Sergei Yushanov
Certified Consultant
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Posted:
1 decade ago
5 ago 2013, 16:24 GMT-4
Irina,
You can solve your problem with ether “Conjugate Heat Transfer” or “Heat Transfer in Fluids”. There are number of examples of this type of problem in the Model Library (Heat Transfer Module>Tutorial Models, Forced and Natural Convection, for example).
Generally, solver setting in Conjugate Heat Transfer is more robust and stable for convective-dominant problems.
Regards,
Sergei
Irina,
You can solve your problem with ether “Conjugate Heat Transfer” or “Heat Transfer in Fluids”. There are number of examples of this type of problem in the Model Library (Heat Transfer Module>Tutorial Models, Forced and Natural Convection, for example).
Generally, solver setting in Conjugate Heat Transfer is more robust and stable for convective-dominant problems.
Regards,
Sergei
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Posted:
1 decade ago
7 ago 2013, 08:07 GMT-4
Sergei,
Thank you very much for your reply.
I would like to ask: is there a need to use the "Non-Isothermal Pipe Flow" module for such purposes or I can use the standard HT and CFD modules?
Best wishes,
Irina
Sergei,
Thank you very much for your reply.
I would like to ask: is there a need to use the "Non-Isothermal Pipe Flow" module for such purposes or I can use the standard HT and CFD modules?
Best wishes,
Irina
Sergei Yushanov
Certified Consultant
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Posted:
1 decade ago
8 ago 2013, 10:45 GMT-4
Irina,
Yes, you can use standard HT and CFD interfaces to model this type of problem. You would need manually couple energy and momentum balance equations, although this coupling is quite straightforward.
Non-Isothermal Pipe Flow is a simplification: pipe is treated as 1D system and experimental correlations are used to model flow and heat transfer along the pipe length (you wouldn’t get cross-sectional distributions for the flow and temperature). This interface allows to model huge pipe systems but accuracy is somewhat sacrificed.
Regards,
Sergei
Irina,
Yes, you can use standard HT and CFD interfaces to model this type of problem. You would need manually couple energy and momentum balance equations, although this coupling is quite straightforward.
Non-Isothermal Pipe Flow is a simplification: pipe is treated as 1D system and experimental correlations are used to model flow and heat transfer along the pipe length (you wouldn’t get cross-sectional distributions for the flow and temperature). This interface allows to model huge pipe systems but accuracy is somewhat sacrificed.
Regards,
Sergei
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Posted:
8 years ago
10 ago 2016, 12:39 GMT-4
Hi!! please help me
my model is solid with heat flux on the upper face and fluid moving under lower face , I used Conjugate heat transfer
,but the result show that there are no heat transfer between solid and liquid!!
Hi!! please help me
my model is solid with heat flux on the upper face and fluid moving under lower face , I used Conjugate heat transfer
,but the result show that there are no heat transfer between solid and liquid!!
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Posted:
8 years ago
13 dic 2016, 02:57 GMT-5
Hi, have you solved that issue? I am using Conjugate heat transfer, but I notice no heat transfer between solid and fluid in my solution... Thank you in advance!
Hi, have you solved that issue? I am using Conjugate heat transfer, but I notice no heat transfer between solid and fluid in my solution... Thank you in advance!