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 2597
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 3 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 60.462 |
0.08400 |
0.45800 |
0.09300 |
0.50800 |
| 56.742 |
0.11400 |
0.26600 |
0.15100 |
0.44000 |
| 60.062 |
0.11400 |
0.62000 |
0.10400 |
0.51100 |
| 53.729 |
0.13450 |
0.13450 |
0.22600 |
0.32200 |
| 56.262 |
0.13450 |
0.73100 |
0.11900 |
0.52800 |
| 60.128 |
0.17600 |
0.41200 |
0.18600 |
0.44300 |
| 56.702 |
0.23100 |
0.23100 |
0.26300 |
0.36200 |
| 57.862 |
0.23100 |
0.53800 |
0.19500 |
0.45000 |
| 54.396 |
0.26600 |
0.11400 |
0.36300 |
0.22400 |
| 55.662 |
0.26600 |
0.62000 |
0.22000 |
0.47400 |
| 57.262 |
0.33300 |
0.33300 |
0.29500 |
0.35400 |
| 55.595 |
0.41200 |
0.17600 |
0.40200 |
0.22900 |
| 56.129 |
0.41200 |
0.41200 |
0.31900 |
0.36200 |
| 53.929 |
0.45800 |
0.08400 |
0.48800 |
0.12900 |
| 53.262 |
0.45800 |
0.45800 |
0.35900 |
0.38400 |
| 55.809 |
0.53800 |
0.23100 |
0.42600 |
0.24100 |
| 53.729 |
0.62000 |
0.11400 |
0.52000 |
0.13400 |
| 53.729 |
0.62000 |
0.26600 |
0.46400 |
0.25500 |
| 52.996 |
0.73100 |
0.13450 |
0.55600 |
0.14200 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Morachevskii A.G.; Zharov V.T.: Liquid-Vapor Equilibrium in the Ternary System Benzene-Cyclohexane Ethyl Alcohol. J.Appl.Chem.USSR 36 (1963) 2689-2691 |
Vapor-Liquid Equilibrium Data Set 2643
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 3 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 314.27 |
0.08400 |
0.45800 |
0.10000 |
0.52900 |
| 314.74 |
0.11400 |
0.26600 |
0.15400 |
0.44000 |
| 314.29 |
0.11400 |
0.62000 |
0.11200 |
0.53400 |
| 316.17 |
0.13450 |
0.13450 |
0.23700 |
0.34200 |
| 314.74 |
0.13450 |
0.73100 |
0.12300 |
0.54800 |
| 314.14 |
0.17600 |
0.41200 |
0.18600 |
0.46400 |
| 314.65 |
0.23100 |
0.23100 |
0.27100 |
0.37200 |
| 314.37 |
0.23100 |
0.53800 |
0.20200 |
0.46600 |
| 315.76 |
0.26600 |
0.11400 |
0.37200 |
0.23300 |
| 314.93 |
0.26600 |
0.62000 |
0.24400 |
0.52800 |
| 314.36 |
0.33300 |
0.33300 |
0.30600 |
0.36700 |
| 315.20 |
0.41200 |
0.17600 |
0.41700 |
0.24200 |
| 314.73 |
0.41200 |
0.41200 |
0.32900 |
0.36900 |
| 316.06 |
0.45800 |
0.08400 |
0.50400 |
0.13500 |
| 315.84 |
0.45800 |
0.45800 |
0.35900 |
0.38600 |
| 315.05 |
0.53800 |
0.23100 |
0.43600 |
0.24900 |
| 316.03 |
0.62000 |
0.11400 |
0.53500 |
0.14100 |
| 315.92 |
0.62000 |
0.26600 |
0.46600 |
0.26100 |
| 315.51 |
0.73100 |
0.13450 |
0.56100 |
0.14900 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Morachevskii A.G.; Zharov V.T.: Liquid-Vapor Equilibrium in the Ternary System Benzene-Cyclohexane Ethyl Alcohol. J.Appl.Chem.USSR 36 (1963) 2689-2691 |
Vapor-Liquid Equilibrium Data Set 2647
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 3 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 337.88 |
0.08400 |
0.45800 |
0.08700 |
0.47300 |
| 338.42 |
0.11400 |
0.26600 |
0.13600 |
0.39700 |
| 338.21 |
0.11400 |
0.62000 |
0.10000 |
0.48300 |
| 339.86 |
0.13450 |
0.13450 |
0.20500 |
0.29200 |
| 339.41 |
0.13450 |
0.73100 |
0.11100 |
0.51300 |
| 337.97 |
0.17600 |
0.41200 |
0.16200 |
0.42700 |
| 338.55 |
0.23100 |
0.23100 |
0.24300 |
0.33400 |
| 338.50 |
0.23100 |
0.53800 |
0.18400 |
0.42600 |
| 339.71 |
0.26600 |
0.11400 |
0.33400 |
0.20000 |
| 339.99 |
0.26600 |
0.62000 |
0.20600 |
0.46000 |
| 338.38 |
0.33300 |
0.33300 |
0.27500 |
0.33000 |
| 339.12 |
0.41200 |
0.17600 |
0.37500 |
0.20000 |
| 339.42 |
0.41200 |
0.41200 |
0.30800 |
0.34500 |
| 340.00 |
0.45800 |
0.08400 |
0.45300 |
0.11500 |
| 342.26 |
0.45800 |
0.45800 |
0.35900 |
0.38000 |
| 339.53 |
0.53800 |
0.23100 |
0.41100 |
0.22200 |
| 340.22 |
0.62000 |
0.11400 |
0.49300 |
0.12200 |
| 341.47 |
0.62000 |
0.26600 |
0.45900 |
0.23700 |
| 341.87 |
0.73100 |
0.13450 |
0.54600 |
0.13500 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Morachevskii A.G.; Zharov V.T.: Liquid-Vapor Equilibrium in the Ternary System Benzene-Cyclohexane Ethyl Alcohol. J.Appl.Chem.USSR 36 (1963) 2689-2691 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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