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| 1. |
The Sieder-Tate correlation for heat transfer in turbulent flow in pipe gives Nu α Re^0.8, 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 |
| B. | (D)^-0.2 |
| C. | (D)^0.2 |
| D. | (D)^1.8 |
| Answer» C. (D)^0.2 | |