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Process Equipment and Plant Design

Process Equipment and Plant Design
The safe distance of habitation from a hazardous chemical plant (TLV of its product < 1000 ppm) should be about __________ kms.

1
15
5
25

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the shortest centre to centre distance between the adjacent tubes is

Called tube clearance
Called tube pitch
Always less than the diameter of the tube
None of these

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Process Equipment and Plant Design
The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

24
34
6
18

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Process Equipment and Plant Design
In case of a 'thin' pressure vessel, the ratio of its diameter to wall thickness is

< 10
30
> 10
> 20

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Process Equipment and Plant Design
Which of the following efficiencies can be greater than 100%?

None of these
Point efficiency
Overall plate efficiency
Murphree plate efficiency

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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
1.5 to 2
2.5 to 5
10 to 15

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