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 10382

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
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]
336.65 0.64000 0.16000 0.85700 0.12100
342.75 0.48000 0.12000 0.78700 0.15400
351.35 0.31900 0.07900 0.68800 0.19500
365.25 0.15900 0.03600 0.53700 0.22500
339.55 0.48000 0.32000 0.80200 0.16500
345.85 0.33800 0.24800 0.64300 0.27400
352.05 0.23800 0.16200 0.47300 0.41300
365.25 0.11900 0.07500 0.45200 0.30100
342.85 0.31900 0.48200 0.72600 0.22800
348.15 0.23900 0.36100 0.58500 0.30900
354.75 0.15900 0.24100 0.43100 0.41200
364.75 0.07900 0.12300 0.32400 0.45600
347.35 0.16000 0.64000 0.63200 0.28300
365.85 0.03900 0.15500 0.17100 0.55800

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

Reference

Source
Al-Karadagi M.B.; Rudakovskaya T.S.; Timofeev V.S.: Untersuchung der Phasengleichgewicht in wässrigen Lösungsmittel-Systemen. Osnovnoi Organ.Sintez.Neftekhim. 11 (1979) 77-79

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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