Make use of "make_shared" where possible
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a945ef2c23
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8 changed files with 43 additions and 43 deletions
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@ -38,6 +38,7 @@ namespace Cantera
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#endif
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using std::shared_ptr;
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using std::make_shared;
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/*!
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* All physical constants are stored here.
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@ -590,39 +590,39 @@ shared_ptr<Reaction> newReaction(const XML_Node& rxn_node)
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// Create a new Reaction object of the appropriate type
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if (type == "elementary" || type == "arrhenius" || type == "") {
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shared_ptr<ElementaryReaction> R(new ElementaryReaction());
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auto R = make_shared<ElementaryReaction>();
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setupElementaryReaction(*R, rxn_node);
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return R;
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} else if (type == "threebody" || type == "three_body") {
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shared_ptr<ThreeBodyReaction> R(new ThreeBodyReaction());
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auto R = make_shared<ThreeBodyReaction>();
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setupThreeBodyReaction(*R, rxn_node);
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return R;
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} else if (type == "falloff") {
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shared_ptr<FalloffReaction> R(new FalloffReaction());
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auto R = make_shared<FalloffReaction>();
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setupFalloffReaction(*R, rxn_node);
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return R;
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} else if (type == "chemact" || type == "chemically_activated") {
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shared_ptr<ChemicallyActivatedReaction> R(new ChemicallyActivatedReaction());
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auto R = make_shared<ChemicallyActivatedReaction>();
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setupChemicallyActivatedReaction(*R, rxn_node);
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return R;
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} else if (type == "plog" || type == "pdep_arrhenius") {
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shared_ptr<PlogReaction> R(new PlogReaction());
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auto R = make_shared<PlogReaction>();
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setupPlogReaction(*R, rxn_node);
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return R;
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} else if (type == "chebyshev") {
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shared_ptr<ChebyshevReaction> R(new ChebyshevReaction());
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auto R = make_shared<ChebyshevReaction>();
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setupChebyshevReaction(*R, rxn_node);
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return R;
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} else if (type == "interface" || type == "surface" || type == "edge" ||
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type == "global") {
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shared_ptr<InterfaceReaction> R(new InterfaceReaction());
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auto R = make_shared<InterfaceReaction>();
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setupInterfaceReaction(*R, rxn_node);
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return R;
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} else if (type == "electrochemical" ||
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type == "butlervolmer_noactivitycoeffs" ||
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type == "butlervolmer" ||
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type == "surfaceaffinity") {
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shared_ptr<ElectrochemicalReaction> R(new ElectrochemicalReaction());
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auto R = make_shared<ElectrochemicalReaction>();
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setupElectrochemicalReaction(*R, rxn_node);
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return R;
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} else {
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@ -49,7 +49,7 @@ FixedChemPotSSTP::FixedChemPotSSTP(const std::string& Ename, doublereal val) :
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setName(pname);
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setNDim(3);
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addElement(Ename);
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shared_ptr<Species> sp(new Species(pname, parseCompString(Ename + ":1.0")));
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auto sp = make_shared<Species>(pname, parseCompString(Ename + ":1.0"));
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double c[4] = {298.15, val, 0.0, 0.0};
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shared_ptr<SpeciesThermoInterpType> stit(
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newSpeciesThermoInterpType("const_cp", 0.1, 1e30, OneAtm, c));
