This version has a significantly better treatment of the activity
coefficients as the solvent disappears. There are options to get rid of the singularity.
This commit is contained in:
parent
0cebba592f
commit
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2 changed files with 536 additions and 42 deletions
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@ -25,22 +25,42 @@
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*/
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#include "IdealMolalSoln.h"
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//#include "importCTML.h"
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#include "ThermoFactory.h"
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#include <math.h>
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#ifndef MAX
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#define MAX(x,y) (( (x) > (y) ) ? (x) : (y))
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#endif
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namespace Cantera {
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static double xxSmall = 1.0E-150;
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/**
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* Default constructor
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*/
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IdealMolalSoln::IdealMolalSoln() :
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MolalityVPSSTP(),
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m_formGC(2)
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m_formGC(2),
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typeCutoff_(0),
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X_o_cutoff_(0.20),
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gamma_o_min_(0.00001),
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gamma_k_min_(10.0),
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cCut_(.05),
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slopefCut_(0.6),
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dfCut_(0.0),
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efCut_(0.0),
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afCut_(0.0),
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bfCut_(0.0),
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slopegCut_(0.0),
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dgCut_(0.0),
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egCut_(0.0),
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agCut_(0.0),
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bgCut_(0.0)
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{
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}
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/**
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/*
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* Copy Constructor:
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*
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* Note this stuff will not work until the underlying phase
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@ -56,7 +76,7 @@ namespace Cantera {
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*this = b;
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}
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/**
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/*
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* operator=()
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*
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* Note this stuff will not work until the underlying phase
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@ -68,29 +88,75 @@ namespace Cantera {
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MolalityVPSSTP::operator=(b);
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m_speciesMolarVolume = b.m_speciesMolarVolume;
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m_formGC = b.m_formGC;
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typeCutoff_ = b.typeCutoff_;
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X_o_cutoff_ = b.X_o_cutoff_;
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gamma_o_min_ = b.gamma_o_min_;
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gamma_k_min_ = b.gamma_k_min_;
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cCut_ = b.cCut_;
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slopefCut_ = b.slopefCut_;
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dfCut_ = b.dfCut_;
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efCut_ = b.efCut_;
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afCut_ = b.afCut_;
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bfCut_ = b.bfCut_;
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slopegCut_ = b.slopegCut_;
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dgCut_ = b.dgCut_;
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egCut_ = b.egCut_;
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agCut_ = b.agCut_;
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bgCut_ = b.bgCut_;
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m_expg0_RT = b.m_expg0_RT;
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m_pe = b.m_pe;
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m_pp = b.m_pp;
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m_tmpV = b.m_tmpV;
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m_lnActCoeffMolal = b.m_lnActCoeffMolal;
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}
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return *this;
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}
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IdealMolalSoln::IdealMolalSoln(std::string inputFile, std::string id) :
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MolalityVPSSTP(),
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m_formGC(2)
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m_formGC(2),
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typeCutoff_(0),
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X_o_cutoff_(0.2),
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gamma_o_min_(0.00001),
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gamma_k_min_(10.0),
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cCut_(.05),
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slopefCut_(0.6),
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dfCut_(0.0),
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efCut_(0.0),
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afCut_(0.0),
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bfCut_(0.0),
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slopegCut_(0.0),
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dgCut_(0.0),
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egCut_(0.0),
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agCut_(0.0),
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bgCut_(0.0)
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{
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constructPhaseFile(inputFile, id);
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}
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IdealMolalSoln::IdealMolalSoln(XML_Node& root, std::string id) :
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MolalityVPSSTP(),
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m_formGC(2)
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m_formGC(2),
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typeCutoff_(0),
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X_o_cutoff_(0.2),
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gamma_o_min_(0.00001),
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gamma_k_min_(10.0),
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cCut_(.05),
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slopefCut_(0.6),
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dfCut_(0.0),
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efCut_(0.0),
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afCut_(0.0),
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bfCut_(0.0),
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slopegCut_(0.0),
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dgCut_(0.0),
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egCut_(0.0),
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agCut_(0.0),
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bgCut_(0.0)
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{
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constructPhaseXML(root, id);
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}
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/**
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/*
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*
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* ~IdealMolalSoln(): (virtual)
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*
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@ -457,8 +523,8 @@ namespace Cantera {
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* activities at the current solution temperature,
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* pressure, and solution concentration.
