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Process Equipment and Plant Design

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

Inside diameter
Wall thickness
None of these
Outside diameter

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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
Inadequate equipment design
Faulty operating procedures

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Process Equipment and Plant Design
Wind load consideration in the design of a support can be neglected, when the vessel is

Tall but empty
None of these
Tall (say 30 metres), but is full of liquid
Short (< 2 m) and housed indoor

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Process Equipment and Plant Design
What is the slope of the operating line in the rectifying section of a distillation coloumn?

∞
> 1

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Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Thick walled tall
Tall but empty
Large horizontal cylindrical
Small

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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.

15
5
25
1

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