-
-
September 19, 2018 at 3:07 am
tlcong
SubscriberHi, I read lots of papers on the topic of DNS and LES simulation. Most of the simulations are carried out for the Couette flow between two parallel plates with constant pressure gradient along the flow direction. The size of the computational domain is often determined by several times of half of the channel height between two plates (&delta
, such 2πδ*πδ*2δ. However, the absolute value of the δ is not given. Can anyone give some instruction on how to determine the value of δ.
-
September 19, 2018 at 7:39 am
raul.raghav
SubscriberUsually the non-dimensional friction Reynolds number is provided from which you can evaluate half of the distance between the plates (delta).
Re_tau = (u_tau * delta) / kin-visc
u_tau = sqrt (wall-shear/density)
-
September 19, 2018 at 8:51 am
paguado
Ansys EmployeeHi tlcong,
If δ is the channel height why should it be given? The important thing is to keep non-dimensional variables constant so that if you increase the channel height you have to increase the domain size. Of course your integral turbulent structures will be larger as you increase δ.
-
September 20, 2018 at 9:57 am
tlcong
SubscriberDifferent δ with same u_tau and and Re_tau will lead to different Reynolds number based on the bulk velocity(Re_bulk). We need to determine the Re_bulk with given δ. However, for most cases, the δ is not given. Is there anyway to determine it? Or there is conventional values for the δ in DNS simulation?
-
September 20, 2018 at 10:00 am
tlcong
Subscriber
Usually the non-dimensional friction Reynolds number is provided from which you can evaluate half of the distance between the plates (delta).
Re_tau = (u_tau * delta) / kin-visc
u_tau = sqrt (wall-shear/density)
However, the wall-shear stress is unknown in the simulation. (only Re_tau is given in the publications)
-
- You must be logged in to reply to this topic.

Boost Ansys Fluent Simulations with AWS
Computational Fluid Dynamics (CFD) helps engineers design products in which the flow of fluid components is a significant challenge. These different use cases often require large complex models to solve on a traditional workstation. Click here to join this event to learn how to leverage Ansys Fluids on the cloud, thanks to Ansys Gateway powered by AWS.

Earth Rescue – An Ansys Online Series
The climate crisis is here. But so is the human ingenuity to fight it. Earth Rescue reveals what visionary companies are doing today to engineer radical new ideas in the fight against climate change. Click here to watch the first episode.

Ansys Blog
Subscribe to the Ansys Blog to get great new content about the power of simulation delivered right to your email on a weekly basis. With content from Ansys experts, partners and customers you will learn about product development advances, thought leadership and trends and tips to better use Ansys tools. Sign up here.
- Suppress Fluent to open with GUI while performing in journal file
- Floating point exception in Fluent
- What are the differences between CFX and Fluent?
- Heat transfer coefficient
- Getting graph and tabular data from result in workbench mechanical
- The solver failed with a non-zero exit code of : 2
- Difference between K-epsilon and K-omega Turbulence Model
- Time Step Size and Courant Number
- Mesh Interfaces in ANSYS FLUENT
- error in cfd post
-
2726
-
2146
-
1357
-
1150
-
462
© 2023 Copyright ANSYS, Inc. All rights reserved.