201. In a laboratory test run, the rate of drying was found to be 0.5 x 10-3 kg/m2.s, when the moisture content reduced from 0.4 to 0.1 on dry basis. The critical moisture content of the material is 0.08 on a dry basis. A tray dryer is used to dry 100 kg (dry basis) of the same material under identical conditions. The surface area of the material is 0.04 m2/kg of dry solid. The time required (in seconds) to reduce the moisture content of the solids from 0.3 to 0.2 (dry basis) is
202. In a liquid-liquid heat exchanger, for the same process temperature, the ratio of the LMTD in parallel flow to the LMTD in counter flow is always
203. In a multipass shell and tube heat exchanger, tube side return pressure loss is equal to _________ the velocity head.
204. In a multiple effect evaporator, the effect of boiling point elevation is to
205. In a parallel flow heat exchanger, if the outlet temperature of hot and cold fluids are the same, then the log mean temperature difference (LMTD) is
206. In a shell and tube heat exchanger, floating head is used for
207. In a shell and tube heat exchanger, putting a longitudinal baffle across the shell, forces the shell side fluid to pass _________ through the heat exchanger.
208. In a shell and tube heat exchanger, square pitch compared to triangular pitch
209. In a shell and tube heat exchanger, the height of 25 percent cut baffles is equal to (where, D = inside diameter of shell).
210. In a shell and tube heat exchanger, the shell side fluid velocity can‟t be changed by changing the