_ddX ()
	Calculate derivatives for forward rates-of-progress with respect to species mole fractions at constant temperature, pressure and molar concentration.

virtual void	getRevRatesOfProgress_ddT (double *drop)
	Calculate derivatives for reverse rates-of-progress with respect to temperature at constant pressure, molar concentration and mole fractions.

virtual void	getRevRatesOfProgress_ddP (double *drop)
	Calculate derivatives for reverse rates-of-progress with respect to pressure at constant temperature, molar concentration and mole fractions.

virtual void	getRevRatesOfProgress_ddC (double *drop)
	Calculate derivatives for reverse rates-of-progress with respect to molar concentration at constant temperature, pressure and mole fractions.

virtual Eigen::SparseMatrix< double >	revRatesOfProgress_ddX ()
	Calculate derivatives for reverse rates-of-progress with respect to species mole fractions at constant temperature, pressure and molar concentration.

virtual void	getNetRatesOfProgress_ddT (double *drop)
	Calculate derivatives for net rates-of-progress with respect to temperature at constant pressure, molar concentration and mole fractions.

virtual void	getNetRatesOfProgress_ddP (double *drop)
	Calculate derivatives for net rates-of-progress with respect to pressure at constant temperature, molar concentration and mole fractions.

virtual void	getNetRatesOfProgress_ddC (double *drop)
	Calculate derivatives for net rates-of-progress with respect to molar concentration at constant temperature, pressure and mole fractions.

virtual Eigen::SparseMatrix< double >	netRatesOfProgress_ddX ()
	Calculate derivatives for net rates-of-progress with respect to species mole fractions at constant temperature, pressure and molar concentration.

void	getCreationRates_ddT (double *dwdot)
	Calculate derivatives for species creation rates with respect to temperature at constant pressure, molar concentration and mole fractions.

void	getCreationRates_ddP (double *dwdot)
	Calculate derivatives for species creation rates with respect to pressure at constant temperature, molar concentration and mole fractions.

void	getCreationRates_ddC (double *dwdot)
	Calculate derivatives for species creation rates with respect to molar concentration at constant temperature, pressure and mole fractions.

Eigen::SparseMatrix< double >	creationRates_ddX ()
	Calculate derivatives for species creation rates with respect to species mole fractions at constant temperature, pressure and molar concentration.

Eigen::SparseMatrix< double >	creationRates_ddCi ()
	Calculate derivatives for species creation rates with respect to species concentration at constant temperature, pressure, and concentration of all other species.

void	getDestructionRates_ddT (double *dwdot)
	Calculate derivatives for species destruction rates with respect to temperature at constant pressure, molar concentration and mole fractions.

void	getDestructionRates_ddP (double *dwdot)
	Calculate derivatives for species destruction rates with respect to pressure at constant temperature, molar concentration and mole fractions.

void	getDestructionRates_ddC (double *dwdot)
	Calculate derivatives for species destruction rates with respect to molar concentration at constant temperature, pressure and mole fractions.

Eigen::SparseMatrix< double >	destructionRates_ddX ()
	Calculate derivatives for species destruction rates with respect to species mole fractions at constant temperature, pressure and molar concentration.

Eigen::SparseMatrix< double >	destructionRates_ddCi ()
	Calculate derivatives for species destruction rates with respect to species concentration at constant temperature, pressure, and concentration of all other species.

void	getNetProductionRates_ddT (double *dwdot)
	Calculate derivatives for species net production rates with respect to temperature at constant pressure, molar concentration and mole fractions.

void	getNetProductionRates_ddP (double *dwdot)
	Calculate derivatives for species net production rates with respect to pressure at constant temperature, molar concentration and mole fractions.

void	getNetProductionRates_ddC (double *dwdot)
	Calculate derivatives for species net production rates with respect to molar concentration at constant temperature, pressure and mole fractions.

Eigen::SparseMatrix< double >	netProductionRates_ddX ()
	Calculate derivatives for species net production rates with respect to species mole fractions at constant temperature, pressure and molar concentration.

Eigen::SparseMatrix< double >	netProductionRates_ddCi ()
	Calculate derivatives for species net production rates with respect to species concentration at constant temperature, pressure, and concentration of all other species.

virtual double	reactantStoichCoeff (size_t k, size_t i) const
	Stoichiometric coefficient of species k as a reactant in reaction i.

Eigen::SparseMatrix< double >	reactantStoichCoeffs () const
	Stoichiometric coefficient matrix for reactants.

virtual double	productStoichCoeff (size_t k, size_t i) const
	Stoichiometric coefficient of species k as a product in reaction i.

Eigen::SparseMatrix< double >	productStoichCoeffs () const
	Stoichiometric coefficient matrix for products.

Eigen::SparseMatrix< double >	revProductStoichCoeffs () const
	Stoichiometric coefficient matrix for products of reversible reactions.

virtual double	reactantOrder (size_t k, size_t i) const
	Reactant order of species k in reaction i.

virtual double	productOrder (int k, int i) const
	product Order of species k in reaction i.

bool	isReversible (size_t i) const
	True if reaction i has been declared to be reversible.

