-
-
August 8, 2019 at 8:11 pm
trippleD
SubscriberHello,
i have a question about the near-wall region.
As you can see on the picture, the inner layer consits of three layers:
- viscous sublayer
- buffer layer
- fully turbulent region
In the documentation, you can find the follwing explanation:
Numerous experiments have shown that the near-wall region can be largely subdivided into three layers. In the innermost layer, called the “viscous sublayer”, the flow is almost laminar, and the (molecular) viscosity plays a dominant role in momentum and heat or mass transfer. In the outer layer, called the fully-turbulent layer, turbulence plays a major role. Finally, there is an interim region between the viscous sublayer and the fully turbulent layer where the effects of molecular viscosity and turbulence are equally important.
The explanation isn't clear for me. Is the outer layer, mentioned in te explanation that one that ist named the same as in the picture? The rigth layer of ther inner layer is fully turbulent as well. So is the outer layer and the right layer of the inner layer one layer (the same) or different? Which layer does the explanation mean exactly?
Thanks for your help,
trippled
-
August 9, 2019 at 5:58 am
DrAmine
Ansys EmployeeYes the outer layer mentioned is the log-law region. Viscous+buffer layer+log-law layer constitute less than 0.15-0.2 of the whole boundary layer. The right layer called fully turbulent layer or velocity defect layer (for modeling requires some wake functions).
-
August 9, 2019 at 6:56 am
trippleD
Subscriber
Yes the outer layer mentioned is the log-law region. Viscous+buffer layer+log-law layer constitute less than 0.15-0.2 of the whole boundary layer. The right layer called fully turbulent layer or velocity defect layer (for modeling requires some wake functions).
I'm sorry but it is still not clear for me
1: viscous sublayer
2: buffer layer
3: log-law region
4: outer region
So which layer is mentioned in the documentation
Numerous experiments have shown that the near-wall region can be largely subdivided into three layers. In the innermost layer, called the “viscous sublayer”, the flow is almost laminar, and the (molecular) viscosity plays a dominant role in momentum and heat or mass transfer. In the outer layer, called the fully-turbulent layer, turbulence plays a major role. Finally, there is an interim region between the viscous sublayer and the fully turbulent layer where the effects of molecular viscosity and turbulence are equally important.
Sorry for double asking but thanks a lot
-
August 9, 2019 at 9:21 am
DrAmine
Ansys Employeelog-law layer.
-
September 22, 2019 at 8:52 am
trippleD
SubscriberThe vleocity u, is it the absolut velocity or the velocity in a special direction?
-
- 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
-
2706
-
2142
-
1355
-
1144
-
462
© 2023 Copyright ANSYS, Inc. All rights reserved.