Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa Montón, J.; Muñoz, R.; Burguet, M.; Torre, J.d.l.; Fluid Phase Equilibria 2005, 227, 19-25
- 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 | 797.83 |
324; 2-methyl-1-propanol; 00147