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Mass Transfer

Mass Transfer
At 750°K and 1 atm, the approximate value of Schmidt number for air is

0.01
10
0.1
1

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

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

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Mass Transfer
The adiabatic saturation curve for a vapour-gas mixture is

Slightly concave upward
None of these
Straight line
Slightly concave downward

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Mass Transfer
Weeping in a distillation column

Results due to very high gas velocity
Results due to very low gas velocity
Increases tray efficiency
Provides large interfacial surface for mass transfer

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Mass Transfer
Minimum reflux ratio in a distillation column results in

Minimum number of trays
Minimum reboiler size
Optimum number of trays
Maximum condenser size

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Mass Transfer
Solvent used in extractive distillation

Does not alter the relative volatility of the original components
Forms a high boiling azeotrope
Is of low volatility
Forms a low boiling azeotrope

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