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HEAT TRANSFER

Heat Transfer
All analogy equations connecting friction factor and heat transfer co-efficient apply only to

Form friction
Turbulent flow
Both A and B
Wall or skin friction

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Heat Transfer
The main purpose of providing fins on heat transfer surface is to increase the

Heat transfer co-efficient
Mechanical strength of the equipment
Heat transfer area
Temperature gradient

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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
50
37
45

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Heat Transfer
The rate of heat transfer is a product of overall heat transfer co-efficient, the difference in temperature and the

Nusselt number
Heat transfer area
Heating volume
None of these

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Heat Transfer
Multiple effect evaporation accounts for

Steam economy
Lower operating costs
None of these
Investment economy

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