Heat Transfer
In a forward feed multiple effect, the pressure build up will be

highest at the inlet of the last effect
least at the inlet of the first effect
highest at the outlet of the last effect
least at the outlet of the last effect

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Heat Transfer
In a shell and tube heat exchanger,

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

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Heat Transfer
Condensing film co-efficient for steam on horizontal tubes ranges from 5000 to 15000 Kcal/hr.m² .°C. Condensation of vapor is carried out inside the tube in a shell and tube heat exchanger, when the

Lower pressure drop through the exchanger is desired
Condensate is corrosive in nature
Higher condensing film co-efficient is desired
Temperature of the incoming vapor is very high

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