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Heat Transfer

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

√(ΔT)
(ΔT)³
(ΔT)⁴
(ΔT)²

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Heat Transfer
The inside heat transfer co-efficient in case of turbulent flow of liquid in the tube side in a 1-2 shell and tube heat exchanger is increased by __________ times, when the number of tube passes is increased to 8.

20.4
40.8
40.4
20.8

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Heat Transfer
Nucleate boiling is promoted

On rough surfaces
On polished surfaces
In the absence of agitation
None of these

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Heat Transfer
When warm and cold liquids are mixed, the heat transfer is mainly by

conduction
convection
none of the listed here
radiation

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Heat Transfer
Steam side heat transfer co-efficient in an evaporator is in the range of __________ kcal/hr.m²°C.

5000-15000
1000-1500
100-500
18537

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Heat Transfer
The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe, where the wall heat flux is constant, is

2.36
Dependent on NRe only
4.36
120.36

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