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): Vapor pressure
- Methodology: EBULLIO:UFactor:16
- Phase(s): Liquid
- Substances:
Data
| T (K) | P (kPa) |
| 389.90 | 101.3 |
1804; isobutyl acetate; 00317