Heat transfer rate through the wall of a circular tube with convection acting on the outer surface is given per unit of its length by
where i refers to the innertube surface and o the outer tube surface. Increasing r0 will reduce the heat transfer as long as
(a) r0
(b) r0 = k/h
(c) r0> k/h
(d )r0> 2k/h
(e) Increasing r0 will always reduce the heat transfer.
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