-
-
November 27, 2022 at 2:54 pm
164170007
SubscriberHello all, I am doing simulation of catalytic reaction of hydrogen with air in presence of catalyst, where I have many inlets (BLUE LINES). 4 small inlet for hydrogen and 1 inlet for oxygen and 1 outlet and whole reactor is coated with catalyst (neglecting small dimensions of hydrogen inlet geometry).
I am using UDF for kinetics which is giving correct result with literature when hydrogen and air are enetring with one inlet (No multiple inlets), so I dont think its because of UDF. But in the multiple inlet geometry I only changed the boundary conditions of species mole fraction which I gave 1 for H2 and 1 for O2 for multiple inlet case. (ONE INLET CASE I had given H2/O2 ratio like 0.5:0.5 at the inlet). The whole simulation is for steady state and laminar conditions and I am using species transport volumetric reactions model for both cases.
I am not getting what wrong is happening with simulation and why despite decrease in residuals its showing divergence error. Please see the mesh for my simulation, I dont think its an issue.
Thanks in advance,
Regards,
Vinay
-
November 29, 2022 at 4:41 pm
Rob
Ansys EmployeeIf you plot the results at 1000, 1500 and 2000 iterations how does the model look? I'm wondering what's causing the instability, and the earlier results may give some clues as to what's going on.
-
December 2, 2022 at 11:00 am
-
December 6, 2022 at 11:21 am
Rob
Ansys EmployeeI don't think you're doing anything wrong as such. The first hydrogen inlet triggers a reaction with the oxygen supply. That gives a very high temperature reason, and may or may not use up a large amount of oxygen. You then get an unstable flame in the system. Without knowing what the other settings (inlet, material density etc) I can't really guess what's going on, but suspect the model is OK, but possibly missing something when compared to reality.
-
- 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
-
2148
-
1359
-
1150
-
462
© 2023 Copyright ANSYS, Inc. All rights reserved.