Simplified AqueousKinetics by eliminating class AqueousKineticsData
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2 changed files with 64 additions and 147 deletions
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@ -32,40 +32,7 @@ namespace Cantera
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// forward references
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class ReactionData;
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class AqueousKineticsData;
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class Thermo;
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/**
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* Holds mechanism-specific data.
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*/
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class AqueousKineticsData
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{
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public:
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AqueousKineticsData();
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~AqueousKineticsData();
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AqueousKineticsData(const AqueousKineticsData& right);
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AqueousKineticsData& operator=(const AqueousKineticsData& right);
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doublereal m_logp_ref;
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doublereal m_logc_ref;
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vector_fp m_ropf;
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vector_fp m_ropr;
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vector_fp m_ropnet;
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vector_fp m_rfn_low;
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vector_fp m_rfn_high;
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bool m_ROP_ok;
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doublereal m_temp;
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vector_fp m_rfn;
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vector_fp m_rkcn;
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};
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/**
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* Kinetics manager for elementary aqueous-phase chemistry. This
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@ -141,7 +108,7 @@ public:
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*/
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virtual void getFwdRatesOfProgress(doublereal* fwdROP) {
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updateROP();
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std::copy(m_kdata->m_ropf.begin(), m_kdata->m_ropf.end(), fwdROP);
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std::copy(m_ropf.begin(), m_ropf.end(), fwdROP);
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}
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/**
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@ -152,7 +119,7 @@ public:
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*/
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virtual void getRevRatesOfProgress(doublereal* revROP) {
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updateROP();
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std::copy(m_kdata->m_ropr.begin(), m_kdata->m_ropr.end(), revROP);
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std::copy(m_ropr.begin(), m_ropr.end(), revROP);
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}
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/**
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@ -163,7 +130,7 @@ public:
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*/
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virtual void getNetRatesOfProgress(doublereal* netROP) {
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updateROP();
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std::copy(m_kdata->m_ropnet.begin(), m_kdata->m_ropnet.end(), netROP);
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std::copy(m_ropnet.begin(), m_ropnet.end(), netROP);
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}
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@ -253,8 +220,7 @@ public:
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//#ifdef HWMECH
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//get_wdot(&m_kdata->m_ropnet[0], net);
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//#else
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m_rxnstoich->getNetProductionRates(m_kk,
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&m_kdata->m_ropnet[0], net);
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m_rxnstoich->getNetProductionRates(m_kk, &m_ropnet[0], net);
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//#endif
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}
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@ -267,8 +233,7 @@ public:
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*/
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virtual void getCreationRates(doublereal* cdot) {
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updateROP();
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m_rxnstoich->getCreationRates(m_kk, &m_kdata->m_ropf[0],
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&m_kdata->m_ropr[0], cdot);
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m_rxnstoich->getCreationRates(m_kk, &m_ropf[0], &m_ropr[0], cdot);
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}
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/**
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@ -280,9 +245,7 @@ public:
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*/
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virtual void getDestructionRates(doublereal* ddot) {
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updateROP();
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m_rxnstoich->getDestructionRates(m_kk, &m_kdata->m_ropf[0],
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&m_kdata->m_ropr[0], ddot);
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m_rxnstoich->getDestructionRates(m_kk, &m_ropf[0], &m_ropr[0], ddot);
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}
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//@}
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@ -406,11 +369,21 @@ protected:
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std::vector<std::string> m_rxneqn;
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AqueousKineticsData* m_kdata;
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vector_fp m_conc;
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vector_fp m_grt;
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//! @name Aqueous kinetics data
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//!@{
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vector_fp m_ropf;
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vector_fp m_ropr;
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vector_fp m_ropnet;
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bool m_ROP_ok;
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doublereal m_temp;
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vector_fp m_rfn;
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vector_fp m_rkcn;
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//!@}
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private:
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@ -21,49 +21,6 @@ using namespace std;
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namespace Cantera
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{
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//====================================================================================================================
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AqueousKineticsData::AqueousKineticsData() :
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m_logp_ref(0.0),
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m_logc_ref(0.0),
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m_ROP_ok(false),
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m_temp(0.0)
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{
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}
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//====================================================================================================================
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AqueousKineticsData::~AqueousKineticsData()
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{
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}
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//====================================================================================================================
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AqueousKineticsData::AqueousKineticsData(const AqueousKineticsData& right) :
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m_logp_ref(0.0),
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m_logc_ref(0.0),
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m_ROP_ok(false),
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m_temp(0.0)
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{
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*this=right;
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}
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//====================================================================================================================
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AqueousKineticsData& AqueousKineticsData::operator=(const AqueousKineticsData& right)
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{
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if (this != &right) {
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m_logp_ref = right.m_logp_ref;
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m_logc_ref = right.m_logc_ref;
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m_ropf = right.m_ropf;
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m_ropr = right.m_ropr;
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m_ropnet = right.m_ropnet;
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m_rfn_low = right.m_rfn_low;
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m_rfn_high = right.m_rfn_high;
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m_ROP_ok = right.m_ROP_ok;
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m_temp = right.m_temp;
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m_rfn = right.m_rfn;
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m_rkcn = right.m_rkcn;
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}
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return *this;
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}
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//====================================================================================================================
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//====================================================================================================================
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/**
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* Construct an empty reaction mechanism.
