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Process Equipment and Plant Design

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

0.25
0.1
0.5
0.8

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Process Equipment and Plant Design
In actual operation of a bubble cap distillation tower, the __________ at the bottom of the tower is more than that at the top of the tower.

All of these
Vapour molecular weight
Molal flow rate of vapour
Pressure and temperature

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

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

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Process Equipment and Plant Design
In packed absorption tower, onset of flooding usually occurs at a pressure drop of about __________ mm of water column per metre height of packing.

50-75
200-250
750-1000
25-50

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the baffles on shell side is primarily provided for

Increasing pressure drop
Creating turbulence
Fixing the tubes
Reducing scale deposition

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Process Equipment and Plant Design
In a __________ rivetted joint, the rivets in the various rows are opposite to each other.

None of these
Chain
Diamond
Zig-zag

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