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Process Equipment and Plant Design

Process Equipment and Plant Design
The difficulty of liquid distribution in packed towers is accentuated, when the ratio of tower diameter to packing diameter is

> 20 < 50
< 7
> 7 < 15
< 30

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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 = 1/G0.6
Δp = G2
Δp = G
Δp = G0.5

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Process Equipment and Plant Design
Bubble cap plate column is

Used only for distillation, not for absorption
A continuous contactor
A finite stage contactor
A differential stage contactor

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Process Equipment and Plant Design
An underdesigned steam trap will

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

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Process Equipment and Plant Design
Pressure drop per tray in the atmospheric distillation column is about __________ psi.

0.01 - 0.5
0.5 - 1.0
0.07 - 0.12
43833

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Process Equipment and Plant Design
Joint efficiency (J) for a seamless pipe is

< 0.5
0.85
1.2
1

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