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Mass Transfer

Mass Transfer
Penetration model (theory) for mass transfer was enunciated by

Kissinevskii
Danckwerts
Toor and Marchello
Higbie

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Mass Transfer
Desirable value of absorption factor in an absorber is

0.5
< 1
1
> 1

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Mass Transfer
During constant rate period, the rate of drying decreases with the

Increase in air humidity
Decrease in air temperature
Neither A nor B
Both A & B

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

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

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Mass Transfer
Which of the following quantities need not be fixed before starting the design of a co-current absorber?

Heat gain or loss
Flow rate of entering liquid
None of the listed here
Flow rate of gas

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Mass Transfer
Unsaturated air (with dry bulb and wet bulb temperatures being 45°C and 25°C respectively) is passed through a water spray chamber maintained at 23°C. The air will be cooled and

None of these
Humidified with wet bulb temperature decreasing
Dehumidified
Humidified at constant wet bulb temperature

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