void IdealGasPhase::getCp_R_ref(doublereal* cprt) const
{
const vector_fp& _cpr = cp_R_ref();
copy(_cpr.begin(), _cpr.end(), cprt);
}
doublereal IdealGasPhase::cp_mole() const
{
return GasConstant * mean_X(cp_R_ref());
}
/*
* Returns the species standard state Cv in J kmol-1 K-1 at the
* current temperature and pressure.
*
* @return returns the species standard state Cv in J kmol-1 K-1
*/
doublereal PDSS::cpDelp_mole() const {
doublereal tmp = cp_R_ref();
return(cp_mole() - GasConstant * tmp);
}
void IdealGasPhase::getPartialMolarCp(doublereal* cpbar) const
{
const vector_fp& _cp = cp_R_ref();
scale(_cp.begin(), _cp.end(), cpbar, GasConstant);
}
/*
* Returns the vector of nondimensional
* constant pressure heat capacities of the reference state
* at the current temperature and reference pressure.
*/
void PecosGasPhase::getCp_R_ref(doublereal *cprt) const {
const array_fp& _cpr = cp_R_ref();
copy(_cpr.begin(), _cpr.end(), cprt);
}
/*
* Molar heat capacity at constant pressure. Units: J/kmol/K.
* For an ideal gas mixture,
* \f[
* \hat c_p(t) = \sum_k \hat c^0_{p,k}(T).
* \f]
* The reference-state pure-species heat capacities
* \f$ \hat c^0_{p,k}(T) \f$ are computed by the species thermodynamic
* property manager.
* @see SpeciesThermo
*/
doublereal PecosGasPhase::cp_mole() const {
return GasConstant * mean_X(&cp_R_ref()[0]);
}
doublereal LatticePhase::cp_mole() const
{
return GasConstant * mean_X(cp_R_ref());
}
void LatticePhase::getCp_R(doublereal* cpr) const
{
const vector_fp& _cpr = cp_R_ref();
std::copy(_cpr.begin(), _cpr.end(), cpr);
}
void IdealSolidSolnPhase::getCp_R(doublereal* cpr) const
{
const vector_fp& _cpr = cp_R_ref();
copy(_cpr.begin(), _cpr.end(), cpr);
}