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 22432

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 C4H10O 74.123 71-36-3 1-Butanol
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]
373.45 0.20090 0.64870
364.02 0.41000 0.48420
361.58 0.60040 0.32510
355.25 0.80360 0.16100
375.98 0.20450 0.48050
366.40 0.40870 0.36100
360.20 0.59760 0.24000
356.04 0.80050 0.12000
378.54 0.20100 0.32260
368.82 0.40150 0.24080
361.89 0.60750 0.16080
356.89 0.80200 0.08000
381.56 0.20800 0.16060
371.53 0.40650 0.12100
363.79 0.60930 0.08000
357.87 0.80100 0.04040

(T - temperature, x - liquid mole fraction)

Reference

Source
Beldeeva L.N.; Pilyuckenko S.L.; Iordan V.F.; Garber Y.N.: Separation of C1-C4 Alcohol from Their Alkyl Acetates by Extractive Rectification with Reference to A Butanol-Butyl Acetate Mixture. J.Appl.Chem.USSR 64 (1991) 2497-2500

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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