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June 5, 2001, 09:35 |
Porous Media
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#1 |
Guest
Posts: n/a
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Hi!
How does Fluent 5 deal with flow through porous media? I am worried that when I set up a porous zone, Fluent only sets resistances which I can relate from the Ergun equations, but not the true porosity. I have chemical reactions so I need the superficial velocity to be taken into account. Can anybody help me please? |
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June 12, 2001, 07:14 |
Re: Porous Media
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#2 |
Guest
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Hi again!
As nobody has answered me, does that mean I cannot do what I wish to do? Can somebody from Fluent help me? Isa |
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June 12, 2001, 13:27 |
Re: Porous Media
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#3 |
Guest
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I don't fully your question but this topic has been already discused in this forum, please search for answers.
Anyway, fluent accounts for the porous media by using a sink term as you suggests so, the liquid never "touches" the solid and the velocity is constant and you cannot model the liquid-solid drag forces. You can approximate by using vinst=vsup/epsilon ( vinst=interstitial velocity, vsup=superficial velocity, epsilon=porosity) If you want to account for other phenomena aside the porosity you must use another approach such as some modification of the kozeni-carman equation if you are in the laminar regime. cheers. Newbie |
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