Cantera  2.0
Public Member Functions | Protected Member Functions | Protected Attributes | List of all members
Interface Class Reference

An interface between multiple bulk phases. More...

#include <Interface.h>

Inheritance diagram for Interface:
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Public Member Functions

 Interface (std::string infile, std::string id, std::vector< Cantera::ThermoPhase * > otherPhases)
 Constructor.
 
 Interface (const Interface &ii)
 Copy Constructor.
 
Interfaceoperator= (const Interface &right)
 Assignment operator.
 
virtual ~Interface ()
 Destructor. Does nothing.
 
bool operator! ()
 Not operator.
 
bool ready () const
 return whether the object has been instantiated
 
ThermoPhaseduplMyselfAsThermoPhase () const
 Duplicator from the ThermoPhase parent class.
 
virtual int eosType () const
 Equation of state type flag.
 
virtual doublereal enthalpy_mole () const
 Return the Molar Enthalpy. Units: J/kmol.
 
virtual doublereal intEnergy_mole () const
 Return the Molar Internal Energy. Units: J/kmol.
 
virtual void getChemPotentials (doublereal *mu) const
 Get the species chemical potentials. Units: J/kmol.
 
virtual void getPartialMolarEnthalpies (doublereal *hbar) const
 Returns an array of partial molar enthalpies for the species in the mixture.
 
virtual void getPartialMolarEntropies (doublereal *sbar) const
 Returns an array of partial molar entropies of the species in the solution.
 
virtual void getPartialMolarCp (doublereal *cpbar) const
 Return an array of partial molar heat capacities for the species in the mixture.
 
virtual void getPartialMolarVolumes (doublereal *vbar) const
 Return an array of partial molar volumes for the species in the mixture.
 
virtual void getStandardChemPotentials (doublereal *mu0) const
 Get the array of chemical potentials at unit activity for the standard state species at the current T and P of the solution.
 
virtual void getActivityConcentrations (doublereal *c) const
 Return a vector of activity concentrations for each species.
 
virtual doublereal standardConcentration (size_t k=0) const
 Return the standard concentration for the kth species.
 
virtual doublereal logStandardConc (size_t k=0) const
 Return the log of the standard concentration for the kth species.
 
virtual void setParameters (int n, doublereal *const c)
 Set the equation of state parameters from the argument list.
 
virtual void setParametersFromXML (const XML_Node &thermoData)
 Set the Equation-of-State parameters by reading an XML Node Input.
 
virtual void initThermo ()
 Initialize the SurfPhase object after all species have been set up.
 
virtual void setStateFromXML (const XML_Node &state)
 Set the initial state of the Surface Phase from an XML_Node.
 
doublereal siteDensity ()
 Returns the site density.
 
void setPotentialEnergy (int k, doublereal pe)
 Sets the potential energy of species k.
 
doublereal potentialEnergy (int k)
 Return the potential energy of species k.
 
void setSiteDensity (doublereal n0)
 Set the site density of the surface phase (kmol m-2)
 
virtual void getGibbs_RT (doublereal *grt) const
 Get the nondimensional Gibbs functions for the species in their standard states at the current T and P of the solution.
 
virtual void getEnthalpy_RT (doublereal *hrt) const
 Get the nondimensional Enthalpy functions for the species standard states at their standard states at the current T and P of the solution.
 
virtual void getEntropy_R (doublereal *sr) const
 Get the array of nondimensional Entropy functions for the species standard states at the current T and P of the solution.
 
virtual void getCp_R (doublereal *cpr) const
 Get the nondimensional Heat Capacities at constant pressure for the species standard states at the current T and P of the solution.
 
virtual void getStandardVolumes (doublereal *vol) const
 Get the molar volumes of the species standard states at the current T and P of the solution.
 
virtual doublereal pressure () const
 Return the thermodynamic pressure (Pa).
 
virtual void setPressure (doublereal p)
 Set the internally stored pressure (Pa) at constant temperature and composition.
 
virtual void getGibbs_RT_ref (doublereal *grt) const
 Returns the vector of nondimensional Gibbs Free Energies of the reference state at the current temperature of the solution and the reference pressure for the species.
 
virtual void getEnthalpy_RT_ref (doublereal *hrt) const
 Returns the vector of nondimensional enthalpies of the reference state at the current temperature of the solution and the reference pressure for the species.
 
virtual void getEntropy_R_ref (doublereal *er) const
 Returns the vector of nondimensional entropies of the reference state at the current temperature of the solution and the reference pressure for each species.
 
virtual void getCp_R_ref (doublereal *cprt) const
 Returns the vector of nondimensional constant pressure heat capacities of the reference state at the current temperature of the solution and reference pressure for each species.
 
void setCoverages (const doublereal *theta)
 Set the surface site fractions to a specified state.
 
void setCoveragesNoNorm (const doublereal *theta)
 Set the surface site fractions to a specified state.
 
void setCoveragesByName (std::string cov)
 Set the coverages from a string of colon-separated name:value pairs.
 
void getCoverages (doublereal *theta) const
 Return a vector of surface coverages.
 
doublereal _RT () const
 Return the Gas Constant multiplied by the current temperature.
 
XML_Nodexml ()
 Returns a reference to the XML_Node stored for the phase.
 
void saveState (vector_fp &state) const
 Save the current internal state of the phase Write to vector 'state' the current internal state.
 
void saveState (size_t lenstate, doublereal *state) const
 Write to array 'state' the current internal state.
 
void restoreState (const vector_fp &state)
 Restore a state saved on a previous call to saveState.
 
void restoreState (size_t lenstate, const doublereal *state)
 Restore the state of the phase from a previously saved state vector.
 
doublereal molecularWeight (size_t k) const
 Molecular weight of species k.
 
doublereal molarMass (size_t k) const
 Return the Molar mass of species k Alternate name for molecular weight.
 
void getMolecularWeights (vector_fp &weights) const
 Copy the vector of molecular weights into vector weights.
 
void getMolecularWeights (int iwt, doublereal *weights) const
 Copy the vector of molecular weights into array weights.
 
void getMolecularWeights (doublereal *weights) const
 Copy the vector of molecular weights into array weights.
 
const vector_fpmolecularWeights () const
 Return a const reference to the internal vector of molecular weights.
 
doublereal size (size_t k) const
 This routine returns the size of species k.
 
doublereal charge (size_t k) const
 Dimensionless electrical charge of a single molecule of species k The charge is normalized by the the magnitude of the electron charge.
 
doublereal chargeDensity () const
 Charge density [C/m^3].
 
size_t nDim () const
 Returns the number of spatial dimensions (1, 2, or 3)
 
void setNDim (size_t ndim)
 Set the number of spatial dimensions (1, 2, or 3).
 
virtual void freezeSpecies ()
 Call when finished adding species.
 
bool speciesFrozen ()
 True if freezeSpecies has been called.
 
int stateMFNumber () const
 Return the State Mole Fraction Number.
 
void stateMFChangeCalc (bool forceChange=false)
 Every time the mole fractions have changed, this routine will increment the stateMFNumber.
 
virtual KineticsduplMyselfAsKinetics (const std::vector< thermo_t * > &tpVector) const
 Duplication routine for objects which inherit from Kinetics.
 
virtual int ID () const
 Return the ID of the kinetics object.
 
virtual int type () const
 Return the type of the kinetics object.
 
void setElectricPotential (int n, doublereal V)
 Set the electric potential in the nth phase.
 
void incrementRxnCount ()
 Increment the number of reactions in the mechanism by one.
 
void selectPhase (const doublereal *data, const thermo_t *phase, doublereal *phase_data)
 Extract from array data the portion pertaining to phase phase.
 
Information Methods
virtual doublereal refPressure () const
 Returns the reference pressure in Pa.
 
virtual doublereal minTemp (size_t k=npos) const
 Minimum temperature for which the thermodynamic data for the species or phase are valid.
 
doublereal Hf298SS (const int k) const
 Report the 298 K Heat of Formation of the standard state of one species (J kmol-1)
 
virtual void modifyOneHf298SS (const int k, const doublereal Hf298New)
 Modify the value of the 298 K Heat of Formation of one species in the phase (J kmol-1)
 
virtual doublereal maxTemp (size_t k=npos) const
 Maximum temperature for which the thermodynamic data for the species are valid.
 
bool chargeNeutralityNecessary () const
 Returns the chargeNeutralityNecessity boolean.
 
Molar Thermodynamic Properties of the Solution
virtual doublereal entropy_mole () const
 Molar entropy. Units: J/kmol/K.
 
virtual doublereal gibbs_mole () const
 Molar Gibbs function. Units: J/kmol.
 
virtual doublereal cp_mole () const
 Molar heat capacity at constant pressure. Units: J/kmol/K.
 
virtual doublereal cv_mole () const
 Molar heat capacity at constant volume. Units: J/kmol/K.
 
Mechanical Properties
virtual doublereal isothermalCompressibility () const
 Returns the isothermal compressibility. Units: 1/Pa.
 
virtual doublereal thermalExpansionCoeff () const
 Return the volumetric thermal expansion coefficient. Units: 1/K.
 
virtual void updateDensity ()
 
Electric Potential

The phase may be at some non-zero electrical potential.

These methods set or get the value of the electric potential.

void setElectricPotential (doublereal v)
 Set the electric potential of this phase (V).
 
doublereal electricPotential () const
 Returns the electric potential of this phase (V).
 
Activities, Standard States, and Activity Concentrations

The activity \(a_k\) of a species in solution is related to the chemical potential by

\[ \mu_k = \mu_k^0(T,P) + \hat R T \log a_k. \]

The quantity \(\mu_k^0(T,P)\) is the standard chemical potential at unit activity, which depends on temperature and pressure, but not on composition.

The activity is dimensionless.

virtual int activityConvention () const
 This method returns the convention used in specification of the activities, of which there are currently two, molar- and molality-based conventions.
 
virtual int standardStateConvention () const
 This method returns the convention used in specification of the standard state, of which there are currently two, temperature based, and variable pressure based.
 
virtual void getUnitsStandardConc (double *uA, int k=0, int sizeUA=6) const
 Returns the units of the standard and generalized concentrations.
 
virtual void getActivities (doublereal *a) const
 Get the array of non-dimensional activities at the current solution temperature, pressure, and solution concentration.
 
virtual void getActivityCoefficients (doublereal *ac) const
 Get the array of non-dimensional molar-based activity coefficients at the current solution temperature, pressure, and solution concentration.
 
virtual void getLnActivityCoefficients (doublereal *lnac) const
 Get the array of non-dimensional molar-based ln activity coefficients at the current solution temperature, pressure, and solution concentration.
 
Partial Molar Properties of the Solution
virtual void getChemPotentials_RT (doublereal *mu) const
 Get the array of non-dimensional species chemical potentials These are partial molar Gibbs free energies.
 
void getElectrochemPotentials (doublereal *mu) const
 Get the species electrochemical potentials.
 
virtual void getPartialMolarIntEnergies (doublereal *ubar) const
 Return an array of partial molar internal energies for the species in the mixture.
 
virtual void getdPartialMolarVolumes_dT (doublereal *d_vbar_dT) const
 Return an array of derivatives of partial molar volumes wrt temperature for the species in the mixture.
 
virtual void getdPartialMolarVolumes_dP (doublereal *d_vbar_dP) const
 Return an array of derivatives of partial molar volumes wrt pressure for the species in the mixture.
 
Properties of the Standard State of the Species in the Solution
virtual void getPureGibbs (doublereal *gpure) const
 Get the Gibbs functions for the standard state of the species at the current T and P of the solution.
 
virtual void getIntEnergy_RT (doublereal *urt) const
 Returns the vector of nondimensional Internal Energies of the standard state species at the current T and P of the solution.
 
virtual void getdStandardVolumes_dT (doublereal *d_vol_dT) const
 Get the derivative of the molar volumes of the species standard states wrt temperature at the current T and P of the solution.
 
virtual void getdStandardVolumes_dP (doublereal *d_vol_dP) const
 Get the derivative molar volumes of the species standard states wrt pressure at the current T and P of the solution.
 
Thermodynamic Values for the Species Reference States
virtual void getGibbs_ref (doublereal *g) const
 Returns the vector of the gibbs function of the reference state at the current temperature of the solution and the reference pressure for the species.
 
virtual void getIntEnergy_RT_ref (doublereal *urt) const
 Returns the vector of nondimensional internal Energies of the reference state at the current temperature of the solution and the reference pressure for each species.
 
virtual void getStandardVolumes_ref (doublereal *vol) const
 Get the molar volumes of the species reference states at the current T and P_ref of the solution.
 
virtual void setReferenceComposition (const doublereal *const x)
 Sets the reference composition.
 
virtual void getReferenceComposition (doublereal *const x) const
 Gets the reference composition.
 
Specific Properties
doublereal enthalpy_mass () const
 Specific enthalpy.
 
doublereal intEnergy_mass () const
 Specific internal energy.
 
doublereal entropy_mass () const
 Specific entropy.
 
doublereal gibbs_mass () const
 Specific Gibbs function.
 
doublereal cp_mass () const
 Specific heat at constant pressure.
 
doublereal cv_mass () const
 Specific heat at constant volume.
 
Setting the State

These methods set all or part of the thermodynamic state.

virtual void setState_TPX (doublereal t, doublereal p, const doublereal *x)
 Set the temperature (K), pressure (Pa), and mole fractions.
 
void setState_TPX (doublereal t, doublereal p, compositionMap &x)
 Set the temperature (K), pressure (Pa), and mole fractions.
 
void setState_TPX (doublereal t, doublereal p, const std::string &x)
 Set the temperature (K), pressure (Pa), and mole fractions.
 
void setState_TPY (doublereal t, doublereal p, const doublereal *y)
 Set the internally stored temperature (K), pressure (Pa), and mass fractions of the phase.
 
void setState_TPY (doublereal t, doublereal p, compositionMap &y)
 Set the internally stored temperature (K), pressure (Pa), and mass fractions of the phase.
 
void setState_TPY (doublereal t, doublereal p, const std::string &y)
 Set the internally stored temperature (K), pressure (Pa), and mass fractions of the phase.
 
void setState_TP (doublereal t, doublereal p)
 Set the temperature (K) and pressure (Pa)
 
void setState_PX (doublereal p, doublereal *x)
 Set the pressure (Pa) and mole fractions.
 
void setState_PY (doublereal p, doublereal *y)
 Set the internally stored pressure (Pa) and mass fractions.
 
virtual void setState_HP (doublereal h, doublereal p, doublereal tol=1.e-4)
 Set the internally stored specific enthalpy (J/kg) and pressure (Pa) of the phase.
 
virtual void setState_UV (doublereal u, doublereal v, doublereal tol=1.e-4)
 Set the specific internal energy (J/kg) and specific volume (m^3/kg).
 
virtual void setState_SP (doublereal s, doublereal p, doublereal tol=1.e-4)
 Set the specific entropy (J/kg/K) and pressure (Pa).
 
virtual void setState_SV (doublereal s, doublereal v, doublereal tol=1.e-4)
 Set the specific entropy (J/kg/K) and specific volume (m^3/kg).
 
Chemical Equilibrium

Chemical equilibrium.

virtual void setToEquilState (const doublereal *lambda_RT)
 This method is used by the ChemEquil equilibrium solver.
 
void setElementPotentials (const vector_fp &lambda)
 Stores the element potentials in the ThermoPhase object.
 
bool getElementPotentials (doublereal *lambda) const
 Returns the element potentials stored in the ThermoPhase object.
 
Critical State Properties.

These methods are only implemented by some subclasses, and may be moved out of ThermoPhase at a later date.

virtual doublereal critTemperature () const
 Critical temperature (K).
 
virtual doublereal critPressure () const
 Critical pressure (Pa).
 
virtual doublereal critDensity () const
 Critical density (kg/m3).
 
Saturation Properties.

These methods are only implemented by subclasses that implement full liquid-vapor equations of state.

They may be moved out of ThermoPhase at a later date.

virtual doublereal satTemperature (doublereal p) const
 Return the saturation temperature given the pressure.
 
virtual doublereal satPressure (doublereal t) const
 Return the saturation pressure given the temperature.
 
virtual doublereal vaporFraction () const
 Return the fraction of vapor at the current conditions.
 
virtual void setState_Tsat (doublereal t, doublereal x)
 Set the state to a saturated system at a particular temperature.
 
virtual void setState_Psat (doublereal p, doublereal x)
 Set the state to a saturated system at a particular pressure.
 
Initialization Methods - For Internal Use (ThermoPhase)
void saveSpeciesData (const size_t k, const XML_Node *const data)
 Store a reference pointer to the XML tree containing the species data for this phase.
 
const std::vector< const
XML_Node * > & 
speciesData () const
 Return a pointer to the vector of XML nodes containing the species data for this phase.
 
void setSpeciesThermo (SpeciesThermo *spthermo)
 Install a species thermodynamic property manager.
 
virtual SpeciesThermospeciesThermo (int k=-1)
 Return a changeable reference to the calculation manager for species reference-state thermodynamic properties.
 
virtual void initThermoFile (std::string inputFile, std::string id)
 
virtual void initThermoXML (XML_Node &phaseNode, std::string id)
 Import and initialize a ThermoPhase object using an XML tree.
 
virtual void installSlavePhases (Cantera::XML_Node *phaseNode)
 Add in species from Slave phases.
 
virtual void getParameters (int &n, doublereal *const c) const
 Get the equation of state parameters in a vector.
 
Derivatives of Thermodynamic Variables needed for Applications
virtual void getdlnActCoeffds (const doublereal dTds, const doublereal *const dXds, doublereal *dlnActCoeffds) const
 Get the change in activity coefficients wrt changes in state (temp, mole fraction, etc) along a line in parameter space or along a line in physical space.
 
virtual void getdlnActCoeffdlnX_diag (doublereal *dlnActCoeffdlnX_diag) const
 Get the array of ln mole fraction derivatives of the log activity coefficients - diagonal component only.
 
virtual void getdlnActCoeffdlnN_diag (doublereal *dlnActCoeffdlnN_diag) const
 Get the array of log species mole number derivatives of the log activity coefficients.
 
virtual void getdlnActCoeffdlnN (const size_t ld, doublereal *const dlnActCoeffdlnN)
 Get the array of derivatives of the log activity coefficients with respect to the log of the species mole numbers.
 
virtual void getdlnActCoeffdlnN_numderiv (const size_t ld, doublereal *const dlnActCoeffdlnN)
 
Printing
virtual std::string report (bool show_thermo=true) const
 returns a summary of the state of the phase as a string
 
virtual void reportCSV (std::ofstream &csvFile) const
 returns a summary of the state of the phase to a comma separated file
 
Name and ID

Class Phase contains two strings that identify a phase. The ID is the value of the ID attribute of the XML phase node that is used to initialize a phase when it is read. The name field is also initialized to the value of the ID attribute of the XML phase node.

However, the name field may be changed to another value during the course of a calculation. For example, if a phase is located in two places, but has the same constitutive input, the ids of the two phases will be the same, but the names of the two phases may be different.

It is an error to have two phases in a single problem with the same name or the same id (or the name from one phase being the same as the id of another phase). Thus, it is expected that there is a 1-1 correspondence between names and unique phases within a Cantera problem.

std::string id () const
 Return the string id for the phase.
 
void setID (std::string id)
 Set the string id for the phase.
 
std::string name () const
 Return the name of the phase.
 
void setName (std::string nm)
 Sets the string name for the phase.
 
Element and Species Information
std::string elementName (size_t m) const
 Name of the element with index m.
 
size_t elementIndex (std::string name) const
 Return the index of element named 'name'.
 
const std::vector< std::string > & elementNames () const
 Return a read-only reference to the vector of element names.
 
doublereal atomicWeight (size_t m) const
 Atomic weight of element m.
 
doublereal entropyElement298 (size_t m) const
 Entropy of the element in its standard state at 298 K and 1 bar.
 
int atomicNumber (size_t m) const
 Atomic number of element m.
 
int elementType (size_t m) const
 Return the element constraint type Possible types include:
 
int changeElementType (int m, int elem_type)
 Change the element type of the mth constraint Reassigns an element type.
 
const vector_fpatomicWeights () const
 Return a read-only reference to the vector of atomic weights.
 
size_t nElements () const
 Number of elements.
 
void checkElementIndex (size_t m) const
 Check that the specified element index is in range Throws an exception if m is greater than nElements()-1.
 
void checkElementArraySize (size_t mm) const
 Check that an array size is at least nElements() Throws an exception if mm is less than nElements().
 
doublereal nAtoms (size_t k, size_t m) const
 Number of atoms of element m in species k.
 
void getAtoms (size_t k, double *atomArray) const
 Get a vector containing the atomic composition of species k.
 
size_t speciesIndex (std::string name) const
 Returns the index of a species named 'name' within the Phase object.
 
std::string speciesName (size_t k) const
 Name of the species with index k.
 
std::string speciesSPName (int k) const
 Returns the expanded species name of a species, including the phase name This is guaranteed to be unique within a Cantera problem.
 
const std::vector< std::string > & speciesNames () const
 Return a const reference to the vector of species names.
 
size_t nSpecies () const
 Returns the number of species in the phase.
 
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 kk) const
 Check that an array size is at least nSpecies() Throws an exception if kk is less than nSpecies().
 
Set thermodynamic state

Set the internal thermodynamic state by setting the internally stored temperature, density and species composition. Note that the composition is always set first.

Temperature and density are held constant if not explicitly set.

void setMoleFractionsByName (compositionMap &xMap)
 Set the species mole fractions by name.
 
void setMoleFractionsByName (const std::string &x)
 Set the mole fractions of a group of species by name.
 
void setMassFractionsByName (compositionMap &yMap)
 Set the species mass fractions by name.
 
void setMassFractionsByName (const std::string &x)
 Set the species mass fractions by name.
 
void setState_TRX (doublereal t, doublereal dens, const doublereal *x)
 Set the internally stored temperature (K), density, and mole fractions.
 
void setState_TRX (doublereal t, doublereal dens, compositionMap &x)
 Set the internally stored temperature (K), density, and mole fractions.
 
void setState_TRY (doublereal t, doublereal dens, const doublereal *y)
 Set the internally stored temperature (K), density, and mass fractions.
 
void setState_TRY (doublereal t, doublereal dens, compositionMap &y)
 Set the internally stored temperature (K), density, and mass fractions.
 
void setState_TNX (doublereal t, doublereal n, const doublereal *x)
 Set the internally stored temperature (K), molar density (kmol/m^3), and mole fractions.
 
void setState_TR (doublereal t, doublereal rho)
 Set the internally stored temperature (K) and density (kg/m^3)
 
void setState_TX (doublereal t, doublereal *x)
 Set the internally stored temperature (K) and mole fractions.
 
void setState_TY (doublereal t, doublereal *y)
 Set the internally stored temperature (K) and mass fractions.
 
void setState_RX (doublereal rho, doublereal *x)
 Set the density (kg/m^3) and mole fractions.
 
void setState_RY (doublereal rho, doublereal *y)
 Set the density (kg/m^3) and mass fractions.
 
Composition
void getMoleFractionsByName (compositionMap &x) const
 Get the mole fractions by name.
 
doublereal moleFraction (size_t k) const
 Return the mole fraction of a single species.
 
doublereal moleFraction (std::string name) const
 Return the mole fraction of a single species.
 
doublereal massFraction (size_t k) const
 Return the mass fraction of a single species.
 
doublereal massFraction (std::string name) const
 Return the mass fraction of a single species.
 
void getMoleFractions (doublereal *const x) const
 Get the species mole fraction vector.
 
virtual void setMoleFractions (const doublereal *const x)
 Set the mole fractions to the specified values There is no restriction on the sum of the mole fraction vector.
 
virtual void setMoleFractions_NoNorm (const doublereal *const x)
 Set the mole fractions to the specified values without normalizing.
 
void getMassFractions (doublereal *const y) const
 Get the species mass fractions.
 
const doublereal * massFractions () const
 Return a const pointer to the mass fraction array.
 
virtual void setMassFractions (const doublereal *const y)
 Set the mass fractions to the specified values and normalize them.
 
virtual void setMassFractions_NoNorm (const doublereal *const y)
 Set the mass fractions to the specified values without normalizing.
 
void getConcentrations (doublereal *const c) const
 Get the species concentrations (kmol/m^3).
 
doublereal concentration (const size_t k) const
 Concentration of species k.
 
virtual void setConcentrations (const doublereal *const conc)
 Set the concentrations to the specified values within the phase.
 
const doublereal * moleFractdivMMW () const
 Returns a const pointer to the start of the moleFraction/MW array.
 
Thermodynamic Properties
doublereal temperature () const
 Temperature (K).
 
virtual doublereal density () const
 Density (kg/m^3).
 
doublereal molarDensity () const
 Molar density (kmol/m^3).
 
doublereal molarVolume () const
 Molar volume (m^3/kmol).
 
virtual void setDensity (const doublereal density)
 Set the internally stored density (kg/m^3) of the phase Note the density of a phase is an independent variable.
 
virtual void setMolarDensity (const doublereal molarDensity)
 Set the internally stored molar density (kmol/m^3) of the phase.
 
virtual void setTemperature (const doublereal temp)
 Set the internally stored temperature of the phase (K).
 
Mean Properties
doublereal mean_X (const doublereal *const Q) const
 Evaluate the mole-fraction-weighted mean of an array Q.
 
doublereal mean_Y (const doublereal *const Q) const
 Evaluate the mass-fraction-weighted mean of an array Q.
 
doublereal meanMolecularWeight () const
 The mean molecular weight. Units: (kg/kmol)
 
doublereal sum_xlogx () const
 Evaluate \( \sum_k X_k \log X_k \).
 
doublereal sum_xlogQ (doublereal *const Q) const
 Evaluate \( \sum_k X_k \log Q_k \).
 
Adding Elements and Species

These methods are used to add new elements or species.

These are not usually called by user programs.

Since species are checked to insure that they are only composed of declared elements, it is necessary to first add all elements before adding any species.

void addElement (const std::string &symbol, doublereal weight=-12345.0)
 Add an element.
 
void addElement (const XML_Node &e)
 Add an element from an XML specification.
 
void addUniqueElement (const std::string &symbol, doublereal weight=-12345.0, int atomicNumber=0, doublereal entropy298=ENTROPY298_UNKNOWN, int elem_type=CT_ELEM_TYPE_ABSPOS)
 Add an element, checking for uniqueness The uniqueness is checked by comparing the string symbol.
 
void addUniqueElement (const XML_Node &e)
 Add an element, checking for uniqueness The uniqueness is checked by comparing the string symbol.
 
void addElementsFromXML (const XML_Node &phase)
 Add all elements referenced in an XML_Node tree.
 
void freezeElements ()
 Prohibit addition of more elements, and prepare to add species.
 
bool elementsFrozen ()
 True if freezeElements has been called.
 
size_t addUniqueElementAfterFreeze (const std::string &symbol, doublereal weight, int atomicNumber, doublereal entropy298=ENTROPY298_UNKNOWN, int elem_type=CT_ELEM_TYPE_ABSPOS)
 Add an element after elements have been frozen, checking for uniqueness The uniqueness is checked by comparing the string symbol.
 
void addSpecies (const std::string &name, const doublereal *comp, doublereal charge=0.0, doublereal size=1.0)
 
void addUniqueSpecies (const std::string &name, const doublereal *comp, doublereal charge=0.0, doublereal size=1.0)
 Add a species to the phase, checking for uniqueness of the name This routine checks for uniqueness of the string name.
 
Reaction Rates Of Progress
virtual void getFwdRatesOfProgress (doublereal *fwdROP)
 Return the forward rates of progress for each reaction.
 
virtual void getRevRatesOfProgress (doublereal *revROP)
 Return the reverse rates of progress for each reaction.
 
virtual void getNetRatesOfProgress (doublereal *netROP)
 Return the net rates of progress for each reaction.
 
virtual void getEquilibriumConstants (doublereal *kc)
 Get the equilibrium constants of all reactions, whether the reaction is reversible or not.
 
void getExchangeCurrentQuantities ()
 
virtual void getDeltaGibbs (doublereal *deltaG)
 Return the vector of values for the reaction gibbs free energy change.
 
virtual void getDeltaElectrochemPotentials (doublereal *deltaM)
 Return the vector of values for the reaction electrochemical free energy change.
 
virtual void getDeltaEnthalpy (doublereal *deltaH)
 Return the vector of values for the reactions change in enthalpy.
 
virtual void getDeltaEntropy (doublereal *deltaS)
 Return the vector of values for the change in entropy due to each reaction.
 
virtual void getDeltaSSGibbs (doublereal *deltaG)
 Return the vector of values for the reaction standard state gibbs free energy change.
 
virtual void getDeltaSSEnthalpy (doublereal *deltaH)
 Return the vector of values for the change in the standard state enthalpies of reaction.
 
virtual void getDeltaSSEntropy (doublereal *deltaS)
 Return the vector of values for the change in the standard state entropies for each reaction.
 
Species Production Rates
virtual void getCreationRates (doublereal *cdot)
 Returns the Species creation rates [kmol/m^2/s].
 
virtual void getDestructionRates (doublereal *ddot)
 Return the Species destruction rates [kmol/m^2/s].
 
virtual void getNetProductionRates (doublereal *net)
 Return the species net production rates [kmol/m^2/s].
 
Reaction Mechanism Informational Query Routines
virtual doublereal reactantStoichCoeff (size_t k, size_t i) const
 Stoichiometric coefficient of species k as a reactant in reaction i.
 
virtual doublereal productStoichCoeff (size_t k, size_t i) const
 Stoichiometric coefficient of species k as a product in reaction i.
 
virtual int reactionType (size_t i) const
 Flag specifying the type of reaction.
 
virtual void getActivityConcentrations (doublereal *const conc)
 Get the vector of activity concentrations used in the kinetics object.
 
doublereal electrochem_beta (size_t irxn) const
 Return the charge transfer rxn Beta parameter for the ith reaction.
 
virtual bool isReversible (size_t i)
 True if reaction i has been declared to be reversible.
 
virtual std::string reactionString (size_t i) const
 Return a string representing the reaction.
 
virtual void getFwdRateConstants (doublereal *kfwd)
 Update the rates of progress of the reactions in the reaction mechanism.
 
virtual void getRevRateConstants (doublereal *krev, bool doIrreversible=false)
 Update the rates of progress of the reactions in the reaction mechanism.
 
virtual void getActivationEnergies (doublereal *E)
 Return the activation energies in Kelvin.
 
