Fully Developed Flow between two parallel plates

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The discussion focuses on solving a practice exam problem involving fully developed flow between two parallel plates, one with constant heat flux and the other insulated. The velocity profile has been established, but there is confusion regarding the appropriate equations for temperature distribution due to the specific boundary conditions. Participants suggest starting with the governing equations and applying boundary conditions, emphasizing that the insulated plate results in zero heat flux. It is noted that in fully developed flow, only the diffusion term perpendicular to the plates should remain, as there are no gradients in the flow direction. The conversation highlights the importance of carefully considering the effects of viscous dissipation based on the scenario.
JasonB_VT
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Hey you all,

I have a practice exam problem which is causing some difficulty for me.

Basically I have a fully developed flow through two parallel plates. One plate has a constant heat flux and the other plate is heavily insulated.

I have found the velocity profile: U=2*Uinf*(1-r^2/h^2)
where h is the radius.

Now I have set up the boundary condition to solve the differential equation but I'm confused on which equation to use. There is a general equation (I would post it here but its too messy) that will solve temperature distributions in a tube. With these equations, however, there is either a constant temperature or constant flux around the whole boundary.

I am confused on how to go about solving this problem, any advice will help! Thank you.
 
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You can basically start with governing equations. Start canceling out terms until you're left with a differential equation that you can solve.

For example, you can show that radial velocity = 0; you know that d/dz = 0 as well.
 
Like minger mentioned start with the governing equation and then apply the boundary conditions. Which in your case would be constant heat flux at both boundaries. Heavily insulated means no heat flux which is a constant heat flux of 0.

If the flow is fully developed for both velocity and temperature between two plates you should only be left with the diffusion term perpendicular to the plates because there is no temperature gradient in the flow direction and no velocity component perpendicular to the plates. The only other thing to consider would be viscous dissipation but I guess it depends on the situation whether or not you want to keep that term.
 
My idea is that I want to use immerse Whitetail Antlers in a fishtank to measure their volumetric displacement (the Boone and Crockett system is the current record measurement standard to place in a juxtaposition with) I would use some sight glass plumbed into the side of the tank to get the change in height so that I can multiply by the tank cross-section. Simple Idea. But... Is there a simple mechanical way to amplify the height in the sight glass to increase measurement precision...

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