Cantera
3.0.0
|
This is the complete list of members for RedlichKwongMFTP, including all inherited members.
_updateReferenceStateThermo() const | MixtureFugacityTP | protectedvirtual |
a_coeff_vec (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
a_vec_Curr_ (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
activityConvention() const | ThermoPhase | virtual |
addElement(const string &symbol, double weight=-12345.0, int atomicNumber=0, double entropy298=ENTROPY298_UNKNOWN, int elem_type=CT_ELEM_TYPE_ABSPOS) | Phase | |
addSpecies(shared_ptr< Species > spec) override | RedlichKwongMFTP | virtual |
addSpeciesAlias(const string &name, const string &alias) | Phase | |
addUndefinedElements() | Phase | |
assertCompressible(const string &setter) const | Phase | inlineprotected |
assignDensity(const double density_) | Phase | protected |
atomicNumber(size_t m) const | Phase | |
atomicWeight(size_t m) const | Phase | |
atomicWeights() const | Phase | |
b_vec_Curr_ (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
calcCriticalConditions(double &pc, double &tc, double &vc) const override (defined in RedlichKwongMFTP) | RedlichKwongMFTP | virtual |
calculateAB(double temp, double &aCalc, double &bCalc) const | RedlichKwongMFTP | |
calculatePsat(double TKelvin, double &molarVolGas, double &molarVolLiquid) | MixtureFugacityTP | |
caseSensitiveSpecies() const | Phase | inline |
changeElementType(int m, int elem_type) | Phase | |
charge(size_t k) const | Phase | inline |
chargeDensity() const | Phase | |
chargeNeutralityNecessary() const | ThermoPhase | inline |
checkElementArraySize(size_t mm) const | Phase | |
checkElementIndex(size_t m) const | Phase | |
checkSpeciesArraySize(size_t kk) const | Phase | |
checkSpeciesIndex(size_t k) const | Phase | |
CoeffSource enum name (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
compatibleWithMultiPhase() const | ThermoPhase | inlinevirtual |
compositionChanged() override | MixtureFugacityTP | protectedvirtual |
concentration(const size_t k) const | Phase | virtual |
corr0(double TKelvin, double pres, double &densLiq, double &densGas, double &liqGRT, double &gasGRT) | MixtureFugacityTP | protected |
cp_mass() const | ThermoPhase | inline |
cp_mole() const override | RedlichKwongMFTP | virtual |
critCompressibility() const override | MixtureFugacityTP | protectedvirtual |
critDensity() const override | MixtureFugacityTP | protectedvirtual |
critPressure() const override | MixtureFugacityTP | protectedvirtual |
critTemperature() const override | MixtureFugacityTP | protectedvirtual |
critVolume() const override | MixtureFugacityTP | protectedvirtual |
cv_mass() const | ThermoPhase | inline |
cv_mole() const override | RedlichKwongMFTP | virtual |
da_dt() const (defined in RedlichKwongMFTP) | RedlichKwongMFTP | |
density() const | Phase | inlinevirtual |
densityCalc(double T, double pressure, int phase, double rhoguess) override | RedlichKwongMFTP | virtual |
densSpinodalGas() const override | RedlichKwongMFTP | virtual |
densSpinodalLiquid() const override | RedlichKwongMFTP | virtual |
dpdni_ | RedlichKwongMFTP | mutableprotected |
dpdT_ | RedlichKwongMFTP | mutableprotected |
dpdV_ | RedlichKwongMFTP | mutableprotected |
dpdVCalc(double TKelvin, double molarVol, double &presCalc) const override | RedlichKwongMFTP | virtual |
electricPotential() const | ThermoPhase | inline |
electronTemperature() const | Phase | inlinevirtual |
elementalMassFraction(const size_t m) const | Phase | |
elementalMoleFraction(const size_t m) const | Phase | |
elementIndex(const string &name) const | Phase | |
elementName(size_t m) const | Phase | |
elementNames() const | Phase | |
elementType(size_t m) const | Phase | |
enthalpy_mass() const | ThermoPhase | inline |