AnyMap	parameters ()
	Return the parameters for a phase definition which are needed to reconstruct an identical object using the newKinetics function.

shared_ptr< Reaction >	reaction (size_t i)
	Return the Reaction object for reaction i.

shared_ptr< const Reaction >	reaction (size_t i) const

void	skipUndeclaredSpecies (bool skip)
	Determine behavior when adding a new reaction that contains species not defined in any of the phases associated with this kinetics manager.

bool	skipUndeclaredSpecies () const

void	skipUndeclaredThirdBodies (bool skip)
	Determine behavior when adding a new reaction that contains third-body efficiencies for species not defined in any of the phases associated with this kinetics manager.

bool	skipUndeclaredThirdBodies () const

void	setExplicitThirdBodyDuplicateHandling (const string &flag)
	Specify how to handle duplicate third body reactions where one reaction has an explicit third body and the other has the generic third body with a non-zero efficiency for the former third body.

string	explicitThirdBodyDuplicateHandling () const

double	multiplier (size_t i) const
	The current value of the multiplier for reaction i.

virtual void	invalidateCache ()

Protected Member Functions
Internal service methods
Note These methods are for internal use, and seek to avoid code duplication while evaluating terms used for rate constants, rates of progress, and their derivatives.
void	applyEquilibriumConstants (double *rop)
	Multiply rate with inverse equilibrium constant.

Eigen::SparseMatrix< double >	calculateCompositionDerivatives (StoichManagerN &stoich, const vector< double > &in)
	Process mole fraction derivative.

void	assertDerivativesValid (const string &name)
	Helper function ensuring that all rate derivatives can be calculated.

Protected Member Functions inherited from Kinetics
virtual void	updateROP ()

double	checkDuplicateStoich (map< int, double > &r1, map< int, double > &r2) const
	Check whether `r1` and `r2` represent duplicate stoichiometries This function returns a ratio if two reactions are duplicates of one another, and 0.0 otherwise.

Protected Attributes
vector< double >	m_grt
	Temporary work vector of length m_kk.

bool	m_redo_rates = false

vector< double >	m_conc
	Array of concentrations for each species in the kinetics mechanism.

vector< double >	m_actConc
	Array of activity concentrations for each species in the kinetics object.

vector< double >	m_mu0
	Vector of standard state chemical potentials for all species.

vector< double >	m_mu
	Vector of chemical potentials for all species.

vector< double >	m_mu0_Kc
	Vector of standard state electrochemical potentials modified by a standard concentration term.

vector< double >	m_phi
	Vector of phase electric potentials.

SurfPhase *	m_surf = nullptr
	Pointer to the single surface phase.

ImplicitSurfChem *	m_integrator = nullptr
	Pointer to the Implicit surface chemistry object.

bool	m_ROP_ok = false

double	m_temp = 0.0
	Current temperature of the data.

int	m_phaseExistsCheck = false
	Int flag to indicate that some phases in the kinetics mechanism are non-existent.

vector< bool >	m_phaseExists
	Vector of booleans indicating whether phases exist or not.

vector< int >	m_phaseIsStable
	Vector of int indicating whether phases are stable or not.

vector< vector< bool > >	m_rxnPhaseIsReactant
	Vector of vector of booleans indicating whether a phase participates in a reaction as a reactant.

vector< vector< bool > >	m_rxnPhaseIsProduct
	Vector of vector of booleans indicating whether a phase participates in a reaction as a product.

int	m_ioFlag = 0

size_t	m_nDim = 2
	Number of dimensions of reacting phase (2 for InterfaceKinetics, 1 for EdgeKinetics)

vector< double >	m_rbuf0
	Buffers for partial rop results with length nReactions()

vector< double >	m_rbuf1

bool	m_jac_skip_coverage_dependence = false
	A flag used to neglect rate coefficient coverage dependence in derivative formation.

bool	m_jac_skip_electrochemistry = false
	A flag used to neglect electrochemical contributions in derivative formation.

double	m_jac_rtol_delta = 1e-8
	Relative tolerance used in developing numerical portions of specific derivatives.

bool	m_has_electrochemistry = false
	A flag stating if the object uses electrochemistry.

bool	m_has_coverage_dependence = false
	A flag stating if the object has coverage dependent rates.

Protected Attributes inherited from Kinetics
ValueCache	m_cache
	Cache for saved calculations within each Kinetics object.

vector< unique_ptr< MultiRateBase > >	m_rateHandlers
	Vector of rate handlers.

map< string, size_t >	m_rateTypes
	Mapping of rate handlers.

size_t	m_kk = 0
	The number of species in all of the phases that participate in this kinetics mechanism.

vector< double >	m_perturb
	Vector of perturbation factors for each reaction's rate of progress vector.

vector< shared_ptr< Reaction > >	m_reactions
	Vector of Reaction objects represented by this Kinetics manager.

vector< shared_ptr< ThermoPhase > >	m_thermo
	m_thermo is a vector of pointers to ThermoPhase objects that are involved with this kinetics operator

vector< size_t >	m_start
	m_start is a vector of integers specifying the beginning position for the species vector for the n'th phase in the kinetics class.

