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

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

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Heat Transfer
For a multipass shell and tube heat exchanger, the LMTD correction factor is always

Between 1 & 2
> 1
< 1
1

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Heat Transfer
Double pipe heat exchangers are preferably useful, when

Requirement of heat transfer area is low
High viscosity liquid is to be cooled
Overall heat transfer co-efficient is very high
A corrosive liquid is to be heated

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Heat Transfer
The interchange factor for radiation heat transfer from surface 'x' to surface 'y' in case of an infinite parallel planes with emis-sivities εx & εy is given by

Εx . εy
(εx + εy)/(εx + εy - εx . εy)
1/εx + 1/εy
Εx + εy

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Heat Transfer
Peclet number (Pe) is given by

Pe = Re.Pr
Pe = Nu.Re
Pe = Pr/Re
Pe = Re/Pr

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MORE MCQ ON Heat Transfer

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