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Heat Transfer

Heat Transfer
At what value of Prandtl number, the hydrodynamic and thermal boundary layers are identical?

0.5
1
1.5
80

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Heat Transfer
Nusselt number for full developed, laminar, constant property flow in a pipe at uniform heat flux is

4.364
18
0.72
83

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Heat Transfer
With increase in temperature, the thermal conductivity of most liquids

Remains same
Increases
First increases upto a certain temperature and then becomes constant
Decreases

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Heat Transfer
Sensible heat of hot industrial flue gases can not be recovered by a/an

Regenerator
Ceramic recuperator
Economiser
None of these

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Heat Transfer
Heat produced when a steady state current, I passes through an electrical conductor having resistance, 'R' is

IR2
I2R
IR
None of the listed here

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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 diameter
Tube layout
Tube pitch
No. of baffles

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