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Process Equipment and Plant Design

Process Equipment and Plant Design
Maximum size of the raschig rings used in a packed tower is about __________ of the coloumn diameter.

1/10th
1/30th
1/50th
1/20th

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

60°
90°
45°
15°

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

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

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Process Equipment and Plant Design
Maximum allowable vapour velocity in a bubble cap tower is determined by the

None of these
Vapour density
Diameter of the column
Entrainment considerations

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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.

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

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Process Equipment and Plant Design
For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

D2/(d1 + d2)
(d1 + d2)/d1
(d1 + d2)/d2
D1/(d1 + d2)

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