-
-
November 18, 2019 at 11:18 pm
LukeM
SubscriberHello,
I am simulating single-phase flow through a pipe. I'm trying to add mass transfer to my simulations, but I encountered some unexpected issues with the boundary conditions.
I'm blowing air through my pipe, and I'm trying to simulate pure benzene on the walls of the pipe diffusing into the airflow. I set the wall mass fraction of benzene to 1.0. But when I ran my simulation, it seemed like the air was being replaced with benzene, rather than benzene being added to the gas flow. The image below shows the mass fraction of benzene moving through the pipe (benzene enters the pipe in the last 2/3rds of the pipe). The mass fraction of benzene leaving the pipe is nearly 1. Where did the air go?
The density in my pipe is also changing through the pipe.
I'm wondering if my choice of a volume-weighted-mixing-law is causing the change in density. But why is the air disappearing?
-
November 19, 2019 at 6:07 am
DrAmine
Ansys EmployeeI would rather provide a flux for the component. You might add a source term in the first cell layer to the wall. Check the order of the species in the mixture panel. -
November 19, 2019 at 3:49 pm
LukeM
SubscriberThat's a good idea. Unfortunately, the flux is the value I'm trying to measure. I'm trying to measure the amount of benzene that enters the air by the end of the pipe. Sorry, I probably should have mentioned that in my original post. Is there any other way besides defining the flux?
-
November 19, 2019 at 4:19 pm
DrAmine
Ansys EmployeeSource term. Setting the value of the specie at wall is not equivalent to having a source of that specie through the wall. -
November 19, 2019 at 4:54 pm
LukeM
SubscriberBut what value do I give the source term? I'm trying to measure the amount of benzene entering the system, so I can't specify the amount coming through the wall.
-
November 20, 2019 at 7:14 am
DrAmine
Ansys EmployeeThe value you want to add as source into the domain: if you do not know that than you need to make assumptions.
You want to measure the amount coming in: then you need to define the walls as inlets.
-
- 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
-
5340
-
3345
-
2471
-
1308
-
1016
© 2023 Copyright ANSYS, Inc. All rights reserved.