-
-
November 2, 2018 at 11:26 am
-
November 2, 2018 at 11:50 am
DrAmine
Ansys EmployeeTo get away with the warning: Adjust your tracking parameters (Increase Max Number of Steps for example). Moreover as you are trying to calculate the collisions your particle time step size has to be at leat 1/10 of the collision time. You need then to approximate the collision time based on the spring constant, reduced mass and coefficient of restitution.
-
November 2, 2018 at 5:49 pm
MohAgha1
SubscriberDear Mr. Amine;
Thanks for your response.
I tried reducing the dem time step to 1e-5, the fluid time step to 1e-4 and increased the maximum number of DPM time steps to 50,000.
Unfortunately, the warning still exists and there is a non-realistic solids void fraction of 0.002 ?!
Can the problem in the parcel's mass flow?
I calculated it into Matlab m-file as follows:
total_mass_flow = 0.3*0.3*0.01*0.6*density; % mass of the solids occupied 0.3x0.3x0.01 2D domain with 0.6 initial void fraction
m_p = (pi/6)*diameter*diameter*diameter*density; % physical particle mass
n_p = total_mass_flow/m_p/x_count/y_count/z_count; % total number of physical particles/parcel
mass_flow = n_p*m_p/1e-8; % parcel mass flowrate in 1e-8 injection time period
Regards;
Mohamed
-
November 3, 2018 at 1:01 pm
DrAmine
Ansys EmployeeIt does not make a sense increasing the number of steps. Check the collision time as mentioned. Regarding mass flow from MATLAB I won't comment. You have the possibility of volume injection in Fluent. Use it meanwhile switch off flow. After the particles settled down switch on flow. You do not require other non drag forces for solids. Use DDPM for dense beds.
-
- 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
-
2656
-
2120
-
1347
-
1118
-
461
© 2023 Copyright ANSYS, Inc. All rights reserved.