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): Mole fraction
- Methodology: CHROM:UFactor:4
- Phase(s): Gas' Liquid
- Substances:
Data
| x (mol mol-1) | x (mol mol-1) |
| 0.0252 | 0.2009 |
| 0.4629 | 0.7923 |
| 0.5241 | 0.8087 |
| 0.5834 | 0.8267 |
| 0.6420 | 0.837 |
| 0.6967 | 0.8506 |
| 0.7526 | 0.8669 |
| 0.8062 | 0.8891 |
| 0.8576 | 0.9126 |
| 0.9003 | 0.9349 |
| 0.9354 | 0.9539 |
| 0.0494 | 0.3211 |
| 0.9504 | 0.9634 |
| 0.9674 | 0.9741 |
| 0.9832 | 0.9858 |
| 0.0730 | 0.411 |
| 0.0968 | 0.4693 |
| 0.1454 | 0.5734 |
| 0.2022 | 0.6453 |
| 0.2707 | 0.708 |
| 0.3365 | 0.7435 |
| 0.4007 | 0.7706 |
9769; 1-propanol + isopropyl ether; 00101:00250