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May 11, 2017, 16:53 |
How to simulate a flow in a 3D Pipe
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#1 |
New Member
Changli Han
Join Date: May 2017
Posts: 3
Rep Power: 9 |
1.I get scenario with a 3D pipe with a diameter of 5 meters, and with a length of 200 meters, also its bended shape in space likes a snake. I only know the water velocity inside of pipe is around 0.18m/s(at least at the entrance), no information about the pressure. How should I set the boundary conditions regarding the velocity, and also the pressure. Totally no clue about what the zeroGradient thing is doing.
2.And also want to know if I set the inlet velocity using the surfaceNormalFixedValue, how should I set the inlet pressure together with the outlet's velocity and outlet's pressure? |
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May 12, 2017, 01:23 |
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#2 |
Senior Member
Uwe Pilz
Join Date: Feb 2017
Location: Leipzig, Germany
Posts: 744
Rep Power: 15 |
I recommend to set
inlet: - U: fixed value, your velocity - p: zerogradient outlet: - U: zero gradient - p: fixed value 0 (reference pressure) wall: - U: uniform (0 0 0 ) - p: zero gradient Depending on your model you need boundary conditions for the auxiliary values like k, epsilon or omega and/or others. Beside this I recommend to avoid 3D at least in the first step. Use the cylinder symmetry instead. You have to mesh a 5° slice which is 1 element wide. Use the wedge boundary conditions at the free sides.
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Uwe Pilz -- Die der Hauptbewegung überlagerte Schwankungsbewegung ist in ihren Einzelheiten so hoffnungslos kompliziert, daß ihre theoretische Berechnung aussichtslos erscheint. (Hermann Schlichting, 1950) |
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May 31, 2017, 17:44 |
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#3 |
New Member
Changli Han
Join Date: May 2017
Posts: 3
Rep Power: 9 |
Thank you for your suggestions, everything works fine with laminar case, and right now I need to consider some cases with turbulence model like k-w SST model. Then how should I set the boundary conditions in this case? Usually what kind of values can be used as default? And also I want to ask which turbulence model are the most common in reality? Is it k-w SST? Looking forward for your reply!
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June 1, 2017, 07:38 |
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#4 |
Senior Member
Uwe Pilz
Join Date: Feb 2017
Location: Leipzig, Germany
Posts: 744
Rep Power: 15 |
After "laminar" the next step is RANS. There are two models wide accepted: k-epsilon and k-omega.
I recommend to start with k-epsilon which is easier to understand and to implement (you don't need to implement it, it is ready available). It si numerical stable and does not lean toward instability. k-omega has advantages in mixed flow (steep pressure gradients) where laminar and fully turbulent regions of the flow are in one model. k-omega tends to overestimate the turbulence form my experience. All in all k-epsilon gives a better solution far away from the walls, where k-omega is too turbulent. k-omega gives a better answer in the Prandtl layer and describes the evolution of turbulence better. I am sure there exist more advanced models, which try to combine pros and cons. In most cases they are not as universal applicable as k-epsilon and k-omega.
__________________
Uwe Pilz -- Die der Hauptbewegung überlagerte Schwankungsbewegung ist in ihren Einzelheiten so hoffnungslos kompliziert, daß ihre theoretische Berechnung aussichtslos erscheint. (Hermann Schlichting, 1950) |
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June 2, 2017, 05:04 |
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#5 |
New Member
Changli Han
Join Date: May 2017
Posts: 3
Rep Power: 9 |
why the next step is to have transient + k-epsilon instead of steady + k-epislon? And can I consider I do steady + k-epislon then we get the mean field directly?
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Tags |
pipe, pressure, setting, velocity |
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