Calculate Nusselt Number: Free Convection Air Vertical Channel Different Temps

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The discussion centers on calculating the Nusselt number for free convection of air in a vertical channel with walls at different temperatures. Participants express uncertainty about which equations, specifically the Bar-Cohen and Rohsenow equations, apply to their scenario, particularly regarding symmetric and asymmetric heating conditions. There is a noted lack of literature addressing asymmetric heating in vertical channels, leading to suggestions of using enclosure equations as approximations. Concerns are raised about how different heating configurations can significantly affect the computed Nusselt number and convection coefficients. The conversation highlights the complexity of modeling free convection in such setups and the need for further research.
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What expression should be used to calculate Nusselt number for free convection (of air) in a vertical channel with walls at different temperatures?

I have the Bar-Cohen and Rohsenow equations, but I am unsure which situation this corresponds to (and thus which constants to use).
Symmetric isothermal plates (wouldn't this imply Ts,1 = Ts,2 which is not the case?)
Symmetric isoflux
Isothermal/adiabatic (I am leaning towards this)
Isoflux/adiabatic
 
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Wow...I think we're looking at the same book, and I'm surprised this isn't in here. They have good relations for a fully enclosed cavity, which I'm sure you've seen in the next section. They also have a case for flow between concentric cylinders, but nothing about asymmetric heating.

This led me to literature, and I was more surprised on how little I find even in journal papers. The closest I've found so far is FORCED convection between asymmetrically heated plates. I'm going to keep looking for you though.

boy there are a LOT of different types of uniform heating though isn't there?
 
Maybe I can use the enclosure equations as an approximation.
 
That's what I was originally thinking, however the computed Nusselt number can very quite a bit if you assume L/H = 100:1, or 1000:1, etc. This of course affects the convection coefficient. Also, the enclosed space assumes that there will be a complete convection current. In your case of "infinte" parallel plates, I would think that there would be none. There will probably be some swirl, but I wouldn't think that the flow would come "down", so long as both wall temps are higher than the incoming temp.
 
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