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RedlichKwongMFTP Member List

This is the complete list of members for RedlichKwongMFTP, including all inherited members.

_RT() const ThermoPhaseinline
_updateReferenceStateThermo() const MixtureFugacityTPprotectedvirtual
a_coeff_vec (defined in RedlichKwongMFTP)RedlichKwongMFTPprotected
a_vec_Curr_ (defined in RedlichKwongMFTP)RedlichKwongMFTPprotected
activityConvention() const ThermoPhasevirtual
addElement(const std::string &symbol, doublereal weight=-12345.0, int atomicNumber=0, doublereal entropy298=ENTROPY298_UNKNOWN, int elem_type=CT_ELEM_TYPE_ABSPOS)Phase
addElement(const XML_Node &e)Phase
addElementsFromXML(const XML_Node &phase)Phase
addSpecies(shared_ptr< Species > spec)ThermoPhasevirtual
Cantera::Phase::addSpecies(const std::string &name, const doublereal *comp, doublereal charge=0.0, doublereal size=1.0)Phase
addUndefinedElements()Phase
addUniqueElement(const std::string &symbol, doublereal weight=-12345.0, int atomicNumber=0, doublereal entropy298=ENTROPY298_UNKNOWN, int elem_type=CT_ELEM_TYPE_ABSPOS)Phase
addUniqueElement(const XML_Node &e)Phase
addUniqueElementAfterFreeze(const std::string &symbol, doublereal weight, int atomicNumber, doublereal entropy298=ENTROPY298_UNKNOWN, int elem_type=CT_ELEM_TYPE_ABSPOS)Phase
addUniqueSpecies(const std::string &name, const doublereal *comp, doublereal charge=0.0, doublereal size=1.0)Phase
applyStandardMixingRules()RedlichKwongMFTPprivate
atomicNumber(size_t m) const Phase
atomicWeight(size_t m) const Phase
atomicWeights() const Phase
b_vec_Curr_ (defined in RedlichKwongMFTP)RedlichKwongMFTPprotected
calcCriticalConditions(doublereal a, doublereal b, doublereal a0_coeff, doublereal aT_coeff, doublereal &pc, doublereal &tc, doublereal &vc) const (defined in RedlichKwongMFTP)RedlichKwongMFTP
calcDensity()RedlichKwongMFTPprotectedvirtual
calculateAB(doublereal temp, doublereal &aCalc, doublereal &bCalc) const RedlichKwongMFTP
calculatePsat(doublereal TKelvin, doublereal &molarVolGas, doublereal &molarVolLiquid)MixtureFugacityTP
changeElementType(int m, int elem_type)Phase
charge(size_t k) const Phaseinline
chargeDensity() const Phase
chargeNeutralityNecessary() const ThermoPhaseinline
checkElementArraySize(size_t mm) const Phase
checkElementIndex(size_t m) const Phase
checkSpeciesArraySize(size_t kk) const Phase
checkSpeciesIndex(size_t k) const Phase
concentration(const size_t k) const Phase
corr0(doublereal TKelvin, doublereal pres, doublereal &densLiq, doublereal &densGas, doublereal &liqGRT, doublereal &gasGRT)MixtureFugacityTPprotected
cp_mass() const ThermoPhaseinline
cp_mole() const RedlichKwongMFTPvirtual
critCompressibility() const RedlichKwongMFTPvirtual
critDensity() const RedlichKwongMFTPvirtual
critPressure() const RedlichKwongMFTPvirtual
critTemperature() const RedlichKwongMFTPvirtual
critVolume() const RedlichKwongMFTPvirtual
cv_mass() const ThermoPhaseinline
cv_mole() const RedlichKwongMFTPvirtual
cv_vib(int, double) const ThermoPhaseinlinevirtual
da_dt() const (defined in RedlichKwongMFTP)RedlichKwongMFTP
density() const Phaseinlinevirtual
densityCalc(doublereal TKelvin, doublereal pressure, int phase, doublereal rhoguess)RedlichKwongMFTPvirtual
densSpinodalGas() const RedlichKwongMFTPvirtual
densSpinodalLiquid() const RedlichKwongMFTPvirtual
dpdni_RedlichKwongMFTPmutableprotected
dpdT_RedlichKwongMFTPmutableprotected
dpdV_RedlichKwongMFTPmutableprotected
dpdVCalc(doublereal TKelvin, doublereal molarVol, doublereal &presCalc) const RedlichKwongMFTPvirtual
duplMyselfAsThermoPhase() const RedlichKwongMFTPvirtual
