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Residual Curves & Convergence in Combustion Modeling |
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September 25, 2016, 01:50 |
Residual Curves & Convergence in Combustion Modeling
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#1 |
New Member
eydad
Join Date: Jan 2014
Posts: 5
Rep Power: 12 |
Hi guys;
I am modeling a non-premixed industrial combustion by ANSYS Fluent 17. I am using Species-Non-Premixed PDF Model+DOI method for radiation. I maintained default values of all under relaxation factors except following factors which I decreased them 0.05 to decrease resonances in my residual diagram: Turbulent Viscosity, Energy, Temperature, Discrete Ordinates, Mean Mixture Fractions, Mixture Fraction Variance. Here is my residual curve: As you see there is no change in factors (except DOI curve). When can I consider my solution as finalized solution? ------------------------------------------------------------------------------------ 2nd Question: Consider a furnace which is empty and its burner is working in high-fire. Is it possible for temperature of furnace to increase equal or even higher than adiabatic flame temperature (AFT)? Last edited by Muh.Hesan; September 25, 2016 at 03:07. |
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October 2, 2016, 07:04 |
Please . . .
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#2 |
New Member
eydad
Join Date: Jan 2014
Posts: 5
Rep Power: 12 |
Anybody? . . .
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Tags |
ansys, combustion, fluent, pdf |
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