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Process Equipment and Plant Design

Process Equipment and Plant Design
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

One-fourth of
1.25-1.50 times
2.5 times
Less than

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Process Equipment and Plant Design
Speed of industrial paddle agitator ranges from __________ rpm.

500 to 750
20 to 100
1000 to 2000
1 to 5

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Process Equipment and Plant Design
For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

D1/(d1 + d2)
D2/(d1 + d2)
(d1 + d2)/d1
(d1 + d2)/d2

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Process Equipment and Plant Design
The minimum plate spacing in most of the pertroleum refinery distillation columns (of dia > 3 ft) is normally __________ inches.

6
34
18
12

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Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.60-0.90
0.5-0.65
0.15-030
0.75-0.85

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

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

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