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 18042
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 4 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
x3 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
y3 [mol/mol] |
| 43.263 |
0.10700 |
0.33700 |
0.26900 |
0.15000 |
0.27700 |
0.31100 |
| 40.423 |
0.05000 |
0.54400 |
0.21200 |
0.07100 |
0.42800 |
0.28300 |
| 44.530 |
0.19800 |
0.41300 |
0.17500 |
0.27300 |
0.30800 |
0.21100 |
| 41.717 |
0.15100 |
0.56100 |
0.22700 |
0.21900 |
0.42000 |
0.27500 |
| 38.650 |
0.04500 |
0.58800 |
0.11900 |
0.06600 |
0.48000 |
0.19300 |
| 42.796 |
0.05000 |
0.26800 |
0.52900 |
0.07200 |
0.24700 |
0.47400 |
| 43.743 |
0.16300 |
0.42400 |
0.33100 |
0.22200 |
0.33000 |
0.33700 |
| 43.970 |
0.12500 |
0.17400 |
0.61400 |
0.18900 |
0.17300 |
0.49700 |
| 46.516 |
0.17200 |
0.16300 |
0.42800 |
0.23700 |
0.14500 |
0.38800 |
| 43.023 |
0.05400 |
0.24300 |
0.47000 |
0.07400 |
0.22200 |
0.45000 |
| 46.543 |
0.19400 |
0.19100 |
0.34800 |
0.26700 |
0.15700 |
0.33800 |
| 42.943 |
0.05100 |
0.16400 |
0.46600 |
0.07100 |
0.16400 |
0.46400 |
| 44.503 |
0.10400 |
0.16700 |
0.33800 |
0.15300 |
0.16100 |
0.37900 |
| 43.223 |
0.05100 |
0.08800 |
0.45700 |
0.08100 |
0.09800 |
0.48600 |
| 44.156 |
0.10600 |
0.07000 |
0.41100 |
0.16500 |
0.07200 |
0.44000 |
| 44.383 |
0.15200 |
0.33100 |
0.23000 |
0.21000 |
0.26900 |
0.27800 |
| 44.023 |
0.15700 |
0.40600 |
0.22700 |
0.21600 |
0.31000 |
0.26100 |
| 42.716 |
0.10500 |
0.40100 |
0.24800 |
0.14400 |
0.31700 |
0.31300 |
| 43.210 |
0.20700 |
0.48700 |
0.23900 |
0.29300 |
0.35200 |
0.26400 |
| 43.343 |
0.07300 |
0.11700 |
0.67600 |
0.12400 |
0.12200 |
0.54400 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.; Tamura K.: Isothermal (vapour + liquid) equilibria of (ethanol + propanone + acetonitrile + benzene) at the temperature 318.15 K. J.Chem.Thermodyn. 30 (1998) 153-159 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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