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8726
applications/utilities/thermophysical/adiabaticFlameT/Hydrogen.log
Normal file
8726
applications/utilities/thermophysical/adiabaticFlameT/Hydrogen.log
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File diff suppressed because it is too large
Load Diff
@ -0,0 +1,3 @@
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adiabaticFlameT.C
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EXE = $(FOAM_APPBIN)/adiabaticFlameT
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@ -0,0 +1,2 @@
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EXE_INC = -I$(LIB_SRC)/thermophysicalModels/specie/lnInclude
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EXE_LIBS = -lspecie
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@ -0,0 +1,194 @@
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/*---------------------------------------------------------------------------*\
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========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2011-2013 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
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|
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Description
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Calculates the adiabatic flame temperature for a given fuel over a
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range of unburnt temperatures and equivalence ratios.
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\*---------------------------------------------------------------------------*/
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#include "argList.H"
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#include "Time.H"
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#include "dictionary.H"
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#include "IFstream.H"
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#include "OSspecific.H"
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#include "specie.H"
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#include "perfectGas.H"
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#include "thermo.H"
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#include "janafThermo.H"
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#include "absoluteEnthalpy.H"
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using namespace Foam;
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typedef species::thermo<janafThermo<perfectGas<specie> >, absoluteEnthalpy>
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thermo;
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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int main(int argc, char *argv[])
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{
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argList::validArgs.append("controlFile");
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argList args(argc, argv);
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const fileName controlFileName = args[1];
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// Construct control dictionary
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IFstream controlFile(controlFileName);
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// Check controlFile stream is OK
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if (!controlFile.good())
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{
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FatalErrorIn(args.executable())
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<< "Cannot read file " << controlFileName
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<< exit(FatalError);
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}
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dictionary control(controlFile);
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scalar P(readScalar(control.lookup("P")));
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scalar T0(readScalar(control.lookup("T0")));
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const word fuelName(control.lookup("fuel"));
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scalar n(readScalar(control.lookup("n")));
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scalar m(readScalar(control.lookup("m")));
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||||
|
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|
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Info<< nl << "Reading thermodynamic data dictionary" << endl;
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||||
|
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fileName thermoDataFileName(findEtcFile("thermoData/thermoData"));
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|
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// Construct control dictionary
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IFstream thermoDataFile(thermoDataFileName);
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|
||||
// Check thermoData stream is OK
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||||
if (!thermoDataFile.good())
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{
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FatalErrorIn(args.executable())
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<< "Cannot read file " << thermoDataFileName
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<< exit(FatalError);
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}
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dictionary thermoData(thermoDataFile);
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scalar stoicO2 = n + m/4.0;
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scalar stoicN2 = (0.79/0.21)*(n + m/4.0);
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scalar stoicCO2 = n;
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scalar stoicH2O = m/2.0;
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||||
thermo fuel
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(
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"fuel",
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thermo(thermoData.subDict(fuelName))
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);
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thermo oxidant
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(
|
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"oxidant",
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stoicO2*thermo(thermoData.subDict("O2"))
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+ stoicN2*thermo(thermoData.subDict("N2"))
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);
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dimensionedScalar stoichiometricAirFuelMassRatio
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(
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"stoichiometricAirFuelMassRatio",
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dimless,
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(oxidant.W()*oxidant.nMoles())/fuel.W()
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);
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Info<< "stoichiometricAirFuelMassRatio "
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<< stoichiometricAirFuelMassRatio << ';' << endl;
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|
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for (int i=0; i<300; i++)
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{
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scalar equiv = (i + 1)*0.01;
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scalar ft = 1/(1 + stoichiometricAirFuelMassRatio.value()/equiv);
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Info<< "phi = " << equiv << nl
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<< "ft = " << ft << endl;
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scalar o2 = (1.0/equiv)*stoicO2;
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scalar n2 = (0.79/0.21)*o2;
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scalar fres = max(1.0 - 1.0/equiv, 0.0);
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scalar ores = max(1.0/equiv - 1.0, 0.0);
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scalar fburnt = 1.0 - fres;
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thermo fuel
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(
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"fuel",
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thermo(thermoData.subDict(fuelName))
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);
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Info<< "fuel " << fuel << ';' << endl;
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|
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thermo oxidant
|
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(
|
||||
"oxidant",
|
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o2*thermo(thermoData.subDict("O2"))
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+ n2*thermo(thermoData.subDict("N2"))
|
||||
);
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Info<< "oxidant " << (1/oxidant.nMoles())*oxidant << ';' << endl;
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|
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thermo reactants
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(
|
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"reactants",
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fuel + oxidant
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);
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Info<< "reactants " << (1/reactants.nMoles())*reactants << ';' << endl;
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thermo burntProducts
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(
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"burntProducts",
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+ (n2 - (0.79/0.21)*ores*stoicO2)*thermo(thermoData.subDict("N2"))
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+ fburnt*stoicCO2*thermo(thermoData.subDict("CO2"))
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+ fburnt*stoicH2O*thermo(thermoData.subDict("H2O"))
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);
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Info<< "burntProducts "
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<< (1/burntProducts.nMoles())*burntProducts << ';' << endl;
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thermo products
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(
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"products",
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fres*fuel
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+ n2*thermo(thermoData.subDict("N2"))
|
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+ fburnt*stoicCO2*thermo(thermoData.subDict("CO2"))
|
||||
+ fburnt*stoicH2O*thermo(thermoData.subDict("H2O"))
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||||
+ ores*stoicO2*thermo(thermoData.subDict("O2"))
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||||
);
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Info<< "products " << (1/products.nMoles())*products << ';' << endl;
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scalar Tad = products.THa(reactants.Ha(P, T0), P, 1000.0);
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Info<< "Tad = " << Tad << nl << endl;
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||||
}
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Info<< nl << "end" << endl;
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||||
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||||
return 0;
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||||
}
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||||
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||||
|
||||
// ************************************************************************* //
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||||
@ -0,0 +1,67 @@
|
||||
/*--------------------------------*- C++ -*----------------------------------*\
|
||||
| ========= | |
|
||||
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
|
||||
| \\ / O peration | Version: dev |
|
||||
| \\ / A nd | Web: www.OpenFOAM.org |
|
||||
| \\/ M anipulation | |
|
||||
\*---------------------------------------------------------------------------*/
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||||
FoamFile
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{
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version 2.0;
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||||
format ascii;
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note "settings for calculating the adiabatic flame temperature";
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||||
class dictionary;
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||||
object controlDict;
|
||||
}
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
P 1e5;
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T0 300.0;
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|
||||
H2
|
||||
{
|
||||
fuel H2;
|
||||
n 0;
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||||
m 2;
|
||||
}
|
||||
|
||||
CH4
|
||||
{
|
||||
fuel CH4___ANHARMONIC;
|
||||
n 1;
|
||||
m 4;
|
||||
}
|
||||
|
||||
ETHYLENE
|
||||
{
|
||||
fuel C2H4;
|
||||
n 2;
|
||||
m 4;
|
||||
}
|
||||
|
||||
PROPANE
|
||||
{
|
||||
fuel C3H8;
|
||||
n 3;
|
||||
m 8;
|
||||
}
|
||||
|
||||
OCTANE
|
||||
{
|
||||
fuel C8H18(L)_isooctane;
|
||||
n 8;
|
||||
m 18;
|
||||
}
|
||||
|
||||
N-HEPTANE
|
||||
{
|
||||
fuel C7H16_n-heptane;
|
||||
n 7;
|
||||
m 16;
|
||||
}
|
||||
|
||||
$H2;
|
||||
// $CH4;
|
||||
// $PROPANE;
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,4 @@
|
||||
|
||||
chemkinToFoam.C
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||||
EXE = $(FOAM_APPBIN)/chemkinToFoam
|
||||
@ -0,0 +1,8 @@
|
||||
EXE_INC = \
|
||||
-I$(LIB_SRC)/thermophysicalModels/specie/lnInclude \
|
||||
-I$(LIB_SRC)/thermophysicalModels/reactionThermo/lnInclude
|
||||
|
||||
EXE_LIBS = \
|
||||
-lreactionThermophysicalModels \
|
||||
-lfluidThermophysicalModels \
|
||||
-lspecie
|
||||
@ -0,0 +1,78 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2011-2013 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
|
||||
chemkinToFoam
|
||||
|
||||
Description
|
||||
Converts CHEMKINIII thermodynamics and reaction data files into
|
||||
OpenFOAM format.
