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Mass Transfer

Mass Transfer
The absorption factor is defined as (where, L = liquid flow rate, G = gas flow rate and, m = slope of the equilibrium line)

LG/m
G/mL
L/mG
ML/G

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Mass Transfer
HETP is numerically equal to HTU, only when the operating line

Lies above the equilibrium line
Is far from the equilibrium line
Lies below the equilibrium line
And equilibrium lines are parallel

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Mass Transfer
Schimdt number and Lewis number for pure air at atmospheric conditions are respectively

1 and 0
>1 and ≈ 1
< 1 and ≈ 1
0 and ≈ 1

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Mass Transfer
High pressure at the bottom of a distillation tower handling heat sensitive materials results in

Erosion of the tower
Increased relative volatility
Very efficient operation
Thermal decomposition of bottoms

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Mass Transfer
Back-trapping in a distillation column

Increases tray efficiency
Reduces pressure drop
Decreases tray efficiency
Is desirable, as it provides improved vapour-liquid contact

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Mass Transfer
At what value of reflux ratio, number of theoretical plates in a distillation column is minimum?

< 1
∞
1

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