Unformatted text preview: function of axial position x, mean inlet temperature T mi , tube perimeter P, tube length L, mass flowrate m and specific heat c p . Clearly draw the differential control volume, labelling x, dx, x+dx, and all heat transfer rates. 3. For fullydeveloped forced convection through a tube with a uniform wall heat flux q s ”, from a differential control volume, derive the mean temperature in the tube T(x) as a function of axial position x, mean outlet temperature T mo , tube perimeter P, tube length L, mass flowrate m and specific heat c p . Clearly draw the differential control volume, labelling x, dx, x+dx, and all heat transfer rates....
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 Fall '08
 Kuznetsov
 Heat, Heat Transfer, 40°C, 1.5m, 4°C, 0.6 m/s

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