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Process Equipment and Plant Design

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

Diameter of the column
Entrainment considerations
None of these
Vapour density

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Process Equipment and Plant Design
Theoretically calculated diameter of the stripping section of the continuous rectification column is __________ that of the enriching section.

Same as
Either more or less (depending upon relative volatility)
More than
Less than

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Process Equipment and Plant Design
The ratio of shear stress to shear strain is called

Bulk modulus
Shear modulus
Modulus of elasticity
Modulus of rigidity

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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
0.4-0.9
1.2-1.5
0.2-0.5

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

4 to 8
12.5 to 18.5
3 to 12.5
L to 3

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Process Equipment and Plant Design
In packed absorption tower, onset of flooding usually occurs at a pressure drop of about __________ mm of water column per metre height of packing.

25-50
50-75
200-250
750-1000

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