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Mass Transfer

Mass Transfer
Rate of leaching increases with increasing

Pressure
Temperature
Viscosity of solvent
Size of the solid

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Mass Transfer
In a moderately sized packed absorption tower, channeling (which is most severe with stacked packings) can be minimised by taking the ratio of tower diameter to packing diameter

> 4 :1
< 8 : 1
< 6:1
> 8:1

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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
A total condenser is used
The latent heat of vaporisation of the more and less volatile components are greatly different
An azeotrope forms

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Mass Transfer
Pressure drop through plate tower as compared to that through packed tower, for the same duty will be

More
Either A or B; depends on the packing height
Equal
Less

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Mass Transfer
In distillation columns, the number of bubble caps per tray primarily depends upon the

Allowable gas and liquid velocities
Feed composition
Allowable gas velocity
Allowable liquid velocity

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Mass Transfer
The relative saturation of an unsaturated mixture of gas and vapor is independent of the

Temperature of the mixture
Nature of the vapor
Composition of the mixture
None of these

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