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

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

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Heat Transfer
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

6000
2000
5000
4000

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