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Mass Transfer

Mass Transfer
Desirable value of absorption factor in an absorber is

> 1
0.5
< 1
1

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Mass Transfer
Condensation of a vapour-gas mixture just begins, when (where, p = partial pressure of the vapour P = vapour pressure of the liquid )

P >>P
P < P
P
P = P

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

K ∝ √D
K ∝ D
K ∝ D2
K ∝ D1.5

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Mass Transfer
Which of the following is the most suitable for extraction in a system having very low density difference?

Centrifugal extractor
Mixer-settler extractor
Packed extraction tower
Pulsed extractor

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Mass Transfer
In case of non-ideal gases and liquids, the molal diffusivity

Is independent of pressure
Varies directly as the pressure
Varies inversely as the pressure
Is equal to the volumetric diffusivity

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Mass Transfer
Weeping in a distillation column

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

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