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March 11, 2014, 11:42 |
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#21 | |
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François Grégoire
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July 10, 2017, 13:08 |
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#22 | |
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AnsysUser
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August 14, 2017, 05:09 |
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#23 |
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Taiwan,new north city
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hello guys,
i am also doing the forced convection problem between the solid body and fluid domain. i have read all of your comments and i followed all of it. so my question is that after i changes the reference temperature in fluent i got some h value. but i wanna make sure whether that h value is correct or not. if somebody explain, how to write a UDF for calculating the exact h value. Thanks in advance. |
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August 20, 2018, 07:41 |
about udf.
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#24 | |
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sujal
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can you please elaborate on how and where to write udf.? |
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August 31, 2020, 07:41 |
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#25 | |
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Sai Krishna
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Regards |
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December 21, 2021, 07:14 |
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#26 | |
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physics baali
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December 21, 2021, 14:43 |
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#27 |
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Lucky
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This entire thread is whack.
The bulk temperature is the mixed temperature at each location. It is not the average of the inlet and outlet. It is the temperature the flow would have if you magically somehow mixed all of it together. The inlet has an inlet bulk temperature. The outlet has an outlet bulk temperature. Everywhere, has a bulk temperature. For internal heat transfer, the bulk temperature is commonly used as the reference temperature for the heat transfer coefficient but also for all the fluid properties. Some people are too lazy, or they just don't have the skill to calculate the bulk temperature and they will use the average of the inlet and outlet instead as a very crude approximation. The wall temperature should not be used for the reference temperature, that would just make the heat transfer coefficient undefined because htc=q"/0. Wall temperature you get from Fluent. |
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December 29, 2021, 08:13 |
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#28 |
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physics baali
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thank you a lot about the answer, but how can i found wall temperature from fluent
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December 29, 2021, 17:29 |
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#29 |
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Lucky
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There is a variable literally labeled wall temperature in Fluent. Just plot it.
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