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#include "argList.H"
|
||||
#include "chemkinReader.H"
|
||||
#include "OFstream.H"
|
||||
|
||||
using namespace Foam;
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
int main(int argc, char *argv[])
|
||||
{
|
||||
argList::validArgs.append("CHEMKINFile");
|
||||
argList::validArgs.append("CHEMKINThermodynamicsFile");
|
||||
argList::validArgs.append("FOAMChemistryFile");
|
||||
argList::validArgs.append("FOAMThermodynamicsFile");
|
||||
|
||||
argList::addBoolOption
|
||||
(
|
||||
"newFormat",
|
||||
"read Chemkin thermo file in new format"
|
||||
);
|
||||
|
||||
argList args(argc, argv);
|
||||
|
||||
bool newFormat = args.optionFound("newFormat");
|
||||
|
||||
speciesTable species;
|
||||
|
||||
chemkinReader cr(args[1], species, args[2], newFormat);
|
||||
|
||||
OFstream reactionsFile(args[3]);
|
||||
reactionsFile
|
||||
<< "species" << cr.species() << token::END_STATEMENT << nl << nl;
|
||||
|
||||
cr.reactions().write(reactionsFile);
|
||||
|
||||
|
||||
OFstream thermoFile(args[4]);
|
||||
cr.speciesThermo().write(thermoFile);
|
||||
|
||||
Info<< "End\n" << endl;
|
||||
|
||||
return 0;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,3 @@
|
||||
equilibriumCO.C
|
||||
|
||||
EXE = $(FOAM_APPBIN)/equilibriumCO
|
||||
@ -0,0 +1,2 @@
|
||||
EXE_INC = -I$(LIB_SRC)/thermophysicalModels/specie/lnInclude
|
||||
EXE_LIBS = -lspecie
|
||||
@ -0,0 +1,136 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2011-2013 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
|
||||
equilibriumCO
|
||||
|
||||
Description
|
||||
Calculates the equilibrium level of carbon monoxide.
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#include "argList.H"
|
||||
#include "Time.H"
|
||||
#include "dictionary.H"
|
||||
#include "IFstream.H"
|
||||
#include "OSspecific.H"
|
||||
#include "IOmanip.H"
|
||||
|
||||
#include "specie.H"
|
||||
#include "perfectGas.H"
|
||||
#include "thermo.H"
|
||||
#include "janafThermo.H"
|
||||
#include "absoluteEnthalpy.H"
|
||||
|
||||
#include "SLPtrList.H"
|
||||
|
||||
using namespace Foam;
|
||||
|
||||
typedef species::thermo<janafThermo<perfectGas<specie> >, absoluteEnthalpy>
|
||||
thermo;
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
int main(int argc, char *argv[])
|
||||
{
|
||||
#include "setRootCase.H"
|
||||
#include "createTime.H"
|
||||
|
||||
Info<< nl << "Reading thermodynamic data IOdictionary" << endl;
|
||||
|
||||
IOdictionary thermoData
|
||||
(
|
||||
IOobject
|
||||
(
|
||||
"thermoData",
|
||||
runTime.constant(),
|
||||
runTime,
|
||||
IOobject::MUST_READ_IF_MODIFIED,
|
||||
IOobject::NO_WRITE,
|
||||
false
|
||||
)
|
||||
);
|
||||
|
||||
|
||||
|
||||
scalar P = 1e5;
|
||||
scalar T = 3000.0;
|
||||
|
||||
SLPtrList<thermo> EQreactions;
|
||||
|
||||
EQreactions.append
|
||||
(
|
||||
new thermo
|
||||
(
|
||||
thermo(thermoData.subDict("CO2"))
|
||||
==
|
||||
thermo(thermoData.subDict("CO"))
|
||||
+ 0.5*thermo(thermoData.subDict("O2"))
|
||||
)
|
||||
);
|
||||
|
||||
EQreactions.append
|
||||
(
|
||||
new thermo
|
||||
(
|
||||
thermo(thermoData.subDict("O2"))
|
||||
==
|
||||
2.0*thermo(thermoData.subDict("O"))
|
||||
)
|
||||
);
|
||||
|
||||
EQreactions.append
|
||||
(
|
||||
new thermo
|
||||
(
|
||||
thermo(thermoData.subDict("H2O"))
|
||||
==
|
||||
thermo(thermoData.subDict("H2"))
|
||||
+ 0.5*thermo(thermoData.subDict("O2"))
|
||||
)
|
||||
);
|
||||
|
||||
EQreactions.append
|
||||
(
|
||||
new thermo
|
||||
(
|
||||
thermo(thermoData.subDict("H2O"))
|
||||
==
|
||||
thermo(thermoData.subDict("H"))
|
||||
+ thermo(thermoData.subDict("OH"))
|
||||
)
|
||||
);
|
||||
|
||||
|
||||
forAllConstIter(SLPtrList<thermo>, EQreactions, iter)
|
||||
{
|
||||
Info<< "Kc(EQreactions) = " << iter().Kc(P, T) << endl;
|
||||
}
|
||||
|
||||
Info<< nl << "end" << endl;
|
||||
|
||||
return 0;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,481 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
| ========= | |
|
||||
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
|
||||
| \\ / O peration | Version: dev |
|
||||
| \\ / A nd | Web: www.OpenFOAM.org |
|
||||
| \\/ M anipulation | |
|
||||
\*---------------------------------------------------------------------------*/
|
||||
Build : dev-27a117d1f441
|
||||
Exec : equilibriumFlameT controlDict
|
||||
Date : Jan 16 2013
|
||||
Time : 15:40:39
|
||||
Host : "dm"
|
||||
PID : 4638
|
||||
Case : /home/dm2/henry/OpenFOAM/OpenFOAM-dev/applications/utilities/thermophysical/equilibriumFlameT
|
||||
nProcs : 1
|
||||
sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE).
|
||||
SetNaN : Initialising allocated memory to NaN (FOAM_SETNAN).
|
||||
fileModificationChecking : Monitoring run-time modified files using timeStampMaster
|
||||
allowSystemOperations : Allowing user-supplied system call operations
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
Reading thermodynamic data dictionary
|
||||
|
||||
Reading thermodynamic data for relevant species
|
||||
|
||||
stoichiometricAirFuelMassRatio stoichiometricAirFuelMassRatio [0 0 0 0 0 0 0] 34.0741;
|
||||
Equilibrium flame temperature data (1 bar)
|
||||
|
||||
Phi ft T0 Tad Teq Terror O2res (mole frac)
|
||||
|
||||
0.6 0.017304 300 1849.36 1848.92 0.441261 0.0746347
|
||||
0.6 0.017304 400 1932.16 1931.28 0.879009 0.0746693
|
||||
0.6 0.017304 500 2015.31 2013.66 1.6553 0.0747311
|
||||
0.6 0.017304 600 2099.1 2096.14 2.96655 0.074836
|
||||
0.6 0.017304 700 2183.84 2178.76 5.08632 0.0750065
|
||||
0.6 0.017304 800 2269.77 2261.4 8.37223 0.0752722
|
||||
0.6 0.017304 900 2356.97 2343.72 13.2521 0.0756689
|
||||
0.6 0.017304 1000 2445.26 2425.09 20.1747 0.0762341
|
||||
0.6 0.017304 1100 2534.41 2504.86 29.5499 0.077003
|
||||
0.6 0.017304 1200 2624.41 2582.69 41.7235 0.0780054
|
||||
0.6 0.017304 1300 2715.19 2658.28 56.9132 0.0792609
|
||||
0.6 0.017304 1400 2806.69 2731.49 75.1966 0.0807775
|
||||
0.6 0.017304 1500 2898.84 2802.32 96.5198 0.0825522
|
||||
0.6 0.017304 1600 2991.6 2870.87 120.724 0.0845729
|
||||
0.6 0.017304 1700 3084.9 2937.32 147.577 0.0868217
|
||||
0.6 0.017304 1800 3178.71 3001.9 176.81 0.0892764
|
||||
0.6 0.017304 1900 3272.98 3064.84 208.131 0.0919138
|
||||
0.6 0.017304 2000 3367.66 3126.4 241.253 0.09471
|
||||
0.6 0.017304 2100 3462.72 3186.82 275.903 0.0976445
|
||||
0.6 0.017304 2200 3558.12 3246.2 311.925 0.100726
|
||||
0.6 0.017304 2300 3653.84 3303.74 350.096 0.104207
|
||||
0.6 0.017304 2400 3749.83 3350.89 398.934 0.110203
|
||||
0.6 0.017304 2500 3846.07 3351.34 494.73 0.126061
