[Thermo] Clean up implementation of MaskellSolidSolnPhase
Eliminate several member variables which shadow variables of the VPStandardState class, and actually contained the same information calculated a different way.
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2 changed files with 0 additions and 44 deletions
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@ -136,25 +136,6 @@ private:
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*/
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doublereal m_Pcurrent;
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/**
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* Function to call through to m_spthermo->update and fill m_h0_RT,
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* m_cp0_R, m_g0_RT, m_s0_R.
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*/
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void _updateThermo() const;
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//! Vector containing the species reference enthalpies at T = m_tlast
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mutable vector_fp m_h0_RT;
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//! Vector containing the species reference constant pressure heat
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//! capacities at T = m_tlast
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mutable vector_fp m_cp0_R;
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//! Vector containing the species reference Gibbs functions at T = m_tlast
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mutable vector_fp m_g0_RT;
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//! Vector containing the species reference entropies at T = m_tlast
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mutable vector_fp m_s0_R;
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//! Value of the enthalpy change on mixing due to protons changing from type
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//! B to type A configurations.
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doublereal h_mixing;
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@ -19,10 +19,6 @@ namespace Cantera
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MaskellSolidSolnPhase::MaskellSolidSolnPhase() :
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m_Pcurrent(OneAtm),
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m_h0_RT(2),
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m_cp0_R(2),
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m_g0_RT(2),
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m_s0_R(2),
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h_mixing(0.0),
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product_species_index(-1),
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reactant_species_index(-1)
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@ -41,7 +37,6 @@ void MaskellSolidSolnPhase::getActivityConcentrations(doublereal* c) const
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doublereal MaskellSolidSolnPhase::enthalpy_mole() const
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{
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_updateThermo();
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const doublereal h0 = RT() * mean_X(m_h0_RT);
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const doublereal r = moleFraction(product_species_index);
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const doublereal fmval = fm(r);
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@ -55,7 +50,6 @@ doublereal xlogx(doublereal x)
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doublereal MaskellSolidSolnPhase::entropy_mole() const
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{
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_updateThermo();
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const doublereal s0 = GasConstant * mean_X(m_s0_R);
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const doublereal r = moleFraction(product_species_index);
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const doublereal fmval = fm(r);
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@ -105,7 +99,6 @@ void MaskellSolidSolnPhase::setMolarDensity(const doublereal n)
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void MaskellSolidSolnPhase::getActivityCoefficients(doublereal* ac) const
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{
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_updateThermo();
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static const int cacheId = m_cache.getId();
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CachedArray cached = m_cache.getArray(cacheId);
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if (!cached.validate(temperature(), pressure(), stateMFNumber())) {
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@ -125,7 +118,6 @@ void MaskellSolidSolnPhase::getActivityCoefficients(doublereal* ac) const
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void MaskellSolidSolnPhase::getChemPotentials(doublereal* mu) const
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{
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_updateThermo();
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const doublereal r = moleFraction(product_species_index);
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const doublereal pval = p(r);
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const doublereal rfm = r * fm(r);
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@ -169,7 +161,6 @@ void MaskellSolidSolnPhase::getPartialMolarVolumes(doublereal* vbar) const
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void MaskellSolidSolnPhase::getPureGibbs(doublereal* gpure) const
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{
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_updateThermo();
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for (size_t sp=0; sp < m_kk; ++sp) {
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gpure[sp] = RT() * m_g0_RT[sp];
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}
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@ -238,22 +229,6 @@ void MaskellSolidSolnPhase::setProductSpecies(const std::string& name)
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reactant_species_index = (product_species_index == 0) ? 1 : 0;
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}
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void MaskellSolidSolnPhase::_updateThermo() const
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{
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assert(m_kk == 2);
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static const int cacheId = m_cache.getId();
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CachedScalar cached = m_cache.getScalar(cacheId);
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// Update the thermodynamic functions of the reference state.
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doublereal tnow = temperature();
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if (!cached.validate(tnow)) {
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m_spthermo.update(tnow, m_cp0_R.data(), m_h0_RT.data(), m_s0_R.data());
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for (size_t k = 0; k < m_kk; k++) {
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m_g0_RT[k] = m_h0_RT[k] - m_s0_R[k];
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}
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}
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}
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doublereal MaskellSolidSolnPhase::s() const
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{
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return 1 + std::exp(h_mixing / RT());
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