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Heat Transfer

Heat Transfer
The unit of heat transfer co-efficient in SI unit is

J/M2°K
J/m°K
W/m2°K
W/m°K

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Heat Transfer
In a shell and tube heat exchanger, the tube side heat transfer co-efficient just at the entrance of the tube is

Zero
Same as average heat transfer co-efficient for tube side
Infinity
None of these

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Heat Transfer
Open pan evaporators are preferred to be used, when the solution to be concentrated is

Corrosive
Scaling
Highly viscous
Salty

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Heat Transfer
In case of heat flow by conduction for a cylindrical body with an internal heat source, the nature of temperature distribution is

None of these
Parabolic
Linear
Hyperbolic

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Heat Transfer
The Sieder-Tate correlation for heat transfer in turbulent flow in pipe gives Nu α Re0.8, where, Nu is the Nusselt number and Re is the Reynolds number for the flow. Assuming that this relation is valid, the heat transfer co-efficient varies with the pipe diameter (D) as

(D)1.8
(D)-1.8
(D)-0.2
(D)0.2

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Heat Transfer
With increase in porosity, the thermal conductivity of a solid substance

Decreases
May increase or decrease; depends on the solid
Increases
Remains unchanged

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