|
||||
0.6 0.017304 2600 3942.53 3291.95 650.58 0.151488
|
||||
0.6 0.017304 2700 4039.19 3236.21 802.988 0.17406
|
||||
0.6 0.017304 2800 4136.03 3245.34 890.687 0.186501
|
||||
0.6 0.017304 2900 4233.03 3344.34 888.683 0.186501
|
||||
0.6 0.017304 3000 4330.16 3443.39 886.77 0.186501
|
||||
0.65 0.018719 300 1944.33 1943.23 1.10762 0.0647597
|
||||
0.65 0.018719 400 2026.59 2024.53 2.05315 0.0648355
|
||||
0.65 0.018719 500 2109.23 2105.61 3.62082 0.0649618
|
||||
0.65 0.018719 600 2192.53 2186.42 6.10504 0.065163
|
||||
0.65 0.018719 700 2276.78 2266.9 9.88012 0.0654705
|
||||
0.65 0.018719 800 2362.23 2346.84 15.3867 0.0659212
|
||||
0.65 0.018719 900 2448.96 2425.87 23.0886 0.0665545
|
||||
0.65 0.018719 1000 2536.81 2503.41 33.3941 0.0674057
|
||||
0.65 0.018719 1100 2625.53 2578.93 46.5953 0.0685004
|
||||
0.65 0.018719 1200 2715.11 2652.24 62.8776 0.0698558
|
||||
0.65 0.018719 1300 2805.51 2723.23 82.2781 0.0714767
|
||||
0.65 0.018719 1400 2896.63 2791.92 104.71 0.0733571
|
||||
0.65 0.018719 1500 2988.44 2858.44 129.993 0.0754833
|
||||
0.65 0.018719 1600 3080.86 2922.97 157.886 0.0778362
|
||||
0.65 0.018719 1700 3173.85 2985.73 188.117 0.0803935
|
||||
0.65 0.018719 1800 3267.36 3046.95 220.404 0.0831323
|
||||
0.65 0.018719 1900 3361.34 3106.87 254.469 0.0860297
|
||||
0.65 0.018719 2000 3455.75 3165.68 290.067 0.0890703
|
||||
0.65 0.018719 2100 3550.55 3223.35 327.196 0.0923026
|
||||
0.65 0.018719 2200 3645.71 3278.01 367.698 0.0962479
|
||||
0.65 0.018719 2300 3741.18 3314.72 426.463 0.104431
|
||||
0.65 0.018719 2400 3836.94 3292.03 544.908 0.124389
|
||||
0.65 0.018719 2500 3932.96 3229.29 703.673 0.149514
|
||||
0.65 0.018719 2600 4029.21 3177.81 851.399 0.170937
|
||||
0.65 0.018719 2700 4125.67 3175.22 950.445 0.184778
|
||||
0.65 0.018719 2800 4222.31 3274.1 948.203 0.184778
|
||||
0.65 0.018719 2900 4319.11 3373.04 946.07 0.184778
|
||||
0.65 0.018719 3000 4416.05 3472.02 944.031 0.184778
|
||||
0.7 0.0201299 300 2035.76 2033.25 2.51585 0.0551272
|
||||
0.7 0.0201299 400 2117.53 2113.15 4.37823 0.0552783
|
||||
0.7 0.0201299 500 2199.71 2192.43 7.27913 0.0555149
|
||||
0.7 0.0201299 600 2282.56 2270.96 11.6037 0.0558696
|
||||
0.7 0.0201299 700 2366.37 2348.58 17.7905 0.0563794
|
||||
0.7 0.0201299 800 2451.38 2425.09 26.2928 0.0570833
|
||||
0.7 0.0201299 900 2537.69 2500.17 37.5154 0.0580165
|
||||
0.7 0.0201299 1000 2625.11 2573.39 51.7294 0.0592034
|
||||
0.7 0.0201299 1100 2713.43 2644.39 69.0438 0.0606547
|
||||
0.7 0.0201299 1200 2802.64 2713.17 89.4684 0.062373
|
||||
0.7 0.0201299 1300 2892.67 2779.78 112.888 0.06435
|
||||
0.7 0.0201299 1400 2983.45 2844.35 139.106 0.0665705
|
||||
0.7 0.0201299 1500 3074.93 2907.05 167.878 0.0690147
|
||||
0.7 0.0201299 1600 3167.04 2968.1 198.938 0.0716609
|
||||
0.7 0.0201299 1700 3259.73 3027.72 232.012 0.0744866
|
||||
0.7 0.0201299 1800 3352.96 3086.12 266.841 0.0774712
|
||||
0.7 0.0201299 1900 3446.67 3143.43 303.236 0.0806124
|
||||
0.7 0.0201299 2000 3540.82 3199.29 341.528 0.0840445
|
||||
0.7 0.0201299 2100 3635.38 3249.5 385.874 0.0888593
|
||||
0.7 0.0201299 2200 3730.29 3268.93 461.361 0.100608
|
||||
0.7 0.0201299 2300 3825.54 3223.58 601.959 0.124079
|
||||
0.7 0.0201299 2400 3921.08 3163.25 757.829 0.147885
|
||||
0.7 0.0201299 2500 4016.89 3115.4 901.49 0.168314
|
||||
0.7 0.0201299 2600 4112.93 3104.31 1008.62 0.183086
|
||||
0.7 0.0201299 2700 4209.19 3203.06 1006.13 0.183086
|
||||
0.7 0.0201299 2800 4305.63 3301.88 1003.76 0.183086
|
||||
0.7 0.0201299 2900 4402.25 3400.75 1001.5 0.183086
|
||||
0.7 0.0201299 3000 4499.01 3499.67 999.336 0.183086
|
||||
0.75 0.0215368 300 2123.87 2118.6 5.26414 0.0457828
|
||||
0.75 0.0215368 400 2205.19 2196.54 8.64652 0.0460605
|
||||
0.75 0.0215368 500 2286.96 2273.35 13.6024 0.0464696
|
||||
0.75 0.0215368 600 2369.39 2348.84 20.555 0.0470463
|
||||
0.75 0.0215368 700 2452.79 2422.87 29.9229 0.0478271
|
||||
0.75 0.0215368 800 2537.4 2495.33 42.0731 0.0488441
|
||||
0.75 0.0215368 900 2623.32 2566.06 57.2623 0.0501209
|
||||
0.75 0.0215368 1000 2710.36 2634.79 75.5739 0.0516661
|
||||
0.75 0.0215368 1100 2798.31 2701.37 96.9358 0.0534755
|
||||
0.75 0.0215368 1200 2887.16 2765.93 121.226 0.0555401
|
||||
0.75 0.0215368 1300 2976.85 2828.61 148.241 0.0578437
|
||||
0.75 0.0215368 1400 3067.31 2889.57 177.736 0.0603667
|
||||
0.75 0.0215368 1500 3158.48 2949.02 209.456 0.063088
|
||||
0.75 0.0215368 1600 3250.3 3007.15 243.145 0.0659865
|
||||
0.75 0.0215368 1700 3342.71 3064.14 278.571 0.069047
|
||||
0.75 0.0215368 1800 3435.67 3119.98 315.691 0.0723035
|
||||
0.75 0.0215368 1900 3529.12 3173.54 355.588 0.0760823
|
||||
0.75 0.0215368 2000 3623.03 3215.17 407.865 0.0827504
|
||||
0.75 0.0215368 2100 3717.35 3207.15 510.202 0.0997809
|
||||
0.75 0.0215368 2200 3812.04 3147 665.038 0.124757
|
||||
0.75 0.0215368 2300 3907.07 3092.14 814.923 0.146832
|
||||
0.75 0.0215368 2400 4002.4 3047.13 955.268 0.166424
|
||||
0.75 0.0215368 2500 4098 3032.67 1065.33 0.181425
|
||||
0.75 0.0215368 2600 4193.84 3131.28 1062.56 0.181425
|
||||
0.75 0.0215368 2700 4289.91 3229.97 1059.94 0.181425
|
||||
0.75 0.0215368 2800 4386.16 3328.72 1057.44 0.181425
|
||||
0.75 0.0215368 2900 4482.59 3427.53 1055.06 0.181425
|
||||
0.75 0.0215368 3000 4579.17 3526.39 1052.78 0.181425
|
||||
0.8 0.0229397 300 2208.84 2198.55 10.2856 0.0368016
|
||||
0.8 0.0229397 400 2289.76 2273.78 15.9817 0.0372748
|
||||
0.8 0.0229397 500 2371.15 2347.32 23.8229 0.0379294
|
||||
0.8 0.0229397 600 2453.21 2419.04 34.1694 0.0387973
|
||||
0.8 0.0229397 700 2536.24 2488.92 47.3167 0.039905
|
||||
0.8 0.0229397 800 2620.48 2557.01 63.4684 0.0412715
|
||||
0.8 0.0229397 900 2706.03 2623.32 82.7038 0.0429054
|
||||
0.8 0.0229397 1000 2792.71 2687.77 104.941 0.0448014
|
||||
0.8 0.0229397 1100 2880.31 2750.32 129.984 0.0469441
|
||||
0.8 0.0229397 1200 2968.83 2811.18 157.651 0.0493193
|
||||
0.8 0.0229397 1300 3058.2 2870.49 187.709 0.0519078
|
||||
0.8 0.0229397 1400 3148.36 2928.44 219.918 0.05469
|
||||
0.8 0.0229397 1500 3239.24 2985.19 254.048 0.0576479
|
||||
0.8 0.0229397 1600 3330.78 3040.84 289.946 0.0607847
|
||||
0.8 0.0229397 1700 3422.93 3094.94 327.986 0.0642431
|
||||
0.8 0.0229397 1800 3515.63 3144.62 371.018 0.0687801
|
||||
0.8 0.0229397 1900 3608.84 3166.57 442.271 0.0796671
|
||||
0.8 0.0229397 2000 3702.52 3123.82 578.694 0.102453
|
||||
0.8 0.0229397 2100 3796.61 3062.37 734.239 0.126254
|
||||
0.8 0.0229397 2200 3891.08 3012.82 878.258 0.146769
|
||||
0.8 0.0229397 2300 3985.9 2969.95 1015.95 0.165648
|
||||
