-
-
September 27, 2017 at 11:19 am
nselvara
Ansys EmployeeFor models where no pressure boundary is being used, but it's desired to set a pressure level at some location, the following procedure can be used: 1) Set the Reference Pressure on the domain Basic Settings tab 2) Under Solver Control, under the Advanced Options tab, check the "Pressure Level Information" box. Change the option from Automatic to Cartesian Coordinates and enter the coordinates of the location where the pressure level is to be set. Check the box "Relative Pressure Level", and enter the desired pressure. The value should be set such that the Relative Pressure plus Reference Pressure is equal to the absolute static pressure.
-
September 27, 2017 at 11:19 am
nselvara
Ansys EmployeeHow to Specify Inlet Pressure Value for Model Without Pressure Boundaries?
-
- 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.