electricPotential() const ThermoPhaseinline
elementalMassFraction(const size_t m) const Phase
elementalMoleFraction(const size_t m) const Phase
elementIndex(const std::string &name) const Phase
elementName(size_t m) const Phase
elementNames() const Phase
elementsFrozen()Phase
elementType(size_t m) const Phase
enthalpy_mass() const ThermoPhaseinline
enthalpy_mole() const RedlichKwongMFTPvirtual
entropy_mass() const ThermoPhaseinline
entropy_mole() const RedlichKwongMFTPvirtual
entropyElement298(size_t m) const Phase
eosType() const RedlichKwongMFTPvirtual
equilibrate(const std::string &XY, const std::string &solver="auto", double rtol=1e-9, int max_steps=50000, int max_iter=100, int estimate_equil=0, int log_level=0)ThermoPhase
fdpdv_ (defined in MixtureFugacityTP)MixtureFugacityTPprotected
forcedSolutionBranch() const MixtureFugacityTPvirtual
forcedState_MixtureFugacityTPprotected
freezeElements()Phase
getActivities(doublereal *a) const ThermoPhasevirtual
getActivityCoefficients(doublereal *ac) const RedlichKwongMFTPvirtual
getActivityConcentrations(doublereal *c) const RedlichKwongMFTPvirtual
getAtoms(size_t k, double *atomArray) const Phase
getChemPotentials(doublereal *mu) const RedlichKwongMFTPvirtual
getChemPotentials_RT(doublereal *mu) const RedlichKwongMFTPvirtual
getConcentrations(doublereal *const c) const Phase
getCp_R(doublereal *cpr) const MixtureFugacityTPvirtual
getCp_R_ref(doublereal *cprt) const MixtureFugacityTPvirtual
getCsvReportData(std::vector< std::string > &names, std::vector< vector_fp > &data) const ThermoPhaseprotectedvirtual
getdlnActCoeffdlnN(const size_t ld, doublereal *const dlnActCoeffdlnN)ThermoPhasevirtual
getdlnActCoeffdlnN_diag(doublereal *dlnActCoeffdlnN_diag) const MixtureFugacityTPinlinevirtual
getdlnActCoeffdlnN_numderiv(const size_t ld, doublereal *const dlnActCoeffdlnN) (defined in ThermoPhase)ThermoPhasevirtual
getdlnActCoeffdlnX_diag(doublereal *dlnActCoeffdlnX_diag) const ThermoPhaseinlinevirtual
getdlnActCoeffds(const doublereal dTds, const doublereal *const dXds, doublereal *dlnActCoeffds) const ThermoPhaseinlinevirtual
getdPartialMolarVolumes_dP(doublereal *d_vbar_dP) const ThermoPhaseinlinevirtual
getdPartialMolarVolumes_dT(doublereal *d_vbar_dT) const ThermoPhaseinlinevirtual
getdStandardVolumes_dP(doublereal *d_vol_dP) const ThermoPhaseinlinevirtual
getdStandardVolumes_dT(doublereal *d_vol_dT) const ThermoPhaseinlinevirtual
getElectrochemPotentials(doublereal *mu) const ThermoPhaseinline
getElementPotentials(doublereal *lambda) const ThermoPhase
getEnthalpy_RT(doublereal *hrt) const MixtureFugacityTPvirtual
getEnthalpy_RT_ref(doublereal *hrt) const MixtureFugacityTPvirtual
getEntropy_R(doublereal *sr) const MixtureFugacityTPvirtual
getEntropy_R_ref(doublereal *er) const MixtureFugacityTPvirtual
getGibbs_ref(doublereal *g) const MixtureFugacityTPvirtual
getGibbs_RT(doublereal *grt) const MixtureFugacityTPvirtual
getGibbs_RT_ref(doublereal *grt) const MixtureFugacityTPvirtual
getIntEnergy_RT(doublereal *urt) const MixtureFugacityTPvirtual
getIntEnergy_RT_ref(doublereal *urt) const ThermoPhaseinlinevirtual
getLnActivityCoefficients(doublereal *lnac) const ThermoPhasevirtual
getMassFractions(doublereal *const y) const Phase
getMassFractionsByName(double threshold=0.0) const Phase
getMolecularWeights(vector_fp &weights) const Phase
getMolecularWeights(doublereal *weights) const Phase
getMoleFractions(doublereal *const x) const Phase
getMoleFractionsByName(compositionMap &x) const Phase
getMoleFractionsByName(double threshold=0.0) const Phase