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*
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* The max against 8.689E-3 is to limit the activity
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* coefficient to be greater than 1.0E-50.
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* The max against xmolSolventMIN is to limit the activity
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* coefficient to be finite as the solvent mf goes to zero.
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*/
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void IdealMolalSoln::getActivities(doublereal* ac) const {
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_updateStandardStateThermo();
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@ -466,14 +532,29 @@ namespace Cantera {
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* Update the molality array, m_molalities()
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* This requires an update due to mole fractions
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*/
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calcMolalities();
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for (int k = 0; k < m_kk; k++) {
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ac[k] = m_molalities[k];
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if (typeCutoff_ == 0) {
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calcMolalities();
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for (int k = 0; k < m_kk; k++) {
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ac[k] = m_molalities[k];
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}
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double xmolSolvent = moleFraction(m_indexSolvent);
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xmolSolvent = fmaxx(m_xmolSolventMIN, xmolSolvent);
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ac[m_indexSolvent] =
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exp((xmolSolvent - 1.0)/xmolSolvent);
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} else {
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s_updateIMS_lnMolalityActCoeff();
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/*
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* Now calculate the array of activities.
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*/
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for (int k = 1; k < m_kk; k++) {
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ac[k] = m_molalities[k] * exp(m_lnActCoeffMolal[k]);
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}
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double xmolSolvent = moleFraction(m_indexSolvent);
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ac[m_indexSolvent] =
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exp(m_lnActCoeffMolal[m_indexSolvent]) * xmolSolvent;
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}
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double xmolSolvent = moleFraction(m_indexSolvent);
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xmolSolvent = fmaxx(8.689E-3, xmolSolvent);
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ac[m_indexSolvent] =
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exp((xmolSolvent - 1.0)/xmolSolvent);
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}
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/*
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@ -484,18 +565,26 @@ namespace Cantera {
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* See Denbigh
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* (note solvent activity coefficient is on the molar scale).
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*
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* The max against 5.0E-3 (1/200) is to limit the activity
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* coefficient to be greater than 1.0E-50.
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* The max against xmolSolventMIN is to limit the activity
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* coefficient to be finite as the solvent mf goes to zero.
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*/
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void IdealMolalSoln::
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getMolalityActivityCoefficients(doublereal* acMolality) const {
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for (int k = 0; k < m_kk; k++) {
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acMolality[k] = 1.0;
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if (typeCutoff_ == 0) {
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for (int k = 0; k < m_kk; k++) {
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acMolality[k] = 1.0;
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}
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double xmolSolvent = moleFraction(m_indexSolvent);
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xmolSolvent = fmaxx(m_xmolSolventMIN, xmolSolvent);
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acMolality[m_indexSolvent] =
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exp((xmolSolvent - 1.0)/xmolSolvent) / xmolSolvent;
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} else {
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s_updateIMS_lnMolalityActCoeff();
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std::copy(m_lnActCoeffMolal.begin(), m_lnActCoeffMolal.end(), acMolality);
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for (int k = 0; k < m_kk; k++) {
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acMolality[k] = exp(acMolality[k]);
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}
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}
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double xmolSolvent = moleFraction(m_indexSolvent);
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xmolSolvent = fmaxx(8.689E-3, xmolSolvent);
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acMolality[m_indexSolvent] =
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exp((xmolSolvent - 1.0)/xmolSolvent) / xmolSolvent;
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}
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//
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@ -525,7 +614,11 @@ namespace Cantera {
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*/
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void IdealMolalSoln::getChemPotentials(doublereal* mu) const{
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double xx;
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const double xxSmall = 1.0E-150;
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//const double xxSmall = 1.0E-150;
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// Assertion is made for speed
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AssertThrow(m_indexSolvent == 0, "solvent not the first species");
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/*
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* First get the standard chemical potentials
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* -> this requires updates of standard state as a function
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@ -538,24 +631,46 @@ namespace Cantera {
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* This requires an update due to mole fractions
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*/
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calcMolalities();
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/*
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* get the solvent mole fraction
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*/
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double xmolSolvent = moleFraction(m_indexSolvent);
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/*
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*
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*/
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doublereal RT = GasConstant * temperature();
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for (int k = 0; k < m_kk; k++) {
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if (k != m_indexSolvent) {
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if (typeCutoff_ == 0 || xmolSolvent > 3.* X_o_cutoff_/2.0) {
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for (int k = 1; k < m_kk; k++) {
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xx = fmaxx(m_molalities[k], xxSmall);
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mu[k] += RT * log(xx);
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}
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/*
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* Do the solvent
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* -> see my notes
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*/
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xx = fmaxx(xmolSolvent, xxSmall);
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mu[m_indexSolvent] +=
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(RT * (xmolSolvent - 1.0) / xx);
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} else {
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/*
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* Update the activity coefficients
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* This also updates the internal molality array.
