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Thermal resistance in non-isothermal pipe flow (nipfl)
Posted 3 mag 2016, 09:30 GMT-4 Fluid & Heat, Heat Transfer & Phase Change, Geometry, Modeling Tools & Definitions, Parameters, Variables, & Functions Version 4.4, Version 5.0, Version 5.1, Version 5.2 2 Replies
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I'm using non-isothermal pipe flow model and heat transfer in solids physics in order to simulate a bore hole heat exchanger (BHE). the problem consist of a tube modeling by nipfl and a ground around the tube modeling as a solid heat transfer. The program seems to simulate the problem in a reasonable way but when the thermal resistance (R) is calculated, the obtained R by Comsol is higher almost 30 % compared with R obtained by formula or 2D model. I guess since this module simulate the pipe flow as a 1D problem and there is a gap between the pipe and solid which in graphics shows as a solid part, it adds the value of thermal resistance. Can anyone help or has a suggestion?
In attachment you can find the file.
kind regards,
Amin
Attachments:
Hello Amin Jahanbin
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