Related Questions

In case of __________ distillation, a solvent is added to alter the relative volatility of the mixture to be separated.
A Molecular
B Azeotropic
C Extractive
D Flash
In a binary system, separation is very efficient, when the relative volatility is
A 1
B > 1
C 0.5
The relative volatility of a binary mixture at the azeotropic composition is
A 1
B > 1
C 0
D ∞
For a binary mixture with low relative volatility,
A Use steam distillation
B Use molecular distillation
C Use high pressure distillation
D An azeotrope may be formed during distillation
The relative volatility of a binary mixture at constant temperature __________ the total pressure.
A Decreases with increase in
B Increases with increase in
C Is independent of
D None of these
For a binary mixture with low relative volatility, continuous rectification to get pure products will require
A Low reflux ratio
B Less number of trays
C Small cross-section column
D High reflux ratio
Relative volatility varies with the concentration of component for an ideal solution. The relative volatity of a binary mixture may be defined as the ratio of vapor pressure of component 'A' to that of component 'B', when
A Only vapor phase follows Raoult's law
B Only liquid phase obeys Dalton's law
C Liquid phase obeys Dalton's law and vapor phase obeys Raoult's law
D Vapor phase obeys Dalton's law and liquid phase obeys Raoult's law
When the mixture to be distilled has a very high boiling point and the product material is heat sensitive, the separation technique to be used is __________ distillation.
A Continuous
B Steam
C Azerotropic
D None of these
__________ is used as an 'entrainer' for the separation of acetic acid-water mixture by distillation.
A Furfural
B Benzol
C Butyl acetate
D Hexane
When the liquid phase and vapour phase of a binary system obeys Raoult's and Dalton's law respectively, the relative volatility is the ratio of
A Vapour pressure of component A to that of component B
B Vapour pressure of component A to the total pressure
C Vapour pressure of component A to the partial pressure of A
D Partial pressure of component A to the total pressure

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