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November 21, 2019, 16:13 |
thermal expansion coefficient in FLUENT
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#1 |
New Member
Chaatouf Dounia
Join Date: Jun 2019
Posts: 11
Rep Power: 6 |
Hello everyone,
my study case is transient natural convection in which I'm using boussinisq density in air property, the problem is in the thermal expansion coefficient. -I search online, and I found a value of 0.0032 (1/k) for air. -but I found a tutorial video in YouTube that use 0.036 (1/k), -when I'm using a value of 0.00032(1/k) I found good results. so my question is! is it logical if I use 0.00032 ? and how can I know the right value in my case? I'll be so grateful for any comments or answers. Best wishes, Dounia |
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November 21, 2019, 17:07 |
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#2 |
Senior Member
Lucky
Join Date: Apr 2011
Location: Orlando, FL USA
Posts: 5,674
Rep Power: 66 |
For ideal gases, you have (see Thermal expansion). You can use more real properties if you like.
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July 29, 2020, 03:29 |
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#3 | |
New Member
Join Date: Jun 2020
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Quote:
Many thanks, Bryce |
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July 29, 2020, 05:07 |
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#4 |
Senior Member
Alexander
Join Date: Apr 2013
Posts: 2,363
Rep Power: 34 |
I'm not sure if there is predefined in UDF macro to get thermal coef value
what you can do is: 1. get thermal coef value using scheme, write it to any variable (to get this variable you may use TUI commands and pick-a-real command. On the other hand, there should be a scheme name of variable for thermal coef which I don't know) 2. read this variable in UDF
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January 9, 2021, 03:05 |
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#5 | |
New Member
Join Date: Jun 2020
Posts: 6
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Quote:
Thanks for your advice, as I searched there is no macro to access the thermal expansion coefficients. However, I can calculate it using matlab via REFPROP (the values versus temperature). Could you give more details about your approach? Thanks, Bryce |
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