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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

34
6
24
18

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

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Process Equipment and Plant Design
The ideal size of round bubble caps to be used in industrial distillation column having a diameter of 3-6 metres is __________ cms.

15
50
7.5
5

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Process Equipment and Plant Design
Which of the following is the most common type of baffle used in industrial shell and tube heat exchanger?

25% cut segmental baffle
75% cut segmental baffle
Disk and doughnut baffle
Orifice baffle

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Process Equipment and Plant Design
Which tube arrangement in a heat exchanger would facilitate highest heat transfer rate?

Triangular pitch
Diagonal square pitch
Heat transfer rate is independent of tube arrangement
Square pitch

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Process Equipment and Plant Design
Maximum plate efficiency is achieved in case of __________ flow.

Cross
Split
Cascade
Reverse

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