Separation of two or more components of a liquid solution can not be achieved by

Mass Transfer
Separation of two or more components of a liquid solution can not be achieved by

Absorption

Fractional crystallisation

Liquid extraction

Evaporation

Absorption

Fractional crystallisation

Liquid extraction

Evaporation

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Mass Transfer
When acetone is added in a two layer mixture of methyl isobutyl ketone and water at 30°C, the acetone distributes between the two layers and the composition of the layer follows two solubility curves. For this system,

As the acetone concentration increases, the solubility curves approach each other

Both the phases become identical at a particular common point on both the solubility curves called the plait point

The distribution curve which is a plot between x (acetone concentration in one phase) and y (acetone concentration in other phase) is analogous to x-y curve used in distillation and absorption termina

All of these

As the acetone concentration increases, the solubility curves approach each other

Both the phases become identical at a particular common point on both the solubility curves called the plait point

The distribution curve which is a plot between x (acetone concentration in one phase) and y (acetone concentration in other phase) is analogous to x-y curve used in distillation and absorption termina

All of these

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Mass Transfer
At a fixed total pressure, humidity depends only on the

Partial pressure of vapour in the mixture

Heat capacity of the vapour

None of these

Density of the vapour

Partial pressure of vapour in the mixture

Heat capacity of the vapour

None of these

Density of the vapour

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Mass Transfer
Dew point of an air-water vapor mixture

All of the listed here

At constant humidity & total pressure is fixed

Decreases with decrease in pressure

Corresponding to any point on the humidity chart is obtained by projecting a line through this point parallel to the temperature axis and to the saturation curve

All of the listed here

At constant humidity & total pressure is fixed

Decreases with decrease in pressure

Corresponding to any point on the humidity chart is obtained by projecting a line through this point parallel to the temperature axis and to the saturation curve

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Mass Transfer
In gas-liquid contact operation, the number of ideal stages, N = (xa - xb)/(xb - x*b) . This is true when the stripping factor 'S' is

S = ∞

S = 1

S < 1

S > 1

S = ∞

S = 1

S < 1

S > 1

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Mass Transfer
Sides of equilateral-triangular co-ordinates (on which ternary liquid system is plotted) represent

A binary mixture

A ternary mixture

A pure component

Partially miscible ternary system

A binary mixture

A ternary mixture

A pure component

Partially miscible ternary system

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Mass Transfer

Mass Transfer Separation of two or more components of a liquid solution can not be achieved by

Mass Transfer When acetone is added in a two layer mixture of methyl isobutyl ketone and water at 30°C, the acetone distributes between the two layers and the composition of the layer follows two solubility curves. For this system,

Mass Transfer At a fixed total pressure, humidity depends only on the

Mass Transfer Dew point of an air-water vapor mixture

Mass Transfer In gas-liquid contact operation, the number of ideal stages, N = (xa - xb)/(xb - x*b) . This is true when the stripping factor 'S' is

Mass Transfer Sides of equilateral-triangular co-ordinates (on which ternary liquid system is plotted) represent

Mass Transfer
Separation of two or more components of a liquid solution can not be achieved by

Mass Transfer
When acetone is added in a two layer mixture of methyl isobutyl ketone and water at 30°C, the acetone distributes between the two layers and the composition of the layer follows two solubility curves. For this system,

Mass Transfer
At a fixed total pressure, humidity depends only on the

Mass Transfer
Dew point of an air-water vapor mixture

Mass Transfer
In gas-liquid contact operation, the number of ideal stages, N = (xa - xb)/(xb - x*b) . This is true when the stripping factor 'S' is

Mass Transfer
Sides of equilateral-triangular co-ordinates (on which ternary liquid system is plotted) represent