enthalpy_mole() const override | MixtureFugacityTP | virtual |
entropy_mass() const | ThermoPhase | inline |
entropy_mole() const override | MixtureFugacityTP | virtual |
entropyElement298(size_t m) const | Phase | |
equilibrate(const string &XY, const string &solver="auto", double rtol=1e-9, int max_steps=50000, int max_iter=100, int estimate_equil=0, int log_level=0) | ThermoPhase | |
equivalenceRatio(const double *fuelComp, const double *oxComp, ThermoBasis basis=ThermoBasis::molar) const | ThermoPhase | |
equivalenceRatio(const string &fuelComp, const string &oxComp, ThermoBasis basis=ThermoBasis::molar) const | ThermoPhase | |
equivalenceRatio(const Composition &fuelComp, const Composition &oxComp, ThermoBasis basis=ThermoBasis::molar) const | ThermoPhase | |
equivalenceRatio() const | ThermoPhase | |
findIsomers(const Composition &compMap) const | Phase | virtual |
findIsomers(const string &comp) const | Phase | virtual |
findSpeciesLower(const string &nameStr) const | Phase | private |
forcedSolutionBranch() const | MixtureFugacityTP | |
forcedState_ | MixtureFugacityTP | protected |
fullStates() const | Phase | virtual |
getActivities(double *a) const | ThermoPhase | virtual |
getActivityCoefficients(double *ac) const override | RedlichKwongMFTP | virtual |
getActivityConcentrations(double *c) const override | MixtureFugacityTP | virtual |
getAtoms(size_t k, double *atomArray) const | Phase | |
getCharges(double *charges) const | Phase | |
getChemPotentials(double *mu) const override | RedlichKwongMFTP | virtual |
getChemPotentials_RT(double *mu) const override | RedlichKwongMFTP | virtual |
getCompositionFromMap(const Composition &comp) const | Phase | |
getConcentrations(double *const c) const | Phase | virtual |
getCp_R(double *cpr) const override | MixtureFugacityTP | virtual |
getCp_R_ref(double *cprt) const override | MixtureFugacityTP | virtual |
getCsvReportData(vector< string > &names, vector< vector< double > > &data) const | ThermoPhase | protectedvirtual |
getdlnActCoeffdlnN(const size_t ld, double *const dlnActCoeffdlnN) | ThermoPhase | virtual |
getdlnActCoeffdlnN_diag(double *dlnActCoeffdlnN_diag) const | ThermoPhase | inlinevirtual |
getdlnActCoeffdlnN_numderiv(const size_t ld, double *const dlnActCoeffdlnN) (defined in ThermoPhase) | ThermoPhase | virtual |
getdlnActCoeffdlnX_diag(double *dlnActCoeffdlnX_diag) const | ThermoPhase | inlinevirtual |
getdlnActCoeffds(const double dTds, const double *const dXds, double *dlnActCoeffds) const | ThermoPhase | inlinevirtual |
getElectrochemPotentials(double *mu) const | ThermoPhase | |
getEnthalpy_RT(double *hrt) const override | MixtureFugacityTP | virtual |
getEnthalpy_RT_ref(double *hrt) const override | MixtureFugacityTP | virtual |
getEntropy_R(double *sr) const override | MixtureFugacityTP | virtual |
getEntropy_R_ref(double *er) const override | MixtureFugacityTP | virtual |
getGibbs_ref(double *g) const override | MixtureFugacityTP | virtual |
getGibbs_RT(double *grt) const override | MixtureFugacityTP | virtual |
getGibbs_RT_ref(double *grt) const override | MixtureFugacityTP | virtual |
getIntEnergy_RT(double *urt) const override | MixtureFugacityTP | virtual |
getIntEnergy_RT_ref(double *urt) const | ThermoPhase | inlinevirtual |
getLnActivityCoefficients(double *lnac) const | ThermoPhase | virtual |
getMassFractions(double *const y) const | Phase | |
getMassFractionsByName(double threshold=0.0) const | Phase | |
getMolecularWeights(vector< double > &weights) const | Phase | |
getMolecularWeights(double *weights) const | Phase | |
getMoleFractions(double *const x) const | Phase | |
getMoleFractionsByName(double threshold=0.0) const | Phase | |
getParameters(AnyMap &phaseNode) const | ThermoPhase | protectedvirtual |