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@ -99,7 +99,7 @@ void GeneralSpeciesThermo::install_STIT(size_t index,
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void GeneralSpeciesThermo::installPDSShandler(size_t k, PDSS* PDSS_ptr,
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VPSSMgr* vpssmgr_ptr)
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{
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shared_ptr<SpeciesThermoInterpType> stit_ptr(new STITbyPDSS(vpssmgr_ptr, PDSS_ptr));
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auto stit_ptr = make_shared<STITbyPDSS>(vpssmgr_ptr, PDSS_ptr);
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install_STIT(k, stit_ptr);
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}
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@ -61,7 +61,7 @@ shared_ptr<Species> newSpecies(const XML_Node& species_node)
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{
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std::string name = species_node["name"];
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compositionMap comp = parseCompString(species_node.child("atomArray").value());
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shared_ptr<Species> s(new Species(name, comp));
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auto s = make_shared<Species>(name, comp);
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if (species_node.hasChild("charge")) {
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s->charge = getFloat(species_node, "charge");
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}
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@ -129,12 +129,12 @@ shared_ptr<TransportData> newTransportData(const XML_Node& transport_node)
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{
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std::string model = transport_node["model"];
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if (model == "gas_transport") {
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shared_ptr<GasTransportData> tr(new GasTransportData());
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auto tr = make_shared<GasTransportData>();
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setupGasTransportData(*tr, transport_node);
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return tr;
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} else {
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// Transport model not handled here
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return shared_ptr<TransportData>(new TransportData());
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return make_shared<TransportData>();
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}
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}
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@ -54,7 +54,7 @@ TEST_F(KineticsFromScratch, add_elementary_reaction)
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Composition reac = parseCompString("O:1 H2:1");
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Composition prod = parseCompString("H:1 OH:1");
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Arrhenius rate(3.87e1, 2.7, 6260.0 / GasConst_cal_mol_K);
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shared_ptr<ElementaryReaction> R(new ElementaryReaction(reac, prod, rate));
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auto R = make_shared<ElementaryReaction>(reac, prod, rate);
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kin.addReaction(R);
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kin.finalize();
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@ -71,7 +71,7 @@ TEST_F(KineticsFromScratch, add_three_body_reaction)
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Arrhenius rate(1.2e11, -1.0, 0.0);
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ThirdBody tbody;
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tbody.efficiencies = parseCompString("AR:0.83 H2:2.4 H2O:15.4");
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shared_ptr<ThreeBodyReaction> R(new ThreeBodyReaction(reac, prod, rate, tbody));
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auto R = make_shared<ThreeBodyReaction>(reac, prod, rate, tbody);
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kin.addReaction(R);
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kin.finalize();
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@ -85,7 +85,7 @@ TEST_F(KineticsFromScratch, undefined_third_body)
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Arrhenius rate(1.2e11, -1.0, 0.0);
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ThirdBody tbody;
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tbody.efficiencies = parseCompString("H2:0.1 CO2:0.83");
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shared_ptr<ThreeBodyReaction> R(new ThreeBodyReaction(reac, prod, rate, tbody));
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auto R = make_shared<ThreeBodyReaction>(reac, prod, rate, tbody);
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ASSERT_THROW(kin.addReaction(R), CanteraError);
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}
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@ -97,7 +97,7 @@ TEST_F(KineticsFromScratch, skip_undefined_third_body)
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Arrhenius rate(1.2e11, -1.0, 0.0);
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ThirdBody tbody;
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tbody.efficiencies = parseCompString("H2:0.1 CO2:0.83");
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shared_ptr<ThreeBodyReaction> R(new ThreeBodyReaction(reac, prod, rate, tbody));
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auto R = make_shared<ThreeBodyReaction>(reac, prod, rate, tbody);
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kin.skipUndeclaredThirdBodies(true);
