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March 15, 2024 at 9:17 amjackzhe551Subscriber
IN vof/mixture model ,I calculate the one fluid heat exchanger by fluent,I only care the outlet temperature and pressure,can steady mode be used for calculation?
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March 15, 2024 at 11:36 amRobForum Moderator
It depends. Steady boundaries don't always mean you have a steady flow field.
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March 15, 2024 at 11:38 amjackzhe551Subscriber
But if steady mode cannot calculate,transient mode cannot calculate,too?
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March 16, 2024 at 7:01 amjackzhe551Subscriber
could you help me remind Prashanth that he always does not reply to me, maybe he did not see.phase change hydrogen in heat exchanger (ansys.com)
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March 16, 2024 at 10:57 amjackzhe551Subscriber
If we do not calculate the physical properties from NIST, where can we get the hydrogen physical properties polynomial?
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March 18, 2024 at 9:56 amRobForum Moderator
Textbooks? There are other databases and methods, however it's not data I can share as I'm very limited in what I can do on here.
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March 19, 2024 at 7:18 amjackzhe551Subscriber
Do 2020 R2 support importing Rgp files? In the user guide for 2020, I cannot find the RGP table tutorial.Additionally,I cannot understand the tutorial,like fig shows,these words are written in a txt file or not?and then import into fluent udf?and the commands are written in console to launch python?
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March 19, 2024 at 11:16 amRobForum Moderator
That's the 21R2 documentation, so it may not be available in 2020 as there's no reference to RGP in 2020R2 Fluent documentation. The above looks like Python, but also refer to system coupling.
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March 23, 2024 at 3:37 pmjackzhe551Subscriber
A strange thing happened, my heat exchanger cold fluid (H2) inlet is at 22K, while the hot fluid inlet is at 360K. The cold fluid is H2, and I used NIST real gas, but without using tables, so there shouldn't be any limitations on the range of property parameters. However, in the calculation, it shows that the temperature has dropped to 13.939K. I expected the cold fluid to start heating up from 22K, so how could it drop below 22K? I'm puzzled that NIST doesn't seem to work well. Could you please provide me with a polynomial property equation for H2? Thank you."
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March 25, 2024 at 11:10 amRobForum Moderator
We don't provide fluid material properties other than what's in the Fluent solver, and I'd treat those with some caution. Check the materials input for whatever you've set up, and both operating and boundary conditions.
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