getPartialMolarCp(double *cpbar) const override | RedlichKwongMFTP | inlinevirtual |
getPartialMolarEnthalpies(double *hbar) const override | RedlichKwongMFTP | virtual |
getPartialMolarEntropies(double *sbar) const override | RedlichKwongMFTP | virtual |
getPartialMolarIntEnergies(double *ubar) const override | RedlichKwongMFTP | virtual |
getPartialMolarVolumes(double *vbar) const override | RedlichKwongMFTP | virtual |
getPureGibbs(double *gpure) const override | MixtureFugacityTP | virtual |
getSpeciesParameters(const string &name, AnyMap &speciesNode) const override | RedlichKwongMFTP | virtual |
getStandardChemPotentials(double *mu) const override | MixtureFugacityTP | virtual |
getStandardVolumes(double *vol) const override | MixtureFugacityTP | virtual |
getStandardVolumes_ref(double *vol) const override | MixtureFugacityTP | virtual |
gibbs_mass() const | ThermoPhase | inline |
gibbs_mole() const | ThermoPhase | inlinevirtual |
gibbs_RT_ref() const | MixtureFugacityTP | protected |
hasPhaseTransition() const | Phase | inlinevirtual |
Hf298SS(const size_t k) const | ThermoPhase | inline |
hresid() const override | RedlichKwongMFTP | protectedvirtual |
ignoreUndefinedElements() | Phase | |
initThermo() override | RedlichKwongMFTP | virtual |
initThermoFile(const string &inputFile, const string &id) | ThermoPhase | |
input() const | ThermoPhase | |
input() (defined in ThermoPhase) | ThermoPhase | |
intEnergy_mass() const | ThermoPhase | inline |
intEnergy_mole() const | ThermoPhase | inlinevirtual |
invalidateCache() override | ThermoPhase | virtual |
inverseMolecularWeights() const | Phase | |
isCompressible() const | Phase | inlinevirtual |
isIdeal() const | ThermoPhase | inlinevirtual |
isothermalCompressibility() const override | RedlichKwongMFTP | virtual |
isPure() const | Phase | inlinevirtual |
iState_ | MixtureFugacityTP | protected |
liquidVolEst(double TKelvin, double &pres) const override | RedlichKwongMFTP | virtual |
logStandardConc(size_t k=0) const | ThermoPhase | virtual |
m_a_current | RedlichKwongMFTP | protected |
m_atomicNumbers | Phase | private |
m_atomicWeights | Phase | private |
m_b_current | RedlichKwongMFTP | protected |
m_binaryParameters | RedlichKwongMFTP | protected |
m_cache | Phase | mutableprotected |
m_caseSensitiveSpecies | Phase | protected |
m_chargeNeutralityNecessary | ThermoPhase | protected |
m_coeffSource | RedlichKwongMFTP | protected |
m_cp0_R | MixtureFugacityTP | mutableprotected |
m_dens | Phase | private |
m_elem_type | Phase | private |
m_elementNames | Phase | private |
m_entropy298 | Phase | private |
m_formTempParam | RedlichKwongMFTP | protected |
m_g0_RT | MixtureFugacityTP | mutableprotected |
m_h0_RT | MixtureFugacityTP | mutableprotected |
m_input | ThermoPhase | protected |
m_kk | Phase | protected |
m_mm | Phase | private |
m_mmw | Phase | private |
m_molwts | Phase | private |
m_name | Phase | private |
m_ndim | Phase | protected |
m_partialMolarVolumes (defined in RedlichKwongMFTP) | RedlichKwongMFTP | mutableprotected |
m_phi | ThermoPhase | protected |
m_pp | RedlichKwongMFTP | mutableprotected |
m_rmolwts | Phase | private |
m_s0_R | MixtureFugacityTP | mutableprotected |
m_species (defined in Phase) | Phase | protected |
m_speciesCharge | Phase | protected |
m_speciesComp | Phase | protected |
m_speciesIndices | Phase | private |
m_speciesLower | Phase | private |
m_speciesNames | Phase | private |
m_spthermo | ThermoPhase | protected |
m_ssConvention | ThermoPhase | protected |
m_stateNum | Phase | private |
m_temp | Phase | private |
m_tlast | ThermoPhase | mutableprotected |
m_tmpV | MixtureFugacityTP | mutableprotected |
m_undefinedElementBehavior | Phase | protected |
m_y | Phase | mutableprivate |
m_ym | Phase | mutableprivate |
massFraction(size_t k) const | Phase | |
