Note: This discussion is about an older version of the COMSOL Multiphysics® software. The information provided may be out of date.
Discussion Closed This discussion was created more than 6 months ago and has been closed. To start a new discussion with a link back to this one, click here.
Conjugate heat transfer pipe flow
Posted 01.11.2012, 18:30 GMT-4 Fluid & Heat, Heat Transfer & Phase Change Version 4.3 5 Replies
Please login with a confirmed email address before reporting spam
Hello,
I am trying to simulate a very simple laminar flow inside a pipe problem with a constant temperature at the walls. I have a cylinder made of water(liquid), and where one part is kept at a constant temperature at the wall, and rest of the wall changes from 293 to 393 for the remaining of the length.
My biggest issue is not so much the heat transfer part of the problem, but the velocity profile at various points of the pipe. I know I should get the same velocity profile everywhere and it should be a parabolic profile and since I am using a mean velocity of 0.02 m/s I know that my Vmax will be 0.04. However I only get this velocity profile at the inlet and not in the rest of the pipe. When I keep the walls temperature constant ( at 293 throughout) I get the correct velocity profile, it is only when I inflict the temperature gradient when the velocity profile changes, even though I am keeping my properties constant.
Any help will be appreciated. I am attaching my model
Thank you very much!
I am trying to simulate a very simple laminar flow inside a pipe problem with a constant temperature at the walls. I have a cylinder made of water(liquid), and where one part is kept at a constant temperature at the wall, and rest of the wall changes from 293 to 393 for the remaining of the length.
My biggest issue is not so much the heat transfer part of the problem, but the velocity profile at various points of the pipe. I know I should get the same velocity profile everywhere and it should be a parabolic profile and since I am using a mean velocity of 0.02 m/s I know that my Vmax will be 0.04. However I only get this velocity profile at the inlet and not in the rest of the pipe. When I keep the walls temperature constant ( at 293 throughout) I get the correct velocity profile, it is only when I inflict the temperature gradient when the velocity profile changes, even though I am keeping my properties constant.
Any help will be appreciated. I am attaching my model
Thank you very much!
Attachments:
5 Replies Last Post 07.11.2012, 14:29 GMT-5