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Heat Transfer

Heat Transfer
Steam consumption in kg/hr in case of an evaporator is given by (where, C & E are capacity the economy of the evaporator respectively)

C/E
E/C
CE
1/CE

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Heat Transfer
For evaporation of viscous solution in a multiple effect evaporator, the prefered feeding scheme is

Backward
Forward
Parallel
None of these

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Heat Transfer
Hot water (0.01 m³ /min) enters the tube side of a counter current shell and tube heat exchanger at 80°C and leaves at 50°C. Cold oil (0.05 m³/min) of density 800 kg/m³ and specific heat of 2 kJ/kg.K enters at 20°C. The log mean temperature difference in °C is approximately

32
37
45
50

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Heat Transfer
One kilogram of water at 0°C is changed to superheated steam of one atm pressure and 300° C. The major heat consumption in the process will be to

Heat the water from 0°C to 100°C
Data insufficient, can
Evaporate the water
To superheat the steam

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Heat Transfer
The advantage of using a 1 - 2 shell and tube heat exchanger over a 1 - 1 shell and tube heat exchanger is

Lower tube side pressure drop
Lower shell side pressure drop
Higher tube side heat transfer co-efficient
Higher shell side heat transfer co-efficient

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

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