0.8 0.0229397 2400 4081.02 2960.34 1120.68 0.179795
|
||||
0.8 0.0229397 2500 4176.43 3058.81 1117.62 0.179795
|
||||
0.8 0.0229397 2600 4272.08 3157.36 1114.72 0.179795
|
||||
0.8 0.0229397 2700 4367.96 3255.99 1111.97 0.179795
|
||||
0.8 0.0229397 2800 4464.03 3354.68 1109.35 0.179795
|
||||
0.8 0.0229397 2900 4560.28 3453.43 1106.85 0.179795
|
||||
0.8 0.0229397 3000 4656.69 3552.23 1104.46 0.179795
|
||||
0.85 0.0243385 300 2290.86 2271.89 18.9685 0.0282998
|
||||
0.85 0.0243385 400 2371.41 2343.55 27.8685 0.0290475
|
||||
0.85 0.0243385 500 2452.45 2413.1 39.3563 0.0300172
|
||||
0.85 0.0243385 600 2534.18 2480.55 53.6235 0.0312269
|
||||
0.85 0.0243385 700 2616.86 2546.07 70.7851 0.0326882
|
||||
0.85 0.0243385 800 2700.75 2609.87 90.8809 0.0344063
|
||||
0.85 0.0243385 900 2785.96 2672.1 113.86 0.0363784
|
||||
0.85 0.0243385 1000 2872.32 2732.77 139.549 0.0385908
|
||||
0.85 0.0243385 1100 2959.59 2791.88 167.705 0.041024
|
||||
0.85 0.0243385 1200 3047.8 2849.65 198.145 0.043663
|
||||
0.85 0.0243385 1300 3136.87 2906.22 230.656 0.0464908
|
||||
0.85 0.0243385 1400 3226.75 2961.68 265.07 0.0495028
|
||||
0.85 0.0243385 1500 3317.35 3015.81 301.538 0.0527804
|
||||
0.85 0.0243385 1600 3408.63 3066.84 341.787 0.0568065
|
||||
0.85 0.0243385 1700 3500.53 3104.48 396.051 0.0640162
|
||||
0.85 0.0243385 1800 3592.99 3084.34 508.645 0.0828878
|
||||
0.85 0.0243385 1900 3685.97 3019.83 666.138 0.107717
|
||||
0.85 0.0243385 2000 3779.41 2965.44 813.977 0.129098
|
||||
0.85 0.0243385 2100 3873.29 2919.57 953.72 0.148417
|
||||
0.85 0.0243385 2200 3967.55 2878.14 1089.41 0.166695
|
||||
0.85 0.0243385 2300 4062.16 2887.39 1174.78 0.178193
|
||||
0.85 0.0243385 2400 4157.09 2985.7 1171.39 0.178193
|
||||
0.85 0.0243385 2500 4252.31 3084.1 1168.2 0.178193
|
||||
0.85 0.0243385 2600 4347.77 3182.59 1165.18 0.178193
|
||||
0.85 0.0243385 2700 4443.47 3281.16 1162.31 0.178193
|
||||
0.85 0.0243385 2800 4539.37 3379.79 1159.58 0.178193
|
||||
0.85 0.0243385 2900 4635.44 3478.48 1156.96 0.178193
|
||||
0.85 0.0243385 3000 4731.69 3577.23 1154.46 0.178193
|
||||
0.9 0.0257334 300 2370.09 2336.78 33.3173 0.0204491
|
||||
0.9 0.0257334 400 2450.31 2404.16 46.1529 0.0215394
|
||||
0.9 0.0257334 500 2531.04 2469.35 61.6865 0.0228649
|
||||
0.9 0.0257334 600 2612.44 2532.52 79.921 0.0244277
|
||||
0.9 0.0257334 700 2694.8 2593.97 100.836 0.0262275
|
||||
0.9 0.0257334 800 2778.38 2653.99 124.39 0.0282621
|
||||
0.9 0.0257334 900 2863.28 2712.78 150.491 0.030525
|
||||
0.9 0.0257334 1000 2949.32 2770.36 178.952 0.0330009
|
||||
0.9 0.0257334 1100 3036.28 2826.74 209.547 0.035672
|
||||
0.9 0.0257334 1200 3124.2 2882.03 242.174 0.0385401
|
||||
0.9 0.0257334 1300 3212.99 2935.98 277.011 0.0416893
|
||||
0.9 0.0257334 1400 3302.6 2986.9 315.702 0.045578
|
||||
0.9 0.0257334 1500 3392.94 3028.82 364.12 0.0515944
|
||||
0.9 0.0257334 1600 3483.97 3019.41 464.567 0.068226
|
||||
0.9 0.0257334 1700 3575.63 2951.2 624.433 0.0935821
|
||||
0.9 0.0257334 1800 3667.86 2892.42 775.443 0.115391
|
||||
0.9 0.0257334 1900 3760.61 2843.56 917.05 0.134916
|
||||
0.9 0.0257334 2000 3853.85 2799.75 1054.09 0.153338
|
||||
0.9 0.0257334 2100 3947.51 2759.06 1188.45 0.171094
|
||||
0.9 0.0257334 2200 4041.57 2813.86 1227.71 0.176619
|
||||
0.9 0.0257334 2300 4135.99 2912 1223.99 0.176619
|
||||
0.9 0.0257334 2400 4230.73 3010.24 1220.48 0.176619
|
||||
0.9 0.0257334 2500 4325.76 3108.59 1217.17 0.176619
|
||||
0.9 0.0257334 2600 4421.04 3207.02 1214.03 0.176619
|
||||
0.9 0.0257334 2700 4516.56 3305.52 1211.04 0.176619
|
||||
0.9 0.0257334 2800 4612.29 3404.1 1208.19 0.176619
|
||||
0.9 0.0257334 2900 4708.2 3502.73 1205.47 0.176619
|
||||
0.9 0.0257334 3000 4804.28 3601.43 1202.85 0.176619
|
||||
0.95 0.0271242 300 2446.69 2390.47 56.2165 0.0135013
|
||||
0.95 0.0271242 400 2526.6 2453.56 73.0446 0.014947
|
||||
0.95 0.0271242 500 2607.03 2514.76 92.2714 0.016606
|
||||
0.95 0.0271242 600 2688.14 2574.31 113.833 0.0184742
|
||||
0.95 0.0271242 700 2770.21 2632.51 137.7 0.0205501
|
||||
0.95 0.0271242 800 2853.49 2689.64 163.85 0.0228334
|
||||
0.95 0.0271242 900 2938.09 2745.85 192.246 0.0253261
|
||||
0.95 0.0271242 1000 3023.84 2800.95 222.894 0.0280617
|
||||
0.95 0.0271242 1100 3110.52 2854.04 256.478 0.0312581
|
||||
0.95 0.0271242 1200 3198.16 2901.95 296.209 0.0357143
|
||||
0.95 0.0271242 1300 3286.69 2937.18 349.506 0.0429733
|
||||
0.95 0.0271242 1400 3376.04 2901.93 474.111 0.0635068
|
||||
0.95 0.0271242 1500 3466.14 2818.66 647.478 0.0895965
|
||||
0.95 0.0271242 1600 3556.93 2756.28 800.654 0.110895
|
||||
0.95 0.0271242 1700 3648.36 2703.85 944.503 0.130251
|
||||
0.95 0.0271242 1800 3740.37 2656.95 1083.42 0.148612
|
||||
0.95 0.0271242 1900 3832.91 2615.22 1217.69 0.165993
|
||||
0.95 0.0271242 2000 3925.93 2641.98 1283.95 0.175073
|
||||
0.95 0.0271242 2100 4019.4 2739.8 1279.6 0.175073
|
||||
0.95 0.0271242 2200 4113.26 2837.76 1275.51 0.175073
|
||||
0.95 0.0271242 2300 4207.49 2935.83 1271.66 0.175073
|
||||
0.95 0.0271242 2400 4302.04 3034.02 1268.03 0.175073
|
||||
0.95 0.0271242 2500 4396.89 3132.3 1264.59 0.175073
|
||||
0.95 0.0271242 2600 4492 3230.67 1261.33 0.175073
|
||||
0.95 0.0271242 2700 4587.35 3329.12 1258.23 0.175073
|
||||
0.95 0.0271242 2800 4682.91 3427.64 1255.27 0.175073
|
||||
0.95 0.0271242 2900 4778.66 3526.22 1252.44 0.175073
|
||||
0.95 0.0271242 3000 4874.58 3624.86 1249.72 0.175073
|
||||
1 0.0285111 300 2520.79 2428.95 91.8415 0.00783223
|
||||
1 0.0285111 400 2600.42 2489.16 111.262 0.00954474
|
||||
1 0.0285111 500 2680.58 2547.46 133.116 0.0115427
|
||||
1 0.0285111 600 2761.42 2603.06 158.358 0.0140645
|
||||
1 0.0285111 700 2843.21 2656.82 186.389 0.0169302
|
||||
1 0.0285111 800 2926.22 2705.82 220.398 0.0208555
|
||||
1 0.0285111 900 3010.54 2717.47 293.073 0.031931
|
||||
1 0.0285111 1000 3096.01 2308.21 787.803 0.102583
|
||||
1 0.0285111 1100 3182.42 2231.26 951.156 0.118119
|
||||
1 0.0285111 1200 3269.8 2192.08 1077.72 0.134773
|
||||
1 0.0285111 1300 3358.08 2047.07 1311.01 0.173419
|
||||
1 0.0285111 1400 3447.18 2082.4 1364.79 0.173554
|
||||
1 0.0285111 1500 3537.05 2179.02 1358.03 0.173554
|
||||
1 0.0285111 1600 3627.61 2275.87 1351.74 0.173554
|
||||
1 0.0285111 1700 3718.82 2372.94 1345.88 0.173554
|
||||
1 0.0285111 1800 3810.62 2470.21 1340.41 0.173554
|
||||
1 0.0285111 1900 3902.95 2567.65 1335.3 0.173554
|
||||
1 0.0285111 2000 3995.78 2665.26 1330.52 0.173554
|
||||
1 0.0285111 2100 4089.05 2763.02 1326.03 0.173554
|
||||
1 0.0285111 2200 4182.73 2860.91 1321.82 0.173554
|
||||