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@ -73,13 +30,13 @@ AqueousKinetics::AqueousKinetics(thermo_t* thermo) :
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m_nfall(0),
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m_nirrev(0),
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m_nrev(0),
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m_ROP_ok(false),
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m_temp(0.0),
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m_finalized(false)
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{
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if (thermo != 0) {
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addPhase(*thermo);
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}
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m_kdata = new AqueousKineticsData;
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m_kdata->m_temp = 0.0;
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m_rxnstoich = new ReactionStoichMgr;
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}
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//====================================================================================================================
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@ -88,6 +45,8 @@ AqueousKinetics::AqueousKinetics(const AqueousKinetics& right) :
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m_nfall(0),
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m_nirrev(0),
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m_nrev(0),
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m_ROP_ok(false),
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m_temp(0.0),
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m_finalized(false)
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{
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*this = right;
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@ -95,7 +54,6 @@ AqueousKinetics::AqueousKinetics(const AqueousKinetics& right) :
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//====================================================================================================================
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AqueousKinetics::~AqueousKinetics()
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{
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delete m_kdata;
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delete m_rxnstoich;
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}
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//====================================================================================================================
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@ -126,7 +84,13 @@ AqueousKinetics& AqueousKinetics::operator=(const AqueousKinetics& right)
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m_revindex = right.m_revindex;
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m_rxneqn = right.m_rxneqn;
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*m_kdata = *(right.m_kdata);
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m_ropf = right.m_ropf;
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m_ropr = right.m_ropr;
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m_ropnet = right.m_ropnet;
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m_ROP_ok = right.m_ROP_ok;
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m_temp = right.m_temp;
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m_rfn = right.m_rfn;
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m_rkcn = right.m_rkcn;
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m_conc = right.m_conc;
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m_grt = right.m_grt;
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@ -160,15 +124,12 @@ update_C() {}
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void AqueousKinetics::_update_rates_T()
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{
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doublereal T = thermo().temperature();
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// m_kdata->m_logStandConc = log(thermo().standardConcentration());
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doublereal logT = log(T);
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m_rates.update(T, logT, &m_kdata->m_rfn[0]);
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m_rates.update(T, logT, &m_rfn[0]);
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m_kdata->m_temp = T;
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m_temp = T;
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updateKc();
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m_kdata->m_ROP_ok = false;
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m_ROP_ok = false;
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};
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@ -181,7 +142,7 @@ _update_rates_C()
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{
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thermo().getActivityConcentrations(&m_conc[0]);
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m_kdata->m_ROP_ok = false;
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m_ROP_ok = false;
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}
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/**
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@ -189,28 +150,27 @@ _update_rates_C()
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*/
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void AqueousKinetics::updateKc()
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{
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vector_fp& m_rkc = m_kdata->m_rkcn;
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doublereal rt = GasConstant* m_kdata->m_temp;
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doublereal rt = GasConstant * m_temp;
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thermo().getStandardChemPotentials(&m_grt[0]);
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fill(m_rkc.begin(), m_rkc.end(), 0.0);
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fill(m_rkcn.begin(), m_rkcn.end(), 0.0);
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for (size_t k = 0; k < thermo().nSpecies(); k++) {
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doublereal logStandConc_k = thermo().logStandardConc(k);
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m_grt[k] -= rt * logStandConc_k;
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}
