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Mass Transfer

Mass Transfer
Mass transfer co-efficient (K) and diffusivity (D) are related according to film theory as

K ∝ D
K ∝ √D
K ∝ D1.5
K ∝ D2

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Mass Transfer
In distillation columns, the number of bubble caps per tray primarily depends upon the

Allowable liquid velocity
Allowable gas and liquid velocities
Feed composition
Allowable gas velocity

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Mass Transfer
The binary diffusivity in gases at atmospheric conditions is about

10-9 cm/sec
10-4 cm²/seC₂
10-1 cm²/sec
10-3 sec/cm

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Mass Transfer
Gaseous diffusion co-efficient increases with increase in the

Both Pressure & Temperature
Temperature
None of the listed here
Pressure

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Mass Transfer
Which of the following equipments is not used for gas dispersion?

Spray towers
Agitated vessels
Perforated sieve tray towers
Bubble cap tray towers

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

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

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