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 11431
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 42.170 |
0.20000 |
0.06300 |
0.29700 |
0.08300 |
| 39.610 |
0.67600 |
0.08000 |
0.45300 |
0.12100 |
| 36.450 |
0.79800 |
0.05400 |
0.53700 |
0.10600 |
| 41.850 |
0.53200 |
0.13700 |
0.38800 |
0.16600 |
| 42.823 |
0.32500 |
0.11900 |
0.31900 |
0.13500 |
| 43.076 |
0.25100 |
0.25300 |
0.27600 |
0.24200 |
| 42.290 |
0.34800 |
0.35700 |
0.31300 |
0.32000 |
| 41.423 |
0.46600 |
0.30800 |
0.35900 |
0.30900 |
| 37.664 |
0.44200 |
0.48500 |
0.38800 |
0.46600 |
| 38.850 |
0.35800 |
0.53100 |
0.34200 |
0.46900 |
| 40.677 |
0.13500 |
0.53300 |
0.18900 |
0.42700 |
| 39.597 |
0.05800 |
0.47600 |
0.10800 |
0.42300 |
| 38.877 |
0.09400 |
0.66200 |
0.14600 |
0.52600 |
| 37.344 |
0.14900 |
0.73000 |
0.21100 |
0.57800 |
| 36.997 |
0.26000 |
0.67000 |
0.30100 |
0.56200 |
| 34.157 |
0.06200 |
0.86600 |
0.11600 |
0.73600 |
| 40.730 |
0.41000 |
0.41200 |
0.34600 |
0.37700 |
| 39.903 |
0.20900 |
0.60200 |
0.24700 |
0.47400 |
| 42.130 |
0.21100 |
0.39800 |
0.24600 |
0.33900 |
| 36.490 |
0.76000 |
0.14300 |
0.52600 |
0.23900 |
| 36.370 |
0.68400 |
0.25200 |
0.49700 |
0.35000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.: By Ethanol, Acetonitrile and Benzene. Fluid Phase Equilib. 19 (1985) 13-20 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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