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October 23, 2000, 12:23 |
3D,Solid-Liquid simulation in stirred tank
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#1 |
Guest
Posts: n/a
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Hi friends,
I am new in CFD but I am working with 3D simulation of mixing-tank bioreactor with 2 phases involved for the moment(water as fluid and beads as solid and the initial solid vol fraction is about 0.3)(3-phase simulation are waiting to be solved afterward).My system have 2 radial impeller with no buffle. I used Eulerian(granular) multiphase model to investigate the suspension of beads(solid particles)by turn on the time-dependence option...... At first ,I run the simulation with Multi-reference frame(MRF). After getting the converged solution.....I check the average value of solid vol fraction....it appeared to be about zero( instead of about 0.3) which look weird. But,then, I find the limitations of the Eulerian Multiphase model that it cannot be used with sliding or deforming meshes.(from fluent user's guide vol.2 page9-5 ) My question is..... Is the fixed velocity( as an impeller model instead of MRF or sliding mesh) become the only way I can use to deal with my simulation ??....(according to limitation I mentioned) Any more suggestion are gladly welcome. Thank you in advance. Mike Thai's son |
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June 25, 2010, 10:23 |
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#2 |
New Member
Li Liu
Join Date: Nov 2009
Posts: 16
Rep Power: 0 |
Hi, i am also working on two phase simulation now (water and glass beads),I think u can use the SG method for your simulation,but using MFR can get you steady state result, if the volume fraction is 0 instead of 0.3 using MFR, maybe there is something wrong with other parameter setting, not due tot the MFR method?...
Hope you will figure it out... Lily |
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