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kin.addReaction(R);
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@ -120,8 +120,7 @@ TEST_F(KineticsFromScratch, add_falloff_reaction)
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vector_fp falloff_params { 0.7346, 94.0, 1756.0, 5182.0 };
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ThirdBody tbody;
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tbody.efficiencies = parseCompString("AR:0.7 H2:2.0 H2O:6.0");
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shared_ptr<FalloffReaction> R(new FalloffReaction(reac, prod, low_rate,
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high_rate, tbody));
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auto R = make_shared<FalloffReaction>(reac, prod, low_rate, high_rate, tbody);
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R->falloff = newFalloff(TROE_FALLOFF, falloff_params);
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kin.addReaction(R);
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kin.finalize();
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@ -145,7 +144,7 @@ TEST_F(KineticsFromScratch, add_plog_reaction)
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{ 100.0*101325, Arrhenius(5.963200e+56, -11.529, 52599.6 / GasConst_cal_mol_K) }
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};
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shared_ptr<PlogReaction> R(new PlogReaction(reac, prod, Plog(rates)));
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auto R = make_shared<PlogReaction>(reac, prod, Plog(rates));
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kin.addReaction(R);
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kin.finalize();
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check_rates(3);
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@ -162,7 +161,7 @@ TEST_F(KineticsFromScratch, plog_invalid_rate)
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{ 100.0*101325, Arrhenius(5.9632e+56, -11.529, 52599.6 / GasConst_cal_mol_K) }
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};
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shared_ptr<PlogReaction> R(new PlogReaction(reac, prod, Plog(rates)));
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auto R = make_shared<PlogReaction>(reac, prod, Plog(rates));
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ASSERT_THROW(kin.addReaction(R), CanteraError);
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}
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@ -193,7 +192,7 @@ TEST_F(KineticsFromScratch, add_chebyshev_reaction)
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coeffs(2,3) = -7.6385e-03;
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ChebyshevRate rate(290, 3000, 1000.0, 10000000.0, coeffs);
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shared_ptr<ChebyshevReaction> R(new ChebyshevReaction(reac, prod, rate));
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auto R = make_shared<ChebyshevReaction>(reac, prod, rate);
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kin.addReaction(R);
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kin.finalize();
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check_rates(4);
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@ -204,7 +203,7 @@ TEST_F(KineticsFromScratch, undeclared_species)
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Composition reac = parseCompString("CO:1 OH:1");
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Composition prod = parseCompString("CO2:1 H:1");
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Arrhenius rate(3.87e1, 2.7, 6260.0 / GasConst_cal_mol_K);
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shared_ptr<ElementaryReaction> R(new ElementaryReaction(reac, prod, rate));
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auto R = make_shared<ElementaryReaction>(reac, prod, rate);
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ASSERT_THROW(kin.addReaction(R), CanteraError);
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ASSERT_EQ(0, kin.nReactions());
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@ -215,7 +214,7 @@ TEST_F(KineticsFromScratch, skip_undeclared_species)
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Composition reac = parseCompString("CO:1 OH:1");
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Composition prod = parseCompString("CO2:1 H:1");
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Arrhenius rate(3.87e1, 2.7, 6260.0 / GasConst_cal_mol_K);
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shared_ptr<ElementaryReaction> R(new ElementaryReaction(reac, prod, rate));
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auto R = make_shared<ElementaryReaction>(reac, prod, rate);
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kin.skipUndeclaredSpecies(true);
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kin.addReaction(R);
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@ -227,7 +226,7 @@ TEST_F(KineticsFromScratch, negative_A_error)
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Composition reac = parseCompString("O:1 H2:1");
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Composition prod = parseCompString("H:1 OH:1");
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Arrhenius rate(-3.87e1, 2.7, 6260.0 / GasConst_cal_mol_K);
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shared_ptr<ElementaryReaction> R(new ElementaryReaction(reac, prod, rate));
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auto R = make_shared<ElementaryReaction>(reac, prod, rate);
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ASSERT_THROW(kin.addReaction(R), CanteraError);
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ASSERT_EQ(0, kin.nReactions());
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@ -238,7 +237,7 @@ TEST_F(KineticsFromScratch, allow_negative_A)
