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) |
| 0.0500 | 853.94 |
| 0.9003 | 731.28 |
| 0.9498 | 725.19 |
| 0.0995 | 845.89 |
| 0.2004 | 829.97 |
| 0.2999 | 814.46 |
| 0.4001 | 799.53 |
| 0.5003 | 784.92 |
| 0.6001 | 770.99 |
| 0.7004 | 757.31 |
| 0.8003 | 744.27 |
30580; diisopropyl ether + toluene; 00023:00250