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Mass Transfer

Mass Transfer
Diameter to height ratio for a rashig ring is

5
1
2
0.5

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

T1.5
√T
T
T3

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Mass Transfer
In distillation column design, the McCabe-Thiele procedure is inadequate and a Ponchan-Savarit procedure is needed, when

Saturated feed is not used
The latent heat of vaporisation of the more and less volatile components are greatly different
A total condenser is used
An azeotrope forms

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Mass Transfer
Design calculation for multiple component distillation is done by

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

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Mass Transfer
For the case of flow of air past a wet bulb thermometer (air water vapour system), the approximate value of Hâ‚‚/ky.Cz is around

1
0.24
0.6
0.72

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Mass Transfer
In a single stage extraction process, 10 kg of pure solvent S (containing no solute A) is mixed with 30 kg of feed F containing A at a mass fraction xf = 0.2. The mixture splits into an extract phase E and a raf-finate phase R containing A at xB = 0.5 and xR = 0.05 respectively. The total mass of the extract phase is (in Kg)

8.25
10
6.89
8.89

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