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Composition reac = parseCompString("O:1 H2:1");
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Composition prod = parseCompString("H:1 OH:1");
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Arrhenius rate(-3.87e1, 2.7, 6260.0 / GasConst_cal_mol_K);
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shared_ptr<ElementaryReaction> R(new ElementaryReaction(reac, prod, rate));
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auto R = make_shared<ElementaryReaction>(reac, prod, rate);
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R->allow_negative_pre_exponential_factor = true;
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kin.addReaction(R);
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@ -250,7 +249,7 @@ TEST_F(KineticsFromScratch, invalid_reversible_with_orders)
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Composition reac = parseCompString("O:1 H2:1");
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Composition prod = parseCompString("H:1 OH:1");
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Arrhenius rate(3.87e1, 2.7, 6260.0 / GasConst_cal_mol_K);
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shared_ptr<ElementaryReaction> R(new ElementaryReaction(reac, prod, rate));
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auto R = make_shared<ElementaryReaction>(reac, prod, rate);
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R->orders["H2"] = 0.5;
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ASSERT_THROW(kin.addReaction(R), CanteraError);
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@ -262,7 +261,7 @@ TEST_F(KineticsFromScratch, negative_order_override)
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Composition reac = parseCompString("O:1 H2:1");
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Composition prod = parseCompString("H:1 OH:1");
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Arrhenius rate(3.87e1, 2.7, 6260.0 / GasConst_cal_mol_K);
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shared_ptr<ElementaryReaction> R(new ElementaryReaction(reac, prod, rate));
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auto R = make_shared<ElementaryReaction>(reac, prod, rate);
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R->reversible = false;
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R->allow_negative_orders = true;
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R->orders["H2"] = - 0.5;
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@ -276,7 +275,7 @@ TEST_F(KineticsFromScratch, invalid_negative_orders)
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Composition reac = parseCompString("O:1 H2:1");
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Composition prod = parseCompString("H:1 OH:1");
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Arrhenius rate(3.87e1, 2.7, 6260.0 / GasConst_cal_mol_K);
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shared_ptr<ElementaryReaction> R(new ElementaryReaction(reac, prod, rate));
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auto R = make_shared<ElementaryReaction>(reac, prod, rate);
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R->reversible = false;
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R->orders["H2"] = - 0.5;
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@ -289,7 +288,7 @@ TEST_F(KineticsFromScratch, nonreactant_order_override)
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Composition reac = parseCompString("O:1 H2:1");
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Composition prod = parseCompString("H:1 OH:1");
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Arrhenius rate(3.87e1, 2.7, 6260.0 / GasConst_cal_mol_K);
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shared_ptr<ElementaryReaction> R(new ElementaryReaction(reac, prod, rate));
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auto R = make_shared<ElementaryReaction>(reac, prod, rate);
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R->reversible = false;
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R->allow_nonreactant_orders = true;
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R->orders["OH"] = 0.5;
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@ -303,7 +302,7 @@ TEST_F(KineticsFromScratch, invalid_nonreactant_order)
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Composition reac = parseCompString("O:1 H2:1");
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Composition prod = parseCompString("H:1 OH:1");
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Arrhenius rate(3.87e1, 2.7, 6260.0 / GasConst_cal_mol_K);
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shared_ptr<ElementaryReaction> R(new ElementaryReaction(reac, prod, rate));
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auto R = make_shared<ElementaryReaction>(reac, prod, rate);
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R->reversible = false;
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R->orders["OH"] = 0.5;
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@ -368,7 +367,7 @@ TEST_F(InterfaceKineticsFromScratch, add_surface_reaction)
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Composition prod = parseCompString("OH(m):1 (m):1");
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Arrhenius rate(5e21, 0, 100.0e6 / GasConstant); // kJ/mol -> J/kmol
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shared_ptr<InterfaceReaction>R(new InterfaceReaction(reac, prod, rate));
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auto R = make_shared<InterfaceReaction>(reac, prod, rate);
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kin.addReaction(R);
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kin.finalize();
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check_rates(3);
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@ -383,7 +382,7 @@ TEST_F(InterfaceKineticsFromScratch, add_sticking_reaction)