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*/
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s_updateIMS_lnMolalityActCoeff();
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for (int k = 1; k < m_kk; k++) {
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xx = MAX(m_molalities[k], xxSmall);
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mu[k] += RT * (log(xx) + m_lnActCoeffMolal[k]);
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}
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xx = MAX(xmolSolvent, xxSmall);
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mu[m_indexSolvent] +=
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RT * (log(xx) + m_lnActCoeffMolal[m_indexSolvent]);
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}
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/*
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* Do the solvent
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* -> see my notes
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*/
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double xmolSolvent = moleFraction(m_indexSolvent);
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xx = fmaxx(xmolSolvent, xxSmall);
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mu[m_indexSolvent] +=
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(RT * (xmolSolvent - 1.0) / xx);
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}
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/*
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@ -603,14 +718,37 @@ namespace Cantera {
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doublereal R = GasConstant;
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doublereal mm;
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calcMolalities();
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for (int k = 0; k < m_kk; k++) {
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if (k != m_indexSolvent) {
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mm = fmaxx(SmallNumber, m_molalities[k]);
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sbar[k] -= R * log(mm);
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if (typeCutoff_ == 0) {
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for (int k = 0; k < m_kk; k++) {
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if (k != m_indexSolvent) {
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mm = fmaxx(SmallNumber, m_molalities[k]);
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sbar[k] -= R * log(mm);
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}
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}
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double xmolSolvent = moleFraction(m_indexSolvent);
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sbar[m_indexSolvent] -= (R * (xmolSolvent - 1.0) / xmolSolvent);
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} else {
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/*
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* Update the activity coefficients, This also update the
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* internally stored molalities.
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*/
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s_updateIMS_lnMolalityActCoeff();
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/*
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* First we will add in the obvious dependence on the T
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* term out front of the log activity term
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*/
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doublereal mm;
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for (int k = 0; k < m_kk; k++) {
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if (k != m_indexSolvent) {
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mm = fmaxx(SmallNumber, m_molalities[k]);
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sbar[k] -= R * (log(mm) + m_lnActCoeffMolal[k]);
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}
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}
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double xmolSolvent = moleFraction(m_indexSolvent);
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mm = fmaxx(SmallNumber, xmolSolvent);
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sbar[m_indexSolvent] -= R *(log(mm) + m_lnActCoeffMolal[m_indexSolvent]);
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}
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double xmolSolvent = moleFraction(m_indexSolvent);
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sbar[m_indexSolvent] -= (R * (xmolSolvent - 1.0) / xmolSolvent);
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}
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/*
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@ -862,6 +1000,50 @@ namespace Cantera {
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solventName = nameSolventa[0];
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}
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if (thermoNode.hasChild("activityCoefficients")) {
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XML_Node& acNode = thermoNode.child("activityCoefficients");
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std::string modelString = acNode.attrib("model");
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typeCutoff_ = 0;
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if (modelString != "IdealMolalSoln") {
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throw CanteraError("IdealMolalSoln::initThermoXML",
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"unknown ActivityCoefficient model: " + modelString);
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}
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if (acNode.hasChild("idealMolalSolnCutoff")) {
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XML_Node& ccNode = acNode.child("idealMolalSolnCutoff");
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modelString = ccNode.attrib("model");
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if (modelString != "") {
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if (modelString == "polyExp") {
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typeCutoff_ = 2;
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} else if (modelString == "poly") {
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typeCutoff_ = 1;
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} else {
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throw CanteraError("IdealMolalSoln::initThermoXML",
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"Unknown idealMolalSolnCutoff form: " + modelString);
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}
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if (ccNode.hasChild("gamma_o_limit")) {
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gamma_o_min_ = getFloat(ccNode, "gamma_o_limit");
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}
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if (ccNode.hasChild("gamma_k_limit")) {
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gamma_k_min_ = getFloat(ccNode, "gamma_k_limit");
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}
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if (ccNode.hasChild("X_o_cutoff")) {
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X_o_cutoff_ = getFloat(ccNode, "X_o_cutoff");
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}
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if (ccNode.hasChild("c_0_param")) {
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cCut_ = getFloat(ccNode, "c_0_param");
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}
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if (ccNode.hasChild("slope_f_limit")) {
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slopefCut_ = getFloat(ccNode, "slope_f_limit");
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}
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if (ccNode.hasChild("slope_g_limit")) {
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slopegCut_ = getFloat(ccNode, "slope_g_limit");
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}
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}
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}
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}
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/*
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* Reconcile the solvent name and index.
