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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

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

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Process Equipment and Plant Design
Shortest distance between two tubes is

Called tube pitch
Called tube clearance
None of these
More in case of triangular pitch as compared to square pitch of tube layout

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Process Equipment and Plant Design
The slope of operating line in the rectifying section of a distillation column is unity, if the reflux ratio is

∞
0
Minimum
1

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Process Equipment and Plant Design
A 'rupture disc' is provided in chemical equipments as an accessory meant for

Relieving excess pressure
Creating turbulence
Enhancing mixing rate
Avoiding vortex formation

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Process Equipment and Plant Design
For high pressure process equipments/vessels, the connected nozzle should be

Flanged
Screwed
Brazed
Welded

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Be fabricated very easily
Withstand higher pressure for a given metallic shell thickness
Be designed without wind load considerations
Be supported very easily

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