map< string, size_t >	m_phaseindex
	Mapping of the phase name to the position of the phase within the kinetics object.

size_t	m_mindim = 4
	number of spatial dimensions of lowest-dimensional phase.

vector< double >	m_rfn
	Forward rate constant for each reaction.

vector< double >	m_delta_gibbs0
	Delta G^0 for all reactions.

vector< double >	m_rkcn
	Reciprocal of the equilibrium constant in concentration units.

vector< double >	m_ropf
	Forward rate-of-progress for each reaction.

vector< double >	m_ropr
	Reverse rate-of-progress for each reaction.

vector< double >	m_ropnet
	Net rate-of-progress for each reaction.

vector< size_t >	m_revindex
	Indices of reversible reactions.

vector< size_t >	m_irrev
	Indices of irreversible reactions.

vector< double >	m_dH
	The enthalpy change for each reaction to calculate Blowers-Masel rates.

vector< double >	m_rbuf
	Buffer used for storage of intermediate reaction-specific results.

bool	m_skipUndeclaredSpecies = false
	See skipUndeclaredSpecies()

bool	m_skipUndeclaredThirdBodies = false
	See skipUndeclaredThirdBodies()

bool	m_hasUndeclaredThirdBodies = false
	Flag indicating whether reactions include undeclared third bodies.

string	m_explicit_third_body_duplicates = "warn"

std::weak_ptr< Solution >	m_root
	reference to Solution

map< void *, function< void()> >	m_reactionAddedCallbacks
	Callback functions that are invoked when the reaction is added.

StoichManagerN	m_reactantStoich
	Stoichiometry manager for the reactants for each reaction.

StoichManagerN	m_productStoich
	Stoichiometry manager for the products for each reaction.

StoichManagerN	m_revProductStoich
	Stoichiometry manager for the products of reversible reactions.

Eigen::SparseMatrix< double >	m_stoichMatrix
	Net stoichiometry (products - reactants)

Constructor & Destructor Documentation

◆ InterfaceKinetics()

InterfaceKinetics ( )

default

Constructor.

◆ ~InterfaceKinetics()

~InterfaceKinetics ( )

override

Definition at line 17 of file InterfaceKinetics.cpp.

Member Function Documentation

◆ resizeReactions()

void resizeReactions ( )

overridevirtual

Finalize Kinetics object and associated objects.

Reimplemented from Kinetics.

Definition at line 22 of file InterfaceKinetics.cpp.

◆ kineticsType()

string kineticsType ( ) const

inlineoverridevirtual

Identifies the Kinetics manager type.

Each class derived from Kinetics should override this method to return a meaningful identifier.

Since: Starting in Cantera 3.0, the name returned by this method corresponds to the canonical name used in the YAML input format.

Reimplemented from Kinetics.

Definition at line 64 of file InterfaceKinetics.h.

◆ setElectricPotential()

void setElectricPotential	(	int	n,
		double	V
	)

Set the electric potential in the nth phase.

Parameters

n	phase Index in this kinetics object.
V	Electric potential (volts)

Definition at line 38 of file InterfaceKinetics.cpp.

◆ getEquilibriumConstants()

void getEquilibriumConstants ( double * kc )

overridevirtual

Equilibrium constant for all reactions including the voltage term.

Kc = exp(deltaG/RT)

where deltaG is the electrochemical potential difference between products minus reactants.

Reimplemented from Kinetics.

Definition at line 166 of file InterfaceKinetics.cpp.

◆ getDeltaGibbs()

void getDeltaGibbs ( double * deltaG )

overridevirtual

Return the vector of values for the reaction Gibbs free energy change.

(virtual from Kinetics.h) These values depend upon the concentration of the solution.

units = J kmol-1

Parameters

deltaG Output vector of deltaG's for reactions Length: nReactions().

Reimplemented from Kinetics.

Definition at line 287 of file InterfaceKinetics.cpp.

◆ getDeltaElectrochemPotentials()

void getDeltaElectrochemPotentials ( double * deltaM )

overridevirtual

Return the vector of values for the reaction electrochemical free energy change.

These values depend upon the concentration of the solution and the voltage of the phases

units = J kmol-1

Parameters

deltaM Output vector of deltaM's for reactions Length: nReactions().

Reimplemented from Kinetics.

Definition at line 304 of file InterfaceKinetics.cpp.

◆ getDeltaEnthalpy()

void getDeltaEnthalpy ( double * deltaH )

overridevirtual

Return the vector of values for the reactions change in enthalpy.

These values depend upon the concentration of the solution.

units = J kmol-1

Parameters

deltaH Output vector of deltaH's for reactions Length: nReactions().

Reimplemented from Kinetics.

Definition at line 315 of file InterfaceKinetics.cpp.

◆ getDeltaEntropy()

void getDeltaEntropy ( double * deltaS )

overridevirtual

Return the vector of values for the reactions change in entropy.

