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Process Equipment and Plant Design

Process Equipment and Plant Design
Back-trapping in a distillation column results due to

High gas velocity
Low reflux ratio
Low gas velocity
Excessive liquid gradient over the tray

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Process Equipment and Plant Design
The minimum plate spacing in most of the pertroleum refinery distillation columns (of dia > 3 ft) is normally __________ inches.

34
18
6
12

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Process Equipment and Plant Design
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

5-7.5
15-20
10-12.5
2.5-3.0

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Process Equipment and Plant Design
In distillation columns, bubble caps are held in place over trays by

Bolts
Rivets
A hold down bar
Both B and C

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

Either A or B
Floating head tube sheet
Neither A nor B
U-bend

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Process Equipment and Plant Design
In a __________ rivetted joint, the number of rivets decreases from the innermost row to the outermost row.

Diamond
None of these
Chain
Zig-zag

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