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 133
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 76.047 |
0.00000 |
0.00000 |
| 107.484 |
0.00500 |
0.28500 |
| 130.869 |
0.01600 |
0.40700 |
| 138.002 |
0.03300 |
0.43800 |
| 141.868 |
0.06000 |
0.46300 |
| 143.468 |
0.07900 |
0.47200 |
| 145.108 |
0.09800 |
0.48200 |
| 147.148 |
0.14500 |
0.48800 |
| 148.308 |
0.17500 |
0.49600 |
| 148.988 |
0.21800 |
0.49900 |
| 149.348 |
0.39900 |
0.51200 |
| 149.561 |
0.47900 |
0.51600 |
| 149.641 |
0.52200 |
0.51700 |
| 149.494 |
0.57000 |
0.52000 |
| 149.388 |
0.61300 |
0.52100 |
| 149.308 |
0.65700 |
0.52200 |
| 149.254 |
0.73300 |
0.52300 |
| 148.961 |
0.79000 |
0.52400 |
| 147.761 |
0.82800 |
0.53300 |
| 145.028 |
0.87700 |
0.54000 |
| 144.241 |
0.88300 |
0.54300 |
| 141.762 |
0.90200 |
0.56100 |
| 138.495 |
0.91900 |
0.57400 |
| 131.603 |
0.93800 |
0.61600 |
| 126.470 |
0.95100 |
0.64500 |
| 121.590 |
0.96200 |
0.68100 |
| 116.670 |
0.96700 |
0.71400 |
| 111.484 |
0.97900 |
0.75200 |
| 110.471 |
0.98000 |
0.76300 |
| 83.900 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Scheller M.; Schuberth H.; Koennecke H.G.: Ergebnisse von Dampfflüssigkeits-Phasengleichgewichtsuntersuchungen am System n-Hexan-Methylcyclohexan-Methanol bei 60°C. J.Prakt.Chem. 311 (1969) 974-982 |
Vapor-Liquid Equilibrium Data Set 155
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 44.396 |
0.00000 |
0.00000 |
| 73.301 |
0.04500 |
0.41720 |
| 82.567 |
0.11370 |
0.48440 |
| 83.513 |
0.24180 |
0.49330 |
| 84.020 |
0.51330 |
0.49880 |
| 84.033 |
0.76870 |
0.49190 |
| 83.766 |
0.77600 |
0.49930 |
| 83.206 |
0.87490 |
0.50700 |
| 82.407 |
0.89570 |
0.50700 |
| 82.287 |
0.90980 |
0.50140 |
| 80.913 |
0.91850 |
0.52610 |
| 80.220 |
0.92260 |
0.52550 |
| 81.460 |
0.92820 |
0.51900 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Ferguson J.B.: The System Methyl Alcohol-n-Hexane at 45 Degrees. J.Phys.Chem. 36 (1932) 1123-1128 |
Diagrams
List of All References
| Source |
| Ferguson J.B.: The System Methyl Alcohol-n-Hexane at 45 Degrees. J.Phys.Chem. 36 (1932) 1123-1128 |
| Scheller M.; Schuberth H.; Koennecke H.G.: Ergebnisse von Dampfflüssigkeits-Phasengleichgewichtsuntersuchungen am System n-Hexan-Methylcyclohexan-Methanol bei 60°C. J.Prakt.Chem. 311 (1969) 974-982 |
Vapor-Liquid Equilibrium Data Overview
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