Dortmund Data Bank
Vapor-Liquid Equilibrium Data
The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.
Vapor-Liquid Equilibrium Data Set 7057
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
| 41.361 |
0.33260 |
0.66740 |
| 41.326 |
0.32730 |
0.65700 |
| 41.033 |
0.31530 |
0.63270 |
| 40.639 |
0.30020 |
0.60250 |
| 40.194 |
0.28380 |
0.56950 |
| 39.521 |
0.26390 |
0.52970 |
| 39.071 |
0.25070 |
0.50310 |
| 38.477 |
0.23410 |
0.46990 |
| 37.828 |
0.21720 |
0.43580 |
| 42.089 |
0.66940 |
0.33060 |
| 42.061 |
0.65460 |
0.32330 |
| 41.949 |
0.63100 |
0.31160 |
| 41.749 |
0.60100 |
0.29690 |
| 41.434 |
0.56870 |
0.28090 |
| 40.999 |
0.52910 |
0.26130 |
| 40.641 |
0.50230 |
0.24810 |
| 40.177 |
0.46960 |
0.23190 |
| 39.579 |
0.42950 |
0.21210 |
| 38.460 |
0.65430 |
0.02340 |
| 38.987 |
0.63140 |
0.05760 |
| 39.526 |
0.60360 |
0.09910 |
| 40.025 |
0.57040 |
0.14870 |
| 40.451 |
0.53050 |
0.20820 |
| 40.635 |
0.50400 |
0.24780 |
| 40.785 |
0.47050 |
0.29770 |
| 40.833 |
0.43780 |
0.34650 |
| 37.116 |
0.32960 |
0.02080 |
| 37.286 |
0.31770 |
0.05610 |
| 37.416 |
0.30220 |
0.10220 |
| 37.493 |
0.28420 |
0.15590 |
| 37.484 |
0.26460 |
0.21400 |
| 37.448 |
0.25110 |
0.25440 |
| 37.269 |
0.23410 |
0.30480 |
| 37.250 |
0.21740 |
0.35440 |
| 28.164 |
0.02110 |
0.33600 |
| 30.845 |
0.05750 |
0.32350 |
| 33.391 |
0.10560 |
0.30700 |
| 35.218 |
0.15600 |
0.28970 |
| 36.894 |
0.21860 |
0.26830 |
| 37.637 |
0.25960 |
0.25420 |
| 38.370 |
0.31030 |
0.23680 |
| 38.930 |
0.36140 |
0.21930 |
| 30.230 |
0.02030 |
0.65610 |
| 32.436 |
0.05650 |
0.63180 |
| 34.684 |
0.10280 |
0.60080 |
| 36.676 |
0.15370 |
0.56670 |
| 38.160 |
0.21370 |
0.52660 |
| 39.007 |
0.25410 |
0.49950 |
| 39.995 |
0.31610 |
0.45800 |
| 40.359 |
0.35140 |
0.43440 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Wilson S.R.; Patel R.B.; Abbott M.M.; van Ness H.C.: Excess Thermodynamic Functions for Ternary Systems. J.Chem.Eng.Data 24 (1979) 130-132 |
List of All References
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH