Heat Transfer
Overall heat transfer co-efficient for cooling of hydrocarbons by water is about

50 -100 W/m² . °K
50 -100 BTU/hr. ft.2°F
1000 - 1500 BTU/hr. ft.2°F
50 -100 Kcal/hr.m².°C

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Heat Transfer
A dilute aqueous solution is to be concentrated in an evaporator system. High pressure steam is available. Multiple effect evaporator system is employed, because

Boiling point elevation in a single effect system is much higher than that in any effect in a multieffect system
Total amount of vapor produced per Kg of feed steam in a multiple effect system is much higher than in a single effect
Total heat transfer area of all the effects is -less than that in a single effect evaporator system
Heat transfer co-efficient in a single effect is much lower than that in any effect in a multieffect system

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