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 14660
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 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
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] |
| 67.874 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 27.771 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
| 23.198 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
| 41.597 |
0.41100 |
0.39800 |
0.33200 |
0.34300 |
| 50.303 |
0.38300 |
0.19400 |
0.25100 |
0.13900 |
| 44.703 |
0.30300 |
0.42100 |
0.25800 |
0.31300 |
| 37.184 |
0.69900 |
0.19900 |
0.48600 |
0.27400 |
| 40.957 |
0.61700 |
0.20200 |
0.41100 |
0.22600 |
| 37.437 |
0.53400 |
0.37900 |
0.42500 |
0.40300 |
| 41.357 |
0.51900 |
0.29200 |
0.37200 |
0.28400 |
| 57.382 |
0.10800 |
0.21400 |
0.08300 |
0.11200 |
| 60.755 |
0.12500 |
0.12800 |
0.08700 |
0.06500 |
| 40.037 |
0.19400 |
0.60700 |
0.22200 |
0.46300 |
| 46.823 |
0.20500 |
0.42000 |
0.18600 |
0.28000 |
| 58.155 |
0.20700 |
0.13000 |
0.13700 |
0.07200 |
| 48.596 |
0.10400 |
0.44300 |
0.10300 |
0.27300 |
| 37.624 |
0.08900 |
0.73800 |
0.13300 |
0.56400 |
| 37.410 |
0.29600 |
0.60100 |
0.31400 |
0.51100 |
| 45.810 |
0.09800 |
0.51900 |
0.11000 |
0.34400 |
| 38.530 |
0.09700 |
0.71200 |
0.13700 |
0.54900 |
| 37.557 |
0.19600 |
0.71400 |
0.25400 |
0.59300 |
| 36.530 |
0.19200 |
0.70800 |
0.24600 |
0.58200 |
| 35.810 |
0.14700 |
0.75600 |
0.20900 |
0.62400 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.; Miyazaki K.: Isothermal vapour-liquid equilibrium for the ternary system ethanol + acetonitrile + acetone at 45 °C. Thermochim.Acta 206 (1992) 285-296 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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