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Eulerian Multi-Phase Fluidized bed convergence |
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June 5, 2020, 06:16 |
Eulerian Multi-Phase Fluidized bed convergence
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#1 |
New Member
arif
Join Date: Jun 2017
Posts: 3
Rep Power: 9 |
I didn't take convergent results whatever i tried in eulerian multi-phase flow. Mesh quality is enough in terms of skewness and orthogonal qualities. I have problem about continuity eqn convergence. If any possible advice such as time step, under relaxation or scheme, i will be appreciated greatly.
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June 5, 2020, 07:39 |
Flow Description
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#2 |
Senior Member
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The description of your case is rather vague and very generic. Assuming the mesh is good, the problem could be in physical setup. Numerics, such as, URF or time-step would help only if the physical setup is correct. Otherwise, doesn't matter what time-step or URF you use, the case will keep on diverging. You need to share more details of the setup, such as, material properties, boundary conditions, phase interactions, etc.
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Regards, Vinerm PM to be used if and only if you do not want something to be shared publicly. PM is considered to be of the least priority. |
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June 5, 2020, 07:52 |
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#3 |
New Member
arif
Join Date: Jun 2017
Posts: 3
Rep Power: 9 |
Model: Eularian Granular Multi-Phase
Phases: Air and Sand Inlet B.C: Velocity Inlet Outlet: Pressure Outlet Wall: Specularity Coefficient as 0,6 Laminar 2-D Implicit phase coupled Pressure: Tried PRESTO and second order Volume Fraction: First Order Least Square based I tried initiliazation from fluent user guide tips Time Steps: 0,001, 0,0001, 0,00001 URF: I tried different urf for momentum and pressure. Not exact convergent results I tried variable time steps so i had floating point. I have always floating point exception after some iteration while changing time step. Geometry has conical section at the bottom. Drag Model: Gidaspow |
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June 5, 2020, 07:58 |
Flow
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#4 |
Senior Member
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Why is the flow laminar? Air cannot even move sand if laminar.
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Regards, Vinerm PM to be used if and only if you do not want something to be shared publicly. PM is considered to be of the least priority. |
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June 5, 2020, 08:04 |
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#5 |
New Member
arif
Join Date: Jun 2017
Posts: 3
Rep Power: 9 |
I tried turbulence and i had same error. There are a lots of laminar cases in multiphase simulation while simulating sand and air. But i will try again for turbulence.
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July 5, 2020, 12:33 |
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#6 | |
Member
George Corner
Join Date: Dec 2016
Posts: 30
Rep Power: 10 |
Hi,
apply k-epsilon model then follow the below procedures 1, 2 and 3: 1-model>multhiphase>phases>secondary phase (solid phase)> Diameter: [your desire size] granular viscosity: Gidespaw or syamlal O'brian granular bulk viscosity: lun et al. frictional voscosity: Schaefer Angle of internal friction: leave it by default frictional pressure: based-ktgf fractional modulus: derived frictional packing limit: by default granular temp: algebraic solid pressure: lun et al. radial distribution: lun et al. elasticity modulus: derived packing limit: 0.63 [packing limit can be increased or decreased by yourself. maximum packing limit can be 0.74 also. the high packing limit prevent particles to jump and leave the bed immediately] 2- model>multhiphase>phases>phase interaction> drag choose: Gidespow or syamlal O'brien. [if you choose Gidespow on granular viscosity then you must choose Gidespow for drag also. these two must be same] 3- solution methods scheme: phase couple simple gradient: least squred... momentum: second order upwind volume fraction: Quick turbuetn kinetoc: first order turbulent diss: first order transient formulation: second order implicit Good luck Quote:
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