mixtureAdiabaticFlameT: Add conversion of volume fraction to mass fractions
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@ -2,7 +2,7 @@
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========= |
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\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
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\\ / O peration | Website: https://openfoam.org
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\\ / A nd | Copyright (C) 2011-2018 OpenFOAM Foundation
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\\ / A nd | Copyright (C) 2011-2019 OpenFOAM Foundation
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\\/ M anipulation |
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-------------------------------------------------------------------------------
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License
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@ -73,7 +73,7 @@ int main(int argc, char *argv[])
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dictionary properties(propertiesFile);
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scalar P(readScalar(properties.lookup("P")));
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scalar p(readScalar(properties.lookup("P")));
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scalar T0(readScalar(properties.lookup("T0")));
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mixture rMix(properties.lookup("reactants"));
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mixture pMix(properties.lookup("products"));
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@ -97,31 +97,27 @@ int main(int argc, char *argv[])
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dictionary thermoData(thermoDataFile);
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thermo reactants
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(
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rMix[0].volFrac()*thermo(thermoData.subDict(rMix[0].name()))
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);
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const thermo reactant0(thermoData.subDict(rMix[0].name()));
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for (label i = 1; i < rMix.size(); i++)
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thermo reactants(rMix[0].volFrac()*reactant0.rho(p, T0)*reactant0);
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for (label i=1; i<rMix.size(); i++)
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{
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reactants = reactants
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+ rMix[i].volFrac()*thermo(thermoData.subDict(rMix[i].name()));
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const thermo reactanti(thermoData.subDict(rMix[i].name()));
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reactants += rMix[i].volFrac()*reactanti.rho(p, T0)*reactanti;
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}
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const thermo product0(thermoData.subDict(pMix[0].name()));
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thermo products(pMix[0].volFrac()*product0.rho(p, T0)*product0);
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thermo products
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(
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2*pMix[0].volFrac()*thermo(thermoData.subDict(pMix[0].name()))
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);
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for (label i = 1; i < pMix.size(); i++)
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for (label i=1; i<pMix.size(); i++)
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{
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products = products
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+ 2*pMix[i].volFrac()*thermo(thermoData.subDict(pMix[i].name()));
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const thermo producti(thermoData.subDict(pMix[i].name()));
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products += pMix[i].volFrac()*producti.rho(p, T0)*producti;
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}
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Info<< "Adiabatic flame temperature of mixture " << rMix.name() << " = "
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<< products.THa(reactants.Ha(P, T0), P, 1000.0) << " K" << endl;
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<< products.THa(reactants.Ha(p, T0), p, 1000.0) << " K" << endl;
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return 0;
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}
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