These values depend upon the concentration of the solution.

units = J kmol-1 Kelvin-1

Parameters

deltaS Output vector of deltaS's for reactions Length: nReactions().

Reimplemented from Kinetics.

Definition at line 326 of file InterfaceKinetics.cpp.

◆ getDeltaSSGibbs()

void getDeltaSSGibbs ( double * deltaG )

overridevirtual

Return the vector of values for the reaction standard state Gibbs free energy change.

These values don't depend upon the concentration of the solution.

units = J kmol-1

Parameters

deltaG Output vector of ss deltaG's for reactions Length: nReactions().

Reimplemented from Kinetics.

Definition at line 337 of file InterfaceKinetics.cpp.

◆ getDeltaSSEnthalpy()

void getDeltaSSEnthalpy ( double * deltaH )

overridevirtual

Return the vector of values for the change in the standard state enthalpies of reaction.

These values don't depend upon the concentration of the solution.

units = J kmol-1

Parameters

deltaH Output vector of ss deltaH's for reactions Length: nReactions().

Reimplemented from Kinetics.

Definition at line 351 of file InterfaceKinetics.cpp.

◆ getDeltaSSEntropy()

void getDeltaSSEntropy ( double * deltaS )

overridevirtual

Return the vector of values for the change in the standard state entropies for each reaction.

These values don't depend upon the concentration of the solution.

units = J kmol-1 Kelvin-1

Parameters

deltaS Output vector of ss deltaS's for reactions Length: nReactions().

Reimplemented from Kinetics.

Definition at line 368 of file InterfaceKinetics.cpp.

◆ getActivityConcentrations()

void getActivityConcentrations ( double *const conc )

overridevirtual

Get the vector of activity concentrations used in the kinetics object.

Parameters

[out] conc Vector of activity concentrations. Length is equal to the number of species in the kinetics object

Reimplemented from Kinetics.

Definition at line 111 of file InterfaceKinetics.cpp.

◆ getFwdRateConstants()

void getFwdRateConstants ( double * kfwd )

overridevirtual

Return the forward rate constants.

The computed values include all temperature-dependent and pressure-dependent contributions. By default, third-body concentrations are only considered if they are part of the reaction rate definition; for a legacy implementation that includes third-body concentrations see Cantera::use_legacy_rate_constants(). Length is the number of reactions. Units are a combination of kmol, m^3 and s, that depend on the rate expression for the reaction.

Parameters

kfwd	Output vector containing the forward reaction rate constants. Length: nReactions().

Reimplemented from Kinetics.

Definition at line 177 of file InterfaceKinetics.cpp.

◆ getRevRateConstants()

void getRevRateConstants	(	double *	krev,
		bool	doIrreversible = `false`
	)

overridevirtual

Return the reverse rate constants.

The computed values include all temperature-dependent and pressure-dependent contributions. By default, third-body concentrations are only considered if they are part of the reaction rate definition; for a legacy implementation that includes third-body concentrations see Cantera::use_legacy_rate_constants(). Length is the number of reactions. Units are a combination of kmol, m^3 and s, that depend on the rate expression for the reaction. Note, this routine will return rate constants for irreversible reactions if the default for doIrreversible is overridden.

Parameters

krev	Output vector of reverse rate constants
doIrreversible	boolean indicating whether irreversible reactions should be included.

Reimplemented from Kinetics.

Definition at line 186 of file InterfaceKinetics.cpp.

◆ addThermo()

void addThermo ( shared_ptr< ThermoPhase > thermo )

overridevirtual

Add a thermo phase to the kinetics manager object.

This must be done before the function init() is called or before any reactions are input. The lowest dimensional phase, where reactions occur, must be added first.

This function calls Kinetics::addThermo). It also sets the following fields:

   m_phaseExists[]

Parameters

thermo Reference to the ThermoPhase to be added.

Reimplemented from Kinetics.

Definition at line 488 of file InterfaceKinetics.cpp.

◆ init()

void init ( )

overridevirtual

Prepare the class for the addition of reactions, after all phases have been added.

This method is called automatically when the first reaction is added. It needs to be called directly only in the degenerate case where there are no reactions. The base class method does nothing, but derived classes may use this to perform any initialization (allocating arrays, etc.) that requires knowing the phases.

Reimplemented from Kinetics.

Definition at line 495 of file InterfaceKinetics.cpp.

◆ resizeSpecies()

void resizeSpecies ( )

overridevirtual

Resize arrays with sizes that depend on the total number of species.

Automatically called before adding each Reaction and Phase.

Reimplemented from Kinetics.

Definition at line 502 of file InterfaceKinetics.cpp.

◆ addReaction()

bool addReaction	(	shared_ptr< Reaction >	r,
		bool	resize = `true`
	)

overridevirtual

Add a single reaction to the mechanism.

Derived classes should call the base class method in addition to handling their own specialized behavior.

Parameters

r	Pointer to the Reaction object to be added.
resize	If `true`, resizeReactions is called after reaction is added.

Returns: true if the reaction is added or false if it was skipped

Reimplemented from Kinetics.

Definition at line 384 of file InterfaceKinetics.cpp.

