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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

None of these
Bubble cap plate
Packed
Sieve plate

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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.

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

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Process Equipment and Plant Design
The stress developed in a material without any permanent set is called the

Ultimate stress
Yield stress
Breaking stress
Elastic limit

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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.

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

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

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

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Process Equipment and Plant Design
The distance between the top of the slots and the liquid surface when the static liquid is just ready to flow over the overflow weir is called

Static submergence
Downcomer liquid seal
Skirt clearance
None of these

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