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ENH: tutorial thermo input updates
This commit is contained in:
@ -25,34 +25,49 @@ stoichiometricAirFuelMassRatio
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// ft = 0.0352993
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// Tad = 1650.1
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||||
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fuel fuel 1 44.0962
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||||
100 5000 1000
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||||
7.53414 0.0188722 -6.27185e-06 9.14756e-10 -4.78381e-14 -16467.5 -17.8923
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||||
0.933554 0.0264246 6.10597e-06 -2.19775e-08 9.51493e-12 -13958.5 19.2017
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||||
1.67212e-06 170.672;
|
||||
//fuel fuel 1 44.0962
|
||||
// 100 5000 1000
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||||
// 7.53414 0.0188722 -6.27185e-06 9.14756e-10 -4.78381e-14 -16467.5 -17.8923
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||||
// 0.933554 0.0264246 6.10597e-06 -2.19775e-08 9.51493e-12 -13958.5 19.2017
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||||
// 1.67212e-06 170.672;
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||||
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||||
oxidant oxidant 1 28.8504
|
||||
100 6000 1000
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||||
3.10131 0.00124137 -4.18816e-07 6.64158e-11 -3.91274e-15 -985.266 5.35597
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||||
3.58378 -0.000727005 1.67057e-06 -1.09203e-10 -4.31765e-13 -1050.53 3.11239
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||||
1.67212e-06 170.672;
|
||||
//oxidant oxidant 1 28.8504
|
||||
// 100 6000 1000
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||||
// 3.10131 0.00124137 -4.18816e-07 6.64158e-11 -3.91274e-15 -985.266 5.35597
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||||
// 3.58378 -0.000727005 1.67057e-06 -1.09203e-10 -4.31765e-13 -1050.53 3.11239
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||||
// 1.67212e-06 170.672;
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||||
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||||
reactants reactants 1 29.2068
|
||||
100 5000 1000
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||||
3.20495 0.00165359 -5.55661e-07 8.62503e-11 -4.93973e-15 -1347.25 4.81241
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||||
3.52181 -9.21936e-05 1.77427e-06 -6.2049e-10 -1.99209e-13 -1352.32 3.48856
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||||
1.67212e-06 170.672;
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||||
reactants
|
||||
{
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||||
nMoles 1;
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||||
molWeight 29.2068;
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||||
Tlow 100;
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Thigh 5000;
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Tcommon 1000;
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||||
highCpCoeffs (3.20495 0.00165359 -5.55661e-07 8.62503e-11 -4.93973e-15 -1347.25 4.81241);
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||||
lowCpCoeffs (3.52181 -9.21936e-05 1.77427e-06 -6.2049e-10 -1.99209e-13 -1352.32 3.48856);
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||||
As 1.67212e-06;
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||||
Ts 170.672;
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||||
}
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||||
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||||
burntProducts burntProducts 1 28.3233
|
||||
100 6000 1000
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||||
3.10558 0.00179747 -5.94696e-07 9.05605e-11 -5.08443e-15 -11003.6 5.12104
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||||
3.49796 0.000638555 -1.83881e-07 1.20989e-09 -7.68691e-13 -11080.5 3.18188
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||||
1.67212e-06 170.672;
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||||
//burntProducts burntProducts 1 28.3233
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||||
// 100 6000 1000
