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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
Thin spherical shells subjected to internal pressure, develop __________ stresses.

Circumferential
Both A & B
Neither A nor B
Radial

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Process Equipment and Plant Design
Hazards associated with the relief valve leakage for extremely hazardous material storage can be taken care of by providing

None of these
Surge chamber
Rupture diaphragm
Dikes

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Process Equipment and Plant Design
Wall thickness of schedule 40 pipe as compared to that of schedule 80 pipe is

More
Less
Same
Cither A or B; depends upon the I.D. of the pipe

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Process Equipment and Plant Design
Accidents in chemical plants are mostly due to

Improper layout of the equipments
Failure of equipments
Faulty operating procedures
Inadequate equipment design

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Process Equipment and Plant Design
__________ is the determining factor for the number of bubble caps to be used per tray.

Permissible slot velocity
Vapor load
Tray diameter
Liquid load

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