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Mass Transfer

Mass Transfer
Liquid diffusivity is of the order of __________ cm² /second.

0.1
0.01
> 1
10-5 to 10-6

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Mass Transfer
Design calculation for multiple component distillation is done by

Tray to tray calculations
Ponchon-Savarit method
Mccabe-Thiele method
Enthalpy concentration method

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Mass Transfer
Most important factor to be considered in the selection of packings for absorbers is the __________ of packing.

Size
Cost
Porosity
Durability

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Mass Transfer
During sensible cooling process

Both B and C
Relative humidity decreases
Relative humidity increases
Wet bulb temperature decreases

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Mass Transfer
Out of the following gas-liquid contacting devices, for a given set of operating conditions, gas pressure drop is the least in __________ tower.

Packed
Bubble cap
Perforated tray
Wetted wall

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Mass Transfer
Surface renewal model of mass transfer was enunciated by

Danckwerts
Toor and Marchello
Stefan
Fick

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