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MoDeNa
1.0
Software framework facilitating sequential multi-scale modelling
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MoDeNa
1.0
Software framework facilitating sequential multi-scale modelling
|
All the experimental data required for the source terms calculations. More...
Go to the source code of this file.
Variables | |
| double | Pr = 101325.0 |
| initial/final pressure of the mixture, Pa | |
| double | Temp0 = 297 |
| initial temperature, K | |
| double | A_OH = 1965.0 |
| pre-exponential factor for the gelling reaction, 1/s | |
| double | E_OH = 5.487e4 |
| activation energy for the gelling reaction, J/mol | |
| double | OH_0 = 3765.0 |
| Initial concentration of polyol OH groups in the mixutre, mol/m3. | |
| double | NCO_0 = 3765.0 |
| Initial concentration of isocianate NCO groups in the mixutre, mol/m3. | |
| double | W_0 = -1.0 |
| Initial concentration of water in the mixture, mol/m3. | |
| double | catalyst |
| double | polyol1_ini |
| double | polyol2_ini |
| double | amine_ini |
| double | isocyanate1_ini |
| double | isocyanate2_ini |
| double | isocyanate3_ini |
| double | A_W = 1.385e3 |
| pre-exponential factor for the blowing reaction, 1/s | |
| double | E_W = 3.266e4 |
| activation energy for the blowing reaction, J/mol | |
| double | RR = 8.3145 |
| ideal gas constant, J/mol K | |
| double | rhoPoly = 1100.0 |
| density of the liquid polymer, kg/m3 | |
| double | rhoBL = 1467.0 |
| density of the blowing agent, kg/m3 | |
| double | DH_OH = -7.49e4 |
| Reaction heat for the gelling reaction, J/mol. | |
| double | DH_W = -8.6e4 |
| Reaction heat for the blowing reaction, J/mol. | |
| double | C_Poly = 1800.0 |
| double | C_CO2 = 836.6 |
| CO2 specific heat, J/kg K. | |
| double | C_BG = 593.0 |
| Specific heat of the physical blowing agent in gas phase, J/kg K. | |
| double | C_BL = 870.0 |
| Specific heat of the physical blowing agent in liquid phase, J/kg K. | |
| double | lambda = 2.0e5 |
| Latent heat of blowing agent, J/kg. | |
| double | C_TOT |
| Total specifc heat of the mixture. | |
| int | phBL = 1 |
| type of physical blowing agent 1 = pentane, 2 = R-11 | |
| int | denMod |
| density mode, 1 = modena, 2 = constant | |
| int | kinMod = 2 |
| kinetics model, 1 = Baser, 2 = Baser with R(x) More... | |
| bool | dilution = true |
| use dilution effect | |
| double | X_gel |
| double | M_CO2 = 44.0 |
| Molecular mass of carbon dioxide, kg/kmol. | |
| double | M_B = 137.37 |
| Molecular mass of blowing agent, kg/kmol. | |
| double | M_NCO = 615.0 |
| Molecular weight of NCO, kg/kmol. | |
| double | M_air = 29.0 |
| Molecular weight of air, kg/kmol. | |
| double | L0 = 0.155 |
| Initial weight fraction of blowing agent in the liquid, -. | |
| double | CO2_0 = 0.0 |
| Initial weight fraction of CO2 in the liquid, -. | |
| double | surfaceTension = 25e-3 |
| required for the computation of partial pressure | |
| double | sig = 1e-1 |
| correlated to variance of initial distribution | |
| double | init_size = 2.0e-6 |
| initial mean bubble diameter, m | |
| double | NN = 0.138e12 |
| correlated to number of initial bubbles in m^3 | |
| double | air_g |
| air weight fraction | |
| double | abs_err = 1e-6 |
| absolute error | |
| double | rel_err = 1e-6 |
| relative error | |
| double | dt = 1e0 |
| time step, s | |
| double | tend = 200 |
| end time, s | |
| bool | realizabilityCheck = false |
| std::string | bubbleMode |
| bool | apparentViscosity |
All the experimental data required for the source terms calculations.
Definition in file experimentalInputs.h.
| int kinMod = 2 |
kinetics model, 1 = Baser, 2 = Baser with R(x)
Definition at line 125 of file experimentalInputs.h.
1.8.13