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Heat Transfer

Heat Transfer
Prandtl number for most of dry gases is about

150
0.72
0.001
70

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Heat Transfer
Heat sensitive materials can be concentrated in an evaporator employing

High residence time
Vacuum
None of these
High pressure

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Heat Transfer
With increase in temperature, the thermal conductivity of most liquids

Remains same
Increases
Decreases
First increases upto a certain temperature and then becomes constant

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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
d2
√d
d1.5

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Heat Transfer
The non-dimensional temperature gradient in a liquid at the wall of a pipe is the

Heat flux
Prandtl number
Nusselt number
Schmidt number

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Heat Transfer
Air is best heated with steam in a heat exchanger of

plate type
double pipe type with fin on steam side
shell and tube type
double pipe type with fin on air side

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