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@ -885,6 +1067,7 @@ namespace Cantera {
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" should be first species");
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}
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/*
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* Now go get the molar volumes
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*/
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@ -900,6 +1083,11 @@ namespace Cantera {
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m_speciesMolarVolume[k] = getFloat(*ss, "molarVolume", "toSI");
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}
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typeCutoff_ = 2;
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if (typeCutoff_ == 2) {
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calcIMSCutoffParams_();
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}
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MolalityVPSSTP::initThermoXML(phaseNode, id);
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/*
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* Set the state
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@ -960,6 +1148,130 @@ namespace Cantera {
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return 0.0;
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}
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// This function will be called to update the internally storred
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// natural logarithm of the molality activity coefficients
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/*
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* Normally they are all one. However, sometimes they are not,
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* due to stability schemes
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*
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* gamma_k_molar = gamma_k_molal / Xmol_solvent
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*
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* gamma_o_molar = gamma_o_molal
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*/
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void IdealMolalSoln::s_updateIMS_lnMolalityActCoeff() const {
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int k;
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double tmp;
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/*
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* Calculate the molalities. Currently, the molalities
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* may not be current with respect to the contents of the
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* State objects' data.
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*/
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calcMolalities();
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double xmolSolvent = moleFraction(m_indexSolvent);
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double xx = MAX(m_xmolSolventMIN, xmolSolvent);
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if (typeCutoff_ == 0) {
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for (k = 1; k < m_kk; k++) {
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m_lnActCoeffMolal[k]= 0.0;
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}
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m_lnActCoeffMolal[m_indexSolvent] = - log(xx) + (xx - 1.0)/xx;
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return;
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} else if (typeCutoff_ == 1) {
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if (xmolSolvent > 3.0 * X_o_cutoff_/2.0 ) {
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for (k = 1; k < m_kk; k++) {
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m_lnActCoeffMolal[k]= 0.0;
