695 lines
19 KiB
C++
695 lines
19 KiB
C++
/**
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* @file MolalityVPSSTP.cpp
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* Definitions for intermediate ThermoPhase object for phases which
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* employ molality based activity coefficient formulations
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* (see \ref thermoprops
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* and class \link Cantera::MolalityVPSSTP MolalityVPSSTP\endlink).
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*
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* Header file for a derived class of ThermoPhase that handles
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* variable pressure standard state methods for calculating
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* thermodynamic properties that are further based upon activities
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* based on the molality scale. These include most of the methods for
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* calculating liquid electrolyte thermodynamics.
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*/
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/*
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* Copyright (2005) Sandia Corporation. Under the terms of
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* Contract DE-AC04-94AL85000 with Sandia Corporation, the
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* U.S. Government retains certain rights in this software.
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*/
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#include "cantera/thermo/MolalityVPSSTP.h"
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#include "cantera/base/stringUtils.h"
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#include <iomanip>
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#include <cstdio>
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#include <fstream>
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using namespace std;
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namespace Cantera
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{
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MolalityVPSSTP::MolalityVPSSTP() :
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VPStandardStateTP(),
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m_indexSolvent(0),
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m_pHScalingType(PHSCALE_PITZER),
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m_indexCLM(npos),
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m_weightSolvent(18.01528),
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m_xmolSolventMIN(0.01),
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m_Mnaught(18.01528E-3)
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{
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/*
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* Change the default to be that charge neutrality in the
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* phase is necessary condition for the proper specification
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* of thermodynamic functions within the phase
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*/
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m_chargeNeutralityNecessary = true;
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}
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MolalityVPSSTP::MolalityVPSSTP(const MolalityVPSSTP& b) :
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VPStandardStateTP(),
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m_indexSolvent(b.m_indexSolvent),
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m_pHScalingType(b.m_pHScalingType),
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m_indexCLM(b.m_indexCLM),
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m_xmolSolventMIN(b.m_xmolSolventMIN),
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m_Mnaught(b.m_Mnaught),
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m_molalities(b.m_molalities)
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{
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*this = operator=(b);
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}
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MolalityVPSSTP& MolalityVPSSTP::
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operator=(const MolalityVPSSTP& b)
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{
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if (&b != this) {
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VPStandardStateTP::operator=(b);
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m_indexSolvent = b.m_indexSolvent;
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m_pHScalingType = b.m_pHScalingType;
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m_indexCLM = b.m_indexCLM;
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m_weightSolvent = b.m_weightSolvent;
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m_xmolSolventMIN = b.m_xmolSolventMIN;
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m_Mnaught = b.m_Mnaught;
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m_molalities = b.m_molalities;
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}
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return *this;
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}
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ThermoPhase*
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MolalityVPSSTP::duplMyselfAsThermoPhase() const
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{
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return new MolalityVPSSTP(*this);
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}
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/*
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* -------------- Utilities -------------------------------
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*/
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int MolalityVPSSTP::eosType() const
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{
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return 0;
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}
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void MolalityVPSSTP::setpHScale(const int pHscaleType)
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{
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m_pHScalingType = pHscaleType;
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if (pHscaleType != PHSCALE_PITZER && pHscaleType != PHSCALE_NBS) {
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throw CanteraError("MolalityVPSSTP::setpHScale",
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"Unknown scale type: " + int2str(pHscaleType));
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}
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}
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int MolalityVPSSTP::pHScale() const
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{
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return m_pHScalingType;
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}
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void MolalityVPSSTP::setSolvent(size_t k)
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{
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if (k >= m_kk) {
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throw CanteraError("MolalityVPSSTP::setSolute ",
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"bad value");
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}
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m_indexSolvent = k;
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AssertThrowMsg(m_indexSolvent==0, "MolalityVPSSTP::setSolvent",
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"Molality-based methods limit solvent id to being 0");
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m_weightSolvent = molecularWeight(k);
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m_Mnaught = m_weightSolvent / 1000.;
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}
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size_t MolalityVPSSTP::solventIndex() const
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{
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return m_indexSolvent;
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}
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void MolalityVPSSTP::
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setMoleFSolventMin(doublereal xmolSolventMIN)
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{
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if (xmolSolventMIN <= 0.0) {
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throw CanteraError("MolalityVPSSTP::setSolute ", "trouble");
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} else if (xmolSolventMIN > 0.9) {
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throw CanteraError("MolalityVPSSTP::setSolute ", "trouble");
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}
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m_xmolSolventMIN = xmolSolventMIN;
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}
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doublereal MolalityVPSSTP::moleFSolventMin() const
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{
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return m_xmolSolventMIN;
