341. The advantage of using a 1 - 2 shell and tube heat exchanger over a 1 - 1 shell and tube heat exchanger is
342. The average heat transfer co-efficient for laminar film condensation on vertical surface is inversely proportional to (where, ΔT = Temperature drop across condensate film)
(ΔT)1/4
343. The average heat transfer co-efficient over the entire length of the plate (ha) and the local heat transfer co-efficient (hL), in case of heat transfer over a flat plate in laminar zone is related as
ha = 2hL
344. The capacity of double-effect evaporator is less than half of the capacity of two single effects, each of which is operating over same terminal temperature difference, when the
345. The characteristic dimensionless groups for heat transfer to a fluid flowing through a pipe in laminar flow are
346. The critical radius 'r' of insulation on a pipe is given by
347. The critical radius of insulation for a spherical shell is (where, K = thermal conductivity of insulating material h0 = heat transfer coefficient at the outer surface)
2K/h0
348. The critical radius of insulation for cylindrical pipe is (where, hi = heat transfer coefficient at inside of the pipe)
K/h0
349. The dimensionless group in mass transfer that is equivalent to Prandtl number in heat transfer is
350. The Dittus-Boelter equation for convective heat transfer [(i.e. h = 0.023 (K/D) (Re)0.8 (Pr)0.8] cannot be used for