Search found 284 matches
- Mon Apr 22, 2024 1:49 pm
- Forum: code_saturne usage
- Topic: Mixture multiphase model
- Replies: 7
- Views: 67519
Re: Mixture multiphase model
Hello Daniele, You are correct, I want to solve a dispersed phase inside a continuous one. At the moment I use the core of the VOF implementation to modify the physical properties (density, viscosity, Cp) as a function of the void fraction. Also, I change/remove the interface-capturing model and the...
- Fri Apr 19, 2024 2:42 pm
- Forum: code_saturne usage
- Topic: meshing criteria
- Replies: 4
- Views: 3101
Re: meshing criteria
Hello,
This type of mesh can be done with Salome using the Viscous Layer Hypothesis.
Here you have a link to examples and docs.
https://docs.salome-platform.org/latest ... eshes.html
Regards,
Luciano
This type of mesh can be done with Salome using the Viscous Layer Hypothesis.
Here you have a link to examples and docs.
https://docs.salome-platform.org/latest ... eshes.html
Regards,
Luciano
- Tue Apr 16, 2024 1:14 pm
- Forum: code_saturne usage
- Topic: meshing criteria
- Replies: 4
- Views: 3101
Re: meshing criteria
Hello, As Yvan mentioned in the previous post, it seems to be a problem with overlapping boundary zones. Anyways, the quality criteria of the "tablierbeton1.med" tetrahedral mesh is not good and you should improve it. The Mesh_5 is a better quality mesh, but you have to fix some issues in ...
- Thu Apr 11, 2024 2:33 pm
- Forum: code_saturne usage
- Topic: Mixture multiphase model
- Replies: 7
- Views: 67519
Re: Mixture multiphase model
Thank you very much Daniele, for your answer on this topic. My first attempt was to use the solution that you mentioned, but in my case, I have a mass transfer between phases, similar to a boiling or cavitation process. It is not clear why you mention that it "will not be possible with the spac...
- Fri Jan 19, 2024 7:20 pm
- Forum: code_saturne usage
- Topic: Mixture multiphase model
- Replies: 7
- Views: 67519
Re: Mixture multiphase model
Ok Yvan,
Thank you for your answer.
I will wait for any recommendations.
Best regards,
Luciano
Thank you for your answer.
I will wait for any recommendations.
Best regards,
Luciano
- Wed Dec 20, 2023 3:42 pm
- Forum: code_saturne usage
- Topic: Mixture multiphase model
- Replies: 7
- Views: 67519
Mixture multiphase model
Hello, I have a question regarding utilizing CS to solve multiphase flows using a mixture model. In fact, CS can solve multiphase flows using VOF, an interface-capturing model that combines some highly compressive NVD scheme with a artificial drift flux (cs_vof_deshpande_drift_flux) to compress the ...
- Wed Oct 26, 2022 5:33 pm
- Forum: code_saturne usage
- Topic: Pressure drop in long pipe
- Replies: 8
- Views: 9382
Re: Pressure drop in long pipe
Hello,
Did you use the same mesh in CFX and CS?
Regards,
Luciano
Did you use the same mesh in CFX and CS?
Regards,
Luciano
- Mon Oct 03, 2022 1:09 pm
- Forum: code_saturne usage
- Topic: Venturi pipe flow VOF convergence issue
- Replies: 6
- Views: 10981
Re: Venturi pipe flow VOF convergence issue
Hello Luciano and Yvan, @ Luciano: thank you for the update. I set the upwind scheme for velocity only and the simulation was running without interruptions. My question is: did you use that Scheme in your simulations or it is just a workaround for me? The results of the previous post was with the s...
- Mon Oct 03, 2022 3:48 am
- Forum: code_saturne usage
- Topic: Tube heat enchange
- Replies: 12
- Views: 14951
Re: Tube heat enchange
Hello, To have rough wall option, you have to set a turbulence model and also a wall function, for default no wall function is used, soy the rough wall option is in gray. But I have no option rough wall even if I tick turbulence. Attached is the case (The mesh correspond to the first post and should...
- Mon Oct 03, 2022 3:24 am
- Forum: code_saturne usage
- Topic: Venturi pipe flow VOF convergence issue
- Replies: 6
- Views: 10981
Re: Venturi pipe flow VOF convergence issue
Hello, 1) if I run the simulation with the Time Step Option = "Constant" (and reference time step = 0.0002 as suggested) the simulation stacks because of an excess of fluid speed. Did you face the same issue? No, but in your setup all the numerical scheme where in automatic, you can try to...