Cantera
2.2.1
|
This is the complete list of members for RedlichKwongMFTP, including all inherited members.
_RT() const | ThermoPhase | inline |
_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 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) | ThermoPhase | virtual |
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() | RedlichKwongMFTP | private |
atomicNumber(size_t m) const | Phase | |
atomicWeight(size_t m) const | Phase | |
atomicWeights() const | Phase | |
b_vec_Curr_ (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
calcCriticalConditions(doublereal a, doublereal b, doublereal a0_coeff, doublereal aT_coeff, doublereal &pc, doublereal &tc, doublereal &vc) const (defined in RedlichKwongMFTP) | RedlichKwongMFTP | |
calcDensity() | RedlichKwongMFTP | protectedvirtual |
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 | 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 | |
concentration(const size_t k) const | Phase | |
corr0(doublereal TKelvin, doublereal pres, doublereal &densLiq, doublereal &densGas, doublereal &liqGRT, doublereal &gasGRT) | MixtureFugacityTP | protected |
cp_mass() const | ThermoPhase | inline |
cp_mole() const | RedlichKwongMFTP | virtual |
critCompressibility() const | RedlichKwongMFTP | virtual |
critDensity() const | RedlichKwongMFTP | virtual |
critPressure() const | RedlichKwongMFTP | virtual |
critTemperature() const | RedlichKwongMFTP | virtual |
critVolume() const | RedlichKwongMFTP | virtual |
cv_mass() const | ThermoPhase | inline |
cv_mole() const | RedlichKwongMFTP | virtual |
cv_vib(int, double) const | ThermoPhase | inlinevirtual |
da_dt() const (defined in RedlichKwongMFTP) | RedlichKwongMFTP | |
density() const | Phase | inlinevirtual |
densityCalc(doublereal TKelvin, doublereal pressure, int phase, doublereal rhoguess) | RedlichKwongMFTP | virtual |
densSpinodalGas() const | RedlichKwongMFTP | virtual |
densSpinodalLiquid() const | RedlichKwongMFTP | virtual |
dpdni_ | RedlichKwongMFTP | mutableprotected |
dpdT_ | RedlichKwongMFTP | mutableprotected |
dpdV_ | RedlichKwongMFTP | mutableprotected |
dpdVCalc(doublereal TKelvin, doublereal molarVol, doublereal &presCalc) const | RedlichKwongMFTP | virtual |
duplMyselfAsThermoPhase() const | RedlichKwongMFTP | virtual |
electricPotential() const | ThermoPhase | inline |
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 | ThermoPhase | inline |
enthalpy_mole() const | RedlichKwongMFTP | virtual |
entropy_mass() const | ThermoPhase | inline |
entropy_mole() const | RedlichKwongMFTP | virtual |
entropyElement298(size_t m) const | Phase | |
eosType() const | RedlichKwongMFTP | virtual |
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) | MixtureFugacityTP | protected |
forcedSolutionBranch() const | MixtureFugacityTP | virtual |
forcedState_ | MixtureFugacityTP | protected |
freezeElements() | Phase | |
getActivities(doublereal *a) const | ThermoPhase | virtual |
getActivityCoefficients(doublereal *ac) const | RedlichKwongMFTP | virtual |
getActivityConcentrations(doublereal *c) const | RedlichKwongMFTP | virtual |
getAtoms(size_t k, double *atomArray) const | Phase | |
getChemPotentials(doublereal *mu) const | RedlichKwongMFTP | virtual |
getChemPotentials_RT(doublereal *mu) const | RedlichKwongMFTP | virtual |
getConcentrations(doublereal *const c) const | Phase | |
getCp_R(doublereal *cpr) const | MixtureFugacityTP | virtual |
getCp_R_ref(doublereal *cprt) const | MixtureFugacityTP | virtual |
getCsvReportData(std::vector< std::string > &names, std::vector< vector_fp > &data) const | ThermoPhase | protectedvirtual |
getdlnActCoeffdlnN(const size_t ld, doublereal *const dlnActCoeffdlnN) | ThermoPhase | virtual |
getdlnActCoeffdlnN_diag(doublereal *dlnActCoeffdlnN_diag) const | MixtureFugacityTP | inlinevirtual |
getdlnActCoeffdlnN_numderiv(const size_t ld, doublereal *const dlnActCoeffdlnN) (defined in ThermoPhase) | ThermoPhase | virtual |