1 0.0285111 2300 4276.77 2958.92 1317.85 0.173554
|
||||
1 0.0285111 2400 4371.14 3057.05 1314.1 0.173554
|
||||
1 0.0285111 2500 4465.82 3155.27 1310.54 0.173554
|
||||
1 0.0285111 2600 4560.76 3253.59 1307.17 0.173554
|
||||
1 0.0285111 2700 4655.94 3351.98 1303.96 0.173554
|
||||
1 0.0285111 2800 4751.34 3450.45 1300.89 0.173554
|
||||
1 0.0285111 2900 4846.93 3548.98 1297.95 0.173554
|
||||
1 0.0285111 3000 4942.7 3647.57 1295.13 0.173554
|
||||
1.05 0.029894 300 2492.46 2407.6 84.8585 0.00720339
|
||||
1.05 0.029894 400 2572.23 2468.77 103.454 0.00882851
|
||||
1.05 0.029894 500 2652.51 2528.16 124.356 0.0107005
|
||||
1.05 0.029894 600 2733.46 2585.15 148.303 0.0130117
|
||||
1.05 0.029894 700 2815.33 2639.93 175.395 0.0157578
|
||||
1.05 0.029894 800 2898.38 2693.11 205.275 0.0188396
|
||||
1.05 0.029894 900 2982.74 2723.45 259.288 0.0266549
|
||||
1.05 0.029894 1000 3068.23 2622.42 445.805 0.0547019
|
||||
1.05 0.029894 1100 3154.64 2157.67 996.976 0.129741
|
||||
1.05 0.029894 1200 3242.02 2280.98 961.044 0.127053
|
||||
1.05 0.029894 1300 3330.29 2050.85 1279.44 0.170376
|
||||
1.05 0.029894 1400 3419.38 2125.13 1294.25 0.16278
|
||||
1.05 0.029894 1500 3509.23 2169.74 1339.48 0.170593
|
||||
1.05 0.029894 1600 3599.77 2266.59 1333.18 0.170593
|
||||
1.05 0.029894 1700 3690.96 2363.65 1327.3 0.170593
|
||||
1.05 0.029894 1800 3782.73 2460.91 1321.82 0.170593
|
||||
1.05 0.029894 1900 3875.03 2558.35 1316.69 0.170593
|
||||
1.05 0.029894 2000 3967.83 2655.94 1311.88 0.170593
|
||||
1.05 0.029894 2100 4061.07 2753.69 1307.38 0.170593
|
||||
1.05 0.029894 2200 4154.72 2851.57 1303.14 0.170593
|
||||
1.05 0.029894 2300 4248.73 2949.58 1299.15 0.170593
|
||||
1.05 0.029894 2400 4343.07 3047.69 1295.38 0.170593
|
||||
1.05 0.029894 2500 4437.72 3145.91 1291.81 0.170593
|
||||
1.05 0.029894 2600 4532.63 3244.21 1288.42 0.170593
|
||||
1.05 0.029894 2700 4627.79 3342.6 1285.19 0.170593
|
||||
1.05 0.029894 2800 4723.16 3441.06 1282.11 0.170593
|
||||
1.05 0.029894 2900 4818.73 3539.58 1279.15 0.170593
|
||||
1.05 0.029894 3000 4914.48 3638.16 1276.32 0.170593
|
||||
1.1 0.031273 300 2464.87 2386.5 78.3786 0.00662398
|
||||
1.1 0.031273 400 2544.79 2448.61 96.1825 0.00816896
|
||||
1.1 0.031273 500 2625.2 2508.98 116.227 0.0099387
|
||||
1.1 0.031273 600 2706.25 2567.32 138.926 0.0120454
|
||||
1.1 0.031273 700 2788.2 2623.15 165.049 0.0146643
|
||||
1.1 0.031273 800 2871.31 2677.34 193.962 0.017615
|
||||
1.1 0.031273 900 2955.7 2719.78 235.92 0.0231087
|
||||
1.1 0.031273 1000 3041.21 2693.5 347.71 0.0402781
|
||||
1.1 0.031273 1100 3127.63 2167.25 960.385 0.125446
|
||||
1.1 0.031273 1200 3215.01 2111.06 1103.96 0.14489
|
||||
1.1 0.031273 1300 3303.28 2053.83 1249.45 0.167407
|
||||
1.1 0.031273 1400 3392.36 2173.47 1218.89 0.15138
|
||||
1.1 0.031273 1500 3482.19 2160.73 1321.46 0.167732
|
||||
1.1 0.031273 1600 3572.72 2257.57 1315.15 0.167732
|
||||
1.1 0.031273 1700 3663.88 2354.63 1309.25 0.167732
|
||||
1.1 0.031273 1800 3755.63 2451.88 1303.75 0.167732
|
||||
1.1 0.031273 1900 3847.91 2549.3 1298.61 0.167732
|
||||
1.1 0.031273 2000 3940.68 2646.89 1293.79 0.167732
|
||||
1.1 0.031273 2100 4033.89 2744.63 1289.26 0.167732
|
||||
1.1 0.031273 2200 4127.51 2842.51 1285.01 0.167732
|
||||
1.1 0.031273 2300 4221.5 2940.5 1281 0.167732
|
||||
1.1 0.031273 2400 4315.82 3038.61 1277.21 0.167732
|
||||
1.1 0.031273 2500 4410.43 3136.81 1273.62 0.167732
|
||||
1.1 0.031273 2600 4505.32 3235.11 1270.21 0.167732
|
||||
1.1 0.031273 2700 4600.46 3333.49 1266.97 0.167732
|
||||
1.1 0.031273 2800 4695.81 3431.94 1263.87 0.167732
|
||||
1.1 0.031273 2900 4791.36 3530.45 1260.9 0.167732
|
||||
1.1 0.031273 3000 4887.08 3629.03 1258.05 0.167732
|
||||
1.15 0.0326481 300 2438.01 2365.65 72.3675 0.00608988
|
||||
1.15 0.0326481 400 2518.07 2428.67 89.4064 0.00755975
|
||||
1.15 0.0326481 500 2598.61 2489.96 108.651 0.00924133
|
||||
1.15 0.0326481 600 2679.76 2549.42 130.344 0.0112026
|
||||
1.15 0.0326481 700 2761.79 2606.41 155.383 0.0136615
|
||||
1.15 0.0326481 800 2844.96 2661.52 183.443 0.0165071
|
||||
1.15 0.0326481 900 2929.39 2711.04 218.35 0.0205875
|
||||
1.15 0.0326481 1000 3014.93 2720.02 294.911 0.0321946
|
||||
1.15 0.0326481 1100 3101.36 2251.55 849.815 0.109583
|
||||
1.15 0.0326481 1200 3188.75 2233.94 954.807 0.119285
|
||||
1.15 0.0326481 1300 3277.01 2056.18 1220.83 0.164505
|
||||
1.15 0.0326481 1400 3366.09 2095.8 1270.29 0.164884
|
||||
1.15 0.0326481 1500 3455.91 2151.97 1303.94 0.164965
|
||||
1.15 0.0326481 1600 3546.42 2248.81 1297.61 0.164965
|
||||
1.15 0.0326481 1700 3637.57 2345.86 1291.71 0.164965
|
||||
1.15 0.0326481 1800 3729.29 2443.1 1286.19 0.164965
|
||||
1.15 0.0326481 1900 3821.55 2540.52 1281.03 0.164965
|
||||
1.15 0.0326481 2000 3914.3 2638.1 1276.2 0.164965
|
||||
1.15 0.0326481 2100 4007.49 2735.83 1271.66 0.164965
|
||||
1.15 0.0326481 2200 4101.08 2833.69 1267.39 0.164965
|
||||
1.15 0.0326481 2300 4195.04 2931.68 1263.36 0.164965
|
||||
1.15 0.0326481 2400 4289.34 3029.78 1259.56 0.164965
|
||||
1.15 0.0326481 2500 4383.93 3127.98 1255.95 0.164965
|
||||
1.15 0.0326481 2600 4478.8 3226.27 1252.53 0.164965
|
||||
1.15 0.0326481 2700 4573.91 3324.64 1249.27 0.164965
|
||||
1.15 0.0326481 2800 4669.24 3423.08 1246.16 0.164965
|
||||
1.15 0.0326481 2900 4764.77 3521.59 1243.18 0.164965
|
||||
1.15 0.0326481 3000 4860.48 3620.16 1240.32 0.164965
|
||||
1.2 0.0340193 300 2411.84 2345.05 66.7936 0.00559749
|
||||
1.2 0.0340193 400 2492.05 2408.96 83.0903 0.00699607
|
||||
1.2 0.0340193 500 2572.72 2471.14 101.574 0.00859836
|
||||
1.2 0.0340193 600 2653.97 2531.58 122.394 0.010447
|
||||
1.2 0.0340193 700 2736.08 2589.76 146.318 0.012734
|
||||
1.2 0.0340193 800 2819.31 2645.91 173.4 0.0154441
|
||||
1.2 0.0340193 900 2903.78 2699.56 204.22 0.0187
|
||||
1.2 0.0340193 1000 2989.35 2727.81 261.538 0.0270303
|
||||
1.2 0.0340193 1100 3075.8 2577.07 498.722 0.0617691
|
||||
1.2 0.0340193 1200 3163.19 2290.04 873.153 0.105911
|
||||
1.2 0.0340193 1300 3251.46 2053.86 1197.6 0.159385
|
||||
1.2 0.0340193 1400 3340.53 2100.7 1239.83 0.162141
|
||||
1.2 0.0340193 1500 3430.34 2143.45 1286.89 0.162287
|
||||
1.2 0.0340193 1600 3520.84 2240.28 1280.56 0.162287
|
||||
1.2 0.0340193 1700 3611.98 2337.33 1274.65 0.162287
|
||||
1.2 0.0340193 1800 3703.68 2434.56 1269.12 0.162287
|
||||
1.2 0.0340193 1900 3795.92 2531.98 1263.95 0.162287
|
||||
1.2 0.0340193 2000 3888.65 2629.55 1259.1 0.162287
|
||||
1.2 0.0340193 2100 3981.82 2727.27 1254.54 0.162287
|
||||
1.2 0.0340193 2200 4075.39 2825.13 1250.26 0.162287
|
||||
