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 15812
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 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] |
| 73.514 |
0.10100 |
0.29900 |
0.45500 |
0.09500 |
0.28300 |
0.45700 |
| 73.341 |
0.11800 |
0.30800 |
0.33600 |
0.09000 |
0.28400 |
0.38900 |
| 72.941 |
0.13700 |
0.14000 |
0.55300 |
0.12200 |
0.15200 |
0.53100 |
| 74.461 |
0.11100 |
0.22000 |
0.48900 |
0.10000 |
0.21800 |
0.48500 |
| 75.727 |
0.03400 |
0.23000 |
0.48800 |
0.02700 |
0.21900 |
0.47300 |
| 68.154 |
0.03700 |
0.65700 |
0.18100 |
0.04100 |
0.53600 |
0.25400 |
| 74.021 |
0.10900 |
0.21700 |
0.41600 |
0.08700 |
0.21600 |
0.44400 |
| 67.088 |
0.09300 |
0.52300 |
0.08800 |
0.08100 |
0.47500 |
0.14100 |
| 72.034 |
0.11200 |
0.34600 |
0.24300 |
0.08000 |
0.31600 |
0.32900 |
| 73.581 |
0.11500 |
0.27800 |
0.33100 |
0.08400 |
0.26500 |
0.39200 |
| 73.434 |
0.13300 |
0.28200 |
0.49600 |
0.13300 |
0.27500 |
0.48500 |
| 68.034 |
0.07500 |
0.07900 |
0.78400 |
0.10800 |
0.10700 |
0.65200 |
| 71.861 |
0.18600 |
0.19700 |
0.44100 |
0.15600 |
0.20200 |
0.46300 |
| 73.061 |
0.14400 |
0.23500 |
0.37000 |
0.11400 |
0.23700 |
0.41100 |
| 60.502 |
0.05200 |
0.04900 |
0.07800 |
0.03400 |
0.09800 |
0.20700 |
| 67.221 |
0.07700 |
0.59200 |
0.12900 |
0.07100 |
0.49700 |
0.20200 |
| 74.167 |
0.10100 |
0.26900 |
0.48200 |
0.09400 |
0.25800 |
0.47400 |
| 69.928 |
0.22700 |
0.24600 |
0.20600 |
0.16500 |
0.26600 |
0.29100 |
| 69.194 |
0.10000 |
0.31800 |
0.12900 |
0.06600 |
0.33400 |
0.22400 |
| 73.167 |
0.17800 |
0.19600 |
0.33300 |
0.12400 |
0.22500 |
0.39600 |
| 61.328 |
0.07100 |
0.81500 |
0.07400 |
0.11500 |
0.69800 |
0.12700 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.: Isothermal (vapour + liquid) equilibria of (ethanol + propan-2-ol + acetonitrile + benzene) and (propan-2-ol + butan-2-ol + acetonitrile + benzene). J.Chem.Thermodyn. 26 (1994) 1287-1291 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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