getdlnActCoeffdlnX_diag(doublereal *dlnActCoeffdlnX_diag) const | ThermoPhase | inlinevirtual |
getdlnActCoeffds(const doublereal dTds, const doublereal *const dXds, doublereal *dlnActCoeffds) const | ThermoPhase | inlinevirtual |
getdPartialMolarVolumes_dP(doublereal *d_vbar_dP) const | ThermoPhase | inlinevirtual |
getdPartialMolarVolumes_dT(doublereal *d_vbar_dT) const | ThermoPhase | inlinevirtual |
getdStandardVolumes_dP(doublereal *d_vol_dP) const | ThermoPhase | inlinevirtual |
getdStandardVolumes_dT(doublereal *d_vol_dT) const | ThermoPhase | inlinevirtual |
getElectrochemPotentials(doublereal *mu) const | ThermoPhase | inline |
getElementPotentials(doublereal *lambda) const | ThermoPhase | |
getEnthalpy_RT(doublereal *hrt) const | MixtureFugacityTP | virtual |
getEnthalpy_RT_ref(doublereal *hrt) const | MixtureFugacityTP | virtual |
getEntropy_R(doublereal *sr) const | MixtureFugacityTP | virtual |
getEntropy_R_ref(doublereal *er) const | MixtureFugacityTP | virtual |
getGibbs_ref(doublereal *g) const | MixtureFugacityTP | virtual |
getGibbs_RT(doublereal *grt) const | MixtureFugacityTP | virtual |
getGibbs_RT_ref(doublereal *grt) const | MixtureFugacityTP | virtual |
getIntEnergy_RT(doublereal *urt) const | MixtureFugacityTP | virtual |
getIntEnergy_RT_ref(doublereal *urt) const | ThermoPhase | inlinevirtual |
getLnActivityCoefficients(doublereal *lnac) const | ThermoPhase | virtual |
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 | ThermoPhase | inlinevirtual |
getPartialMolarCp(doublereal *cpbar) const | RedlichKwongMFTP | virtual |
getPartialMolarEnthalpies(doublereal *hbar) const | RedlichKwongMFTP | virtual |
getPartialMolarEntropies(doublereal *sbar) const | RedlichKwongMFTP | virtual |
getPartialMolarIntEnergies(doublereal *ubar) const | RedlichKwongMFTP | virtual |
getPartialMolarVolumes(doublereal *vbar) const | RedlichKwongMFTP | virtual |
getPureGibbs(doublereal *gpure) const | MixtureFugacityTP | virtual |
getReferenceComposition(doublereal *const x) const | ThermoPhase | virtual |
getStandardChemPotentials(doublereal *mu) const | MixtureFugacityTP | virtual |
getStandardVolumes(doublereal *vol) const | MixtureFugacityTP | virtual |
getStandardVolumes_ref(doublereal *vol) const | MixtureFugacityTP | virtual |
getUnitsStandardConc(double *uA, int k=0, int sizeUA=6) const | RedlichKwongMFTP | virtual |
gibbs_mass() const | ThermoPhase | inline |
gibbs_mole() const | ThermoPhase | inlinevirtual |
gibbs_RT_ref() const | MixtureFugacityTP | protected |
Hf298SS(const int k) const | ThermoPhase | inline |
hresid() const | RedlichKwongMFTP | protectedvirtual |
id() const | Phase | |
ignoreUndefinedElements() | Phase | |
initLengths() | RedlichKwongMFTP | private |
initThermo() | RedlichKwongMFTP | virtual |
initThermoFile(const std::string &inputFile, const std::string &id) | ThermoPhase | virtual |
initThermoXML(XML_Node &phaseNode, const std::string &id) | RedlichKwongMFTP | virtual |
installSlavePhases(Cantera::XML_Node *phaseNode) | ThermoPhase | virtual |
intEnergy_mass() const | ThermoPhase | inline |
intEnergy_mole() const | ThermoPhase | inlinevirtual |
isothermalCompressibility() const | ThermoPhase | inlinevirtual |
iState_ | MixtureFugacityTP | protected |
liquidVolEst(doublereal TKelvin, doublereal &pres) const | RedlichKwongMFTP | virtual |
logStandardConc(size_t k=0) const | ThermoPhase | virtual |
m_a_current | RedlichKwongMFTP | protected |
m_b_current | RedlichKwongMFTP | protected |
m_cache | Phase | mutableprotected |
m_chargeNeutralityNecessary | ThermoPhase | protected |
m_cp0_R | MixtureFugacityTP | mutableprotected |
m_formTempParam | RedlichKwongMFTP | protected |
m_g0_RT | MixtureFugacityTP | mutableprotected |
m_h0_RT | MixtureFugacityTP | mutableprotected |
m_hasElementPotentials | ThermoPhase | protected |