◆ modifyReaction()

void modifyReaction	(	size_t	i,
		shared_ptr< Reaction >	rNew
	)

overridevirtual

Modify the rate expression associated with a reaction.

The stoichiometric equation, type of the reaction, reaction orders, third body efficiencies, reversibility, etc. must be unchanged.

Parameters

i	Index of the reaction to be modified
rNew	Reaction with the new rate expressions

Reimplemented from Kinetics.

Definition at line 447 of file InterfaceKinetics.cpp.

◆ setMultiplier()

void setMultiplier	(	size_t	i,
		double	f
	)

overridevirtual

Set the multiplier for reaction i to f.

Parameters

i	index of the reaction
f	value of the multiplier.

Reimplemented from Kinetics.

Definition at line 474 of file InterfaceKinetics.cpp.

◆ updateROP()

void updateROP ( )

overridevirtual

Internal routine that updates the Rates of Progress of the reactions.

This is actually the guts of the functionality of the object

Reimplemented from Kinetics.

Definition at line 201 of file InterfaceKinetics.cpp.

◆ _update_rates_T()

void _update_rates_T ( )

Update properties that depend on temperature.

Current objects that this function updates: m_kdata->m_rfn updateKc();

Definition at line 44 of file InterfaceKinetics.cpp.

◆ _update_rates_phi()

void _update_rates_phi ( )

Update properties that depend on the electric potential.

Definition at line 81 of file InterfaceKinetics.cpp.

◆ _update_rates_C()

void _update_rates_C ( )

Update properties that depend on the species mole fractions and/or concentration,.

This method fills out the array of generalized concentrations by calling method getActivityConcentrations for each phase, which classes representing phases should overload to return the appropriate quantities.

Definition at line 92 of file InterfaceKinetics.cpp.

◆ advanceCoverages()

void advanceCoverages	(	double	tstep,
		double	rtol = `1.e-7`,
		double	atol = `1.e-14`,
		double	maxStepSize = `0`,
		size_t	maxSteps = `20000`,
		size_t	maxErrTestFails = `7`
	)

Advance the surface coverages in time.

This method carries out a time-accurate advancement of the surface coverages for a specified amount of time.

\[ \dot {\theta}_k = \dot s_k (\sigma_k / s_0) \]

Parameters

tstep	Time value to advance the surface coverages
rtol	The relative tolerance for the integrator
atol	The absolute tolerance for the integrator
maxStepSize	The maximum step-size the integrator is allowed to take. If zero, this option is disabled.
maxSteps	The maximum number of time-steps the integrator can take. If not supplied, uses the default value in CVodeIntegrator (20000).
maxErrTestFails	the maximum permissible number of error test failures If not supplied, uses the default value in CVODES (7).

Definition at line 519 of file InterfaceKinetics.cpp.

◆ solvePseudoSteadyStateProblem()

void solvePseudoSteadyStateProblem	(	int	ifuncOverride = `-1`,
		double	timeScaleOverride = `1.0`
	)

Solve for the pseudo steady-state of the surface problem.

This is the same thing as the advanceCoverages() function, but at infinite times.

Note, a direct solve is carried out under the hood here, to reduce the computational time.

Parameters

ifuncOverride	One of the values defined in Surface Problem Solver Methods. The default is -1, which means that the program will decide.
timeScaleOverride	When a pseudo transient is selected this value can be used to override the default time scale for integration which is one. When SFLUX_TRANSIENT is used, this is equal to the time over which the equations are integrated. When SFLUX_INITIALIZE is used, this is equal to the time used in the initial transient algorithm, before the equation system is solved directly.

Definition at line 535 of file InterfaceKinetics.cpp.

◆ setIOFlag()

void setIOFlag ( int ioFlag )

Definition at line 480 of file InterfaceKinetics.cpp.

◆ updateMu0()

void updateMu0 ( )

virtual

Update the standard state chemical potentials and species equilibrium constant entries.

Virtual because it is overridden when dealing with experimental open circuit voltage overrides

Definition at line 148 of file InterfaceKinetics.cpp.

◆ updateKc()

void updateKc ( )

Update the equilibrium constants and stored electrochemical potentials in molar units for all reversible reactions and for all species.

Irreversible reactions have their equilibrium constant set to zero. For reactions involving charged species the equilibrium constant is adjusted according to the electrostatic potential.

Definition at line 117 of file InterfaceKinetics.cpp.

◆ setPhaseExistence()

void setPhaseExistence	(	const size_t	iphase,
		const int	exists
	)

Set the existence of a phase in the reaction object.

Tell the kinetics object whether a phase in the object exists. This is actually an extrinsic specification that must be carried out on top of the intrinsic calculation of the reaction rate. The routine will also flip the IsStable boolean within the kinetics object as well.

Parameters

iphase	Index of the phase. This is the order within the internal thermo vector object
exists	Boolean indicating whether the phase exists or not

Definition at line 549 of file InterfaceKinetics.cpp.

◆ setPhaseStability()

void setPhaseStability	(	const size_t	iphase,
		const int	isStable
	)

Set the stability of a phase in the reaction object.

