Atkins' Physical Chemistry
Atkins' Physical Chemistry
11th Edition
ISBN: 9780198769866
Author: ATKINS, P. W. (peter William), De Paula, Julio, Keeler, JAMES
Publisher: Oxford University Press
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Chapter 5, Problem 5.2IA
Interpretation Introduction

Interpretation: The vapour pressure/composition curve for a mixture of benzene (B) and ethanoic acid (E) at 50°C for the given vapour pressure data has to be plotted.  The activity and activity coefficients of both components on the basis of Raoult’s law have to be deduced.  Taking B as a solute, its activity and activity coefficients have to be deduced on the basis of Henry’s law.  The excess Gibbs energy of the mixture has to be evaluated over the given composition range.

Concept introduction: The Raoult’s law states that the ratio of the partial pressure of each component to the partial pressure in the vapour pressure when it is present as a pure liquid is equal to its composition in the liquid phase.  Henry’s law states that the amount the partial vapour pressure is directly proportional to the amount of substance dissolved.  It involves an empirical constant KH called Henry’s constant.

Expert Solution & Answer
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Answer to Problem 5.2IA

The vapour pressure/composition curve for a mixture of benzene and ethanoic acid for the given vapour pressure data is plotted as below,

Atkins' Physical Chemistry, Chapter 5, Problem 5.2IA , additional homework tip  1

The activity and activity coefficient of ethanoic acid on the basis of Raoult’s law is shown in the table below.

xEaEγE
0.0160.0161
0.04390.04391
0.08350.08351
0.11380.11381
0.17140.17141
0.29730.29731
0.36960.36961
0.58340.58341
0.66040.66041
0.84370.84371
0.99310.99311

The activity and activity coefficients of benzene on the basis of Raoult’s law is shown in the table below,

xBaBγB
0.9840.9841
0.95610.95611
0.91650.91651
0.88620.88621
0.82860.82861
0.70270.70271
0.63040.63041
0.41660.41661
0.33960.33961
0.15630.15631
0.00690.00691

The activity and activity coefficients of benzene on the basis of Henry’s law are shown in the table below,

xBaBγB
0.9840.7308380.742721
0.95610.7101160.742721
0.91650.6807040.742721
0.88620.65820.742721
0.82860.6154190.742721
0.70270.521910.742721
0.63040.4682120.742721
0.41660.3094180.742721
0.33960.2522280.742721
0.15630.1160870.742721
0.00690.0051250.742721

The excess Gibbs energy is 766.3Jmol-1_.

Explanation of Solution

The vapour pressure data for a mixture of benzene (B) and ethanoic acid (E) at 50°C is given as,

xEpE/kPapB/kPa
0.0160.48435.05
0.04390.96734.29
0.08351.53533.28
0.11381.8932.64
0.17142.4530.9
0.29733.3128.16
0.36963.8326.08
0.58344.8420.42
0.66045.3618.01
0.84376.7610
0.99317.290.47

The total mole fraction of the components is 1.

    xB+xE=1

The mole fraction of benzene (xB) in the solution is calculated in the table as,

xExB=1xE
0.0160.984
0.04390.9561
0.08350.9165
0.11380.8862
0.17140.8286
0.29730.7027
0.36960.6304
0.58340.4166
0.66040.3396
0.84370.1563
0.99310.0069

The total pressure (p) of the solution is,

    p=pE+pB                                                                                                   (1)

Where,

  • pE is the vapour pressure of ethanoic acid.
  • pB is the vapour pressure of benzene.

According to Dalton’s law of partial pressures, the partial pressure of benzene (pB') is given by the formula,

    pB'=xBp                                                                                                      (2)

Where

  • xB is the mole fraction of benzene.

Substitute the value of p from equation (1) in equation (2).

    pB'=xB(pE+pB)                                                                                        (3)

The mole fraction of benzene (xB) is 0.984.

The vapour pressure of ethanoic acid (pE) is 0.484kPa.

The vapour pressure of benzene (pB) is 35.05kPa.

Substitute the value of xB, pE and pB in equation(3).

    pB'=0.984(0.484kPa+35.05kPa)=34.965kPa

Similarly, the values of pB' and p are calculated for all values of xB in the table as shown,

xB=1xEp/kPapB'/kPa
0.98435.53434.96546
0.956135.25733.70922
0.916534.81531.90795
0.886234.5330.60049
0.828633.3527.63381
0.702731.4722.11397
0.630429.9118.85526
0.416625.2610.52332
0.339623.377.936452
0.156316.762.619588
0.00697.760.053544

The graph between mole fraction of benzene (xB) and the partial pressure of benzene (pB') is plotted as,

Atkins' Physical Chemistry, Chapter 5, Problem 5.2IA , additional homework tip  2

According to Raoult’s law the relation between the partial pressure of benzene is given by the expression,

    pB'=xBpB*

Where,

  • pB* is the vapour pressure of the pure substance.

