Reaktoro  v2.11.0
A unified framework for modeling chemically reactive systems
EquilibriumConditions Member List

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

activity(String const &species, real const &value) -> voidEquilibriumConditions
charge(real const &value, String const &unit="mol") -> voidEquilibriumConditions
chemicalPotential(String const &substance, real const &value, String const &unit="J/mol") -> voidEquilibriumConditions
Eh(real const &value, String const &unit="V") -> voidEquilibriumConditions
elementAmount(StringOrIndex const &element, real const &value, String const &unit="mol") -> voidEquilibriumConditions
elementAmountInPhase(StringOrIndex const &element, StringOrIndex const &phase, real const &value, String const &unit="mol") -> voidEquilibriumConditions
elementMass(StringOrIndex const &element, real const &value, String const &unit="kg") -> voidEquilibriumConditions
elementMassInPhase(StringOrIndex const &element, StringOrIndex const &phase, real const &value, String const &unit="kg") -> voidEquilibriumConditions
enthalpy(real const &value, String const &unit="J") -> voidEquilibriumConditions
entropy(real const &value, String const &unit="J/K") -> voidEquilibriumConditions
EquilibriumConditions(ChemicalSystem const &system)EquilibriumConditionsexplicit
EquilibriumConditions(EquilibriumSpecs const &specs)EquilibriumConditionsexplicit
fugacity(String const &species, real const &value, String const &unit="bar") -> voidEquilibriumConditions
gibbsEnergy(real const &value, String const &unit="J") -> voidEquilibriumConditions
helmholtzEnergy(real const &value, String const &unit="J") -> voidEquilibriumConditions
initialComponentAmounts() const -> ArrayXdConstRefEquilibriumConditions
initialComponentAmountsGetOrCompute(VectorXdConstRef const &n0) const -> ArrayXdEquilibriumConditions
initialComponentAmountsGetOrCompute(ChemicalState const &state0) const -> ArrayXdEquilibriumConditions
inputNames() const -> Strings const &EquilibriumConditions
inputValue(String const &name) const -> real const &EquilibriumConditions
inputValues() const -> ArrayXrConstRefEquilibriumConditions
inputValuesGetOrCompute(ChemicalState const &state0) const -> ArrayXrEquilibriumConditions
internalEnergy(real const &value, String const &unit="J") -> voidEquilibriumConditions
lgActivity(String const &species, real const &value) -> voidEquilibriumConditions
lnActivity(String const &species, real const &value) -> voidEquilibriumConditions
lowerBoundsControlVariablesP() const -> ArrayXdConstRefEquilibriumConditions
pE(real const &value) -> voidEquilibriumConditions
pH(real const &value) -> voidEquilibriumConditions
phaseAmount(StringOrIndex const &phase, real const &value, String const &unit="mol") -> voidEquilibriumConditions
phaseMass(StringOrIndex const &phase, real const &value, String const &unit="kg") -> voidEquilibriumConditions
phaseVolume(StringOrIndex const &phase, real const &value, String const &unit="m3") -> voidEquilibriumConditions
pMg(real const &value) -> voidEquilibriumConditions
pressure(real const &value, String const &unit="Pa") -> voidEquilibriumConditions
set(String const &input, real const &val) -> voidEquilibriumConditions
setInitialComponentAmounts(VectorXdConstRef const &c0) -> voidEquilibriumConditions
setInitialComponentAmountsFromSpeciesAmounts(VectorXdConstRef const &n0) -> voidEquilibriumConditions
setInitialComponentAmountsFromState(ChemicalState const &state0) -> voidEquilibriumConditions
setInputVariable(String const &name, real const &val) -> voidEquilibriumConditions
setInputVariable(Index index, real const &val) -> voidEquilibriumConditions
setInputVariables(ArrayXrConstRef const &values) -> voidEquilibriumConditions
setLowerBoundPressure(double value, String const &unit="Pa") -> voidEquilibriumConditions
setLowerBoundsControlVariablesP(ArrayXdConstRef const &values) -> voidEquilibriumConditions
setLowerBoundTemperature(double value, String const &unit="K") -> voidEquilibriumConditions
setLowerBoundTitrant(String const &substance, double value, String const &unit="mol") -> voidEquilibriumConditions
setUpperBoundPressure(double value, String const &unit="Pa") -> voidEquilibriumConditions
setUpperBoundsControlVariablesP(ArrayXdConstRef const &values) -> voidEquilibriumConditions
setUpperBoundTemperature(double value, String const &unit="K") -> voidEquilibriumConditions
setUpperBoundTitrant(String const &substance, double value, String const &unit="mol") -> voidEquilibriumConditions
system() const -> ChemicalSystem const &EquilibriumConditions
temperature(real const &value, String const &unit="K") -> voidEquilibriumConditions
upperBoundsControlVariablesP() const -> ArrayXdConstRefEquilibriumConditions
volume(real const &value, String const &unit="m3") -> voidEquilibriumConditions