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): Mass density
- Methodology: VIBTUB:UFactor:4
- Phase(s): Liquid
- Substances:
Data
| T (K) | P (kPa) | ρ (kg m-3) |
| 298.15 | 101.325 | 814.85 |
72; 1-hexanol; 00045