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Mass Transfer

Mass Transfer
H₂S present in naphtha reformed gas is removed by absorbing with

HCl
Ethanolamine
K₂CO₃
Vacuum gas oil

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Mass Transfer
Perforated plate towers are unique for solvent extraction because, they provide

Better contact of the phase
None of these
Repeated coalescence & redispersion of the drop phase
Higher contact area

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Mass Transfer
Heat sensitive materials with very high latent heat of vaporisation may be economically separated using

Absorption
Liquid extraction
Distillation
Evaporation

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Mass Transfer
With increase in gas rate, the number of transfer units, NtoG, for a fixed degree of absorption by a fixed amount of solvent

Decreases linearly
Decreases
Increases
Remains unaffected

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Mass Transfer
Diffusion co-efficient generally depends upon the temperature, pressure & the nature of the components of the system. Its dimension is not the same as that of the

Volumetric diffusivity
Mass transfer co-efficient
Kinematic viscosity
Thermal diffusivity

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Mass Transfer
Diffusivity in concentrated solutions differs from that in dilute solutions, because of the changes in

Degree of ideality of the solution
Both A & B
Neither A nor B
Viscosity with concentration

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MORE MCQ ON Mass Transfer

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