Phase equilibria in the ternary system isobutyl alcohol + isobutyl acetate + 1-hexanol and the binary systems isobutyl alcohol + 1-hexanol, isobutyl acetate + 1-hexanol at 101.3 kPa Muñoz, R.; Montón, J.; Burguet, M.; de la Torre, J.; Fluid Phase Equilibria 2005, 235, 64-71
- Journal: Fluid Phase Equilibria
- Sample Quantity(ies): Boiling point at pressure
- Methodology: EBULLIO:UFactor:8
- Phase(s): Liquid
- Substances:
Data
| x (mol mol-1) | Tbp (K) |
| 0 | 430.06 |
| 0.229 | 409.73 |
| 0.312 | 404.53 |
| 0.351 | 402.58 |
| 0.412 | 399.65 |
| 0.470 | 397.38 |
| 0.521 | 395.03 |
| 0.575 | 392.85 |
| 0.629 | 390.97 |
| 0.686 | 389.01 |
| 0.743 | 387.29 |
| 0.008 | 429.13 |
| 0.792 | 385.82 |
| 0.847 | 384.3 |
| 0.896 | 383.13 |
| 0.941 | 382.04 |
| 1 | 381.09 |
| 0.050 | 424.7 |
| 0.054 | 424.27 |
| 0.079 | 422.16 |
| 0.101 | 419.8 |
| 0.116 | 418.49 |
| 0.145 | 415.88 |
| 0.205 | 411.53 |
30021; 2-methyl-1-propanol + hexan-1-ol; 00045:00147