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

Temperature 313.15 K

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.: Vapour–liquid 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

Vapor-Liquid Equilibrium of 1-Butanol+1-Hexene
See larger image

List of All References

Source
Ghellai S.; Belabbaci A.; Villamanan R.M.; Martin M.C.; Villamanan M.A.; Negadi L.: Vapour–liquid 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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