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 15574

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H6O 46.069 64-17-5 Ethanol
2 C6H6 78.114 71-43-2 Benzene
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]
351.55 1.00000 0.00000 1.00000 0.00000
353.25 0.00000 1.00000 0.00000 1.00000
399.25 0.00000 0.00000 0.00000 0.00000
346.95 0.72500 0.17600 0.68400 0.29100
350.45 0.64200 0.15500 0.71000 0.23900
356.15 0.48300 0.11800 0.72700 0.16200
364.55 0.32200 0.07800 0.69500 0.10100
378.65 0.15700 0.04000 0.52600 0.05000
344.95 0.46600 0.42800 0.52000 0.46600
348.05 0.41300 0.38000 0.55400 0.41000
355.55 0.31200 0.28800 0.57000 0.34000
366.85 0.20300 0.18700 0.53000 0.26000
382.05 0.10400 0.09600 0.34200 0.17400
344.45 0.36000 0.54000 0.47000 0.51900
347.55 0.33700 0.46500 0.48100 0.49200
360.25 0.22000 0.30200 0.50800 0.37200
367.85 0.16900 0.23300 0.47900 0.31400
382.15 0.08500 0.11700 0.31000 0.22200
345.75 0.18000 0.72000 0.40200 0.59000
349.95 0.16000 0.64000 0.39700 0.58200
359.85 0.12000 0.48000 0.34700 0.56000
371.55 0.08000 0.32000 0.26300 0.49900
384.85 0.04000 0.16000 0.15700 0.32400

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

Reference

Source
Anton N.D.; Nguen T.T.; Igoshina V.S.; Tikhonova N.K.; Timofeev V.S.; Serafimov L.A.: Untersuchung der physikalisch-chemischen Eigenschaften in ternären Lösungsmittelsystemen. Tr.Mosk.Inst.Tonkoj Khim.Tekhnol. 3 (1973) 105-109

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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