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Modeling a cross flow in a staggered tube bundle using ANSYS CFX |
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#1 |
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New Member
ASHRAF ALFANDI
Join Date: Oct 2012
Posts: 8
Rep Power: 2 ![]() |
Hi every one,
Task: Modeling a cross flow in a staggered tube bundle using ANSYS CFX. Given: The fluid is water of 300 deg Clausius flowing with inlet velocity 1 m/s,the boundary conditions are defined very well. Problem: The results shows that water temperature is not changing along the domain; water temp. inlet same as outlet. So I am not sure about the reason of that, Turbulence model, or water velocity, Heat transfer mode ( Total energy or Thermal Energy) ? Please help me . |
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#2 |
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Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 6,980
Rep Power: 59 ![]() ![]() ![]() |
First of all, please do not hijack threads. Start a new thread for a new question - especially when your question is not related to the original thread.
This problem could be caused by many things - it could be inaccuracy in your simulation (see http://www.cfd-online.com/Wiki/Ansys..._inaccurate.3F for tips) or it could be that the setup you are modelling does not result in significant heat being transferred to the water. From the sketchy details you have posted I cannot tell. Also - are you sure you are using a thermal model? You would not get any heat transfer if you have not enabled thermal modelling. Also how have you modelled the tube bank? |
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#3 | |
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New Member
ASHRAF ALFANDI
Join Date: Oct 2012
Posts: 8
Rep Power: 2 ![]() |
Quote:
I really appreciate your replay, I am so sorry that i didn't started a new thread. I am sure that I am using the thermal modeling. But what I am not sure about is that may be I didn't make the setup well. The tube bank is modeled as a cylinders, not Conjugate heat transfer Thanks so much for your kind response |
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#4 |
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Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 6,980
Rep Power: 59 ![]() ![]() ![]() |
Can you post an image? Also your CCL would help.
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