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}
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void MolalityVPSSTP::calcMolalities() const
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{
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getMoleFractions(DATA_PTR(m_molalities));
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double xmolSolvent = m_molalities[m_indexSolvent];
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if (xmolSolvent < m_xmolSolventMIN) {
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xmolSolvent = m_xmolSolventMIN;
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}
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double denomInv = 1.0/ (m_Mnaught * xmolSolvent);
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for (size_t k = 0; k < m_kk; k++) {
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m_molalities[k] *= denomInv;
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}
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}
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void MolalityVPSSTP::getMolalities(doublereal* const molal) const
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{
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calcMolalities();
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for (size_t k = 0; k < m_kk; k++) {
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molal[k] = m_molalities[k];
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}
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}
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void MolalityVPSSTP::setMolalities(const doublereal* const molal)
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{
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double Lsum = 1.0 / m_Mnaught;
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for (size_t k = 1; k < m_kk; k++) {
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m_molalities[k] = molal[k];
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Lsum += molal[k];
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}
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double tmp = 1.0 / Lsum;
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m_molalities[m_indexSolvent] = tmp / m_Mnaught;
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double sum = m_molalities[m_indexSolvent];
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for (size_t k = 1; k < m_kk; k++) {
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m_molalities[k] = tmp * molal[k];
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sum += m_molalities[k];
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}
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if (sum != 1.0) {
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tmp = 1.0 / sum;
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for (size_t k = 0; k < m_kk; k++) {
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m_molalities[k] *= tmp;
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}
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}
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setMoleFractions(DATA_PTR(m_molalities));
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/*
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* Essentially we don't trust the input: We calculate
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* the molalities from the mole fractions that we
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* just obtained.
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*/
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calcMolalities();
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}
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void MolalityVPSSTP::setMolalitiesByName(compositionMap& mMap)
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{
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/*
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* HKM -> Might need to be more complicated here, setting
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* neutrals so that the existing mole fractions are
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* preserved.
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*/
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size_t kk = nSpecies();
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doublereal x;
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/*
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* Get a vector of mole fractions
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*/
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vector_fp mf(kk, 0.0);
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getMoleFractions(DATA_PTR(mf));
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double xmolS = mf[m_indexSolvent];
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double xmolSmin = std::max(xmolS, m_xmolSolventMIN);
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compositionMap::iterator p;
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for (size_t k = 0; k < kk; k++) {
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p = mMap.find(speciesName(k));
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if (p != mMap.end()) {
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x = mMap[speciesName(k)];
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if (x > 0.0) {
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mf[k] = x * m_Mnaught * xmolSmin;
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}
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}
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}
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/*
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* check charge neutrality
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*/
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size_t largePos = npos;
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double cPos = 0.0;
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size_t largeNeg = npos;
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double cNeg = 0.0;
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double sum = 0.0;
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for (size_t k = 0; k < kk; k++) {
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double ch = charge(k);
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if (mf[k] > 0.0) {
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if (ch > 0.0) {
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if (ch * mf[k] > cPos) {
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largePos = k;
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cPos = ch * mf[k];
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}
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}
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if (ch < 0.0) {
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if (fabs(ch) * mf[k] > cNeg) {
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largeNeg = k;
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cNeg = fabs(ch) * mf[k];
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}
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}
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}
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sum += mf[k] * ch;
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}
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if (sum != 0.0) {
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if (sum > 0.0) {
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if (cPos > sum) {
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mf[largePos] -= sum / charge(largePos);
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} else {
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throw CanteraError("MolalityVPSSTP:setMolalitiesbyName",
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"unbalanced charges");
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}
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} else {
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if (cNeg > (-sum)) {
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mf[largeNeg] -= (-sum) / fabs(charge(largeNeg));
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} else {
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throw CanteraError("MolalityVPSSTP:setMolalitiesbyName",
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"unbalanced charges");
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}
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}
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}
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sum = 0.0;
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for (size_t k = 0; k < kk; k++) {
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sum += mf[k];
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}
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sum = 1.0/sum;
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for (size_t k = 0; k < kk; k++) {
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mf[k] *= sum;
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}
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setMoleFractions(DATA_PTR(mf));
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/*
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* After we formally set the mole fractions, we
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* calculate the molalities again and store it in
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* this object.
