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:16
- Phase(s): Liquid
- Substances:
Data
| x (mol mol-1) | Tbp (K) |
| 0 | 430.06 |
| 0.475 | 404.05 |
| 0.536 | 402.1 |
| 0.596 | 400.38 |
| 0.657 | 398.44 |
| 0.699 | 397.06 |
| 0.753 | 395.71 |
| 0.806 | 394.29 |
| 0.853 | 393.17 |
| 0.900 | 392.06 |
| 0.940 | 391.09 |
| 0.041 | 427.08 |
| 0.974 | 390.35 |
| 1 | 389.9 |
| 0.078 | 424.37 |
| 0.135 | 420.74 |
| 0.191 | 417.06 |
| 0.265 | 413.15 |
| 0.321 | 410.38 |
| 0.372 | 408.49 |
| 0.427 | 406.08 |
30022; 2-methylpropyl ethanoate + hexan-1-ol; 00045:00317