-
-
March 25, 2020 at 12:57 pm
Battery
SubscriberI have some issues with the thermal models of pouch cells in serie configuration. As example the thermal model of 4 battery pouch cells in series has exactly the same maximum temperature as one cell. Also cell 1 & 4 in the battery pack should be the same whilst the two cells in the middle (cell 2&3) should be hotter because the accumulated heat in the middle of the pack is more difficult to dissipate.
What I am doing wrong? Reviewed my project several times but can't find any issues. Only thing I'm not sure about is: do I need to define the areas between the cells as air?
Â
I do get this warnings and I already did run the command "/mesh/modify-zones/slit-interior-between-diff-solids parallel" but it doesn't change the models.
Â
Â
-
March 26, 2020 at 12:49 pm
Battery
SubscriberTo add to my question:
The images below are from the paper: "Transient Temperature Distributions on Lithium-Ion Polymer SLI Battery" by Yiqun Liu, Y. Gene Liao * and Ming-Chia Lai. This paper describes how the thermal models should look like. It says that the cells in the middle have the highest temperature because heat accumulated in the middle of the pack is more difficult to dissipate.
-
March 27, 2020 at 4:30 pm
spatel
Ansys EmployeeAre the cells actually in contact with each other and also what are the thermal boundary conditions to dissipate the heat - convection boundary.
-
March 28, 2020 at 10:42 am
Battery
Subscriber
Are the cells actually in contact with each other and also what are the thermal boundary conditions to dissipate the heat - convection boundary.
Yesterday I made a new project and tried to remake the battery in the paper with the same dimensions to compare results and to verify my working method. This is what happens when boundary conditions are the same on all the cell walls:Â
Â
This is the result when I remove all boundary conditions on the cells in the middle. This clearly looks much better and compares better to the results in the paper. The cells have 3 to 7mm space in between them. The space is filled with air in the simulation (also was wondering if I need to define this area with air?). At the cells on the outside convection happens and the cells on the inside conduction I suppose? Anyway I'm not sure how I can use conduction in Ansys.
Here you can see the boundary conditions used on the cells on the outside. But what should I use for the cells on the inside because conduction isn't listed in the BC interface. I found shell conduction but this asks me for a wall thickness.
Â
-
April 1, 2020 at 11:44 am
Battery
SubscriberI had a response from the writers of the paper and they told me that you need to add an air volume between the cells. How can you do this?
-
April 3, 2020 at 10:09 am
spatel
Ansys EmployeeThanks for the additional information.
From the last two images you shared it is clear that there is a physical gap between the cells being modelled. And this gap is not meshed and so not modelled - hence this means conduction cannot be accounted since there is no mesh in the gap.Â
So either:
- mesh the gap in between the cells and model the air (accurate and solver works out heat transfer to/from the air gap) - make sure to have at least 3 prism layers close to the battery cell faces)
or
- you modify the thermal boundary conditions of cells faces that are facing each other to have have lower heat transfer which is what would happen as the heat transfer coefficient and air temperature in between cells will be higher.
First option makes good sense in your case as in the other option you will have to somehow try to find suitable heat transfer coefficient and air temperature values which will need to be approximate somehow as these are not typically availableÂ
Â
-
June 30, 2022 at 10:02 am
ali.abbas
SubscriberHi Spatel,
Â
Just a small question if i desgined a solid body which is directly connected to the cells and considered this body as fluid region in ansys fluent, does it do the job?
-
-
April 8, 2020 at 11:41 am
Battery
SubscriberThanks Spatel.
I did mesh the gap between the cells and this solved the issue. Unfortunately this isn't covered in the tutorial. You can see the result below:
But I don't really understand why we have to do this. If the air between the cells needs to be meshed, why the air on the outside of the cells doesn't need a mesh?Â
Â
-
April 15, 2020 at 10:02 am
Battery
SubscriberBump
-
June 30, 2022 at 9:57 am
ali.abbas
Subscriberdear battery how did you add the volume of air between the cells?
-
-
April 17, 2020 at 2:16 pm
Rob
Forum ModeratorOn the outside of a cell we can add an external HTC and temperature, between the cells (I assume) you're expecting to see heat transfer so we need to include that in the model.Â
-
August 10, 2020 at 1:46 pm
AngelFalls
SubscriberDear Battery, did you use any boundary condition for the air domain? Which solution method did you use? Thank you.n
-
- The topic ‘Incorrect thermal model’ is closed to new replies.
- The legend values are not changing.
- LPBF Simulation of dissimilar materials in ANSYS mechanical (Thermal Transient)
- Convergence error in modal analysis
- APDL, memory, solid
- How to model a bimodular material in Mechanical
- Meaning of the error
- Simulate a fan on the end of shaft
- Real Life Example of a non-symmetric eigenvalue problem
- Nonlinear load cases combinations
- How can the results of Pressures and Motions for all elements be obtained?
-
4062
-
1487
-
1308
-
1156
-
1021
© 2025 Copyright ANSYS, Inc. All rights reserved.