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Heat Transfer

Heat Transfer
The most conducive surface for dropwise condensation to occur is the __________ surface.

Coated
Smooth
Oily
Glazed & polished

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Heat Transfer
The overall heat transfer co-efficient for a shell and tube heat exchanger for clean surfaces is U0 = 400 W/m².K. The fouling factor after one year of operation is found to be hd0 = 2000 W/m².K. The overall heat transfer co-efficient at this time is

333W/m².K
894W/m².K
287 W/m².K
1200W/m².K

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

Backward
Forward
Parallel
None of these

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Heat Transfer
Overall thermal resistance for conductive heat transfer through a series of flat resistances is equal to the

Sum of all resistances
Minimum resistance presents in the series
Average of all resistances
Maximum resistance in the series

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Heat Transfer
__________ paint has the minimum absorption co-efficient.

Black
Grey
Light cream
White lead

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Heat Transfer
The average heat transfer co-efficient over the entire length of the plate (ha) and the local heat transfer co-efficient (hL), in case of heat transfer over a flat plate in lminar zone is related as

Ha = 2hL
Ha = hL
Ha= 5hL
Ha = 0.8hL

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