Constructors and General Information about Mechanism
virtual void assignShallowPointers (const std::vector< thermo_t * > &tpVector)
 Reassign the shallow pointers within the FKinetics object.
 
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().
 
Information/Lookup Functions about Phases and Species
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 (std::string ph)
 Return the phase index of a phase in the list of phases defined within the object.
 
size_t surfacePhaseIndex ()
 This returns the integer index of the phase which has ThermoPhase type cSurf.
 
size_t reactionPhaseIndex ()
 Phase where the reactions occur.
 
thermo_tthermo (size_t n=0)
 This method returns a reference to the nth ThermoPhase object defined in this kinetics mechanism.
 
const thermo_tthermo (size_t n=0) const
 
thermo_tphase (size_t n=0)
 This method returns a reference to the nth ThermoPhase defined in this kinetics mechanism.
 
const thermo_tphase (size_t n=0) const
 This method returns a reference to the nth ThermoPhase defined in this kinetics mechanism.
 
size_t nTotalSpecies () const
 The total number of species in all phases participating in the kinetics mechanism.
 
size_t start (size_t n)
 Returns the starting index of the species in the nth phase associated with the reaction mechanism.
 
size_t kineticsSpeciesIndex (size_t k, size_t n) const
 The location of species k of phase n in species arrays.
 
size_t kineticsSpeciesIndex (const std::string &nm) const
 This routine will look up a species number based on the input std::string nm.
 
size_t kineticsSpeciesIndex (const std::string &nm, const std::string &ph) const
 This routine will look up a species number based on the input std::string nm.
 
std::string kineticsSpeciesName (size_t k) const
 Return the std::string name of the kth species in the kinetics manager.
 
thermo_tspeciesPhase (std::string nm)
 This function looks up the std::string name of a species and returns a reference to the ThermoPhase object of the phase where the species resides.
 
thermo_tspeciesPhase (size_t k)
 This function takes as an argument the kineticsSpecies index (i.e., 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)
 This function takes as an argument the kineticsSpecies index (i.e., the list index in the list of species in the kinetics manager) and returns the index of the phase owning the species.
 
Reaction Rates Of Progress
virtual void getReactionDelta (const doublereal *property, doublereal *deltaProperty)
 Change in species properties.
 
Reaction Mechanism Informational Query Routines
virtual doublereal reactantOrder (size_t k, size_t i) const
 Reactant order of species k in reaction i.
 
virtual doublereal productOrder (int k, int i) const
 product Order of species k in reaction i.
 
virtual const std::vector
< size_t > & 
reactants (size_t i) const
 Returns a read-only reference to the vector of reactant index numbers for reaction i.
 
virtual const std::vector
< size_t > & 
products (size_t i) const
 Returns a read-only reference to the vector of product index numbers for reaction i.
 
Reaction Mechanism Construction
virtual const std::vector
< grouplist_t > & 
reactantGroups (size_t i)
 
virtual const std::vector
< grouplist_t > & 
productGroups (size_t i)
 
Altering Reaction Rates

These methods alter reaction rates.

They are designed primarily for carrying out sensitivity analysis, but may be used for any purpose requiring dynamic alteration of rate constants. For each reaction, a real-valued multiplier may be defined that multiplies the reaction rate coefficient. The multiplier may be set to zero to completely remove a reaction from the mechanism.

doublereal multiplier (size_t i) const
 The current value of the multiplier for reaction i.
 
void setMultiplier (size_t i, doublereal f)
 Set the multiplier for reaction i to f.
 

Protected Member Functions

void init (const vector_fp &mw)
 
void setMolecularWeight (const int k, const double mw)
 Set the molecular weight of a single species to a given value.
 

Protected Attributes

bool m_ok
 Flag indicating that the object has been instantiated.
 
Cantera::XML_Nodem_r
 XML_Node pointer to the XML File object that contains the Surface and the Interfacial Reaction object description.
 
doublereal m_n0
 Surface site density (kmol m-2)
 
doublereal m_logn0
 log of the surface site density
 
doublereal m_tmin
 Minimum temperature for valid species standard state thermo props.
 
doublereal m_tmax
 Maximum temperature for valid species standard state thermo props.
 
doublereal m_press
 Current value of the pressure (Pa)
 
doublereal m_tlast
 Current value of the temperature (Kelvin)
 
vector_fp m_h0
 Temporary storage for the reference state enthalpies.
 
vector_fp m_s0
 Temporary storage for the reference state entropies.
 
vector_fp m_cp0
 Temporary storage for the reference state heat capacities.
 
vector_fp m_mu0
 Temporary storage for the reference state gibbs energies.
 
vector_fp m_work
 Temporary work array.
 
vector_fp m_pe
 Potential energy of each species in the surface phase.
 
vector_fp m_logsize
 vector storing the log of the size of each species.
 
SpeciesThermom_spthermo
 Pointer to the calculation manager for species reference-state thermodynamic properties.
 
std::vector< const XML_Node * > m_speciesData
 Vector of pointers to the species databases.
 
doublereal m_phi
 Stored value of the electric potential for this phase.
 
vector_fp m_lambdaRRT
 Vector of element potentials.
 
bool m_hasElementPotentials
 Boolean indicating whether there is a valid set of saved element potentials for this phase.
 
bool m_chargeNeutralityNecessary
 Boolean indicating whether a charge neutrality condition is a necessity.
 
int m_ssConvention
 Contains the standard state convention.
 
std::vector< doublereal > xMol_Ref
 Reference Mole Fraction Composition.
 
size_t m_kk
 Number of species in the phase.
 
size_t m_ndim
 Dimensionality of the phase.
 
vector_fp m_speciesComp
 Atomic composition of the species.
 
vector_fp m_speciesSize
 Vector of species sizes.
 
vector_fp m_speciesCharge
 Vector of species charges. length m_kk.
 
size_t m_ii
 Number of reactions in the mechanism.
 
size_t m_kk
 The number of species in all of the phases that participate in this kinetics mechanism.
 
vector_fp m_perturb
 Vector of perturbation factors for each reaction's rate of progress vector.
 
std::vector< std::vector
< size_t > > 
m_reactants
 This is a vector of vectors containing the reactants for each reaction.
 
std::vector< std::vector
< size_t > > 
m_products
 This is a vector of vectors containing the products for each reaction.
 
std::vector< thermo_t * > m_thermo
 m_thermo is a vector of pointers to ThermoPhase objects that are involved with this kinetics operator
 
std::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.
 
std::map< std::string, size_t > m_phaseindex
 Mapping of the phase id, i.e., the id attribute in the xml phase element to the position of the phase within the kinetics object.
 
size_t m_surfphase
 Index in the list of phases of the one surface phase.
 
size_t m_rxnphase
 Phase Index where reactions are assumed to be taking place.
 
size_t m_mindim
 number of spatial dimensions of lowest-dimensional phase.
 

Reaction Mechanism Construction

vector_fp m_grt
 Temporary work vector of length m_kk.
 
std::vector< size_t > m_revindex
 List of reactions numbers which are reversible reactions.
 
Rate1< SurfaceArrheniusm_rates
 Templated class containing the vector of reactions for this interface.
 
bool m_redo_rates
 
std::map< size_t, std::pair
< int, size_t > > 
m_index
 Vector of information about reactions in the mechanism.
 
std::vector< size_t > m_irrev
 Vector of irreversible reaction numbers.
 
ReactionStoichMgr m_rxnstoich
 Stoichiometric manager for the reaction mechanism.
 
size_t m_nirrev
 Number of irreversible reactions in the mechanism.
 
size_t m_nrev
 Number of reversible reactions in the mechanism.
 
std::vector< std::map< size_t,
doublereal > > 
m_rrxn
 m_rrxn is a vector of maps, containing the reactant stoichiometric coefficient information
 
std::vector< std::map< size_t,
doublereal > > 
m_prxn
 m_prxn is a vector of maps, containing the reactant stoichiometric coefficient information
 
std::vector< std::string > m_rxneqn
 String expression for each rxn.
 
InterfaceKineticsDatam_kdata
 Temporary data storage used in calculating the rates of of reactions.
 
vector_fp m_conc
 an array of generalized concentrations for each species
 
vector_fp m_mu0
 Vector of standard state chemical potentials.
 
vector_fp m_phi
 Vector of phase electric potentials.
 
vector_fp m_pot
 Vector of potential energies due to Voltages.
 
vector_fp m_rwork
 Vector temporary.
 
vector_fp m_E
 Vector of raw activation energies for the reactions.
 
SurfPhasem_surf
 Pointer to the single surface phase.
 
ImplicitSurfChemm_integrator
 Pointer to the Implicit surface chemistry object.
 
vector_fp m_beta
 
std::vector< size_t > m_ctrxn
 Vector of reaction indexes specifying the id of the current transfer reactions in the mechanism.
 
vector_int m_ctrxn_ecdf
 Vector of booleans indicating whether the charge transfer reaction may be described by an exchange current density expression.
 
vector_fp m_StandardConc
 
vector_fp m_deltaG0
 
vector_fp m_ProdStanConcReac
 
bool m_finalized
 boolean indicating whether mechanism has been finalized
 
bool m_has_coverage_dependence
 Boolean flag indicating whether any reaction in the mechanism has a coverage dependent forward reaction rate.
 
bool m_has_electrochem_rxns
 Boolean flag indicating whether any reaction in the mechanism has a beta electrochemical parameter.
 
bool m_has_exchange_current_density_formulation
 Boolean flag indicating whether any reaction in the mechanism is described by an exchange current density expression.
 
int m_phaseExistsCheck
 Int flag to indicate that some phases in the kinetics mechanism are non-existent.
 
std::vector< bool > m_phaseExists
 Vector of booleans indicating whether phases exist or not.
 
std::vector< int > m_phaseIsStable
 Vector of int indicating whether phases are stable or not.
 
std::vector< bool * > m_rxnPhaseIsReactant
 Vector of vector of booleans indicating whether a phase participates in a reaction as a reactant.
 
std::vector< bool * > m_rxnPhaseIsProduct
 Vector of vector of booleans indicating whether a phase participates in a reaction as a product.
 
std::vector< int > m_phaseIsIntermediate
 Vector of ints indicating whether zeroed phase is an intermediate for the formation of another phase.
 
int m_numIntermediatePhases
 
std::vector< doublereal > m_rxnRateFactorPhaseIntermediates
 Reaction rate reduction factor for intermediates.
 
std::vector< doublereal > m_speciesTmpP
 Work vector having length number of species.
 
std::vector< doublereal > m_speciesTmpD
 
int m_ioFlag
 
virtual void addPhase (thermo_t &thermo)
 Add a phase to the kinetics manager object.
 
virtual void init ()
 Prepare the class for the addition of reactions.
 
virtual void addReaction (ReactionData &r)
 Add a single reaction to the mechanism.
 
virtual void finalize ()
 Finish adding reactions and prepare for use.
 
void updateROP ()
 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 (doublereal tstep)
 Advance the surface coverages in time.
 
void solvePseudoSteadyStateProblem (int ifuncOverride=-1, doublereal timeScaleOverride=1.0)
 Solve for the pseudo steady-state of the surface problem.
 
void setIOFlag (int ioFlag)
 
void checkPartialEquil ()
 
size_t reactionNumber () const
 
void addElementaryReaction (ReactionData &r)
 
void addGlobalReaction (const ReactionData &r)
 
void installReagents (const ReactionData &r)
 
void updateKc ()
 Update the equilibrium constants in molar units for all reversible reactions.
 
void registerReaction (size_t rxnNumber, int type, size_t loc)
 Write values into m_index.
 
void applyButlerVolmerCorrection (doublereal *const kf)
 Apply corrections for interfacial charge transfer reactions.
 
void applyExchangeCurrentDensityFormulation (doublereal *const kfwd)
 When an electrode reaction rate is optionally specified in terms of its exchange current density, extra vectors need to be precalculated.
 
void setPhaseExistence (const size_t iphase, const bool exists)
 Set the existence of a phase in the reaction object.
 
void setPhaseStability (const int iphase, const int isStable)
 Set the stability of a phase in the reaction object.
 
int phaseExistence (const int iphase) const
 Gets the phase existence int for the ith phase.
 
int phaseStability (const int iphase) const
 Gets the phase stability int for the ith phase.
 

Detailed Description

An interface between multiple bulk phases.

This class is defined mostly for convenience. It inherits both from Cantera::SurfPhase and Cantera::InterfaceKinetics. It therefore represents a surface phase, and also acts as the kinetics manager to manage reactions occurring on the surface, possibly involving species from other phases.

Definition at line 23 of file Interface.h.

Constructor & Destructor Documentation

Interface ( std::string  infile,
std::string  id,
std::vector< Cantera::ThermoPhase * >  otherPhases 
)
inline

Constructor.

Construct an Interface instance from a specification in an input file.

Parameters
infileCantera input file in CTI or CTML format.
idIdentification string to distinguish between multiple definitions within one input file.
otherPhasesNeighboring phases that may participate in the reactions on this interface. Don't include the surface phase
Deprecated:
While it's convenient to have the surface phase and the interfacial reaction together, this class doesn't satisfy the primary issue, which is one of instantiation of all the ThermoPhase classes that accompany a surface reaction. This is accomplished by the PhaseList class along with the ReactingSurface class. These classes will be migrated into Cantera soon.

Definition at line 47 of file Interface.h.

References Cantera::get_XML_File(), Cantera::get_XML_Node(), Cantera::importKinetics(), Cantera::importPhase(), Interface::m_ok, and Interface::m_r.

Interface ( const Interface ii)
inline

Copy Constructor.

Parameters
iiInterface object to be copied.

Definition at line 70 of file Interface.h.

virtual ~Interface ( )
inlinevirtual

Destructor. Does nothing.

Definition at line 93 of file Interface.h.

Member Function Documentation

Interface& operator= ( const Interface right)
inline

Assignment operator.

Parameters
rightInterface object to be copied.

Definition at line 81 of file Interface.h.

References Interface::m_ok, Interface::m_r, InterfaceKinetics::operator=(), and SurfPhase::operator=().

bool operator! ( )
inline

Not operator.

Definition at line 97 of file Interface.h.

References Interface::m_ok.

bool ready ( ) const
inlinevirtual

return whether the object has been instantiated

Returns
Returns a bool.

Reimplemented from InterfaceKinetics.

Definition at line 105 of file Interface.h.

References Interface::m_ok.

ThermoPhase * duplMyselfAsThermoPhase ( ) const
virtualinherited

Duplicator from the ThermoPhase parent class.

Reimplemented from ThermoPhase.

Definition at line 147 of file SurfPhase.cpp.

References SurfPhase::SurfPhase().

virtual int eosType ( ) const
inlinevirtualinherited

Equation of state type flag.

Redefine this to return cSurf, listed in mix_defs.h.

Reimplemented from ThermoPhase.

Reimplemented in EdgePhase.

Definition at line 212 of file SurfPhase.h.

References Cantera::cSurf.

doublereal enthalpy_mole ( ) const
virtualinherited

Return the Molar Enthalpy. Units: J/kmol.

For an ideal solution,

\[ \hat h(T,P) = \sum_k X_k \hat h^0_k(T), \]

and is a function only of temperature. The standard-state pure-species Enthalpies \( \hat h^0_k(T) \) are computed by the species thermodynamic property manager.

See Also
SpeciesThermo

Reimplemented from ThermoPhase.

Definition at line 154 of file SurfPhase.cpp.

References SurfPhase::_updateThermo(), DATA_PTR, SurfPhase::m_h0, SurfPhase::m_n0, and Phase::mean_X().

Referenced by SurfPhase::intEnergy_mole().

doublereal intEnergy_mole ( ) const
virtualinherited

Return the Molar Internal Energy. Units: J/kmol.

For a surface phase, the pressure is not a relevant thermodynamic variable, and so the Enthalpy is equal to the Internal Energy.

Reimplemented from ThermoPhase.

Definition at line 173 of file SurfPhase.cpp.

References SurfPhase::enthalpy_mole().

void getChemPotentials ( doublereal *  mu) const
virtualinherited

Get the species chemical potentials. Units: J/kmol.

This function returns a vector of chemical potentials of the species in solution at the current temperature, pressure and mole fraction of the solution.

Parameters
muOutput vector of species chemical potentials. Length: m_kk. Units: J/kmol

Reimplemented from ThermoPhase.

Definition at line 232 of file SurfPhase.cpp.

References SurfPhase::_updateThermo(), DATA_PTR, Cantera::GasConstant, SurfPhase::getActivityConcentrations(), SurfPhase::logStandardConc(), Phase::m_kk, SurfPhase::m_mu0, SurfPhase::m_work, and Phase::temperature().

void getPartialMolarEnthalpies ( doublereal *  hbar) const
virtualinherited

Returns an array of partial molar enthalpies for the species in the mixture.

Units (J/kmol)

Parameters
hbarOutput vector of species partial molar enthalpies. Length: m_kk. units are J/kmol.

Reimplemented from ThermoPhase.

Definition at line 182 of file SurfPhase.cpp.

References Cantera::GasConstant, SurfPhase::getEnthalpy_RT(), Phase::m_kk, and Phase::temperature().

void getPartialMolarEntropies ( doublereal *  sbar) const
virtualinherited

Returns an array of partial molar entropies of the species in the solution.

Units: J/kmol/K.

Parameters
sbarOutput vector of species partial molar entropies. Length = m_kk. units are J/kmol/K.

Reimplemented from ThermoPhase.

Definition at line 197 of file SurfPhase.cpp.

References Cantera::GasConstant, SurfPhase::getEntropy_R(), and Phase::m_kk.

void getPartialMolarCp ( doublereal *  cpbar) const
virtualinherited

Return an array of partial molar heat capacities for the species in the mixture.

Units: J/kmol/K

Parameters
cpbarOutput vector of species partial molar heat capacities at constant pressure. Length = m_kk. units are J/kmol/K.

Reimplemented from ThermoPhase.

Definition at line 211 of file SurfPhase.cpp.

References Cantera::GasConstant, SurfPhase::getCp_R(), and Phase::m_kk.

void getPartialMolarVolumes ( doublereal *  vbar) const
virtualinherited

Return an array of partial molar volumes for the species in the mixture.

Units: m^3/kmol.

Parameters
vbarOutput vector of species partial molar volumes. Length = m_kk. units are m^3/kmol.

Reimplemented from ThermoPhase.

Definition at line 221 of file SurfPhase.cpp.

References SurfPhase::getStandardVolumes().

void getStandardChemPotentials ( doublereal *  mu0) const
virtualinherited

Get the array of chemical potentials at unit activity for the standard state species at the current T and P of the solution.

These are the standard state chemical potentials \( \mu^0_k(T,P) \). The values are evaluated at the current temperature and pressure of the solution

Parameters
mu0Output vector of chemical potentials. Length: m_kk.

Reimplemented from ThermoPhase.

Definition at line 226 of file SurfPhase.cpp.

References SurfPhase::_updateThermo(), and SurfPhase::m_mu0.

void getActivityConcentrations ( doublereal *  c) const
virtualinherited

Return a vector of activity concentrations for each species.

For this phase the activity concentrations, \( C^a_k \), are defined to be equal to the actual concentrations, \( C^s_k \). Activity concentrations are

\[ C^a_k = C^s_k = \frac{\theta_k n_0}{s_k} \]

where \( \theta_k \) is the surface site fraction for species k, \( n_0 \) is the surface site density for the phase, and \( s_k \) is the surface size of species k.

\( C^a_k\) that are defined such that \( a_k = C^a_k / C^0_k, \) where \( C^0_k \) is a standard concentration defined below and \( a_k \) are activities used in the thermodynamic functions. These activity concentrations are used by kinetics manager classes to compute the forward and reverse rates of elementary reactions. Note that they may or may not have units of concentration — they might be partial pressures, mole fractions, or surface coverages,

Parameters
cvector of activity concentration (kmol m-2).

Reimplemented from ThermoPhase.

Definition at line 243 of file SurfPhase.cpp.

References Phase::getConcentrations().

Referenced by SurfPhase::getChemPotentials().

doublereal standardConcentration ( size_t  k = 0) const
virtualinherited

Return the standard concentration for the kth species.

The standard concentration \( C^0_k \) used to normalize the activity (i.e., generalized) concentration. For this phase, the standard concentration is species- specific

\[ C^0_k = \frac{n_0}{s_k} \]

This definition implies that the activity is equal to \( \theta_k \).

Parameters
kOptional parameter indicating the species. The default is to assume this refers to species 0.
Returns
Returns the standard Concentration in units of m3 kmol-1.

Reimplemented from ThermoPhase.

Definition at line 248 of file SurfPhase.cpp.

References SurfPhase::m_n0, and Phase::size().

Referenced by SurfPhase::getStandardVolumes().

doublereal logStandardConc ( size_t  k = 0) const
virtualinherited

Return the log of the standard concentration for the kth species.

Parameters
kspecies index (default 0)

Reimplemented from ThermoPhase.

Definition at line 253 of file SurfPhase.cpp.

References SurfPhase::m_logn0, and SurfPhase::m_logsize.

Referenced by SurfPhase::getChemPotentials().

void setParameters ( int  n,
doublereal *const  c 
)
virtualinherited

Set the equation of state parameters from the argument list.

The only parameter that can be set is the site density.

Set equation of state parameters.

Parameters
nnumber of parameters. Must be one
carray of n coefficients c[0] = The site density (kmol m-2)

Reimplemented from ThermoPhase.

Definition at line 259 of file SurfPhase.cpp.

References SurfPhase::m_logn0, and SurfPhase::m_n0.

Referenced by SurfPhase::setSiteDensity().

void setParametersFromXML ( const XML_Node thermoData)
virtualinherited

Set the Equation-of-State parameters by reading an XML Node Input.

The Equation-of-State data consists of one item, the site density.

Parameters
thermoDataReference to an XML_Node named thermo containing the equation-of-state data. The XML_Node is within the phase XML_Node describing the SurfPhase object.

An example of the contents of the thermoData XML_Node is provided below. The units attribute is used to supply the units of the site density in any convenient form. Internally it is changed into MKS form.

*    <thermo model="Surface">
*       <site_density units="mol/cm2"> 3e-09 </site_density>
*    </thermo>
* 

Reimplemented from ThermoPhase.

Reimplemented in EdgePhase.

Definition at line 474 of file SurfPhase.cpp.

References XML_Node::_require(), ctml::getFloat(), SurfPhase::m_logn0, and SurfPhase::m_n0.

void initThermo ( )
virtualinherited

Initialize the SurfPhase object after all species have been set up.

Initialize.

This method is provided to allow subclasses to perform any initialization required after all species have been added. For example, it might be used to resize internal work arrays that must have an entry for each species. The base class implementation does nothing, and subclasses that do not require initialization do not need to overload this method. When importing a CTML phase description, this method is called from ThermoPhase::initThermoXML(), which is called from importPhase(), just prior to returning from function importPhase().

See Also
importCTML.cpp

Reimplemented from ThermoPhase.

Definition at line 330 of file SurfPhase.cpp.

References DATA_PTR, SurfPhase::m_cp0, SurfPhase::m_h0, Phase::m_kk, SurfPhase::m_logsize, SurfPhase::m_mu0, SurfPhase::m_pe, SurfPhase::m_s0, SurfPhase::m_work, SurfPhase::setCoverages(), and Phase::size().

void setStateFromXML ( const XML_Node state)
virtualinherited

Set the initial state of the Surface Phase from an XML_Node.

State variables that can be set by this routine are the temperature and the surface site coverages.

Parameters
stateXML_Node containing the state information

An example of the XML code block is given below.

*   <state>
*      <temperature units="K">1200.0</temperature>
*      <coverages>c6H*:0.1, c6HH:0.9</coverages>
*   </state>
* 

Reimplemented from ThermoPhase.

Definition at line 486 of file SurfPhase.cpp.

References ctml::getChildValue(), ctml::getOptionalFloat(), XML_Node::hasChild(), SurfPhase::setCoveragesByName(), and Phase::setTemperature().

doublereal siteDensity ( )
inlineinherited

Returns the site density.

Site density kmol m-2

Definition at line 429 of file SurfPhase.h.

References SurfPhase::m_n0.

Referenced by ReactingSurf1D::eval().

void setPotentialEnergy ( int  k,
doublereal  pe 
)
inherited

Sets the potential energy of species k.

Parameters
kSpecies index
peValue of the potential energy (J kmol-1)

Definition at line 351 of file SurfPhase.cpp.

References SurfPhase::_updateThermo(), and SurfPhase::m_pe.

doublereal potentialEnergy ( int  k)
inlineinherited

Return the potential energy of species k.

Returns the potential energy of species, k, J kmol-1

Parameters
kSpecies index

Definition at line 448 of file SurfPhase.h.

References SurfPhase::m_pe.

void setSiteDensity ( doublereal  n0)
inherited

Set the site density of the surface phase (kmol m-2)

Parameters
n0Site density of the surface phase (kmol m-2)

Definition at line 357 of file SurfPhase.cpp.

References SurfPhase::setParameters().

void getGibbs_RT ( doublereal *  grt) const
virtualinherited

Get the nondimensional Gibbs functions for the species in their standard states at the current T and P of the solution.

Parameters
grtOutput vector of nondimensional standard state gibbs free energies Length: m_kk.

Reimplemented from ThermoPhase.

Definition at line 273 of file SurfPhase.cpp.

References SurfPhase::_updateThermo(), Cantera::GasConstant, SurfPhase::m_mu0, Cantera::scale(), and Phase::temperature().

Referenced by SurfPhase::getGibbs_RT_ref().

void getEnthalpy_RT ( doublereal *  hrt) const
virtualinherited

Get the nondimensional Enthalpy functions for the species standard states at their standard states at the current T and P of the solution.

Parameters
hrtOutput vector of nondimensional standard state enthalpies. Length: m_kk.

Reimplemented from ThermoPhase.

Definition at line 281 of file SurfPhase.cpp.

References SurfPhase::_updateThermo(), Cantera::GasConstant, SurfPhase::m_h0, Cantera::scale(), and Phase::temperature().

Referenced by SurfPhase::getEnthalpy_RT_ref(), and SurfPhase::getPartialMolarEnthalpies().

void getEntropy_R ( doublereal *  sr) const
virtualinherited

Get the array of nondimensional Entropy functions for the species standard states at the current T and P of the solution.

Parameters
srOutput vector of nondimensional standard state entropies. Length: m_kk.

Reimplemented from ThermoPhase.

Definition at line 288 of file SurfPhase.cpp.

References SurfPhase::_updateThermo(), Cantera::GasConstant, SurfPhase::m_s0, and Cantera::scale().

Referenced by SurfPhase::getEntropy_R_ref(), and SurfPhase::getPartialMolarEntropies().

void getCp_R ( doublereal *  cpr) const
virtualinherited

Get the nondimensional Heat Capacities at constant pressure for the species standard states at the current T and P of the solution.

Parameters
cprOutput vector of nondimensional standard state heat capacities Length: m_kk.

Reimplemented from ThermoPhase.

Definition at line 295 of file SurfPhase.cpp.

References SurfPhase::_updateThermo(), Cantera::GasConstant, SurfPhase::m_cp0, and Cantera::scale().

Referenced by SurfPhase::getCp_R_ref(), and SurfPhase::getPartialMolarCp().

void getStandardVolumes ( doublereal *  vol) const
virtualinherited

Get the molar volumes of the species standard states at the current T and P of the solution.

units = m^3 / kmol

Parameters
volOutput vector containing the standard state volumes. Length: m_kk.

Reimplemented from ThermoPhase.

Definition at line 302 of file SurfPhase.cpp.

References SurfPhase::_updateThermo(), Phase::m_kk, and SurfPhase::standardConcentration().

Referenced by SurfPhase::getPartialMolarVolumes().

virtual doublereal pressure ( ) const
inlinevirtualinherited

Return the thermodynamic pressure (Pa).

This method must be overloaded in derived classes. Since the mass density, temperature, and mass fractions are stored, this method should use these values to implement the mechanical equation of state \( P(T, \rho, Y_1, \dots, Y_K) \).

Reimplemented from ThermoPhase.

Definition at line 509 of file SurfPhase.h.

References SurfPhase::m_press.

virtual void setPressure ( doublereal  p)
inlinevirtualinherited

Set the internally stored pressure (Pa) at constant temperature and composition.

This method must be reimplemented in derived classes, where it may involve the solution of a nonlinear equation. Within Cantera, the independent variable is the density. Therefore, this function solves for the density that will yield the desired input pressure. The temperature and composition iare held constant during this process.

This base class function will print an error, if not overwritten.

Parameters
pinput Pressure (Pa)

Reimplemented from ThermoPhase.

Definition at line 526 of file SurfPhase.h.

References SurfPhase::m_press.

void getGibbs_RT_ref ( doublereal *  grt) const
virtualinherited

Returns the vector of nondimensional Gibbs Free Energies of the reference state at the current temperature of the solution and the reference pressure for the species.

Parameters
grtOutput vector containing the nondimensional reference state Gibbs Free energies. Length: m_kk.

Reimplemented from ThermoPhase.

Definition at line 310 of file SurfPhase.cpp.

References SurfPhase::getGibbs_RT().

void getEnthalpy_RT_ref ( doublereal *  hrt) const
virtualinherited

Returns the vector of nondimensional enthalpies of the reference state at the current temperature of the solution and the reference pressure for the species.

Parameters
hrtOutput vector of nondimensional standard state enthalpies. Length: m_kk.

Reimplemented from ThermoPhase.

Definition at line 315 of file SurfPhase.cpp.

References SurfPhase::getEnthalpy_RT().

void getEntropy_R_ref ( doublereal *  er) const
virtualinherited

Returns the vector of nondimensional entropies of the reference state at the current temperature of the solution and the reference pressure for each species.

Parameters
erOutput vector containing the nondimensional reference state entropies. Length: m_kk.

Reimplemented from ThermoPhase.

Definition at line 320 of file SurfPhase.cpp.

References SurfPhase::getEntropy_R().

void getCp_R_ref ( doublereal *  cprt) const
virtualinherited

Returns the vector of nondimensional constant pressure heat capacities of the reference state at the current temperature of the solution and reference pressure for each species.

Parameters
cprtOutput vector of nondimensional reference state heat capacities at constant pressure for the species. Length: m_kk

Reimplemented from ThermoPhase.

Definition at line 325 of file SurfPhase.cpp.

References SurfPhase::getCp_R().

void setCoverages ( const doublereal *  theta)
inherited

Set the surface site fractions to a specified state.

Set the coverage fractions to a specified state.

