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Mass Transfer

Mass Transfer
Boiling point diagram is not affected by the ambient

Humidity
Temperature
Pressure
Both B and C

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Mass Transfer
Very tall packed towers are divided into series of beds to

Avoid flooding
Reduce the overall pressure drop
Avoid channelling
Reduce liquid hold-up

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Mass Transfer
Stefan's law describes the mass transfer by

Both A & B
Bulk flow
Diffusion
Neither A nor B

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Mass Transfer
Tower diameter may be decreased by

Using higher reflux ratio
Use of increased tray spacing
Increasing the liquid flow rate
Increasing the vapour flow rate

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Mass Transfer
Flooding results in

Good contact between the fluids
High tray efficiency
Low tray efficiency
High gas velocity

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Mass Transfer
If the specific heats of a gas and a vapor are 0.2KJ/Kg.°K and 1.5 KJ/Kg.°K respectively, and the humidity is 0.01; the humid heat in KJ/°Kg. is

0.31
0.107
0.017
0.215

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