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Process Equipment and Plant Design

Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

4 to 8
3 to 12.5
12.5 to 18.5
L to 3

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Process Equipment and Plant Design
Generally, as the length of the liquid path on a tray is increased beyond 5 ft, the overall column efficiency

Decreases
Increases
Remains same
May increase or decrease depending upon the plate spacing

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Process Equipment and Plant Design
Liquid/petroleum fuel storage tanks are built underground (as in case of petrol pumps), when the storage capacity is less than __________ kilolitres.

20
30
85
45

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Process Equipment and Plant Design
An underdesigned steam trap will

None of these
Back up condensate and cause water hammer in steam line
Destroy itself of acceleration wear due to rapid recycling
Waste steam

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Process Equipment and Plant Design
Pressure drop (Δp) and the superficial gas mass velocity (G) in case of packed absorption tower operating in the preloading range are related as

Δp = G0.5
Δp = G2
Δp = G
Δp = 1/G0.6

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Process Equipment and Plant Design
An increase in the liquid resistance to interphase mass transfer and a resultant reduction in plate efficiency is caused by

Decrease in gas solubility for absorbers
An increase in relatived volatility for rectification columns
An increase in liquid viscosity
All of these

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