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Mass Transfer

Mass Transfer
The suitable evaporator for concentration of foaming liquids is a __________ evaporator.

Vacuum
Long tube
Falling film
Short tube

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Mass Transfer
The value of NA/(NA + NB), for steady state equimolal counter diffusion of two gases 'A' and 'B' is

∞
1
2
0.5

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Mass Transfer
The interfacial area per unit volume of dispersion, in a gas-liquid contactor, for fractional hold up of gas = 0.1 and gas bubble diameter = 0.5 mm is given by (in m²/m³)

100
500
1000
50

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Mass Transfer
In rectifying section of a continuous distillation column, the

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

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Mass Transfer
During constant rate drying period, vaporisation rate per unit drying surface area

Does not change with time
Does not affect the moisture content of the wet solid
Increases with time
Decreases with time

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Mass Transfer
According to the Fenske equation, what will be the minimum number of plates required in a distillation column to separate an equimolar binary mixture of components A and B into an overhead fraction containing 99 mol% A and a bottom fraction containing 98 mol% B? Assume that relative volatility (αAB = 2) does not change appreciably in the coloumn.

6
10
12
8

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