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*/
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calcMolalities();
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}
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void MolalityVPSSTP::setMolalitiesByName(const std::string& x)
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{
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compositionMap xx = parseCompString(x, speciesNames());
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setMolalitiesByName(xx);
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}
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/*
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* - Activities, Standard States, Activity Concentrations -----------
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*/
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int MolalityVPSSTP::activityConvention() const
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{
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return cAC_CONVENTION_MOLALITY;
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}
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void MolalityVPSSTP::getActivityConcentrations(doublereal* c) const
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{
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err("getActivityConcentrations");
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}
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doublereal MolalityVPSSTP::standardConcentration(size_t k) const
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{
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err("standardConcentration");
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return -1.0;
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}
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doublereal MolalityVPSSTP::logStandardConc(size_t k) const
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{
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err("logStandardConc");
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return -1.0;
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}
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void MolalityVPSSTP::getActivities(doublereal* ac) const
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{
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err("getActivities");
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}
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void MolalityVPSSTP::getActivityCoefficients(doublereal* ac) const
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{
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getMolalityActivityCoefficients(ac);
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AssertThrow(m_indexSolvent==0, "MolalityVPSSTP::getActivityCoefficients");
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double xmolSolvent = moleFraction(m_indexSolvent);
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if (xmolSolvent < m_xmolSolventMIN) {
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xmolSolvent = m_xmolSolventMIN;
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}
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for (size_t k = 1; k < m_kk; k++) {
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ac[k] /= xmolSolvent;
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}
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}
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void MolalityVPSSTP::getMolalityActivityCoefficients(doublereal* acMolality) const
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{
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getUnscaledMolalityActivityCoefficients(acMolality);
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applyphScale(acMolality);
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}
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doublereal MolalityVPSSTP::osmoticCoefficient() const
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{
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/*
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* First, we calculate the activities all over again
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*/
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vector_fp act(m_kk);
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getActivities(DATA_PTR(act));
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/*
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* Then, we calculate the sum of the solvent molalities
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*/
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double sum = 0;
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for (size_t k = 1; k < m_kk; k++) {
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sum += std::max(m_molalities[k], 0.0);
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}
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double oc = 1.0;
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double lac = log(act[m_indexSolvent]);
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if (sum > 1.0E-200) {
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oc = - lac / (m_Mnaught * sum);
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}
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return oc;
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}
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void MolalityVPSSTP::getElectrochemPotentials(doublereal* mu) const
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{
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getChemPotentials(mu);
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double ve = Faraday * electricPotential();
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for (size_t k = 0; k < m_kk; k++) {
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mu[k] += ve*charge(k);
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}
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}
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doublereal MolalityVPSSTP::err(const std::string& msg) const
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{
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throw CanteraError("MolalityVPSSTP","Base class method "
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+msg+" called. Equation of state type: "+int2str(eosType()));
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return 0;
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}
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void MolalityVPSSTP::getUnitsStandardConc(double* uA, int k, int sizeUA) const
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{
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for (int i = 0; i < sizeUA; i++) {
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if (i == 0) {
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uA[0] = 1.0;
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}
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if (i == 1) {
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uA[1] = -int(nDim());
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}
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if (i == 2) {