As the graph between the partial pressure of benzene and mole fraction of benzene is a straight line, hence, it follows Raoult’s law.

According to Raoult’s law the relation between the partial pressure of ethanoic acid is given by the expression,

    pE'=xEpE*                                                                                                     (4)

Where,

  • pE* is the vapour pressure of the pure substance.
  • xE is the mole fraction of ethanoic acid.
  • pE' is the partial pressure of ethanoic acid.

The vapour pressure of pure ethanoic acid (pE*) at 50°C is 7.615kPa.

The mole fraction of ethanoic acid (xE) is 0.0160.

Substitute the value of pE* and xE in equation (4).

    pE'=0.016×7.615kPa=0.1218kPa

The mole fraction of ethanoic acid in vapour (yE) is given by the formula,

    yE=pE'p                                                                                                        (5)

The partial pressure of ethanoic acid (pE') is 0.1218kPa.

The total pressure of the mixture (p) when mole fraction of ethanoic acid is 0.016 is 35.534kPa

Substitute the value of pE' and p in equation (5).

    yE=0.1218kPa35.534kPA=0.00342

The activity of ethanoic acid (aE) is given as,

    aE=yEppE*                                                                                                       (6)

Substitute the values of yE, p, and pE* in equation (6).

    aE=0.00342×35.534kPa7.615kPa=0.0159

The activity coefficient (γE) of ethanoic acid is given as,

    γE=aExE                                                                                                         (7)

Substitute the value of aE and xE in equation (7).

    γE=0.01590.016=0.99

Similarly, the values of aE and γE are calculated for all values of xE in the table as shown,

xEpE'/kPayEaEγE
0.0160.121840.0034290.0161
0.04390.3342990.0094820.04391
0.08350.6358530.0182640.08351
0.11380.8665870.0250970.11381
0.17141.3052110.0391370.17141
0.29732.263940.071940.29731
0.36962.8145040.0940990.36961
0.58344.4425910.1758750.58341
0.66045.0289460.2151880.66041
0.84376.4247760.383340.84371
0.99317.5624570.9745430.99311

According to Raoult’s law the relation between the partial pressure of benzene is given by the expression,

    pB'=xBpB*                                                                                                     (8)

Where,

  • pB* is the vapour pressure of the pure substance.
  • xB is the mole fraction of benzene.
  • pB' is the partial pressure of benzene.

The vapour pressure of pure benzene (pB*) at 50°C is 34.66kPa.

The mole fraction of benzene (xB) is 0.984.

Substitute the value of pB* and xB in equation (8).

    pB'=0.984×33.66kPa=33.121kPa

The mole fraction of benzene in vapour (yB) is given by the formula,

    yB=pB'p                                                                                                       (9)

The partial pressure of benzene (pB') is 33.121kPa.

The total pressure of the mixture (p) when mole fraction of benzene is 0.984 is 35.534kPa.

Substitute the value of pB' and p in equation (9).

    yB=33.121kPa35.534kPA=0.932

The activity of benzene (aB) is given as,

    aB=yBppB*                                                                                                     (10)

Substitute the values of yB, p, and pB* in equation (10).

    aB=0.932×35.534kPa33.66kPa=0.984

The activity coefficient (γB) of benzene is given as,

    γB=aBxB                                                                                                       (11)

Substitute the value of aB and xB in equation (11).

    γB=0.9840.984=1

Similarly, the values of aB and γB are calculated for all values of xB in the table as shown,

xBpB'/kPayBaBγB
0.98433.121440.9321060.9841
0.956132.182330.9127930.95611
0.916530.849390.8860950.91651
0.886229.829490.8638720.88621
0.828627.890680.8363020.82861
0.702723.652880.7516010.70271
0.630421.219260.7094370.63041
0.416614.022760.5551370.41661
0.339611.430940.4891290.33961
0.15635.2610580.3139060.15631
0.00690.2322540.029930.00691

According to Henry’s law the partial pressure of benzene (pB') is given as,

  pB'=xBKH                                                                                                  (12)

Where

  • pB' is the vapour pressure of benzene in the solution.
  • KH is Henry’s constant.
  • xB is the mole fraction of benzene in the solution.

From the graph plotted between the partial pressure of benzene and mole fraction of benzene,

When mole fraction of benzene (xB) is 0.4, the partial pressure of benzene (pB') is 10kPa.

Substitute the value of xB and pB' in equation (12).

    10kPa=0.4×KHKH=25kPa

The mole fraction of benzene in the vapour phase is given as,

    yB=KHxBp                                                                                                    (13)

The mole fraction of benzene (xB) is 0.984.

