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Free Surface Modelling and Reversed Flow Error |
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August 10, 2004, 12:43 |
Free Surface Modelling and Reversed Flow Error
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#1 |
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Hi, I'm a new user of Fluent. i'm trying to model a 2d rectangular tank with a free surface. I have read that the VOF model is used for tracking a free-surface, but that is not my case. I have used a pressure outlet boundary condition in the top of the tank, but an error appears showing that there is reversed flow in a given number of faces. I have read that the apropriate boundary condition to be used is a symetry boundary.
Does Anyone know why, and if is this correct? Thanks in advance Javier |
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August 11, 2004, 08:23 |
Re: Free Surface Modelling and Reversed Flow Error
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#2 |
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What type of flow are you modelising? Where are the inlet and the outlet? I am currently doing the same (tank, VOF..) with a velocity inlet and a pressure outlet for the vertical sides, and symmetry for the top and the bottom. It works, so I could help you if it was the same...
Raphael |
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August 11, 2004, 16:30 |
Re: Free Surface Modelling and Reversed Flow Error
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#3 |
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The inlets and aoutlets are microjets placed at the bottom. The top of the tank is the free surface. I try the symetry boundary at the top and it works good, but i will try with VOF to see how it is altered.
Thanks for your help, and feel free to email me for anything related to the modelation. Best regards. Javier |
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August 13, 2004, 13:53 |
Re: Free Surface Modelling and Reversed Flow Error
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#4 |
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Have you ticked the box "specified operating density" in the operating conditions panel? I had problems with hydrostatic pressure in the light phase, above the surface, with important pressure variations, and a disturbace of the flow. As soon as I ticked this box, problems were solved, and hydrostatic pressure was OK.
Hope this helps. Raphael |
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August 16, 2004, 12:37 |
Re: Free Surface Modelling and Reversed Flow Error
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#5 |
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Yes, I have done that, But now appears another error when i'm running the VOF. It says:
"Turbulent Viscosity limited to turbulent viscosity ratio of 1.000000e+05 in 8 cells" In the plot of the residuals one can see how the grow in time (not all, but someones). I had to change the pressure inlet zone type for the upper boundary to a symmetry boundary to avoid the reversed flow error. I have reduced the under-relaxation factors for al ecuations. But I can't control the break down of the model. Best Regards, Javier. |
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