|
[Sponsors] |
February 16, 2021, 13:52 |
Peak/Maximum Reynold's number
|
#1 |
New Member
-
Join Date: Oct 2020
Posts: 22
Rep Power: 5 |
Hi,
I am using CFD to compute the pressure and flow in 2D axisymmetric models of blood flow through a stenosis. In several papers I read the terms 'maximum Reynold's number' or 'peak Reynold's number'. In some papers these values are computed at the inlet of the model, while in other papers in the center of the stenosis. I would say that the latter one is better, but I am not sure why one would consider it at the inlet. I want to use this value of the Reynold's number to determine whether using a laminar model is justified or a transition/turbulence model must be used. More details on my CFD case: at the inlet a velocity is prescribed and the outlet is stress-free. A no slip condition is applied to wall and the model is rigid. So my question is: at which location can the peak/maximum Reynold's number best be determined? Thanks for your help! |
|
February 17, 2021, 04:36 |
|
#2 | |
Senior Member
Filippo Maria Denaro
Join Date: Jul 2010
Posts: 6,768
Rep Power: 71 |
Quote:
As you prescribed the velocity at the inlet, you have a known Re number for the inlet condition. In the interior, the local Re number depends on the flow conditions thus you cannot say the peak before having the solution. Some rude approximation could be obtained in terms of the averaged velocity using the continuity equation as Ainlet*v_av_i= Astenosis*v_av_s. That would allow to evaluate v_av_s Last edited by FMDenaro; February 17, 2021 at 12:56. |
||
February 17, 2021, 11:05 |
|
#3 |
New Member
-
Join Date: Oct 2020
Posts: 22
Rep Power: 5 |
Thanks Filippo, that answers my question!
|
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
[snappyHexMesh] snappyHexMesh sticking point | natty_king | OpenFOAM Meshing & Mesh Conversion | 11 | February 20, 2024 09:12 |
decomposePar no field transfert | Jeanp | OpenFOAM Pre-Processing | 3 | June 18, 2022 12:01 |
[Other] Equal decomposition of cylindrical fluid domain | Sean95 | OpenFOAM Meshing & Mesh Conversion | 3 | February 12, 2019 03:34 |
Cluster ID's not contiguous in compute-nodes domain. ??? | Shogan | FLUENT | 1 | May 28, 2014 15:03 |
decomposePar pointfield | flying | OpenFOAM Running, Solving & CFD | 28 | December 30, 2013 15:05 |