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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ strain is measured using a 'strain rosetter'.

None of these
Volumetric
Linear
Shear

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Process Equipment and Plant Design
In a shell and tube heat exchanger, tube side __________ of the mass velocity.

Neither A nor B
Both A & B
Heat transfer co-efficient is proportional to 0.8th power
Pressure drop is proportional to the square

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Process Equipment and Plant Design
Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

Is of high specific gravity
Containing suspended solids flows at low velocity
Containing suspended solids flows at high velocity
Is highly viscous

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Process Equipment and Plant Design
In the downcomer of a distillation column, the minimum recommended residence time is about __________ seconds.

5
2.5
17.5
12.5

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Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

8
2
4
1/2

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Process Equipment and Plant Design
Le/D for fully open gate valves would be

Around 7
Both B and C
Much more than that for fully open globe valves
Much less (say 2% than that for fully open globe valves)

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