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 1382
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
x1 [mol/mol] |
y1 [mol/mol] |
0.00000 |
0.00000 |
0.05000 |
0.12200 |
0.10000 |
0.21700 |
0.20000 |
0.37900 |
0.30000 |
0.48600 |
0.40000 |
0.57900 |
0.50000 |
0.65500 |
0.60000 |
0.71800 |
0.70000 |
0.78600 |
0.80000 |
0.85800 |
0.90000 |
0.92900 |
0.95000 |
0.96300 |
1.00000 |
1.00000 |
(x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Lesteva T.M.; Logunova G.I.; Chernaya V.I.: Certain Physicochemical Properties of Hex-1-ene-Solvent Systems. Zh.Fiz.Khim. 53 (1979) 1180-1183 |
Vapor-Liquid Equilibrium Data Set 4281
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
x1 [mol/mol] |
y1 [mol/mol] |
0.00000 |
0.00000 |
0.05000 |
0.11400 |
0.10000 |
0.21100 |
0.20000 |
0.36100 |
0.30000 |
0.47500 |
0.40000 |
0.56700 |
0.50000 |
0.64100 |
0.60000 |
0.70700 |
0.70000 |
0.77600 |
0.80000 |
0.84800 |
0.90000 |
0.92200 |
0.95000 |
0.96000 |
1.00000 |
1.00000 |
(x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Lesteva T.M.; Logunova G.I.; Chernaya V.I.: Certain Physicochemical Properties of Hex-1-ene-Solvent Systems. Zh.Fiz.Khim. 53 (1979) 1180-1183 |
Vapor-Liquid Equilibrium Data Set 4361
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
6.070 |
0.00000 |
7.111 |
0.06900 |
7.861 |
0.14200 |
8.790 |
0.24200 |
9.823 |
0.40300 |
10.570 |
0.52600 |
10.907 |
0.59000 |
11.716 |
0.73900 |
12.206 |
0.83800 |
12.644 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Vera J.H.; Prausnitz J.M.: Vapor-Liquid Equilibria in Binary Aromatic Olefin Systems. J.Chem.Eng.Data 16 (1971) 149-154 |
Diagrams
List of All References
Source |
Vera J.H.; Prausnitz J.M.: Vapor-Liquid Equilibria in Binary Aromatic Olefin Systems. J.Chem.Eng.Data 16 (1971) 149-154 |
Lesteva T.M.; Logunova G.I.; Chernaya V.I.: Certain Physicochemical Properties of Hex-1-ene-Solvent Systems. Zh.Fiz.Khim. 53 (1979) 1180-1183 |
Vapor-Liquid Equilibrium Data Overview
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