massFraction(const string &name) const | Phase | |
massFractions() const | Phase | inline |
massFractionsToMoleFractions(const double *Y, double *X) const | Phase | |
maxTemp(size_t k=npos) const | ThermoPhase | inlinevirtual |
mean_X(const double *const Q) const | Phase | |
mean_X(const vector< double > &Q) const | Phase | |
meanMolecularWeight() const | Phase | inline |
minTemp(size_t k=npos) const | ThermoPhase | inlinevirtual |
mixtureFraction(const double *fuelComp, const double *oxComp, ThermoBasis basis=ThermoBasis::molar, const string &element="Bilger") const | ThermoPhase | |
mixtureFraction(const string &fuelComp, const string &oxComp, ThermoBasis basis=ThermoBasis::molar, const string &element="Bilger") const | ThermoPhase | |
mixtureFraction(const Composition &fuelComp, const Composition &oxComp, ThermoBasis basis=ThermoBasis::molar, const string &element="Bilger") const | ThermoPhase | |
MixtureFugacityTP()=default | MixtureFugacityTP | |
modifyOneHf298SS(const size_t k, const double Hf298New) | ThermoPhase | inlinevirtual |
modifySpecies(size_t k, shared_ptr< Species > spec) override | ThermoPhase | virtual |
molarDensity() const | Phase | virtual |
molarVolume() const | Phase | virtual |
molecularWeight(size_t k) const | Phase | |
molecularWeights() const | Phase | |
moleFractdivMMW() const | Phase | |
moleFraction(size_t k) const | Phase | |
moleFraction(const string &name) const | Phase | |
moleFractions_ | MixtureFugacityTP | protected |
moleFractionsToMassFractions(const double *X, double *Y) const | Phase | |
name() const | Phase | |
nativeMode() const | Phase | |
nativeState() const | Phase | virtual |
nAtoms(size_t k, size_t m) const | Phase | |
nDim() const | Phase | inline |
nElements() const | Phase | |
NSolns_ (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
nSpecies() const | Phase | inline |
o2Present(const double *y) const | ThermoPhase | private |
o2Required(const double *y) const | ThermoPhase | private |
omega_a | RedlichKwongMFTP | privatestatic |
omega_b | RedlichKwongMFTP | privatestatic |
omega_vc | RedlichKwongMFTP | privatestatic |
operator=(const Phase &)=delete (defined in Phase) | Phase | |
parameters(bool withInput=true) const | ThermoPhase | |
partialStates() const | Phase | virtual |
Phase()=default | Phase | |
Phase(const Phase &)=delete (defined in Phase) | Phase | |
phaseOfMatter() const | ThermoPhase | inlinevirtual |
phaseState(bool checkState=false) const | MixtureFugacityTP | |
pressure() const override | RedlichKwongMFTP | virtual |
pressureDerivatives() const | RedlichKwongMFTP | |
psatEst(double TKelvin) const | MixtureFugacityTP | protectedvirtual |
ready() const | Phase | virtual |
RedlichKwongMFTP(const string &infile="", const string &id="") | RedlichKwongMFTP | explicit |
refPressure() const | ThermoPhase | inlinevirtual |
report(bool show_thermo=true, double threshold=-1e-14) const | ThermoPhase | virtual |
reportCSV(std::ofstream &csvFile) const | ThermoPhase | virtual |
reportSolnBranchActual() const | MixtureFugacityTP | |
resetHf298(const size_t k=npos) | ThermoPhase | virtual |
restoreState(const vector< double > &state) | Phase | |
restoreState(size_t lenstate, const double *state) | Phase | virtual |
RT() const | ThermoPhase | inline |
satPressure(double TKelvin) override | MixtureFugacityTP | virtual |
satTemperature(double p) const | ThermoPhase | inlinevirtual |
saveState(vector< double > &state) const | Phase | |
saveState(size_t lenstate, double *state) const | Phase | virtual |
setBinaryCoeffs(const string &species_i, const string &species_j, double a0, double a1) | RedlichKwongMFTP | |
setCaseSensitiveSpecies(bool cflag=true) | Phase | inline |
setConcentrations(const double *const conc) | Phase | virtual |
