Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + 1,2-Ethanediol and Propene + Acetophenone Horstmann, S.; Gardeler, H.; Wilken, M.; Fischer, K.; Gmehling, J.; Journal of Chemical & Engineering Data 2004, 49, 1508-1511
- Journal: Journal of Chemical & Engineering Data
- Sample Quantity(ies): Vapor pressure
- Methodology: CCELL:UFactor:2
- Phase(s): Liquid
- Substances:
Data
| x (mol mol-1) | P (kPa) |
| 0 | 0.22 |
| 0.17827 | 3.43 |
| 0.23101 | 4.42 |
| 0.28891 | 5.52 |
| 0.34875 | 6.69 |
| 0.41455 | 7.99 |
| 0.47769 | 9.27 |
| 0.53779 | 10.49 |
| 0.59256 | 11.61 |
| 0.64202 | 12.64 |
| 0.68626 | 13.55 |
| 0.00327 | 0.28 |
| 0.72541 | 14.37 |
| 0.75942 | 15.09 |
| 0.78920 | 15.72 |
| 0.78979 | 15.81 |
| 0.82005 | 16.42 |
| 0.84816 | 16.99 |
| 0.87391 | 17.5 |
| 0.89719 | 17.94 |
| 0.91800 | 18.38 |
| 0.93601 | 18.74 |
| 0.00949 | 0.39 |
| 0.95154 | 19.04 |
| 0.96334 | 19.22 |
| 0.97303 | 19.43 |
| 0.98075 | 19.58 |
| 0.98667 | 19.7 |
| 0.99114 | 19.78 |
| 0.99405 | 19.83 |
| 0.99597 | 19.87 |
| 0.99740 | 19.92 |
| 0.99841 | 19.89 |
| 0.01634 | 0.51 |
| 0.99915 | 19.88 |
| 0.99968 | 19.92 |
| 1 | 19.93 |
| 0.02723 | 0.71 |
| 0.04142 | 0.96 |
| 0.06340 | 1.35 |
| 0.09276 | 1.87 |
| 0.13218 | 2.58 |
1643; 1,2-ethanediol + water; 00004:00068