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Mass Transfer

Mass Transfer
The relative volatility of a binary mixture at the azeotropic composition is

1
∞
> 1

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Mass Transfer
As complete saturation of an adsorbent is approached, the differential heat of adsrop-tion approaches

Zero
None of these
That of normal condensation
Integral heat of adsorption

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Mass Transfer
In case of absorption, both the operating and equilibrium lines will be straight for

None of these
Isothermal operation
Dilute solutions and isothermal operation
Dilute solutions

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Mass Transfer
High pressure at the bottom of a distillation tower handling heat sensitive materials results in

Thermal decomposition of bottoms
Very efficient operation
Increased relative volatility
Erosion of the tower

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Mass Transfer
Use of packed towers for distillation is generally limited to the

Vacuum distillation
Multicomponent distillation
Small sizes
High pressure operation

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Mass Transfer
For a binary mixture with low relative volatility, continuous rectification to get pure products will require

High reflux ratio
Low reflux ratio
Small cross-section column
Less number of trays

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