m_kk | Phase | protected |
m_lambdaRRT | ThermoPhase | protected |
m_logc0 | MixtureFugacityTP | mutableprotected |
m_ndim | Phase | protected |
m_partialMolarVolumes (defined in RedlichKwongMFTP) | RedlichKwongMFTP | mutableprotected |
m_pc_Species (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
m_Pcurrent | MixtureFugacityTP | protected |
m_phi | ThermoPhase | protected |
m_pp | RedlichKwongMFTP | mutableprotected |
m_s0_R | MixtureFugacityTP | mutableprotected |
m_species (defined in Phase) | Phase | protected |
m_speciesCharge | Phase | protected |
m_speciesComp | Phase | protected |
m_speciesData | ThermoPhase | protected |
m_speciesSize | Phase | protected |
m_spthermo | ThermoPhase | protected |
m_ssConvention | ThermoPhase | protected |
m_standardMixingRules | RedlichKwongMFTP | protected |
m_tc_Species (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
m_tlast | ThermoPhase | mutableprotected |
m_Tlast_ref | MixtureFugacityTP | mutableprotected |
m_tmpV | RedlichKwongMFTP | mutableprotected |
m_undefinedElementBehavior | Phase | protected |
m_vc_Species (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
massFraction(size_t k) const | Phase | |
massFraction(const std::string &name) const | Phase | |
massFractions() const | Phase | inline |
maxTemp(size_t k=npos) const | ThermoPhase | inlinevirtual |
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 | Phase | inline |
minTemp(size_t k=npos) const | ThermoPhase | inlinevirtual |
MixtureFugacityTP() | MixtureFugacityTP | |
MixtureFugacityTP(const MixtureFugacityTP &b) | MixtureFugacityTP | |
modifyOneHf298SS(const size_t k, const doublereal Hf298New) | MixtureFugacityTP | virtual |
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_ | MixtureFugacityTP | protected |
name() const | Phase | |
nAtoms(size_t k, size_t m) const | Phase | |
nDim() const | Phase | inline |
nElements() const | Phase | |
NicholsSolve(double TKelvin, double pres, doublereal a, doublereal b, doublereal Vroot[3]) const | RedlichKwongMFTP | |
NSolns_ (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
nSpecies() const | Phase | inline |
omega_a | RedlichKwongMFTP | static |
omega_b | RedlichKwongMFTP | static |
omega_vc | RedlichKwongMFTP | static |
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 | RedlichKwongMFTP | virtual |
pressureCalc(doublereal TKelvin, doublereal molarVol) const | RedlichKwongMFTP | virtual |
pressureDerivatives() const | RedlichKwongMFTP | |
psatEst(doublereal TKelvin) const | MixtureFugacityTP | protectedvirtual |
readXMLCrossFluid(XML_Node &pureFluidParam) | RedlichKwongMFTP | private |
readXMLPureFluid(XML_Node &pureFluidParam) | RedlichKwongMFTP | private |
ready() const | Phase | virtual |
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 | ThermoPhase | inlinevirtual |
report(bool show_thermo=true, doublereal threshold=-1e-14) const | ThermoPhase | virtual |
reportCSV(std::ofstream &csvFile) const | ThermoPhase | virtual |
reportSolnBranchActual() const | MixtureFugacityTP | virtual |
restoreState(const vector_fp &state) | Phase | |
restoreState(size_t lenstate, const doublereal *state) | Phase | |
satPressure(doublereal TKelvin) | MixtureFugacityTP | virtual |
satTemperature(doublereal p) const | ThermoPhase | inlinevirtual |
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) | RedlichKwongMFTP | protectedvirtual |
setDensity(const doublereal density_) | Phase | inlinevirtual |
setElectricPotential(doublereal v) | ThermoPhase | inline |
setElementPotentials(const vector_fp &lambda) | ThermoPhase | |
setForcedSolutionBranch(int solnBranch) | MixtureFugacityTP | virtual |
setID(const std::string &id) | Phase | |
setMassFractions(const doublereal *const y) | RedlichKwongMFTP | protectedvirtual |
setMassFractions_NoNorm(const doublereal *const y) | RedlichKwongMFTP | protectedvirtual |