getParameters(int &n, doublereal *const c) const ThermoPhaseinlinevirtual
getPartialMolarCp(doublereal *cpbar) const RedlichKwongMFTPvirtual
getPartialMolarEnthalpies(doublereal *hbar) const RedlichKwongMFTPvirtual
getPartialMolarEntropies(doublereal *sbar) const RedlichKwongMFTPvirtual
getPartialMolarIntEnergies(doublereal *ubar) const RedlichKwongMFTPvirtual
getPartialMolarVolumes(doublereal *vbar) const RedlichKwongMFTPvirtual
getPureGibbs(doublereal *gpure) const MixtureFugacityTPvirtual
getReferenceComposition(doublereal *const x) const ThermoPhasevirtual
getStandardChemPotentials(doublereal *mu) const MixtureFugacityTPvirtual
getStandardVolumes(doublereal *vol) const MixtureFugacityTPvirtual
getStandardVolumes_ref(doublereal *vol) const MixtureFugacityTPvirtual
getUnitsStandardConc(double *uA, int k=0, int sizeUA=6) const RedlichKwongMFTPvirtual
gibbs_mass() const ThermoPhaseinline
gibbs_mole() const ThermoPhaseinlinevirtual
gibbs_RT_ref() const MixtureFugacityTPprotected
Hf298SS(const int k) const ThermoPhaseinline
hresid() const RedlichKwongMFTPprotectedvirtual
id() const Phase
ignoreUndefinedElements()Phase
initLengths()RedlichKwongMFTPprivate
initThermo()RedlichKwongMFTPvirtual
initThermoFile(const std::string &inputFile, const std::string &id)ThermoPhasevirtual
initThermoXML(XML_Node &phaseNode, const std::string &id)RedlichKwongMFTPvirtual
installSlavePhases(Cantera::XML_Node *phaseNode)ThermoPhasevirtual
intEnergy_mass() const ThermoPhaseinline
intEnergy_mole() const ThermoPhaseinlinevirtual
isothermalCompressibility() const ThermoPhaseinlinevirtual
iState_MixtureFugacityTPprotected
liquidVolEst(doublereal TKelvin, doublereal &pres) const RedlichKwongMFTPvirtual
logStandardConc(size_t k=0) const ThermoPhasevirtual
m_a_currentRedlichKwongMFTPprotected
m_b_currentRedlichKwongMFTPprotected
m_cachePhasemutableprotected
m_chargeNeutralityNecessaryThermoPhaseprotected
m_cp0_RMixtureFugacityTPmutableprotected
m_formTempParamRedlichKwongMFTPprotected
m_g0_RTMixtureFugacityTPmutableprotected
m_h0_RTMixtureFugacityTPmutableprotected
m_hasElementPotentialsThermoPhaseprotected
m_kkPhaseprotected
m_lambdaRRTThermoPhaseprotected
m_logc0MixtureFugacityTPmutableprotected
m_ndimPhaseprotected
m_partialMolarVolumes (defined in RedlichKwongMFTP)RedlichKwongMFTPmutableprotected
m_pc_Species (defined in RedlichKwongMFTP)RedlichKwongMFTPprotected
m_PcurrentMixtureFugacityTPprotected
m_phiThermoPhaseprotected
m_ppRedlichKwongMFTPmutableprotected
m_s0_RMixtureFugacityTPmutableprotected
m_species (defined in Phase)Phaseprotected
m_speciesChargePhaseprotected
m_speciesCompPhaseprotected
m_speciesDataThermoPhaseprotected
m_speciesSizePhaseprotected
m_spthermoThermoPhaseprotected
m_ssConventionThermoPhaseprotected
m_standardMixingRulesRedlichKwongMFTPprotected
m_tc_Species (defined in RedlichKwongMFTP)RedlichKwongMFTPprotected
m_tlastThermoPhasemutableprotected
m_Tlast_refMixtureFugacityTPmutableprotected
m_tmpVRedlichKwongMFTPmutableprotected
m_undefinedElementBehaviorPhaseprotected
m_vc_Species (defined in RedlichKwongMFTP)RedlichKwongMFTPprotected
massFraction(size_t k) const Phase
massFraction(const std::string &name) const Phase
massFractions() const Phaseinline
maxTemp(size_t k=npos) const ThermoPhaseinlinevirtual
mean_X(const doublereal *const Q) const Phase
mean_X(const vector_fp &Q) const Phase
mean_Y(const doublereal *const Q) const Phase
meanMolecularWeight() const Phaseinline
minTemp(size_t k=npos) const ThermoPhaseinlinevirtual
MixtureFugacityTP()MixtureFugacityTP
MixtureFugacityTP(const MixtureFugacityTP &b)MixtureFugacityTP
