LuckyTran |
April 24, 2018 02:41 |
Quote:
Originally Posted by mariam.sara
(Post 690053)
Thanks Lucky for the reply. I aware the Nusselt number is different in each wall. I attempted now to evaluate Nu just at the bottom wall of cavity I already used the Tinfinity as reference temperature for it but it give me wrong values of Nu some of it are negative?
Thanks
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I'm afraid you still miss the point. Your idea is that the value of Nusselt number differs is due to the differences in heat flux. But the reference temperature that is used to define the heat transfer coefficient per Newton's Law of Cooling is what I meant by different definitions of heat transfer coefficient.
My previous point is that when you write down h as the boundary condition for the left wall, it already has an implied reference temperature. Now if you try to use a different reference temperature for the other walls, then you have two different types of heat transfer coefficients that are defined based on different reference temperatures. Maybe this is desired, maybe it is not. I don't know your preference.
For enclosures, one often takes some sort of mean temperatures e.g. (TH + TC)/2. You have a three temperature problem where it is not so clear which reference temperature to use, it depends on what story you want to tell and what picture you want to paint.
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