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Mass Transfer

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

μ
1/μ
√μ
μ²

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Mass Transfer
Pick out the system with maximum boiling azeotrope at 1 atm.

Acetone chloroform
Benzene-ethyl alcohol
Ethyl alcohol-water
None of these

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Mass Transfer
The reason for preferring packed towers over plate towers in distillation practice is that the packed tower operation gives

Low pressure drop and high hold up
High pressure drop and high hold up
High pressure drop and low hold up
Low pressure drop and low hold up

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Mass Transfer
H₂S is being absorbed in a gas absorber unit. The height of the transfer unit based on the overall mass transfer coefficient on the gas side is 0.4 m. The equilibrium data is given by, y = 1.5 x. The bulk concentration of H₂S has to be reduced from 0.05 to 0.001 mole fraction in the gas side. The height of the tower (in metres) corresponding to an operating line given by, y = 5x + 0.001 is

1.56
1
2
0.56

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Mass Transfer
Weight of 1 m³ of humid air as compared to 1 m³ of dry air, under the same conditions, is

More
Unpredictable
Less
Same

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Mass Transfer
Dimension of mass diffusivity is the same as that of

Dynamic viscosity
Surface tension
Pressure
Kinematic viscosity

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MORE MCQ ON Mass Transfer

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