Isothermal vapor-liquid equilibrium at 333.15 K and excess molar volumes at 298.15 K for the ternary system di-isopropyl ether + n-propyl alcohol + toluene and its binary subsystems Hwang, I.C.; Park, S.J.; Lee, S.Y.; Ahn, H.S.; Fluid Phase Equilibria 2008, 270, 103-108
- Journal: Fluid Phase Equilibria
- Sample Quantity(ies): Mass density
- Methodology: VIBTUB:UFactor:2
- Phase(s): Liquid
- Substances:
Data
| x (mol mol-1) | ρ (kg m-3) |
| 0.0508 | 794.63 |
| 0.9015 | 725.59 |
| 0.9514 | 722.22 |
| 0.0999 | 789.64 |
| 0.2000 | 779.84 |
| 0.2998 | 770.67 |
| 0.3993 | 762.07 |
| 0.4999 | 754.19 |
| 0.6006 | 746.71 |
| 0.7007 | 739.41 |
| 0.8001 | 732.66 |
9769; 1-propanol + isopropyl ether; 00101:00250