This routine converts to concentrations in kmol/m2, using m_n0, the surface site density, and size(k), which is defined to be the number of surface sites occupied by the kth molecule. It then calls Phase::setConcentrations to set the internal concentration in the object.

Parameters
thetaThis is the surface site fraction for the kth species in the surface phase. This is a dimensionless quantity.

This routine normalizes the theta's to 1, before application

This routine converts to concentrations in kmol/m2, using m_n0, the surface site density, and size(k), which is defined to be the number of surface sites occupied by the kth molecule. It then calls Phase::setConcentrations to set the internal concentration in the object.

Definition at line 382 of file SurfPhase.cpp.

References DATA_PTR, Phase::m_kk, SurfPhase::m_n0, SurfPhase::m_work, Phase::setConcentrations(), and Phase::size().

Referenced by ReactingSurf1D::eval(), SurfPhase::initThermo(), and SurfPhase::setCoveragesByName().

void setCoveragesNoNorm ( const doublereal *  theta)
inherited

Set the surface site fractions to a specified state.

This routine converts to concentrations in kmol/m2, using m_n0, the surface site density, and size(k), which is defined to be the number of surface sites occupied by the kth molecule. It then calls Phase::setConcentrations to set the internal concentration in the object.

Parameters
thetaThis is the surface site fraction for the kth species in the surface phase. This is a dimensionless quantity.

Definition at line 406 of file SurfPhase.cpp.

References DATA_PTR, Phase::m_kk, SurfPhase::m_n0, SurfPhase::m_work, Phase::setConcentrations(), and Phase::size().

void setCoveragesByName ( std::string  cov)
inherited

Set the coverages from a string of colon-separated name:value pairs.

Parameters
covString containing colon-separated name:value pairs

Definition at line 428 of file SurfPhase.cpp.

References DATA_PTR, Phase::nSpecies(), Cantera::parseCompString(), SurfPhase::setCoverages(), and Phase::speciesName().

Referenced by SurfPhase::setStateFromXML().

void getCoverages ( doublereal *  theta) const
inherited

Return a vector of surface coverages.

Get the coverages.

Parameters
thetaArray theta must be at least as long as the number of species.

Definition at line 419 of file SurfPhase.cpp.

References Phase::getConcentrations(), Phase::m_kk, SurfPhase::m_n0, and Phase::size().

Referenced by ReactingSurf1D::_getInitialSoln(), and InterfaceKinetics::_update_rates_T().

virtual doublereal refPressure ( ) const
inlinevirtualinherited
virtual doublereal minTemp ( size_t  k = npos) const
inlinevirtualinherited

Minimum temperature for which the thermodynamic data for the species or phase are valid.

If no argument is supplied, the value returned will be the lowest temperature at which the data for all species are valid. Otherwise, the value will be only for species k. This function is a wrapper that calls the species thermo minTemp function.

Parameters
kindex of the species. Default is -1, which will return the max of the min value over all species.

Reimplemented in LatticeSolidPhase.

Definition at line 181 of file ThermoPhase.h.

References ThermoPhase::m_spthermo, and SpeciesThermo::minTemp().

Referenced by MultiPhase::addPhase(), ChemEquil::equilibrate(), LiquidTransport::initLiquid(), SimpleTransport::initLiquid(), AqueousTransport::initLiquid(), ThermoPhase::setState_HPorUV(), ThermoPhase::setState_SPorSV(), TransportFactory::setupLiquidTransport(), and TransportFactory::setupMM().

doublereal Hf298SS ( const int  k) const
inlineinherited

Report the 298 K Heat of Formation of the standard state of one species (J kmol-1)

The 298K Heat of Formation is defined as the enthalpy change to create the standard state of the species from its constituent elements in their standard states at 298 K and 1 bar.

Parameters
kspecies index
Returns
Returns the current value of the Heat of Formation at 298K and 1 bar

Definition at line 221 of file ThermoPhase.h.

References ThermoPhase::err().

virtual void modifyOneHf298SS ( const int  k,
const doublereal  Hf298New 
)
inlinevirtualinherited

Modify the value of the 298 K Heat of Formation of one species in the phase (J kmol-1)

The 298K heat of formation is defined as the enthalpy change to create the standard state of the species from its constituent elements in their standard states at 298 K and 1 bar.

Parameters
kSpecies k
Hf298NewSpecify the new value of the Heat of Formation at 298K and 1 bar

Definition at line 233 of file ThermoPhase.h.

References ThermoPhase::err().

virtual doublereal maxTemp ( size_t  k = npos) const
inlinevirtualinherited

Maximum temperature for which the thermodynamic data for the species are valid.

If no argument is supplied, the value returned will be the highest temperature at which the data for all species are valid. Otherwise, the value will be only for species k. This function is a wrapper that calls the species thermo maxTemp function.

Parameters
kindex of the species. Default is -1, which will return the min of the max value over all species.

Reimplemented in LatticeSolidPhase.

Definition at line 250 of file ThermoPhase.h.

References ThermoPhase::m_spthermo, and SpeciesThermo::maxTemp().

Referenced by MultiPhase::addPhase(), ChemEquil::equilibrate(), LiquidTransport::initLiquid(), SimpleTransport::initLiquid(), AqueousTransport::initLiquid(), ThermoPhase::setState_HPorUV(), ThermoPhase::setState_SPorSV(), TransportFactory::setupLiquidTransport(), and TransportFactory::setupMM().

bool chargeNeutralityNecessary ( ) const
inlineinherited

Returns the chargeNeutralityNecessity boolean.

Some phases must have zero net charge in order for their thermodynamics functions to be valid. If this is so, then the value returned from this function is true. If this is not the case, then this is false. Now, ideal gases have this parameter set to false, while solution with molality-based activity coefficients have this parameter set to true.

Definition at line 261 of file ThermoPhase.h.

References ThermoPhase::m_chargeNeutralityNecessary.

virtual doublereal entropy_mole ( ) const
inlinevirtualinherited
virtual doublereal gibbs_mole ( ) const
inlinevirtualinherited
virtual doublereal cp_mole ( ) const
inlinevirtualinherited
virtual doublereal cv_mole ( ) const
inlinevirtualinherited
virtual doublereal isothermalCompressibility ( ) const
inlinevirtualinherited

Returns the isothermal compressibility. Units: 1/Pa.

The isothermal compressibility is defined as

\[ \kappa_T = -\frac{1}{v}\left(\frac{\partial v}{\partial P}\right)_T \]

or

\[ \kappa_T = \frac{1}{\rho}\left(\frac{\partial \rho}{\partial P}\right)_T \]

Reimplemented in HMWSoln, DebyeHuckel, IdealGasPhase, IdealMolalSoln, MetalSHEelectrons, PureFluidPhase, FixedChemPotSSTP, MineralEQ3, StoichSubstanceSSTP, WaterSSTP, RedlichKwongMFTP, and IdealSolnGasVPSS.

Definition at line 348 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by SingleSpeciesTP::cv_mole().

virtual doublereal thermalExpansionCoeff ( ) const
inlinevirtualinherited

Return the volumetric thermal expansion coefficient. Units: 1/K.

The thermal expansion coefficient is defined as

\[ \beta = \frac{1}{v}\left(\frac{\partial v}{\partial T}\right)_P \]

Reimplemented in HMWSoln, DebyeHuckel, IdealGasPhase, IdealMolalSoln, MetalSHEelectrons, PureFluidPhase, FixedChemPotSSTP, MineralEQ3, StoichSubstanceSSTP, and WaterSSTP.

Definition at line 360 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by SingleSpeciesTP::cv_mole().

virtual void updateDensity ( )
inlinevirtualinherited
Deprecated:

Definition at line 366 of file ThermoPhase.h.

References Cantera::deprecatedMethod().

void setElectricPotential ( doublereal  v)
inlineinherited

Set the electric potential of this phase (V).

This is used by classes InterfaceKinetics and EdgeKinetics to compute the rates of charge-transfer reactions, and in computing the electrochemical potentials of the species.

Each phase may have its own electric potential.

Parameters
vInput value of the electric potential in Volts

Definition at line 390 of file ThermoPhase.h.

References ThermoPhase::m_phi.

Referenced by InterfaceKinetics::setElectricPotential(), vcs_VolPhase::setElectricPotential(), and vcs_VolPhase::setState_TP().

doublereal electricPotential ( ) const
inlineinherited
int activityConvention ( ) const
virtualinherited

This method returns the convention used in specification of the activities, of which there are currently two, molar- and molality-based conventions.

Currently, there are two activity conventions:

  • Molar-based activities Unit activity of species at either a hypothetical pure solution of the species or at a hypothetical pure ideal solution at infinite dilution cAC_CONVENTION_MOLAR 0
    • default
  • Molality-based activities (unit activity of solutes at a hypothetical 1 molal solution referenced to infinite dilution at all pressures and temperatures). cAC_CONVENTION_MOLALITY 1

Reimplemented in MolalityVPSSTP.

Definition at line 143 of file ThermoPhase.cpp.

References Cantera::cAC_CONVENTION_MOLAR.

Referenced by vcs_MultiPhaseEquil::reportCSV(), and LiquidTransport::stefan_maxwell_solve().

int standardStateConvention ( ) const
virtualinherited

This method returns the convention used in specification of the standard state, of which there are currently two, temperature based, and variable pressure based.

Currently, there are two standard state conventions:

  • Temperature-based activities cSS_CONVENTION_TEMPERATURE 0
    • default
  • Variable Pressure and Temperature -based activities cSS_CONVENTION_VPSS 1
  • Thermodynamics is set via slave ThermoPhase objects with nothing being carried out at this ThermoPhase object level cSS_CONVENTION_SLAVE 2

Reimplemented in PureFluidPhase, LatticeSolidPhase, MixtureFugacityTP, and VPStandardStateTP.

Definition at line 148 of file ThermoPhase.cpp.

References ThermoPhase::m_ssConvention.

Referenced by Cantera::importPhase().

void getUnitsStandardConc ( double *  uA,
int  k = 0,
int  sizeUA = 6 
) const
virtualinherited

Returns the units of the standard and generalized concentrations.

Note they have the same units, as their ratio is defined to be equal to the activity of the kth species in the solution, which is unitless.

This routine is used in print out applications where the units are needed. Usually, MKS units are assumed throughout the program and in the XML input files.

The base ThermoPhase class assigns the default quantities of (kmol/m3) for all species. Inherited classes are responsible for overriding the default values if necessary.

Parameters
uAOutput vector containing the units uA[0] = kmol units - default = 1 uA[1] = m units - default = -nDim(), the number of spatial dimensions in the Phase class. uA[2] = kg units - default = 0; uA[3] = Pa(pressure) units - default = 0; uA[4] = Temperature units - default = 0; uA[5] = time units - default = 0
kspecies index. Defaults to 0.
sizeUAoutput int containing the size of the vector. Currently, this is equal to 6.

Reimplemented in HMWSoln, DebyeHuckel, IdealSolidSolnPhase, MolalityVPSSTP, IdealMolalSoln, MetalSHEelectrons, FixedChemPotSSTP, MineralEQ3, StoichSubstanceSSTP, RedlichKwongMFTP, GibbsExcessVPSSTP, IdealSolnGasVPSS, and StoichSubstance.

Definition at line 848 of file ThermoPhase.cpp.

References Phase::nDim().

void getActivities ( doublereal *  a) const
virtualinherited

Get the array of non-dimensional activities at the current solution temperature, pressure, and solution concentration.

Note, for molality based formulations, this returns the molality based activities.

We resolve this function at this level by calling on the activityConcentration function. However, derived classes may want to override this default implementation.

Parameters
aOutput vector of activities. Length: m_kk.

Reimplemented in HMWSoln, DebyeHuckel, MolalityVPSSTP, IdealMolalSoln, GibbsExcessVPSSTP, PureFluidPhase, and SingleSpeciesTP.

Definition at line 158 of file ThermoPhase.cpp.

References ThermoPhase::getActivityConcentrations(), Phase::nSpecies(), and ThermoPhase::standardConcentration().

Referenced by vcs_MultiPhaseEquil::reportCSV(), and ThermoPhase::reportCSV().

virtual void getActivityCoefficients ( doublereal *  ac) const
inlinevirtualinherited
void getLnActivityCoefficients ( doublereal *  lnac) const
virtualinherited

Get the array of non-dimensional molar-based ln activity coefficients at the current solution temperature, pressure, and solution concentration.

Parameters
lnacOutput vector of ln activity coefficients. Length: m_kk.

Reimplemented in MargulesVPSSTP, RedlichKisterVPSSTP, and MolarityIonicVPSSTP.

Definition at line 166 of file ThermoPhase.cpp.

References ThermoPhase::getActivityCoefficients(), and Phase::m_kk.

Referenced by GibbsExcessVPSSTP::getActivityCoefficients(), IonsFromNeutralVPSSTP::getChemPotentials(), and IonsFromNeutralVPSSTP::s_update_lnActCoeff().

virtual void getChemPotentials_RT ( doublereal *  mu) const
inlinevirtualinherited

Get the array of non-dimensional species chemical potentials These are partial molar Gibbs free energies.

\( \mu_k / \hat R T \). Units: unitless

Parameters
muOutput vector of dimensionless chemical potentials. Length: m_kk.

Reimplemented in IdealSolidSolnPhase, RedlichKwongMFTP, SingleSpeciesTP, IdealSolnGasVPSS, StoichSubstance, MixtureFugacityTP, and VPStandardStateTP.

Definition at line 583 of file ThermoPhase.h.

References ThermoPhase::err().

void getElectrochemPotentials ( doublereal *  mu) const
inlineinherited

Get the species electrochemical potentials.

These are partial molar quantities. This method adds a term \( F z_k \phi_p \) to each chemical potential. The electrochemical potential of species k in a phase p, \( \zeta_k \), is related to the chemical potential via the following equation,

\[ \zeta_{k}(T,P) = \mu_{k}(T,P) + F z_k \phi_p \]

Parameters
muOutput vector of species electrochemical potentials. Length: m_kk. Units: J/kmol

Definition at line 616 of file ThermoPhase.h.

References Phase::charge(), ThermoPhase::electricPotential(), ThermoPhase::getChemPotentials(), and Phase::m_kk.

Referenced by InterfaceKinetics::getDeltaElectrochemPotentials().

virtual void getPartialMolarIntEnergies ( doublereal *  ubar) const
inlinevirtualinherited

Return an array of partial molar internal energies for the species in the mixture.

Units: J/kmol.

Parameters
ubarOutput vector of species partial molar internal energies. Length = m_kk. units are J/kmol.

Reimplemented in IdealGasPhase, RedlichKwongMFTP, SingleSpeciesTP, IdealSolnGasVPSS, and PureFluidPhase.

Definition at line 650 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by MolalityVPSSTP::reportCSV(), and ThermoPhase::reportCSV().

virtual void getdPartialMolarVolumes_dT ( doublereal *  d_vbar_dT) const
inlinevirtualinherited

Return an array of derivatives of partial molar volumes wrt temperature for the species in the mixture.

Units: m^3/kmol.

The derivative is at constant pressure

Parameters
d_vbar_dTOutput vector of derivatives of species partial molar volumes wrt T. Length = m_kk. units are m^3/kmol/K.

Definition at line 683 of file ThermoPhase.h.

References ThermoPhase::err().

virtual void getdPartialMolarVolumes_dP ( doublereal *  d_vbar_dP) const
inlinevirtualinherited

Return an array of derivatives of partial molar volumes wrt pressure for the species in the mixture.

Units: m^3/kmol.

The derivative is at constant temperature

Parameters
d_vbar_dPOutput vector of derivatives of species partial molar volumes wrt P. Length = m_kk. units are m^3/kmol/Pa.

Definition at line 695 of file ThermoPhase.h.

References ThermoPhase::err().

virtual void getPureGibbs ( doublereal *  gpure) const
inlinevirtualinherited

Get the Gibbs functions for the standard state of the species at the current T and P of the solution.

Units are Joules/kmol

Parameters
gpureOutput vector of standard state gibbs free energies Length: m_kk.

Reimplemented in IdealSolidSolnPhase, LatticePhase, IdealGasPhase, SingleSpeciesTP, StoichSubstance, MixtureFugacityTP, VPStandardStateTP, and ConstDensityThermo.

Definition at line 754 of file ThermoPhase.h.

References ThermoPhase::err().

virtual void getIntEnergy_RT ( doublereal *  urt) const
inlinevirtualinherited

Returns the vector of nondimensional Internal Energies of the standard state species at the current T and P of the solution.

Parameters
urtoutput vector of nondimensional standard state internal energies of the species. Length: m_kk.

Reimplemented in IdealSolidSolnPhase, IdealGasPhase, MetalSHEelectrons, FixedChemPotSSTP, MineralEQ3, StoichSubstanceSSTP, WaterSSTP, MixtureFugacityTP, and VPStandardStateTP.

Definition at line 764 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by SingleSpeciesTP::getPartialMolarIntEnergies().

virtual void getdStandardVolumes_dT ( doublereal *  d_vol_dT) const
inlinevirtualinherited

Get the derivative of the molar volumes of the species standard states wrt temperature at the current T and P of the solution.

The derivative is at constant pressure units = m^3 / kmol / K

Parameters
d_vol_dTOutput vector containing derivatives of standard state volumes wrt T Length: m_kk.

Definition at line 800 of file ThermoPhase.h.

References ThermoPhase::err().

virtual void getdStandardVolumes_dP ( doublereal *  d_vol_dP) const
inlinevirtualinherited

Get the derivative molar volumes of the species standard states wrt pressure at the current T and P of the solution.

The derivative is at constant temperature. units = m^3 / kmol / Pa

Parameters
d_vol_dPOutput vector containing the derivative of standard state volumes wrt P. Length: m_kk.

Definition at line 813 of file ThermoPhase.h.

References ThermoPhase::err().

virtual void getGibbs_ref ( doublereal *  g) const
inlinevirtualinherited

Returns the vector of the gibbs function of the reference state at the current temperature of the solution and the reference pressure for the species.

units = J/kmol

Parameters
gOutput vector containing the reference state Gibbs Free energies. Length: m_kk. Units: J/kmol.

Reimplemented in LatticePhase, IdealSolidSolnPhase, IdealGasPhase, LatticeSolidPhase, MixtureFugacityTP, FixedChemPotSSTP, VPStandardStateTP, SingleSpeciesTP, PureFluidPhase, StoichSubstance, and WaterSSTP.

Definition at line 856 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by vcs_VolPhase::_updateG0().

virtual void getIntEnergy_RT_ref ( doublereal *  urt) const
inlinevirtualinherited

Returns the vector of nondimensional internal Energies of the reference state at the current temperature of the solution and the reference pressure for each species.

Parameters
urtOutput vector of nondimensional reference state internal energies of the species. Length: m_kk

Reimplemented in IdealSolidSolnPhase, IdealGasPhase, FixedChemPotSSTP, MetalSHEelectrons, MineralEQ3, and StoichSubstanceSSTP.

Definition at line 879 of file ThermoPhase.h.

References ThermoPhase::err().

virtual void getStandardVolumes_ref ( doublereal *  vol) const
inlinevirtualinherited

Get the molar volumes of the species reference states at the current T and P_ref of the solution.

units = m^3 / kmol

Parameters
volOutput vector containing the standard state volumes. Length: m_kk.

Reimplemented in IdealGasPhase, MixtureFugacityTP, VPStandardStateTP, and WaterSSTP.

Definition at line 904 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by PDSS_IonsFromNeutral::molarVolume_ref().

void setReferenceComposition ( const doublereal *const  x)
virtualinherited

Sets the reference composition.

Parameters
xMole fraction vector to set the reference composition to. If this is zero, then the reference mole fraction is set to the current mole fraction vector.

Definition at line 992 of file ThermoPhase.cpp.

References DATA_PTR, Phase::getMoleFractions(), Phase::m_kk, and ThermoPhase::xMol_Ref.

Referenced by ThermoPhase::initThermoXML().

void getReferenceComposition ( doublereal *const  x) const
virtualinherited

Gets the reference composition.

The reference mole fraction is a safe mole fraction.

Parameters
xMole fraction vector containing the reference composition.

Definition at line 1013 of file ThermoPhase.cpp.

References Phase::m_kk, and ThermoPhase::xMol_Ref.

doublereal enthalpy_mass ( ) const
inlineinherited
doublereal intEnergy_mass ( ) const
inlineinherited
doublereal entropy_mass ( ) const
inlineinherited
doublereal gibbs_mass ( ) const
inlineinherited
doublereal cp_mass ( ) const
inlineinherited
doublereal cv_mass ( ) const
inlineinherited
doublereal _RT ( ) const
inlineinherited
void setState_TPX ( doublereal  t,
doublereal  p,
const doublereal *  x 
)
virtualinherited

Set the temperature (K), pressure (Pa), and mole fractions.

Note, the mole fractions are set first before the pressure is set. Setting the pressure may involve the solution of a nonlinear equation.

Parameters
tTemperature (K)
pPressure (Pa)
xVector of mole fractions. Length is equal to m_kk.

Reimplemented in SingleSpeciesTP, and MixtureFugacityTP.

Definition at line 174 of file ThermoPhase.cpp.

References Phase::setMoleFractions(), ThermoPhase::setPressure(), and Phase::setTemperature().

Referenced by MultiTransport::getMassFluxes(), DustyGasTransport::getMolarFluxes(), MultiPhase::setMoles(), and MultiPhase::setPhaseMoleFractions().

void setState_TPX ( doublereal  t,
doublereal  p,
compositionMap x 
)
inherited

Set the temperature (K), pressure (Pa), and mole fractions.

Note, the mole fractions are set first before the pressure is set. Setting the pressure may involve the solution of a nonlinear equation.

Parameters
tTemperature (K)
pPressure (Pa)
xComposition map of mole fractions. Species not in the composition map are assumed to have zero mole fraction

Definition at line 181 of file ThermoPhase.cpp.

References Phase::setMoleFractionsByName(), ThermoPhase::setPressure(), and Phase::setTemperature().

void setState_TPX ( doublereal  t,
doublereal  p,
const std::string &  x 
)
inherited

Set the temperature (K), pressure (Pa), and mole fractions.

Note, the mole fractions are set first before the pressure is set. Setting the pressure may involve the solution of a nonlinear equation.

Parameters
tTemperature (K)
pPressure (Pa)
xString containing a composition map of the mole fractions. Species not in the composition map are assumed to have zero mole fraction

Definition at line 188 of file ThermoPhase.cpp.

References ThermoPhase::err(), Phase::nSpecies(), Cantera::parseCompString(), CanteraError::save(), Phase::setMoleFractionsByName(), ThermoPhase::setPressure(), Phase::setTemperature(), and Phase::speciesName().

void setState_TPY ( doublereal  t,
doublereal  p,
const doublereal *  y 
)
inherited

Set the internally stored temperature (K), pressure (Pa), and mass fractions of the phase.

Note, the mass fractions are set first before the pressure is set. Setting the pressure may involve the solution of a nonlinear equation.

Parameters
tTemperature (K)
pPressure (Pa)
yVector of mass fractions. Length is equal to m_kk.

Definition at line 206 of file ThermoPhase.cpp.

References Phase::setMassFractions(), ThermoPhase::setPressure(), and Phase::setTemperature().

void setState_TPY ( doublereal  t,
doublereal  p,
compositionMap y 
)
inherited

Set the internally stored temperature (K), pressure (Pa), and mass fractions of the phase.

Note, the mass fractions are set first before the pressure is set. Setting the pressure may involve the solution of a nonlinear equation.

Parameters
tTemperature (K)
pPressure (Pa)
yComposition map of mass fractions. Species not in the composition map are assumed to have zero mass fraction

Definition at line 214 of file ThermoPhase.cpp.

References Phase::setMassFractionsByName(), ThermoPhase::setPressure(), and Phase::setTemperature().

void setState_TPY ( doublereal  t,
doublereal  p,
const std::string &  y 
)
inherited

Set the internally stored temperature (K), pressure (Pa), and mass fractions of the phase.

Note, the mass fractions are set first before the pressure is set. Setting the pressure may involve the solution of a nonlinear equation.

Parameters
tTemperature (K)
pPressure (Pa)
yString containing a composition map of the mass fractions. Species not in the composition map are assumed to have zero mass fraction

Definition at line 222 of file ThermoPhase.cpp.

References ThermoPhase::err(), Phase::nSpecies(), Cantera::parseCompString(), CanteraError::save(), Phase::setMassFractionsByName(), ThermoPhase::setPressure(), Phase::setTemperature(), and Phase::speciesName().

void setState_TP ( doublereal  t,
doublereal  p 
)
inherited
void setState_PX ( doublereal  p,
doublereal *  x 
)
inherited

Set the pressure (Pa) and mole fractions.

Note, the mole fractions are set first before the pressure is set. Setting the pressure may involve the solution of a nonlinear equation.

Parameters
pPressure (Pa)
xVector of mole fractions. Length is equal to m_kk.

Definition at line 249 of file ThermoPhase.cpp.

References Phase::setMoleFractions(), and ThermoPhase::setPressure().

Referenced by vcs_VolPhase::_updateMoleFractionDependencies(), IdealSolnGasVPSS::setToEquilState(), RedlichKwongMFTP::setToEquilState(), IdealGasPhase::setToEquilState(), and IdealSolidSolnPhase::setToEquilState().

void setState_PY ( doublereal  p,
doublereal *  y 
)
inherited

Set the internally stored pressure (Pa) and mass fractions.

Note, the temperature is held constant during this operation. Note, the mass fractions are set first before the pressure is set. Setting the pressure may involve the solution of a nonlinear equation.

Parameters
pPressure (Pa)
yVector of mass fractions. Length is equal to m_kk.

Definition at line 256 of file ThermoPhase.cpp.

References Phase::setMassFractions(), and ThermoPhase::setPressure().

void setState_HP ( doublereal  h,
doublereal  p,
doublereal  tol = 1.e-4 
)
virtualinherited

Set the internally stored specific enthalpy (J/kg) and pressure (Pa) of the phase.

Parameters
hSpecific enthalpy (J/kg)
pPressure (Pa)
tolOptional parameter setting the tolerance of the calculation. Defaults to 1.0E-4

Reimplemented in SingleSpeciesTP, and PureFluidPhase.

Definition at line 263 of file ThermoPhase.cpp.

References ThermoPhase::setState_HPorUV().

Referenced by FlowReactor::updateState(), and ConstPressureReactor::updateState().

void setState_UV ( doublereal  u,
doublereal  v,
doublereal  tol = 1.e-4 
)
virtualinherited

Set the specific internal energy (J/kg) and specific volume (m^3/kg).

This function fixes the internal state of the phase so that the specific internal energy and specific volume have the value of the input parameters.

Parameters
uspecific internal energy (J/kg)
vspecific volume (m^3/kg).
tolOptional parameter setting the tolerance of the calculation. Defaults to 1.0E-4

Reimplemented in SingleSpeciesTP, and PureFluidPhase.

Definition at line 270 of file ThermoPhase.cpp.

References ThermoPhase::setState_HPorUV().

Referenced by Reactor::updateState().

void setState_SP ( doublereal  s,
doublereal  p,
doublereal  tol = 1.e-4 
)
virtualinherited

Set the specific entropy (J/kg/K) and pressure (Pa).

This function fixes the internal state of the phase so that the specific entropy and the pressure have the value of the input parameters.

Parameters
sspecific entropy (J/kg/K)
pspecific pressure (Pa).
tolOptional parameter setting the tolerance of the calculation. Defaults to 1.0E-4

Reimplemented in SingleSpeciesTP, and PureFluidPhase.

Definition at line 546 of file ThermoPhase.cpp.

References ThermoPhase::setState_SPorSV().

void setState_SV ( doublereal  s,
doublereal  v,
doublereal  tol = 1.e-4 
)
virtualinherited

Set the specific entropy (J/kg/K) and specific volume (m^3/kg).

This function fixes the internal state of the phase so that the specific entropy and specific volume have the value of the input parameters.

Parameters
sspecific entropy (J/kg/K)
vspecific volume (m^3/kg).
tolOptional parameter setting the tolerance of the calculation. Defaults to 1.0E-4

Reimplemented in SingleSpeciesTP, and PureFluidPhase.

Definition at line 553 of file ThermoPhase.cpp.

References ThermoPhase::setState_SPorSV().

virtual void setToEquilState ( const doublereal *  lambda_RT)
inlinevirtualinherited

This method is used by the ChemEquil equilibrium solver.

It sets the state such that the chemical potentials satisfy

\[ \frac{\mu_k}{\hat R T} = \sum_m A_{k,m} \left(\frac{\lambda_m} {\hat R T}\right) \]

where \( \lambda_m \) is the element potential of element m. The temperature is unchanged. Any phase (ideal or not) that implements this method can be equilibrated by ChemEquil.

Parameters
lambda_RTInput vector of dimensionless element potentials The length is equal to nElements().

Reimplemented in HMWSoln, DebyeHuckel, IdealSolidSolnPhase, IdealGasPhase, IdealMolalSoln, MolalityVPSSTP, RedlichKwongMFTP, IdealSolnGasVPSS, and ConstDensityThermo.

Definition at line 1193 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by ChemEquil::setToEquilState().

void setElementPotentials ( const vector_fp lambda)
inherited

Stores the element potentials in the ThermoPhase object.

Called by function 'equilibrate' in ChemEquil.h to transfer the element potentials to this object after every successful equilibration routine. The element potentials are stored in their dimensionless forms, calculated by dividing by RT.

Parameters
lambdaInput vector containing the element potentials. Length = nElements. Units are Joules/kmol.

Definition at line 1106 of file ThermoPhase.cpp.

References Cantera::GasConstant, ThermoPhase::m_hasElementPotentials, ThermoPhase::m_lambdaRRT, Phase::nElements(), and Phase::temperature().

Referenced by Cantera::equilibrate(), ChemEquil::equilibrate(), and Cantera::vcs_equilibrate().

bool getElementPotentials ( doublereal *  lambda) const
inherited

Returns the element potentials stored in the ThermoPhase object.

Returns the stored element potentials. The element potentials are retrieved from their stored dimensionless forms by multiplying by RT.

Parameters
lambdaOutput vector containing the element potentials. Length = nElements. Units are Joules/kmol.
Returns
bool indicating whether there are any valid stored element potentials. The calling routine should check this bool. In the case that there aren't any, lambda is not touched.

Definition at line 1129 of file ThermoPhase.cpp.

References Cantera::GasConstant, ThermoPhase::m_hasElementPotentials, ThermoPhase::m_lambdaRRT, Phase::nElements(), and Phase::temperature().

