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I was trying to model a fixed bed gasifier in cold condition. |
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January 20, 2012, 02:04
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I was trying to model a fixed bed gasifier in cold condition.
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#1 |
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New Member
Jay Prakash Srivastava
Join Date: May 2011
Location: INDIA
Posts: 1
Rep Power: 0  |
Details of the model are as under:
General Solver: Pressure- Based Velocity Formulation - Absolute Time- Steady Model: Eulerian, scheme- Implicit Viscous Model- K-Epsilon(2eqn), Realizable, Standard wall Function, Mixture Phase- Phase-1 AIR Phase-2 Carbon Solid Boundary Condition- Air Inlet Velo: 1 m/sec Coal Inlet : 0.5 m/sec Volume Fraction: 0.63 Pressure Velocity Coupling : Scheme : Multiphase Coupled Gradient: Green - Gauss Cell Based. But I was getting the volume fraction for phase 2 as 0. Please help me in this regard. |
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January 30, 2012, 10:45
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#2 |
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Senior Member
Join Date: May 2011
Posts: 231
Rep Power: 16 |
hi,
did you solve the problem...I am also doing solid-gas multiphase simulations circulating fluidized bed reactor using multiphaseEulerFoam in OpenFoam. I have similar problem.did you solve it? |
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Linear Mode
