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 24291

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 C6H14 86.177 110-54-3 Hexane
3 C3H8O 60.096 67-63-0 2-Propanol
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Constant Value

Pressure 101.30 kPa

Data Table

T [K] x1 [mol/mol] x2 [mol/mol] y1 [mol/mol] y2 [mol/mol]
330.05 0.62674 0.07040 0.73298 0.12494
324.65 0.66753 0.22494 0.72126 0.24948
336.05 0.31670 0.07115 0.52216 0.15364
335.15 0.11337 0.22922 0.24203 0.39604
325.25 0.37452 0.50483 0.56698 0.35913
331.15 0.12589 0.50909 0.27769 0.47790
334.65 0.60816 0.00000 0.80540 0.00000
339.05 0.40822 0.00000 0.67453 0.00000
337.75 0.00000 0.31736 0.00000 0.52170
335.85 0.00000 0.51125 0.00000 0.60040
322.75 0.68998 0.31001 0.74399 0.25601
322.85 0.49728 0.50272 0.68820 0.31180

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

Reference

Source
Kozhenkov A.V.; Sobolev D.M.; Malenko Yu.I.: Liquid-Vapor Equilibrium in the Four-Component Acetone-Hexane-Isopropanol-Toluene System. Zh.Prikl.Khim. 62 (1989) 1319-1322

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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