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 18774
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 24.645 |
0.00000 |
| 25.537 |
0.03230 |
| 27.367 |
0.10490 |
| 28.382 |
0.14770 |
| 29.546 |
0.19800 |
| 30.657 |
0.24860 |
| 31.727 |
0.29830 |
| 32.799 |
0.34980 |
| 33.785 |
0.39820 |
| 34.798 |
0.44910 |
| 34.786 |
0.44960 |
| 35.784 |
0.49910 |
| 35.758 |
0.49940 |
| 36.758 |
0.54920 |
| 36.725 |
0.54960 |
| 37.708 |
0.59900 |
| 37.688 |
0.60050 |
| 38.634 |
0.65070 |
| 39.555 |
0.70030 |
| 40.458 |
0.74900 |
| 41.385 |
0.79990 |
| 42.285 |
0.84910 |
| 43.210 |
0.90110 |
| 44.240 |
0.95840 |
| 44.992 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Segovia J.J.; Martin M.C.; Chamorro C.R.; Villamanan M.A.: Vapor-Liquid Equilibrium of Ternary Mixtures Containing Methyl tert-Butyl Ether and/or Substitution Hydrocarbons. Methyl tert-Butyl Ether + Heptane + Cyclohexane and Methyl tert-Butyl Ether + Cyclohexane + 1-Hexene at 313.15 K. J.Chem.Eng.Data 43 (1998) 1021-1026 |
Vapor-Liquid Equilibrium Data Set 22865
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 24.654 |
0.00000 |
| 24.655 |
0.00000 |
| 31.861 |
0.30530 |
| 39.798 |
0.71400 |
| 44.978 |
1.00000 |
| 44.950 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Chamorro C.R.; Segovia J.J.; Martin M.C.; Villamanan M.A.: Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor-Liquid Equilibrium of Ternary Mixtures Containing Di-isopropyl Ether of Cyclohexane and 1-Hexene + Benzene at 313.15 K. J.Chem.Eng.Data 47 (2002) 316-321 |
Vapor-Liquid Equilibrium Data Set 22877
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 24.654 |
0.00000 |
| 24.650 |
0.00000 |
| 31.421 |
0.28640 |
| 39.523 |
0.70110 |
| 44.910 |
1.00000 |
| 44.947 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Chamorro C.R.; Segovia J.J.; Martin M.C.; Villamanan M.A.: Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor-Liquid Equilibrium of Binary and Ternary Mixtures Containing Di-isopropyl Ether or Heptane and 1-Hexene + Cyclohexane at 313.15 K. J.Chem.Eng.Data 46 (2001) 1574-1579 |
Diagrams
List of All References
| Source |
| Segovia J.J.; Martin M.C.; Chamorro C.R.; Villamanan M.A.: Vapor-Liquid Equilibrium of Ternary Mixtures Containing Methyl tert-Butyl Ether and/or Substitution Hydrocarbons. Methyl tert-Butyl Ether + Heptane + Cyclohexane and Methyl tert-Butyl Ether + Cyclohexane + 1-Hexene at 313.15 K. J.Chem.Eng.Data 43 (1998) 1021-1026 |
| Chamorro C.R.; Segovia J.J.; Martin M.C.; Villamanan M.A.: Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor-Liquid Equilibrium of Binary and Ternary Mixtures Containing Di-isopropyl Ether or Heptane and 1-Hexene + Cyclohexane at 313.15 K. J.Chem.Eng.Data 46 (2001) 1574-1579 |
| Chamorro C.R.; Segovia J.J.; Martin M.C.; Villamanan M.A.: Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor-Liquid Equilibrium of Ternary Mixtures Containing Di-isopropyl Ether of Cyclohexane and 1-Hexene + Benzene at 313.15 K. J.Chem.Eng.Data 47 (2002) 316-321 |
Vapor-Liquid Equilibrium Data Overview
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