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): Mole fraction
- Methodology: CHROM:UFactor:6
- Phase(s): Gas' Liquid
- Substances:
Data
| x (mol mol-1) | x (mol mol-1) |
| 0 | 0.0 |
| 0.475 | 0.784 |
| 0.536 | 0.818 |
| 0.596 | 0.844 |
| 0.657 | 0.881 |
| 0.699 | 0.895 |
| 0.753 | 0.917 |
| 0.806 | 0.937 |
| 0.853 | 0.955 |
| 0.900 | 0.969 |
| 0.940 | 0.982 |
| 0.041 | 0.129 |
| 0.974 | 0.992 |
| 1 | 1.0 |
| 0.078 | 0.241 |
| 0.135 | 0.366 |
| 0.191 | 0.484 |
| 0.265 | 0.584 |
| 0.321 | 0.655 |
| 0.372 | 0.698 |
| 0.427 | 0.74 |
30022; 2-methylpropyl ethanoate + hexan-1-ol; 00045:00317