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}
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m_lnActCoeffMolal[m_indexSolvent] = - log(xx) + (xx - 1.0)/xx;
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return;
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} else if (xmolSolvent < X_o_cutoff_/2.0) {
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tmp = log(xx * gamma_k_min_);
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for (k = 1; k < m_kk; k++) {
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m_lnActCoeffMolal[k]= tmp;
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}
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m_lnActCoeffMolal[m_indexSolvent] = log(gamma_o_min_);
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return;
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} else {
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/*
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* If we are in the middle region, calculate the connecting polynomials
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*/
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double xminus = xmolSolvent - X_o_cutoff_/2.0;
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double xminus2 = xminus * xminus;
|
||||
double xminus3 = xminus2 * xminus;
|
||||
double x_o_cut2 = X_o_cutoff_ * X_o_cutoff_;
|
||||
double x_o_cut3 = x_o_cut2 * X_o_cutoff_;
|
||||
|
||||
double h2 = 3.5 * xminus2 / X_o_cutoff_ - 2.0 * xminus3 / x_o_cut2;
|
||||
double h2_prime = 7.0 * xminus / X_o_cutoff_ - 6.0 * xminus2 / x_o_cut2;
|
||||
|
||||
double h1 = (1.0 - 3.0 * xminus2 / x_o_cut2 + 2.0 * xminus3/ x_o_cut3);
|
||||
double h1_prime = (- 6.0 * xminus / x_o_cut2 + 6.0 * xminus2/ x_o_cut3);
|
||||
|
||||
double h1_g = h1 / gamma_o_min_;
|
||||
double h1_g_prime = h1_prime / gamma_o_min_;
|
||||
|
||||
double alpha = 1.0 / ( exp(1.0) * gamma_k_min_);
|
||||
double h1_f = h1 * alpha;
|
||||
double h1_f_prime = h1_prime * alpha;
|
||||
|
||||
double f = h2 + h1_f;
|
||||
double f_prime = h2_prime + h1_f_prime;
|
||||
|
||||
double g = h2 + h1_g;
|
||||
double g_prime = h2_prime + h1_g_prime;
|
||||
|
||||
tmp = (xmolSolvent/ g * g_prime + (1.0-xmolSolvent) / f * f_prime);
|
||||
double lngammak = -1.0 - log(f) + tmp * xmolSolvent;
|
||||
double lngammao =-log(g) - tmp * (1.0-xmolSolvent);
|
||||
|
||||
tmp = log(xmolSolvent) + lngammak;
|
||||
for (k = 1; k < m_kk; k++) {
|
||||
m_lnActCoeffMolal[k]= tmp;
|
||||
}
|
||||
m_lnActCoeffMolal[m_indexSolvent] = lngammao;
|
||||
}
|
||||
}
|
||||
|
||||
// Exponentials - trial 2
|
||||
else if (typeCutoff_ == 2) {
|
||||
if (xmolSolvent > X_o_cutoff_) {
|
||||
for (k = 1; k < m_kk; k++) {
|
||||
m_lnActCoeffMolal[k]= 0.0;
|
||||
}
|
||||
m_lnActCoeffMolal[m_indexSolvent] = - log(xx) + (xx - 1.0)/xx;
|
||||
return;
|
||||
} else {
|
||||
|
||||
double xoverc = xmolSolvent/cCut_;
|
||||
double eterm = std::exp(-xoverc);
|
||||
|
||||
double fptmp = bfCut_ - afCut_ / cCut_ - bfCut_*xoverc
|
||||
+ 2.0*dfCut_*xmolSolvent - dfCut_*xmolSolvent*xoverc;
|
||||
double f_prime = 1.0 + eterm*fptmp;
|
||||
double f = xmolSolvent + efCut_ + eterm * (afCut_ + xmolSolvent * (bfCut_ + dfCut_*xmolSolvent));
|
||||
|
||||
double gptmp = bgCut_ - agCut_ / cCut_ - bgCut_*xoverc
|
||||
+ 2.0*dgCut_*xmolSolvent - dgCut_*xmolSolvent*xoverc;
|
||||
double g_prime = 1.0 + eterm*gptmp;
|
||||
double g = xmolSolvent + egCut_ + eterm * (agCut_ + xmolSolvent * (bgCut_ + dgCut_*xmolSolvent));
|
||||
|
||||
tmp = (xmolSolvent / g * g_prime + (1.0 - xmolSolvent) / f * f_prime);
|
||||
double lngammak = -1.0 - log(f) + tmp * xmolSolvent;
|
||||
double lngammao =-log(g) - tmp * (1.0-xmolSolvent);
|
||||
|
||||
tmp = log(xx) + lngammak;
|
||||
for (k = 1; k < m_kk; k++) {
|
||||
m_lnActCoeffMolal[k]= tmp;
|
||||
}
|
||||
m_lnActCoeffMolal[m_indexSolvent] = lngammao;
|
||||
}
|
||||
}
|
||||
return;
|
||||
}
|
||||
|
||||
/*
|
||||
* This internal function adjusts the lengths of arrays.