Referenced by ChemEquil::equilibrate().

virtual doublereal critTemperature ( ) const
inlinevirtualinherited
virtual doublereal critPressure ( ) const
inlinevirtualinherited

Critical pressure (Pa).

Reimplemented in HMWSoln, IdealMolalSoln, RedlichKwongMFTP, PureFluidPhase, and WaterSSTP.

Definition at line 1242 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by MixtureFugacityTP::calculatePsat(), and MixtureFugacityTP::psatEst().

virtual doublereal critDensity ( ) const
inlinevirtualinherited

Critical density (kg/m3).

Reimplemented in HMWSoln, IdealMolalSoln, RedlichKwongMFTP, PureFluidPhase, and WaterSSTP.

Definition at line 1248 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by MixtureFugacityTP::densityCalc(), and MixtureFugacityTP::phaseState().

virtual doublereal satTemperature ( doublereal  p) const
inlinevirtualinherited

Return the saturation temperature given the pressure.

Parameters
pPressure (Pa)

Reimplemented in HMWSoln, DebyeHuckel, SingleSpeciesTP, and PureFluidPhase.

Definition at line 1267 of file ThermoPhase.h.

References ThermoPhase::err().

virtual doublereal satPressure ( doublereal  t) const
inlinevirtualinherited

Return the saturation pressure given the temperature.

Parameters
tTemperature (Kelvin)

Reimplemented in HMWSoln, DebyeHuckel, SingleSpeciesTP, PureFluidPhase, and WaterSSTP.

Definition at line 1276 of file ThermoPhase.h.

References ThermoPhase::err().

virtual doublereal vaporFraction ( ) const
inlinevirtualinherited

Return the fraction of vapor at the current conditions.

Reimplemented in HMWSoln, DebyeHuckel, SingleSpeciesTP, PureFluidPhase, and WaterSSTP.

Definition at line 1282 of file ThermoPhase.h.

References ThermoPhase::err().

virtual void setState_Tsat ( doublereal  t,
doublereal  x 
)
inlinevirtualinherited

Set the state to a saturated system at a particular temperature.

Parameters
tTemperature (kelvin)
xFraction of vapor

Reimplemented in HMWSoln, DebyeHuckel, SingleSpeciesTP, and PureFluidPhase.

Definition at line 1292 of file ThermoPhase.h.

References ThermoPhase::err().

virtual void setState_Psat ( doublereal  p,
doublereal  x 
)
inlinevirtualinherited

Set the state to a saturated system at a particular pressure.

Parameters
pPressure (Pa)
xFraction of vapor

Reimplemented in HMWSoln, DebyeHuckel, SingleSpeciesTP, and PureFluidPhase.

Definition at line 1301 of file ThermoPhase.h.

References ThermoPhase::err().

void saveSpeciesData ( const size_t  k,
const XML_Node *const  data 
)
inherited

Store a reference pointer to the XML tree containing the species data for this phase.

The following methods are used in the process of constructing the phase and setting its parameters from a specification in an input file. They are not normally used in application programs. To see how they are used, see files importCTML.cpp and ThermoFactory.cpp.

This is used to access data needed to construct transport manager later.

Parameters
kSpecies index
dataPointer to the XML_Node data containing information about the species in the phase.

Definition at line 1050 of file ThermoPhase.cpp.

References ThermoPhase::m_speciesData.

Referenced by FixedChemPotSSTP::FixedChemPotSSTP(), and Cantera::importPhase().

const std::vector< const XML_Node * > & speciesData ( ) const
inherited

Return a pointer to the vector of XML nodes containing the species data for this phase.

Definition at line 1060 of file ThermoPhase.cpp.

References Phase::m_kk, and ThermoPhase::m_speciesData.

Referenced by MineralEQ3::initThermoXML(), DebyeHuckel::initThermoXML(), TransportFactory::initTransport(), LatticeSolidPhase::installSlavePhases(), and TransportFactory::setupLiquidTransport().

void setSpeciesThermo ( SpeciesThermo spthermo)
inherited

Install a species thermodynamic property manager.

The species thermodynamic property manager computes properties of the pure species for use in constructing solution properties. It is meant for internal use, and some classes derived from ThermoPhase may not use any species thermodynamic property manager. This method is called by function importPhase() in importCTML.cpp.

Parameters
spthermoinput pointer to the species thermodynamic property manager.

Definition at line 886 of file ThermoPhase.cpp.

References ThermoPhase::m_spthermo.

Referenced by FixedChemPotSSTP::FixedChemPotSSTP(), Cantera::importPhase(), LatticeSolidPhase::installSlavePhases(), and VPSSMgrFactory::newVPSSMgr().

SpeciesThermo & speciesThermo ( int  k = -1)
virtualinherited

Return a changeable reference to the calculation manager for species reference-state thermodynamic properties.

Parameters
kSpeices id. The default is -1, meaning return the default

Reimplemented in LatticeSolidPhase.

Definition at line 904 of file ThermoPhase.cpp.

References ThermoPhase::m_spthermo.

Referenced by PDSS_ConstVol::constructPDSSXML(), PDSS_SSVol::constructPDSSXML(), PDSS_ConstVol::initThermo(), PDSS_IdealGas::initThermo(), PDSS_IonsFromNeutral::initThermo(), PDSS_SSVol::initThermo(), VPSSMgrFactory::newVPSSMgr(), and PDSS::PDSS().

void initThermoFile ( std::string  inputFile,
std::string  id 
)
virtualinherited

Initialization of a ThermoPhase object using an ctml file.

This routine is a precursor to initThermoXML(XML_Node*) routine, which does most of the work. Here we read extra information about the XML description of a phase. Regular information about elements and species and their reference state thermodynamic information have already been read at this point. For example, we do not need to call this function for ideal gas equations of state.

Parameters
inputFileXML file containing the description of the phase
idOptional parameter identifying the name of the phase. If none is given, the first XML phase element encountered will be used.

Definition at line 928 of file ThermoPhase.cpp.

References XML_Node::build(), XML_Node::copy(), Cantera::findInputFile(), Cantera::findXMLPhase(), ThermoPhase::initThermoXML(), and Phase::xml().

void initThermoXML ( XML_Node phaseNode,
std::string  id 
)
virtualinherited

Import and initialize a ThermoPhase object using an XML tree.

Here we read extra information about the XML description of a phase. Regular information about elements and species and their reference state thermodynamic information have already been read at this point. For example, we do not need to call this function for ideal gas equations of state. This function is called from importPhase() after the elements and the species are initialized with default ideal solution level data.

The default implementation in ThermoPhase calls the virtual function initThermo() and then sets the "state" of the phase by looking for an XML element named "state", and then interpreting its contents by calling the virtual function setStateFromXML().

Parameters
phaseNodeThis object must be the phase node of a complete XML tree description of the phase, including all of the species data. In other words while "phase" must point to an XML phase object, it must have sibling nodes "speciesData" that describe the species in the phase.
idID of the phase. If nonnull, a check is done to see if phaseNode is pointing to the phase with the correct id.

Reimplemented in HMWSoln, DebyeHuckel, IdealSolidSolnPhase, LatticePhase, IdealMolalSoln, MolalityVPSSTP, MixedSolventElectrolyte, MargulesVPSSTP, RedlichKisterVPSSTP, PhaseCombo_Interaction, MixtureFugacityTP, IonsFromNeutralVPSSTP, FixedChemPotSSTP, electrodeElectron, VPStandardStateTP, RedlichKwongMFTP, MineralEQ3, MetalSHEelectrons, WaterSSTP, StoichSubstanceSSTP, MolarityIonicVPSSTP, IdealSolnGasVPSS, and PseudoBinaryVPSSTP.

Definition at line 979 of file ThermoPhase.cpp.

References XML_Node::child(), XML_Node::hasChild(), ThermoPhase::setReferenceComposition(), and ThermoPhase::setStateFromXML().

Referenced by Cantera::importPhase(), ThermoPhase::initThermoFile(), StoichSubstanceSSTP::initThermoXML(), MetalSHEelectrons::initThermoXML(), VPStandardStateTP::initThermoXML(), electrodeElectron::initThermoXML(), FixedChemPotSSTP::initThermoXML(), MixtureFugacityTP::initThermoXML(), LatticePhase::initThermoXML(), and IdealSolidSolnPhase::initThermoXML().

void installSlavePhases ( Cantera::XML_Node phaseNode)
virtualinherited

Add in species from Slave phases.

This hook is used for cSS_CONVENTION_SLAVE phases

Parameters
phaseNodeXML Element for the phase

Reimplemented in LatticeSolidPhase.

Definition at line 1045 of file ThermoPhase.cpp.

Referenced by Cantera::importPhase().

virtual void getParameters ( int &  n,
doublereal *const  c 
) const
inlinevirtualinherited

Get the equation of state parameters in a vector.

The number and meaning of these depends on the subclass.

Parameters
nnumber of parameters
carray of n coefficients

Reimplemented in HMWSoln, DebyeHuckel, LatticePhase, IdealMolalSoln, SingleSpeciesTP, FixedChemPotSSTP, MineralEQ3, MetalSHEelectrons, StoichSubstanceSSTP, StoichSubstance, and ConstDensityThermo.

Definition at line 1462 of file ThermoPhase.h.

virtual void getdlnActCoeffds ( const doublereal  dTds,
const doublereal *const  dXds,
doublereal *  dlnActCoeffds 
) const
inlinevirtualinherited

Get the change in activity coefficients wrt changes in state (temp, mole fraction, etc) along a line in parameter space or along a line in physical space.

Parameters
dTdsInput of temperature change along the path
dXdsInput vector of changes in mole fraction along the path. length = m_kk Along the path length it must be the case that the mole fractions sum to one.
dlnActCoeffdsOutput vector of the directional derivatives of the log Activity Coefficients along the path. length = m_kk units are 1/units(s). if s is a physical coordinate then the units are 1/m.

Reimplemented in MixedSolventElectrolyte, MargulesVPSSTP, RedlichKisterVPSSTP, PhaseCombo_Interaction, and IonsFromNeutralVPSSTP.

Definition at line 1511 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by IonsFromNeutralVPSSTP::getdlnActCoeffds(), and LiquidTransport::update_Grad_lnAC().

virtual void getdlnActCoeffdlnX_diag ( doublereal *  dlnActCoeffdlnX_diag) const
inlinevirtualinherited

Get the array of ln mole fraction derivatives of the log activity coefficients - diagonal component only.

This function is a virtual method. For ideal mixtures (unity activity coefficients), this can return zero. Implementations should take the derivative of the logarithm of the activity coefficient with respect to the logarithm of the mole fraction variable that represents the standard state. This quantity is to be used in conjunction with derivatives of that mole fraction variable when the derivative of the chemical potential is taken.

units = dimensionless

Parameters
dlnActCoeffdlnX_diagOutput vector of derivatives of the log Activity Coefficients wrt the mole fractions. length = m_kk

Reimplemented in MixedSolventElectrolyte, MargulesVPSSTP, RedlichKisterVPSSTP, PhaseCombo_Interaction, and IonsFromNeutralVPSSTP.

Definition at line 1533 of file ThermoPhase.h.

References ThermoPhase::err().

Referenced by IonsFromNeutralVPSSTP::s_update_dlnActCoeff_dlnX_diag().

virtual void getdlnActCoeffdlnN_diag ( doublereal *  dlnActCoeffdlnN_diag) const
inlinevirtualinherited

Get the array of log species mole number derivatives of the log activity coefficients.

This function is a virtual method. For ideal mixtures (unity activity coefficients), this can return zero. Implementations should take the derivative of the logarithm of the activity coefficient with respect to the logarithm of the concentration-like variable (i.e. moles) that represents the standard state. This quantity is to be used in conjunction with derivatives of that species mole number variable when the derivative of the chemical potential is taken.

units = dimensionless

Parameters
dlnActCoeffdlnN_diagOutput vector of derivatives of the log Activity Coefficients. length = m_kk

Reimplemented in MixedSolventElectrolyte, MargulesVPSSTP, RedlichKisterVPSSTP, PhaseCombo_Interaction, IonsFromNeutralVPSSTP, MixtureFugacityTP, and VPStandardStateTP.

Definition at line 1554 of file ThermoPhase.h.

References ThermoPhase::err().

void getdlnActCoeffdlnN ( const size_t  ld,
doublereal *const  dlnActCoeffdlnN 
)
virtualinherited

Get the array of derivatives of the log activity coefficients with respect to the log of the species mole numbers.

Implementations should take the derivative of the logarithm of the activity coefficient with respect to a species log mole number (with all other species mole numbers held constant). The default treatment in the ThermoPhase object is to set this vector to zero.

units = 1 / kmol

dlnActCoeffdlnN[ ld * k + m] will contain the derivative of log act_coeff for the mth species with respect to the number of moles of the kth species.

\[ \frac{d \ln(\gamma_m) }{d \ln( n_k ) }\Bigg|_{n_i} \]

Parameters
ldNumber of rows in the matrix
dlnActCoeffdlnNOutput vector of derivatives of the log Activity Coefficients. length = m_kk * m_kk

Reimplemented in MolalityVPSSTP, MixedSolventElectrolyte, MargulesVPSSTP, RedlichKisterVPSSTP, PhaseCombo_Interaction, IonsFromNeutralVPSSTP, and GibbsExcessVPSSTP.

Definition at line 1158 of file ThermoPhase.cpp.

References Phase::m_kk.

Referenced by vcs_VolPhase::_updateLnActCoeffJac().

std::string report ( bool  show_thermo = true) const
virtualinherited
void reportCSV ( std::ofstream &  csvFile) const
virtualinherited
XML_Node & xml ( )
inherited
std::string id ( ) const
inherited
void setID ( std::string  id)
inherited

Set the string id for the phase.

Parameters
idString id of the phase

Definition at line 135 of file Phase.cpp.

References Phase::id(), and Phase::m_id.

Referenced by FixedChemPotSSTP::FixedChemPotSSTP(), and Cantera::importPhase().

std::string name ( ) const
inherited
void setName ( std::string  nm)
inherited

Sets the string name for the phase.

Parameters
nmString name of the phase

Definition at line 145 of file Phase.cpp.

References Phase::m_name.

Referenced by FixedChemPotSSTP::FixedChemPotSSTP(), and Cantera::importPhase().

string elementName ( size_t  m) const
inherited
size_t elementIndex ( std::string  name) const
inherited

Return the index of element named 'name'.

The index is an integer assigned to each element in the order it was added. Returns npos if the specified element is not found.

Parameters
nameName of the element

Definition at line 175 of file Phase.cpp.

References Phase::m_elementNames, Phase::m_mm, and Cantera::npos.

Referenced by Phase::addUniqueElementAfterFreeze(), MultiPhase::init(), WaterSSTP::initThermoXML(), LatticeSolidPhase::installSlavePhases(), Cantera::installSpecies(), Cantera::LookupGe(), and PDSS_HKFT::LookupGe().

const vector< string > & elementNames ( ) const
inherited

Return a read-only reference to the vector of element names.

Definition at line 185 of file Phase.cpp.

References Phase::m_elementNames.

Referenced by ChemEquil::equilibrate(), ChemEquil::estimateEP_Brinkley(), and IonsFromNeutralVPSSTP::initThermoXML().

doublereal atomicWeight ( size_t  m) const
inherited

Atomic weight of element m.

Parameters
mElement index

Definition at line 190 of file Phase.cpp.

References Phase::m_atomicWeights.

Referenced by ChemEquil::initialize(), and WaterSSTP::initThermoXML().

doublereal entropyElement298 ( size_t  m) const
inherited

Entropy of the element in its standard state at 298 K and 1 bar.

Parameters
mElement index

Definition at line 195 of file Phase.cpp.

References AssertThrowMsg, AssertTrace, ENTROPY298_UNKNOWN, Phase::m_entropy298, and Phase::m_mm.

Referenced by LatticeSolidPhase::installSlavePhases(), Cantera::LookupGe(), and PDSS_HKFT::LookupGe().

int atomicNumber ( size_t  m) const
inherited

Atomic number of element m.

Parameters
mElement index

Definition at line 209 of file Phase.cpp.

References Phase::m_atomicNumbers.

Referenced by MultiPhase::addPhase(), and LatticeSolidPhase::installSlavePhases().

int elementType ( size_t  m) const
inherited

Return the element constraint type Possible types include:

CT_ELEM_TYPE_TURNEDOFF -1 CT_ELEM_TYPE_ABSPOS 0 CT_ELEM_TYPE_ELECTRONCHARGE 1 CT_ELEM_TYPE_CHARGENEUTRALITY 2 CT_ELEM_TYPE_LATTICERATIO 3 CT_ELEM_TYPE_KINETICFROZEN 4 CT_ELEM_TYPE_SURFACECONSTRAINT 5 CT_ELEM_TYPE_OTHERCONSTRAINT 6

The default is CT_ELEM_TYPE_ABSPOS.

Parameters
mElement index
Returns
Returns the element type

Definition at line 214 of file Phase.cpp.

References Phase::m_elem_type.

Referenced by LatticeSolidPhase::installSlavePhases(), and vcs_VolPhase::transferElementsFM().

int changeElementType ( int  m,
int  elem_type 
)
inherited

Change the element type of the mth constraint Reassigns an element type.

Parameters
mElement index
elem_typeNew elem type to be assigned
Returns
Returns the old element type

Definition at line 219 of file Phase.cpp.

References Phase::m_elem_type.

const vector_fp & atomicWeights ( ) const
inherited

Return a read-only reference to the vector of atomic weights.

Definition at line 204 of file Phase.cpp.

References Phase::m_atomicWeights.

Referenced by LatticeSolidPhase::installSlavePhases().

size_t nElements ( ) const
inherited
void checkElementIndex ( size_t  m) const
inherited

Check that the specified element index is in range Throws an exception if m is greater than nElements()-1.

Definition at line 155 of file Phase.cpp.

References Phase::m_mm.

Referenced by Phase::elementName(), and Phase::nAtoms().

void checkElementArraySize ( size_t  mm) const
inherited

Check that an array size is at least nElements() Throws an exception if mm is less than nElements().

Used before calls which take an array pointer.

Definition at line 162 of file Phase.cpp.

References Phase::m_mm.

doublereal nAtoms ( size_t  k,
size_t  m 
) const
inherited
void getAtoms ( size_t  k,
double *  atomArray 
) const
inherited

Get a vector containing the atomic composition of species k.

Parameters
kspecies index
atomArrayvector containing the atomic number in the species. Length: m_mm

Definition at line 233 of file Phase.cpp.

References Phase::m_mm, and Phase::m_speciesComp.

Referenced by LatticeSolidPhase::installSlavePhases().

size_t speciesIndex ( std::string  name) const
inherited
string speciesName ( size_t  k) const
inherited

Name of the species with index k.

Parameters
kindex of the species

Definition at line 257 of file Phase.cpp.

References Phase::checkSpeciesIndex(), and Phase::m_speciesNames.

Referenced by StFlow::componentName(), ReactingSurf1D::componentName(), ChemEquil::estimateElementPotentials(), ChemEquil::estimateEP_Brinkley(), MolalityVPSSTP::findCLMIndex(), TransportFactory::fitProperties(), AqueousTransport::getLiquidTransportData(), Phase::getMoleFractionsByName(), Cantera::importSolution(), MultiPhase::init(), ChemEquil::initialize(), LiquidTransport::initLiquid(), SimpleTransport::initLiquid(), IdealMolalSoln::initThermoXML(), DebyeHuckel::initThermoXML(), FlowDevice::install(), LatticeSolidPhase::installSlavePhases(), Kinetics::kineticsSpeciesName(), solveProb::print_header(), HMWSoln::printCoeffs(), PhaseCombo_Interaction::readXMLBinarySpecies(), RedlichKisterVPSSTP::readXMLBinarySpecies(), MargulesVPSSTP::readXMLBinarySpecies(), MixedSolventElectrolyte::readXMLBinarySpecies(), PureFluidPhase::report(), MolalityVPSSTP::report(), ThermoPhase::report(), PureFluidPhase::reportCSV(), vcs_MultiPhaseEquil::reportCSV(), MolalityVPSSTP::reportCSV(), ThermoPhase::reportCSV(), HMWSoln::s_updatePitzer_d2lnMolalityActCoeff_dT2(), HMWSoln::s_updatePitzer_dlnMolalityActCoeff_dP(), HMWSoln::s_updatePitzer_dlnMolalityActCoeff_dT(), HMWSoln::s_updatePitzer_lnMolalityActCoeff(), StFlow::save(), SurfPhase::setCoveragesByName(), ChemEquil::setInitialMoles(), Phase::setMassFractionsByName(), MolalityVPSSTP::setMolalitiesByName(), Phase::setMoleFractionsByName(), ThermoPhase::setState_TPX(), ThermoPhase::setState_TPY(), Inlet1D::showSolution(), ReactingSurf1D::showSolution(), Phase::speciesSPName(), and ChemEquil::update().

std::string speciesSPName ( int  k) const
inherited

Returns the expanded species name of a species, including the phase name This is guaranteed to be unique within a Cantera problem.

Parameters
kSpecies index within the phase
Returns
The "phaseName:speciesName" string

Definition at line 282 of file Phase.cpp.

References Phase::m_name, and Phase::speciesName().

const vector< string > & speciesNames ( ) const
inherited
size_t nSpecies ( ) const
inlineinherited

Returns the number of species in the phase.

Definition at line 252 of file Phase.h.

References Phase::m_kk.

Referenced by MultiPhase::addPhase(), InterfaceKinetics::applyButlerVolmerCorrection(), Kinetics::assignShallowPointers(), MultiPhase::calcElemAbundances(), Phase::chargeDensity(), MultiPhaseEquil::computeReactionSteps(), PDSS_IonsFromNeutral::constructPDSSXML(), RedlichKisterVPSSTP::cp_mole(), MargulesVPSSTP::cp_mole(), MixedSolventElectrolyte::cp_mole(), PhaseCombo_Interaction::cp_mole(), SolidTransport::electricalConductivity(), RedlichKisterVPSSTP::enthalpy_mole(), MargulesVPSSTP::enthalpy_mole(), MixedSolventElectrolyte::enthalpy_mole(), PhaseCombo_Interaction::enthalpy_mole(), RedlichKisterVPSSTP::entropy_mole(), MargulesVPSSTP::entropy_mole(), MixedSolventElectrolyte::entropy_mole(), PhaseCombo_Interaction::entropy_mole(), ChemEquil::equilibrate(), vcs_MultiPhaseEquil::equilibrate_TP(), ChemEquil::estimateElementPotentials(), ThermoPhase::getActivities(), MetalPhase::getActivityConcentrations(), MetalPhase::getChemPotentials(), IonsFromNeutralVPSSTP::getdlnActCoeffds(), MetalPhase::getEnthalpy_RT(), MetalPhase::getEntropy_R(), AqueousKinetics::getEquilibriumConstants(), InterfaceKinetics::getEquilibriumConstants(), MultiTransport::getMassFluxes(), LTI_Pairwise_Interaction::getMatrixTransProp(), LTI_StefanMaxwell_PPN::getMatrixTransProp(), SolidTransport::getMixDiffCoeffs(), LTI_MoleFracs::getMixTransProp(), LTI_MassFracs::getMixTransProp(), LTI_Log_MoleFracs::getMixTransProp(), LTI_Pairwise_Interaction::getMixTransProp(), LTI_StefanMaxwell_PPN::getMixTransProp(), LTI_MoleFracs_ExpT::getMixTransProp(), SolidTransport::getMobilities(), MultiTransport::getMolarFluxes(), Phase::getMoleFractionsByName(), MultiPhase::getMoles(), MetalPhase::getStandardChemPotentials(), ImplicitSurfChem::ImplicitSurfChem(), Cantera::importSolution(), LiquidTranInteraction::init(), MultiPhase::init(), AqueousKinetics::init(), GasKinetics::init(), InterfaceKinetics::init(), GasTransport::initGas(), ChemEquil::initialize(), DustyGasTransport::initialize(), PseudoBinaryVPSSTP::initLengths(), IdealSolnGasVPSS::initLengths(), MolarityIonicVPSSTP::initLengths(), GibbsExcessVPSSTP::initLengths(), VPStandardStateTP::initLengths(), IonsFromNeutralVPSSTP::initLengths(), MixtureFugacityTP::initLengths(), VPSSMgr::initLengths(), PhaseCombo_Interaction::initLengths(), RedlichKisterVPSSTP::initLengths(), MargulesVPSSTP::initLengths(), MixedSolventElectrolyte::initLengths(), MolalityVPSSTP::initLengths(), IdealMolalSoln::initLengths(), IdealSolidSolnPhase::initLengths(), DebyeHuckel::initLengths(), HMWSoln::initLengths(), LiquidTransport::initLiquid(), SimpleTransport::initLiquid(), AqueousTransport::initLiquid(), ConstDensityThermo::initThermo(), StoichSubstance::initThermo(), StoichSubstanceSSTP::initThermo(), LatticeSolidPhase::initThermo(), SingleSpeciesTP::initThermo(), LatticePhase::initThermo(), FlowDevice::install(), rxninfo::installReaction(), LatticeSolidPhase::installSlavePhases(), Kinetics::nTotalSpecies(), solveProb::print_header(), PseudoBinaryVPSSTP::report(), MolarityIonicVPSSTP::report(), PureFluidPhase::report(), MolalityVPSSTP::report(), ThermoPhase::report(), PureFluidPhase::reportCSV(), vcs_MultiPhaseEquil::reportCSV(), MolalityVPSSTP::reportCSV(), ThermoPhase::reportCSV(), Phase::restoreState(), IonsFromNeutralVPSSTP::s_update_dlnActCoeff_dlnN(), Phase::saveState(), Kinetics::selectPhase(), ImplicitSurfChem::setConcSpecies(), SurfPhase::setCoveragesByName(), Phase::setMassFractionsByName(), MolalityVPSSTP::setMolalitiesByName(), Phase::setMoleFractionsByName(), MultiPhase::setMoles(), SolidTransport::setParameters(), MultiPhase::setPhaseMoleFractions(), vcs_VolPhase::setPtrThermoPhase(), ThermoPhase::setState_TPX(), ThermoPhase::setState_TPY(), Transport::setThermo(), ReactorBase::setThermoMgr(), TransportFactory::setupLiquidTransport(), TransportFactory::setupMM(), Inlet1D::showSolution(), solveSP::solveSP(), StFlow::StFlow(), vcs_VolPhase::transferElementsFM(), AqueousKinetics::updateKc(), InterfaceKinetics::updateKc(), ConstPressureReactor::updateState(), Reactor::updateState(), and MultiPhase::uploadMoleFractionsFromPhases().

void checkSpeciesIndex ( size_t  k) const
inherited

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

Definition at line 268 of file Phase.cpp.

References Phase::m_kk.

Referenced by Phase::concentration(), Phase::massFraction(), Phase::molecularWeight(), Phase::moleFraction(), Phase::nAtoms(), and Phase::speciesName().

void checkSpeciesArraySize ( size_t  kk) const
inherited

Check that an array size is at least nSpecies() Throws an exception if kk is less than nSpecies().

Used before calls which take an array pointer.

Definition at line 275 of file Phase.cpp.

References Phase::m_kk.

void saveState ( vector_fp state) const
inherited

Save the current internal state of the phase Write to vector 'state' the current internal state.

Parameters
stateoutput vector. Will be resized to nSpecies() + 2.

Definition at line 288 of file Phase.cpp.

References Phase::nSpecies().

Referenced by ChemEquil::equilibrate(), ChemEquil::estimateEP_Brinkley(), TransportFactory::newTransport(), ReactorBase::setThermoMgr(), FlowReactor::updateState(), ConstPressureReactor::updateState(), and Reactor::updateState().

void saveState ( size_t  lenstate,
doublereal *  state 
) const
inherited

Write to array 'state' the current internal state.

Parameters
lenstatelength of the state array. Must be >= nSpecies()+2
stateoutput vector. Must be of length nSpecies() + 2 or greater.

Definition at line 293 of file Phase.cpp.

References Phase::density(), Phase::getMassFractions(), and Phase::temperature().

void restoreState ( const vector_fp state)
inherited

Restore a state saved on a previous call to saveState.

Parameters
stateState vector containing the previously saved state.

Definition at line 300 of file Phase.cpp.

Referenced by ChemEquil::equilibrate(), ChemEquil::estimateEP_Brinkley(), MultiTransport::getMassFluxes(), FlowReactor::initialize(), ConstPressureReactor::initialize(), Reactor::initialize(), and TransportFactory::newTransport().

void restoreState ( size_t  lenstate,
const doublereal *  state 
)
inherited

Restore the state of the phase from a previously saved state vector.

Parameters
lenstateLength of the state vector
stateVector of state conditions.

Definition at line 305 of file Phase.cpp.

References Phase::nSpecies(), Phase::setDensity(), Phase::setMassFractions_NoNorm(), and Phase::setTemperature().

void setMoleFractionsByName ( compositionMap xMap)
inherited

Set the species mole fractions by name.

@param xMap map from species names to mole fraction values.

Species not listed by name in xMap are set to zero.

Definition at line 362 of file Phase.cpp.

References Phase::nSpecies(), Phase::setMoleFractions(), and Phase::speciesName().

Referenced by Inlet1D::setMoleFractions(), OutletRes1D::setMoleFractions(), Phase::setMoleFractionsByName(), ThermoPhase::setState_TPX(), Phase::setState_TRX(), MixtureFugacityTP::setStateFromXML(), and ThermoPhase::setStateFromXML().

void setMoleFractionsByName ( const std::string &  x)
inherited

Set the mole fractions of a group of species by name.

Species which are not listed by name in the composition map are set to zero.

Parameters
xstring x in the form of a composition map

Definition at line 376 of file Phase.cpp.

References Phase::nSpecies(), Cantera::parseCompString(), Phase::setMoleFractionsByName(), and Phase::speciesName().

void setMassFractionsByName ( compositionMap yMap)
inherited

Set the species mass fractions by name.

@param yMap map from species names to mass fraction values.

Species not listed by name in yMap are set to zero.

Definition at line 416 of file Phase.cpp.

References Phase::nSpecies(), Phase::setMassFractions(), and Phase::speciesName().

Referenced by Phase::setMassFractionsByName(), ThermoPhase::setState_TPY(), Phase::setState_TRY(), MixtureFugacityTP::setStateFromXML(), and ThermoPhase::setStateFromXML().

void setMassFractionsByName ( const std::string &  x)
inherited

Set the species mass fractions by name.

Species not listed by name in x are set to zero.

Parameters
xString containing a composition map

Definition at line 430 of file Phase.cpp.