setConcentrationsNoNorm(const double *const conc) | Phase | virtual |
setDensity(const double density_) | Phase | virtual |
setElectricPotential(double v) | ThermoPhase | inline |
setElectronTemperature(double etemp) | Phase | inlinevirtual |
setEquivalenceRatio(double phi, const double *fuelComp, const double *oxComp, ThermoBasis basis=ThermoBasis::molar) | ThermoPhase | |
setEquivalenceRatio(double phi, const string &fuelComp, const string &oxComp, ThermoBasis basis=ThermoBasis::molar) | ThermoPhase | |
setEquivalenceRatio(double phi, const Composition &fuelComp, const Composition &oxComp, ThermoBasis basis=ThermoBasis::molar) | ThermoPhase | |
setForcedSolutionBranch(int solnBranch) | MixtureFugacityTP | |
setMassFractions(const double *const y) | Phase | virtual |
setMassFractions_NoNorm(const double *const y) | Phase | virtual |
setMassFractionsByName(const Composition &yMap) | Phase | |
setMassFractionsByName(const string &x) | Phase | |
setMixtureFraction(double mixFrac, const double *fuelComp, const double *oxComp, ThermoBasis basis=ThermoBasis::molar) | ThermoPhase | |
setMixtureFraction(double mixFrac, const string &fuelComp, const string &oxComp, ThermoBasis basis=ThermoBasis::molar) | ThermoPhase | |
setMixtureFraction(double mixFrac, const Composition &fuelComp, const Composition &oxComp, ThermoBasis basis=ThermoBasis::molar) | ThermoPhase | |
setMolarDensity(const double molarDensity) | Phase | virtual |
setMolecularWeight(const int k, const double mw) | Phase | protected |
setMoleFractions(const double *const x) | Phase | virtual |
setMoleFractions_NoNorm(const double *const x) | Phase | virtual |
setMoleFractionsByName(const Composition &xMap) | Phase | |
setMoleFractionsByName(const string &x) | Phase | |
setMolesNoTruncate(const double *const N) | Phase | virtual |
setName(const string &nm) | Phase | |
setNDim(size_t ndim) | Phase | inline |
setParameters(const AnyMap &phaseNode, const AnyMap &rootNode=AnyMap()) | ThermoPhase | virtual |
setPressure(double p) override | MixtureFugacityTP | virtual |
setSpeciesCoeffs(const string &species, double a0, double a1, double b) | RedlichKwongMFTP | |
setState(const AnyMap &state) | ThermoPhase | virtual |
setState_conditional_TP(double t, double p, bool set_p) | ThermoPhase | private |
setState_DP(double rho, double p) | ThermoPhase | inlinevirtual |
setState_HP(double h, double p, double tol=1e-9) | ThermoPhase | virtual |
setState_HPorUV(double h, double p, double tol=1e-9, bool doUV=false) | ThermoPhase | private |
setState_Psat(double p, double x) | ThermoPhase | inlinevirtual |
setState_PV(double p, double v, double tol=1e-9) | ThermoPhase | inlinevirtual |
setState_PX(double p, double *x) | ThermoPhase | virtual |
setState_PY(double p, double *y) | ThermoPhase | virtual |
setState_RP(double rho, double p) | ThermoPhase | |
setState_RPX(double rho, double p, const double *x) | ThermoPhase | virtual |
setState_RPX(double rho, double p, const Composition &x) | ThermoPhase | virtual |
setState_RPX(double rho, double p, const string &x) | ThermoPhase | virtual |
setState_RPY(double rho, double p, const double *y) | ThermoPhase | virtual |
setState_RPY(double rho, double p, const Composition &y) | ThermoPhase | virtual |
setState_RPY(double rho, double p, const string &y) | ThermoPhase | virtual |
setState_RX(double rho, double *x) | Phase | |
setState_RY(double rho, double *y) | Phase | |
setState_SH(double s, double h, double tol=1e-9) | ThermoPhase | inlinevirtual |
setState_SP(double s, double p, double tol=1e-9) | ThermoPhase | virtual |
setState_SPorSV(double s, double p, double tol=1e-9, bool doSV=false) | ThermoPhase | private |
setState_ST(double s, double t, double tol=1e-9) | ThermoPhase | inlinevirtual |
setState_SV(double s, double v, double tol=1e-9) | ThermoPhase | virtual |
