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Process Equipment and Plant Design

Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

Horizontal
None of these
Thin shperical (e.g. Horton sphere)
Thick walled vertical

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Process Equipment and Plant Design
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

G1.5
G0.2
G0.5
G0.8

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Process Equipment and Plant Design
The minimum plate spacing in most of the pertroleum refinery distillation columns (of dia > 3 ft) is normally __________ inches.

18
34
12
6

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Process Equipment and Plant Design
Maximum acceptable total liquid gradient over a tray is about __________ mm.

12.5
30.5
5.5
45.5

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Process Equipment and Plant Design
Diameter of bubble caps used in high pressure columns is __________ as compared to that used in identical vacuum columns.

Same
Less
Either A or B; no generalisation can be made
More

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Process Equipment and Plant Design
Liquid/petroleum fuel storage tanks are built underground (as in case of petrol pumps), when the storage capacity is less than __________ kilolitres.

20
45
30
85

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