-
-
November 2, 2018 at 2:57 pm
bektass
SubscriberHi everyone,
? m working on two-phase unsteady particle tracking with 3D geometry. One phase is water-liquid(continuous phase) and other nitrogen. the volume fraction of nitrogen is sufficiently low in terms of water-liquid. Actually, ? wanna track one or two nitrogen particles in the flowing water-liquid and ?'m using the eulerian method with eulerian parameter which is dense discrete phase model as multiphase model, injection type is group in the fluid domain.
Is it logical or not? If your answer is no, can you give me advise for my model. Because ?' am not sure about using dense discrete phase model which is the only granular type particle or not.
Thanks for your time.
-
November 2, 2018 at 4:16 pm
Rob
Ansys EmployeeIf you're looking at a low particle loading the DPM model is the best one to use. Read up on it in the Help to understand what the benefits & limitations are.
-
November 9, 2018 at 1:07 pm
bektass
SubscriberI will investigate it more. Thank you for your time.
-
- You must be logged in to reply to this topic.

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 in cfd post
-
2534
-
2066
-
1285
-
1104
-
459
© 2023 Copyright ANSYS, Inc. All rights reserved.