Tell the kinetics object whether a phase in the object is stable. Species in an unstable phase will not be allowed to have a positive rate of formation from this kinetics object. This is actually an extrinsic specification that must be carried out on top of the intrinsic calculation of the reaction rate.

While conceptually not needed since kinetics is consistent with thermo when taken as a whole, in practice it has found to be very useful to turn off the creation of phases which shouldn't be forming. Typically this can reduce the oscillations in phase formation and destruction which are observed.

Parameters

iphase	Index of the phase. This is the order within the internal thermo vector object
isStable	Flag indicating whether the phase is stable or not

Definition at line 580 of file InterfaceKinetics.cpp.

◆ phaseExistence()

int phaseExistence ( const size_t iphase ) const

Gets the phase existence int for the ith phase.

Parameters

iphase Phase Id

Returns: The int specifying whether the kinetics object thinks the phase exists or not. If it exists, then species in that phase can be a reactant in reactions.

Definition at line 568 of file InterfaceKinetics.cpp.

◆ phaseStability()

int phaseStability ( const size_t iphase ) const

Gets the phase stability int for the ith phase.

Parameters

iphase Phase Id

Returns: The int specifying whether the kinetics object thinks the phase is stable with nonzero mole numbers. If it stable, then the kinetics object will allow for rates of production of of species in that phase that are positive.

Definition at line 574 of file InterfaceKinetics.cpp.

◆ interfaceCurrent()

double interfaceCurrent ( const size_t iphase )

Gets the interface current for the ith phase.

Parameters

iphase Phase Id

Returns: The double specifying the interface current. The interface current is useful when charge transfer reactions occur at an interface. It is defined here as the net positive charge entering the phase specified by the Phase Id. (Units: A/m^2 for a surface reaction, A/m for an edge reaction).

Definition at line 590 of file InterfaceKinetics.cpp.

◆ setDerivativeSettings()

void setDerivativeSettings ( const AnyMap & settings )

overridevirtual

Set/modify derivative settings.

Parameters

settings AnyMap containing settings determining derivative evaluation.

Reimplemented from Kinetics.

Definition at line 643 of file InterfaceKinetics.cpp.

◆ getDerivativeSettings()

void getDerivativeSettings ( AnyMap & settings ) const

overridevirtual

Retrieve derivative settings.

Parameters

settings AnyMap containing settings determining derivative evaluation.

Reimplemented from Kinetics.

Definition at line 659 of file InterfaceKinetics.cpp.

◆ fwdRatesOfProgress_ddCi()

Eigen::SparseMatrix< double > fwdRatesOfProgress_ddCi ( )

overridevirtual

Calculate derivatives for forward rates-of-progress with respect to species concentration at constant temperature, pressure and remaining species concentrations.

The method returns a matrix with nReactions() rows and nTotalSpecies() columns. For a derivative with respect to \( c_i \), all other \( c_j \) are held constant.

Warning: This method is an experimental part of the Cantera API and may be changed or removed without notice.

Since: New in Cantera 3.0.

Reimplemented from Kinetics.

Definition at line 607 of file InterfaceKinetics.cpp.

◆ revRatesOfProgress_ddCi()

Eigen::SparseMatrix< double > revRatesOfProgress_ddCi ( )

overridevirtual

Calculate derivatives for forward rates-of-progress with respect to species concentration at constant temperature, pressure and remaining species concentrations.

The method returns a matrix with nReactions() rows and nTotalSpecies() columns. For a derivative with respect to \( c_i \), all other \( c_j \) are held constant.

Warning: This method is an experimental part of the Cantera API and may be changed or removed without notice.

Since: New in Cantera 3.0.

Reimplemented from Kinetics.

Definition at line 617 of file InterfaceKinetics.cpp.

◆ netRatesOfProgress_ddCi()

Eigen::SparseMatrix< double > netRatesOfProgress_ddCi ( )

overridevirtual

Calculate derivatives for net rates-of-progress with respect to species concentration at constant temperature, pressure, and remaining species concentrations.

The method returns a matrix with nReactions() rows and nTotalSpecies() columns. For a derivative with respect to \( c_i \), all other \( c_j \) are held constant.

Warning: This method is an experimental part of the Cantera API and may be changed or removed without notice.

Since: New in Cantera 3.0.

Reimplemented from Kinetics.

Definition at line 628 of file InterfaceKinetics.cpp.

◆ applyEquilibriumConstants()

void applyEquilibriumConstants ( double * rop )

protected

Multiply rate with inverse equilibrium constant.

Definition at line 684 of file InterfaceKinetics.cpp.

◆ calculateCompositionDerivatives()

Eigen::SparseMatrix< double > calculateCompositionDerivatives	(	StoichManagerN &	stoich,
		const vector< double > &	in
	)

protected

Process mole fraction derivative.

Parameters

stoich	stoichiometry manager
in	rate expression used for the derivative calculation

Returns: a sparse matrix of derivative contributions for each reaction of dimensions nTotalReactions by nTotalSpecies

Definition at line 666 of file InterfaceKinetics.cpp.

