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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
Packed
Bubble cap plate
Sieve plate

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Process Equipment and Plant Design
Power required for agitation depends upon the

Size of agitator & the tank
All of these
Agitator type & speed of agitation
Height & properties of the liquid

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Process Equipment and Plant Design
Lessing ring is formed by the addition of a partition across the centre of a raschig ring, which results in an area increase of about __________ percent.

5
20
35
55

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Process Equipment and Plant Design
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

3 to 5
6 to 12
2 to 3
4 to 8

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Process Equipment and Plant Design
Which of the following efficiencies can be greater than 100%?

Point efficiency
Murphree plate efficiency
None of these
Overall plate efficiency

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Process Equipment and Plant Design
Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

Same
Less
More
More or less depending upon the pressure & temperature inside the vessel and the nature of the fluid contained therein

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