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||||
// 3.10558 0.00179747 -5.94696e-07 9.05605e-11 -5.08443e-15 -11003.6 5.12104
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||||
// 3.49796 0.000638555 -1.83881e-07 1.20989e-09 -7.68691e-13 -11080.5 3.18188
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// 1.67212e-06 170.672;
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||||
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products
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||||
{
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nMoles 1;
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||||
molWeight 28.5396;
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||||
Tlow 100;
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Thigh 5000;
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Tcommon 1000;
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highCpCoeffs (3.10383 0.00156927 -5.22523e-07 8.06527e-11 -4.60363e-15 -6892.54 5.21744);
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lowCpCoeffs (3.53318 7.81943e-05 5.77097e-07 6.68595e-10 -6.30433e-13 -6964.71 3.15336);
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||||
As 1.67212e-06;
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||||
Ts 170.672;
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||||
}
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||||
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products products 1 28.5396
|
||||
100 5000 1000
|
||||
3.10383 0.00156927 -5.22523e-07 8.06527e-11 -4.60363e-15 -6892.54 5.21744
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||||
3.53318 7.81943e-05 5.77097e-07 6.68595e-10 -6.30433e-13 -6964.71 3.15336
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1.67212e-06 170.672;
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||||
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// ************************************************************************* //
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@ -21,38 +21,30 @@ thermoType
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stoichiometricAirFuelMassRatio
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stoichiometricAirFuelMassRatio [0 0 0 0 0 0 0] 15.675;
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// phi = 0.57
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// ft = 0.0352993
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// Tad = 1650.1
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reactants
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||||
{
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||||
nMoles 1;
|
||||
molWeight 29.2068;
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||||
Tlow 100;
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||||
Thigh 5000;
|
||||
Tcommon 1000;
|
||||
highCpCoeffs (3.20495 0.00165359 -5.55661e-07 8.62503e-11 -4.93973e-15 -1347.25 4.81241);
|
||||
lowCpCoeffs (3.52181 -9.21936e-05 1.77427e-06 -6.2049e-10 -1.99209e-13 -1352.32 3.48856);
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||||
As 1.67212e-06;
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||||
Ts 170.672;
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||||
}
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||||
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fuel fuel 1 44.0962
|
||||
100 5000 1000
|
||||
7.53414 0.0188722 -6.27185e-06 9.14756e-10 -4.78381e-14 -16467.5 -17.8923
|
||||
0.933554 0.0264246 6.10597e-06 -2.19775e-08 9.51493e-12 -13958.5 19.2017
|
||||
1.67212e-06 170.672;
|
||||
|
||||
oxidant oxidant 1 28.8504
|
||||
100 6000 1000
|
||||
3.10131 0.00124137 -4.18816e-07 6.64158e-11 -3.91274e-15 -985.266 5.35597
|
||||
3.58378 -0.000727005 1.67057e-06 -1.09203e-10 -4.31765e-13 -1050.53 3.11239
|
||||
1.67212e-06 170.672;
|
||||
|
||||
reactants reactants 1 29.2068
|
||||
100 5000 1000
|
||||
3.20495 0.00165359 -5.55661e-07 8.62503e-11 -4.93973e-15 -1347.25 4.81241
|
||||
3.52181 -9.21936e-05 1.77427e-06 -6.2049e-10 -1.99209e-13 -1352.32 3.48856
|
||||
1.67212e-06 170.672;
|
||||
|
||||
burntProducts burntProducts 1 28.3233
|
||||
100 6000 1000
|
||||
3.10558 0.00179747 -5.94696e-07 9.05605e-11 -5.08443e-15 -11003.6 5.12104
|
||||
3.49796 0.000638555 -1.83881e-07 1.20989e-09 -7.68691e-13 -11080.5 3.18188
