-
-
November 19, 2019 at 2:34 am
otani
SubscriberI am running a model with the following specifications:
- pressure-based
- 2-D, axisymmetric
- steady
- turbulent (sst k-omega)
- species transport (binary system of dimethylformamide and carbon dioxide)
- UDFs for density, specific heat, viscosity, and thermal conductivity for CO2
- UDFs for specific heat, viscosity, and thermal conductivity for DMF
- polynomial fit for density for DMF
- pressure outlet
- two mass flow inlets, one for each species at nearly equivalent mass flow rate, different hydraulic diameter
- constrained temperature range [300,335]K due to range of data UDFs are based on
Continuity residual is staying consistently at E-3 and not dropping. I have tried many things like changing the polynomial fit to be higher order, changing the computational schemes for momentum, changing the relaxation factors, refining my mesh, and nothing has made it converge. Eventually around 30,000 iterations, the simulation diverges. Attached is a photo of the residuals up to the point of divergence.
Any advice would be greatly appreciated. I can provide more information as necessary.
-
November 19, 2019 at 6:02 am
DrAmine
Ansys EmployeeWhat about mass imbalances and energy from flux report as well as behaviour of some monitor points? -
November 19, 2019 at 6:34 pm
otani
SubscriberHi Amine,
Thank you for your response. I've added the flux reports below. Could you expand upon what you mean by the "behavior of some monitor points"?
Mass Flow Rate (kg/s)
--
innerinlet 0.00034
interior-surface_body -0.92569468
outerinlet 0.00031
outlet -0.00064999698
wall -0
Net 3.018828e-09
Custom Vector Based Flux
Total Energy
--
axis -9.0669255e-24
innerinlet 4.2376269e-07
interior-surface_body -0.0010646494
outerinlet 3.2457537e-07
outlet -6.8616645e-07
wall 3.5971273e-08
Net -0.0010645512
Thanks much,
Courtney
-
- 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: Received signal SIGSEGV
-
5162
-
3251
-
2443
-
1308
-
954
© 2023 Copyright ANSYS, Inc. All rights reserved.