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Heat Transfer

Heat Transfer
Evaporator tubes are generally

Vertical
Inclined
Random
Horizontal

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Heat Transfer
While the total emissivity of a perfect black body is unity, the same for a real body is

1
between 0 and 1
0
>1

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Heat Transfer
For flow over a flat plate, the ratio of thermal boundary layer thickness, 'xt' and hydrodynamic boundary layer thickness 'x' is equal to (where, NPr = Prandtl number)

NPr-1/3
NPr
NPr1/3
NPr-1

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Heat Transfer
In case of a supercooled solution, which is on the verge of crystallisation, the free energy of the solution as compared to that of the solid is

Less
Same
More
More or less; depends on the nature of solution

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Heat Transfer
In SI units, thermal conductivity is expressed in

Watt/m². °K
Watt/m4. °K
Watt/m.°K
Watt/m². °K

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Heat Transfer
Dropwise condensation of steam on cooling surface is promoted

An oily surface
Only in presence of air
None of these
When both the steam and the tube are clean

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MORE MCQ ON Heat Transfer

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