Q.57 A binary mixture of benzene and toluene under vapour-liquid equilibrium at 80 oC follows ideal Raoult’s law. At this condition, the saturation pressures of benzene and toluene are 101 kPa and 40 kPa, respectively. If the mole fraction of benzene in the liquid phase is 0.6, the corresponding mole fraction of benzene in the vapour phase will be _______. (Round off to two decimal places)

Q.57 A binary mixture of benzene and toluene under vapour-liquid equilibrium at
80 oC follows ideal Raoult’s law. At this condition, the saturation pressures of
benzene and toluene are 101 kPa and 40 kPa, respectively. If the mole fraction
of benzene in the liquid phase is 0.6, the corresponding mole fraction of benzene
in the vapour phase will be _______.
(Round off to two decimal places)

Benzene and toluene form an ideal binary mixture under vapor–liquid equilibrium (VLE) at 80°C.
Using Raoult’s law, with benzene liquid mole fraction of 0.6 and saturation
pressures of 101 kPa (benzene) and 40 kPa (toluene),
the vapor mole fraction of benzene is found to be 0.79.

Raoult’s Law Basics

Raoult’s law states that the partial pressure of a component in an ideal mixture equals the
product of its liquid mole fraction and its pure-component saturation pressure:

Pi = xi Pi

The total pressure is the sum of all partial pressures, and the vapor mole fraction is given by:

yi = Pi / P

Benzene–toluene behaves nearly ideally, making Raoult’s law applicable.

Step-by-Step Calculation

  • Benzene liquid mole fraction, xB = 0.6
  • Toluene liquid mole fraction, xT = 0.4

Benzene partial pressure:
0.6 × 101 = 60.6 kPa

Toluene partial pressure:
0.4 × 40 = 16 kPa

Total pressure:
60.6 + 16 = 76.6 kPa

Vapor mole fraction of benzene:
yB = 60.6 / 76.6 = 0.79

Why 0.79 Is Correct

Benzene has a higher saturation pressure than toluene, making it more volatile.
As a result, benzene is enriched in the vapor phase:

yB > xB

Incorrect answers often arise from ignoring volatility differences or using the wrong total
pressure. The correct value rounded to two decimal places is 0.79.

Common Errors Explained

Error Type Calculation Result Why Incorrect
Direct equality yB = xB 0.60 Ignores volatility difference
Wrong component yT = xT 0.40 Calculates toluene fraction instead
Wrong total pressure 60.6 / 80.6 0.75 Incorrect pressure summation
Correct 60.6 / 76.6 0.79 Correct use of Raoult’s law

 

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