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July 14, 2020, 15:27 |
High Pressure and Turbulence
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#1 |
Member
Andy Robertson
Join Date: Mar 2009
Location: Long Island NY
Posts: 46
Rep Power: 17 |
Folks,
I have a high pressure device flowing air through a series of baffles. Working pressure around 2000psi I am using ideal gas law and Standard K-Epsilon. Max Mach number around 0.2 I am running into the TVR limiter almost everywhere. Mass and pressure seem well converged. But the turbulent viscosity field seems unrealistic. I would expect high values in the baffles themselves, but not in some of the low velocity regions. Is there a pressure dependency to the turbulent viscosity I am not understanding. IE should I just set the limiter an order (or two) of magnitude higher. Andy |
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July 15, 2020, 01:26 |
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#2 |
Senior Member
Chaotic Water
Join Date: Jul 2012
Location: Elgrin Fau
Posts: 435
Rep Power: 17 |
Might be coarse mesh.
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July 15, 2020, 12:07 |
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#3 |
Member
Andy Robertson
Join Date: Mar 2009
Location: Long Island NY
Posts: 46
Rep Power: 17 |
It may be a mesh density issue.
However, I am wondering if this is related to density through the normal stress. As I recall (and I may be a bit out of date here) Star's (and other's) implementation of K-E results in an unphysical turbulent viscosity in regions of high normal stress. And as the K term is per unit mass, and I have a high density (at least for a gas) so perhaps that overshoot due to normal stress is magnified. I am going to try increasing the mesh density a bit (have to keep the run time finite ;-) and perhaps shift to the realizable KE. Not a high swirl device but may even try RSM Any other thoughts out there? AndyR |
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