References Phase::nSpecies(), Cantera::parseCompString(), Phase::setMassFractionsByName(), and Phase::speciesName().

void setState_TRX ( doublereal  t,
doublereal  dens,
const doublereal *  x 
)
inherited

Set the internally stored temperature (K), density, and mole fractions.

Parameters
tTemperature in kelvin
densDensity (kg/m^3)
xvector of species mole fractions, length m_kk

Definition at line 441 of file Phase.cpp.

References Phase::setDensity(), Phase::setMoleFractions(), and Phase::setTemperature().

void setState_TRX ( doublereal  t,
doublereal  dens,
compositionMap x 
)
inherited

Set the internally stored temperature (K), density, and mole fractions.

Parameters
tTemperature in kelvin
densDensity (kg/m^3)
xComposition Map containing the mole fractions. Species not included in the map are assumed to have a zero mole fraction.

Definition at line 455 of file Phase.cpp.

References Phase::setDensity(), Phase::setMoleFractionsByName(), and Phase::setTemperature().

void setState_TRY ( doublereal  t,
doublereal  dens,
const doublereal *  y 
)
inherited

Set the internally stored temperature (K), density, and mass fractions.

Parameters
tTemperature in kelvin
densDensity (kg/m^3)
yvector of species mass fractions, length m_kk

Definition at line 462 of file Phase.cpp.

References Phase::setDensity(), Phase::setMassFractions(), and Phase::setTemperature().

void setState_TRY ( doublereal  t,
doublereal  dens,
compositionMap y 
)
inherited

Set the internally stored temperature (K), density, and mass fractions.

Parameters
tTemperature in kelvin
densDensity (kg/m^3)
yComposition Map containing the mass fractions. Species not included in the map are assumed to have a zero mass fraction.

Definition at line 469 of file Phase.cpp.

References Phase::setDensity(), Phase::setMassFractionsByName(), and Phase::setTemperature().

void setState_TNX ( doublereal  t,
doublereal  n,
const doublereal *  x 
)
inherited

Set the internally stored temperature (K), molar density (kmol/m^3), and mole fractions.

Parameters
tTemperature in kelvin
nmolar density (kmol/m^3)
xvector of species mole fractions, length m_kk

Definition at line 448 of file Phase.cpp.

References Phase::setMolarDensity(), Phase::setMoleFractions(), and Phase::setTemperature().

void setState_TR ( doublereal  t,
doublereal  rho 
)
inherited

Set the internally stored temperature (K) and density (kg/m^3)

Parameters
tTemperature in kelvin
rhoDensity (kg/m^3)

Definition at line 476 of file Phase.cpp.

References Phase::setDensity(), and Phase::setTemperature().

Referenced by PureFluidPhase::setState_HP(), PureFluidPhase::setState_SP(), PureFluidPhase::setState_SV(), PDSS_IonsFromNeutral::setState_TR(), and PureFluidPhase::setState_UV().

void setState_TX ( doublereal  t,
doublereal *  x 
)
inherited

Set the internally stored temperature (K) and mole fractions.

Parameters
tTemperature in kelvin
xvector of species mole fractions, length m_kk

Definition at line 482 of file Phase.cpp.

References Phase::setMoleFractions(), and Phase::setTemperature().

void setState_TY ( doublereal  t,
doublereal *  y 
)
inherited

Set the internally stored temperature (K) and mass fractions.

Parameters
tTemperature in kelvin
yvector of species mass fractions, length m_kk

Definition at line 488 of file Phase.cpp.

References Phase::setMassFractions(), and Phase::setTemperature().

void setState_RX ( doublereal  rho,
doublereal *  x 
)
inherited

Set the density (kg/m^3) and mole fractions.

Parameters
rhoDensity (kg/m^3)
xvector of species mole fractions, length m_kk

Definition at line 494 of file Phase.cpp.

References Phase::setDensity(), and Phase::setMoleFractions().

void setState_RY ( doublereal  rho,
doublereal *  y 
)
inherited

Set the density (kg/m^3) and mass fractions.

Parameters
rhoDensity (kg/m^3)
yvector of species mass fractions, length m_kk

Definition at line 500 of file Phase.cpp.

References Phase::setDensity(), and Phase::setMassFractions().

doublereal molecularWeight ( size_t  k) const
inherited
doublereal molarMass ( size_t  k) const
inlineinherited

Return the Molar mass of species k Alternate name for molecular weight.

@param k  index for species
@return   Return the molar mass of species k kg/kmol.
Deprecated:
use molecularWeight instead

Definition at line 388 of file Phase.h.

References Phase::molecularWeight().

void getMolecularWeights ( vector_fp weights) const
inherited

Copy the vector of molecular weights into vector weights.

Parameters
weightsOutput vector of molecular weights (kg/kmol)

Definition at line 512 of file Phase.cpp.

References Phase::molecularWeights().

void getMolecularWeights ( int  iwt,
doublereal *  weights 
) const
inherited

Copy the vector of molecular weights into array weights.

@param iwt      Unused.
@param weights  Output array of molecular weights (kg/kmol)
Deprecated:

Definition at line 521 of file Phase.cpp.

References Phase::molecularWeights().

void getMolecularWeights ( doublereal *  weights) const
inherited

Copy the vector of molecular weights into array weights.

Parameters
weightsOutput array of molecular weights (kg/kmol)

Definition at line 527 of file Phase.cpp.

References Phase::molecularWeights().

const vector_fp & molecularWeights ( ) const
inherited
doublereal size ( size_t  k) const
inlineinherited
void getMoleFractionsByName ( compositionMap x) const
inherited

Get the mole fractions by name.

Parameters
[out]xcomposition map containing the species mole fractions.

Definition at line 538 of file Phase.cpp.

References Phase::moleFraction(), Phase::nSpecies(), and Phase::speciesName().

doublereal moleFraction ( size_t  k) const
inherited

Return the mole fraction of a single species.

Parameters
kspecies index
Returns
Mole fraction of the species

Definition at line 552 of file Phase.cpp.

References Phase::checkSpeciesIndex(), Phase::m_mmw, and Phase::m_ym.

Referenced by Phase::chargeDensity(), SolidTransport::electricalConductivity(), ChemEquil::equilibrate(), IdealMolalSoln::getActivities(), DebyeHuckel::getActivities(), HMWSoln::getActivities(), MolalityVPSSTP::getActivityCoefficients(), IdealSolnGasVPSS::getActivityConcentrations(), RedlichKwongMFTP::getActivityConcentrations(), ConstDensityThermo::getChemPotentials(), IdealSolnGasVPSS::getChemPotentials(), RedlichKwongMFTP::getChemPotentials(), IdealSolidSolnPhase::getChemPotentials(), IdealMolalSoln::getChemPotentials(), IdealGasPhase::getChemPotentials(), LatticePhase::getChemPotentials(), DebyeHuckel::getChemPotentials(), HMWSoln::getChemPotentials(), IdealSolidSolnPhase::getChemPotentials_RT(), IdealMolalSoln::getMolalityActivityCoefficients(), Phase::getMoleFractionsByName(), IdealSolnGasVPSS::getPartialMolarEntropies(), RedlichKwongMFTP::getPartialMolarEntropies(), IdealGasPhase::getPartialMolarEntropies(), IdealMolalSoln::getPartialMolarEntropies(), IdealSolidSolnPhase::getPartialMolarEntropies(), LatticePhase::getPartialMolarEntropies(), DebyeHuckel::getPartialMolarEntropies(), HMWSoln::getPartialMolarEntropies(), Phase::moleFraction(), DebyeHuckel::s_update_d2lnMolalityActCoeff_dT2(), DebyeHuckel::s_update_dlnMolalityActCoeff_dP(), DebyeHuckel::s_update_dlnMolalityActCoeff_dT(), DebyeHuckel::s_update_lnMolalityActCoeff(), HMWSoln::s_update_lnMolalityActCoeff(), IdealMolalSoln::s_updateIMS_lnMolalityActCoeff(), HMWSoln::s_updateIMS_lnMolalityActCoeff(), HMWSoln::s_updatePitzer_lnMolalityActCoeff(), and ChemEquil::setInitialMoles().

doublereal moleFraction ( std::string  name) const
inherited

Return the mole fraction of a single species.

Parameters
nameString name of the species
Returns
Mole fraction of the species

Definition at line 558 of file Phase.cpp.

References Phase::moleFraction(), Cantera::npos, and Phase::speciesIndex().

doublereal massFraction ( size_t  k) const
inherited

Return the mass fraction of a single species.

Parameters
kspecies index
Returns
Mass fraction of the species

Definition at line 573 of file Phase.cpp.

References Phase::checkSpeciesIndex(), and Phase::m_y.

doublereal massFraction ( std::string  name) const
inherited

Return the mass fraction of a single species.

Parameters
nameString name of the species
Returns
Mass Fraction of the species

Definition at line 579 of file Phase.cpp.

References Phase::massFractions(), Cantera::npos, and Phase::speciesIndex().

void getMoleFractions ( doublereal *const  x) const
inherited

Get the species mole fraction vector.

Parameters
xOn return, x contains the mole fractions. Must have a length greater than or equal to the number of species.

Definition at line 547 of file Phase.cpp.

References Phase::m_mmw, Phase::m_ym, and Cantera::scale().

Referenced by IdealMolalSoln::calcDensity(), DebyeHuckel::calcDensity(), HMWSoln::calcDensity(), IonsFromNeutralVPSSTP::calcIonMoleFractions(), MolalityVPSSTP::calcMolalities(), HMWSoln::calcMolalitiesCropped(), IdealMolalSoln::enthalpy_mole(), HMWSoln::enthalpy_mole(), ChemEquil::estimateElementPotentials(), ChemEquil::estimateEP_Brinkley(), GibbsExcessVPSSTP::getActivities(), LatticePhase::getActivityConcentrations(), MultiTransport::getMassFluxes(), LTI_Pairwise_Interaction::getMatrixTransProp(), LTI_StefanMaxwell_PPN::getMatrixTransProp(), LTI_MoleFracs::getMixTransProp(), LTI_Log_MoleFracs::getMixTransProp(), LTI_Pairwise_Interaction::getMixTransProp(), LTI_StefanMaxwell_PPN::getMixTransProp(), LTI_MoleFracs_ExpT::getMixTransProp(), LatticeSolidPhase::getMoleFractions(), DustyGasTransport::initialize(), GibbsExcessVPSSTP::initThermo(), HMWSoln::printCoeffs(), HMWSoln::relative_molal_enthalpy(), PseudoBinaryVPSSTP::report(), MolarityIonicVPSSTP::report(), PureFluidPhase::report(), MolalityVPSSTP::report(), ThermoPhase::report(), PureFluidPhase::reportCSV(), MolalityVPSSTP::reportCSV(), ThermoPhase::reportCSV(), MixtureFugacityTP::setConcentrations(), GibbsExcessVPSSTP::setConcentrations(), MixtureFugacityTP::setMassFractions(), GibbsExcessVPSSTP::setMassFractions(), MixtureFugacityTP::setMassFractions_NoNorm(), GibbsExcessVPSSTP::setMassFractions_NoNorm(), MolalityVPSSTP::setMolalitiesByName(), MixtureFugacityTP::setMoleFractions(), GibbsExcessVPSSTP::setMoleFractions(), MixtureFugacityTP::setMoleFractions_NoNorm(), GibbsExcessVPSSTP::setMoleFractions_NoNorm(), MultiPhase::setMoles(), vcs_VolPhase::setPtrThermoPhase(), ThermoPhase::setReferenceComposition(), MixtureFugacityTP::setState_TP(), MixtureFugacityTP::setState_TR(), AqueousTransport::stefan_maxwell_solve(), ChemEquil::update(), MixTransport::update_C(), MultiTransport::update_C(), AqueousTransport::update_C(), SimpleTransport::update_C(), LiquidTransport::update_C(), solveSP::updateMFKinSpecies(), DustyGasTransport::updateTransport_C(), and MultiPhase::uploadMoleFractionsFromPhases().

void setMoleFractions ( const doublereal *const  x)
virtualinherited

Set the mole fractions to the specified values There is no restriction on the sum of the mole fraction vector.

Internally, the Phase object will normalize this vector before storing its contents.

Parameters
xArray of unnormalized mole fraction values (input). Must have a length greater than or equal to the number of species, m_kk.

Reimplemented in IonsFromNeutralVPSSTP, GibbsExcessVPSSTP, LatticePhase, MixtureFugacityTP, IdealSolidSolnPhase, LatticeSolidPhase, and RedlichKwongMFTP.

Definition at line 317 of file Phase.cpp.

References Phase::m_kk, Phase::m_mmw, Phase::m_molwts, Phase::m_y, Phase::m_ym, ckr::max(), and Phase::stateMFChangeCalc().

Referenced by ChemEquil::calcEmoles(), ChemEquil::equilibrate(), ChemEquil::estimateElementPotentials(), ChemEquil::estimateEP_Brinkley(), PureFluidPhase::initThermo(), SingleSpeciesTP::initThermo(), WaterSSTP::initThermoXML(), IonsFromNeutralVPSSTP::setConcentrations(), IonsFromNeutralVPSSTP::setMassFractions(), IonsFromNeutralVPSSTP::setMassFractions_NoNorm(), MolalityVPSSTP::setMolalities(), MolalityVPSSTP::setMolalitiesByName(), Inlet1D::setMoleFractions(), OutletRes1D::setMoleFractions(), LatticeSolidPhase::setMoleFractions(), IdealSolidSolnPhase::setMoleFractions(), MixtureFugacityTP::setMoleFractions(), LatticePhase::setMoleFractions(), GibbsExcessVPSSTP::setMoleFractions(), IonsFromNeutralVPSSTP::setMoleFractions(), IdealSolidSolnPhase::setMoleFractions_NoNorm(), LatticePhase::setMoleFractions_NoNorm(), Phase::setMoleFractionsByName(), ThermoPhase::setState_PX(), Phase::setState_RX(), Phase::setState_TNX(), ThermoPhase::setState_TPX(), Phase::setState_TRX(), and Phase::setState_TX().

void setMoleFractions_NoNorm ( const doublereal *const  x)
virtualinherited

Set the mole fractions to the specified values without normalizing.

This is useful when the normalization condition is being handled by some other means, for example by a constraint equation as part of a larger set of equations.

Parameters
xInput vector of mole fractions. Length is m_kk.

Reimplemented in IonsFromNeutralVPSSTP, GibbsExcessVPSSTP, LatticePhase, MixtureFugacityTP, IdealSolidSolnPhase, and RedlichKwongMFTP.

Definition at line 350 of file Phase.cpp.

References Cantera::dot(), Phase::m_kk, Phase::m_mmw, Phase::m_molwts, Phase::m_y, Phase::m_ym, and Phase::stateMFChangeCalc().

Referenced by MixtureFugacityTP::setMoleFractions_NoNorm(), GibbsExcessVPSSTP::setMoleFractions_NoNorm(), and IonsFromNeutralVPSSTP::setMoleFractions_NoNorm().

void getMassFractions ( doublereal *const  y) const
inherited
const doublereal* massFractions ( ) const
inlineinherited
void setMassFractions ( const doublereal *const  y)
virtualinherited
void setMassFractions_NoNorm ( const doublereal *const  y)
virtualinherited

Set the mass fractions to the specified values without normalizing.

This is useful when the normalization condition is being handled by some other means, for example by a constraint equation as part of a larger set of equations.

Parameters
yInput vector of mass fractions. Length is m_kk.

Reimplemented in IonsFromNeutralVPSSTP, LatticePhase, GibbsExcessVPSSTP, MixtureFugacityTP, LatticeSolidPhase, IdealSolidSolnPhase, and RedlichKwongMFTP.

Definition at line 403 of file Phase.cpp.

References Phase::m_kk, Phase::m_mmw, Phase::m_rmolwts, Phase::m_y, Phase::m_ym, and Phase::stateMFChangeCalc().

Referenced by Phase::restoreState(), StFlow::setGas(), StFlow::setGasAtMidpoint(), IdealSolidSolnPhase::setMassFractions_NoNorm(), MixtureFugacityTP::setMassFractions_NoNorm(), GibbsExcessVPSSTP::setMassFractions_NoNorm(), and LatticePhase::setMassFractions_NoNorm().

void getConcentrations ( doublereal *const  c) const
inherited

Get the species concentrations (kmol/m^3).

@param[out] c Array of species concentrations Length must be

greater than or equal to the number of species.

Definition at line 600 of file Phase.cpp.

References Phase::m_dens, Phase::m_ym, and Cantera::scale().

Referenced by ConstDensityThermo::getActivityConcentrations(), IdealSolnGasVPSS::getActivityConcentrations(), SurfPhase::getActivityConcentrations(), IdealGasPhase::getActivityConcentrations(), SurfPhase::getCoverages(), solveSP::solveSurfProb(), SimpleTransport::update_C(), and LiquidTransport::update_C().

doublereal concentration ( const size_t  k) const
inherited

Concentration of species k.

If k is outside the valid range, an exception will be thrown.

Parameters
kIndex of species

Definition at line 594 of file Phase.cpp.

References Phase::checkSpeciesIndex(), Phase::m_dens, Phase::m_rmolwts, and Phase::m_y.

void setConcentrations ( const doublereal *const  conc)
virtualinherited

Set the concentrations to the specified values within the phase.

We set the concentrations here and therefore we set the overall density of the phase. We hold the temperature constant during this operation. Therefore, we have possibly changed the pressure of the phase by calling this routine.

Parameters
[in]concArray of concentrations in dimensional units. For bulk phases c[k] is the concentration of the kth species in kmol/m3. For surface phases, c[k] is the concentration in kmol/m2. The length of the vector is the numberof species in the phase.

Reimplemented in IonsFromNeutralVPSSTP, GibbsExcessVPSSTP, LatticePhase, MixtureFugacityTP, LatticeSolidPhase, IdealSolidSolnPhase, and RedlichKwongMFTP.

Definition at line 605 of file Phase.cpp.

References Phase::m_kk, Phase::m_mmw, Phase::m_molwts, Phase::m_y, Phase::m_ym, ckr::max(), Phase::setDensity(), and Phase::stateMFChangeCalc().

Referenced by IdealSolidSolnPhase::setConcentrations(), MixtureFugacityTP::setConcentrations(), LatticePhase::setConcentrations(), GibbsExcessVPSSTP::setConcentrations(), ImplicitSurfChem::setConcSpecies(), SurfPhase::setCoverages(), and SurfPhase::setCoveragesNoNorm().

const doublereal * moleFractdivMMW ( ) const
inherited

Returns a const pointer to the start of the moleFraction/MW array.

This array is the array of mole fractions, each divided by the mean molecular weight.

Definition at line 568 of file Phase.cpp.

References Phase::m_ym.

Referenced by IdealSolnGasVPSS::calcDensity(), RedlichKwongMFTP::calcDensity(), IdealSolidSolnPhase::calcDensity(), and IdealSolidSolnPhase::getActivityConcentrations().

doublereal charge ( size_t  k) const
inherited

Dimensionless electrical charge of a single molecule of species k The charge is normalized by the the magnitude of the electron charge.

Parameters
kspecies index

Definition at line 642 of file Phase.cpp.

References Phase::m_speciesCharge.

Referenced by InterfaceKinetics::applyButlerVolmerCorrection(), HMWSoln::calcMolalitiesCropped(), Phase::chargeDensity(), PDSS_HKFT::constructPDSSXML(), SolidTransport::electricalConductivity(), PureFluidPhase::getElectrochemPotentials(), PseudoBinaryVPSSTP::getElectrochemPotentials(), MolarityIonicVPSSTP::getElectrochemPotentials(), GibbsExcessVPSSTP::getElectrochemPotentials(), RedlichKisterVPSSTP::getElectrochemPotentials(), MargulesVPSSTP::getElectrochemPotentials(), ThermoPhase::getElectrochemPotentials(), MixedSolventElectrolyte::getElectrochemPotentials(), MolalityVPSSTP::getElectrochemPotentials(), PhaseCombo_Interaction::getElectrochemPotentials(), InterfaceKinetics::getEquilibriumConstants(), LiquidTransport::initLiquid(), SimpleTransport::initLiquid(), PDSS_HKFT::initThermo(), IonsFromNeutralVPSSTP::initThermoXML(), DebyeHuckel::initThermoXML(), LatticeSolidPhase::installSlavePhases(), HMWSoln::printCoeffs(), PhaseCombo_Interaction::readXMLBinarySpecies(), RedlichKisterVPSSTP::readXMLBinarySpecies(), MargulesVPSSTP::readXMLBinarySpecies(), MixedSolventElectrolyte::readXMLBinarySpecies(), HMWSoln::relative_molal_enthalpy(), HMWSoln::s_updatePitzer_d2lnMolalityActCoeff_dT2(), HMWSoln::s_updatePitzer_dlnMolalityActCoeff_dP(), HMWSoln::s_updatePitzer_dlnMolalityActCoeff_dT(), HMWSoln::s_updatePitzer_lnMolalityActCoeff(), MolalityVPSSTP::setMolalitiesByName(), vcs_VolPhase::transferElementsFM(), and InterfaceKinetics::updateKc().

doublereal chargeDensity ( ) const
inherited

Charge density [C/m^3].

Definition at line 647 of file Phase.cpp.

References Phase::charge(), Phase::moleFraction(), and Phase::nSpecies().

size_t nDim ( ) const
inlineinherited
void setNDim ( size_t  ndim)
inlineinherited

Set the number of spatial dimensions (1, 2, or 3).

The number of spatial dimensions is used for vector involving directions.

Parameters
ndimInput number of dimensions.

Definition at line 530 of file Phase.h.

References Phase::m_ndim.

Referenced by EdgePhase::EdgePhase(), FixedChemPotSSTP::FixedChemPotSSTP(), Cantera::importPhase(), EdgePhase::operator=(), and SurfPhase::SurfPhase().

doublereal temperature ( ) const
inlineinherited

Temperature (K).

Returns
The temperature of the phase

Definition at line 539 of file Phase.h.

References Phase::m_temp.

Referenced by ThermoPhase::_RT(), InterfaceKinetics::_update_rates_T(), MixtureFugacityTP::_updateReferenceStateThermo(), VPStandardStateTP::_updateStandardStateThermo(), ConstDensityThermo::_updateThermo(), SurfPhase::_updateThermo(), LatticeSolidPhase::_updateThermo(), SingleSpeciesTP::_updateThermo(), IdealGasPhase::_updateThermo(), LatticePhase::_updateThermo(), IdealSolidSolnPhase::_updateThermo(), DebyeHuckel::A_Debye_TP(), HMWSoln::A_Debye_TP(), MultiPhase::addPhase(), HMWSoln::ADebye_J(), HMWSoln::ADebye_L(), HMWSoln::ADebye_V(), InterfaceKinetics::applyButlerVolmerCorrection(), InterfaceKinetics::applyExchangeCurrentDensityFormulation(), IdealSolnGasVPSS::calcDensity(), MixtureFugacityTP::calculatePsat(), RedlichKwongMFTP::cp_mole(), SingleSpeciesTP::cv_mole(), HMWSoln::cv_mole(), DebyeHuckel::d2A_DebyedT2_TP(), HMWSoln::d2A_DebyedT2_TP(), DebyeHuckel::dA_DebyedP_TP(), HMWSoln::dA_DebyedP_TP(), DebyeHuckel::dA_DebyedT_TP(), HMWSoln::dA_DebyedT_TP(), WaterSSTP::dthermalExpansionCoeffdT(), IdealSolnGasVPSS::enthalpy_mole(), ConstDensityThermo::enthalpy_mole(), IdealSolidSolnPhase::enthalpy_mole(), LatticePhase::enthalpy_mole(), IdealGasPhase::enthalpy_mole(), ChemEquil::equilibrate(), ChemEquil::estimateElementPotentials(), ChemEquil::estimateEP_Brinkley(), FixedChemPotSSTP::FixedChemPotSSTP(), RedlichKwongMFTP::getActivityCoefficients(), ConstDensityThermo::getChemPotentials(), SurfPhase::getChemPotentials(), MolarityIonicVPSSTP::getChemPotentials(), IdealSolnGasVPSS::getChemPotentials(), IonsFromNeutralVPSSTP::getChemPotentials(), RedlichKwongMFTP::getChemPotentials(), RedlichKisterVPSSTP::getChemPotentials(), MargulesVPSSTP::getChemPotentials(), MixedSolventElectrolyte::getChemPotentials(), PhaseCombo_Interaction::getChemPotentials(), IdealSolidSolnPhase::getChemPotentials(), IdealMolalSoln::getChemPotentials(), IdealGasPhase::getChemPotentials(), LatticePhase::getChemPotentials(), DebyeHuckel::getChemPotentials(), HMWSoln::getChemPotentials(), StoichSubstance::getChemPotentials_RT(), SingleSpeciesTP::getChemPotentials_RT(), IdealSolidSolnPhase::getChemPotentials_RT(), WaterSSTP::getCp_R_ref(), AqueousKinetics::getDeltaSSEnthalpy(), GasKinetics::getDeltaSSEnthalpy(), InterfaceKinetics::getDeltaSSEnthalpy(), PhaseCombo_Interaction::getdlnActCoeffds(), MargulesVPSSTP::getdlnActCoeffds(), MixedSolventElectrolyte::getdlnActCoeffds(), ThermoPhase::getElementPotentials(), WaterSSTP::getEnthalpy_RT(), StoichSubstance::getEnthalpy_RT(), StoichSubstanceSSTP::getEnthalpy_RT(), MineralEQ3::getEnthalpy_RT(), SurfPhase::getEnthalpy_RT(), IdealSolidSolnPhase::getEnthalpy_RT(), LatticePhase::getEnthalpy_RT(), WaterSSTP::getEnthalpy_RT_ref(), PureFluidPhase::getEnthalpy_RT_ref(), WaterSSTP::getEntropy_R_ref(), PureFluidPhase::getEntropy_R_ref(), AqueousKinetics::getEquilibriumConstants(), GasKinetics::getEquilibriumConstants(), InterfaceKinetics::getEquilibriumConstants(), StoichSubstance::getGibbs_ref(), PureFluidPhase::getGibbs_ref(), SingleSpeciesTP::getGibbs_ref(), LatticeSolidPhase::getGibbs_ref(), IdealSolidSolnPhase::getGibbs_ref(), LatticePhase::getGibbs_ref(), WaterSSTP::getGibbs_RT(), StoichSubstance::getGibbs_RT(), SurfPhase::getGibbs_RT(), WaterSSTP::getGibbs_RT_ref(), PureFluidPhase::getGibbs_RT_ref(), StoichSubstanceSSTP::getIntEnergy_RT(), MineralEQ3::getIntEnergy_RT(), IdealSolidSolnPhase::getIntEnergy_RT(), StoichSubstanceSSTP::getIntEnergy_RT_ref(), MineralEQ3::getIntEnergy_RT_ref(), MetalSHEelectrons::getIntEnergy_RT_ref(), IdealSolidSolnPhase::getIntEnergy_RT_ref(), LTI_Pairwise_Interaction::getMatrixTransProp(), LTI_StefanMaxwell_PPN::getMatrixTransProp(), SolidTransport::getMixDiffCoeffs(), LTI_MoleFracs::getMixTransProp(), LTI_MassFracs::getMixTransProp(), LTI_Log_MoleFracs::getMixTransProp(), LTI_MoleFracs_ExpT::getMixTransProp(), SolidTransport::getMobilities(), MolarityIonicVPSSTP::getPartialMolarCp(), RedlichKisterVPSSTP::getPartialMolarCp(), MargulesVPSSTP::getPartialMolarCp(), MixedSolventElectrolyte::getPartialMolarCp(), PhaseCombo_Interaction::getPartialMolarCp(), DebyeHuckel::getPartialMolarCp(), HMWSoln::getPartialMolarCp(), SurfPhase::getPartialMolarEnthalpies(), IdealSolnGasVPSS::getPartialMolarEnthalpies(), MolarityIonicVPSSTP::getPartialMolarEnthalpies(), SingleSpeciesTP::getPartialMolarEnthalpies(), IonsFromNeutralVPSSTP::getPartialMolarEnthalpies(), RedlichKwongMFTP::getPartialMolarEnthalpies(), RedlichKisterVPSSTP::getPartialMolarEnthalpies(), MargulesVPSSTP::getPartialMolarEnthalpies(), MixedSolventElectrolyte::getPartialMolarEnthalpies(), PhaseCombo_Interaction::getPartialMolarEnthalpies(), IdealGasPhase::getPartialMolarEnthalpies(), IdealSolidSolnPhase::getPartialMolarEnthalpies(), LatticePhase::getPartialMolarEnthalpies(), DebyeHuckel::getPartialMolarEnthalpies(), HMWSoln::getPartialMolarEnthalpies(), MolarityIonicVPSSTP::getPartialMolarEntropies(), IonsFromNeutralVPSSTP::getPartialMolarEntropies(), RedlichKwongMFTP::getPartialMolarEntropies(), RedlichKisterVPSSTP::getPartialMolarEntropies(), MargulesVPSSTP::getPartialMolarEntropies(), MixedSolventElectrolyte::getPartialMolarEntropies(), PhaseCombo_Interaction::getPartialMolarEntropies(), DebyeHuckel::getPartialMolarEntropies(), HMWSoln::getPartialMolarEntropies(), IdealSolnGasVPSS::getPartialMolarIntEnergies(), SingleSpeciesTP::getPartialMolarIntEnergies(), RedlichKwongMFTP::getPartialMolarIntEnergies(), IdealGasPhase::getPartialMolarIntEnergies(), RedlichKwongMFTP::getPartialMolarVolumes(), MargulesVPSSTP::getPartialMolarVolumes(), MixedSolventElectrolyte::getPartialMolarVolumes(), PhaseCombo_Interaction::getPartialMolarVolumes(), DebyeHuckel::getPartialMolarVolumes(), HMWSoln::getPartialMolarVolumes(), SingleSpeciesTP::getPureGibbs(), LatticePhase::getPureGibbs(), LTPspecies_Arrhenius::getSpeciesTransProp(), LTPspecies_Poly::getSpeciesTransProp(), LTPspecies_ExpT::getSpeciesTransProp(), WaterSSTP::getStandardChemPotentials(), StoichSubstanceSSTP::getStandardChemPotentials(), MineralEQ3::getStandardChemPotentials(), MetalSHEelectrons::getStandardChemPotentials(), IdealGasPhase::getStandardChemPotentials(), WaterSSTP::getStandardVolumes_ref(), IdealSolnGasVPSS::gibbs_mole(), ConstDensityThermo::gibbs_mole(), StoichSubstance::gibbs_mole(), RedlichKwongMFTP::gibbs_mole(), IdealSolidSolnPhase::gibbs_mole(), ThermoPhase::gibbs_mole(), LatticePhase::gibbs_mole(), IdealGasPhase::gibbs_mole(), RedlichKwongMFTP::hresid(), ConstDensityThermo::intEnergy_mole(), StoichSubstance::intEnergy_mole(), IdealSolidSolnPhase::intEnergy_mole(), LatticePhase::intEnergy_mole(), IdealGasPhase::intEnergy_mole(), IdealGasPhase::logStandardConc(), MixtureFugacityTP::phaseState(), RedlichKwongMFTP::pressure(), IdealGasPhase::pressure(), MixTransport::pressure_ig(), RedlichKwongMFTP::pressureDerivatives(), HMWSoln::relative_enthalpy(), PseudoBinaryVPSSTP::report(), MolarityIonicVPSSTP::report(), PureFluidPhase::report(), MolalityVPSSTP::report(), ThermoPhase::report(), PureFluidPhase::reportCSV(), MolalityVPSSTP::reportCSV(), ThermoPhase::reportCSV(), PhaseCombo_Interaction::s_update_dlnActCoeff_dlnN(), MargulesVPSSTP::s_update_dlnActCoeff_dlnN(), MixedSolventElectrolyte::s_update_dlnActCoeff_dlnN(), PhaseCombo_Interaction::s_update_dlnActCoeff_dlnN_diag(), MargulesVPSSTP::s_update_dlnActCoeff_dlnN_diag(), MixedSolventElectrolyte::s_update_dlnActCoeff_dlnN_diag(), PhaseCombo_Interaction::s_update_dlnActCoeff_dlnX_diag(), MargulesVPSSTP::s_update_dlnActCoeff_dlnX_diag(), MixedSolventElectrolyte::s_update_dlnActCoeff_dlnX_diag(), PhaseCombo_Interaction::s_update_dlnActCoeff_dT(), MargulesVPSSTP::s_update_dlnActCoeff_dT(), MixedSolventElectrolyte::s_update_dlnActCoeff_dT(), RedlichKisterVPSSTP::s_update_dlnActCoeff_dX_(), PhaseCombo_Interaction::s_update_lnActCoeff(), RedlichKisterVPSSTP::s_update_lnActCoeff(), MargulesVPSSTP::s_update_lnActCoeff(), MixedSolventElectrolyte::s_update_lnActCoeff(), HMWSoln::s_updatePitzer_CoeffWRTemp(), HMWSoln::s_updatePitzer_dlnMolalityActCoeff_dP(), HMWSoln::s_updatePitzer_lnMolalityActCoeff(), WaterSSTP::satPressure(), HMWSoln::satPressure(), Phase::saveState(), WaterSSTP::setDensity(), ThermoPhase::setElementPotentials(), ChemEquil::setInitialMoles(), PureFluidPhase::setPressure(), WaterSSTP::setPressure(), GibbsExcessVPSSTP::setPressure(), IdealMolalSoln::setPressure(), VPStandardStateTP::setPressure(), MixtureFugacityTP::setPressure(), IdealGasPhase::setPressure(), IonsFromNeutralVPSSTP::setPressure(), DebyeHuckel::setPressure(), HMWSoln::setPressure(), vcs_VolPhase::setPtrThermoPhase(), SingleSpeciesTP::setState_HP(), ThermoPhase::setState_HPorUV(), SingleSpeciesTP::setState_SP(), ThermoPhase::setState_SPorSV(), SingleSpeciesTP::setState_SV(), SingleSpeciesTP::setState_UV(), MixtureFugacityTP::setStateFromXML(), MixtureFugacityTP::setTemperature(), PureFluidPhase::setTPXState(), ImplicitSurfChem::solvePseudoSteadyStateProblem(), RedlichKwongMFTP::sresid(), IdealSolnGasVPSS::standardConcentration(), IdealGasPhase::standardConcentration(), AqueousTransport::stefan_maxwell_solve(), LiquidTransport::stefan_maxwell_solve(), SolidTransport::thermalConductivity(), MetalSHEelectrons::thermalExpansionCoeff(), IdealGasPhase::thermalExpansionCoeff(), ChemEquil::update(), MixTransport::update_T(), MultiTransport::update_T(), AqueousTransport::update_T(), SimpleTransport::update_T(), LiquidTransport::update_T(), RedlichKwongMFTP::updateAB(), AqueousKinetics::updateKc(), GasKinetics::updateKc(), InterfaceKinetics::updateKc(), VPStandardStateTP::updateStandardStateThermo(), Reactor::updateState(), MultiTransport::updateThermal_T(), DustyGasTransport::updateTransport_T(), and WaterSSTP::vaporFraction().

