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Dye mixing inside a tank : UDS or Species Transport or DPM ?

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Old   March 30, 2023, 07:04
Default Dye mixing inside a tank : UDS or Species Transport or DPM ?
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Dear all,

I am studying the mixing properties inside a tank both experimentally and numerically.

I already realized a steady 3D simulation of the water flow inside the tank. Simulation and experiments are in good agreement.
I also realized experimentally a continuous injection of dye and would like to reproduce this using simulation BUT by using transient solver to get time-dependant informations concerning mixing.

I already tried to use UDS for the dye which have same physical properties as water. As a result, the UDS seems to only diffuse from the inlet and is not convected by the flow. See Attachements at 1s, 100s and 200s.
Here is my procedure step-by-step:
1) I defined a UDS with Flux Function on "mass flow rate"
2) I switched to "Transient" solver
3) In BC, I enter a Specified Value of UDS = 1 at the Inlet and a 0 Flux value on other boundaries.
4) In Controls panel, I unchecked Flow and Turbulence equations to only solve transport equations of my UDS and to keep the flow solution obtained from steady solution.
5) I did NOT initialize and i ran calculations with time-step size = 0.1s.

So my questions are :
- Is it possible to use a steady flow solution and then use this solution to solve time-dependant UDS transport ? I feel like it should be douable but i am probably missing something.
- I think that other methods as Species transport or DPM are also usable in my case ? What would you recommend between those 3 ? (I am afraid that Species Transport and DPM migth require high computation time)

Thank you so much in advance.
Attached Images
File Type: jpg 1s.jpg (15.5 KB, 6 views)
File Type: jpg 100s.jpg (16.2 KB, 4 views)
File Type: jpg 200s.jpg (16.2 KB, 3 views)
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Old   March 17, 2024, 00:45
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Did you get solution to problem?
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