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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ head is the most economical for cylindrical vessels designed for operating at high pressure (> 15 atm.).

Conical
Hemispherical
Dished
Ellipsoidal

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Process Equipment and Plant Design
Corrosion allowance in the design of pressure vessel/chemical equipment is not necessary, if

Wall thickness is > 30 mm
Plain carbon steel and cast iron parts are used
Both B & C
Material of construction is high alloy steel

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Process Equipment and Plant Design
The buckling tendency of compression members is always in the direction of the

Least radius of gyration
None of these
Perpendicular to the axis of the load
Axis of the load

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Process Equipment and Plant Design
In actual operation of distillation column, the vapour is not distributed uniformly among the bubble caps, primarily because of the

Lower skirt clearance
Liquid gradient on the tray
Small downcomer liquid seal
Lower static submergence

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Process Equipment and Plant Design
The safe distance of habitation from a hazardous chemical plant (TLV of its product < 1000 ppm) should be about __________ kms.

1
15
5
25

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

Saddle
Skirt
Lug
Bracket

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