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 6698

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H12 84.161 592-41-6 1-Hexene
2 C6H14 86.177 110-54-3 Hexane
3 C2H6O 46.069 64-17-5 Ethanol
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Constant Value

Temperature 328.15 K

Data Table

x1 [mol/mol] x2 [mol/mol] y1 [mol/mol] y2 [mol/mol]
0.10000 0.10000 0.31500 0.31300
0.20000 0.20000 0.34400 0.32200
0.40000 0.10000 0.57500 0.12700
0.30000 0.20000 0.41700 0.26000
0.10000 0.40000 0.14800 0.52900
0.30000 0.30000 0.37100 0.33500
0.60000 0.10000 0.60700 0.09600
0.50000 0.20000 0.51200 0.18900
0.30000 0.40000 0.30300 0.39800
0.20000 0.50000 0.21000 0.47100
0.70000 0.10000 0.64400 0.08300
0.40000 0.40000 0.35300 0.34900
0.70000 0.20000 0.60600 0.16100
0.50000 0.40000 0.43900 0.30100
0.40000 0.50000 0.36200 0.38000
0.20000 0.70000 0.18500 0.54200

(x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Kudryavtseva L.S.; Viit Kh.Kh.; Eizen O.G.: Liquid-Vapour Equilibria in the Ethanol-Heptane-Isooctane and Hex-1-ene-Hexane-Ethanol Ternary Systems. Viniti (1971) 1-11

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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