c_p = 4.191 KJ/(kh*K)
rho = 976.6 kg/m^3
µ = 3.89*10^-4 (N*s)/m^2
Assume that the water flow within the tube is fully developed.
(1) Determine the average overall heat transfer coefficient, U, with respect to the inner surface area of the tube.
(2) Is the water flow laminar or turbulent?
(3) If the flow rate is doubled, determine the new exit mean (bulk) temperature, T_m,o.
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