The total pressure of the mixture (p) when mole fraction of benzene is 0.984 is 35.534kPa.

Substitute the value of KH, xB, and p in the equation (8).

    yB=25kPa×0.98435.534kPa=0.6922

The activity of benzene (aB) is given as,

    aB=yBppB*                                                                                                     (10)

Substitute the values of yB, p, and pB* in equation (10).

    aB=0.6922×35.534kPa33.66kPa=0.73

The activity coefficient (γB) of benzene is given as,

    γB=aBxB                                                                                                       (11)

Substitute the value of aB and xB in equation (11).

    γB=0.7430.984=0.742

Similarly, the values of aB and γB are calculated for all values of xB in the table.

xBp/kPayBaBγB
0.98435.5340.6922950.7308380.742721
0.956135.2570.677950.7101160.742721
0.916534.8150.6581210.6807040.742721
0.886234.530.6416160.65820.742721
0.828633.350.6211390.6154190.742721
0.702731.470.558230.521910.742721
0.630429.910.5269140.4682120.742721
0.416625.260.4123120.3094180.742721
0.339623.370.3632860.2522280.742721
0.156316.760.2331440.1160870.742721
0.00697.760.0222290.0051250.742721

The excess Gibbs energy is given as,

    ΔGe=xERTlnγE+xBRTlnγB                                                                   (14)

Where,

  • R is the gas constant (8.314JK-1mol-1).
  • T is the temperature in Kelvin.

The temperature of the mixture is 50°C

The temperature values in degree Celsius is converted to Kelvin using the equation given below as,

    T(K)=T(°C)+273.15

Substitute the temperature value in the above equation as follows.

    T(K)=T(°C)+273.15=50+273.15=323.15K

The value of mole fraction of benzene (xB) is 0.984.

The value of mole fraction of ethanoic acid (xE) is 0.016.

The activity coefficient of benzene is (γB) is 0.7427.

The activity coefficient of ethanoic acid (γE) is 1.

Substitute the value of R, T, xB, xE, γB and γE in equation (14).

    ΔGe=xERTlnγE+xBRTlnγB=(0.016×8.314JK-1mol-1×323Kln1+0.984×8.314JK-1mol-1×323Kln0.7427)=0+0.984×8.314JK-1mol-1×323(-0.29)=766.3Jmol-1

Thus the excess Gibbs energy is 766.3Jmol-1_.

