adiabaticFlameT.C

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/*---------------------------------------------------------------------------*\
  =========                 |
  \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox
   \\    /   O peration     |
    \\  /    A nd           | Copyright (C) 2011-2015 OpenFOAM Foundation
     \\/     M anipulation  |
-------------------------------------------------------------------------------
License
    This file is part of OpenFOAM.
 
    OpenFOAM is free software: you can redistribute it and/or modify it
    under the terms of the GNU General Public License as published by
    the Free Software Foundation, either version 3 of the License, or
    (at your option) any later version.
 
    OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
    ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
    FITNESS FOR A PARTICULAR PURPOSE.  See the GNU General Public License
    for more details.
 
    You should have received a copy of the GNU General Public License
    along with OpenFOAM.  If not, see <http://www.gnu.org/licenses/>.
 
Application
    adiabaticFlameT
 
Description
    Calculates the adiabatic flame temperature for a given fuel over a
    range of unburnt temperatures and equivalence ratios.
 
\*---------------------------------------------------------------------------*/
 
#include "argList.H"
#include "Time.H"
#include "dictionary.H"
#include "IFstream.H"
#include "OSspecific.H"
 
#include "specie.H"
#include "perfectGas.H"
#include "thermo.H"
#include "janafThermo.H"
#include "absoluteEnthalpy.H"
 
using namespace Foam;
 
typedef species::thermo<janafThermo<perfectGas<specie> >, absoluteEnthalpy>
    thermo;
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
int main(int argc, char *argv[])
{
    argList::validArgs.append("controlFile");
    argList args(argc, argv);
 
    const fileName controlFileName = args[1];
 
    // Construct control dictionary
    IFstream controlFile(controlFileName);
 
    // Check controlFile stream is OK
    if (!controlFile.good())
    {
        FatalErrorInFunction
            << "Cannot read file " << controlFileName
            << exit(FatalError);
    }
 
    dictionary control(controlFile);
 
 
    scalar P(readScalar(control.lookup("P")));
    scalar T0(readScalar(control.lookup("T0")));
    const word fuelName(control.lookup("fuel"));
    scalar n(readScalar(control.lookup("n")));
    scalar m(readScalar(control.lookup("m")));
 
 
    Info<< nl << "Reading thermodynamic data dictionary" << endl;
 
    fileName thermoDataFileName(findEtcFile("thermoData/thermoData"));
 
    // Construct control dictionary
    IFstream thermoDataFile(thermoDataFileName);
 
    // Check thermoData stream is OK
    if (!thermoDataFile.good())
    {
        FatalErrorInFunction
            << "Cannot read file " << thermoDataFileName
            << exit(FatalError);
    }
 
    dictionary thermoData(thermoDataFile);
 
 
    scalar stoicO2 = n + m/4.0;
    scalar stoicN2 = (0.79/0.21)*(n + m/4.0);
    scalar stoicCO2 = n;
    scalar stoicH2O = m/2.0;
 
    thermo fuel
    (
        "fuel",
        thermo(thermoData.subDict(fuelName))
    );
 
    thermo oxidant
    (
        "oxidant",
        stoicO2*thermo(thermoData.subDict("O2"))
      + stoicN2*thermo(thermoData.subDict("N2"))
    );
 
    dimensionedScalar stoichiometricAirFuelMassRatio
    (
        "stoichiometricAirFuelMassRatio",
        dimless,
        (oxidant.W()*oxidant.nMoles())/fuel.W()
    );
 
    Info<< "stoichiometricAirFuelMassRatio "
        << stoichiometricAirFuelMassRatio << ';' << endl;
 
    for (int i=0; i<300; i++)
    {
        scalar equiv = (i + 1)*0.01;
        scalar ft = 1/(1 + stoichiometricAirFuelMassRatio.value()/equiv);
 
        Info<< "phi = " << equiv << nl
            << "ft = " << ft << endl;
 
        scalar o2 = (1.0/equiv)*stoicO2;
        scalar n2 = (0.79/0.21)*o2;
        scalar fres = max(1.0 - 1.0/equiv, 0.0);
        scalar ores = max(1.0/equiv - 1.0, 0.0);
        scalar fburnt = 1.0 - fres;
 
        thermo fuel
        (
            "fuel",
            thermo(thermoData.subDict(fuelName))
        );
        Info<< "fuel " << fuel << ';' << endl;
 
        thermo oxidant
        (
            "oxidant",
            o2*thermo(thermoData.subDict("O2"))
          + n2*thermo(thermoData.subDict("N2"))
        );
        Info<< "oxidant " << (1/oxidant.nMoles())*oxidant << ';' << endl;
 
        thermo reactants
        (
            "reactants",
            fuel + oxidant
        );
        Info<< "reactants " << (1/reactants.nMoles())*reactants << ';' << endl;
 
        thermo burntProducts
        (
            "burntProducts",
          + (n2 - (0.79/0.21)*ores*stoicO2)*thermo(thermoData.subDict("N2"))
          + fburnt*stoicCO2*thermo(thermoData.subDict("CO2"))
          + fburnt*stoicH2O*thermo(thermoData.subDict("H2O"))
        );
        Info<< "burntProducts "
            << (1/burntProducts.nMoles())*burntProducts << ';' << endl;
 
        thermo products
        (
            "products",
            fres*fuel
          + n2*thermo(thermoData.subDict("N2"))
          + fburnt*stoicCO2*thermo(thermoData.subDict("CO2"))
          + fburnt*stoicH2O*thermo(thermoData.subDict("H2O"))
          + ores*stoicO2*thermo(thermoData.subDict("O2"))
        );
 
        Info<< "products " << (1/products.nMoles())*products << ';' << endl;
 
        scalar Tad = products.THa(reactants.Ha(P, T0), P, 1000.0);
        Info<< "Tad = " << Tad << nl << endl;
    }
 
    Info<< nl << "end" << endl;
 
    return 0;
}
 
 
// ************************************************************************* //