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Heat Transfer

Heat Transfer
Temperature profile in steady state heat transfer is

none of the listed here
hyperbolic
parabolic
Linear

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Heat Transfer
The wavelength at which the maximum monochromatic emissive power occurs for a black body, is (where, T = absolute temperature of the black body)

αT
α T⁴
α 1/T
Independent of T

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Heat Transfer
A composite wall consists of two plates A and B placed in series normal to the flow of heat. The thermal conductivities are kA and kB and the specific heat capacities are CPA and CPB for plates A and B respectively. Plate B has twice the thickness of plate A. At steady state, the temperature difference across plate A is greater than that across plate B, when

CPA < CPB
CPA > CPB
KA < 0.5kB
KA>2 kB

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Heat Transfer
As the difference between the wall temperature and bulk temperature increases, the boiling heat transfer co-efficient

goes through a maximum.
continues to decrease
goes through a minimum
continues to increase

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Heat Transfer
Shell side pressure drop in a shell and tube heat exchanger does not depend upon the

Viscosity, density & mass velocity of shell side fluid
Baffle spacing & shell diameter
None of these
Tube diameter & pitch

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Heat Transfer
When does the heat generated by fluid friction becomes appreciable compared to the heat transferred between the fluids?

None of these
At high fluid velocity
When fluid flows past a smooth surface
At low velocity

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MORE MCQ ON Heat Transfer

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