TAGGED: #fluent-#ansys, #fluent-#cfd-#ansys, udf
-
-
April 8, 2024 at 8:59 am315914335Subscriber
I hope to define the Pre-Exponential Factor of a chemical reaction as a function of the current substance concentration. Therefore, I need to get the mass concentration of a certain substance I need from fluent, and then define the pre-exponential factor through the functional relationship. Hope to get detailed answers and examples.
-
April 8, 2024 at 10:56 amRobForum Moderator
There doesn't look to be a hook in that panel for that, I know it's been asked before so check (search) on here.
-
April 8, 2024 at 11:05 am315914335Subscriber
Maybe UDF is a method. Can you provide relevant examples? I couldn’t find any relevant useful answers before.
-
April 8, 2024 at 11:40 amRobForum Moderator
I can only point you at the UDF documentation; you may find you need to write the whole chemistry model. I did raise an enhancement request last time this was requested, but I can't share any updates on that.
-
April 8, 2024 at 11:43 am
-
April 8, 2024 at 1:48 pmRobForum Moderator
Correct. Hence you may need to do a lot more coding at present.
-
April 8, 2024 at 1:53 pm315914335Subscriber
Hello, can you provide me an example of the code. Do you need to define the entire chemical rate or just Pre-Exponential Factor?
-
April 8, 2024 at 2:12 pmRobForum Moderator
Double check the Fluent theory to make sure it's not doing what you need, but otherwise you may find DEFINE_VR_RATE or DEFINE_NET_REACTION_RATE to be of use. There will be examples using both macros in the UDF manual.
-
April 8, 2024 at 2:14 pm315914335Subscriber
Thank you for your reply
-
- The topic ‘How to defined Pre-Exponential Factor as function in Fluent?’ is closed to new replies.
- Non-Intersected faces found for matching interface periodic-walls
- Unburnt Hydrocarbons contour in ANSYS FORTE for sector mesh
- Help: About the expression of turbulent viscosity in Realizable k-e model
- Cyclone (Stairmand) simulation using RSM
- error udf
- Diesel with Ammonia/Hydrogen blend combustion
- Fluent fails with Intel MPI protocol on 2 nodes
- Mass Conservation Issue in Methane Pyrolysis Shock Tube Simulation
- Script error Code: 800a000d
- Encountering Error in Heterogeneous Surface Reaction
-
1191
-
513
-
488
-
225
-
209
© 2024 Copyright ANSYS, Inc. All rights reserved.