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// compute Delta G^0 for all reversible reactions
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m_rxnstoich->getRevReactionDelta(m_ii, &m_grt[0], &m_rkc[0]);
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m_rxnstoich->getRevReactionDelta(m_ii, &m_grt[0], &m_rkcn[0]);
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//doublereal logStandConc = m_kdata->m_logStandConc;
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doublereal rrt = 1.0/(GasConstant * thermo().temperature());
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for (size_t i = 0; i < m_nrev; i++) {
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size_t irxn = m_revindex[i];
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m_rkc[irxn] = exp(m_rkc[irxn]*rrt);
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m_rkcn[irxn] = exp(m_rkcn[irxn]*rrt);
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}
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for (size_t i = 0; i != m_nirrev; ++i) {
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m_rkc[ m_irrev[i] ] = 0.0;
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m_rkcn[ m_irrev[i] ] = 0.0;
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}
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}
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@ -221,27 +181,26 @@ void AqueousKinetics::updateKc()
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void AqueousKinetics::getEquilibriumConstants(doublereal* kc)
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{
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_update_rates_T();
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vector_fp& rkc = m_kdata->m_rkcn;
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thermo().getStandardChemPotentials(&m_grt[0]);
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fill(rkc.begin(), rkc.end(), 0.0);
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doublereal rt = GasConstant * m_kdata->m_temp;
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fill(m_rkcn.begin(), m_rkcn.end(), 0.0);
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doublereal rt = GasConstant * m_temp;
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for (size_t k = 0; k < thermo().nSpecies(); k++) {
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doublereal logStandConc_k = thermo().logStandardConc(k);
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m_grt[k] -= rt * logStandConc_k;
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}
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// compute Delta G^0 for all reactions
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m_rxnstoich->getReactionDelta(m_ii, &m_grt[0], &rkc[0]);
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m_rxnstoich->getReactionDelta(m_ii, &m_grt[0], &m_rkcn[0]);
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doublereal rrt = 1.0/(GasConstant * thermo().temperature());
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for (size_t i = 0; i < m_ii; i++) {
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kc[i] = exp(-rkc[i]*rrt);
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kc[i] = exp(-m_rkcn[i]*rrt);
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}
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// force an update of T-dependent properties, so that m_rkcn will
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// be updated before it is used next.
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m_kdata->m_temp = 0.0;
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m_temp = 0.0;
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}
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/**
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@ -411,49 +370,41 @@ void AqueousKinetics::getDeltaSSEntropy(doublereal* deltaS)
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void AqueousKinetics::updateROP()
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{
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_update_rates_T();
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_update_rates_C();
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if (m_kdata->m_ROP_ok) {
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if (m_ROP_ok) {
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return;
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}
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const vector_fp& rf = m_kdata->m_rfn;
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const vector_fp& m_rkc = m_kdata->m_rkcn;
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vector_fp& ropf = m_kdata->m_ropf;
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vector_fp& ropr = m_kdata->m_ropr;
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vector_fp& ropnet = m_kdata->m_ropnet;
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// copy rate coefficients into ropf
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copy(rf.begin(), rf.end(), ropf.begin());
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copy(m_rfn.begin(), m_rfn.end(), m_ropf.begin());
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// multiply by perturbation factor
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multiply_each(ropf.begin(), ropf.end(), m_perturb.begin());
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multiply_each(m_ropf.begin(), m_ropf.end(), m_perturb.begin());
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// copy the forward rates to the reverse rates
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copy(ropf.begin(), ropf.end(), ropr.begin());
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copy(m_ropf.begin(), m_ropf.end(), m_ropr.begin());
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// for reverse rates computed from thermochemistry, multiply
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// the forward rates copied into m_ropr by the reciprocals of
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// the equilibrium constants
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multiply_each(ropr.begin(), ropr.end(), m_rkc.begin());
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multiply_each(m_ropr.begin(), m_ropr.end(), m_rkcn.begin());
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// multiply ropf by concentration products
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m_rxnstoich->multiplyReactants(&m_conc[0], &ropf[0]);
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m_rxnstoich->multiplyReactants(&m_conc[0], &m_ropf[0]);