|
||||
1.67212e-06 170.672;
|
||||
|
||||
products products 1 28.5396
|
||||
100 5000 1000
|
||||
3.10383 0.00156927 -5.22523e-07 8.06527e-11 -4.60363e-15 -6892.54 5.21744
|
||||
3.53318 7.81943e-05 5.77097e-07 6.68595e-10 -6.30433e-13 -6964.71 3.15336
|
||||
1.67212e-06 170.672;
|
||||
products
|
||||
{
|
||||
nMoles 1;
|
||||
molWeight 28.5396;
|
||||
Tlow 100;
|
||||
Thigh 5000;
|
||||
Tcommon 1000;
|
||||
highCpCoeffs (3.10383 0.00156927 -5.22523e-07 8.06527e-11 -4.60363e-15 -6892.54 5.21744);
|
||||
lowCpCoeffs (3.53318 7.81943e-05 5.77097e-07 6.68595e-10 -6.30433e-13 -6964.71 3.15336);
|
||||
As 1.67212e-06;
|
||||
Ts 170.672;
|
||||
}
|
||||
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||||
// ************************************************************************* //
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@ -19,15 +19,30 @@ thermoType hhuMixtureThermo<homogeneousMixture<sutherlandTransport<specieTh
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stoichiometricAirFuelMassRatio stoichiometricAirFuelMassRatio [ 0 0 0 0 0 0 0 ] 15.675;
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||||
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fuel fuel 1 44.0962 200 5000 1000 7.53414 0.0188722 -6.27185e-06 9.14756e-10 -4.78381e-14 -16467.5 -17.8923 0.933554 0.0264246 6.10597e-06 -2.19775e-08 9.51493e-12 -13958.5 19.2017 1.67212e-06 170.672;
|
||||
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||||
oxidant oxidant 1 28.8504 200 6000 1000 3.10205 0.00123963 -4.17512e-07 6.60292e-11 -3.87448e-15 -985.517 5.35187 3.58378 -0.0007269 1.66985e-06 -1.08452e-10 -4.31951e-13 -1050.53 3.11223 1.67212e-06 170.672;
|
||||
|
||||
reactants reactants 24.8095 29.4649 200 5000 1000 3.28069 0.00195035 -6.53483e-07 1.00239e-10 -5.64653e-15 -1609.55 4.41496 3.47696 0.000367499 1.84866e-06 -9.8993e-10 -3.10214e-14 -1570.81 3.76075 1.67212e-06 170.672;
|
||||
|
||||
products products 1 28.3233 200 5000 1000 3.106 0.00179682 -5.94382e-07 9.04998e-11 -5.08033e-15 -11003.7 5.11872 3.49612 0.000650364 -2.08029e-07 1.2291e-09 -7.73697e-13 -11080.3 3.18978 1.67212e-06 170.672;
|
||||
|
||||
burntProducts burntProducts 25.8095 28.3233 200 6000 1000 3.106 0.00179682 -5.94382e-07 9.04998e-11 -5.08033e-15 -11003.7 5.11872 3.49612 0.000650364 -2.08029e-07 1.2291e-09 -7.73697e-13 -11080.3 3.18978 1.67212e-06 170.672;
|
||||
reactants
|
||||
{
|
||||
nMoles 24.8095;
|
||||
molWeight 29.4649;
|
||||
Tlow 200;
|
||||
Thigh 5000;
|
||||
Tcommon 1000;
|
||||
highCpCoeffs (3.28069 0.00195035 -6.53483e-07 1.00239e-10 -5.64653e-15 -1609.55 4.41496);
|
||||
lowCpCoeffs ( 3.47696 0.000367499 1.84866e-06 -9.8993e-10 -3.10214e-14 -1570.81 3.76075);
|
||||
As 1.67212e-06;
|
||||
Ts 170.672;
|
||||
}
|
||||
|
||||
products
|
||||
{
|
||||
nMoles 1;
|
||||
molWeight 28.3233;
|
||||
Tlow 200;
|
||||
Thigh 5000;
|
||||
Tcommon 1000;
|
||||
highCpCoeffs (3.106 0.00179682 -5.94382e-07 9.04998e-11 -5.08033e-15 -11003.7 5.11872);
|
||||
lowCpCoeffs (3.49612 0.000650364 -2.08029e-07 1.2291e-09 -7.73697e-13 -11080.3 3.18978);
|
||||
As 1.67212e-06;
|
||||
Ts 170.672;
|
||||
}
|
||||
|
||||
// ************************************************************************* //
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||||
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||||
@ -8,8 +8,17 @@ species
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||||
);
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||||
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||||
reactions
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||||
(
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||||
{
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||||
irreversibleArrheniusReaction
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||||
CH4 + 2O2 = CO2 + 2H2O
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||||
(5.2e16 0 14906)
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||||
);
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||||
{
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||||
reaction "CH4 + 2O2 = CO2 + 2H2O";
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||||
A 5.2e16;
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||||
beta 0;
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||||
Ta 14906;
