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Heat Transfer

Heat Transfer
Peclet number (Pe) is given by

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

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Heat Transfer
The capacity of double-effect evaporator is less than half of the capacity of two single effects, each of which is operating over same terminal temperature difference, when the

Evaporators operate under vacuum
None of these
Solution has an elevation of boiling point
Evaporators opreate at atmospheric pressure

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Heat Transfer
For a counter current heat exchanger with Tih = 80°C, T°c = 60°C, T°h = 50°C and Tic = 30°C, and the temperature difference between the two streams being the same everywhere along Z, the direction of flow of hot fluid. The temperature profile should satisfy

dT/dZ = 0
d²T/dZ² = 0
d²T/dZ² > 0
d²T/dZ² < 0

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Heat Transfer
With increase in temperature, the thermal conductivity of steel

Increases
Increases exponentially
Decreases
Remains unchanged

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Heat Transfer
A concentric double pipe heat exchanger as compared to the shell and tube heat exchanger for the same heat load requires

None of these
Lower maintenance cost
Less heating surface
More space

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Heat Transfer
In a backward feed multiple effect evaporator

None of these
No pumps are required between successive effects
Feed is introduced in the first effect
Feed flows from low pressure to high pressure

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