|
||||
*
|
||||
|
|
@ -977,6 +1289,75 @@ namespace Cantera {
|
|||
m_pp.resize(leng);
|
||||
m_speciesMolarVolume.resize(leng);
|
||||
m_tmpV.resize(leng);
|
||||
m_lnActCoeffMolal.resize(leng);
|
||||
}
|
||||
|
||||
|
||||
void IdealMolalSoln::calcIMSCutoffParams_() {
|
||||
|
||||
|
||||
afCut_ = 1.0 / (std::exp(1.0) * gamma_k_min_);
|
||||
efCut_ = 0.0;
|
||||
bool converged = false;
|
||||
double oldV = 0.0;
|
||||
int its;
|
||||
for (its = 0; its < 100 && !converged; its++) {
|
||||
oldV = efCut_;
|
||||
afCut_ = 1.0 / (std::exp(1.0) * gamma_k_min_) -efCut_;
|
||||
|
||||
bfCut_ = afCut_ / cCut_ + slopefCut_ - 1.0;
|
||||
|
||||
dfCut_ = ((- afCut_/cCut_ + bfCut_ - bfCut_*X_o_cutoff_/cCut_)
|
||||
/
|
||||
(X_o_cutoff_*X_o_cutoff_/cCut_ - 2.0 * X_o_cutoff_));
|
||||
|
||||
double tmp = afCut_ + X_o_cutoff_*( bfCut_ + dfCut_ *X_o_cutoff_);
|
||||
double eterm = std::exp(-X_o_cutoff_/cCut_);
|
||||
|
||||
efCut_ = - eterm * (tmp);
|
||||
|
||||
if (fabs(efCut_ - oldV) < 1.0E-14) {
|
||||
converged = true;
|
||||
}
|
||||
}
|
||||
|
||||
if (!converged) {
|
||||
throw CanteraError(" IdealMolalSoln::calcCutoffParams_()",
|
||||
" failed to converge on the f polynomial");
|
||||
}
|
||||
converged = false;
|
||||
double f_0 = afCut_ + efCut_;
|
||||
double f_prime_0 = 1.0 - afCut_ / cCut_ + bfCut_;
|
||||
|
||||
egCut_ = 0.0;
|
||||
|
||||
for (its = 0; its < 100 && !converged; its++) {
|
||||
oldV = egCut_;
|
||||
|
||||
double lng_0 = -log(gamma_o_min_) - f_prime_0 / f_0;
|
||||
|
||||
agCut_ = exp(lng_0) - egCut_;
|
||||
|
||||
bgCut_ = agCut_ / cCut_ + slopegCut_ - 1.0;
|
||||
|
||||
dgCut_ = ((- agCut_/cCut_ + bgCut_ - bgCut_*X_o_cutoff_/cCut_)
|
||||
/
|
||||
(X_o_cutoff_*X_o_cutoff_/cCut_ - 2.0 * X_o_cutoff_));
|
||||
|
||||
double tmp = agCut_ + X_o_cutoff_*( bgCut_ + dgCut_ *X_o_cutoff_);
|
||||
double eterm = std::exp(-X_o_cutoff_/cCut_);
|
||||
|
||||
egCut_ = - eterm * (tmp);
|
||||
|
||||
if (fabs(egCut_ - oldV) < 1.0E-14) {
|
||||
converged = true;
|
||||
}
|
||||
}
|
||||
if (!converged) {
|
||||
throw CanteraError(" IdealMolalSoln::calcCutoffParams_()",
|
||||
" failed to converge on the f polynomial");
|
||||
}
|
||||
|
||||
}
|
||||
|
||||
}
|
||||
|
|
|
|||
|
|
@ -84,6 +84,31 @@ namespace Cantera {
|
|||
*
|
||||
* The value and form of the activity concentration will affect
|
||||
* reaction rate constants involving species in this phase.
