Mutiphase_Eulerian_Eulerain_porous media
Hi Arturo,
I'm stuck at a packed bed simulation in Fluent. The packed bed model is represented by air/water streams in porous media in Eulerian framework. I aim at my model to predict pressure drop and liquid volume fraction in the bed. Kindly let me know, 1) Is viscous resistance needs to be entered for both phase? I've calculated this resistance (1/m2) by Ergun Equation for single phase. But how do we account for two phase here? I've used "Schiller Naumann" drag law to calculate "interphase coupling" considering 5 mm water bubble dia. Do you feel it necessary to introduce two momentum source terms instead of entering viscous/inertial resistance? A technical reply will be highly appreciated. Regards, SM Quote:
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FLUENT Eulerian packed bed model can be seen as a three-phase Euler-Euler model, where one phase has zero velocity, and represents the porous zone. This makes things a bit easier, since you automatically have sum(vol. Fraction) = 1.
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fluent_porous media_packed_bed
Hi Alberto,
Thanks for your reply. I've implemented 3 phase E-E model in Fluent, patching solid phase with constant packing factor 0.63 in the computational domain. But this 3 phase strategy is really computationally expensive and time consuming. All I'm looking at is replacing the solid phase with "porous media" incorporating the suitable momentum sink terms in 2 phase E-E simulation. This saves time yet gives reasonable accuracy. Any technical suggestion is more than welcome. Regards, SM Quote:
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I don't see why it is so much more computationally expensive of the two-phase simulation you have to run anyway, since you are not solving for the particle phase (it has constant zero velocity and constant volume fraction). The proper momentum sink is given by the drag coefficient, which should be based on the Ergun law for the phase pairs involving the porous zone.
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Hi everyone,
I'm trying simulation porous media in rectangular channel, but the result isn't suitable with any research. So, would you help me. I wish someone can check my simulation and give some reports if there is something wrong. Thank you for your help. Please send your e-mail, than i will send you my works to to your email. my e-mail: oky.andytya.net@gmail.com Regrads, OKY Andytya P note: I use ANSYS Fluent 6.3 [CFD] |
Oky,
1E+06 $ please |
To: Dr. Alexander VAKHRUSHEV
I have been visited the website and make some contact. Theres is a problem with the address. Would you like give your personal e-mail / website, because it's very helpfull. Tjanh you. Regrads Oky Andytya oky.andytya.net@gmail.com |
help in modeling compressible flow through porous media with heat transfer
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Hi Hrv, I was looking for some help in modeling compressible flow in porous media, and to me you seem to be a senior member in this field. i would appreciate any help in this regard, if it does distract you from your schedule, I would understand, In my problem I hava a vertical cylindrical domain and the complete domain is filled with porous media of porosity 0.6. Air inters to the domain at a velocity of 0.3 Mach no. and temp of 1000 degree centigrade, through 18 thin pipes mounted circumferentially at the side. and Air comes out from the top of the cylinder after passing through the porous media. Actually I was facing problem in definig a porous zone on a tetrahedral mesh which I imported to discretize-setup as a *.stl import from star-CD mesh file. Also the imported mesh shows an extra patch "patch0", which has 0 face, and the rhoPorousSimpleFoam solver complains about this patch 0, and gives fatal error. Please help me in getting some way to overcome this error. Also I would be grateful if you could suggest a solver for such kind of problems. Regards, MLD |
Hi, everyone
How to get the value of convection coefficient [h] from Fluent directly ?? Regrads, Oky |
chemical reaction into porous media openfoam
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Thank you in advance |
Have you checked porousSimpleFoam?
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yeah but there is not chemical reaction in porousSimpleFoam
how can i modify |
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