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Mass Transfer

Mass Transfer
Mass transfer co-efficient (K) and diffusivity (D) are related according to film theory as

K ∝ √D
K ∝ D
K ∝ D1.5
K ∝ D2

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Mass Transfer
Fenske-Underwood equation used for calculating the minimum number of theoretical plates in distillation column is valid for

Total reflux
Constant molal overflow
All of these
Constant relative volatility

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Mass Transfer
Molecular seives are porous

Synthetic zeolites crystals/metal alumino-silicates
Alumina
None of these
Silica

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Mass Transfer
In stripping section of continuous distillation column, the

Liquid is enriched with high boiler
Liquid is stripped of high boiler
None of these
Vapour is stripped of low boiler

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Mass Transfer
The value of Lewis number (Le = Sc/Pr) for air-water vapour system is around

600
0.24
3.97
1

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Mass Transfer
In the layout plan for a vacuum distillation unit, operating at 60 mm Hg, supported by a barometric condenser, the appropriate place for the location of vacuum drum for collecting the distillate will be

2 metres above the ground
At ground level
5 metres above ground
10 metres above ground

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