The upper critical solution temperature has been reported as 403.7 K,4 417.2 K,1 and 417.65 K.2 The UCST of McLure et al.4 is rejected. The remaining values give an average recommended value of: UCST = 417.5 ±0.4 K. The corresponding critical solution composition has been reported as xcl = 0.8358.2
All experimental values reported2 have been approximated by an equation based on the scaling law (described in the introduction to this volume) for which the following parameters have been derived:
For approximation xcl and UCST from Rogalski and Stryjek2 have been used. In the opinion of the evaluators, the mutual solubilities calculated by this equation may be treated as tentative. The results of calculations for the selected temperatures are presented in the following table. This relationship together with experimental points2-3 are also presented in Fig. 12.
Calculated mutual solubility of acetonitrile (1) and hexadecane (2)
| C T (K) | D 100w1 | D x1 |
|---|---|---|
| 313.2 | 1.7 | 7.9 x 10-2 |
| 333.2 | 3.9 | 1.63 x 10-1 |
| 343.2 | 5.2 | 2.09 x 10-1 |
| 353.2 | 6.7 | 2.57 x 10-1 |
| 363.2 | 8.5 | 3.09 x 10-1 |
| 373.2 | 10.6 | 3.64 x 10-1 |
| 383.2 | 13.3 | 4.26 x 10-1 |
| 393.2 | 16.9 | 4.95 x 10-1 |
| 403.2 | 22.0 | 5.77 x 10-1 |
| 408.2 | 25.8 | 6.27 x 10-1 |
| 413.2 | 31.6 | 6.91 x 10-1 |
| 414.2 | 33.3 | 7.07 x 10-1 |
| 415.2 | 35.4 | 7.26 x 10-1 |
| 416.2 | 38.0 | 7.48 x 10-1 |
| 416.7 | 40.0 | 7.63 x 10-1 |
| 417.2 | 42.6 | 7.82 x 10-1 |
| 313.2 | 99.8 | 9.99 x 10-1 |
| 333.2 | 95.8 | 9.91 x 10-1 |
| 343.2 | 93.1 | 9.85 x 10-1 |
| 353.2 | 91.0 | 9.80 x 10-1 |
| 363.2 | 88.6 | 9.74 x 10-1 |
| 373.2 | 86.2 | 9.68 x 10-1 |
| 383.2 | 84.0 | 9.62 x 10-1 |
| 393.2 | 81.1 | 9.54 x 10-1 |
| 403.2 | 77.1 | 9.42 x 10-1 |
| 408.2 | 74.2 | 9.33 x 10-1 |
| 413.2 | 69.9 | 9.18 x 10-1 |
| 414.2 | 68.5 | 9.13 x 10-1 |
| 415.2 | 66.9 | 9.07 x 10-1 |
| 416.2 | 64.6 | 8.98 x 10-1 |
| 416.7 | 62.8 | 8.91 x 10-1 |
| 417.2 | 60.3 | 8.80 x 10-1 |
Figure
References:
1
Schmid, H. H. O.; Mangold, H. K.; Lundberg, W. O.; J. Am. Oil Chem. Soc. 42, 372 (1965).
2
Rogalski, M.; Stryjek, R.; Bull. Acad. Pol. Sci.; Ser. Sci. Chim. 28, 139-47 (1980).
3
Stryjek, R.; Luszczyk, M.; Fedorko-Antosik, M.; Bull. Acad. Pol. Sci.: Ser. Sci. Chim. 29, 203-211 (1981).
4
McLure, I. A.; Rodriguez, A. T.; Ingham, P. A.; Steele, J. F.; Fluid Phase Equilib. 8, 271 (1982).