Heat Transfer
Reason for operating an evaporator in multiple effect is to secure

Decreased steam consumption
Increased steam economy
Both A and B
Increased capacity

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Heat Transfer
A process stream of dilute aqueous solution flowing at the rate of10 Kg.s⁻¹ is to be heated. Steam condensate at 95°C is available for heating purpose, also at a rate of 10 Kg.s⁻¹. A 1 - 1 shell and tube heat exchanger is available. The best arrangement is

Counter flow with process stream on shell side
Parallel flow with process stream on tube side
Counter flow with process stream on tube side
Parallel flow with process stream on shell side

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Heat Transfer
In a shell and tube heat exchanger,

There is no relationship between temperature drop and resistance
The temperature drops in the two fluids and the wall are proportional to individual resistances
The temperature drop is inversely proportional to the resistance across which the drop occurs
The relationship is not generalised

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