|
||||
*
|
||||
* @verbatim
|
||||
<thermo model="IdealMolalSoln">
|
||||
<standardConc model="solvent_volume" />
|
||||
<solvent> H2O(l) </solvent>
|
||||
|
||||
<activityCoefficients model="IdealMolalSoln" >
|
||||
<idealMolalSolnCutoff model="polyExp">
|
||||
<gamma_O_limit> 1.0E-5 <gammaOlimit>
|
||||
<gamma_k_limit> 1.0E-5 <gammaklimit>
|
||||
<X_o_cutoff> 0.20 </X_o_cutoff>
|
||||
<C_0_param> 0.05 </C_0_param>
|
||||
<slope_f_limit> 0.6 </slopefLimit>
|
||||
<slope_g_limit> 0.0 </slopegLimit>
|
||||
</idealMolalSolnCutoff>
|
||||
</activityCoefficients>
|
||||
|
||||
|
||||
|
||||
</thermo>
|
||||
|
||||
|
||||
|
||||
@endverbatim
|
||||
*
|
||||
*/
|
||||
class IdealMolalSoln : public MolalityVPSSTP {
|
||||
|
||||
|
|
@ -873,7 +898,13 @@ namespace Cantera {
|
|||
* <TR><TD> 2 </TD><TD> \f$ m_k / (m^{\Delta} V^0_0)\f$</TD><TD> \f$ 1.0 / V^0_0\f$ </TD></TR>
|
||||
* </TABLE>
|
||||
*/
|
||||
int m_formGC;
|
||||
int m_formGC;
|
||||
|
||||
public:
|
||||
//! Cutoff type
|
||||
int typeCutoff_;
|
||||
|
||||
private:
|
||||
|
||||
/**
|
||||
* Vector containing the species reference exp(-G/RT) functions
|
||||
|
|
@ -895,12 +926,94 @@ namespace Cantera {
|
|||
* vector of size m_kk, used as a temporary holding area.
|
||||
*/
|
||||
mutable vector_fp m_tmpV;
|
||||
|
||||
//! Logarithm of the molal activity coefficients
|
||||
/*!
|
||||
* Normally these are all one. However, stability schemes will change that
|
||||
*/
|
||||
mutable vector_fp m_lnActCoeffMolal;
|
||||
public:
|
||||
//! value of the solute mole fraction that centers the cutoff polynomials
|
||||
//! for the cutoff =1 process;
|
||||
doublereal X_o_cutoff_;
|
||||
|
||||
//! gamma_o value for the cutoff process at the zero solvent point
|
||||
doublereal gamma_o_min_;
|
||||
|
||||
//! gamma_k minimun for the cutoff process at the zero solvent point
|
||||
doublereal gamma_k_min_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment having to do with rate of exp decay
|
||||
doublereal cCut_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment
|
||||
/*!
|
||||
* This is the slope of the f function at the zero solvent point
|
||||
* Default value is 0.6
|
||||
*/
|
||||
doublereal slopefCut_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment having to do with rate of exp decay
|
||||
doublereal dfCut_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment having to do with rate of exp decay
|
||||
doublereal efCut_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment having to do with rate of exp decay
|
||||
doublereal afCut_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment having to do with rate of exp decay
|
||||
doublereal bfCut_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment
|
||||
/*!
|
||||
* This is the slope of the g function at the zero solvent point
|
||||
* Default value is 0.0
|
||||
*/
|
||||
doublereal slopegCut_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment having to do with rate of exp decay
|
||||
doublereal dgCut_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment having to do with rate of exp decay
|
||||
doublereal egCut_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment having to do with rate of exp decay
|
||||
doublereal agCut_;
|
||||
|
||||
//! Parameter in the polyExp cutoff treatment having to do with rate of exp decay
|
||||
doublereal bgCut_;
|
||||
|
||||
private:
|
||||
|
||||
//! Internal error message
|
||||
/*!
|
||||
* param msg message to be printed
|
||||
*/
|
||||
doublereal err(std::string msg) const;
|
||||
|
||||
//! This function will be called to update the internally storred
|
||||
//! natural logarithm of the molality activity coefficients
|
||||
/*!
|
||||
* Normally the solutes are all zero. However, sometimes they are not,
|
||||
* due to stability schemes
|
||||
*/
|
||||
void s_updateIMS_lnMolalityActCoeff() const;
|
||||
|
||||
//! This internal function adjusts the lengths of arrays.
|
||||
/*!
|
||||
* This function is not virtual nor is it inherited
|
||||
*/
|
||||
void initLengths();
|
||||
|
||||
//! Calculate parameters for cutoff treatments of activity coefficients
|
||||
/*!
|
||||
* Some cutoff treatments for the activity coefficients
|
||||
* actually require some calculations to create a consistent treatment.
|
||||
*
|
||||
* This routine is called during the setup to calculate these parameters
|
||||
*/
|
||||
void calcIMSCutoffParams_();
|
||||
};
|
||||
|
||||
/* @} */
|
||||
|
|
|
|||
Loading…
Add table
Reference in a new issue