Heat Transfer
Economy of a multiple effect evaporator is not influenced much by the

boiling point elevations
rate of heat transfer
ratio of the weight of the thin liquor to thick liquor
temperature of the feed

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Heat Transfer
Baffle spacing

Should be less than the inside diameter of the shell
Is not the same as baffle pitch
Should be less than one fifth the diameter of the shell
None of these

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Heat Transfer
1000 Kg of liquid at 30°C in a well stirred vessel has to be heated to 120°C, using immersed coils carrying condensing steam at 150°C. The area of the steam coils is 1.2 m² and the overall heat transfer co-efficient to the liquid is 1500 W/m².°C. Assuming negligible heat loss to the surrounding and specific heat capacity of the liquid to be 4 kJ/kg.°C, the time taken for the liquid to reach desired temperature will be

22 min
44 min
51 min
15 min

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