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Composition prod = parseCompString("H(m):2");
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Arrhenius rate(0.1, 0, 0.0);
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shared_ptr<InterfaceReaction>R(new InterfaceReaction(reac, prod, rate, true));
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auto R = make_shared<InterfaceReaction>(reac, prod, rate, true);
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kin.addReaction(R);
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kin.finalize();
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check_rates(0);
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@ -32,9 +32,9 @@ TEST_F(SpeciesThermoInterpTypeTest, install_const_cp)
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{
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// Compare against instantiation from CTI file
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IdealGasPhase p2("../data/simplephases.cti", "simple1");
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shared_ptr<Species> sO2(new Species("O2", parseCompString("O:2")));
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shared_ptr<Species> sH2(new Species("H2", parseCompString("H:2")));
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shared_ptr<Species> sH2O(new Species("H2O", parseCompString("H:2 O:1")));
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auto sO2 = make_shared<Species>("O2", parseCompString("O:2"));
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auto sH2 = make_shared<Species>("H2", parseCompString("H:2"));
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auto sH2O = make_shared<Species>("H2O", parseCompString("H:2 O:1"));
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sO2->thermo.reset(new ConstCpPoly(200, 5000, 101325, c_o2));
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sH2->thermo.reset(new ConstCpPoly(200, 5000, 101325, c_h2));
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sH2O->thermo.reset(new ConstCpPoly(200, 5000, 101325, c_h2o));
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@ -54,8 +54,8 @@ TEST_F(SpeciesThermoInterpTypeTest, DISABLED_install_bad_pref)
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{
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// Currently broken because GeneralSpeciesThermo does not enforce reference
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// pressure consistency.
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shared_ptr<Species> sO2(new Species("O2", parseCompString("O:2")));
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shared_ptr<Species> sH2(new Species("H2", parseCompString("H:2")));
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auto sO2 = make_shared<Species>("O2", parseCompString("O:2"));
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auto sH2 = make_shared<Species>("H2", parseCompString("H:2"));
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sO2->thermo.reset(new ConstCpPoly(200, 5000, 101325, c_o2));
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sH2->thermo.reset(new ConstCpPoly(200, 5000, 100000, c_h2));
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p.addSpecies(sO2);
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@ -67,9 +67,9 @@ TEST_F(SpeciesThermoInterpTypeTest, install_nasa)
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{
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// Compare against instantiation from CTI file
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IdealGasPhase p2("../data/simplephases.cti", "nasa1");
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shared_ptr<Species> sO2(new Species("O2", parseCompString("O:2")));
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shared_ptr<Species> sH2(new Species("H2", parseCompString("H:2")));
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shared_ptr<Species> sH2O(new Species("H2O", parseCompString("H:2 O:1")));
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auto sO2 = make_shared<Species>("O2", parseCompString("O:2"));
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auto sH2 = make_shared<Species>("H2", parseCompString("H:2"));
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auto sH2O = make_shared<Species>("H2O", parseCompString("H:2 O:1"));
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sO2->thermo.reset(new NasaPoly2(200, 3500, 101325, o2_nasa_coeffs));
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sH2->thermo.reset(new NasaPoly2(200, 3500, 101325, h2_nasa_coeffs));
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sH2O->thermo.reset(new NasaPoly2(200, 3500, 101325, h2o_nasa_coeffs));
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@ -89,8 +89,8 @@ TEST_F(SpeciesThermoInterpTypeTest, install_shomate)
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{
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// Compare against instantiation from CTI file
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IdealGasPhase p2("../data/simplephases.cti", "shomate1");
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shared_ptr<Species> sCO(new Species("CO", parseCompString("C:1 O:1")));
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shared_ptr<Species> sCO2(new Species("CO2", parseCompString("C:1 O:2")));
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auto sCO = make_shared<Species>("CO", parseCompString("C:1 O:1"));
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auto sCO2 = make_shared<Species>("CO2", parseCompString("C:1 O:2"));
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sCO->thermo.reset(new ShomatePoly2(200, 6000, 101325, co_shomate_coeffs));
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sCO2->thermo.reset(new ShomatePoly2(200, 6000, 101325, co2_shomate_coeffs));
|
||||
p.addSpecies(sCO);
|
||||
|
|
|
|||
Loading…
Add table
Reference in a new issue