An existing forced-circulation evaporator with a heat-transfer area of 232 m2 is to be used to concentrate 44 wt% NaOH to 65 wt% NaOH using steam at 3 atm gage (barometer reads 1 atm). The feed temperature will be 40oC and pressure in the vapor space of the evaporator will be 2.0 psia. The overall heat-transfer coefficient for the given conditions is estimated to be 2,000 W/m2 - oC. The density of the feed solution is 1,450 kg/m3 . Neglecting heat losses from the evaporator, determine the: (a) temperature of the solution in the evaporator in oC; (b) heating steam in kg/h; (c) m3 /h of feed; (d) kg/ h of concentrated NaOH solution; (e) rate of evaporation in kg/h.
An existing forced-circulation evaporator with a heat-transfer area of 232 m2 is to be used to concentrate 44 wt% NaOH to 65 wt% NaOH using steam at 3 atm gage (barometer reads 1 atm). The feed temperature will be 40oC and pressure in the vapor space of the evaporator will be 2.0 psia. The overall heat-transfer coefficient for the given conditions is estimated to be 2,000 W/m2 - oC. The density of the feed solution is 1,450 kg/m3 . Neglecting heat losses from the evaporator, determine the: (a) temperature of the solution in the evaporator in oC; (b) heating steam in kg/h; (c) m3 /h of feed; (d) kg/ h of concentrated NaOH solution; (e) rate of evaporation in kg/h.
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