virtual doublereal density ( ) const
inlinevirtualinherited

Density (kg/m^3).

Returns
The density of the phase

Reimplemented in HMWSoln.

Definition at line 545 of file Phase.h.

References Phase::m_dens.

Referenced by MixtureFugacityTP::calculatePsat(), SingleSpeciesTP::cv_mole(), HMWSoln::density(), WaterSSTP::dthermalExpansionCoeffdT(), WaterSSTP::getCp_R_ref(), WaterSSTP::getEnthalpy_RT_ref(), WaterSSTP::getEntropy_R_ref(), WaterSSTP::getGibbs_RT_ref(), MultiTransport::getMassFluxes(), ConstDensityThermo::getParameters(), StoichSubstance::getParameters(), StoichSubstanceSSTP::getParameters(), MetalSHEelectrons::getParameters(), MineralEQ3::getParameters(), SingleSpeciesTP::getPartialMolarVolumes(), MultiTransport::getSpeciesFluxes(), SimpleTransport::getSpeciesVdiff(), SimpleTransport::getSpeciesVdiffES(), SingleSpeciesTP::getStandardVolumes(), WaterSSTP::getStandardVolumes_ref(), RedlichKwongMFTP::hresid(), Phase::molarDensity(), MixtureFugacityTP::phaseState(), RedlichKwongMFTP::pressure(), PseudoBinaryVPSSTP::report(), MolarityIonicVPSSTP::report(), PureFluidPhase::report(), MolalityVPSSTP::report(), ThermoPhase::report(), PureFluidPhase::reportCSV(), MolalityVPSSTP::reportCSV(), ThermoPhase::reportCSV(), WaterSSTP::satPressure(), Phase::saveState(), IdealMolalSoln::setDensity(), IdealSolidSolnPhase::setDensity(), Phase::setDensity(), DebyeHuckel::setDensity(), WaterSSTP::setPressure(), MixtureFugacityTP::setState_TP(), IonsFromNeutralVPSSTP::setState_TP(), MixtureFugacityTP::setStateFromXML(), MixtureFugacityTP::setTemperature(), WaterSSTP::setTemperature(), PureFluidPhase::setTPXState(), RedlichKwongMFTP::sresid(), ChemEquil::update(), SimpleTransport::update_C(), LiquidTransport::update_C(), ConstPressureReactor::updateState(), StFlow::updateThermo(), WaterSSTP::vaporFraction(), and MixtureFugacityTP::z().

doublereal molarDensity ( ) const
inherited

Molar density (kmol/m^3).

Returns
The molar density of the phase

Definition at line 627 of file Phase.cpp.

References Phase::density(), and Phase::meanMolecularWeight().

Referenced by solveSP::calc_t(), SolidTransport::electricalConductivity(), ConstDensityThermo::enthalpy_mole(), StoichSubstance::enthalpy_mole(), IdealSolidSolnPhase::enthalpy_mole(), LatticePhase::enthalpy_mole(), ConstDensityThermo::getChemPotentials(), StoichSubstanceSSTP::getEnthalpy_RT(), MineralEQ3::getEnthalpy_RT(), StoichSubstanceSSTP::getIntEnergy_RT(), MineralEQ3::getIntEnergy_RT(), StoichSubstanceSSTP::getIntEnergy_RT_ref(), MineralEQ3::getIntEnergy_RT_ref(), MetalSHEelectrons::getIntEnergy_RT_ref(), LatticePhase::getParameters(), PureFluidPhase::getPartialMolarVolumes(), StoichSubstance::getPartialMolarVolumes(), IdealGasPhase::getPartialMolarVolumes(), MixTransport::getSpeciesFluxes(), AqueousTransport::getSpeciesFluxesExt(), SimpleTransport::getSpeciesFluxesExt(), StoichSubstance::getStandardVolumes(), IdealGasPhase::getStandardVolumes(), IdealSolnGasVPSS::intEnergy_mole(), ConstDensityThermo::intEnergy_mole(), StoichSubstance::intEnergy_mole(), RedlichKwongMFTP::intEnergy_mole(), IonsFromNeutralVPSSTP::intEnergy_mole(), IdealSolidSolnPhase::intEnergy_mole(), LatticePhase::intEnergy_mole(), DebyeHuckel::intEnergy_mole(), HMWSoln::intEnergy_mole(), ConstDensityThermo::logStandardConc(), Phase::molarVolume(), IdealGasPhase::pressure(), MixTransport::pressure_ig(), IdealMolalSoln::setMolarDensity(), DebyeHuckel::setMolarDensity(), and ConstDensityThermo::standardConcentration().

doublereal molarVolume ( ) const
inherited
virtual void setDensity ( const doublereal  density)
inlinevirtualinherited

Set the internally stored density (kg/m^3) of the phase Note the density of a phase is an independent variable.

Parameters
[in]densitydensity (kg/m^3).

Reimplemented in HMWSoln, DebyeHuckel, WaterSSTP, IdealSolidSolnPhase, and IdealMolalSoln.

Definition at line 560 of file Phase.h.

References Phase::density(), and Phase::m_dens.

Referenced by IdealSolnGasVPSS::calcDensity(), RedlichKwongMFTP::calcDensity(), GibbsExcessVPSSTP::calcDensity(), IdealMolalSoln::calcDensity(), IdealSolidSolnPhase::calcDensity(), LatticeSolidPhase::calcDensity(), DebyeHuckel::calcDensity(), HMWSoln::calcDensity(), StoichSubstanceSSTP::initThermoXML(), WaterSSTP::initThermoXML(), MetalSHEelectrons::initThermoXML(), MineralEQ3::initThermoXML(), electrodeElectron::initThermoXML(), Phase::restoreState(), Phase::setConcentrations(), WaterSSTP::setDensity(), ConstDensityThermo::setParameters(), StoichSubstance::setParameters(), StoichSubstanceSSTP::setParameters(), MetalSHEelectrons::setParameters(), MineralEQ3::setParameters(), electrodeElectron::setParameters(), SemiconductorPhase::setParametersFromXML(), MetalPhase::setParametersFromXML(), StoichSubstance::setParametersFromXML(), ConstDensityThermo::setParametersFromXML(), StoichSubstanceSSTP::setParametersFromXML(), MetalSHEelectrons::setParametersFromXML(), PureFluidPhase::setPressure(), IdealGasPhase::setPressure(), ThermoPhase::setState_HPorUV(), PureFluidPhase::setState_Psat(), Phase::setState_RX(), Phase::setState_RY(), ThermoPhase::setState_SPorSV(), SingleSpeciesTP::setState_SV(), MixtureFugacityTP::setState_TP(), IonsFromNeutralVPSSTP::setState_TP(), Phase::setState_TR(), MixtureFugacityTP::setState_TR(), Phase::setState_TRX(), Phase::setState_TRY(), PureFluidPhase::setState_Tsat(), SingleSpeciesTP::setState_UV(), ThermoPhase::setStateFromXML(), and Reactor::updateState().

void setMolarDensity ( const doublereal  molarDensity)
virtualinherited

Set the internally stored molar density (kmol/m^3) of the phase.

Parameters
[in]molarDensityInput molar density (kmol/m^3).

Reimplemented in HMWSoln, DebyeHuckel, IdealSolidSolnPhase, and IdealMolalSoln.

Definition at line 632 of file Phase.cpp.

References Phase::m_dens, and Phase::meanMolecularWeight().

Referenced by LatticePhase::calcDensity(), LatticePhase::setParameters(), and Phase::setState_TNX().

virtual void setTemperature ( const doublereal  temp)
inlinevirtualinherited
doublereal mean_X ( const doublereal *const  Q) const
inherited

Evaluate the mole-fraction-weighted mean of an array Q.

\[ \sum_k X_k Q_k. \]

Q should contain pure-species molar property values.

Parameters
[in]QArray of length m_kk that is to be averaged.
Returns
mole-fraction-weighted mean of Q

Definition at line 658 of file Phase.cpp.

References Phase::m_mmw, and Phase::m_ym.

Referenced by IdealSolnGasVPSS::cp_mole(), ConstDensityThermo::cp_mole(), RedlichKwongMFTP::cp_mole(), IonsFromNeutralVPSSTP::cp_mole(), IdealSolidSolnPhase::cp_mole(), IdealMolalSoln::cp_mole(), LatticePhase::cp_mole(), IdealGasPhase::cp_mole(), DebyeHuckel::cp_mole(), HMWSoln::cp_mole(), IonsFromNeutralVPSSTP::cv_mole(), IdealSolnGasVPSS::enthalpy_mole(), ConstDensityThermo::enthalpy_mole(), RedlichKwongMFTP::enthalpy_mole(), IdealSolidSolnPhase::enthalpy_mole(), IonsFromNeutralVPSSTP::enthalpy_mole(), IdealMolalSoln::enthalpy_mole(), SurfPhase::enthalpy_mole(), LatticePhase::enthalpy_mole(), IdealGasPhase::enthalpy_mole(), DebyeHuckel::enthalpy_mole(), HMWSoln::enthalpy_mole(), IdealSolnGasVPSS::entropy_mole(), ConstDensityThermo::entropy_mole(), RedlichKwongMFTP::entropy_mole(), IonsFromNeutralVPSSTP::entropy_mole(), IdealSolidSolnPhase::entropy_mole(), IdealMolalSoln::entropy_mole(), LatticePhase::entropy_mole(), IdealGasPhase::entropy_mole(), DebyeHuckel::entropy_mole(), HMWSoln::entropy_mole(), IonsFromNeutralVPSSTP::gibbs_mole(), IdealSolidSolnPhase::gibbs_mole(), IdealMolalSoln::gibbs_mole(), DebyeHuckel::gibbs_mole(), HMWSoln::gibbs_mole(), ConstDensityThermo::intEnergy_mole(), IdealSolidSolnPhase::intEnergy_mole(), IdealMolalSoln::intEnergy_mole(), LatticePhase::intEnergy_mole(), IdealGasPhase::intEnergy_mole(), and HMWSoln::relative_enthalpy().

doublereal mean_Y ( const doublereal *const  Q) const
inherited

Evaluate the mass-fraction-weighted mean of an array Q.

\[ \sum_k Y_k Q_k \]

Parameters
[in]QArray of species property values in mass units.
Returns
The mass-fraction-weighted mean of Q.

Definition at line 663 of file Phase.cpp.

References Cantera::dot(), and Phase::m_y.

doublereal meanMolecularWeight ( ) const
inlineinherited
doublereal sum_xlogx ( ) const
inherited
doublereal sum_xlogQ ( doublereal *const  Q) const
inherited

Evaluate \( \sum_k X_k \log Q_k \).

Parameters
QVector of length m_kk to take the log average of
Returns
The indicated sum.

Definition at line 673 of file Phase.cpp.

References Phase::m_mmw, Phase::m_ym, and Cantera::sum_xlogQ().

void addElement ( const std::string &  symbol,
doublereal  weight = -12345.0 
)
inherited

Add an element.

Parameters
symbolAtomic symbol std::string.
weightAtomic mass in amu.

Definition at line 678 of file Phase.cpp.

References CT_ELEM_TYPE_ABSPOS, CT_ELEM_TYPE_ELECTRONCHARGE, Cantera::LookupWtElements(), Phase::m_atomicWeights, Phase::m_elem_type, Phase::m_elementNames, Phase::m_elementsFrozen, and Phase::m_mm.

Referenced by Phase::addElement().

void addElement ( const XML_Node e)
inherited

Add an element from an XML specification.

Parameters
eReference to the XML_Node where the element is described.

Definition at line 701 of file Phase.cpp.

References Phase::addElement().

void addUniqueElement ( const std::string &  symbol,
doublereal  weight = -12345.0,
int  atomicNumber = 0,
doublereal  entropy298 = ENTROPY298_UNKNOWN,
int  elem_type = CT_ELEM_TYPE_ABSPOS 
)
inherited

Add an element, checking for uniqueness The uniqueness is checked by comparing the string symbol.

If not unique, nothing is done.

Parameters
symbolString symbol of the element
weightAtomic weight of the element (kg kmol-1).
atomicNumberAtomic number of the element (unitless)
entropy298Entropy of the element at 298 K and 1 bar in its most stable form. The default is the value ENTROPY298_UNKNOWN, which is interpreted as an unknown, and if used will cause Cantera to throw an error.
elem_typeSpecifies the type of the element constraint equation. This defaults to CT_ELEM_TYPE_ABSPOS, i.e., an element.

Definition at line 708 of file Phase.cpp.

References CT_ELEM_TYPE_ELECTRONCHARGE, Cantera::LookupWtElements(), Phase::m_atomicNumbers, Phase::m_atomicWeights, Phase::m_elem_type, Phase::m_elementNames, Phase::m_elementsFrozen, Phase::m_entropy298, and Phase::m_mm.

Referenced by Phase::addElementsFromXML(), Phase::addUniqueElement(), Phase::addUniqueElementAfterFreeze(), and FixedChemPotSSTP::FixedChemPotSSTP().

void addUniqueElement ( const XML_Node e)
inherited

Add an element, checking for uniqueness The uniqueness is checked by comparing the string symbol.

If not unique, nothing is done.

Parameters
eReference to the XML_Node where the element is described.

Definition at line 755 of file Phase.cpp.

References Phase::addUniqueElement(), Cantera::atofCheck(), XML_Node::child(), ENTROPY298_UNKNOWN, XML_Node::hasAttrib(), XML_Node::hasChild(), and Cantera::stripws().

void addElementsFromXML ( const XML_Node phase)
inherited

Add all elements referenced in an XML_Node tree.

Parameters
phaseReference to the root XML_Node of a phase

Definition at line 780 of file Phase.cpp.

References Phase::addUniqueElement(), XML_Node::child(), XML_Node::findByAttr(), Cantera::get_XML_File(), ctml::getStringArray(), XML_Node::hasAttrib(), XML_Node::hasChild(), and XML_Node::root().

Referenced by Cantera::importPhase().

void freezeElements ( )
inherited

Prohibit addition of more elements, and prepare to add species.

Definition at line 831 of file Phase.cpp.

References Phase::m_elementsFrozen.

Referenced by FixedChemPotSSTP::FixedChemPotSSTP().

bool elementsFrozen ( )
inherited

True if freezeElements has been called.

Definition at line 836 of file Phase.cpp.

References Phase::m_elementsFrozen.

size_t addUniqueElementAfterFreeze ( const std::string &  symbol,
doublereal  weight,
int  atomicNumber,
doublereal  entropy298 = ENTROPY298_UNKNOWN,
int  elem_type = CT_ELEM_TYPE_ABSPOS 
)
inherited

Add an element after elements have been frozen, checking for uniqueness The uniqueness is checked by comparing the string symbol.

If not unique, nothing is done.

Parameters
symbolString symbol of the element
weightAtomic weight of the element (kg kmol-1).
atomicNumberAtomic number of the element (unitless)
entropy298Entropy of the element at 298 K and 1 bar in its most stable form. The default is the value ENTROPY298_UNKNOWN, which if used will cause Cantera to throw an error.
elem_typeSpecifies the type of the element constraint equation. This defaults to CT_ELEM_TYPE_ABSPOS, i.e., an element.

Definition at line 841 of file Phase.cpp.

References Phase::addUniqueElement(), Phase::elementIndex(), Phase::m_elementsFrozen, Phase::m_kk, Phase::m_mm, Phase::m_speciesComp, and Cantera::npos.

Referenced by LatticeSolidPhase::installSlavePhases().

void addUniqueSpecies ( const std::string &  name,
const doublereal *  comp,
doublereal  charge = 0.0,
doublereal  size = 1.0 
)
inherited

Add a species to the phase, checking for uniqueness of the name This routine checks for uniqueness of the string name.

It only adds the species if it is unique.

Parameters
nameString name of the species
compArray containing the elemental composition of the species.
chargeCharge of the species. Defaults to zero.
sizeSize of the species (meters). Defaults to 1 meter.

Definition at line 919 of file Phase.cpp.

References Phase::m_kk, Phase::m_mm, Phase::m_speciesCharge, Phase::m_speciesComp, Phase::m_speciesNames, and Phase::m_speciesSize.

Referenced by FixedChemPotSSTP::FixedChemPotSSTP(), LatticeSolidPhase::installSlavePhases(), and Cantera::installSpecies().

void freezeSpecies ( )
virtualinherited

Call when finished adding species.

Prepare to use them for calculation of mixture properties.

Definition at line 952 of file Phase.cpp.

References Phase::init(), Phase::m_speciesFrozen, and Phase::molecularWeights().

Referenced by FixedChemPotSSTP::FixedChemPotSSTP(), and Cantera::importPhase().

bool speciesFrozen ( )
inlineinherited

True if freezeSpecies has been called.

Definition at line 694 of file Phase.h.

References Phase::m_speciesFrozen.

int stateMFNumber ( ) const
inlineinherited

Return the State Mole Fraction Number.

Definition at line 701 of file Phase.h.

References Phase::m_stateNum.

Referenced by SimpleTransport::update_C(), and LiquidTransport::update_C().

void stateMFChangeCalc ( bool  forceChange = false)
inlineinherited

Every time the mole fractions have changed, this routine will increment the stateMFNumber.

@param forceChange If this is true then the stateMFNumber always

changes. This defaults to false.

Deprecated:

Definition at line 115 of file Phase.cpp.

References Phase::m_stateNum.

Referenced by Phase::setConcentrations(), Phase::setMassFractions(), Phase::setMassFractions_NoNorm(), Phase::setMoleFractions(), and Phase::setMoleFractions_NoNorm().

void init ( const vector_fp mw)
protectedinherited

Initialize. Make a local copy of the vector of molecular weights, and resize the composition arrays to the appropriate size.

Parameters
mwVector of molecular weights of the species.

Definition at line 958 of file Phase.cpp.

References Cantera::int2str(), Phase::m_kk, Phase::m_mmw, Phase::m_molwts, Phase::m_rmolwts, Phase::m_y, Phase::m_ym, and Cantera::Tiny.

Referenced by Phase::freezeSpecies().

void setMolecularWeight ( const int  k,
const double  mw 
)
inlineprotectedinherited

Set the molecular weight of a single species to a given value.

Parameters
kid of the species
mwMolecular Weight (kg kmol-1)

Definition at line 722 of file Phase.h.

References Phase::m_molwts, and Phase::m_rmolwts.

Referenced by PureFluidPhase::initThermo(), and WaterSSTP::initThermoXML().

Kinetics * duplMyselfAsKinetics ( const std::vector< thermo_t * > &  tpVector) const
virtualinherited

Duplication routine for objects which inherit from Kinetics.

This virtual routine can be used to duplicate Kinetics objects inherited from Kinetics even if the application only has a pointer to Kinetics to work with.

These routines are basically wrappers around the derived copy constructor.

Parameters
tpVectorVector of shallow pointers to ThermoPhase objects. this is the m_thermo vector within this object

Reimplemented from Kinetics.

Reimplemented in EdgeKinetics.

Definition at line 253 of file InterfaceKinetics.cpp.

References Kinetics::assignShallowPointers(), and InterfaceKinetics::InterfaceKinetics().

int ID ( ) const
virtualinherited

Return the ID of the kinetics object.

Deprecated:
use type() instead

Reimplemented from Kinetics.

Reimplemented in EdgeKinetics.

Definition at line 231 of file InterfaceKinetics.cpp.

int type ( ) const
virtualinherited

Return the type of the kinetics object.

Reimplemented from Kinetics.

Reimplemented in EdgeKinetics.

Definition at line 236 of file InterfaceKinetics.cpp.

Referenced by InterfaceKinetics::registerReaction().

void setElectricPotential ( int  n,
doublereal  V 
)
inherited

Set the electric potential in the nth phase.

Parameters
nphase Index in this kinetics object.
VElectric potential (volts)

Definition at line 265 of file InterfaceKinetics.cpp.

References ThermoPhase::setElectricPotential(), and Kinetics::thermo().

virtual void getFwdRatesOfProgress ( doublereal *  fwdROP)
inlinevirtualinherited

Return the forward rates of progress for each reaction.

Parameters
fwdROPvector of rates of progress. length = number of reactions, Units are kmol m-2 s-1.

Reimplemented from Kinetics.

Definition at line 181 of file InterfaceKinetics.h.

References InterfaceKinetics::m_kdata, and InterfaceKinetics::updateROP().

virtual void getRevRatesOfProgress ( doublereal *  revROP)
inlinevirtualinherited

Return the reverse rates of progress for each reaction.

Parameters
revROPvector of rates of progress. length = number of reactions, Units are kmol m-2 s-1.

Reimplemented from Kinetics.

Definition at line 191 of file InterfaceKinetics.h.

References InterfaceKinetics::m_kdata, and InterfaceKinetics::updateROP().

virtual void getNetRatesOfProgress ( doublereal *  netROP)
inlinevirtualinherited

Return the net rates of progress for each reaction.

Parameters
netROPvector of rates of progress. length = number of reactions, Units are kmol m-2 s-1.

Reimplemented from Kinetics.

Definition at line 201 of file InterfaceKinetics.h.

References InterfaceKinetics::m_kdata, and InterfaceKinetics::updateROP().

void getEquilibriumConstants ( doublereal *  kc)
virtualinherited

Get the equilibrium constants of all reactions, whether the reaction is reversible or not.

Get the equilibrium constants of all reactions, whether reversible or not.

Parameters
kcReturns the concentration equation constant for the reaction. Length is the number of reactions

Reimplemented from Kinetics.

Definition at line 449 of file InterfaceKinetics.cpp.

References Phase::charge(), DATA_PTR, Cantera::GasConstant, ReactionStoichMgr::getReactionDelta(), ThermoPhase::getStandardChemPotentials(), ThermoPhase::logStandardConc(), Kinetics::m_ii, InterfaceKinetics::m_mu0, InterfaceKinetics::m_phi, InterfaceKinetics::m_rxnstoich, Kinetics::m_start, Kinetics::nPhases(), Phase::nSpecies(), Phase::temperature(), and Kinetics::thermo().

Referenced by InterfaceKinetics::getRevRateConstants().

void getDeltaGibbs ( doublereal *  deltaG)
virtualinherited

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

These values depend upon the concentration of the solution.

units = J kmol-1

Parameters
deltaGOutput vector of deltaG's for reactions Length: m_ii.

Reimplemented from Kinetics.

Definition at line 841 of file InterfaceKinetics.cpp.

References DATA_PTR, ThermoPhase::getChemPotentials(), ReactionStoichMgr::getReactionDelta(), InterfaceKinetics::m_grt, InterfaceKinetics::m_rxnstoich, Kinetics::m_start, Kinetics::nPhases(), and Kinetics::thermo().

void getDeltaElectrochemPotentials ( doublereal *  deltaM)
virtualinherited

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
deltaMOutput vector of deltaM's for reactions Length: m_ii.

Reimplemented from Kinetics.

Definition at line 871 of file InterfaceKinetics.cpp.

References DATA_PTR, ThermoPhase::getElectrochemPotentials(), ReactionStoichMgr::getReactionDelta(), InterfaceKinetics::m_grt, InterfaceKinetics::m_rxnstoich, Kinetics::m_start, Kinetics::nPhases(), and Kinetics::thermo().

void getDeltaEnthalpy ( doublereal *  deltaH)
virtualinherited

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

These values depend upon the concentration of the solution.

units = J kmol-1

Reimplemented from Kinetics.

Definition at line 899 of file InterfaceKinetics.cpp.

References DATA_PTR, ThermoPhase::getPartialMolarEnthalpies(), ReactionStoichMgr::getReactionDelta(), InterfaceKinetics::m_grt, InterfaceKinetics::m_rxnstoich, Kinetics::m_start, Kinetics::nPhases(), and Kinetics::thermo().

void getDeltaEntropy ( doublereal *  deltaS)
virtualinherited

Return the vector of values for the change in entropy due to each reaction.

These values depend upon the concentration of the solution.

units = J kmol-1 Kelvin-1

Parameters
deltaSvector of Enthalpy changes Length = m_ii, number of reactions

Reimplemented from Kinetics.

Definition at line 928 of file InterfaceKinetics.cpp.

References DATA_PTR, ThermoPhase::getPartialMolarEntropies(), ReactionStoichMgr::getReactionDelta(), InterfaceKinetics::m_grt, InterfaceKinetics::m_rxnstoich, Kinetics::m_start, Kinetics::nPhases(), and Kinetics::thermo().

void getDeltaSSGibbs ( doublereal *  deltaG)
virtualinherited

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

getDeltaSSGibbs():

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

Parameters
deltaGvector of rxn SS free energy changes units = J kmol-1

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

Reimplemented from Kinetics.

Definition at line 955 of file InterfaceKinetics.cpp.

References DATA_PTR, ReactionStoichMgr::getReactionDelta(), ThermoPhase::getStandardChemPotentials(), InterfaceKinetics::m_grt, InterfaceKinetics::m_rxnstoich, Kinetics::m_start, Kinetics::nPhases(), and Kinetics::thermo().

void getDeltaSSEnthalpy ( doublereal *  deltaH)
virtualinherited

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

getDeltaSSEnthalpy():

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

Parameters
deltaHvector of rxn SS enthalpy changes units = J kmol-1

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

Reimplemented from Kinetics.

Definition at line 984 of file InterfaceKinetics.cpp.

References DATA_PTR, Cantera::GasConstant, ThermoPhase::getEnthalpy_RT(), ReactionStoichMgr::getReactionDelta(), InterfaceKinetics::m_grt, Kinetics::m_kk, InterfaceKinetics::m_rxnstoich, Kinetics::m_start, Kinetics::nPhases(), Phase::temperature(), and Kinetics::thermo().

void getDeltaSSEntropy ( doublereal *  deltaS)
virtualinherited

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.

Parameters
deltaSvector of rxn SS entropy changes units = J kmol-1 Kelvin-1

Reimplemented from Kinetics.

Definition at line 1017 of file InterfaceKinetics.cpp.

