Isothermal vapor-liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol + 1-hexene + methylbenzene at 313.15 K Belabbaci, A.; Ghezouali, C.; Villamañán, R.M.; Segovia, J.J.; Villamañán, M.A.; Negadi, L.; Fluid Phase Equilibria 2015, 386, 1-6
- Journal: Fluid Phase Equilibria
- Sample Quantity(ies): Vapor pressure
- Methodology: Closed cell (Static) method
- Phase(s): Liquid
- Substances:
Data
| T (K) | P (kPa) |
| 313.15 | 45.002 |
1990; 1-hexene; 00650