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Process Equipment and Plant Design

Process Equipment and Plant Design
Saddle supports are used for supporting __________ vessels.

Thick walled vertical
Tall vertical
Thick spherical
Horizontal cylinderical

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Process Equipment and Plant Design
Normally, the ratio of the total riser area to the tower cross sectional area (for bubble cap towers of diameter more than 3 ft) is around

0.4-0.6
0.1-0.2
0.35-0.75
0.55-0.85

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Process Equipment and Plant Design
Tube height in a calendria type evaporator is normally less than __________ metres.

2
5.5
1
3.5

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Process Equipment and Plant Design
In a distillation column, bubble caps are located on trays with a pitch of __________ times the outside diameter of the caps.

1.6 to 2
1.3 to 2
1.5 to 3
2.5

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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.

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

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Process Equipment and Plant Design
At the following point for a given packing and set of fluids, the pressure drop per metre of packed height, with variation in fluid rates and operating pressure

May increase or decrease depending upon the solubility of the gas in the liquid
Increases
Remains same
Decreases

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