modifyOneHf298SS(const size_t k, const doublereal Hf298New)MixtureFugacityTPvirtual
molarDensity() const Phase
molarVolume() const Phase
molecularWeight(size_t k) const Phase
molecularWeights() const Phase
moleFractdivMMW() const Phase
moleFraction(size_t k) const Phase
moleFraction(const std::string &name) const Phase
moleFractions_MixtureFugacityTPprotected
name() const Phase
nAtoms(size_t k, size_t m) const Phase
nDim() const Phaseinline
nElements() const Phase
NicholsSolve(double TKelvin, double pres, doublereal a, doublereal b, doublereal Vroot[3]) const RedlichKwongMFTP
NSolns_ (defined in RedlichKwongMFTP)RedlichKwongMFTPprotected
nSpecies() const Phaseinline
omega_aRedlichKwongMFTPstatic
omega_bRedlichKwongMFTPstatic
omega_vcRedlichKwongMFTPstatic
operator=(const RedlichKwongMFTP &right)RedlichKwongMFTP
Cantera::MixtureFugacityTP::operator=(const MixtureFugacityTP &b)MixtureFugacityTP
Cantera::ThermoPhase::operator=(const ThermoPhase &right)ThermoPhase
Cantera::Phase::operator=(const Phase &right)Phase
Phase()Phase
Phase(const Phase &right)Phase
phaseState(bool checkState=false) const MixtureFugacityTP
pressure() const RedlichKwongMFTPvirtual
pressureCalc(doublereal TKelvin, doublereal molarVol) const RedlichKwongMFTPvirtual
pressureDerivatives() const RedlichKwongMFTP
psatEst(doublereal TKelvin) const MixtureFugacityTPprotectedvirtual
readXMLCrossFluid(XML_Node &pureFluidParam)RedlichKwongMFTPprivate
readXMLPureFluid(XML_Node &pureFluidParam)RedlichKwongMFTPprivate
ready() const Phasevirtual
realNumberRangeBehavior_Phase
RedlichKwongMFTP()RedlichKwongMFTP
RedlichKwongMFTP(const std::string &infile, std::string id="")RedlichKwongMFTP
RedlichKwongMFTP(XML_Node &phaseRef, const std::string &id="")RedlichKwongMFTP
RedlichKwongMFTP(int testProb)RedlichKwongMFTP
RedlichKwongMFTP(const RedlichKwongMFTP &right)RedlichKwongMFTP
refPressure() const ThermoPhaseinlinevirtual
report(bool show_thermo=true, doublereal threshold=-1e-14) const ThermoPhasevirtual
reportCSV(std::ofstream &csvFile) const ThermoPhasevirtual
reportSolnBranchActual() const MixtureFugacityTPvirtual
restoreState(const vector_fp &state)Phase
restoreState(size_t lenstate, const doublereal *state)Phase
satPressure(doublereal TKelvin)MixtureFugacityTPvirtual
satTemperature(doublereal p) const ThermoPhaseinlinevirtual
saveSpeciesData(const size_t k, const XML_Node *const data)ThermoPhase
saveState(vector_fp &state) const Phase
saveState(size_t lenstate, doublereal *state) const Phase
setConcentrations(const doublereal *const c)RedlichKwongMFTPprotectedvirtual
setDensity(const doublereal density_)Phaseinlinevirtual
setElectricPotential(doublereal v)ThermoPhaseinline
setElementPotentials(const vector_fp &lambda)ThermoPhase
setForcedSolutionBranch(int solnBranch)MixtureFugacityTPvirtual
setID(const std::string &id)Phase
setMassFractions(const doublereal *const y)RedlichKwongMFTPprotectedvirtual
setMassFractions_NoNorm(const doublereal *const y)RedlichKwongMFTPprotectedvirtual
setMassFractionsByName(const compositionMap &yMap)Phase
setMassFractionsByName(const std::string &x)Phase
setMolarDensity(const doublereal molarDensity)Phasevirtual
setMolecularWeight(const int k, const double mw)Phaseinlineprotected
setMoleFractions(const doublereal *const x)RedlichKwongMFTPprotectedvirtual
setMoleFractions_NoNorm(const doublereal *const x)RedlichKwongMFTPprotectedvirtual
setMoleFractions_NoState(const doublereal *const x) (defined in MixtureFugacityTP)MixtureFugacityTPprotected
setMoleFractionsByName(const compositionMap &xMap)Phase
