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Mass Transfer

Mass Transfer
The value of L/mG ratio for economical absorption operation ranges from

0.8 to 1.2
2.5 to 3.5
1.25 to 2.0
0.5 to 0.8

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

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

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Mass Transfer
With decrease in the throughput (compared with the design capacity) for a bubble cap distillation column, its efficiency

Decreases
May increase or decrease ; depends on individual design
Remains same
Increases

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Mass Transfer
NSc/NPr is called the

Lewis number
Sherwood number
Psychrometric ratio
Stantan number

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Mass Transfer
H₂S present in naphtha reformed gas is removed by absorbing with

K₂CO₃
HCl
Vacuum gas oil
Ethanolamine

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Mass Transfer
'ADDUCTS' and 'CLATHRATES' are used in case of

Crystallisation
Extractive distillation
None of these
Absorption

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