Tagged: heat-pipe, heat-transfer-coefficient, laminar, yplus
-
-
January 3, 2023 at 3:46 pm
Kilian Nuss
SubscriberHi Ansys Comunity,My questions regard a internal laminar flow simulation in a pipe with a constant temperature at the wall.The velocity of the fluid is around 0.01m/s and has a high dynamic viscosity of 100mPas. Reynolds number does not exceed over 100.The main goal is to determine the heat transfer coefficient and the temperature profil.After reading articles about resolving turbulent flow my issue is to decided which solver I should use and what y+ value is recommended.So could you please give me any advice for this instance?Furthermore, how can i check if I resolved the heat transfer/temperature profil appropriately analougous to turbulent flows and their boundary layers.Thank you in advance. -
January 4, 2023 at 6:10 am
SRP
SubscriberHi,
For selection of model, please refer to the theory guide: 4.18. Near-Wall Treatments for Wall-Bounded Turbulent Flows (ansys.com)
I suggest to create an additional variable for the eddy viscosity ratio. Then by plotting this variable on a suitable plane, and superimposing mesh in the near-wall region, we can visualize the boundary layer resolution.
Hope you find this useful
Thank you
-
January 4, 2023 at 1:32 pm
Rob
Ansys EmployeeMesh resolution studies can help here too: keep refining the mesh until it stops changing. Also, don't forget to check you resolve any flow separation and bulk flow phenomena. Too many fall foul of focussing on the near wall region to the detriment of the rest of the flow domain so miss what's going on.
-
January 10, 2023 at 1:53 pm
Kilian Nuss
Subscriberso you would advice me to use a turbulent flow model instead of the laminar? even though the Re<100?
thank you Rob for the advice I am going to keep it in mind when I am doing the mesh refinement.
-
January 11, 2023 at 10:02 am
Rob
Ansys EmployeeGenerally no. It can be worth running one case laminar & again turbulent to see if there's a significant difference. Reason being if you're borderline transitional due to flow conditions (not Re - that's a guide) it can show up in the turbulent case.
Note, depending on conditions transition flow in a pipe can occur at Re 800-1000 The undergrad experiment when I was at Uni gave very odd results every 20mins: that coincided with a bus parking outside....
-
- You must be logged in to reply to this topic.

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
-
2688
-
2138
-
1351
-
1136
-
462
© 2023 Copyright ANSYS, Inc. All rights reserved.