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Process Equipment and Plant Design

Process Equipment and Plant Design
In hydrostatic testing of welded pipe (for leakage, strength etc.) the ratio of minimum hydrostatic test pressure to internal design pressure is around

1.5
0.5
3.5
2.5

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Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

Thin shperical (e.g. Horton sphere)
Horizontal
Thick walled vertical
None of these

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Process Equipment and Plant Design
If 'D' is the inside diameter of the shell of a shell and tube heat exchanger, then the baffle spacing is usually in the range of

D/5 or minimum 2" to D
None of these
D/5 or minimum 2" to 5D
D/2 or minimum 2" to 5D

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Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.75
0.95
0.85
0.55

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

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

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

Large horizontal cylindrical
Thick walled tall
Small
Tall but empty

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