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Heat Transfer

Heat Transfer
The units of resistance to heat transfer is

W⁻¹m²K
J.m⁻².K⁻¹
W.m⁻².K⁻¹
J.m⁻¹.K⁻¹

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Heat Transfer
The film co-efficient is decreased due to the presence of non-condensing gases in the vapors. The film co-efficient of superheated vapor as compared to that of saturated vapor is

Less
More
Either more or less ; depends on the nature of vapor
Some

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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.

20.4
40.8
20.8
40.4

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Heat Transfer
The film thickness for laminar film condensation on vertical surface __________ from top to bottom.

Cummulatively decreases
Remains constant
Cummulatively increases
And the surface conductance increase

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Heat Transfer
Maximum water velocity in tubes of a 1-2 shell and tube heat exchanger may be around __________ metres/second.

1
20
10
30

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

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

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