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 9827
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
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Constant Value
Data Table
| x1 [mol/mol] |
y1 [mol/mol] |
| 0.10000 |
0.51300 |
| 0.20100 |
0.60700 |
| 0.34300 |
0.66000 |
| 0.40000 |
0.67300 |
| 0.59800 |
0.74400 |
| 0.80000 |
0.81700 |
| 0.90000 |
0.86600 |
(x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kudryavtseva L.S.; Viit H.; Eizen O.G.: 1. Das Flüssigkeit-Dampf-Gleichgewicht der binären Systeme, die Hexen-1 mit Methanol, Äthanol, Isopropanol und Propanol bildet. Eesti NSV Tead.Akad.Toim.Keem.Geol. 18 (1969) 346-352 |
Vapor-Liquid Equilibrium Data Set 16723
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 355.51 |
0.00000 |
0.00000 |
| 350.95 |
0.02400 |
0.12600 |
| 345.70 |
0.07700 |
0.32100 |
| 344.39 |
0.09200 |
0.36400 |
| 343.92 |
0.10500 |
0.37800 |
| 339.71 |
0.18200 |
0.51300 |
| 338.32 |
0.20900 |
0.54900 |
| 337.09 |
0.26100 |
0.57800 |
| 335.71 |
0.31000 |
0.61900 |
| 335.00 |
0.36100 |
0.64300 |
| 334.41 |
0.41000 |
0.66700 |
| 333.96 |
0.44500 |
0.68900 |
| 333.28 |
0.50600 |
0.69100 |
| 332.76 |
0.59400 |
0.72700 |
| 332.56 |
0.65300 |
0.74800 |
| 332.53 |
0.65700 |
0.73700 |
| 332.51 |
0.74600 |
0.76900 |
| 332.38 |
0.75200 |
0.77500 |
| 331.77 |
0.77600 |
0.78500 |
| 331.58 |
0.79800 |
0.79300 |
| 332.44 |
0.83900 |
0.81500 |
| 332.49 |
0.87300 |
0.84300 |
| 336.65 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Wisniak J.; Gabai E.: Isobaric Vapor-Liquid Equilibria in the Systems Methyl Acetate + 1-Hexene + 2-Propanol. J.Chem.Eng.Data 41 (1996) 143-146 |
Diagrams
List of All References
| Source |
| Kudryavtseva L.S.; Viit H.; Eizen O.G.: 1. Das Flüssigkeit-Dampf-Gleichgewicht der binären Systeme, die Hexen-1 mit Methanol, Äthanol, Isopropanol und Propanol bildet. Eesti NSV Tead.Akad.Toim.Keem.Geol. 18 (1969) 346-352 |
| Wisniak J.; Gabai E.: Isobaric Vapor-Liquid Equilibria in the Systems Methyl Acetate + 1-Hexene + 2-Propanol. J.Chem.Eng.Data 41 (1996) 143-146 |
Vapor-Liquid Equilibrium Data Overview
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