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 17033
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 3 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 4 |
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] |
x3 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
y3 [mol/mol] |
| 87.779 |
0.36600 |
0.16300 |
0.15000 |
0.44700 |
0.17100 |
0.09900 |
| 87.166 |
0.26700 |
0.09500 |
0.08700 |
0.46200 |
0.09100 |
0.06500 |
| 89.193 |
0.38000 |
0.05500 |
0.07100 |
0.51000 |
0.05700 |
0.05300 |
| 89.139 |
0.38300 |
0.10600 |
0.07200 |
0.49100 |
0.10800 |
0.05400 |
| 88.299 |
0.27700 |
0.16500 |
0.07400 |
0.43500 |
0.17000 |
0.05000 |
| 86.300 |
0.27400 |
0.11100 |
0.15800 |
0.43300 |
0.10900 |
0.11600 |
| 89.857 |
0.46400 |
0.10600 |
0.06900 |
0.51700 |
0.11200 |
0.04900 |
| 86.140 |
0.25900 |
0.19800 |
0.14300 |
0.39600 |
0.20100 |
0.10000 |
| 85.153 |
0.19000 |
0.11600 |
0.06200 |
0.42300 |
0.12800 |
0.05000 |
| 91.219 |
0.47000 |
0.15500 |
0.06700 |
0.49500 |
0.16300 |
0.05000 |
| 81.607 |
0.20100 |
0.11700 |
0.25000 |
0.36700 |
0.12100 |
0.17000 |
| 91.859 |
0.46100 |
0.17100 |
0.02800 |
0.49600 |
0.17900 |
0.02900 |
| 89.699 |
0.62400 |
0.04400 |
0.06400 |
0.58400 |
0.05000 |
0.05100 |
| 90.566 |
0.60500 |
0.09600 |
0.06600 |
0.57000 |
0.11100 |
0.04900 |
| 88.673 |
0.30700 |
0.30300 |
0.15200 |
0.37400 |
0.32200 |
0.09400 |
| 88.273 |
0.53400 |
0.04600 |
0.14100 |
0.55000 |
0.04900 |
0.10000 |
| 80.353 |
0.16800 |
0.22600 |
0.26500 |
0.29900 |
0.25200 |
0.17100 |
| 89.913 |
0.55000 |
0.04600 |
0.06900 |
0.55800 |
0.05000 |
0.05600 |
| 89.433 |
0.37800 |
0.16400 |
0.08800 |
0.46300 |
0.17100 |
0.06100 |
| 88.393 |
0.46500 |
0.14300 |
0.14300 |
0.49200 |
0.15500 |
0.09900 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.; Tamura K.: Vapor-Liquid Equilibria for Methanol + Acetone + Acetonitrile + Benzene at 328.15 K. J.Chem.Eng.Data 41 (1996) 1135-1137 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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