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Heat Transfer

Heat Transfer
In forced convection, the Nusselt number is a function of

Re and Gr
Re and Pr
Pr and Gr
Re and Sc

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Heat Transfer
The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe whose surface temperature remains constant is

88.66
Dependent on NRe only
3.66
1.66

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Heat Transfer
In a shell and tube heat exchanger, the shell side fluid velocity can not be changed by changing the

Tube pitch
No. of baffles
Tube diameter
Tube layout

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Heat Transfer
The thickness of condensate layer in filmwise condensation depends on the

Liquid flow rate from the surface
All of these
Surface configuration
Condensation rate

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Heat Transfer
Fresh orange juice contains 12% (by weight) solids and the rest water 90% of the fresh juice is sent to an evaporator to remove water and subsequently mixed with the remaining 10% of fresh juice. The resultant product contains 40% solids. The kg of water removed from 1 kg fresh juice is

0.5
0.7
0.6
0.4

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Heat Transfer
Film boiling is usually not desired in commercial equipments, because

the heat transfer rate is low in view of the large temperature drop. @
it is difficult to maintain
none of the listed here
it is not economic

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