Isothermal Vapor-Liquid Equilibrium Measurements for Alcohol + Water/n-Hexane Azeotropic Systems Using Both Dynamic and Automated Static-Synthetic Methods Moodley, K.; Naidoo, P.; Raal, J.D.; Ramjugernath, D.; Journal of Chemical & Engineering Data 2019, 64, 2657-2670
- Journal: Journal of Chemical & Engineering Data
- Sample Quantity(ies): Vapor pressure
- Methodology: Closed cell (Static) method
- Phase(s): Liquid
- Substances:
Data
| x (mol mol-1) | P (kPa) |
| 0 | 14.37 |
| 0.0041 | 15.68 |
| 0.0082 | 16.74 |
| 0.0123 | 17.78 |
| 0.0163 | 18.79 |
| 0.0203 | 19.68 |
| 0.0361 | 23.48 |
| 0.0438 | 25.19 |
| 0.0515 | 26.82 |
| 0.0590 | 28.37 |
| 0.0664 | 29.85 |
| 0.0005 | 14.56 |
| 0.0737 | 31.26 |
| 0.0881 | 33.87 |
| 0.1020 | 36.25 |
| 0.1088 | 37.35 |
| 0.1156 | 38.41 |
| 0.1288 | 40.38 |
| 0.1448 | 42.6 |
| 0.1602 | 44.58 |
| 0.1751 | 46.35 |
| 0.2171 | 50.65 |
| 0.0009 | 14.66 |
| 0.2428 | 52.85 |
| 0.3005 | 56.79 |
| 0.3212 | 57.91 |
| 0.3933 | 60.94 |
| 0.4311 | 62.09 |
| 0.4645 | 62.92 |
| 0.4941 | 63.56 |
| 0.5207 | 64.07 |
| 0.5446 | 64.48 |
| 0.5001 | 63.69 |
| 0.0015 | 14.8 |
| 0.5201 | 64.07 |
| 0.5418 | 64.44 |
| 0.5653 | 64.83 |
| 0.5911 | 65.22 |
| 0.6192 | 65.63 |
| 0.6503 | 66.07 |
| 0.6844 | 66.53 |
| 0.7432 | 67.3 |
| 0.7884 | 67.84 |
| 0.8392 | 68.35 |
| 0.0018 | 14.89 |
| 0.8792 | 68.61 |
| 0.9036 | 68.68 |
| 0.9293 | 68.66 |
| 0.9495 | 68.57 |
| 0.9565 | 68.52 |
| 0.9633 | 68.45 |
| 0.9705 | 68.38 |
| 0.9778 | 68.29 |
| 0.9852 | 68.19 |
| 0.9924 | 68.07 |
| 0.0025 | 15.08 |
| 1 | 67.73 |
| 0.0044 | 15.54 |
| 0.0051 | 15.73 |
| 0.0058 | 15.91 |
9428; dl-2-butanol + hexane; 00002:00120