TAGGED: fluidflow, iterations, timestep, transient
-
-
February 7, 2024 at 5:28 amMohamed RamonSubscriber
Â
In a transient fluid flow simulation of air inside pipe, i set the number of time steps as 6000 and 0.01 step size. Can i stop the solution running after just 2000Â time-step and get the results for just 20 sec of simulation? Or will that affect the results?
In a transient fluid flow simulation of air inside pipe, i set the number of time steps as 6000 and 0.01 step size. Can i stop the solution running after just 2000Â time-step and get the results for just 20 sec of simulation? Or will that affect the results?
In a transient fluid flow simulation of air inside pipe, i set the number of time steps as 6000 and 0.01 step size. Can i stop the solution running after just 2000 time-step and get the results for just 20 sec of simulation? Or will that affect the results?
-
February 7, 2024 at 8:03 amSRPAnsys Employee
Hi,
It's important to note that stopping the simulation early might affect the results, especially if the flow has not fully developed or reached a steady state by 20 seconds. In some cases, such as when dealing with high continuity residuals, it's suggested to reduce the timestep, aiming for an optimum of 10-15 iterations per time step.
-
February 7, 2024 at 8:21 amMohamed RamonSubscriber
I think 20 sec is good as i have 20 iterations ber time step
-
February 7, 2024 at 9:22 amSRPAnsys Employee
Hi,
Did you monitor any parameter to check convergence? If not I suggest you to do so.
-
February 7, 2024 at 9:36 amRobForum Moderator
You can stop a Fluent run at any time and check the results. Assuming each time step converges you'll then have the result for some time of that flow interacting with your initial conditions. Whether that is what you want to see, and what you think you want to see, are entirely different questions, and not something we can easily answer.Â
-
- The topic ‘Time steps in transient simulation’ is closed to new replies.
- How do I get my hands on Ansys Rocky DEM
- 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
- Script Error
- Mass Conservation Issue in Methane Pyrolysis Shock Tube Simulation
- Facing trouble regarding setting up boundary conditions for SOEC Modeling
- convergence issue for transonic flow
- Running ANSYS Fluent on a HPC Cluster
- Point exception in erosion calculation
-
1882
-
802
-
599
-
591
-
366
© 2025 Copyright ANSYS, Inc. All rights reserved.