Test of the Regular Solution Model
Compare the regular solution theory predictions for the activity coefficients of the benzene–2,2,4-trimethyl pentane mixture with the experimental data given in Illustration 9.5-1.
Test of the Regular Solution Model
Compare the regular solution theory predictions for the activity coefficients of the benzene–2,2,4-trimethyl pentane mixture with the experimental data given in Illustration 9.5-1.
From Table 9.6-1 we have \underline{V}^{ L }=89 cc / mol \text { and } \delta=9.2( cal / cc )^{1 / 2} for benzene. The parameters for 2,2,4-trimethyl pentane are not given. However, the molar volume of this compound is approximately 165 cc/mol, and the solubility parameter can be estimated from
\delta=\left(\frac{\Delta_{ vap } \underline{U}}{\underline{V}^{ L }}\right)^{1 / 2}=\left(\frac{\Delta_{ vap } \underline{H}-R T}{\underline{V}^{ L }}\right)^{1 / 2}
where in the numerator we have neglected the liquid molar volume with respect to that of the vapor, and further assumed ideal vapor-phase behavior. Using the value of \Delta_{\text {vap }} \underline{H} found in Illustration 7.7-1, we obtain \delta=6.93( cal / cc )^{1 / 2}.
Our predictions for the activity coefficients, together with the experimental data, are plotted in Fig. 9.6-1. It is evident that although the regular solution theory prediction leads to activity coefficient behavior that is qualitatively correct, the quantitative agreement in this case is, in fact, poor. This example should serve as a warning that theoretical predictions may not always be accurate and that experimental data are to be preferred.
Table 9.6-1 Molar Liquid Volumes and Solubility Parameters of Some Nonpolar Liquids | ||
\underline{V}^{ L }( cc / mol ) | \delta( cal / cc )^{1 / 2} | |
Liquefied gases at 90 K | ||
Nitrogen | 38.1 | 5.3 |
Carbon monoxide | 37.1 | 5.7 |
Argon | 29.0 | 6.8 |
Oxygen | 28.0 | 7.2 |
Methane | 35.3 | 7.4 |
Carbon tetrafluoride | 46.0 | 8.3 |
Ethane | 45.7 | 9.5 |
Liquid solvents at 25°C | ||
Perfluoro-n-heptane | 226 | 6.0 |
Neopentane | 122 | 6.2 |
Isopentane | 117 | 6.8 |
n-Pentane | 116 | 7.1 |
n-Hexane | 132 | 7.3 |
1-Hexene | 126 | 7.3 |
n-Octane | 164 | 7.5 |
n-Hexadecane | 294 | 8.0 |
Cyclohexane | 109 | 8.2 |
Carbon tetrachloride | 97 | 8.6 |
Ethyl benzene | 123 | 8.8 |
Toluene | 107 | 8.9 |
Benzene | 89 | 9.2 |
Styrene | 116 | 9.3 |
Tetrachloroethylene | 103 | 9.3 |
Carbon disulfide | 61 | 10.0 |
Bromine | 51 | 11.5 |
Source: J. M. Prausnitz, Molecular Thermodynamics of Fluid-Phase Equilibria. 1969. Reprinted with permission from Prentice-Hall, Englewood Cliffs, N.J. Note: In regular solution theory the solubility parameter has traditionally been given in the units shown. For this reason the traditional units, rather than SI units, appear in this table. |