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 5640
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C16H34 |
226.446 |
544-76-3 |
Hexadecane |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 0.4346 |
0.03012 |
| 1.5212 |
0.10346 |
| 2.3745 |
0.16018 |
| 4.192 |
0.27733 |
| 6.270 |
0.40729 |
| 8.218 |
0.52569 |
| 8.223 |
0.52638 |
| 11.130 |
0.70020 |
| 13.315 |
0.82973 |
| 16.145 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| McGlashan M.L.; Williamson A.G.: Thermodynamics of Mixtures of n-Hexane + n-Hexadecane. Trans.Faraday Soc. 57 (1961) 588-600 |
Vapor-Liquid Equilibrium Data Set 5641
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C16H34 |
226.446 |
544-76-3 |
Hexadecane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 0.6573 |
0.02980 |
| 2.3025 |
0.10247 |
| 3.604 |
0.15871 |
| 6.377 |
0.27588 |
| 9.586 |
0.40576 |
| 12.496 |
0.52050 |
| 12.615 |
0.52500 |
| 17.089 |
0.69714 |
| 20.532 |
0.82852 |
| 24.947 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| McGlashan M.L.; Williamson A.G.: Thermodynamics of Mixtures of n-Hexane + n-Hexadecane. Trans.Faraday Soc. 57 (1961) 588-600 |
Vapor-Liquid Equilibrium Data Set 5642
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C16H34 |
226.446 |
544-76-3 |
Hexadecane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 0.9613 |
0.02939 |
| 3.3624 |
0.10116 |
| 5.272 |
0.15670 |
| 9.373 |
0.27324 |
| 14.146 |
0.40341 |
| 18.285 |
0.51264 |
| 18.693 |
0.52314 |
| 25.281 |
0.69254 |
| 30.560 |
0.82682 |
| 37.260 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| McGlashan M.L.; Williamson A.G.: Thermodynamics of Mixtures of n-Hexane + n-Hexadecane. Trans.Faraday Soc. 57 (1961) 588-600 |
Diagrams
List of All References
| Source |
| McGlashan M.L.; Williamson A.G.: Thermodynamics of Mixtures of n-Hexane + n-Hexadecane. Trans.Faraday Soc. 57 (1961) 588-600 |
Vapor-Liquid Equilibrium Data Overview
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