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Process Equipment and Plant Design

Process Equipment and Plant Design
Pressure drop per tray in the atmospheric distillation column is about __________ psi.

0.01 - 0.5
43833
0.5 - 1.0
0.07 - 0.12

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Process Equipment and Plant Design
In the design of a paddle agitator, the ratio (paddle dia/tank dia) is normally taken as

0.8
0.5
0.1
0.25

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

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

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

Rivets
Bolts
A hold down bar
Both B and C

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Process Equipment and Plant Design
In the allocated cap area, bubble caps are generally arranged on equilateral triangular pitch. Number of caps fixed on a plate is with a

Either A or B
Neither A nor B
Cap pitch of 1.3-2 times the cap diameter
Clearance of 25-75 mm

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Process Equipment and Plant Design
Compensation against openings in process vessels for giving inlet and outlet connections, for providing sight glasses and manholes etc. is provided for strength and rigidity. The most efficient type of compensation is of __________ type.

Ring plate
Flared out
Fluid in
Nozzle or rim

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