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||||
}
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||||
}
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||||
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// irreversibleArrheniusReaction
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// CH4 + 2O2 = CO2 + 2H2O
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||||
// (5.2e16 0 14906)
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||||
//);
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@ -17,7 +17,15 @@ FoamFile
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||||
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||||
thermoType hPsiThermo<pureMixture<constTransport<specieThermo<hConstThermo<perfectGas>>>>>;
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||||
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||||
mixture air 1 28.9 1000 0 1.8e-05 0.7;
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||||
mixture
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||||
{
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||||
nMoles 1;
|
||||
molWeight 28.9;
|
||||
Cp 1000;
|
||||
Hf 0;
|
||||
Mu 1.8e-05;
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||||
Pr 0.7;
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||||
}
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||||
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||||
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||||
// ************************************************************************* //
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||||
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||||
@ -17,7 +17,15 @@ FoamFile
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||||
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||||
thermoType hPsiThermo<pureMixture<sutherlandTransport<specieThermo<hConstThermo<perfectGas>>>>>;
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||||
|
||||
mixture air 1 28.9 1007 0 1.4792e-06 116;
|
||||
mixture
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||||
{
|
||||
nMoles 1;
|
||||
molWeight 28.9;
|
||||
Cp 1007;
|
||||
Hf 0;
|
||||
As 1.4792e-06;
|
||||
Ts 116;
|
||||
}
|
||||
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||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -17,7 +17,15 @@ FoamFile
|
||||
|
||||
thermoType hPsiThermo<pureMixture<constTransport<specieThermo<hConstThermo<perfectGas>>>>>;
|
||||
|
||||
mixture air 1 28.9 1007 0 1.84e-05 0.7;
|
||||
mixture
|
||||
{
|
||||
nMoles 1;
|
||||
molWeight 28.9;
|
||||
Cp 1007;
|
||||
Hf 0;
|
||||
Mu 1.84e-05;
|
||||
Pr 0.7;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -17,7 +17,15 @@ FoamFile
|
||||
|
||||
thermoType hPsiThermo<pureMixture<sutherlandTransport<specieThermo<hConstThermo<perfectGas>>>>>;
|
||||
|
||||
mixture air 1 28.9 1007 0 1.4792e-06 116;
|
||||
mixture
|
||||
{
|
||||
nMoles 1;
|
||||
molWeight 28.9;
|
||||
Cp 1007;
|
||||
Hf 0;
|
||||
As 1.4792e-06;
|
||||
Ts 116;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -17,7 +17,15 @@ FoamFile
|
||||
|
||||
thermoType hPsiThermo<pureMixture<sutherlandTransport<specieThermo<hConstThermo<perfectGas>>>>>;
|
||||
|
||||
mixture air 1 28.9 1007 0 1.4792e-06 116;
|
||||
mixture
|
||||
{
|
||||
nMoles 1;
|
||||
molWeight 28.9;
|
||||
Cp 1007;
|
||||
Hf 0;
|
||||
As 1.4792e-06;
|
||||
Ts 116;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
|
||||
@ -1,22 +1,28 @@
|
||||
species
|
||||
6
|
||||
(
|
||||
N2
|
||||
O2
|
||||
CH4
|
||||
H2
|
||||
CO2
|
||||
H2O
|
||||
)
|
||||
;
|
||||
N2
|
||||
O2
|
||||
CH4
|
||||
H2
|
||||
CO2
|
||||
H2O
|
||||
);
|
||||
|
||||
reactions
|
||||
2
|
||||
(
|
||||
irreversibleArrheniusReaction
|
||||
CH4 + 2O2^1.0 = CO2 + 2H2O^1.0
|
||||
(7e+06 0 10063.8)
|
||||
irreversibleArrheniusReaction
|
||||
H2 + 0.5O2^1.0 = H2O
|
||||
(4.74342e+12 0 10063.8)
|
||||
);
|
||||
{
|
||||
irreversibleArrheniusReaction
|
||||
{
|
||||
reaction "CH4 + 2O2^1.0 = CO2 + 2H2O^1.0";
|
||||
A 7e+06;
|
||||
beta 0;
|
||||
Ta 10063.8;
|
||||
}
|
||||
irreversibleArrheniusReaction
|
||||
{
|
||||
reaction "H2 + 0.5O2^1.0 = H2O";
|
||||
A 4.74342e+12;
|
||||
beta 0;
|
||||
Ta 10063.8;
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
@ -32,7 +32,10 @@ liquids
|
||||
H2O
|
||||
