nice simulation, i have a question about modeling evaporation of water under vacuum conditions using FLUENT, is it possible or do i have to define a UDF to simulate the mass transfer. thank you
@xeusater It is possible you just need the cpu capability to do it. Thanks for the reply, nice simulation. I've got some lagrangian fluidized bed simulations on my account if you want to check them out.
first you need to get the real flow time, in my case it was from 0 to 9s, approx. Then you get the real part of the time [0, 1,2, 3, etc] and use it as a coefficient to multiply a given initial value of velocity.
For example, for the first second of simmulation: V = 0.1 m/s * [0 (time) + 1] = 0.1m/s
Could you send your models to my mail filosofem@mail.ru. please I am really intresting in fluidized bed furnaces.
filosofemus 5 months ago
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Anyone in the industry should check out Procedyne. These guys do nothing but fluid beds, specializing in fine particles and high temperatures.
nift101 11 months ago
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nice simulation, i have a question about modeling evaporation of water under vacuum conditions using FLUENT, is it possible or do i have to define a UDF to simulate the mass transfer. thank you
justawesome85 11 months ago
is the solid-phase modeled as lagrangian or eulerian? if lagrangian how many particles you using here? cheers.
bikeflat1 1 year ago
@bikeflat1 It's Eulerian approach, there's no way to model dense fluidized beds with the Lagrangian, (that I know, anyway)
xeusater 1 year ago
@xeusater It is possible you just need the cpu capability to do it. Thanks for the reply, nice simulation. I've got some lagrangian fluidized bed simulations on my account if you want to check them out.
bikeflat1 1 year ago
Could you please show me the link of documentation of this work (any type) ?
arman6082 2 years ago
Geldard B, sand 3600kg/m^3, and 550µm diameter
xeusater 2 years ago
I am using Syamlal-Obrien drag force. Nope, I dont have a UDF example. But I think there's one example in the FLUENT tutorials.
xeusater 2 years ago
how did u input the commands for the UDF in order to make it increase in steps
nemesispussy 2 years ago
first you need to get the real flow time, in my case it was from 0 to 9s, approx. Then you get the real part of the time [0, 1,2, 3, etc] and use it as a coefficient to multiply a given initial value of velocity.
For example, for the first second of simmulation: V = 0.1 m/s * [0 (time) + 1] = 0.1m/s
and then for the 2nd second:
V = 0.1 m/s *[1 (time) +1] = 0.2 m/s
Best Regards and happy simulation
xeusater 2 years ago
THE COMMAND U GIVE ABOVE IS NOT WORKING IN THE BOUNDRAY CONDITION WITH GAS INLET VELOCITY , HOW TO MODYFY IT SO THAT IT WORKS THERE.
ERROR ""Y-Velocity (m/s) : 0.1*[1(time)+1] is invalid - real value(s) required""
PLZ HELP
THANKS IN ADVANCE
shoebkhan4u 2 years ago
cool is this grid based? or meta rendered sph?
natethegreatBlitzMax 2 years ago
Awesome! I'm doing a project on the same subject. Can you give me some information about the model and the boundary conditions that you have used?
Thanks
em02154 3 years ago