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Heat Transfer

Heat Transfer
With increase in temperature, the total emissivity of conductors

Decreases
Remains same
Decreases linearly
Increases

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Heat Transfer
All analogy equations connecting friction factor and heat transfer co-efficient apply only to

Turbulent flow
Both A and B
Wall or skin friction
Form friction

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Heat Transfer
In counter flow compared to parallel flow,

LMTD is greater
More surface area is required for a given heat transfer rate
Less surface area is required for a given heat transfer rate
Both A and B

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Heat Transfer
A composite flat wall of a furnace is made of two materials 'A' and 'B'. The thermal conductivity of 'A' is twice of that of material 'B', while the thickness of layer of 'A' is half that of B. If the temperature at the two sides of the wall are 400 and 1200°K, then the temperature drop (in °K) across the layer of material 'A' is

133
125
150
160

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Heat Transfer
The Nusselt number for fully developed (both thermally and hydrodynamically) laminar flow through a circular pipe, where the wall heat flux is constant, is

Dependent on NRe only
120.36
2.36
4.36

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Heat Transfer
Increasing the liquor level in the evaporator results in the

increased true temperature drop
increase in liquor film co-efficient
decreased capacity
decreased effect of hydrostatic head

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MORE MCQ ON Heat Transfer

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