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Mass Transfer

Mass Transfer
Boiling point diagram is not affected by the ambient

Temperature
Pressure
Humidity
Both B and C

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Mass Transfer
The drying time between fixed moisture content within diffusion controlled 'falling rate period' is proportional to (assuming that drying occurs from all surfaces of the solid) (where, T = thickness of the solid )

T²
√T
T³
T

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Mass Transfer
The feed to fractionating column is changed from saturated vapour to saturated liquid. If the separation and reflux ratio remains unchanged, the number of ideal stages will

Remains same
Depend on saturated boiling point; may increase or decrease
Decrease
Increase

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Mass Transfer
Flooding results in

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

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Mass Transfer
Ammonia present in the coke oven gas is removed by washing with

Dilute ammoniacal liquor
Dilute HCl
Caustic solution
Ethanolamine

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Mass Transfer
Acetone is to be removed from air in an isothermal dilute absorber using pure water as solvent. The incoming air contains 5 mole% of acetone (yin = 0.05). The design equation to be used for obtaining the number of trays (N) of the absorber is, N+2 = 6 log (yin/yout).For 98% recovery of acetone, the number of trays required is/are

9
10
8
1

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