◆ assertDerivativesValid()

void assertDerivativesValid ( const string & name )

protected

Helper function ensuring that all rate derivatives can be calculated.

Parameters

name	method name used for error output

Exceptions

CanteraError if coverage dependence or electrochemical reactions are included

Definition at line 675 of file InterfaceKinetics.cpp.

Member Data Documentation

◆ m_grt

vector<double> m_grt

protected

Temporary work vector of length m_kk.

Definition at line 318 of file InterfaceKinetics.h.

◆ m_redo_rates

bool m_redo_rates = false

protected

Definition at line 320 of file InterfaceKinetics.h.

◆ m_conc

vector<double> m_conc

protected

Array of concentrations for each species in the kinetics mechanism.

An array of generalized concentrations \( C_k \) that are defined such that \( a_k = C_k / C^0_k, \) where \( C^0_k \) is a standard concentration/ These generalized concentrations are used by this kinetics manager class to compute the forward and reverse rates of elementary reactions. The "units" for the concentrations of each phase depend upon the implementation of kinetics within that phase. The order of the species within the vector is based on the order of listed ThermoPhase objects in the class, and the order of the species within each ThermoPhase class.

Definition at line 334 of file InterfaceKinetics.h.

◆ m_actConc

vector<double> m_actConc

protected

Array of activity concentrations for each species in the kinetics object.

An array of activity concentrations \( Ca_k \) that are defined such that \( a_k = Ca_k / C^0_k, \) where \( C^0_k \) is a standard concentration. These activity concentrations are used by this kinetics manager class to compute the forward and reverse rates of elementary reactions. The "units" for the concentrations of each phase depend upon the implementation of kinetics within that phase. The order of the species within the vector is based on the order of listed ThermoPhase objects in the class, and the order of the species within each ThermoPhase class.

Definition at line 348 of file InterfaceKinetics.h.

◆ m_mu0

vector<double> m_mu0

protected

Vector of standard state chemical potentials for all species.

This vector contains a temporary vector of standard state chemical potentials for all of the species in the kinetics object

Length = m_kk. Units = J/kmol.

Definition at line 357 of file InterfaceKinetics.h.

◆ m_mu

vector<double> m_mu

protected

Vector of chemical potentials for all species.

This vector contains a vector of chemical potentials for all of the species in the kinetics object

Length = m_kk. Units = J/kmol.

Definition at line 366 of file InterfaceKinetics.h.

◆ m_mu0_Kc

vector<double> m_mu0_Kc

protected

Vector of standard state electrochemical potentials modified by a standard concentration term.

This vector contains a temporary vector of standard state electrochemical potentials + RTln(Cs) for all of the species in the kinetics object

In order to get the units correct for the concentration equilibrium constant, each species needs to have an RT ln(Cs) added to its contribution to the equilibrium constant Cs is the standard concentration for the species. Frequently, for solid species, Cs is equal to 1. However, for gases Cs is P/RT. Length = m_kk. Units = J/kmol.

Definition at line 380 of file InterfaceKinetics.h.

◆ m_phi

vector<double> m_phi

protected

Vector of phase electric potentials.

Temporary vector containing the potential of each phase in the kinetics object. length = number of phases. Units = Volts.

Definition at line 387 of file InterfaceKinetics.h.

◆ m_surf

SurfPhase* m_surf = nullptr

protected

Pointer to the single surface phase.

Definition at line 390 of file InterfaceKinetics.h.

◆ m_integrator

ImplicitSurfChem* m_integrator = nullptr

protected

Pointer to the Implicit surface chemistry object.

Note this object is owned by this InterfaceKinetics object. It may only be used to solve this single InterfaceKinetics object's surface problem uncoupled from other surface phases.

Definition at line 398 of file InterfaceKinetics.h.

◆ m_ROP_ok

bool m_ROP_ok = false

protected

Definition at line 400 of file InterfaceKinetics.h.

◆ m_temp

double m_temp = 0.0

protected

Current temperature of the data.

Definition at line 403 of file InterfaceKinetics.h.

◆ m_phaseExistsCheck

int m_phaseExistsCheck = false

protected

Int flag to indicate that some phases in the kinetics mechanism are non-existent.

We change the ROP vectors to make sure that non-existent phases are treated correctly in the kinetics operator. The value of this is equal to the number of phases which don't exist.

Definition at line 412 of file InterfaceKinetics.h.

◆ m_phaseExists

vector<bool> m_phaseExists

protected

Vector of booleans indicating whether phases exist or not.

Vector of booleans indicating whether a phase exists or not. We use this to set the ROP's so that unphysical things don't happen. For example, a reaction can't go in the forwards direction if a phase in which a reactant is present doesn't exist. Because InterfaceKinetics deals with intrinsic quantities only normally, nowhere else is this extrinsic concept introduced except here.

length = number of phases in the object. By default all phases exist.

Definition at line 425 of file InterfaceKinetics.h.

◆ m_phaseIsStable

vector<int> m_phaseIsStable

protected

Vector of int indicating whether phases are stable or not.