setMoleFractionsByName(const std::string &x)Phase
setName(const std::string &nm)Phase
setNDim(size_t ndim)Phaseinline
setParameters(int n, doublereal *const c)ThermoPhaseinlinevirtual
setParametersFromXML(const XML_Node &thermoNode)RedlichKwongMFTPvirtual
setPressure(doublereal p)MixtureFugacityTPvirtual
setReferenceComposition(const doublereal *const x)ThermoPhasevirtual
setSpeciesThermo(SpeciesThermo *spthermo)ThermoPhase
setState_HP(doublereal h, doublereal p, doublereal tol=1.e-4)ThermoPhasevirtual
setState_Psat(doublereal p, doublereal x)ThermoPhaseinlinevirtual
setState_PX(doublereal p, doublereal *x)ThermoPhasevirtual
setState_PY(doublereal p, doublereal *y)ThermoPhasevirtual
setState_RX(doublereal rho, doublereal *x)Phase
setState_RY(doublereal rho, doublereal *y)Phase
setState_SP(doublereal s, doublereal p, doublereal tol=1.e-4)ThermoPhasevirtual
setState_SV(doublereal s, doublereal v, doublereal tol=1.e-4)ThermoPhasevirtual
setState_TNX(doublereal t, doublereal n, const doublereal *x)Phase
setState_TP(doublereal T, doublereal pres)MixtureFugacityTPvirtual
setState_TPX(doublereal t, doublereal p, const doublereal *x)MixtureFugacityTPvirtual
Cantera::ThermoPhase::setState_TPX(doublereal t, doublereal p, const compositionMap &x)ThermoPhasevirtual
Cantera::ThermoPhase::setState_TPX(doublereal t, doublereal p, const std::string &x)ThermoPhasevirtual
setState_TPY(doublereal t, doublereal p, const doublereal *y)ThermoPhasevirtual
setState_TPY(doublereal t, doublereal p, const compositionMap &y)ThermoPhasevirtual
setState_TPY(doublereal t, doublereal p, const std::string &y)ThermoPhasevirtual
setState_TR(doublereal T, doublereal rho)MixtureFugacityTPvirtual
setState_TRX(doublereal t, doublereal dens, const doublereal *x)Phase
setState_TRX(doublereal t, doublereal dens, const compositionMap &x)Phase
setState_TRY(doublereal t, doublereal dens, const doublereal *y)Phase
setState_TRY(doublereal t, doublereal dens, const compositionMap &y)Phase
setState_Tsat(doublereal t, doublereal x)ThermoPhaseinlinevirtual
setState_TX(doublereal t, doublereal *x)Phase
setState_TY(doublereal t, doublereal *y)Phase
setState_UV(doublereal u, doublereal v, doublereal tol=1.e-4)ThermoPhasevirtual
setStateFromXML(const XML_Node &state)MixtureFugacityTPvirtual
setTemperature(const doublereal temp)RedlichKwongMFTPprotectedvirtual
setToEquilState(const doublereal *lambda_RT)RedlichKwongMFTPvirtual
setXMLdata(XML_Node &xmlPhase)Phase
size(size_t k) const Phaseinline
species(const std::string &name) const Phase
species(size_t k) const Phase
speciesData() const ThermoPhase
speciesIndex(const std::string &name) const Phase
speciesName(size_t k) const Phase
speciesNames() const Phase
speciesSPName(int k) const Phase
speciesThermo(int k=-1)ThermoPhasevirtual
sresid() const RedlichKwongMFTPprotectedvirtual
standardConcentration(size_t k=0) const RedlichKwongMFTPvirtual
standardStateConvention() const MixtureFugacityTPvirtual
stateMFNumber() const Phaseinline
sum_xlogQ(doublereal *const Q) const Phase
sum_xlogx() const Phase
temperature() const Phaseinline
thermalExpansionCoeff() const ThermoPhaseinlinevirtual
ThermoPhase()ThermoPhase
ThermoPhase(const ThermoPhase &right)ThermoPhase
throwUndefinedElements()Phase
updateAB()RedlichKwongMFTP
updateMixingExpressions() (defined in RedlichKwongMFTP)RedlichKwongMFTPvirtual
vaporFraction() const ThermoPhaseinlinevirtual
Vroot_ (defined in RedlichKwongMFTP)RedlichKwongMFTPprotected
xml() const Phase
xMol_RefThermoPhaseprotected
z() const MixtureFugacityTPprotected
~Phase()Phasevirtual
~ThermoPhase()ThermoPhasevirtual