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Process Equipment and Plant Design

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

Both B and C
Bolts
Rivets
A hold down bar

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Process Equipment and Plant Design
Movement of pipeline caused by thermal expansion is taken care by providing

Changes in its direction
Change in the shape of pipeline
All of these
Expansion joint

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Process Equipment and Plant Design
Height of the flights in the rotary drier is in the range of

0.2 to 0.5 d
0.5 to 0.6 d
0.02 to 0.05 d
0.08 to 0.12 d

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

L to 3
12.5 to 18.5
3 to 12.5
4 to 8

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Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Remains constant
Increases very rapidly
Increases linearly
Decreases very rapidly

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Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.5-0.65
0.75-0.85
0.60-0.90
0.15-030

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