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Mass Transfer

Mass Transfer
A good solvent used for absorption should not have very high

Viscosity
Vapor pressure
Freezing point
All of these

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Mass Transfer
Mass transfer co-efficient 'K' according to penetration theory varies with mass dif-fusivity as

1/D
D0.5
D
D1.5

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Mass Transfer
Overall efficiency of the distillation column is

Same as the Murphree efficiency
The ratio of number of actual plates to ideal plates
The ratio of number of ideal plates to actual plates
Always more than the point efficiency

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Mass Transfer
In case of absorption, both the operating and equilibrium lines will be straight for

Isothermal operation
Dilute solutions and isothermal operation
None of these
Dilute solutions

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Mass Transfer
Can the efficiency of a plate in the distillation tower be greater than 100%?

Yes
Never
Normally not; but is possible if infinite number of plates are put
Yes ; if the reflux ratio is maximum

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Mass Transfer
The reason for preferring packed towers over plate towers in distillation practice is that the packed tower operation gives

High pressure drop and low hold up
High pressure drop and high hold up
Low pressure drop and low hold up
Low pressure drop and high hold up

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