91. A coalescer in a mixer-settler liquid-liquid extraction coloumn
92. Tower diameter may be decreased by
93. In a moderately sized packed absorption tower, channeling (which is most severe with stacked packings) can be minimised by taking the ratio of tower diameter to packing diameter
94. Flash distillation is suitable for the separation of components
95. Make up water is required in a cooling tower to replace the water lost by
96. In an absorber, HETP does not vary with the
97. Use of natural draft cooling tower is practised, when the air has low
98. Raoult's law applies to the
99. The difference of wet bulb temperature and adiabatic saturation temperature of unsaturated mixture of any system is
100. Which of the following can be calculated theoretically using steam table and Dalton's law of partial pressure; if the relative humidity and dry bulb temperature of moist air is known?
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