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 671
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 |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
353.85 |
0.00000 |
0.00000 |
352.65 |
0.10100 |
0.13100 |
352.05 |
0.17100 |
0.21100 |
351.55 |
0.25600 |
0.29300 |
350.95 |
0.34300 |
0.37600 |
350.65 |
0.42800 |
0.44500 |
350.55 |
0.52500 |
0.52900 |
350.55 |
0.57100 |
0.56400 |
350.75 |
0.66500 |
0.64500 |
351.05 |
0.75900 |
0.72800 |
351.35 |
0.81000 |
0.77700 |
351.75 |
0.86300 |
0.83400 |
352.45 |
0.94500 |
0.92600 |
353.25 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Nagata I.: Vapor-Liquid Equilibria for the Ternary System Methyl Acetate-Benzene-Cyclohexane. J.Chem.Eng.Data 7 (1962) 461-466 |
Vapor-Liquid Equilibrium Data Set 672
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 |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
353.35 |
0.04500 |
0.05900 |
353.15 |
0.06600 |
0.08400 |
352.65 |
0.10500 |
0.12900 |
352.45 |
0.11800 |
0.14500 |
351.35 |
0.25400 |
0.29000 |
350.65 |
0.38300 |
0.40700 |
350.55 |
0.44900 |
0.46100 |
350.55 |
0.50200 |
0.50200 |
350.55 |
0.55400 |
0.54500 |
350.65 |
0.59700 |
0.58000 |
350.75 |
0.62800 |
0.60500 |
350.75 |
0.64500 |
0.62100 |
350.85 |
0.72000 |
0.68200 |
350.95 |
0.73800 |
0.69800 |
351.15 |
0.75300 |
0.71700 |
351.35 |
0.79800 |
0.75800 |
351.45 |
0.83500 |
0.79800 |
351.85 |
0.87900 |
0.84700 |
352.05 |
0.89300 |
0.86500 |
352.15 |
0.91400 |
0.88900 |
352.35 |
0.92800 |
0.90700 |
352.45 |
0.93700 |
0.91800 |
352.65 |
0.96000 |
0.94800 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Richards A.R.; Hargreaves E.: Vapor-Liquid Equilibria of Close-Boiling Binary Hydrocarbon Mixtures. Ind.Eng.Chem. 36 (1944) 805-808 |
Vapor-Liquid Equilibrium Data Set 673
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 |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
25.990 |
0.12820 |
0.16570 |
26.751 |
0.23540 |
0.27660 |
27.298 |
0.36850 |
0.39120 |
27.480 |
0.49320 |
0.49500 |
27.355 |
0.61430 |
0.59090 |
26.895 |
0.74280 |
0.69790 |
26.003 |
0.86560 |
0.82050 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Scatchard G.; Wood S.E.; Mochel J.M.: III. Benzene-Cyclohexane Mixtures. J.Phys.Chem. 43 (1939) 119-130 |
Diagrams
List of All References
Source |
Richards A.R.; Hargreaves E.: Vapor-Liquid Equilibria of Close-Boiling Binary Hydrocarbon Mixtures. Ind.Eng.Chem. 36 (1944) 805-808 |
Nagata I.: Vapor-Liquid Equilibria for the Ternary System Methyl Acetate-Benzene-Cyclohexane. J.Chem.Eng.Data 7 (1962) 461-466 |
Scatchard G.; Wood S.E.; Mochel J.M.: III. Benzene-Cyclohexane Mixtures. J.Phys.Chem. 43 (1939) 119-130 |
Vapor-Liquid Equilibrium Data Overview
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