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Process Equipment and Plant Design

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

0.55
0.85
0.95
0.75

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Process Equipment and Plant Design
The wall thickness of thin cylindrical shell with hemispherical ends is __________ that of the spherical ends.

Equal to
More than
Less than
Either B or C; depends on maximum permissible internal pressure

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.4-0.9
0.2-0.5
1.2-1.5
0.1-0.2

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

Failure of equipments
Inadequate equipment design
Improper layout of the equipments
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

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

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Process Equipment and Plant Design
Rotary driers are most economically designed for the number of heat transfer units (HTU) from

0.01 to 1
10 to 20
1.5 to 2.5
5 to 10

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