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 4802

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 C4H10O 74.123 71-36-3 1-Butanol
3 H2O 18.015 7732-18-5 Water
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Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] x2 [mol/mol]
333.43 0.66600 0.06500
334.77 0.49200 0.05500
335.96 0.36500 0.04700
337.57 0.26800 0.04200
340.00 0.19200 0.03700
343.03 0.13000 0.03400
347.57 0.07900 0.03100
353.04 0.03600 0.02900
335.59 0.59400 0.13300
337.37 0.42800 0.11200
339.11 0.30800 0.09700
341.92 0.21600 0.08500
345.25 0.14500 0.07600
349.71 0.08700 0.06800
357.20 0.04000 0.06200
338.38 0.51800 0.20300
340.15 0.36300 0.17000
343.05 0.25000 0.14700
346.48 0.16400 0.12900
351.26 0.09800 0.11500
357.43 0.04400 0.10400
341.31 0.43800 0.27800
344.15 0.29400 0.23100
348.79 0.18900 0.19800
352.04 0.11000 0.17400
358.01 0.04900 0.15700
344.86 0.35900 0.35200
348.50 0.22200 0.29300
353.05 0.12800 0.25200
358.12 0.05600 0.22000
348.55 0.27500 0.43000
353.46 0.15200 0.35800
358.40 0.06700 0.30500
353.87 0.18700 0.51200
359.45 0.07700 0.42500
361.06 0.09500 0.59800

(T - temperature, x - liquid mole fraction)

Reference

Source
Ernst R.C.; Litkenhous E.E.; Spanyer J.W.: The Physical Properties of the Ternary System Acetone-n-Butyl Alcohol-Water. J.Phys.Chem. 36 (1932) 842-854

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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