1.2 0.0340193 2300 4169.33 2923.11 1246.22 0.162287
|
||||
1.2 0.0340193 2400 4263.6 3021.2 1242.4 0.162287
|
||||
1.2 0.0340193 2500 4358.17 3119.39 1238.78 0.162287
|
||||
1.2 0.0340193 2600 4453.02 3217.67 1235.34 0.162287
|
||||
1.2 0.0340193 2700 4548.11 3316.04 1232.07 0.162287
|
||||
1.2 0.0340193 2800 4643.42 3414.48 1228.95 0.162287
|
||||
1.2 0.0340193 2900 4738.94 3512.98 1225.96 0.162287
|
||||
1.2 0.0340193 3000 4834.63 3611.54 1223.09 0.162287
|
||||
1.25 0.0353866 300 2386.33 2324.71 61.6276 0.00514364
|
||||
1.25 0.0353866 400 2466.68 2389.48 77.2031 0.00647404
|
||||
1.25 0.0353866 500 2547.49 2452.53 94.9548 0.00800299
|
||||
1.25 0.0353866 600 2628.85 2513.87 114.979 0.00975815
|
||||
1.25 0.0353866 700 2711.04 2573.29 137.745 0.0118577
|
||||
1.25 0.0353866 800 2794.33 2630.39 163.932 0.0144522
|
||||
1.25 0.0353866 900 2878.85 2685.7 193.145 0.0174261
|
||||
1.25 0.0353866 1000 2964.44 2726.14 238.301 0.0235026
|
||||
1.25 0.0353866 1100 3050.91 2678.75 372.156 0.0437591
|
||||
1.25 0.0353866 1200 3138.31 2278.54 859.767 0.105907
|
||||
1.25 0.0353866 1300 3226.58 2199 1027.58 0.135896
|
||||
1.25 0.0353866 1400 3315.66 2103.52 1212.14 0.159473
|
||||
1.25 0.0353866 1500 3405.47 2140.38 1265.09 0.159689
|
||||
1.25 0.0353866 1600 3495.96 2231.99 1263.97 0.159696
|
||||
1.25 0.0353866 1700 3587.08 2329.03 1258.05 0.159696
|
||||
1.25 0.0353866 1800 3678.77 2426.26 1252.51 0.159696
|
||||
1.25 0.0353866 1900 3771 2523.67 1247.33 0.159696
|
||||
1.25 0.0353866 2000 3863.7 2621.24 1242.47 0.159696
|
||||
1.25 0.0353866 2100 3956.85 2718.95 1237.9 0.159696
|
||||
1.25 0.0353866 2200 4050.4 2816.8 1233.6 0.159696
|
||||
1.25 0.0353866 2300 4144.32 2914.78 1229.55 0.159696
|
||||
1.25 0.0353866 2400 4238.57 3012.86 1225.72 0.159696
|
||||
1.25 0.0353866 2500 4333.13 3111.04 1222.08 0.159696
|
||||
1.25 0.0353866 2600 4427.96 3209.32 1218.64 0.159696
|
||||
1.25 0.0353866 2700 4523.03 3307.68 1215.35 0.159696
|
||||
1.25 0.0353866 2800 4618.33 3406.11 1212.22 0.159696
|
||||
1.25 0.0353866 2900 4713.83 3504.61 1209.22 0.159696
|
||||
1.25 0.0353866 3000 4809.51 3603.17 1206.34 0.159696
|
||||
1.3 0.0367501 300 2361.46 2304.62 56.8423 0.0047254
|
||||
1.3 0.0367501 400 2441.96 2370.24 71.7168 0.00599037
|
||||
1.3 0.0367501 500 2522.89 2434.13 88.7599 0.00745029
|
||||
1.3 0.0367501 600 2604.36 2496.32 108.04 0.00912394
|
||||
1.3 0.0367501 700 2686.63 2556.78 129.858 0.011087
|
||||
1.3 0.0367501 800 2769.99 2614.93 155.053 0.0135382
|
||||
1.3 0.0367501 900 2854.55 2671.11 183.441 0.0164082
|
||||
1.3 0.0367501 1000 2940.18 2719.34 220.839 0.020966
|
||||
1.3 0.0367501 1100 3026.67 2716.03 310.638 0.0345757
|
||||
1.3 0.0367501 1200 3114.09 2299.17 814.917 0.0995504
|
||||
1.3 0.0367501 1300 3202.36 2339.63 862.738 0.100832
|
||||
1.3 0.0367501 1400 3291.44 2105.72 1185.72 0.156866
|
||||
1.3 0.0367501 1500 3381.25 2198.32 1182.93 0.146587
|
||||
1.3 0.0367501 1600 3471.74 2223.91 1247.82 0.157186
|
||||
1.3 0.0367501 1700 3562.85 2320.95 1241.9 0.157186
|
||||
1.3 0.0367501 1800 3654.53 2418.18 1236.35 0.157186
|
||||
1.3 0.0367501 1900 3746.74 2515.58 1231.16 0.157186
|
||||
1.3 0.0367501 2000 3839.43 2613.14 1226.29 0.157186
|
||||
1.3 0.0367501 2100 3932.56 2710.86 1221.71 0.157186
|
||||
1.3 0.0367501 2200 4026.1 2808.7 1217.4 0.157186
|
||||
1.3 0.0367501 2300 4120 2906.67 1213.33 0.157186
|
||||
1.3 0.0367501 2400 4214.23 3004.75 1209.49 0.157186
|
||||
1.3 0.0367501 2500 4308.77 3102.92 1205.85 0.157186
|
||||
1.3 0.0367501 2600 4403.58 3201.19 1202.39 0.157186
|
||||
1.3 0.0367501 2700 4498.64 3299.55 1199.09 0.157186
|
||||
1.3 0.0367501 2800 4593.92 3397.98 1195.95 0.157186
|
||||
1.3 0.0367501 2900 4689.41 3496.47 1192.94 0.157186
|
||||
1.3 0.0367501 3000 4785.08 3595.03 1190.05 0.157186
|
||||
1.35 0.0381097 300 2337.2 2284.79 52.412 0.00434014
|
||||
1.35 0.0381097 400 2417.84 2351.24 66.6057 0.00554218
|
||||
1.35 0.0381097 500 2498.91 2415.95 82.9607 0.00693641
|
||||
1.35 0.0381097 600 2580.49 2478.96 101.531 0.00853635
|
||||
1.35 0.0381097 700 2662.85 2540.32 122.523 0.0103923
|
||||
1.35 0.0381097 800 2746.26 2599.53 146.737 0.0126998
|
||||
1.35 0.0381097 900 2830.88 2656.73 174.152 0.0154295
|
||||
1.35 0.0381097 1000 2916.54 2709.67 206.872 0.019057
|
||||
1.35 0.0381097 1100 3003.05 2730.09 272.96 0.0288177
|
||||
1.35 0.0381097 1200 3090.48 2251.76 838.725 0.106808
|
||||
1.35 0.0381097 1300 3178.77 2336.41 842.362 0.0992999
|
||||
1.35 0.0381097 1400 3267.85 2107.34 1160.51 0.154319
|
||||
1.35 0.0381097 1500 3357.67 2235.58 1122.08 0.13749
|
||||
1.35 0.0381097 1600 3448.15 2216.05 1232.1 0.154753
|
||||
1.35 0.0381097 1700 3539.25 2313.09 1226.17 0.154753
|
||||
1.35 0.0381097 1800 3630.93 2410.31 1220.62 0.154753
|
||||
1.35 0.0381097 1900 3723.12 2507.71 1215.42 0.154753
|
||||
1.35 0.0381097 2000 3815.8 2605.27 1210.53 0.154753
|
||||
1.35 0.0381097 2100 3908.92 2702.97 1205.95 0.154753
|
||||
1.35 0.0381097 2200 4002.44 2800.81 1201.63 0.154753
|
||||
1.35 0.0381097 2300 4096.33 2898.78 1197.55 0.154753
|
||||
1.35 0.0381097 2400 4190.55 2996.85 1193.7 0.154753
|
||||
1.35 0.0381097 2500 4285.07 3095.02 1190.04 0.154753
|
||||
1.35 0.0381097 2600 4379.86 3193.29 1186.58 0.154753
|
||||
1.35 0.0381097 2700 4474.91 3291.64 1183.27 0.154753
|
||||
1.35 0.0381097 2800 4570.18 3390.06 1180.12 0.154753
|
||||
1.35 0.0381097 2900 4665.65 3488.55 1177.1 0.154753
|
||||
1.35 0.0381097 3000 4761.31 3587.1 1174.21 0.154753
|
||||
|
||||
end
|
||||
@ -0,0 +1,3 @@
|
||||
equilibriumFlameT.C
|
||||
|
||||
EXE = $(FOAM_APPBIN)/equilibriumFlameT
|
||||
@ -0,0 +1,2 @@
|
||||
EXE_INC = -I$(LIB_SRC)/thermophysicalModels/specie/lnInclude
|
||||
EXE_LIBS = -lspecie
|
||||
@ -0,0 +1,66 @@
|
||||
/*--------------------------------*- C++ -*----------------------------------*\
|
||||
| ========= | |
|
||||
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
|
||||
| \\ / O peration | Version: dev |
|
||||
| \\ / A nd | Web: www.OpenFOAM.org |
|
||||
| \\/ M anipulation | |
|
||||
\*---------------------------------------------------------------------------*/
|
||||
FoamFile
|
||||
{
|
||||
version 2.0;
|
||||
format ascii;
|
||||
note "settings for calculating the equilibrium flame temperature";
|
||||
class dictionary;
|
||||
object controlDict;
|
||||
}
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
P 1e5;
|
||||
|
||||
H2
|
||||
{
|
||||
fuel H2;
|
||||
n 0;
|
||||
m 2;
|
||||
}
|
||||
|
||||
CH4
|
||||
{
|
||||
fuel CH4___ANHARMONIC;
|
||||
n 1;
|
||||
m 4;
|
||||
}
|
||||
|
||||
ETHYLENE
|
||||
{
|
||||
fuel C2H4;