setState_TD(double t, double rho) | Phase | |
setState_TH(double t, double h, double tol=1e-9) | ThermoPhase | inlinevirtual |
setState_TNX(double t, double n, const double *x) | Phase | |
setState_TP(double t, double p) | ThermoPhase | virtual |
setState_TPQ(double T, double P, double Q) | ThermoPhase | |
setState_TPX(double t, double p, const double *x) | ThermoPhase | virtual |
setState_TPX(double t, double p, const Composition &x) | ThermoPhase | virtual |
setState_TPX(double t, double p, const string &x) | ThermoPhase | virtual |
setState_TPY(double t, double p, const double *y) | ThermoPhase | virtual |
setState_TPY(double t, double p, const Composition &y) | ThermoPhase | virtual |
setState_TPY(double t, double p, const string &y) | ThermoPhase | virtual |
setState_TR(double t, double rho) | Phase | |
setState_TRX(double t, double dens, const double *x) | Phase | |
setState_TRX(double t, double dens, const Composition &x) | Phase | |
setState_TRY(double t, double dens, const double *y) | Phase | |
setState_TRY(double t, double dens, const Composition &y) | Phase | |
setState_Tsat(double t, double x) | ThermoPhase | inlinevirtual |
setState_TV(double t, double v, double tol=1e-9) | ThermoPhase | inlinevirtual |
setState_TX(double t, double *x) | Phase | |
setState_TY(double t, double *y) | Phase | |
setState_UP(double u, double p, double tol=1e-9) | ThermoPhase | inlinevirtual |
setState_UV(double u, double v, double tol=1e-9) | ThermoPhase | virtual |
setState_VH(double v, double h, double tol=1e-9) | ThermoPhase | inlinevirtual |
setTemperature(const double temp) override | MixtureFugacityTP | virtual |
setToEquilState(const double *mu_RT) | ThermoPhase | inlinevirtual |
solveCubic(double T, double pres, double a, double b, double Vroot[3]) const | RedlichKwongMFTP | |
Cantera::MixtureFugacityTP::solveCubic(double T, double pres, double a, double b, double aAlpha, double Vroot[3], double an, double bn, double cn, double dn, double tc, double vc) const | MixtureFugacityTP | protected |
soundSpeed() const override | RedlichKwongMFTP | virtual |
species(const string &name) const | Phase | |
species(size_t k) const | Phase | |
speciesIndex(const string &name) const | Phase | |
speciesName(size_t k) const | Phase | |
speciesNames() const | Phase | |
speciesSPName(int k) const | Phase | |
speciesThermo(int k=-1) | ThermoPhase | virtual |
speciesThermo(int k=-1) const (defined in ThermoPhase) | ThermoPhase | virtual |
sresid() const override | RedlichKwongMFTP | protectedvirtual |
standardConcentration(size_t k=0) const override | RedlichKwongMFTP | virtual |
standardConcentrationUnits() const | ThermoPhase | virtual |
standardStateConvention() const override | MixtureFugacityTP | virtual |
stateMFNumber() const | Phase | inline |
stateSize() const | Phase | virtual |
stoichAirFuelRatio(const double *fuelComp, const double *oxComp, ThermoBasis basis=ThermoBasis::molar) const | ThermoPhase | |
stoichAirFuelRatio(const string &fuelComp, const string &oxComp, ThermoBasis basis=ThermoBasis::molar) const | ThermoPhase | |
stoichAirFuelRatio(const Composition &fuelComp, const Composition &oxComp, ThermoBasis basis=ThermoBasis::molar) const | ThermoPhase | |
sum_xlogx() const | Phase | |
temperature() const | Phase | inline |
thermalExpansionCoeff() const override | RedlichKwongMFTP | virtual |
ThermoPhase()=default | ThermoPhase | |
throwUndefinedElements() | Phase | |
type() const override | RedlichKwongMFTP | inlinevirtual |
updateMixingExpressions() override | RedlichKwongMFTP | virtual |
vaporFraction() const | ThermoPhase | inlinevirtual |
Vroot_ (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
z() const | MixtureFugacityTP | protected |
~Phase()=default (defined in Phase) | Phase | virtual |