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 706
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 353.25 |
0.00000 |
0.00000 |
| 350.75 |
0.07300 |
0.14000 |
| 348.25 |
0.17200 |
0.26800 |
| 346.55 |
0.26800 |
0.37600 |
| 345.15 |
0.37200 |
0.46000 |
| 344.05 |
0.46200 |
0.54000 |
| 343.15 |
0.58500 |
0.64400 |
| 342.55 |
0.69200 |
0.72500 |
| 342.25 |
0.79200 |
0.80700 |
| 342.15 |
0.82800 |
0.83800 |
| 342.05 |
0.88300 |
0.88800 |
| 341.95 |
0.94700 |
0.95000 |
| 341.95 |
0.96200 |
0.96400 |
| 341.95 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Prabhu P.S.; van Winkle M.: Effect of Polar Components on the Relative Volatility of the Binary System n-Hexane-Benzene. J.Chem.Eng.Data 8 (1963) 210-214 |
Vapor-Liquid Equilibrium Data Set 707
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 351.55 |
0.00400 |
0.00900 |
| 350.85 |
0.02500 |
0.06000 |
| 350.45 |
0.04300 |
0.08300 |
| 349.15 |
0.07500 |
0.15300 |
| 345.95 |
0.21500 |
0.33300 |
| 342.95 |
0.43000 |
0.54500 |
| 340.95 |
0.71300 |
0.75300 |
| 340.85 |
0.76300 |
0.79000 |
| 340.65 |
0.88900 |
0.89300 |
| 340.55 |
0.96500 |
0.96600 |
| 340.45 |
0.99000 |
0.99000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Tongberg C.O.; Johnston F.: Vapor-Liquid Equilibria for n-Hexane-Benzene Mixtures. Ind.Eng.Chem. Ind.Ed. 25 (1933) 733-735 |
Vapor-Liquid Equilibrium Data Set 1570
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 405.15 |
0.90400 |
0.91900 |
| 405.15 |
0.90600 |
0.91100 |
| 405.05 |
0.90600 |
0.91200 |
| 405.05 |
0.92700 |
0.93100 |
| 404.05 |
0.95900 |
0.96600 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Gothard F.; Minea I.; David G.: n-Hexane Separation from Benzene Mixtures. Oil, gas and petrochemistry in the Rumanian People's Republic. Studies and articles (1963) 71-80 |
Diagrams
List of All References
| Source |
| Tongberg C.O.; Johnston F.: Vapor-Liquid Equilibria for n-Hexane-Benzene Mixtures. Ind.Eng.Chem. Ind.Ed. 25 (1933) 733-735 |
| Prabhu P.S.; van Winkle M.: Effect of Polar Components on the Relative Volatility of the Binary System n-Hexane-Benzene. J.Chem.Eng.Data 8 (1963) 210-214 |
| Gothard F.; Minea I.; David G.: n-Hexane Separation from Benzene Mixtures. Oil, gas and petrochemistry in the Rumanian People's Republic. Studies and articles (1963) 71-80 |
Vapor-Liquid Equilibrium Data Overview
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