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Process Equipment and Plant Design

Process Equipment and Plant Design
for couplings and unions would be

200
60
Negligible
350

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.2-0.5
1.2-1.5
0.1-0.2
0.4-0.9

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Process Equipment and Plant Design
Reflux ratio variation in a distillation column is between

Minimum and infinity
Zero and infinity
Zero and one
None of these

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Process Equipment and Plant Design
Saddle supports are used for supporting __________ vessels.

Thick spherical
Thick walled vertical
Tall vertical
Horizontal cylinderical

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Process Equipment and Plant Design
A minimum clearance of about __________ mm is maintained between the distillation column wall and the bubble cap.

19
76
95
38

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Process Equipment and Plant Design
In inclined long tube vertical evaporators, the tubes are inclined at an angle of

15°
45°
60°
90°

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