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Heat Transfer

Heat Transfer
According to Reynolds analogy, Stanton number is equal to (where, f = Fanning friction factor)

f
f/4
2f
f/2

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Heat Transfer
Calburn analogy is applicable for the value of Prandtl number from

0.001 to 1
120 to 400
0.6 to 120
0.5 to 5

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Heat Transfer
For large heat transfer area requirement, shell and tube heat exchanger is preferred, because it

Is easy to operate and maintain
All of these
Occupies smaller space
Is more economical

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Heat Transfer
The thickness of condensate layer in filmwise condensation depends on the

Condensation rate
All of these
Surface configuration
Liquid flow rate from the surface

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Heat Transfer
Indirect contact heat exchangers are preferred over direct contact heat exchangers, because

Cost of equipment is lower
There is no risk of contamination
There is no mist formation
Heat transfer co-efficient are high

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Heat Transfer
For a perfectly transparent surface (like gases), the

All of these
Reflectivity = 0
Absorptivity = 0
Transmissivity = 1

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MORE MCQ ON Heat Transfer

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