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uA[2] = 0.0;
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}
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if (i == 3) {
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uA[3] = 0.0;
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}
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if (i == 4) {
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uA[4] = 0.0;
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}
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if (i == 5) {
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uA[5] = 0.0;
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}
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}
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}
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void MolalityVPSSTP::setToEquilState(const doublereal* lambda_RT)
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{
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updateStandardStateThermo();
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err("setToEquilState");
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}
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void MolalityVPSSTP::setStateFromXML(const XML_Node& state)
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{
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VPStandardStateTP::setStateFromXML(state);
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string comp = ctml::getChildValue(state,"soluteMolalities");
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if (comp != "") {
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setMolalitiesByName(comp);
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}
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if (state.hasChild("pressure")) {
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double p = ctml::getFloat(state, "pressure", "pressure");
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setPressure(p);
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}
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}
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void MolalityVPSSTP::setState_TPM(doublereal t, doublereal p,
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const doublereal* const molalities)
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{
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setMolalities(molalities);
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setState_TP(t, p);
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}
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void MolalityVPSSTP::setState_TPM(doublereal t, doublereal p, compositionMap& m)
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{
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setMolalitiesByName(m);
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setState_TP(t, p);
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}
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void MolalityVPSSTP::setState_TPM(doublereal t, doublereal p, const std::string& m)
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{
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setMolalitiesByName(m);
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setState_TP(t, p);
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}
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void MolalityVPSSTP::initThermo()
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{
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initLengths();
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VPStandardStateTP::initThermo();
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/*
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* The solvent defaults to species 0
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*/
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setSolvent(0);
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/*
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* Find the Cl- species
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*/
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m_indexCLM = findCLMIndex();
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}
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void MolalityVPSSTP::getUnscaledMolalityActivityCoefficients(doublereal* acMolality) const
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{
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err("getUnscaledMolalityActivityCoefficients");
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}
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void MolalityVPSSTP::applyphScale(doublereal* acMolality) const
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{
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err("applyphScale");
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}
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size_t MolalityVPSSTP::findCLMIndex() const
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{
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size_t indexCLM = npos;
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size_t eCl = npos;
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size_t eE = npos;
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size_t ne = nElements();
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string sn;
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for (size_t e = 0; e < ne; e++) {
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sn = elementName(e);
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if (sn == "Cl" || sn == "CL") {
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eCl = e;
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break;
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}
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}
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// We have failed if we can't find the Cl element index
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if (eCl == npos) {
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return npos;
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}
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for (size_t e = 0; e < ne; e++) {
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sn = elementName(e);
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if (sn == "E" || sn == "e") {
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eE = e;
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break;
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}
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}
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// We have failed if we can't find the E element index
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if (eE == npos) {
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return npos;
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}
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for (size_t k = 1; k < m_kk; k++) {
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doublereal nCl = nAtoms(k, eCl);
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if (nCl != 1.0) {
