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
To superheat the steam
Data insufficient, can
Evaporate the water

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Heat Transfer
If Prandtl number is greater than the Schmidt number, then the

none of the listed here
thermal & concentration boundary layers are of equal thickness
thermal boundary layer lies inside the concentration boundary layer
concentration boundary layer lies inside the thermal boundary layer

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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
Temperature of the incoming vapor is very high
Higher condensing film co-efficient is desired
Condensate is corrosive in nature

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Heat Transfer
Extended heat transfer surface like fins are used to increase the heat transfer rate. Fin efficiency is defined as the ratio of heat transferred across the fin surface to the theoretical heat transfer across an equal area held at the

Temperature of the fin end
Average temperature of the fin
Constant temperature equal to that of the base
Surrounding temperature

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