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Heat Transfer

Heat Transfer
Value of Prandtl number for water ranges from

L to 2
1000 to 2000
100 to 500
5 to 10

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Heat Transfer
For a fluid flowing in an annulus space, the wetted perimeter for heat transfer and pressure drop are

Linearly related
Never different
Different
Same

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Heat Transfer
For evaporation of viscous solution in a multiple effect evaporator, the prefered feeding scheme is

None of these
Forward
Backward
Parallel

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Heat Transfer
Heat flux through several resistances in series in analogous to the current flowing through several.

resistances in series
none of the listed here
capacitors in series
resistances in parallel

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Heat Transfer
The energy radiated from a surface Q at absolute temperature T is related as

None of these
Q ∝ T⁴
Q ∝ T²
Q ∝ T³

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Heat Transfer
Extremely large or small volumes of fluids are generally best routed through the shell side of a shell and tube heat exchanger, because of the

High heat transfer co-efficient
Less corrosion problems
Low pressure drop
Flexibility possible in the baffle arrangement

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