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 34423
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
44.986 |
1.00000 |
44.518 |
0.94980 |
44.066 |
0.89940 |
43.700 |
0.85030 |
43.169 |
0.79940 |
42.603 |
0.74870 |
41.978 |
0.70110 |
41.315 |
0.64950 |
40.508 |
0.59900 |
40.570 |
0.59860 |
39.741 |
0.54880 |
39.688 |
0.54860 |
38.836 |
0.49850 |
38.740 |
0.49830 |
37.694 |
0.44850 |
37.674 |
0.44820 |
36.298 |
0.39870 |
36.239 |
0.39760 |
34.533 |
0.34780 |
32.413 |
0.29760 |
29.672 |
0.24610 |
26.443 |
0.19800 |
22.811 |
0.15410 |
17.341 |
0.10080 |
9.351 |
0.04150 |
2.482 |
0.00000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Ghellai S.; Belabbaci A.; Villamanan R.M.; Martin M.C.; Villamanan M.A.; Negadi L.: Vapourliquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K. J.Chem.Thermodyn. 63 (2013) 164-168 |
Diagrams
List of All References
Source |
Ghellai S.; Belabbaci A.; Villamanan R.M.; Martin M.C.; Villamanan M.A.; Negadi L.: Vapourliquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K. J.Chem.Thermodyn. 63 (2013) 164-168 |
Vapor-Liquid Equilibrium Data Overview
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