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Process Equipment and Plant Design

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 = G
Δp = G2
Δp = 1/G0.6
Δp = G0.5

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Process Equipment and Plant Design
Brass valves are usually made for pipe sizes __________ inches.

>2.5
?1
>3.5
?2

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Process Equipment and Plant Design
Le/D for 90° elbow (medium radius) and 90°square elbow would be respectively around

3 and 5
250 and 600
25 and 60
100 and 250

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

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

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Process Equipment and Plant Design
Power required for agitation depends upon the

Height & properties of the liquid
Size of agitator & the tank
Agitator type & speed of agitation
All of these

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Process Equipment and Plant Design
The operating velocity in the absorption tower is usually 40-50% of the flooding velocity. Packed absorption towers are normally designed for a pressure drop of about __________ mm of water column per metre height of packing.

43835
100-150
1000-1500
20-40

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