);
|
||||
|
||||
H2O H2O defaultCoeffs;
|
||||
H2O
|
||||
{
|
||||
defaultCoeffs yes;
|
||||
}
|
||||
}
|
||||
|
||||
solids
|
||||
@ -43,8 +46,14 @@ solids
|
||||
ash
|
||||
);
|
||||
|
||||
C C defaultCoeffs;
|
||||
ash ash defaultCoeffs;
|
||||
C
|
||||
{
|
||||
defaultCoeffs yes;
|
||||
}
|
||||
ash
|
||||
{
|
||||
defaultCoeffs yes;
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
|
||||
@ -5,5 +5,5 @@ species
|
||||
);
|
||||
|
||||
reactions
|
||||
(
|
||||
);
|
||||
{}
|
||||
|
||||
|
||||
@ -32,7 +32,10 @@ liquids
|
||||
H2O
|
||||
);
|
||||
|
||||
H2O H2O defaultCoeffs;
|
||||
H2O
|
||||
{
|
||||
defaultCoeffs yes;
|
||||
}
|
||||
}
|
||||
|
||||
solids
|
||||
|
||||
@ -5,5 +5,5 @@ species
|
||||
);
|
||||
|
||||
reactions
|
||||
(
|
||||
);
|
||||
{}
|
||||
|
||||
|
||||
@ -1,5 +1,9 @@
|
||||
(
|
||||
N2 N2 1 28.0134
|
||||
N2
|
||||
{
|
||||
nMoles 1;
|
||||
molWeight 28.0134;
|
||||
Hf 0;
|
||||
Sf 0;
|
||||
rhoPolynomial
|
||||
(
|
||||
3.8936E+00
|
||||
@ -10,9 +14,7 @@ N2 N2 1 28.0134
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
0.0 // Heat of formation
|
||||
0.0 // Standard entropy
|
||||
);
|
||||
cpPolynomial
|
||||
(
|
||||
9.7908E+02
|
||||
@ -23,7 +25,7 @@ N2 N2 1 28.0134
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
);
|
||||
muPolynomial
|
||||
(
|
||||
1.5068E-06
|
||||
@ -34,7 +36,7 @@ N2 N2 1 28.0134
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
);
|
||||
kappaPolynomial
|
||||
(
|
||||
3.1494E-03
|
||||
@ -45,55 +47,16 @@ N2 N2 1 28.0134
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
O2 O2 1 31.9988
|
||||
rhoPolynomial
|
||||
(
|
||||
4.4475E+00
|
||||
-1.8805E-02
|
||||
3.6667E-05
|
||||
-3.3323E-08
|
||||
1.1410E-11
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
0.0 // Heat of formation
|
||||
0.0 // Standard entropy
|
||||
cpPolynomial
|
||||
(
|
||||
8.3484E+02
|
||||
2.9297E-01
|
||||
-1.4959E-04
|
||||
3.4143E-07
|
||||
-2.2786E-10
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
muPolynomial
|
||||
(
|
||||
1.5068E-06
|
||||
6.1598E-08
|
||||
-1.8188E-11
|
||||
0
|
||||
0
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
kappaPolynomial
|
||||
(
|
||||
1.6082E-04
|
||||
8.5301E-05
|
||||
-1.4998E-08
|
||||
0
|
||||
0
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
H2O H2O 1 18.0153
|
||||
);
|
||||
}
|
||||
|
||||
|
||||
H2O
|
||||
{
|
||||
nMoles 1;
|
||||
molWeight 18.0153;
|
||||
Hf -1.3423e07;
|
||||
Sf 1.0482e04;
|
||||
rhoPolynomial
|
||||
(
|
||||
2.5039E+00
|
||||
@ -104,9 +67,7 @@ H2O H2O 1 18.0153
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
-1.3423e07 // Heat of formation [J/kg]
|
||||
1.0482e04 // Standard entropy [J/kg/K]
|
||||
);
|
||||
cpPolynomial
|
||||
(
|
||||
1.5631E+03
|
||||
@ -117,7 +78,7 @@ H2O H2O 1 18.0153
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
);
|
||||
muPolynomial
|
||||
(
|
||||
1.5068E-06
|
||||
@ -128,7 +89,7 @@ H2O H2O 1 18.0153
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
);
|
||||
kappaPolynomial
|
||||
(
|
||||
3.7972E-03
|
||||
@ -139,8 +100,16 @@ H2O H2O 1 18.0153
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
air air 1 28.85
|
||||
);
|
||||
}
|
||||
|
||||
|
||||
air
|
||||
{
|
||||
nMoles 1;
|
||||
molWeight 28.85;
|
||||
Hf 0.0;
|
||||
Sf 0.0;
|
||||
rhoPolynomial
|
||||
(
|
||||
4.0097E+00
|
||||
@ -151,9 +120,7 @@ air air 1 28.85
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
0.0
|
||||
0.0
|
||||
);
|
||||
cpPolynomial
|
||||
(
|
||||
9.4876E+02
|
||||
@ -164,7 +131,7 @@ air air 1 28.85
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
);
|
||||
muPolynomial
|
||||
(
|
||||
1.5061E-06
|
||||
@ -175,7 +142,7 @@ air air 1 28.85
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
);
|
||||
kappaPolynomial
|
||||
(
|
||||
2.5219E-03
|
||||
@ -186,6 +153,6 @@ air air 1 28.85
|
||||
0
|
||||
0
|
||||
0
|
||||
)
|
||||
)
|
||||
);
|
||||
}
|
||||
|
||||
|
||||
@ -32,7 +32,10 @@ liquids
|
||||
H2O
|
||||
);
|
||||
|
||||
H2O H2O defaultCoeffs;
|
||||
H2O
|
||||
{
|
||||
defaultCoeffs yes;
|
||||
}
|
||||
}
|
||||
|
||||
solids
|
||||
|
||||
@ -32,7 +32,10 @@ liquids
|
||||
H2O
|
||||
);
|
||||
|
||||
H2O H2O defaultCoeffs;
|
||||
H2O
|
||||
{
|
||||
defaultCoeffs yes;
|
||||
}
|
||||
}
|
||||
|
||||
solids
|
||||
|
||||
Reference in New Issue
Block a user