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//m_reactantStoich.multiply(m_conc.begin(), ropf.begin());
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// for reversible reactions, multiply ropr by concentration
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// products
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m_rxnstoich->multiplyRevProducts(&m_conc[0], &ropr[0]);
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m_rxnstoich->multiplyRevProducts(&m_conc[0], &m_ropr[0]);
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//m_revProductStoich.multiply(m_conc.begin(), ropr.begin());
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for (size_t j = 0; j != m_ii; ++j) {
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ropnet[j] = ropf[j] - ropr[j];
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m_ropnet[j] = m_ropf[j] - m_ropr[j];
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}
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m_kdata->m_ROP_ok = true;
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m_ROP_ok = true;
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}
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/**
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@ -471,17 +422,13 @@ getFwdRateConstants(doublereal* kfwd)
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_update_rates_C();
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// copy rate coefficients into ropf
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const vector_fp& rf = m_kdata->m_rfn;
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vector_fp& ropf = m_kdata->m_ropf;
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copy(rf.begin(), rf.end(), ropf.begin());
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copy(m_rfn.begin(), m_rfn.end(), m_ropf.begin());
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// multiply by perturbation factor
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multiply_each(ropf.begin(), ropf.end(), m_perturb.begin());
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multiply_each(m_ropf.begin(), m_ropf.end(), m_perturb.begin());
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for (size_t i = 0; i < m_ii; i++) {
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kfwd[i] = ropf[i];
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kfwd[i] = m_ropf[i];
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}
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}
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@ -507,18 +454,16 @@ getRevRateConstants(doublereal* krev, bool doIrreversible)
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getFwdRateConstants(krev);
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if (doIrreversible) {
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doublereal* tmpKc = &m_kdata->m_ropnet[0];
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getEquilibriumConstants(tmpKc);
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getEquilibriumConstants(&m_ropnet[0]);
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for (size_t i = 0; i < m_ii; i++) {
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krev[i] /= tmpKc[i];
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krev[i] /= m_ropnet[i];
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}
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} else {
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/*
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* m_rkc[] is zero for irreversibly reactions
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* m_rkcn[] is zero for irreversible reactions
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*/
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const vector_fp& m_rkc = m_kdata->m_rkcn;
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for (size_t i = 0; i < m_ii; i++) {
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krev[i] *= m_rkc[i];
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krev[i] *= m_rkcn[i];
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}
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}
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}
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@ -548,7 +493,7 @@ void AqueousKinetics::addElementaryReaction(ReactionData& r)
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iloc = m_rates.install(reactionNumber(), r);
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// add constant term to rate coeff value vector
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m_kdata->m_rfn.push_back(r.rateCoeffParameters[0]);
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m_rfn.push_back(r.rateCoeffParameters[0]);
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// forward rxn order equals number of reactants
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m_fwdOrder.push_back(r.reactants.size());
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@ -561,9 +506,9 @@ void AqueousKinetics::addElementaryReaction(ReactionData& r)
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void AqueousKinetics::installReagents(const ReactionData& r)
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{
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m_kdata->m_ropf.push_back(0.0); // extend by one for new rxn
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m_kdata->m_ropr.push_back(0.0);
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m_kdata->m_ropnet.push_back(0.0);
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m_ropf.push_back(0.0); // extend by one for new rxn
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m_ropr.push_back(0.0);
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m_ropnet.push_back(0.0);
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size_t n, ns, m;
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doublereal nsFlt;
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||||
doublereal reactantGlobalOrder = 0.0;
|
||||
|
|
@ -610,7 +555,7 @@ void AqueousKinetics::installReagents(const ReactionData& r)
|
|||
}
|
||||
m_products.push_back(pk);
|
||||
|
||||
m_kdata->m_rkcn.push_back(0.0);
|
||||
m_rkcn.push_back(0.0);
|
||||
|
||||
m_rxnstoich->add(reactionNumber(), r);
|
||||
|
||||
|
|
@ -645,7 +590,6 @@ void AqueousKinetics::init()
|
|||
m_prxn.resize(m_kk);
|
||||
m_conc.resize(m_kk);
|
||||
m_grt.resize(m_kk);
|
||||
m_kdata->m_logp_ref = log(thermo().refPressure()) - log(GasConstant);
|
||||
}
|
||||
|
||||
void AqueousKinetics::finalize()
|
||||
|
|
|
|||
Loading…
Add table
Reference in a new issue