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Chapter 5 Solutions

Atkins' Physical Chemistry

Ch. 5 - Prob. 5A.4DQCh. 5 - Prob. 5A.5DQCh. 5 - Prob. 5A.1AECh. 5 - Prob. 5A.1BECh. 5 - Prob. 5A.2AECh. 5 - Prob. 5A.2BECh. 5 - Prob. 5A.3AECh. 5 - Prob. 5A.3BECh. 5 - Prob. 5A.4AECh. 5 - Prob. 5A.4BECh. 5 - Prob. 5A.5AECh. 5 - Prob. 5A.5BECh. 5 - Prob. 5A.6AECh. 5 - Prob. 5A.6BECh. 5 - Prob. 5A.7AECh. 5 - Prob. 5A.7BECh. 5 - Prob. 5A.8AECh. 5 - Prob. 5A.8BECh. 5 - Prob. 5A.9AECh. 5 - Prob. 5A.9BECh. 5 - Prob. 5A.10AECh. 5 - Prob. 5A.10BECh. 5 - Prob. 5A.11AECh. 5 - Prob. 5A.11BECh. 5 - Prob. 5A.1PCh. 5 - Prob. 5A.3PCh. 5 - Prob. 5A.4PCh. 5 - Prob. 5A.5PCh. 5 - Prob. 5A.6PCh. 5 - Prob. 5A.7PCh. 5 - Prob. 5B.1DQCh. 5 - Prob. 5B.2DQCh. 5 - Prob. 5B.3DQCh. 5 - Prob. 5B.4DQCh. 5 - Prob. 5B.5DQCh. 5 - Prob. 5B.6DQCh. 5 - Prob. 5B.7DQCh. 5 - Prob. 5B.1AECh. 5 - Prob. 5B.1BECh. 5 - Prob. 5B.2AECh. 5 - Prob. 5B.2BECh. 5 - Prob. 5B.3AECh. 5 - Prob. 5B.3BECh. 5 - Prob. 5B.4AECh. 5 - Prob. 5B.4BECh. 5 - Prob. 5B.5AECh. 5 - Prob. 5B.5BECh. 5 - Prob. 5B.6AECh. 5 - Prob. 5B.6BECh. 5 - Prob. 5B.7AECh. 5 - Prob. 5B.7BECh. 5 - Prob. 5B.8AECh. 5 - Prob. 5B.8BECh. 5 - Prob. 5B.9AECh. 5 - Prob. 5B.9BECh. 5 - Prob. 5B.10AECh. 5 - Prob. 5B.10BECh. 5 - Prob. 5B.11AECh. 5 - Prob. 5B.11BECh. 5 - Prob. 5B.12AECh. 5 - Prob. 5B.12BECh. 5 - Prob. 5B.1PCh. 5 - Prob. 5B.2PCh. 5 - Prob. 5B.3PCh. 5 - Prob. 5B.4PCh. 5 - Prob. 5B.5PCh. 5 - Prob. 5B.6PCh. 5 - Prob. 5B.9PCh. 5 - Prob. 5B.11PCh. 5 - Prob. 5B.13PCh. 5 - Prob. 5C.1DQCh. 5 - Prob. 5C.2DQCh. 5 - Prob. 5C.3DQCh. 5 - Prob. 5C.1AECh. 5 - Prob. 5C.1BECh. 5 - Prob. 5C.2AECh. 5 - Prob. 5C.2BECh. 5 - Prob. 5C.3AECh. 5 - Prob. 5C.3BECh. 5 - Prob. 5C.4AECh. 5 - Prob. 5C.4BECh. 5 - Prob. 5C.1PCh. 5 - Prob. 5C.2PCh. 5 - Prob. 5C.3PCh. 5 - Prob. 5C.4PCh. 5 - Prob. 5C.5PCh. 5 - Prob. 5C.6PCh. 5 - Prob. 5C.7PCh. 5 - Prob. 5C.8PCh. 5 - Prob. 5C.9PCh. 5 - Prob. 5C.10PCh. 5 - Prob. 5D.1DQCh. 5 - Prob. 5D.2DQCh. 5 - Prob. 5D.1AECh. 5 - Prob. 5D.1BECh. 5 - Prob. 5D.2AECh. 5 - Prob. 5D.2BECh. 5 - Prob. 5D.3AECh. 5 - Prob. 5D.3BECh. 5 - Prob. 5D.4AECh. 5 - Prob. 5D.4BECh. 5 - Prob. 5D.5AECh. 5 - Prob. 5D.5BECh. 5 - Prob. 5D.6AECh. 5 - Prob. 5D.1PCh. 5 - Prob. 5D.2PCh. 5 - Prob. 5D.3PCh. 5 - Prob. 5D.4PCh. 5 - Prob. 5D.5PCh. 5 - Prob. 5D.6PCh. 5 - Prob. 5D.7PCh. 5 - Prob. 5E.1DQCh. 5 - Prob. 5E.2DQCh. 5 - Prob. 5E.3DQCh. 5 - Prob. 5E.4DQCh. 5 - Prob. 5E.1AECh. 5 - Prob. 5E.1BECh. 5 - Prob. 5E.2AECh. 5 - Prob. 5E.2BECh. 5 - Prob. 5E.3AECh. 5 - Prob. 5E.3BECh. 5 - Prob. 5E.4AECh. 5 - Prob. 5E.4BECh. 5 - Prob. 5E.5AECh. 5 - Prob. 5E.5BECh. 5 - Prob. 5E.1PCh. 5 - Prob. 5E.2PCh. 5 - Prob. 5E.3PCh. 5 - Prob. 5F.1DQCh. 5 - Prob. 5F.2DQCh. 5 - Prob. 5F.3DQCh. 5 - Prob. 5F.4DQCh. 5 - Prob. 5F.5DQCh. 5 - Prob. 5F.1AECh. 5 - Prob. 5F.1BECh. 5 - Prob. 5F.2AECh. 5 - Prob. 5F.2BECh. 5 - Prob. 5F.3AECh. 5 - Prob. 5F.3BECh. 5 - Prob. 5F.4AECh. 5 - Prob. 5F.4BECh. 5 - Prob. 5F.5AECh. 5 - Prob. 5F.5BECh. 5 - Prob. 5F.6AECh. 5 - Prob. 5F.6BECh. 5 - Prob. 5F.7AECh. 5 - Prob. 5F.7BECh. 5 - Prob. 5F.8AECh. 5 - Prob. 5F.8BECh. 5 - Prob. 5F.1PCh. 5 - Prob. 5F.2PCh. 5 - Prob. 5F.3PCh. 5 - Prob. 5F.4PCh. 5 - Prob. 5.1IACh. 5 - Prob. 5.2IACh. 5 - Prob. 5.3IACh. 5 - Prob. 5.4IACh. 5 - Prob. 5.5IACh. 5 - Prob. 5.6IACh. 5 - Prob. 5.8IACh. 5 - Prob. 5.9IACh. 5 - Prob. 5.10IA
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