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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

0.85
0.75
0.55
0.95

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Process Equipment and Plant Design
For storing hazardous chemicals in large storage tanks, the minimum safe distance between the two tanks should range between __________ times the tank diameter.

2.5 to 3.5
6 to 8
1 to 1.5
4 to 5

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Process Equipment and Plant Design
Generally, as the length of the liquid path on a tray is increased beyond 5 ft, the overall column efficiency

Remains same
Decreases
May increase or decrease depending upon the plate spacing
Increases

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Process Equipment and Plant Design
Normal screwed fittings are used for pipes upto a diameter of __________ inches.

5
7
1.5
3

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Process Equipment and Plant Design
Theoretically calculated diameter of the stripping section of the continuous rectification column is __________ that of the enriching section.

Less than
More than
Either more or less (depending upon relative volatility)
Same as

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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.

1
5
25
15

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