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continue;
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}
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doublereal nE = nAtoms(k, eE);
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if (nE != 1.0) {
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continue;
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}
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for (size_t e = 0; e < ne; e++) {
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if (e != eE && e != eCl) {
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doublereal nA = nAtoms(k, e);
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if (nA != 0.0) {
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continue;
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}
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}
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}
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sn = speciesName(k);
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if (sn != "Cl-" && sn != "CL-") {
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continue;
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}
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indexCLM = k;
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break;
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}
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return indexCLM;
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}
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// Initialize lengths of local variables after all species have
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// been identified.
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void MolalityVPSSTP::initLengths()
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{
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m_kk = nSpecies();
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m_molalities.resize(m_kk);
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}
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void MolalityVPSSTP::initThermoXML(XML_Node& phaseNode, const std::string& id_)
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{
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initLengths();
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/*
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* The solvent defaults to species 0
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*/
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setSolvent(0);
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VPStandardStateTP::initThermoXML(phaseNode, id_);
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}
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/**
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* Format a summary of the mixture state for output.
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*/
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std::string MolalityVPSSTP::report(bool show_thermo) const
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{
|
|
char p[800];
|
|
string s = "";
|
|
try {
|
|
if (name() != "") {
|
|
sprintf(p, " \n %s:\n", name().c_str());
|
|
s += p;
|
|
}
|
|
sprintf(p, " \n temperature %12.6g K\n", temperature());
|
|
s += p;
|
|
sprintf(p, " pressure %12.6g Pa\n", pressure());
|
|
s += p;
|
|
sprintf(p, " density %12.6g kg/m^3\n", density());
|
|
s += p;
|
|
sprintf(p, " mean mol. weight %12.6g amu\n", meanMolecularWeight());
|
|
s += p;
|
|
|
|
doublereal phi = electricPotential();
|
|
sprintf(p, " potential %12.6g V\n", phi);
|
|
s += p;
|
|
|
|
size_t kk = nSpecies();
|
|
vector_fp x(kk);
|
|
vector_fp molal(kk);
|
|
vector_fp mu(kk);
|
|
vector_fp muss(kk);
|
|
vector_fp acMolal(kk);
|
|
vector_fp actMolal(kk);
|
|
getMoleFractions(&x[0]);
|
|
getMolalities(&molal[0]);
|
|
getChemPotentials(&mu[0]);
|
|
getStandardChemPotentials(&muss[0]);
|
|
getMolalityActivityCoefficients(&acMolal[0]);
|
|
getActivities(&actMolal[0]);
|
|
|
|
size_t iHp = speciesIndex("H+");
|
|
if (iHp != npos) {
|
|
double pH = -log(actMolal[iHp]) / log(10.0);
|
|
sprintf(p, " pH %12.4g \n", pH);
|
|
s += p;
|
|
}
|
|
|
|
if (show_thermo) {
|
|
sprintf(p, " \n");
|
|
s += p;
|
|
sprintf(p, " 1 kg 1 kmol\n");
|
|
s += p;
|
|
sprintf(p, " ----------- ------------\n");
|
|
s += p;
|
|
sprintf(p, " enthalpy %12.6g %12.4g J\n",
|
|
enthalpy_mass(), enthalpy_mole());
|
|
s += p;
|
|
sprintf(p, " internal energy %12.6g %12.4g J\n",
|
|
intEnergy_mass(), intEnergy_mole());
|
|
s += p;
|
|
sprintf(p, " entropy %12.6g %12.4g J/K\n",
|
|
entropy_mass(), entropy_mole());
|
|
s += p;
|
|
sprintf(p, " Gibbs function %12.6g %12.4g J\n",
|
|
gibbs_mass(), gibbs_mole());
|
|
s += p;
|
|
sprintf(p, " heat capacity c_p %12.6g %12.4g J/K\n",
|
|
cp_mass(), cp_mole());
|
|
s += p;
|
|
try {
|
|
sprintf(p, " heat capacity c_v %12.6g %12.4g J/K\n",
|
|
cv_mass(), cv_mole());
|
|
s += p;
|
|
} catch (CanteraError& e) {
|
|
e.save();
|
|
sprintf(p, " heat capacity c_v <not implemented> \n");
|
|
s += p;
|
|
}
|
|
}
|
|
|
|
sprintf(p, " \n");
|
|
s += p;
|
|
if (show_thermo) {
|
|
sprintf(p, " X "
|
|
" Molalities Chem.Pot. ChemPotSS ActCoeffMolal\n");
|
|
s += p;
|
|
sprintf(p, " "
|
|
" (J/kmol) (J/kmol) \n");
|
|
s += p;
|
|
sprintf(p, " ------------- "
|
|
" ------------ ------------ ------------ ------------\n");
|
|
s += p;
|
|
for (size_t k = 0; k < kk; k++) {
|
|
if (x[k] > SmallNumber) {
|
|
sprintf(p, "%18s %12.6g %12.6g %12.6g %12.6g %12.6g\n",
|
|
speciesName(k).c_str(), x[k], molal[k], mu[k], muss[k], acMolal[k]);
|
|
} else {
|
|
sprintf(p, "%18s %12.6g %12.6g N/A %12.6g %12.6g \n",
|
|
speciesName(k).c_str(), x[k], molal[k], muss[k], acMolal[k]);
|
|
}
|
|
s += p;
|
|
}
|
|
} else {
|
|
sprintf(p, " X"
|
|
"Molalities\n");
|
|
s += p;
|
|
sprintf(p, " -------------"
|
|
" ------------\n");
|
|
s += p;
|
|
for (size_t k = 0; k < kk; k++) {
|
|
sprintf(p, "%18s %12.6g %12.6g\n",
|
|
speciesName(k).c_str(), x[k], molal[k]);
|
|
s += p;
|
|
}
|
|
}
|
|
} catch (CanteraError& err) {
|
|
err.save();
|
|
}
|
|
return s;
|
|
}
|
|
|
|
void MolalityVPSSTP::getCsvReportData(std::vector<std::string>& names,
|
|
std::vector<vector_fp>& data) const
|
|
{
|
|
names.clear();
|
|
data.assign(10, vector_fp(nSpecies()));
|
|
|
|
names.push_back("X");
|
|
getMoleFractions(&data[0][0]);
|
|
|
|
names.push_back("Molal");
|
|
getMolalities(&data[1][0]);
|
|
|
|
names.push_back("Chem. Pot. (J/kmol)");
|
|
getChemPotentials(&data[2][0]);
|
|
|
|
names.push_back("Chem. Pot. SS (J/kmol)");
|
|
getStandardChemPotentials(&data[3][0]);
|
|
|
|
names.push_back("Molal Act. Coeff.");
|
|
getMolalityActivityCoefficients(&data[4][0]);
|
|
|
|
names.push_back("Molal Activity");
|
|
getActivities(&data[5][0]);
|
|
|
|
names.push_back("Part. Mol Enthalpy (J/kmol)");
|
|
getPartialMolarEnthalpies(&data[5][0]);
|
|
|
|
names.push_back("Part. Mol. Entropy (J/K/kmol)");
|
|
getPartialMolarEntropies(&data[6][0]);
|
|
|
|
names.push_back("Part. Mol. Energy (J/kmol)");
|
|
getPartialMolarIntEnergies(&data[7][0]);
|
|
|
|
names.push_back("Part. Mol. Cp (J/K/kmol");
|
|
getPartialMolarCp(&data[8][0]);
|
|
|
|
names.push_back("Part. Mol. Cv (J/K/kmol)");
|
|
getPartialMolarVolumes(&data[9][0]);
|
|
}
|
|
|
|
}
|