|
||||
n 2;
|
||||
m 4;
|
||||
}
|
||||
|
||||
PROPANE
|
||||
{
|
||||
fuel C3H8;
|
||||
n 3;
|
||||
m 8;
|
||||
}
|
||||
|
||||
OCTANE
|
||||
{
|
||||
fuel C8H18(L)_isooctane;
|
||||
n 8;
|
||||
m 18;
|
||||
}
|
||||
|
||||
N-HEPTANE
|
||||
{
|
||||
fuel C7H16_n-heptane;
|
||||
n 7;
|
||||
m 16;
|
||||
}
|
||||
|
||||
$H2;
|
||||
// $CH4;
|
||||
// $PROPANE;
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,282 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2011-2013 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
|
||||
equilibriumFlameT
|
||||
|
||||
Description
|
||||
Calculates the equilibrium flame temperature for a given fuel and
|
||||
pressure for a range of unburnt gas temperatures and equivalence
|
||||
ratios; the effects of dissociation on O2, H2O and CO2 are included.
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#include "argList.H"
|
||||
#include "Time.H"
|
||||
#include "dictionary.H"
|
||||
#include "IFstream.H"
|
||||
#include "OSspecific.H"
|
||||
#include "IOmanip.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())
|
||||
{
|
||||
FatalErrorIn(args.executable())
|
||||
<< "Cannot read file " << controlFileName
|
||||
<< abort(FatalError);
|
||||
}
|
||||
|
||||
dictionary control(controlFile);
|
||||
|
||||
|
||||
scalar P(readScalar(control.lookup("P")));
|
||||
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())
|
||||
{
|
||||
FatalErrorIn(args.executable())
|
||||
<< "Cannot read file " << thermoDataFileName
|
||||
<< abort(FatalError);
|
||||
}
|
||||
|
||||
dictionary thermoData(thermoDataFile);
|
||||
|
||||
|
||||
Info<< nl << "Reading thermodynamic data for relevant species"
|
||||
<< nl << endl;
|
||||
|
||||
// Reactants
|
||||
thermo FUEL(thermoData.subDict(fuelName));
|
||||
thermo O2(thermoData.subDict("O2"));
|
||||
thermo N2(thermoData.subDict("N2"));
|
||||
|
||||
// Products
|
||||
thermo CO2(thermoData.subDict("CO2"));
|
||||
thermo H2O(thermoData.subDict("H2O"));
|
||||
|
||||
// Product fragments
|
||||
thermo CO(thermoData.subDict("CO"));
|
||||
thermo H2(thermoData.subDict("H2"));
|
||||
|
||||
|
||||
// Product dissociation reactions
|
||||
|
||||
thermo CO2BreakUp
|
||||
(
|
||||
CO2 == CO + 0.5* O2
|
||||
);
|
||||
|
||||
thermo H2OBreakUp
|
||||
(
|
||||
H2O == H2 + 0.5*O2
|
||||
);
|
||||
|
||||
|
||||
// Stoiciometric number of moles of species for one mole of fuel
|
||||
scalar stoicO2 = n + m/4.0;
|
||||
scalar stoicN2 = (0.79/0.21)*(n + m/4.0);
|
||||
scalar stoicCO2 = n;
|
||||
scalar stoicH2O = m/2.0;
|
||||
|
||||
// Oxidant
|
||||
thermo oxidant
|
||||
(
|
||||
"oxidant",
|
||||
stoicO2*O2
|
||||
+ stoicN2*N2
|
||||
);
|
||||
|
||||
dimensionedScalar stoichiometricAirFuelMassRatio
|
||||
(
|
||||
"stoichiometricAirFuelMassRatio",
|
||||
dimless,
|
||||
(oxidant.W()*oxidant.nMoles())/FUEL.W()
|
||||
);
|
||||
|
||||
Info<< "stoichiometricAirFuelMassRatio "
|
||||
<< stoichiometricAirFuelMassRatio << ';' << endl;
|
||||
|
||||
Info<< "Equilibrium flame temperature data ("
|
||||
<< P/1e5 << " bar)" << nl << nl
|
||||
<< setw(3) << "Phi"
|
||||
<< setw(12) << "ft"
|
||||
<< setw(7) << "T0"
|
||||
<< setw(12) << "Tad"
|
||||
<< setw(12) << "Teq"
|
||||
<< setw(12) << "Terror"
|
||||
<< setw(20) << "O2res (mole frac)" << nl
|
||||
<< endl;
|
||||
|
||||
|
||||
// Loop over equivalence ratios
|
||||
for (int i=0; i<16; i++)
|
||||
{
|
||||
scalar equiv = 0.6 + i*0.05;
|
||||
scalar ft = 1/(1 + stoichiometricAirFuelMassRatio.value()/equiv);
|
||||
|
||||
// Loop over initial temperatures
|
||||
for (int j=0; j<28; j++)
|
||||
{
|
||||
scalar T0 = 300.0 + j*100.0;
|
||||
|
||||
// Number of moles of species for one mole of fuel
|
||||
scalar o2 = (1.0/equiv)*stoicO2;
|
||||
scalar n2 = (0.79/0.21)*o2;
|
||||
scalar fres = max(1.0 - 1.0/equiv, 0.0);
|
||||
scalar fburnt = 1.0 - fres;
|
||||
|
||||
// Initial guess for number of moles of product species
|
||||
// ignoring product dissociation
|
||||
scalar oresInit = max(1.0/equiv - 1.0, 0.0)*stoicO2;
|
||||
scalar co2Init = fburnt*stoicCO2;
|
||||
scalar h2oInit = fburnt*stoicH2O;
|
||||
|
||||
scalar ores = oresInit;
|
||||
scalar co2 = co2Init;
|
||||
scalar h2o = h2oInit;
|
||||
|
||||
scalar co = 0.0;
|
||||
scalar h2 = 0.0;
|
||||
|
||||
// Total number of moles in system
|
||||
scalar N = fres + n2 + co2 + h2o + ores;
|
||||
|
||||
|
||||
// Initial guess for adiabatic flame temperature
|
||||
scalar adiabaticFlameTemperature =
|
||||
T0
|
||||
+ (fburnt/(1.0 + o2 + n2))/(1.0/(1.0 + (1.0 + 0.79/0.21)*stoicO2))
|
||||
*2000.0;
|
||||
|
||||
scalar equilibriumFlameTemperature = adiabaticFlameTemperature;
|
||||
|
||||
|
||||
// Iteration loop for adiabatic flame temperature
|
||||
for (int j=0; j<20; j++)
|
||||
{
|
||||
|
||||
if (j > 0)
|
||||
{
|
||||
co = co2*
|
||||
min
|
||||
(
|
||||
CO2BreakUp.Kn(P, equilibriumFlameTemperature, N)
|
||||
/::sqrt(max(ores, 0.001)),
|
||||
1.0
|
||||
);
|
||||
|
||||
h2 = h2o*
|
||||
min
|
||||
(
|
||||
H2OBreakUp.Kn(P, equilibriumFlameTemperature, N)
|
||||
/::sqrt(max(ores, 0.001)),
|
||||
1.0
|
||||
);
|
||||
|
||||
co2 = co2Init - co;
|
||||
h2o = h2oInit - h2;
|
||||
ores = oresInit + 0.5*co + 0.5*h2;
|
||||
}
|
||||
|
||||
thermo reactants
|
||||
(
|
||||
FUEL + o2*O2 + n2*N2
|
||||
);
|
||||
|
||||
thermo products
|
||||
(
|
||||
fres*FUEL + ores*O2 + n2*N2
|
||||
+ co2*CO2 + h2o*H2O + co*CO + h2*H2
|
||||
);
|
||||
|
||||
|
||||
scalar equilibriumFlameTemperatureNew =
|
||||
products.THa(reactants.Ha(P, T0), P, adiabaticFlameTemperature);
|
||||
|
||||
if (j==0)
|
||||
{
|
||||
adiabaticFlameTemperature = equilibriumFlameTemperatureNew;
|
||||
}
|
||||
else
|
||||
{
|
||||
equilibriumFlameTemperature = 0.5*
|
||||
(
|
||||
equilibriumFlameTemperature
|
||||
+ equilibriumFlameTemperatureNew
|
||||
);
|
||||
}
|
||||
}
|
||||
|
||||
Info<< setw(3) << equiv
|
||||
<< setw(12) << ft
|
||||
<< setw(7) << T0
|
||||
<< setw(12) << adiabaticFlameTemperature
|
||||
<< setw(12) << equilibriumFlameTemperature
|
||||
<< setw(12)
|
||||
<< adiabaticFlameTemperature - equilibriumFlameTemperature
|
||||
<< setw(12) << ores/N
|
||||
<< endl;
|
||||
}
|
||||
}
|
||||
|
||||
Info<< nl << "end" << endl;
|
||||
|
||||
return 0;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,3 @@
|
||||
mixtureAdiabaticFlameT.C
|
||||
|
||||
EXE = $(FOAM_APPBIN)/mixtureAdiabaticFlameT
|
||||
@ -0,0 +1,5 @@
|
||||
EXE_INC = \
|
||||
-I$(LIB_SRC)/thermophysicalModels/specie/lnInclude
|
||||
|
||||
EXE_LIBS = \
|
||||
-lspecie
|
||||
@ -0,0 +1,41 @@
|
||||