References DATA_PTR, Cantera::GasConstant, ThermoPhase::getEntropy_R(), ReactionStoichMgr::getReactionDelta(), InterfaceKinetics::m_grt, Kinetics::m_kk, InterfaceKinetics::m_rxnstoich, Kinetics::m_start, Kinetics::nPhases(), and Kinetics::thermo().

void getCreationRates ( doublereal *  cdot)
virtualinherited

Returns the Species creation rates [kmol/m^2/s].

Return the species creation rates in array cdot, which must be dimensioned at least as large as the total number of species in all phases of the kinetics model

Parameters
cdotVector containing creation rates. length = m_kk. units = kmol/m^2/s

Reimplemented from Kinetics.

Definition at line 513 of file InterfaceKinetics.cpp.

References ReactionStoichMgr::getCreationRates(), InterfaceKinetics::m_kdata, Kinetics::m_kk, InterfaceKinetics::m_rxnstoich, and InterfaceKinetics::updateROP().

void getDestructionRates ( doublereal *  ddot)
virtualinherited

Return the Species destruction rates [kmol/m^2/s].

Return the species destruction rates in array ddot, which must be dimensioned at least as large as the total number of species in all phases of the kinetics model

Parameters
ddotVector containing destruction rates. length = m_kk. units = kmol/m^2/s

Reimplemented from Kinetics.

Definition at line 526 of file InterfaceKinetics.cpp.

References ReactionStoichMgr::getDestructionRates(), InterfaceKinetics::m_kdata, Kinetics::m_kk, InterfaceKinetics::m_rxnstoich, and InterfaceKinetics::updateROP().

void getNetProductionRates ( doublereal *  net)
virtualinherited

Return the species net production rates [kmol/m^2/s].

Species net production rates [kmol/m^2/s]. Return the species net production rates (creation - destruction) in array wdot, which must be dimensioned at least as large as the total number of species in all phases of the kinetics model

Parameters
netVector of species production rates. units kmol m-d s-1, where d is dimension.

Reimplemented from Kinetics.

Definition at line 544 of file InterfaceKinetics.cpp.

References ReactionStoichMgr::getNetProductionRates(), InterfaceKinetics::m_kdata, Kinetics::m_kk, InterfaceKinetics::m_rxnstoich, and InterfaceKinetics::updateROP().

Referenced by solveSP::calc_t(), ReactingSurf1D::eval(), solveSP::fun_eval(), solveProb::print_header(), and solveProb::printIteration().

virtual doublereal reactantStoichCoeff ( size_t  k,
size_t  i 
) const
inlinevirtualinherited

Stoichiometric coefficient of species k as a reactant in reaction i.

Reimplemented from Kinetics.

Definition at line 353 of file InterfaceKinetics.h.

References InterfaceKinetics::m_rrxn.

virtual doublereal productStoichCoeff ( size_t  k,
size_t  i 
) const
inlinevirtualinherited

Stoichiometric coefficient of species k as a product in reaction i.

Reimplemented from Kinetics.

Definition at line 361 of file InterfaceKinetics.h.

References InterfaceKinetics::m_prxn.

virtual int reactionType ( size_t  i) const
inlinevirtualinherited

Flag specifying the type of reaction.

The legal values and their meaning are specific to the particular kinetics manager.

Reimplemented from Kinetics.

Definition at line 370 of file InterfaceKinetics.h.

References InterfaceKinetics::m_index.

void getActivityConcentrations ( doublereal *const  conc)
virtualinherited

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

Parameters
conc(output) Vector of activity concentrations. Length is equal to the number of species in the kinetics object

Reimplemented from Kinetics.

Definition at line 348 of file InterfaceKinetics.cpp.

References InterfaceKinetics::_update_rates_C(), and InterfaceKinetics::m_conc.

doublereal electrochem_beta ( size_t  irxn) const
inherited

Return the charge transfer rxn Beta parameter for the ith reaction.

Returns the beta parameter for a charge transfer reaction. This parameter is not important for non-charge transfer reactions. Note, the parameter defaults to zero. However, a value of 0.5 should be supplied for every charge transfer reaction if no information is known, as a value of 0.5 pertains to a symmetric transition state. The value can vary between 0 to 1.

Parameters
irxnReaction number in the kinetics mechanism
Returns
Beta parameter. This defaults to zero, even for charge transfer reactions.

Definition at line 1363 of file InterfaceKinetics.cpp.

References InterfaceKinetics::m_ctrxn.

virtual bool isReversible ( size_t  i)
inlinevirtualinherited

True if reaction i has been declared to be reversible.

If isReversible(i) is false, then the reverse rate of progress for reaction i is always zero.

Reimplemented from Kinetics.

Definition at line 404 of file InterfaceKinetics.h.

References InterfaceKinetics::m_revindex.

virtual std::string reactionString ( size_t  i) const
inlinevirtualinherited

Return a string representing the reaction.

Reimplemented from Kinetics.

Definition at line 416 of file InterfaceKinetics.h.

References InterfaceKinetics::m_rxneqn.

void getFwdRateConstants ( doublereal *  kfwd)
virtualinherited

Update the rates of progress of the reactions in the reaction mechanism.

This routine operates on internal data.

Reimplemented from Kinetics.

Definition at line 641 of file InterfaceKinetics.cpp.

References InterfaceKinetics::m_kdata, Kinetics::m_perturb, Cantera::multiply_each(), Kinetics::nReactions(), and InterfaceKinetics::updateROP().

Referenced by InterfaceKinetics::getRevRateConstants().

void getRevRateConstants ( doublereal *  krev,
bool  doIrreversible = false 
)
virtualinherited

Update the rates of progress of the reactions in the reaction mechanism.

This routine operates on internal data.

Reimplemented from Kinetics.

Definition at line 661 of file InterfaceKinetics.cpp.

References DATA_PTR, InterfaceKinetics::getEquilibriumConstants(), InterfaceKinetics::getFwdRateConstants(), Kinetics::m_ii, InterfaceKinetics::m_kdata, Cantera::multiply_each(), and Kinetics::nReactions().

void getActivationEnergies ( doublereal *  E)
virtualinherited

Return the activation energies in Kelvin.

length is the number of reactions

Parameters
EOuptut vector of activation energies. Length: m_ii.

Reimplemented from Kinetics.

Definition at line 677 of file InterfaceKinetics.cpp.

References InterfaceKinetics::m_E.

void addPhase ( thermo_t thermo)
virtualinherited

Add a phase to the kinetics manager object.

This must be done before the function init() is called or before any reactions are input.

This function calls the Kinetics operator addPhase. It also sets the following functions

   m_phaseExists[]
Parameters
thermoReference to the ThermoPhase to be added.

Reimplemented from Kinetics.

Definition at line 1294 of file InterfaceKinetics.cpp.

References Kinetics::addPhase(), InterfaceKinetics::m_phaseExists, and InterfaceKinetics::m_phaseIsStable.

Referenced by InterfaceKinetics::InterfaceKinetics().

void init ( )
virtualinherited

Prepare the class for the addition of reactions.

This function must be called after instantiation of the class, but before any reactions are actually added to the mechanism. This function calculates m_kk the number of species in all phases participating in the reaction mechanism. We don't know m_kk previously, before all phases have been added.

Reimplemented from Kinetics.

Definition at line 1309 of file InterfaceKinetics.cpp.

References InterfaceKinetics::m_conc, InterfaceKinetics::m_grt, Kinetics::m_kk, InterfaceKinetics::m_mu0, InterfaceKinetics::m_phi, InterfaceKinetics::m_pot, InterfaceKinetics::m_prxn, InterfaceKinetics::m_rrxn, Kinetics::nPhases(), Phase::nSpecies(), and Kinetics::thermo().

void addReaction ( ReactionData &  r)
virtualinherited

Add a single reaction to the mechanism.

Parameters
rReference to a ReactionData object containing all of the info needed to describe the reaction.

This routine must be called after init() and before finalize(). This function branches on the types of reactions allowed by the interfaceKinetics manager in order to install the reaction correctly in the manager. The manager allows the following reaction types Elementary Surface Global There is no difference between elementary and surface reactions.

Reimplemented from Kinetics.

Definition at line 1052 of file InterfaceKinetics.cpp.

References Kinetics::incrementRxnCount(), InterfaceKinetics::m_rxneqn, InterfaceKinetics::m_rxnPhaseIsProduct, InterfaceKinetics::m_rxnPhaseIsReactant, Kinetics::nPhases(), Kinetics::products(), Kinetics::reactants(), and Kinetics::speciesPhaseIndex().

void finalize ( )
virtualinherited

Finish adding reactions and prepare for use.

This function must be called after all reactions are entered into the mechanism and before the mechanism is used to calculate reaction rates.

This function must be called after all reactions are entered into the mechanism and before the mechanism is used to calculate reaction rates.

Here, we resize work arrays based on the number of reactions, since we don't know this number up to now.

Reimplemented from Kinetics.

Reimplemented in EdgeKinetics.

Definition at line 1332 of file InterfaceKinetics.cpp.

References Kinetics::finalize(), Cantera::int2str(), InterfaceKinetics::m_finalized, Kinetics::m_kk, Kinetics::m_perturb, InterfaceKinetics::m_phaseExists, InterfaceKinetics::m_rwork, InterfaceKinetics::m_surf, Kinetics::m_thermo, Phase::nDim(), Cantera::npos, Kinetics::nReactions(), Kinetics::reactionPhaseIndex(), and Kinetics::thermo().

void updateROP ( )
inherited
void _update_rates_T ( )
inherited
void _update_rates_phi ( )
inherited

Update properties that depend on the electric potential.

This is called to update all of the properties that depend on potential

Definition at line 307 of file InterfaceKinetics.cpp.

References ThermoPhase::electricPotential(), InterfaceKinetics::m_phi, Kinetics::nPhases(), and Kinetics::thermo().

Referenced by InterfaceKinetics::_update_rates_T().

void _update_rates_C ( )
inherited

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

Update properties that depend on concentrations.

This is called to update all of the properties that depend on 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 326 of file InterfaceKinetics.cpp.

References DATA_PTR, ThermoPhase::getActivityConcentrations(), InterfaceKinetics::m_conc, InterfaceKinetics::m_kdata, Kinetics::m_start, Kinetics::nPhases(), and Kinetics::thermo().

Referenced by InterfaceKinetics::getActivityConcentrations(), and InterfaceKinetics::updateROP().

void advanceCoverages ( doublereal  tstep)
inherited

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
tstepTime value to advance the surface coverages

Definition at line 1384 of file InterfaceKinetics.cpp.

References ImplicitSurfChem::initialize(), ImplicitSurfChem::integrate(), and InterfaceKinetics::m_integrator.

void solvePseudoSteadyStateProblem ( int  ifuncOverride = -1,
doublereal  timeScaleOverride = 1.0 
)
inherited

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

Solve for the 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
ifuncOverride4 values are possible 1 SFLUX_INITIALIZE 2 SFLUX_RESIDUAL 3 SFLUX_JACOBIAN 4 SFLUX_TRANSIENT The default is -1, which means that the program will decide.
timeScaleOverrideWhen 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 1410 of file InterfaceKinetics.cpp.

References ImplicitSurfChem::initialize(), InterfaceKinetics::m_integrator, and ImplicitSurfChem::solvePseudoSteadyStateProblem().

void updateKc ( )
inherited
void registerReaction ( size_t  rxnNumber,
int  type,
size_t  loc 
)
inlineinherited

Write values into m_index.

Parameters
rxnNumberreaction number
typereaction type
loclocation ??

Definition at line 572 of file InterfaceKinetics.h.

References InterfaceKinetics::m_index, and InterfaceKinetics::type().

void applyButlerVolmerCorrection ( doublereal *const  kf)
inherited

Apply corrections for interfacial charge transfer reactions.

For reactions that transfer charge across a potential difference, the activation energies are modified by the potential difference. (see, for example, ...). This method applies this correction.

Parameters
kfVector of forward reaction rate constants on which to have the correction applied

Definition at line 562 of file InterfaceKinetics.cpp.

References Phase::charge(), DATA_PTR, Cantera::fp2str(), Cantera::GasConstant, ReactionStoichMgr::getReactionDelta(), Cantera::int2str(), InterfaceKinetics::m_ctrxn, InterfaceKinetics::m_E, InterfaceKinetics::m_phi, InterfaceKinetics::m_pot, InterfaceKinetics::m_rwork, InterfaceKinetics::m_rxnstoich, Kinetics::nPhases(), Phase::nSpecies(), Phase::temperature(), Kinetics::thermo(), and Cantera::writelog().

Referenced by InterfaceKinetics::_update_rates_T().

void applyExchangeCurrentDensityFormulation ( doublereal *const  kfwd)
inherited

When an electrode reaction rate is optionally specified in terms of its exchange current density, extra vectors need to be precalculated.

Definition at line 618 of file InterfaceKinetics.cpp.

References Cantera::GasConstant, InterfaceKinetics::m_ctrxn, InterfaceKinetics::m_ctrxn_ecdf, Phase::temperature(), and Kinetics::thermo().

Referenced by InterfaceKinetics::_update_rates_T().

void setPhaseExistence ( const size_t  iphase,
const bool  exists 
)
inherited

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
iphaseIndex of the phase. This is the order within the internal thermo vector object
existsBoolean indicating whether the phase exists or not

Definition at line 1427 of file InterfaceKinetics.cpp.

References InterfaceKinetics::m_phaseExists, InterfaceKinetics::m_phaseExistsCheck, InterfaceKinetics::m_phaseIsStable, and Kinetics::m_thermo.

void setPhaseStability ( const int  iphase,
const int  isStable 
)
inherited

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
iphaseIndex of the phase. This is the order within the internal thermo vector object
isStableFlag indicating whether the phase is stable or not

Definition at line 1480 of file InterfaceKinetics.cpp.

References InterfaceKinetics::m_phaseIsStable, and Kinetics::m_thermo.

int phaseExistence ( const int  iphase) const
inherited

Gets the phase existence int for the ith phase.

Parameters
iphasePhase Id
Returns
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 1454 of file InterfaceKinetics.cpp.

References InterfaceKinetics::m_phaseExists, and Kinetics::m_thermo.

int phaseStability ( const int  iphase) const
inherited

Gets the phase stability int for the ith phase.

Parameters
iphasePhase Id
Returns
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 1471 of file InterfaceKinetics.cpp.

References InterfaceKinetics::m_phaseIsStable, and Kinetics::m_thermo.

void assignShallowPointers ( const std::vector< thermo_t * > &  tpVector)
virtualinherited

Reassign the shallow pointers within the FKinetics object.

This type or routine is absolute necessary because the Kinetics object doesn't own the ThermoPhase objects. After a duplication, we need to point to different ThermoPhase objects.

We check that the ThermoPhase objects are aligned in the same order and have the following identical properties to the ones that they are replacing. id() eosType() nSpecies()

Parameters
tpVectorVector of shallow pointers to ThermoPhase objects. this is the m_thermo vector within this object

Definition at line 179 of file Kinetics.cpp.

References ThermoPhase::eosType(), Phase::id(), Kinetics::m_thermo, and Phase::nSpecies().

Referenced by EdgeKinetics::duplMyselfAsKinetics(), AqueousKinetics::duplMyselfAsKinetics(), GasKinetics::duplMyselfAsKinetics(), InterfaceKinetics::duplMyselfAsKinetics(), and Kinetics::duplMyselfAsKinetics().

size_t nReactions ( ) const
inlineinherited
void checkReactionIndex ( size_t  m) const
inherited

Check that the specified reaction index is in range Throws an exception if i is greater than nReactions()

Definition at line 136 of file Kinetics.cpp.

References Kinetics::m_ii.

void checkReactionArraySize ( size_t  ii) const
inherited

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

Used before calls which take an array pointer.

Definition at line 143 of file Kinetics.cpp.

References Kinetics::m_ii.

void checkSpeciesIndex ( size_t  k) const
inherited

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

Definition at line 164 of file Kinetics.cpp.

References Kinetics::m_kk.

void checkSpeciesArraySize ( size_t  mm) const
inherited

Check that an array size is at least nSpecies() Throws an exception if kk is less than nSpecies().

Used before calls which take an array pointer.

Definition at line 171 of file Kinetics.cpp.

References Kinetics::m_kk.

size_t nPhases ( ) const
inlineinherited
void checkPhaseIndex ( size_t  m) const
inherited

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

Definition at line 150 of file Kinetics.cpp.

References Kinetics::nPhases().

void checkPhaseArraySize ( size_t  mm) const
inherited

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

Used before calls which take an array pointer.

Definition at line 157 of file Kinetics.cpp.

References Kinetics::nPhases().

size_t phaseIndex ( std::string  ph)
inlineinherited

Return the phase index of a phase in the list of phases defined within the object.

Parameters
phstd::string name of the phase

If a -1 is returned, then the phase is not defined in the Kinetics object.

Definition at line 266 of file Kinetics.h.

References Kinetics::m_phaseindex, and Cantera::npos.

Referenced by Cantera::importKinetics().

size_t surfacePhaseIndex ( )
inlineinherited

This returns the integer index of the phase which has ThermoPhase type cSurf.

For heterogeneous mechanisms, this identifies the one surface phase. For homogeneous mechanisms, this returns -1.

Definition at line 280 of file Kinetics.h.

References Kinetics::m_surfphase.

Referenced by InterfaceKinetics::_update_rates_T(), solveSP::calc_t(), solveSP::fun_eval(), Cantera::getRateCoefficient(), solveProb::print_header(), and solveSP::solveSP().

size_t reactionPhaseIndex ( )
inlineinherited

Phase where the reactions occur.

For heterogeneous mechanisms, one of the phases in the list of phases represents the 2D interface or 1D edge at which the reactions take place. This method returns the index of the phase with the smallest spatial dimension (1, 2, or 3) among the list of phases. If there is more than one, the index of the first one is returned. For homogeneous mechanisms, the value 0 is returned.

Definition at line 294 of file Kinetics.h.

References Kinetics::m_rxnphase.

Referenced by EdgeKinetics::finalize(), and InterfaceKinetics::finalize().

thermo_t& thermo ( size_t  n = 0)
inlineinherited

This method returns a reference to the nth ThermoPhase object defined in this kinetics mechanism.

It is typically used so that member functions of the ThermoPhase object may be called. For homogeneous mechanisms, there is only one object, and this method can be called without an argument to access it.

Parameters
nIndex of the ThermoPhase being sought.

Definition at line 309 of file Kinetics.h.

References Kinetics::m_thermo.

Referenced by AqueousKinetics::_update_rates_C(), InterfaceKinetics::_update_rates_C(), InterfaceKinetics::_update_rates_phi(), InterfaceKinetics::_update_rates_T(), InterfaceKinetics::applyButlerVolmerCorrection(), InterfaceKinetics::applyExchangeCurrentDensityFormulation(), solveSP::calc_t(), EdgeKinetics::finalize(), InterfaceKinetics::finalize(), InterfaceKinetics::getDeltaElectrochemPotentials(), AqueousKinetics::getDeltaEnthalpy(), GasKinetics::getDeltaEnthalpy(), InterfaceKinetics::getDeltaEnthalpy(), AqueousKinetics::getDeltaEntropy(), GasKinetics::getDeltaEntropy(), InterfaceKinetics::getDeltaEntropy(), AqueousKinetics::getDeltaGibbs(), GasKinetics::getDeltaGibbs(), InterfaceKinetics::getDeltaGibbs(), AqueousKinetics::getDeltaSSEnthalpy(), GasKinetics::getDeltaSSEnthalpy(), InterfaceKinetics::getDeltaSSEnthalpy(), AqueousKinetics::getDeltaSSEntropy(), GasKinetics::getDeltaSSEntropy(), InterfaceKinetics::getDeltaSSEntropy(), AqueousKinetics::getDeltaSSGibbs(), GasKinetics::getDeltaSSGibbs(), InterfaceKinetics::getDeltaSSGibbs(), Cantera::getEfficiencies(), AqueousKinetics::getEquilibriumConstants(), GasKinetics::getEquilibriumConstants(), InterfaceKinetics::getEquilibriumConstants(), Cantera::getRateCoefficient(), Cantera::getStick(), ImplicitSurfChem::ImplicitSurfChem(), AqueousKinetics::init(), GasKinetics::init(), InterfaceKinetics::init(), ConstPressureReactor::initialize(), Reactor::initialize(), Kinetics::kineticsSpeciesIndex(), Kinetics::kineticsSpeciesName(), Kinetics::nTotalSpecies(), solveProb::print_header(), InterfaceKinetics::setElectricPotential(), ImplicitSurfChem::solvePseudoSteadyStateProblem(), solveSP::solveSP(), Kinetics::speciesPhase(), AqueousKinetics::updateKc(), GasKinetics::updateKc(), InterfaceKinetics::updateKc(), and solveSP::updateMFKinSpecies().

thermo_t& phase ( size_t  n = 0)
inlineinherited

This method returns a reference to the nth ThermoPhase defined in this kinetics mechanism.

It is typically used so that member functions of the ThermoPhase may be called.

Deprecated:
This method is redundant.
Parameters
nIndex of the ThermoPhase being sought.

Definition at line 324 of file Kinetics.h.

References Cantera::deprecatedMethod(), and Kinetics::m_thermo.

const thermo_t& phase ( size_t  n = 0) const
inlineinherited

This method returns a reference to the nth ThermoPhase defined in this kinetics mechanism.

It is typically used so that member functions of the ThermoPhase may be called.

Deprecated:
This method is redundant.
Parameters
nIndex of the ThermoPhase being sought.

Definition at line 336 of file Kinetics.h.

References Cantera::deprecatedMethod(), and Kinetics::m_thermo.

size_t nTotalSpecies ( ) const
inlineinherited

The total number of species in all phases participating in the kinetics mechanism.

This is useful to dimension arrays for use in calls to methods that return the species production rates, for example.

Definition at line 347 of file Kinetics.h.

References Kinetics::nPhases(), Phase::nSpecies(), and Kinetics::thermo().

Referenced by ReactingSurf1D::init(), and rxninfo::installReaction().

size_t start ( size_t  n)
inlineinherited

Returns the starting index of the species in the nth phase associated with the reaction mechanism.

Parameters
nReturn the index of first species in the nth phase associated with the reaction mechanism.

Definition at line 363 of file Kinetics.h.

References Cantera::deprecatedMethod(), and Kinetics::m_start.

size_t kineticsSpeciesIndex ( size_t  k,
size_t  n 
) const
inlineinherited

The location of species k of phase n in species arrays.

Kinetics manager classes return species production rates in flat arrays, with the species of each phases following one another, in the order the phases were added. This method is useful to find the value for a particular species of a particular phase in arrays returned from methods like getCreationRates that return an array of species-specific quantities.

Example: suppose a heterogeneous mechanism involves three phases. The first contains 12 species, the second 26, and the third 3. Then species arrays must have size at least 41, and positions 0 - 11 are the values for the species in the first phase, positions 12 - 37 are the values for the species in the second phase, etc. Then kineticsSpeciesIndex(7, 0) = 7, kineticsSpeciesIndex(4, 1) = 16, and kineticsSpeciesIndex(2, 2) = 40.

Parameters
kspecies index
nphase index for the species

Definition at line 391 of file Kinetics.h.

References Kinetics::m_start.

Referenced by solveSP::calc_t(), Cantera::checkRxnElementBalance(), ReactingSurf1D::eval(), solveSP::fun_eval(), Cantera::getEfficiencies(), Cantera::getReagents(), Cantera::getStick(), Kinetics::kineticsSpeciesIndex(), solveSP::solveSP(), and solveSP::updateMFKinSpecies().

size_t kineticsSpeciesIndex ( const std::string &  nm) const
inherited

This routine will look up a species number based on the input std::string nm.

The lookup of species will occur for all phases listed in the kinetics object.

return

  • If a match is found, the position in the species list is returned.
  • If no match is found, the value -1 is returned.
Parameters
nmInput string name of the species

Definition at line 263 of file Kinetics.cpp.

References Phase::id(), Kinetics::m_start, Kinetics::m_thermo, Cantera::npos, Phase::speciesIndex(), and Kinetics::thermo().

size_t kineticsSpeciesIndex ( const std::string &  nm,
const std::string &  ph 
) const
inherited

This routine will look up a species number based on the input std::string nm.

The lookup of species will occur in the specified phase of the object, or all phases if ph is "<any>".

return

  • If a match is found, the position in the species list is returned.
  • If no match is found, the value npos (-1) is returned.
Parameters
nmInput string name of the species
phInput string name of the phase.

Definition at line 288 of file Kinetics.cpp.

References Phase::id(), Kinetics::kineticsSpeciesIndex(), Kinetics::m_start, Kinetics::m_thermo, Cantera::npos, Phase::speciesIndex(), and Kinetics::thermo().

string kineticsSpeciesName ( size_t  k) const
inherited

Return the std::string name of the kth species in the kinetics manager.

kineticsSpeciesName():

k is an integer from 0 to ktot - 1, where ktot is the number of species in the kinetics manager, which is the sum of the number of species in all phases participating in the kinetics manager. If k is out of bounds, the std::string "<unknown>" is returned.

Parameters
kspecies index

Return the string name of the kth species in the kinetics manager. k is an integer from 0 to ktot - 1, where ktot is the number of species in the kinetics manager, which is the sum of the number of species in all phases participating in the kinetics manager. If k is out of bounds, the string "<unknown>" is returned.

Definition at line 242 of file Kinetics.cpp.

References Kinetics::m_start, Cantera::npos, Phase::speciesName(), and Kinetics::thermo().

Referenced by Cantera::getStick(), solveSP::printFinal(), solveProb::printIteration(), and solveSP::printIteration().

thermo_t & speciesPhase ( std::string  nm)
inherited

This function looks up the std::string name of a species and returns a reference to the ThermoPhase object of the phase where the species resides.

This function looks up the string name of a species and returns a reference to the ThermoPhase object of the phase where the species resides.

Will throw an error if the species std::string doesn't match.

Parameters
nmString containing the name of the species.

Will throw an error if the species string doesn't match.

Definition at line 315 of file Kinetics.cpp.

References Kinetics::m_thermo, Cantera::npos, Phase::speciesIndex(), and Kinetics::thermo().

Referenced by Cantera::checkRxnElementBalance(), Cantera::getStick(), and rxninfo::installReaction().

thermo_t& speciesPhase ( size_t  k)
inlineinherited

This function takes as an argument the kineticsSpecies index (i.e., the list index in the list of species in the kinetics manager) and returns the species' owning ThermoPhase object.

Parameters
kSpecies index

Definition at line 454 of file Kinetics.h.

References Kinetics::speciesPhaseIndex(), and Kinetics::thermo().

size_t speciesPhaseIndex ( size_t  k)
inherited

This function takes as an argument the kineticsSpecies index (i.e., the list index in the list of species in the kinetics manager) and returns the index of the phase owning the species.

Parameters
kSpecies index

Definition at line 337 of file Kinetics.cpp.

References Cantera::int2str(), Kinetics::m_start, and Cantera::npos.

Referenced by InterfaceKinetics::addReaction(), Cantera::checkRxnElementBalance(), Cantera::getStick(), and Kinetics::speciesPhase().

virtual void getReactionDelta ( const doublereal *  property,
doublereal *  deltaProperty 
)
inlinevirtualinherited

Change in species properties.

Given an array of molar species property values \( z_k, k = 1, \dots, K \), return the array of reaction values

\[ \Delta Z_i = \sum_k \nu_{k,i} z_k, i = 1, \dots, I. \]

For example, if this method is called with the array of standard-state molar Gibbs free energies for the species, then the values returned in array deltaProperty would be the standard-state Gibbs free energies of reaction for each reaction.

Parameters
propertyInput vector of property value. Length: m_kk.
deltaPropertyOutput vector of deltaRxn. Length: m_ii.

Definition at line 547 of file Kinetics.h.

References Kinetics::err().

virtual doublereal reactantOrder ( size_t  k,
size_t  i 
) const
inlinevirtualinherited

Reactant order of species k in reaction i.

This is the nominal order of the activity concentration in determining the forward rate of progress of the reaction

Parameters
kkinetic species index
ireaction index

Definition at line 735 of file Kinetics.h.

References Kinetics::err().

virtual doublereal productOrder ( int  k,
int  i 
) const
inlinevirtualinherited

product Order of species k in reaction i.

This is the nominal order of the activity concentration of species k in determining the reverse rate of progress of the reaction i

For irreversible reactions, this will all be zero.

Parameters
kkinetic species index
ireaction index

Definition at line 750 of file Kinetics.h.

References Kinetics::err().

virtual const std::vector<size_t>& reactants ( size_t  i) const
inlinevirtualinherited

Returns a read-only reference to the vector of reactant index numbers for reaction i.

Parameters
ireaction index

Definition at line 770 of file Kinetics.h.

References Kinetics::m_reactants.

Referenced by InterfaceKinetics::addReaction(), and rxninfo::installReaction().

virtual const std::vector<size_t>& products ( size_t  i) const
inlinevirtualinherited

Returns a read-only reference to the vector of product index numbers for reaction i.

Parameters
ireaction index

Definition at line 780 of file Kinetics.h.

References Kinetics::m_products.

Referenced by InterfaceKinetics::addReaction(), and rxninfo::installReaction().

doublereal multiplier ( size_t  i) const
inlineinherited

The current value of the multiplier for reaction i.

Parameters
iindex of the reaction

Definition at line 953 of file Kinetics.h.

References Kinetics::m_perturb.

void setMultiplier ( size_t  i,
doublereal  f 
)
inlineinherited

Set the multiplier for reaction i to f.

Parameters
iindex of the reaction
fvalue of the multiplier.

Definition at line 962 of file Kinetics.h.

References Kinetics::m_perturb.

void incrementRxnCount ( )
inlineinherited

Increment the number of reactions in the mechanism by one.

Todo:
Should be protected?

Definition at line 972 of file Kinetics.h.

References Kinetics::m_ii, and Kinetics::m_perturb.

Referenced by AqueousKinetics::addReaction(), GasKinetics::addReaction(), and InterfaceKinetics::addReaction().

void selectPhase ( const doublereal *  data,
const thermo_t phase,
doublereal *  phase_data 
)
inherited

Extract from array data the portion pertaining to phase phase.

Takes as input an array of properties for all species in the mechanism and copies those values beloning to a particular phase to the output array.

Parameters
datadata
phasephase
phase_dataphase_data
dataInput data array.
phasePointer to one of the phase objects participating in this reaction mechanism
phase_dataOutput array where the values for the the specified phase are to be written.

