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Heat Transfer

Heat Transfer
In forced convection, the heat transfer depends on

Re, Gr
mainly Gr
Re, Pr
none of the listed here

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Heat Transfer
The ratio of velocity head to tube side return loss in case of a multipass shell and tube heat exchanger is

4
43832
2
43834

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Heat Transfer
The heat transfer by radiation from a mild steel surface is to be reduced by reducing the emissivity of the surface. This can be best achieved by

Painting the surface white (with aluminium paint)
Roughening the surface
Giving the surface a mirror finish
Painting the surface black

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Heat Transfer
When warm and cold liquids are mixed, the heat transfer is mainly by

conduction
radiation
convection
none of the listed here

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Heat Transfer
The overall heat transfer co-efficient for a shell and tube heat exchanger for clean surfaces is U0 = 400 W/m².K. The fouling factor after one year of operation is found to be hd0 = 2000 W/m².K. The overall heat transfer co-efficient at this time is

1200W/m².K
287 W/m².K
333W/m².K
894W/m².K

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Heat Transfer
Value of Nusselt number [Nu = (hD/k)] for the heat transfer by conduction from a droplet or a spherical particle to a surrounding stagnant film is

0.5
100
10
2

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MORE MCQ ON Heat Transfer

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