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Combustion: species mass fraction's boundary conditions |
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November 20, 2014, 04:36 |
Combustion: species mass fraction's boundary conditions
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#1 | |
Senior Member
Freedom
Join Date: May 2014
Posts: 209
Rep Power: 13 |
Hello,everyone.
Now i'm confused with the bc's settings. Yes, I did get some idea with the pressure,velocity boundary conditions' setting. But now i simulate the coal combustion using coalChemistryFoam, and i have 5 species----CH4,CO2,O2,H2O,N2.So i should give the initial boundary conditions about all of the five species! Yes, the mass fraction of CH4, N2,O2 we already know and the max mass fraction of the products(CO2,H2O) we can also calculate. But how can we set the initial bc for the products(CO2,H2O) in the 0 folder of the boundaryField? PS:my idea:
fieldMinMax minmaxdomain output: Quote:
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November 20, 2014, 06:01 |
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#2 |
Member
Artem Shaklein
Join Date: Feb 2010
Location: Russia, Izhevsk
Posts: 43
Rep Power: 16 |
Hello, wenxu.
You should set mass fractions of products in the following way (according to OpenFOAM syntax): initialValue uniform 0; inlet: fixedValue uniform 0; walls: zeroGradient; outlet: you can go with zeroGradient, but I prefer in a case with reverse flow type inletOutlet; inletValue uniform 0; value uniform 0; its mathematical description is: if outflow if inflow All this is according to physics: products can be generated inside a computational domain by chemistry (the source term in the transport equation), but not by flowing through boundaries (the convection and diffusion terms in the transport equation). |
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November 20, 2014, 07:55 |
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#3 |
Senior Member
Freedom
Join Date: May 2014
Posts: 209
Rep Power: 13 |
Thank you,Artem. Your answer is so clearly and powerful.I got that.regards,
wen |
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