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) |
| 0.0192 | 0.1066 |
| 0.4084 | 0.7644 |
| 0.4681 | 0.7993 |
| 0.5287 | 0.8284 |
| 0.5888 | 0.8549 |
| 0.6484 | 0.8764 |
| 0.7085 | 0.896 |
| 0.7688 | 0.9176 |
| 0.8293 | 0.9314 |
| 0.8789 | 0.9529 |
| 0.9198 | 0.9691 |
| 0.0399 | 0.1958 |
| 0.9393 | 0.9775 |
| 0.9603 | 0.985 |
| 0.9795 | 0.9926 |
| 0.0597 | 0.2703 |
| 0.0793 | 0.3269 |
| 0.1194 | 0.4249 |
| 0.1692 | 0.5232 |
| 0.2291 | 0.6117 |
| 0.2888 | 0.6749 |
| 0.3486 | 0.7221 |
30580; diisopropyl ether + toluene; 00023:00250