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Mass Transfer

Mass Transfer
Pore size of the molecular seive 5A is __________ mm.

0.5
50
5
0.05

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Mass Transfer
The interfacial area per unit volume of dispersion, in a gas-liquid contactor, for fractional hold up of gas = 0.1 and gas bubble diameter = 0.5 mm is given by (in m²/m³)

1000
500
50
100

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Mass Transfer
The most efficient cooling tower out of the following is

Natural draft
Forced draft
Induced draft
Atmospheric

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Mass Transfer
Antibiotics are best handled in a

Podbielniak extractor
Pulsed column extractor
Sieve tray contractor
Rotating disc contactor

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Mass Transfer
______ extractor uses centrifugal force for separating the two phases.

Treybal
None of the listed here
Podbielniak
Schiebel

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Mass Transfer
The main reason for dividing a tall packed tower into series of small towers is to

Avoid flooding
Reduce liquid hold up
Minimise the overall pressure drop
Avoid channeling

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