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Heat Transfer

Heat Transfer
What is the emissivity of a black body?

0.5
1
0.9

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Heat Transfer
Steam side heat transfer co-efficient in an evaporator is in the range of __________ kcal/hr.m²°C.

100-500
1000-1500
5000-15000
18537

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Heat Transfer
The most conducive surface for dropwise condensation to occur is the __________ surface.

Coated
Oily
Glazed & polished
Smooth

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Heat Transfer
Prandtl and Reynold's analogies are identical for Prandtl number value of

5
0.5
1

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Heat Transfer
The inside heat transfer co-efficient in case of turbulent flow of liquid in the tube side in a 1-2 shell and tube heat exchanger is increased by __________ times, when the number of tube passes is increased to 8.

20.8
20.4
40.4
40.8

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Heat Transfer
For specified tube outside diameter, higher BWG means higher

none of the listed here
tube thickness
cross-sectional area
weight per unit length

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