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Mass Transfer

Mass Transfer
Penetration theory relates the average mass transfer co-efficient (K) with diffusivity (D) as

K ∝ D
K ∝ D2
K ∝ D1.5
K ∝ √D

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Mass Transfer
In liquid extraction, if the selectivity is unity, then

Solvent flow rate should be very low
Separation of the constituents is the most effective
Amount of solvent required will be minimum
No separation will occur

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Mass Transfer
Water entrained by circulating air in cooling towers is termed as

Vapor load
Drift
None of the listed here
Blow down

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Mass Transfer
The rate of mass transfer is not dependent upon the

None of these
Both A & B
Interfacial surface exposed between the phases
Degree of dispersion of one fluid in the other

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Mass Transfer
For turbulent mass transfer in pipes, the Sherwood number depends on the Reynolds number as

Re
Re0.53
Re0.33
Re0.83

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Mass Transfer
Perforated plate towers are unique for solvent extraction because, they provide

None of these
Better contact of the phase
Higher contact area
Repeated coalescence & redispersion of the drop phase

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