/*--------------------------------*- C++ -*----------------------------------*\
|
||||
| ========= | |
|
||||
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
|
||||
| \\ / O peration | Version: dev |
|
||||
| \\ / A nd | Web: www.OpenFOAM.org |
|
||||
| \\/ M anipulation | |
|
||||
\*---------------------------------------------------------------------------*/
|
||||
FoamFile
|
||||
{
|
||||
version 2.0;
|
||||
format ascii;
|
||||
note "settings for calculating the adiabatic flame temperature";
|
||||
class dictionary;
|
||||
object controlDict;
|
||||
}
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
P 1e5;
|
||||
T0 300;
|
||||
|
||||
reactants
|
||||
3
|
||||
(
|
||||
//reactant volume fraction
|
||||
H2 0.29577
|
||||
O2 0.14788
|
||||
N2 0.55635
|
||||
)
|
||||
hydrogen;
|
||||
|
||||
|
||||
products
|
||||
2
|
||||
(
|
||||
H2O 0.3471
|
||||
N2 0.6529
|
||||
)
|
||||
waterVapour;
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,109 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2011 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/>.
|
||||
|
||||
Class
|
||||
Foam::mixture
|
||||
|
||||
Description
|
||||
|
||||
SourceFiles
|
||||
mixtureI.H
|
||||
mixture.C
|
||||
mixtureIO.C
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#ifndef mixture_H
|
||||
#define mixture_H
|
||||
|
||||
#include "error.H"
|
||||
|
||||
#include "List.H"
|
||||
#include "substance.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
|
||||
/*---------------------------------------------------------------------------*\
|
||||
Class mixture Declaration
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
class mixture
|
||||
:
|
||||
public List<substance>
|
||||
{
|
||||
// Private data
|
||||
|
||||
word name_;
|
||||
|
||||
|
||||
public:
|
||||
|
||||
// Constructors
|
||||
|
||||
//- Construct from Istream
|
||||
mixture(Istream& is)
|
||||
:
|
||||
List<substance>(is),
|
||||
name_(is)
|
||||
{
|
||||
scalar volTot = 0;
|
||||
|
||||
for (label i = 0; i < size(); i++)
|
||||
{
|
||||
volTot += operator[](i).volFrac();
|
||||
}
|
||||
|
||||
if (volTot > 1.001 || volTot < 0.999)
|
||||
{
|
||||
FatalErrorIn("mixture::mixture(istream& is)")
|
||||
<< "Sum of volume fractions for Mixture " << name_
|
||||
<< " = " << volTot << endl
|
||||
<< "Should equal one."
|
||||
<< abort(FatalError);
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
// Access
|
||||
|
||||
const word& name() const
|
||||
{
|
||||
return name_;
|
||||
}
|
||||
};
|
||||
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,127 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2011-2013 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
|
||||
mixtureAdiabaticFlameT
|
||||
|
||||
Description
|
||||
Calculates the adiabatic flame temperature for a given mixture
|
||||
at a given temperature.
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#include "argList.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"
|
||||
#include "mixture.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())
|
||||
{
|
||||
FatalErrorIn(args.executable())
|
||||
<< "Cannot read file " << controlFileName
|
||||
<< abort(FatalError);
|
||||
}
|
||||
|
||||
dictionary control(controlFile);
|
||||
|
||||
|
||||
scalar P(readScalar(control.lookup("P")));
|
||||
scalar T0(readScalar(control.lookup("T0")));
|
||||
mixture rMix(control.lookup("reactants"));
|
||||
mixture pMix(control.lookup("products"));
|
||||
|
||||
|
||||
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())
|
||||
{
|
||||
FatalErrorIn(args.executable())
|
||||
<< "Cannot read file " << thermoDataFileName
|
||||
<< abort(FatalError);
|
||||
}
|
||||
|
||||
dictionary thermoData(thermoDataFile);
|
||||
|
||||
|
||||
thermo reactants
|
||||
(
|
||||
rMix[0].volFrac()*thermo(thermoData.subDict(rMix[0].name()))
|
||||
);
|
||||
|
||||
for (label i = 1; i < rMix.size(); i++)
|
||||
{
|
||||
reactants = reactants
|
||||
+ rMix[i].volFrac()*thermo(thermoData.subDict(rMix[i].name()));
|
||||
}
|
||||
|
||||
|
||||
thermo products
|
||||
(
|
||||
2*pMix[0].volFrac()*thermo(thermoData.subDict(pMix[0].name()))
|
||||
);
|
||||
|
||||
for (label i = 1; i < pMix.size(); i++)
|
||||
{
|
||||
products = products
|
||||
+ 2*pMix[i].volFrac()*thermo(thermoData.subDict(pMix[i].name()));
|
||||
}
|
||||
|
||||
Info<< "Adiabatic flame temperature of mixture " << rMix.name() << " = "
|
||||
<< products.THa(reactants.Ha(P, T0), P, 1000.0) << " K" << endl;
|
||||
|
||||
return 0;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -0,0 +1,118 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2011 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/>.
|
||||
|
||||
Class
|
||||
Foam::substance
|
||||
|
||||
Description
|
||||
|
||||
SourceFiles
|
||||
substanceI.H
|
||||
substance.C
|
||||
substanceIO.C
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#ifndef substance_H
|
||||
#define substance_H
|
||||
|
||||
#include "scalar.H"
|
||||
#include "word.H"
|
||||
#include "Istream.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
namespace Foam
|
||||
{
|
||||
|
||||
/*---------------------------------------------------------------------------*\
|
||||
Class substance Declaration
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
class substance
|
||||
{
|
||||
// Private data
|
||||
|
||||
word name_;
|
||||
scalar volFrac_;
|
||||
|
||||
|
||||
public:
|
||||
|
||||
// Constructors
|
||||
|
||||
//- Construct null
|
||||
substance()
|
||||
{}
|
||||
|
||||
|
||||
// Member Functions
|
||||
|
||||
// Access
|
||||
|
||||
const word& name() const
|
||||
{
|
||||
return name_;
|
||||
}
|
||||
|
||||
scalar volFrac() const
|
||||
{
|
||||
return volFrac_;
|
||||
}
|
||||
|
||||
bool operator==(const substance& s) const
|
||||
{
|
||||
return name_ == s.name_ && volFrac_ == s.volFrac_;
|
||||
}
|
||||
|
||||
bool operator!=(const substance& s) const
|
||||
{
|
||||
return !operator==(s);
|
||||
}
|
||||
|
||||
|
||||
// IOstream Operators
|
||||
|
||||
friend Istream& operator>>(Istream& is, substance& s)
|
||||
{
|
||||
is >> s.name_ >> s.volFrac_;
|
||||
return is;
|
||||
}
|
||||
|
||||
friend Ostream& operator<<(Ostream& os, const substance& s)
|
||||
{
|
||||
os << s.name_ << token::SPACE << s.volFrac_;
|
||||
return os;
|
||||
}
|
||||
};
|
||||
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
} // End namespace Foam
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
#endif
|
||||
|
||||
// ************************************************************************* //
|
||||
Reference in New Issue
Block a user