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Heat Transfer

Heat Transfer
Nusselt number for full developed, laminar, constant property flow in a pipe at uniform heat flux is

4.364
83
0.72
18

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Heat Transfer
Radiant energy received by a body is proportional to (where, d = the distance between the object emitting radiation and that receiving it.)

√d
d1.5
d
d2

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Heat Transfer
The average heat transfer co-efficient over the entire length of the plate (ha) and the local heat transfer co-efficient (hL), in case of heat transfer over a flat plate in lminar zone is related as

Ha= 5hL
Ha = 2hL
Ha = hL
Ha = 0.8hL

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Heat Transfer
Steam condensate is recovered by steam traps and recycled for use as boiler feed water, because of its low

Dissolved soilds content
Suspended solids content
Hardness
All of these

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Heat Transfer
In a heat exchanger with steam outside the tubes, a liquid gets heated to 45°C, when its flow velocity in the tubes is 2 m/s. If the flow velocity is reduced to 1 m/s, other things remaining the same, the temperature of the exit liquid will be

Initially decreases and remains constant thereafter
More than 45°C
Equal to 45°C
Less than 45°C

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Heat Transfer
Log mean temperature difference (LMTD) cannot be used, if

heat transfer co-efficient over the entire heat exchanger is not constant
the heat capacity is not constant and there is a phase change.
there exists an unsteady state
none of the listed here

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