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 5227
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
1.1306 |
0.00000 |
3.609 |
0.14980 |
5.565 |
0.29360 |
6.591 |
0.37790 |
6.861 |
0.40000 |
7.365 |
0.44590 |
7.813 |
0.48610 |
8.067 |
0.51040 |
8.786 |
0.57660 |
9.071 |
0.60920 |
9.773 |
0.67290 |
10.286 |
0.73610 |
11.308 |
0.83220 |
12.122 |
0.91400 |
13.047 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Young K.L.; Mentzer R.A.; Greenkorn R.A.; Chao K.C.: Vapor-Liquid Equilibrium in Mixtures of Cyclohexane + Benzene, + Octene-1, +M-Xylene, and + n-Heptane. J.Chem.Thermodyn. 9 (1977) 979-985 |
Vapor-Liquid Equilibrium Data Set 5544
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
1.5172 |
0.00000 |
5.824 |
0.22580 |
8.059 |
0.37120 |
9.599 |
0.47970 |
10.974 |
0.57510 |
11.839 |
0.64550 |
12.500 |
0.69540 |
13.036 |
0.73500 |
13.756 |
0.79630 |
14.197 |
0.83440 |
14.659 |
0.86180 |
16.135 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Jain D.V.S.; Yadav O.P.: Vapor Pressures and Excess Gibbs Energies of Cyclohexane + o-Xylene + m-Xylene and + p-Xylene. J.Chem.Thermodyn. 5 (1973) 541-544 |
Vapor-Liquid Equilibrium Data Set 5545
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
4.234 |
0.00000 |
13.264 |
0.22340 |
18.260 |
0.36850 |
21.801 |
0.47740 |
24.613 |
0.57330 |
26.632 |
0.64410 |
28.004 |
0.69430 |
29.168 |
0.73410 |
30.837 |
0.79540 |
31.908 |
0.83400 |
32.671 |
0.86150 |
36.677 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Jain D.V.S.; Yadav O.P.: Vapor Pressures and Excess Gibbs Energies of Cyclohexane + o-Xylene + m-Xylene and + p-Xylene. J.Chem.Thermodyn. 5 (1973) 541-544 |
Diagrams
List of All References
Source |
Young K.L.; Mentzer R.A.; Greenkorn R.A.; Chao K.C.: Vapor-Liquid Equilibrium in Mixtures of Cyclohexane + Benzene, + Octene-1, +M-Xylene, and + n-Heptane. J.Chem.Thermodyn. 9 (1977) 979-985 |
Jain D.V.S.; Yadav O.P.: Vapor Pressures and Excess Gibbs Energies of Cyclohexane + o-Xylene + m-Xylene and + p-Xylene. J.Chem.Thermodyn. 5 (1973) 541-544 |
Vapor-Liquid Equilibrium Data Overview
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