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The Sieder-Tate correlation for heat transfer in turbulent flow in pipe gives Nu α Re0.8, where, Nu is the Nusselt number and Re is the Reynolds number for the flow. Assuming that this relation is valid, the heat transfer co-efficient varies with the pipe diameter (D) as | |
A. | (D)-1.8 [Wrong Answer] |
B. | (D))-0.2 [Correct Answer] |
C. | (D)0.2 [Wrong Answer] |
D. | (D)1.8 [Wrong Answer] |