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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffle spacing is generally __________ the I.D. of the shell.

Both B and C
Not less than one fifth of
Not greater than
More than

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Multipass shell and tube heat exchanger
Counter flow of hot and cold fluids
Fouling fluids
Double pipe heat exchanger

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Process Equipment and Plant Design
In case of bubble cap distillation column of diameter greater than 1.2 metres, the cap diameter is roughly about __________ cms.

35
10
30
20

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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
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

1.75
3.5
2.5
1.25

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Process Equipment and Plant Design
If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

Decrease by 22
None of these
Increase by 21.6
Increase by 1.8

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