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cell reynolds number
Posted 12.07.2010, 06:04 GMT-4 1 Reply
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Hi there,
i'm using weakly compressible NS with heat transfer (transient). The flow is buoyancy-driven through heating.
I "experienced", that the temperature distribution, which i'm focussed on, depends on the mesh size in the domain where convection is active (+- 15K at 1000K. This is really annoying me. In this case refining the mesh causes higher temperatures. Further refinement has only little influence. So I don't know what is my criteria for knowing that the flow is modeled correctly.
I always look at the cell reynolds number, to be sure, that the flow is locally laminar. But I don't know if there exists a limit for the local Re-Number. cellRe<30? Using the GLS stabilization is needed for Re>2 for convergence. But is there any thumb rule for knowing: The boundary layer is correctly modeled within an error of about 1% (or 5% or whatever)? or things like that? What is your criteria for meshing flow domains? Your experience?
Thanks in advance!
i'm using weakly compressible NS with heat transfer (transient). The flow is buoyancy-driven through heating.
I "experienced", that the temperature distribution, which i'm focussed on, depends on the mesh size in the domain where convection is active (+- 15K at 1000K. This is really annoying me. In this case refining the mesh causes higher temperatures. Further refinement has only little influence. So I don't know what is my criteria for knowing that the flow is modeled correctly.
I always look at the cell reynolds number, to be sure, that the flow is locally laminar. But I don't know if there exists a limit for the local Re-Number. cellRe<30? Using the GLS stabilization is needed for Re>2 for convergence. But is there any thumb rule for knowing: The boundary layer is correctly modeled within an error of about 1% (or 5% or whatever)? or things like that? What is your criteria for meshing flow domains? Your experience?
Thanks in advance!
1 Reply Last Post 12.07.2010, 08:28 GMT-4