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2.6  Activity-Coefficient Models for the Liquid Phase  49



        EXAMPLE 2.7
                                                                                   I  atm
        yerazunis, plowright, and Smola [31] measured liquid-phase activ-
                                                                    -    aO  Experimental data for toluene   -
        ity  coefficients for the  n-heptaneltoluene system  over the  entire   and n-heptane,  respectively
        concentration range at  1 atm (101.3 kPa). Estimate activity coef-   - Regular solution theory
        ficients for the range of  conditions using regular-solution theory   Regular solution theory
        both with and  without  the  Flory-Huggins  correction. Compare     with Flory-Huggins  correction   -
               values with experimental data.

                                                                                                    -
        SOLUTION
        Experimental liquid-phase compositions and temperatures for 7 of 19
        points are as follows, where H denotes heptane andT denotes toluene:
                   T, "c      XH         XT
                   98.41     1 .OOOO   0.0000
                   98.70     0.9154    0.0846
                   99.58     0.7479    0.2521
                  101.47     0.5096    0.4904                     1.1 -                             -
                  104.52     0.2681    0.7319
                  107.57     0.1087    0.8913
                  110.60     0.0000     1  .OOOO
                                                                    0     0.2   0.4    0.6   0.8    1 .O
        ~t  25"C,  liquid  molar  volumes  are  VH,  = 147.5 cm3/mol and   Mole fraction of n-heptane
        e, 106.8 cm3/n~ol. Solubility parameten  are 7.43 and  8.914
           =
                                                           Figure Z.L4 Liquid-phase activity coefficients for
        (ca~cm')"~, respectively, for H and T. As  an example, consider   n-heptaneltoluene  system at  atm.
        mole fractions in the above table for 104.52"C. From (2-62), vol-
        ume fractions are
                         0.2681(147.5)                     Applying (2-67), with  the Flory-Huggins  correction, to the same
             QH =                         = 0.3359         data point gives
                  0.2681(147.5) + 0.7319(106.8)
              QT = 1 - QH = 1 - 0.3359 = 0.6641                    [         ( 147.5)  +   ( 147.5 )]
                                                                                       1
                                                            y~=exp 0.1923+ln  - -  - 1.179
                                                                                                   =
        Substitution of these values, together with the solubility parame-     117.73       117.73
        ters, into (2-64) gives
                                                           Values  of  y H  and y~  computed in this  manner  are included in
                 147.5[7.430 - 0.3359(7.430) - 0.6641(8.914)12   Figure 2.14. Deviations from experiment are not greater than 12%
         Y~=exp
                              1.987(377.67)                for regular-solution theory  and  not  greater than  6%  when  the
                                                           Flory-Huggins  correction is  included. Unfortunately,  such good
           = 1.212
                                                           agreement is not always obtained with nonpolar hydrocarbon solu-
        Values of y~ and y~ computed in this manner for all seven liquid-   tions, as shown, for example, by Hermsen and Prausnitz [32], who
        phase conditions are plotted in Figure 2.14.       studied the cyclopentane/benzene system.




                                                           Roman numerals refer to classification groups in Tables 2.7
        Nonideal Liquid Solutions
                                                           and 2.8. Starting with Figure 2.15a and taking the other plots
        When  liquids contain  dissimilar polar  species, particularly   in order,  we offer the following explanations for the non-
        those that can form or break hydrogen bonds, the ideal-liquid   idealities. Normal heptane (V) breaks ethanol (11) hydrogen
        solution assumption is almost always invalid and the regular-   bonds, causing strong positive  deviations. In Figure 2.15b,
        solution theory is not applicable. Ewell, Harrison, and Berg   similar but less positive deviations occur when acetone (111)
        [33] provide a very useful classification of molecules based   is  added  to  formamide  (I).  Hydrogen  bonds  are  broken
        on the potential for association or solvation due to hydrogen-   and  formed  with  chloroform  (IV)  and  methanol  (11)  in
        bond formation. If a molecule contains a hydrogen atom at-   Figure 2.15c, resulting in an unusual positive deviation curve
        tached to a donor atom (0, N, F, and in certain cases C), the   for chloroform that passes  through  a maximum.  In Figure
        active hydrogen atom can form a bond with another molecule   2.15d, chloroform (IV) provides active hydrogen atoms that
        containing a donor atom. The classification in Table 2.7 per-   can form hydrogen bonds with oxygen atoms of acetone (111),
        mits qualitative estimates of deviations from Raoult's law for   thus causing negative deviations. For water (I) and n-butanol
        binary pairs when used in conjunction with Table 2.8. Posi-   (11)  in Figure 2.15e, hydrogen bonds of both molecules are
        tive deviations correspond to values of yiL > 1. Nonideality   broken, and nonideality is sufficiently strong to cause forma-
        results in a variety of variations of y,~ with composition, as   tion of two immiscible liquid phases (phase splitting) over a
        shown in Figure 2.15 for several binary systems, where the   wide region of overall composition.
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