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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
Which of the following lengths of heat exchanger tubes are normally not used in practice?

10 metres
6 metres
2.5 metres
0.5 metre

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Process Equipment and Plant Design
Holes of a sieve tray are arranged in triangular pitch of __________ times the hole diameter.

5 to 10
2.5 to 5
10 to 15
1.5 to 2

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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

Creating turbulence
Reducing scale deposition
Fixing the tubes
Increasing pressure drop

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Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

1/D⁵
1/D²
D²
1/D

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Process Equipment and Plant Design
Poisson's ratio of a material is the ratio of unit lateral strain to the unit axial elongation within its elastic limit. The value of Poisson's ratio for structural and pressure vessel steel may be taken as

0.3
0.75
0.01
0.95

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