Definition at line 217 of file Kinetics.cpp.

References Kinetics::m_start, Kinetics::m_thermo, Kinetics::nPhases(), and Phase::nSpecies().

Member Data Documentation

bool m_ok
protected

Flag indicating that the object has been instantiated.

Definition at line 112 of file Interface.h.

Referenced by Interface::Interface(), Interface::operator!(), Interface::operator=(), and Interface::ready().

Cantera::XML_Node* m_r
protected

XML_Node pointer to the XML File object that contains the Surface and the Interfacial Reaction object description.

Definition at line 116 of file Interface.h.

Referenced by Interface::Interface(), and Interface::operator=().

doublereal m_n0
protectedinherited
doublereal m_logn0
protectedinherited
doublereal m_tmin
protectedinherited

Minimum temperature for valid species standard state thermo props.

This is the minimum temperature at which all species have valid standard state thermo props defined.

Definition at line 648 of file SurfPhase.h.

Referenced by SurfPhase::operator=().

doublereal m_tmax
protectedinherited

Maximum temperature for valid species standard state thermo props.

This is the maximum temperature at which all species have valid standard state thermo props defined.

Definition at line 655 of file SurfPhase.h.

Referenced by SurfPhase::operator=().

doublereal m_press
protectedinherited

Current value of the pressure (Pa)

Definition at line 658 of file SurfPhase.h.

Referenced by SurfPhase::operator=(), SurfPhase::pressure(), and SurfPhase::setPressure().

doublereal m_tlast
mutableprotectedinherited

Current value of the temperature (Kelvin)

Definition at line 661 of file SurfPhase.h.

Referenced by SurfPhase::_updateThermo(), and SurfPhase::operator=().

vector_fp m_h0
mutableprotectedinherited

Temporary storage for the reference state enthalpies.

Definition at line 664 of file SurfPhase.h.

Referenced by SurfPhase::_updateThermo(), SurfPhase::enthalpy_mole(), SurfPhase::getEnthalpy_RT(), SurfPhase::initThermo(), and SurfPhase::operator=().

vector_fp m_s0
mutableprotectedinherited

Temporary storage for the reference state entropies.

Definition at line 667 of file SurfPhase.h.

Referenced by SurfPhase::_updateThermo(), SurfPhase::getEntropy_R(), SurfPhase::initThermo(), and SurfPhase::operator=().

vector_fp m_cp0
mutableprotectedinherited

Temporary storage for the reference state heat capacities.

Definition at line 670 of file SurfPhase.h.

Referenced by SurfPhase::_updateThermo(), SurfPhase::getCp_R(), SurfPhase::initThermo(), and SurfPhase::operator=().

vector_fp m_mu0
mutableprotectedinherited

Temporary storage for the reference state gibbs energies.

Definition at line 673 of file SurfPhase.h.

Referenced by SurfPhase::_updateThermo(), SurfPhase::getChemPotentials(), SurfPhase::getGibbs_RT(), SurfPhase::getStandardChemPotentials(), SurfPhase::initThermo(), and SurfPhase::operator=().

vector_fp m_work
mutableprotectedinherited
vector_fp m_pe
mutableprotectedinherited

Potential energy of each species in the surface phase.

Todo:
Fix potential energy Note, the potential energy terms seem to be orphaned at the moment. They are not connected to the Gibbs free energy calculation in this object
Deprecated:

Definition at line 687 of file SurfPhase.h.

Referenced by SurfPhase::initThermo(), SurfPhase::operator=(), SurfPhase::potentialEnergy(), and SurfPhase::setPotentialEnergy().

vector_fp m_logsize
mutableprotectedinherited

vector storing the log of the size of each species.

The size of each species is defined as the number of surface sites each species occupies.

Definition at line 694 of file SurfPhase.h.

Referenced by SurfPhase::initThermo(), SurfPhase::logStandardConc(), and SurfPhase::operator=().

SpeciesThermo* m_spthermo
protectedinherited

Pointer to the calculation manager for species reference-state thermodynamic properties.

This class is called when the reference-state thermodynamic properties of all the species in the phase needs to be evaluated.

Definition at line 1611 of file ThermoPhase.h.

Referenced by MixtureFugacityTP::_updateReferenceStateThermo(), ConstDensityThermo::_updateThermo(), SurfPhase::_updateThermo(), SingleSpeciesTP::_updateThermo(), IdealGasPhase::_updateThermo(), LatticePhase::_updateThermo(), IdealSolidSolnPhase::_updateThermo(), ConstDensityThermo::enthalpy_mole(), LatticePhase::enthalpy_mole(), RedlichKwongMFTP::entropy_mole(), IdealGasPhase::entropy_mole(), FixedChemPotSSTP::FixedChemPotSSTP(), ConstDensityThermo::getChemPotentials(), MixtureFugacityTP::getEntropy_R(), IdealGasPhase::getEntropy_R(), PureFluidPhase::getEntropy_R_ref(), MixtureFugacityTP::getGibbs_RT(), IdealGasPhase::getGibbs_RT(), PureFluidPhase::getGibbs_RT_ref(), IdealGasPhase::getPartialMolarEntropies(), MixtureFugacityTP::getPureGibbs(), IdealGasPhase::getPureGibbs(), MixtureFugacityTP::getStandardChemPotentials(), IdealGasPhase::getStandardChemPotentials(), IdealSolidSolnPhase::initLengths(), ConstDensityThermo::initThermo(), StoichSubstance::initThermo(), StoichSubstanceSSTP::initThermo(), PureFluidPhase::initThermo(), SingleSpeciesTP::initThermo(), IdealGasPhase::initThermo(), LatticePhase::initThermo(), WaterSSTP::initThermoXML(), LatticeSolidPhase::installSlavePhases(), ConstDensityThermo::intEnergy_mole(), LatticePhase::intEnergy_mole(), ThermoPhase::maxTemp(), ThermoPhase::minTemp(), VPStandardStateTP::operator=(), ThermoPhase::operator=(), ThermoPhase::refPressure(), ThermoPhase::setSpeciesThermo(), LatticeSolidPhase::speciesThermo(), ThermoPhase::speciesThermo(), and ThermoPhase::~ThermoPhase().

std::vector<const XML_Node*> m_speciesData
protectedinherited

Vector of pointers to the species databases.

This is used to access data needed to construct the transport manager and other properties later in the initialization process. We create a copy of the XML_Node data read in here. Therefore, we own this data.

Definition at line 1621 of file ThermoPhase.h.

Referenced by LatticeSolidPhase::installSlavePhases(), ThermoPhase::operator=(), ThermoPhase::saveSpeciesData(), ThermoPhase::speciesData(), and ThermoPhase::~ThermoPhase().

doublereal m_phi
protectedinherited

Stored value of the electric potential for this phase.

Units are Volts

Definition at line 1627 of file ThermoPhase.h.

Referenced by ThermoPhase::electricPotential(), IdealMolalSoln::electricPotential(), ThermoPhase::operator=(), and ThermoPhase::setElectricPotential().

vector_fp m_lambdaRRT
protectedinherited

Vector of element potentials.

-> length equal to number of elements

Definition at line 1631 of file ThermoPhase.h.

Referenced by ThermoPhase::getElementPotentials(), ThermoPhase::operator=(), and ThermoPhase::setElementPotentials().

bool m_hasElementPotentials
protectedinherited

Boolean indicating whether there is a valid set of saved element potentials for this phase.

Definition at line 1635 of file ThermoPhase.h.

Referenced by ThermoPhase::getElementPotentials(), ThermoPhase::operator=(), and ThermoPhase::setElementPotentials().

bool m_chargeNeutralityNecessary
protectedinherited

Boolean indicating whether a charge neutrality condition is a necessity.

Note, the charge neutrality condition is not a necessity for ideal gas phases. There may be a net charge in those phases, because the NASA polynomials for ionized species in Ideal gases take this condition into account. However, liquid phases usually require charge neutrality in order for their derived thermodynamics to be valid.

Definition at line 1645 of file ThermoPhase.h.

Referenced by ThermoPhase::chargeNeutralityNecessary(), MolalityVPSSTP::MolalityVPSSTP(), and ThermoPhase::operator=().

int m_ssConvention
protectedinherited

Contains the standard state convention.

Definition at line 1648 of file ThermoPhase.h.

Referenced by ThermoPhase::operator=(), and ThermoPhase::standardStateConvention().

std::vector<doublereal> xMol_Ref
protectedinherited

Reference Mole Fraction Composition.

Occasionally, the need arises to find a safe mole fraction vector to initialize the object to. This contains such a vector. The algorithm will pick up the mole fraction vector that is applied from the state xml file in the input file

Definition at line 1657 of file ThermoPhase.h.

Referenced by ThermoPhase::getReferenceComposition(), ThermoPhase::initThermo(), and ThermoPhase::setReferenceComposition().

size_t m_kk
protectedinherited

Number of species in the phase.

Definition at line 727 of file Phase.h.

Referenced by DebyeHuckel::_lnactivityWaterHelgesonFixedForm(), MixtureFugacityTP::_updateReferenceStateThermo(), ConstDensityThermo::_updateThermo(), SurfPhase::_updateThermo(), IdealGasPhase::_updateThermo(), LatticePhase::_updateThermo(), IdealSolidSolnPhase::_updateThermo(), Phase::addUniqueElementAfterFreeze(), Phase::addUniqueSpecies(), HMWSoln::applyphScale(), RedlichKwongMFTP::applyStandardMixingRules(), GibbsExcessVPSSTP::calcDensity(), IdealMolalSoln::calcDensity(), DebyeHuckel::calcDensity(), HMWSoln::calcDensity(), IonsFromNeutralVPSSTP::calcIonMoleFractions(), MolalityVPSSTP::calcMolalities(), HMWSoln::calcMolalitiesCropped(), IonsFromNeutralVPSSTP::calcNeutralMoleculeMoleFractions(), PseudoBinaryVPSSTP::calcPseudoBinaryMoleFractions(), MolarityIonicVPSSTP::calcPseudoBinaryMoleFractions(), RedlichKwongMFTP::calculateAB(), GibbsExcessVPSSTP::checkMFSum(), Phase::checkSpeciesArraySize(), Phase::checkSpeciesIndex(), HMWSoln::counterIJ_setup(), RedlichKwongMFTP::critDensity(), RedlichKwongMFTP::critPressure(), RedlichKwongMFTP::critTemperature(), ConstDensityThermo::expGibbs_RT(), IdealGasPhase::expGibbs_RT_ref(), IdealSolidSolnPhase::expGibbs_RT_ref(), MolalityVPSSTP::findCLMIndex(), GibbsExcessVPSSTP::getActivities(), IdealMolalSoln::getActivities(), DebyeHuckel::getActivities(), HMWSoln::getActivities(), ConstDensityThermo::getActivityCoefficients(), SingleSpeciesTP::getActivityCoefficients(), IdealSolnGasVPSS::getActivityCoefficients(), IonsFromNeutralVPSSTP::getActivityCoefficients(), GibbsExcessVPSSTP::getActivityCoefficients(), RedlichKwongMFTP::getActivityCoefficients(), LatticeSolidPhase::getActivityCoefficients(), MixedSolventElectrolyte::getActivityCoefficients(), PhaseCombo_Interaction::getActivityCoefficients(), IdealSolidSolnPhase::getActivityCoefficients(), ThermoPhase::getActivityCoefficients(), MolalityVPSSTP::getActivityCoefficients(), IdealGasPhase::getActivityCoefficients(), LatticePhase::getActivityCoefficients(), IdealSolnGasVPSS::getActivityConcentrations(), RedlichKwongMFTP::getActivityConcentrations(), IdealMolalSoln::getActivityConcentrations(), IdealSolidSolnPhase::getActivityConcentrations(), DebyeHuckel::getActivityConcentrations(), HMWSoln::getActivityConcentrations(), ConstDensityThermo::getChemPotentials(), SurfPhase::getChemPotentials(), MolarityIonicVPSSTP::getChemPotentials(), IdealSolnGasVPSS::getChemPotentials(), RedlichKwongMFTP::getChemPotentials(), RedlichKisterVPSSTP::getChemPotentials(), MargulesVPSSTP::getChemPotentials(), MixedSolventElectrolyte::getChemPotentials(), PhaseCombo_Interaction::getChemPotentials(), IdealSolidSolnPhase::getChemPotentials(), IdealMolalSoln::getChemPotentials(), IdealGasPhase::getChemPotentials(), LatticePhase::getChemPotentials(), DebyeHuckel::getChemPotentials(), HMWSoln::getChemPotentials(), VPStandardStateTP::getChemPotentials_RT(), MixtureFugacityTP::getChemPotentials_RT(), IdealSolnGasVPSS::getChemPotentials_RT(), RedlichKwongMFTP::getChemPotentials_RT(), IdealSolidSolnPhase::getChemPotentials_RT(), SurfPhase::getCoverages(), IdealSolidSolnPhase::getCp_R_ref(), RedlichKisterVPSSTP::getd2lnActCoeffdT2(), MargulesVPSSTP::getd2lnActCoeffdT2(), MixedSolventElectrolyte::getd2lnActCoeffdT2(), PhaseCombo_Interaction::getd2lnActCoeffdT2(), IonsFromNeutralVPSSTP::getdlnActCoeffdlnN(), PhaseCombo_Interaction::getdlnActCoeffdlnN(), RedlichKisterVPSSTP::getdlnActCoeffdlnN(), MargulesVPSSTP::getdlnActCoeffdlnN(), MixedSolventElectrolyte::getdlnActCoeffdlnN(), ThermoPhase::getdlnActCoeffdlnN(), IonsFromNeutralVPSSTP::getdlnActCoeffdlnN_diag(), PhaseCombo_Interaction::getdlnActCoeffdlnN_diag(), RedlichKisterVPSSTP::getdlnActCoeffdlnN_diag(), MargulesVPSSTP::getdlnActCoeffdlnN_diag(), MixedSolventElectrolyte::getdlnActCoeffdlnN_diag(), IonsFromNeutralVPSSTP::getdlnActCoeffdlnX_diag(), PhaseCombo_Interaction::getdlnActCoeffdlnX_diag(), RedlichKisterVPSSTP::getdlnActCoeffdlnX_diag(), MargulesVPSSTP::getdlnActCoeffdlnX_diag(), MixedSolventElectrolyte::getdlnActCoeffdlnX_diag(), IonsFromNeutralVPSSTP::getdlnActCoeffds(), PhaseCombo_Interaction::getdlnActCoeffds(), RedlichKisterVPSSTP::getdlnActCoeffds(), MargulesVPSSTP::getdlnActCoeffds(), MixedSolventElectrolyte::getdlnActCoeffds(), RedlichKisterVPSSTP::getdlnActCoeffdT(), MargulesVPSSTP::getdlnActCoeffdT(), MixedSolventElectrolyte::getdlnActCoeffdT(), PhaseCombo_Interaction::getdlnActCoeffdT(), PureFluidPhase::getElectrochemPotentials(), PseudoBinaryVPSSTP::getElectrochemPotentials(), MolarityIonicVPSSTP::getElectrochemPotentials(), GibbsExcessVPSSTP::getElectrochemPotentials(), RedlichKisterVPSSTP::getElectrochemPotentials(), MargulesVPSSTP::getElectrochemPotentials(), ThermoPhase::getElectrochemPotentials(), MixedSolventElectrolyte::getElectrochemPotentials(), MolalityVPSSTP::getElectrochemPotentials(), PhaseCombo_Interaction::getElectrochemPotentials(), IdealSolidSolnPhase::getEnthalpy_RT(), LatticePhase::getEnthalpy_RT(), IdealSolidSolnPhase::getEnthalpy_RT_ref(), MixtureFugacityTP::getEntropy_R(), IdealGasPhase::getEntropy_R(), IdealSolidSolnPhase::getEntropy_R_ref(), WaterSSTP::getGibbs_ref(), LatticeSolidPhase::getGibbs_ref(), IdealSolidSolnPhase::getGibbs_ref(), LatticePhase::getGibbs_ref(), MixtureFugacityTP::getGibbs_RT(), IdealGasPhase::getGibbs_RT(), IdealSolidSolnPhase::getGibbs_RT(), LatticePhase::getGibbs_RT(), IdealSolidSolnPhase::getGibbs_RT_ref(), LatticePhase::getGibbs_RT_ref(), MixtureFugacityTP::getIntEnergy_RT(), IdealGasPhase::getIntEnergy_RT(), IdealSolidSolnPhase::getIntEnergy_RT(), IdealGasPhase::getIntEnergy_RT_ref(), IdealSolidSolnPhase::getIntEnergy_RT_ref(), MolarityIonicVPSSTP::getLnActivityCoefficients(), RedlichKisterVPSSTP::getLnActivityCoefficients(), MargulesVPSSTP::getLnActivityCoefficients(), ThermoPhase::getLnActivityCoefficients(), MolalityVPSSTP::getMolalities(), IdealMolalSoln::getMolalityActivityCoefficients(), DebyeHuckel::getMolalityActivityCoefficients(), IonsFromNeutralVPSSTP::getNeutralMoleculeMoleGrads(), SurfPhase::getPartialMolarCp(), IdealSolnGasVPSS::getPartialMolarCp(), MolarityIonicVPSSTP::getPartialMolarCp(), RedlichKwongMFTP::getPartialMolarCp(), RedlichKisterVPSSTP::getPartialMolarCp(), MargulesVPSSTP::getPartialMolarCp(), MixedSolventElectrolyte::getPartialMolarCp(), PhaseCombo_Interaction::getPartialMolarCp(), IdealSolidSolnPhase::getPartialMolarCp(), IdealMolalSoln::getPartialMolarCp(), LatticePhase::getPartialMolarCp(), DebyeHuckel::getPartialMolarCp(), HMWSoln::getPartialMolarCp(), SurfPhase::getPartialMolarEnthalpies(), IdealSolnGasVPSS::getPartialMolarEnthalpies(), MolarityIonicVPSSTP::getPartialMolarEnthalpies(), IonsFromNeutralVPSSTP::getPartialMolarEnthalpies(), RedlichKwongMFTP::getPartialMolarEnthalpies(), RedlichKisterVPSSTP::getPartialMolarEnthalpies(), MargulesVPSSTP::getPartialMolarEnthalpies(), MixedSolventElectrolyte::getPartialMolarEnthalpies(), PhaseCombo_Interaction::getPartialMolarEnthalpies(), IdealMolalSoln::getPartialMolarEnthalpies(), DebyeHuckel::getPartialMolarEnthalpies(), HMWSoln::getPartialMolarEnthalpies(), SurfPhase::getPartialMolarEntropies(), IdealSolnGasVPSS::getPartialMolarEntropies(), MolarityIonicVPSSTP::getPartialMolarEntropies(), IonsFromNeutralVPSSTP::getPartialMolarEntropies(), RedlichKwongMFTP::getPartialMolarEntropies(), RedlichKisterVPSSTP::getPartialMolarEntropies(), MargulesVPSSTP::getPartialMolarEntropies(), MixedSolventElectrolyte::getPartialMolarEntropies(), PhaseCombo_Interaction::getPartialMolarEntropies(), IdealGasPhase::getPartialMolarEntropies(), IdealMolalSoln::getPartialMolarEntropies(), IdealSolidSolnPhase::getPartialMolarEntropies(), LatticePhase::getPartialMolarEntropies(), DebyeHuckel::getPartialMolarEntropies(), HMWSoln::getPartialMolarEntropies(), IdealSolnGasVPSS::getPartialMolarIntEnergies(), RedlichKwongMFTP::getPartialMolarIntEnergies(), IdealGasPhase::getPartialMolarIntEnergies(), MolarityIonicVPSSTP::getPartialMolarVolumes(), RedlichKwongMFTP::getPartialMolarVolumes(), RedlichKisterVPSSTP::getPartialMolarVolumes(), MargulesVPSSTP::getPartialMolarVolumes(), MixedSolventElectrolyte::getPartialMolarVolumes(), IdealGasPhase::getPartialMolarVolumes(), PhaseCombo_Interaction::getPartialMolarVolumes(), DebyeHuckel::getPartialMolarVolumes(), HMWSoln::getPartialMolarVolumes(), MixtureFugacityTP::getPureGibbs(), IdealGasPhase::getPureGibbs(), LatticePhase::getPureGibbs(), IdealSolidSolnPhase::getPureGibbs(), ThermoPhase::getReferenceComposition(), VPStandardStateTP::getStandardChemPotentials(), MixtureFugacityTP::getStandardChemPotentials(), IdealGasPhase::getStandardChemPotentials(), MixtureFugacityTP::getStandardVolumes(), SurfPhase::getStandardVolumes(), IdealGasPhase::getStandardVolumes(), MixtureFugacityTP::getStandardVolumes_ref(), IdealGasPhase::getStandardVolumes_ref(), HMWSoln::getUnscaledMolalityActivityCoefficients(), HMWSoln::HMWSoln(), Phase::init(), PseudoBinaryVPSSTP::initLengths(), IdealSolnGasVPSS::initLengths(), MolarityIonicVPSSTP::initLengths(), GibbsExcessVPSSTP::initLengths(), RedlichKwongMFTP::initLengths(), VPStandardStateTP::initLengths(), LatticeSolidPhase::initLengths(), IonsFromNeutralVPSSTP::initLengths(), MixtureFugacityTP::initLengths(), PhaseCombo_Interaction::initLengths(), RedlichKisterVPSSTP::initLengths(), MargulesVPSSTP::initLengths(), MixedSolventElectrolyte::initLengths(), MolalityVPSSTP::initLengths(), IdealMolalSoln::initLengths(), IdealSolidSolnPhase::initLengths(), DebyeHuckel::initLengths(), HMWSoln::initLengths(), ConstDensityThermo::initThermo(), SurfPhase::initThermo(), MolarityIonicVPSSTP::initThermo(), StoichSubstanceSSTP::initThermo(), VPStandardStateTP::initThermo(), LatticeSolidPhase::initThermo(), SingleSpeciesTP::initThermo(), IdealGasPhase::initThermo(), LatticePhase::initThermo(), ThermoPhase::initThermo(), RedlichKwongMFTP::initThermoXML(), VPStandardStateTP::initThermoXML(), IonsFromNeutralVPSSTP::initThermoXML(), IdealMolalSoln::initThermoXML(), LatticePhase::initThermoXML(), IdealSolidSolnPhase::initThermoXML(), DebyeHuckel::initThermoXML(), IdealSolidSolnPhase::logStandardConc(), Phase::nSpecies(), VPStandardStateTP::operator=(), Phase::operator=(), ThermoPhase::operator=(), MolalityVPSSTP::osmoticCoefficient(), HMWSoln::printCoeffs(), RedlichKwongMFTP::readXMLCrossFluid(), RedlichKwongMFTP::readXMLPureFluid(), IdealSolidSolnPhase::referenceConcentration(), HMWSoln::relative_enthalpy(), HMWSoln::relative_molal_enthalpy(), DebyeHuckel::s_update_d2lnMolalityActCoeff_dT2(), HMWSoln::s_update_d2lnMolalityActCoeff_dT2(), IonsFromNeutralVPSSTP::s_update_dlnActCoeff_dlnN(), PhaseCombo_Interaction::s_update_dlnActCoeff_dlnN(), MargulesVPSSTP::s_update_dlnActCoeff_dlnN(), MixedSolventElectrolyte::s_update_dlnActCoeff_dlnN(), IonsFromNeutralVPSSTP::s_update_dlnActCoeff_dlnN_diag(), PhaseCombo_Interaction::s_update_dlnActCoeff_dlnN_diag(), MargulesVPSSTP::s_update_dlnActCoeff_dlnN_diag(), MixedSolventElectrolyte::s_update_dlnActCoeff_dlnN_diag(), IonsFromNeutralVPSSTP::s_update_dlnActCoeff_dlnX_diag(), PhaseCombo_Interaction::s_update_dlnActCoeff_dlnX_diag(), MargulesVPSSTP::s_update_dlnActCoeff_dlnX_diag(), MixedSolventElectrolyte::s_update_dlnActCoeff_dlnX_diag(), PhaseCombo_Interaction::s_update_dlnActCoeff_dT(), RedlichKisterVPSSTP::s_update_dlnActCoeff_dT(), MargulesVPSSTP::s_update_dlnActCoeff_dT(), MixedSolventElectrolyte::s_update_dlnActCoeff_dT(), RedlichKisterVPSSTP::s_update_dlnActCoeff_dX_(), IonsFromNeutralVPSSTP::s_update_dlnActCoeffdT(), DebyeHuckel::s_update_dlnMolalityActCoeff_dP(), HMWSoln::s_update_dlnMolalityActCoeff_dP(), DebyeHuckel::s_update_dlnMolalityActCoeff_dT(), HMWSoln::s_update_dlnMolalityActCoeff_dT(), MolarityIonicVPSSTP::s_update_lnActCoeff(), IonsFromNeutralVPSSTP::s_update_lnActCoeff(), PhaseCombo_Interaction::s_update_lnActCoeff(), RedlichKisterVPSSTP::s_update_lnActCoeff(), MargulesVPSSTP::s_update_lnActCoeff(), MixedSolventElectrolyte::s_update_lnActCoeff(), DebyeHuckel::s_update_lnMolalityActCoeff(), HMWSoln::s_update_lnMolalityActCoeff(), IdealMolalSoln::s_updateIMS_lnMolalityActCoeff(), HMWSoln::s_updateIMS_lnMolalityActCoeff(), HMWSoln::s_updatePitzer_CoeffWRTemp(), HMWSoln::s_updatePitzer_d2lnMolalityActCoeff_dT2(), HMWSoln::s_updatePitzer_dlnMolalityActCoeff_dP(), HMWSoln::s_updatePitzer_dlnMolalityActCoeff_dT(), HMWSoln::s_updatePitzer_lnMolalityActCoeff(), HMWSoln::s_updateScaling_pHScaling(), HMWSoln::s_updateScaling_pHScaling_dP(), HMWSoln::s_updateScaling_pHScaling_dT(), HMWSoln::s_updateScaling_pHScaling_dT2(), Phase::setConcentrations(), SurfPhase::setCoverages(), SurfPhase::setCoveragesNoNorm(), Phase::setMassFractions(), Phase::setMassFractions_NoNorm(), MolalityVPSSTP::setMolalities(), Phase::setMoleFractions(), Phase::setMoleFractions_NoNorm(), ThermoPhase::setReferenceComposition(), MolalityVPSSTP::setSolvent(), IdealSolnGasVPSS::setToEquilState(), RedlichKwongMFTP::setToEquilState(), IdealGasPhase::setToEquilState(), IdealSolidSolnPhase::setToEquilState(), ThermoPhase::speciesData(), Phase::speciesIndex(), IdealSolidSolnPhase::standardConcentration(), RedlichKwongMFTP::updateAB(), and ThermoPhase::~ThermoPhase().

size_t m_ndim
protectedinherited

Dimensionality of the phase.

Volumetric phases have dimensionality 3 and surface phases have dimensionality 2.

Definition at line 731 of file Phase.h.

Referenced by Phase::nDim(), Phase::operator=(), and Phase::setNDim().

vector_fp m_speciesComp
protectedinherited

Atomic composition of the species.

The number of atoms of element i in species k is equal to m_speciesComp[k * m_mm + i] The length of this vector is equal to m_kk * m_mm

Definition at line 736 of file Phase.h.

Referenced by Phase::addUniqueElementAfterFreeze(), Phase::addUniqueSpecies(), Phase::getAtoms(), LatticeSolidPhase::installSlavePhases(), Phase::nAtoms(), and Phase::operator=().

vector_fp m_speciesSize
protectedinherited

Vector of species sizes.

length m_kk. Used in some equations of state which employ the constant partial molar volume approximation.

Definition at line 740 of file Phase.h.

Referenced by Phase::addUniqueSpecies(), DebyeHuckel::initLengths(), HMWSoln::initLengths(), MineralEQ3::initThermoXML(), DebyeHuckel::initThermoXML(), Phase::operator=(), Phase::size(), HMWSoln::speciesMolarVolume(), and DebyeHuckel::standardConcentration().

vector_fp m_speciesCharge
protectedinherited
vector_fp m_grt
protectedinherited
std::vector<size_t> m_revindex
protectedinherited

List of reactions numbers which are reversible reactions.

This is a vector of reaction numbers. Each reaction in the list is reversible. Length = number of reversible reactions

Definition at line 655 of file InterfaceKinetics.h.

Referenced by InterfaceKinetics::isReversible(), InterfaceKinetics::operator=(), and InterfaceKinetics::updateKc().

Rate1<SurfaceArrhenius> m_rates
protectedinherited

Templated class containing the vector of reactions for this interface.

The templated class is described in RateCoeffMgr.h The class SurfaceArrhenius is described in RxnRates.h

Definition at line 662 of file InterfaceKinetics.h.

Referenced by InterfaceKinetics::_update_rates_T(), and InterfaceKinetics::operator=().

std::map<size_t, std::pair<int, size_t> > m_index
mutableprotectedinherited

Vector of information about reactions in the mechanism.

The key is the reaction index (0 < i < m_ii). The first pair is the reactionType of the reaction. The second pair is ...

Definition at line 673 of file InterfaceKinetics.h.

Referenced by InterfaceKinetics::operator=(), InterfaceKinetics::reactionType(), and InterfaceKinetics::registerReaction().

std::vector<size_t> m_irrev
protectedinherited

Vector of irreversible reaction numbers.

vector containing the reaction numbers of irreversible reactions.

Definition at line 680 of file InterfaceKinetics.h.

Referenced by InterfaceKinetics::operator=(), and InterfaceKinetics::updateKc().

ReactionStoichMgr m_rxnstoich
protectedinherited
size_t m_nirrev
protectedinherited

Number of irreversible reactions in the mechanism.

Definition at line 692 of file InterfaceKinetics.h.

Referenced by InterfaceKinetics::operator=(), and InterfaceKinetics::updateKc().

size_t m_nrev
protectedinherited

Number of reversible reactions in the mechanism.

Definition at line 695 of file InterfaceKinetics.h.

Referenced by InterfaceKinetics::operator=(), and InterfaceKinetics::updateKc().

std::vector<std::map<size_t, doublereal> > m_rrxn
mutableprotectedinherited

m_rrxn is a vector of maps, containing the reactant stoichiometric coefficient information

m_rrxn has a length equal to the total number of species in the kinetics object. For each species, there exists a map, with the reaction number being the key, and the reactant stoichiometric coefficient for the species being the value. HKM -> mutable because search sometimes creates extra entries. To be fixed in future...

Definition at line 709 of file