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a.lone June 24, 2019 23:11

boussinesq approximation when temperature difference is large
 
I'm studying on the natural convection of spent fuel in the dry storage system.

I understand that boussinesq approximation can be used only when the temperature difference is small.

If the temperature range is 300K-500K for example, is it right to simply use an incompressible ideagl gas law that uses the p=rho*R*T law?

Or can i just use the boussinesq approximation?

i don't know about these.


Thank your reply.

evcelica June 25, 2019 11:38

That temperature range is too large for Boussinesq. I've heard 10% density difference maximum. Ideal gas is not incompressible, it is definitely compressible, and using that for density would be much more appropriate.

a.lone June 25, 2019 20:20

Quote:

Originally Posted by evcelica (Post 737220)
That temperature range is too large for Boussinesq. I've heard 10% density difference maximum. Ideal gas is not incompressible, it is definitely compressible, and using that for density would be much more appropriate.

Thankyou so much!

Sai Krishna September 15, 2020 15:07

Quote:

Originally Posted by evcelica (Post 737220)
That temperature range is too large for Boussinesq. I've heard 10% density difference maximum. Ideal gas is not incompressible, it is definitely compressible, and using that for density would be much more appropriate.

Hi evcelica,
I have a doubt regarding coefficient of thermal expansion which we use in boussinesq approximation.
I am doing simulation for natural convection for a pcb in an enclosure. the freestream temp is 322K. i read bousinesq approximation is valid iff
beta * (T-T_ref) <0.05. in this for beta what should I consider. my fluid is air and as its an ideal gas beta = 1/T. so here what temperature should I use.

Thanks for the help


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