-
-
December 2, 2019 at 7:22 pm
rachels1001
SubscriberHey guys,
I am trying to model a perforation in the side of a pipeline. The pipeline has gas flowing through the main body, with water in the perforation. I am interested in the interface between the water and gas, and so I am using the VOF multiphase model, as the flow is stratified. Because I am implementing the VOF model, I am using the pressure-based pseudo transient solver. I am also using the standard k-omega turbulence model because I am interested in eddy formation.
I am experiencing convergence issues with this simulation. Namely, whenever I run it using either the iterate or dual-time-iterate command, I get the following errors:
"Experiencing convergence difficulties-temporarily relaxing adn trying again...
Divergence detected in AMG solver: pressure coupled / k / omega / phase-1-species-0...etc.
These errors are given immediately, prior to any iterations completing.
I have adjusted my URFs and flow courant number. I am using the following values, and still experiencing these errors:
Flow courant number: 10
Momentum/pressure: 0.5
Density: 0.25
Body forces: 0.75
Turbulence kinetic energy: 0.5
Turbulent viscosity: 0.75
Energy: 0.5
Phase species: 0.75.
I am using the variable time stepping method.
Is there any other things I should try to do to improve convergence? Or, as I am getting these errors, is it probably something wrong with my mesh or setup? Another thing that I am worried about is that my model does have cell zones that contain solid sections, could that be incompatible with the VOF model?
Thanks so much for the help!
Claire
-
December 3, 2019 at 3:38 pm
Rob
Ansys EmployeeHow much mesh have you got in the perforation? If you look at the velocity there & cell size how long does it take for the flow to cross one cell? Remember you'll need 5-10 cells across the liquid jet and any droplets to capture the free surface.
-
December 4, 2019 at 3:25 pm
rachels1001
SubscriberI had around 20 cells across the 3mm diameter of the perforation. The length of the perforation is 12mm, and there is 100 layers of cells along the length of the perforation. There is also 20 inflation layers in the gas pipeline before the perforation.
Removing the solid cell zones did help; however, the simulation still diverges after a short period.
-
December 5, 2019 at 4:56 pm
Rob
Ansys EmployeeIf you look at the results just before it goes wrong can you see anything "odd"? Also, does the free surface pass through (as opposed to along) the inflation region?
-
December 5, 2019 at 6:27 pm
rachels1001
SubscriberHey guys, thanks for the help!
I tried a couple things today, but what eventually worked was refining my mesh even more and converting the mesh to polyhedral elements once I was in fluent. From there, decreasing the under-relaxation factors and courant number and slowly increasing them over the run worked out pretty well.
-
- 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
- Difference between K-epsilon and K-omega Turbulence Model
- The solver failed with a non-zero exit code of : 2
- Time Step Size and Courant Number
- Mesh Interfaces in ANSYS FLUENT
- error: Received signal SIGSEGV
-
5290
-
3311
-
2469
-
1308
-
1016
© 2023 Copyright ANSYS, Inc. All rights reserved.