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Mass Transfer

Mass Transfer
Berl saddle made of carbon cannot be used for

SO₂
Alkalis
Oxidising atmosphere
H₂SO₄

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Mass Transfer
According to Poiseuille's law, the permeability for gas flow through a capillary is proportional to (where, μ = gas viscosity)

√μ
μ
1/μ
μ²

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Mass Transfer
Unsaturated air (with dry and wet bulb temperatures being 35 and 25°C respectively) is passed through water spray chamber maintained at 35°C. The air will be

Both A & B
Dehumidified
Cooled
Humidified

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Mass Transfer
During bottling of cold drinks (e.g. Pepsi), the main resistance to mass transfer for the absorption of carbon dioxide in water lies in the

Gas film
Liquid-gas interface
None of these
Liquid film

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Mass Transfer
Absorption factor is defined as (where, S₁ = slope of the operating line S₂ = slope of the equilibrium curve)

S₁ x S₂
S₂/S₁
S₁ - S₂
S₁/S₂

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Mass Transfer
The minimum number of theoretical plates is required for achieving a given separation in distillation column with

Minimum reflux ratio
Total reflux
No reflux
Zero reflux ratio

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