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Process Equipment and Plant Design

Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.4-0.9
0.1-0.2
1.2-1.5
0.2-0.5

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Process Equipment and Plant Design
Vertical storage vessels are never supported by __________ support.

Skirt
Saddle
Lug
Bracket

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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

1
0
∞
Minimum

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Process Equipment and Plant Design
An underdesigned steam trap will

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

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Process Equipment and Plant Design
For a cylinderical internally pressurised vessel, which of the following closure types would withstand highest pressure, if each closure is of the same material and thickness?

Flat plate
Ellipsoidal (2 : 1)
Hemispherical
Conical

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Process Equipment and Plant Design
Compensation against openings in process vessels for giving inlet and outlet connections, for providing sight glasses and manholes etc. is provided for strength and rigidity. The most efficient type of compensation is of __________ type.

Fluid in
Flared out
Nozzle or rim
Ring plate

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