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Mass Transfer

Mass Transfer
Penetration model (theory) for mass transfer was enunciated by

Higbie
Toor and Marchello
Kissinevskii
Danckwerts

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Mass Transfer
Desirable value of absorption factor in an absorber is

1
0.5
< 1
> 1

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Mass Transfer
The reciprocal of stripping factor is termed as

Relative volatility
Absorption factor
Selectivity index
Murphree efficiency

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Mass Transfer
According to Poiseuille's law, the permeability for gas flow through a capillary is proportional to (where, μ = gas viscosity)

√μ
μ²
1/μ
μ

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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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Mass Transfer
On moving the feed line (q-line) from saturated liquid feed (vertical position) to saturated vapor feed (horizontal feed), if the slope of both the operating lines are to be increased, then it will result in

Increased reboiler load
Increased reflux ratio
None of these
Greater degree of separation with a fixed number of trays

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