Vector of booleans indicating whether a phase is stable or not under the current conditions. We use this to set the ROP's so that unphysical things don't happen.

length = number of phases in the object. By default all phases are stable.

Definition at line 435 of file InterfaceKinetics.h.

◆ m_rxnPhaseIsReactant

vector<vector<bool> > m_rxnPhaseIsReactant

protected

Vector of vector of booleans indicating whether a phase participates in a reaction as a reactant.

m_rxnPhaseIsReactant[j][p] indicates whether a species in phase p participates in reaction j as a reactant.

Definition at line 443 of file InterfaceKinetics.h.

◆ m_rxnPhaseIsProduct

vector<vector<bool> > m_rxnPhaseIsProduct

protected

Vector of vector of booleans indicating whether a phase participates in a reaction as a product.

m_rxnPhaseIsReactant[j][p] indicates whether a species in phase p participates in reaction j as a product.

Definition at line 451 of file InterfaceKinetics.h.

◆ m_ioFlag

int m_ioFlag = 0

protected

Definition at line 453 of file InterfaceKinetics.h.

◆ m_nDim

size_t m_nDim = 2

protected

Number of dimensions of reacting phase (2 for InterfaceKinetics, 1 for EdgeKinetics)

Definition at line 457 of file InterfaceKinetics.h.

◆ m_rbuf0

vector<double> m_rbuf0

protected

Buffers for partial rop results with length nReactions()

Definition at line 460 of file InterfaceKinetics.h.

◆ m_rbuf1

vector<double> m_rbuf1

protected

Definition at line 461 of file InterfaceKinetics.h.

◆ m_jac_skip_coverage_dependence

bool m_jac_skip_coverage_dependence = false

protected

A flag used to neglect rate coefficient coverage dependence in derivative formation.

Definition at line 465 of file InterfaceKinetics.h.

◆ m_jac_skip_electrochemistry

bool m_jac_skip_electrochemistry = false

protected

A flag used to neglect electrochemical contributions in derivative formation.

Definition at line 467 of file InterfaceKinetics.h.

◆ m_jac_rtol_delta

double m_jac_rtol_delta = 1e-8

protected

Relative tolerance used in developing numerical portions of specific derivatives.

Definition at line 469 of file InterfaceKinetics.h.

◆ m_has_electrochemistry

bool m_has_electrochemistry = false

protected

A flag stating if the object uses electrochemistry.

Definition at line 471 of file InterfaceKinetics.h.

◆ m_has_coverage_dependence

bool m_has_coverage_dependence = false

protected

A flag stating if the object has coverage dependent rates.

Definition at line 473 of file InterfaceKinetics.h.

The documentation for this class was generated from the following files:

Detailed Description

Public Member Functions

Protected Member Functions

Protected Attributes

Constructor & Destructor Documentation

◆ InterfaceKinetics()

◆ ~InterfaceKinetics()

Member Function Documentation

◆ resizeReactions()

◆ kineticsType()

◆ setElectricPotential()

◆ getEquilibriumConstants()

◆ getDeltaGibbs()

◆ getDeltaElectrochemPotentials()

◆ getDeltaEnthalpy()

◆ getDeltaEntropy()

◆ getDeltaSSGibbs()

◆ getDeltaSSEnthalpy()

◆ getDeltaSSEntropy()

◆ getActivityConcentrations()

◆ getFwdRateConstants()

◆ getRevRateConstants()

◆ addThermo()

◆ init()

◆ resizeSpecies()

◆ addReaction()

◆ modifyReaction()

◆ setMultiplier()

◆ updateROP()

◆ _update_rates_T()

◆ _update_rates_phi()

◆ _update_rates_C()

◆ advanceCoverages()

◆ solvePseudoSteadyStateProblem()

◆ setIOFlag()

◆ updateMu0()

◆ updateKc()

◆ setPhaseExistence()

◆ setPhaseStability()

◆ phaseExistence()

◆ phaseStability()

◆ interfaceCurrent()

◆ setDerivativeSettings()

◆ getDerivativeSettings()

◆ fwdRatesOfProgress_ddCi()

◆ revRatesOfProgress_ddCi()

◆ netRatesOfProgress_ddCi()

◆ applyEquilibriumConstants()

◆ calculateCompositionDerivatives()

◆ assertDerivativesValid()

Member Data Documentation

◆ m_grt

◆ m_redo_rates

◆ m_conc

◆ m_actConc

◆ m_mu0

◆ m_mu

◆ m_mu0_Kc

◆ m_phi

◆ m_surf

◆ m_integrator

◆ m_ROP_ok

◆ m_temp

◆ m_phaseExistsCheck

◆ m_phaseExists

◆ m_phaseIsStable

◆ m_rxnPhaseIsReactant

◆ m_rxnPhaseIsProduct

◆ m_ioFlag

◆ m_nDim

◆ m_rbuf0

◆ m_rbuf1

◆ m_jac_skip_coverage_dependence

◆ m_jac_skip_electrochemistry

◆ m_jac_rtol_delta

◆ m_has_electrochemistry

◆ m_has_coverage_dependence