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 15543

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 C4H8O2 88.106 141-78-6 Ethyl acetate
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] y1 [mol/mol] y2 [mol/mol]
341.15 0.05100 0.17800 0.13500 0.59000
338.05 0.15200 0.15900 0.36500 0.41500
333.15 0.40500 0.11100 0.59500 0.15300
330.35 0.70300 0.05600 0.85000 0.04500
341.95 0.05200 0.36100 0.13000 0.59500
339.15 0.15500 0.32100 0.32300 0.45000
333.75 0.40800 0.22500 0.61100 0.22000
330.95 0.70700 0.11100 0.81000 0.12100
342.15 0.05200 0.55000 0.11800 0.61000
339.65 0.15000 0.51000 0.27500 0.49000
335.15 0.40000 0.36000 0.55000 0.27400
331.55 0.70000 0.18000 0.78500 0.11000
342.45 0.05200 0.74800 0.10000 0.63000
339.85 0.15000 0.68000 0.25000 0.53000
335.55 0.40000 0.48000 0.52600 0.32500
332.25 0.70100 0.24000 0.77800 0.13800

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

Reference

Source
Timofeev V.S.; Ponomarev V.N.; Baikalova N.M.; Rudakovskaya T.S.: Entwicklung eines technologischen Trennprozesses von Aceton-Methanol-Ethylacetat-Wasser-Mischungen. Fiziko-chimiceskie osnovy rektifikacii (1977) 180-193

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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