-
-
February 2, 2024 at 5:08 amMohamed RamonSubscriber
-
February 2, 2024 at 10:51 amCFD_FriendAnsys Employee
Hi Mohammed,
Can you give a decription to your problem. For some reason I can only see the title (Fluid Flow).
Thanks
-
February 2, 2024 at 1:04 pmMohamed RamonSubscriber
its a simple internal flow inside a pipe. Air flow inside a 0.1 m diamete pipe with about 5 m/s velocity.
Â
-
-
February 2, 2024 at 1:26 pmRobForum Moderator
Have you done the courses in the Learning section on here?Â
-
February 2, 2024 at 1:37 pmMohamed RamonSubscriber
you can give me the link. On the other side, I finished some other courses and working with fluent several years ago and still have the same question. Why i have to set the flow as turbulan or laminar. For example if i have a 0.1 m pipe with internal air flow with 5 m/s velocity, this case according to reynolds numper should me a turbulant flow therefore, asnys should work as that withot asking me. But if i set it as laminar flow, will force the flow to be laminar other than reality !!
-
February 2, 2024 at 1:56 pmRobForum Moderator
/courses/index.php/fluids/
Look at the turbulence question in another way. Why wouldn't you set a turbulence model given you need to decide what you need in your model.Â
-
February 4, 2024 at 5:14 amMohamed RamonSubscriber
I got it but in this case which it's a turbulant flow in real, if i simulate it as laminar flow, how can i accept the laminar result. Would it be false in this case or illogical?
-
February 5, 2024 at 10:06 amRobForum Moderator
There's a theory that if the mesh is fine enough, and the time step small enough that a laminar flow will pick up the turbulent eddies as part of the result. Given the mesh cell count would be near infinity and the run duration would be rather long I'm not sure we'll ever find out.Â
Being slightly more realistic, the result would probably not converge well, and may not be overly accurate. Try running laminar and then turbulent and compare the results.Â
-
- The topic ‘Fluid flow’ is closed to new replies.
- Non-Intersected faces found for matching interface periodic-walls
- Unburnt Hydrocarbons contour in ANSYS FORTE for sector mesh
- Help: About the expression of turbulent viscosity in Realizable k-e model
- Cyclone (Stairmand) simulation using RSM
- error udf
- Diesel with Ammonia/Hydrogen blend combustion
- Fluent fails with Intel MPI protocol on 2 nodes
- Mass Conservation Issue in Methane Pyrolysis Shock Tube Simulation
- Script error Code: 800a000d
- Encountering Error in Heterogeneous Surface Reaction
-
1191
-
513
-
488
-
225
-
209
© 2024 Copyright ANSYS, Inc. All rights reserved.