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 8903

Components

No. Formula Molar Mass CAS Registry Number Name
1 CH4O 32.042 67-56-1 Methanol
2 H2O 18.015 7732-18-5 Water
3 C6H12O2 116.160 123-86-4 Acetic acid butyl ester
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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]
355.36 0.10000 0.72000 0.36400 0.46800
351.45 0.20000 0.64000 0.50200 0.36000
347.75 0.39700 0.48200 0.62400 0.27100
344.15 0.58800 0.32100 0.71300 0.22000
340.75 0.79900 0.16050 0.88800 0.08300
355.81 0.10000 0.54000 0.38000 0.46200
351.80 0.20000 0.48000 0.47900 0.38900
347.80 0.40500 0.35600 0.61800 0.27500
344.15 0.60000 0.24000 0.76000 0.15300
340.55 0.80000 0.12000 0.87100 0.08200
355.38 0.10000 0.36000 0.34900 0.48400
352.70 0.18700 0.32400 0.46700 0.38500
347.38 0.40800 0.23600 0.63400 0.25100
343.83 0.60000 0.16000 0.80100 0.11800
340.36 0.80100 0.07950 0.89100 0.05100
357.60 0.10000 0.18000 0.34300 0.49500
353.02 0.19700 0.16100 0.47900 0.38800
347.49 0.40000 0.12000 0.67300 0.20400
343.50 0.60250 0.07950 0.82900 0.07500
340.15 0.80300 0.03900 0.89900 0.03600

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

Reference

Source
Beregovykh V.V.; Timofeev V.S.; Lukyanova R.N.; Serafimov L.A.: Die Phasengleichgewicht in den Systemen Methanol-Wasser-n-Butylacetat und Ethanol-Wasser- n-Butylacetat bei Atmosphärendruck. Uch.Zap.Mosk.Inst.Tonkoj Khim.Tekhnol. 1 (1971) 24-30

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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