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Heat Transfer

Heat Transfer
In a single effect evaporator, the economy is

None of these
< 1
1
> 1

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Heat Transfer
The heat flux in the nucleate boiling regimes is proportional to (where, ΔT = excess temperature)

√(ΔT)
(ΔT)⁴
(ΔT)²
(ΔT)³

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Heat Transfer
Hot water (0.01 m³ /min) enters the tube side of a counter current shell and tube heat exchanger at 80°C and leaves at 50°C. Cold oil (0.05 m³/min) of density 800 kg/m³ and specific heat of 2 kJ/kg.K enters at 20°C. The log mean temperature difference in °C is approximately

37
50
32
45

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Heat Transfer
The sum of reflectivity and absorptivity for an opaque body is equal to

1
2
0.5

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Heat Transfer
Bulk of the convective heat transfer resistance from a hot tube surface to the fluid flowing in it, is

Uniformly distributed throughout the fluid
None of these
In the central core of the fluid
Mainly confined to a thin film of fluid near the surface

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Heat Transfer
Which characteristic of a fluid is not important in deciding its route in a shell and tube heat exchanger?

None of these
Corrosiveness
Viscosity
Fouling characteristic

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