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Process Equipment and Plant Design

Process Equipment and Plant Design
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

10-12.5
15-20
2.5-3.0
5-7.5

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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
Material of construction is high alloy steel
Both B & C
Plain carbon steel and cast iron parts are used

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Process Equipment and Plant Design
Two iron pipes of the same nominal diameter but different schedule numbers will have the same

Inside diameter
None of these
Wall thickness
Outside diameter

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Process Equipment and Plant Design
Bubble cap plate column is

A differential stage contactor
A continuous contactor
A finite stage contactor
Used only for distillation, not for absorption

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Process Equipment and Plant Design
If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

Increase by 21.6
Decrease by 22
Increase by 1.8
None of these

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

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

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