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 14419
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 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] |
| 68.208 |
0.09600 |
0.13400 |
0.18200 |
0.22900 |
0.11500 |
0.17100 |
| 70.141 |
0.17200 |
0.21800 |
0.15500 |
0.27300 |
0.14000 |
0.14700 |
| 70.741 |
0.23100 |
0.26200 |
0.12000 |
0.32000 |
0.14300 |
0.12100 |
| 59.942 |
0.05100 |
0.28000 |
0.43400 |
0.08100 |
0.23700 |
0.37800 |
| 60.915 |
0.09600 |
0.16000 |
0.60200 |
0.17900 |
0.14100 |
0.45100 |
| 68.181 |
0.16500 |
0.24800 |
0.22600 |
0.25600 |
0.15300 |
0.20600 |
| 56.342 |
0.05100 |
0.28300 |
0.54200 |
0.08800 |
0.24500 |
0.47500 |
| 68.301 |
0.14400 |
0.24500 |
0.22700 |
0.22900 |
0.15900 |
0.20800 |
| 80.420 |
0.38700 |
0.12700 |
0.11600 |
0.46800 |
0.05500 |
0.09900 |
| 60.768 |
0.12800 |
0.13600 |
0.63400 |
0.23800 |
0.11900 |
0.47700 |
| 72.541 |
0.49500 |
0.27200 |
0.06600 |
0.51300 |
0.11400 |
0.08100 |
| 69.048 |
0.24600 |
0.26500 |
0.25300 |
0.31600 |
0.14700 |
0.23100 |
| 69.368 |
0.13500 |
0.18300 |
0.17900 |
0.25700 |
0.12900 |
0.16600 |
| 71.861 |
0.17600 |
0.17400 |
0.19000 |
0.30000 |
0.11200 |
0.16500 |
| 68.181 |
0.16400 |
0.25400 |
0.22600 |
0.25400 |
0.15400 |
0.20600 |
| 71.901 |
0.25500 |
0.22200 |
0.21700 |
0.34200 |
0.11800 |
0.19000 |
| 61.955 |
0.08500 |
0.39800 |
0.13500 |
0.13400 |
0.25700 |
0.15800 |
| 67.381 |
0.11400 |
0.13000 |
0.38700 |
0.22900 |
0.10400 |
0.30000 |
| 78.927 |
0.36600 |
0.14100 |
0.14200 |
0.44800 |
0.06400 |
0.12100 |
| 71.501 |
0.25500 |
0.22900 |
0.20800 |
0.34000 |
0.12200 |
0.18400 |
| 71.194 |
0.24500 |
0.23600 |
0.20700 |
0.33200 |
0.12600 |
0.18700 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.; Fukushima Y.; Miyazaki K.: Vapour-liquid equilibrium in the quaternary system methanol-2-propanol-acetonitrile-benzene at 55°C. Fluid Phase Equilib. 71 (1992) 17-27 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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