setMassFractionsByName(const compositionMap &yMap) | Phase | |
setMassFractionsByName(const std::string &x) | Phase | |
setMolarDensity(const doublereal molarDensity) | Phase | virtual |
setMolecularWeight(const int k, const double mw) | Phase | inlineprotected |
setMoleFractions(const doublereal *const x) | RedlichKwongMFTP | protectedvirtual |
setMoleFractions_NoNorm(const doublereal *const x) | RedlichKwongMFTP | protectedvirtual |
setMoleFractions_NoState(const doublereal *const x) (defined in MixtureFugacityTP) | MixtureFugacityTP | protected |
setMoleFractionsByName(const compositionMap &xMap) | Phase | |
setMoleFractionsByName(const std::string &x) | Phase | |
setName(const std::string &nm) | Phase | |
setNDim(size_t ndim) | Phase | inline |
setParameters(int n, doublereal *const c) | ThermoPhase | inlinevirtual |
setParametersFromXML(const XML_Node &thermoNode) | RedlichKwongMFTP | virtual |
setPressure(doublereal p) | MixtureFugacityTP | virtual |
setReferenceComposition(const doublereal *const x) | ThermoPhase | virtual |
setSpeciesThermo(SpeciesThermo *spthermo) | ThermoPhase | |
setState_HP(doublereal h, doublereal p, doublereal tol=1.e-4) | ThermoPhase | virtual |
setState_Psat(doublereal p, doublereal x) | ThermoPhase | inlinevirtual |
setState_PX(doublereal p, doublereal *x) | ThermoPhase | virtual |
setState_PY(doublereal p, doublereal *y) | ThermoPhase | virtual |
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) | ThermoPhase | virtual |
setState_SV(doublereal s, doublereal v, doublereal tol=1.e-4) | ThermoPhase | virtual |
setState_TNX(doublereal t, doublereal n, const doublereal *x) | Phase | |
setState_TP(doublereal T, doublereal pres) | MixtureFugacityTP | virtual |
setState_TPX(doublereal t, doublereal p, const doublereal *x) | MixtureFugacityTP | virtual |
Cantera::ThermoPhase::setState_TPX(doublereal t, doublereal p, const compositionMap &x) | ThermoPhase | virtual |
Cantera::ThermoPhase::setState_TPX(doublereal t, doublereal p, const std::string &x) | ThermoPhase | virtual |
setState_TPY(doublereal t, doublereal p, const doublereal *y) | ThermoPhase | virtual |
setState_TPY(doublereal t, doublereal p, const compositionMap &y) | ThermoPhase | virtual |
setState_TPY(doublereal t, doublereal p, const std::string &y) | ThermoPhase | virtual |
setState_TR(doublereal T, doublereal rho) | MixtureFugacityTP | virtual |
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) | ThermoPhase | inlinevirtual |
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) | ThermoPhase | virtual |
setStateFromXML(const XML_Node &state) | MixtureFugacityTP | virtual |
setTemperature(const doublereal temp) | RedlichKwongMFTP | protectedvirtual |
setToEquilState(const doublereal *lambda_RT) | RedlichKwongMFTP | virtual |
setXMLdata(XML_Node &xmlPhase) | Phase | |
size(size_t k) const | Phase | inline |
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) | ThermoPhase | virtual |
sresid() const | RedlichKwongMFTP | protectedvirtual |
standardConcentration(size_t k=0) const | RedlichKwongMFTP | virtual |
standardStateConvention() const | MixtureFugacityTP | virtual |
stateMFNumber() const | Phase | inline |
sum_xlogQ(doublereal *const Q) const | Phase | |
sum_xlogx() const | Phase | |
temperature() const | Phase | inline |
thermalExpansionCoeff() const | ThermoPhase | inlinevirtual |
ThermoPhase() | ThermoPhase | |
ThermoPhase(const ThermoPhase &right) | ThermoPhase | |
throwUndefinedElements() | Phase | |
updateAB() | RedlichKwongMFTP | |
updateMixingExpressions() (defined in RedlichKwongMFTP) | RedlichKwongMFTP | virtual |
vaporFraction() const | ThermoPhase | inlinevirtual |
Vroot_ (defined in RedlichKwongMFTP) | RedlichKwongMFTP | protected |
xml() const | Phase | |
xMol_Ref | ThermoPhase | protected |
z() const | MixtureFugacityTP | protected |
~Phase() | Phase | virtual |
~ThermoPhase() | ThermoPhase | virtual |