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 15545

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 CH4O 32.042 67-56-1 Methanol
3 C4H8O2 88.106 141-78-6 Ethyl acetate
4 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] x3 [mol/mol] y1 [mol/mol] y2 [mol/mol] y3 [mol/mol]
339.05 0.10000 0.10100 0.10000 0.30500 0.11900 0.37900
339.65 0.11000 0.11000 0.68000 0.15600 0.19400 0.53800
330.55 0.72600 0.10300 0.09100 0.78700 0.10000 0.06100
337.85 0.17300 0.17300 0.15200 0.37000 0.19000 0.28300
334.65 0.15800 0.57900 0.13900 0.25900 0.52600 0.16600
331.75 0.57900 0.15700 0.13900 0.66700 0.14700 0.10300
336.65 0.21300 0.21300 0.18800 0.38700 0.22500 0.24700
335.95 0.22000 0.22000 0.38600 0.30600 0.24600 0.33000
334.45 0.21400 0.42800 0.18800 0.34400 0.39600 0.18500
332.85 0.42900 0.21300 0.18800 0.53400 0.19700 0.16100
333.15 0.31900 0.31900 0.29000 0.38800 0.32700 0.22500
339.05 0.11600 0.11600 0.30700 0.21300 0.15200 0.44400
338.05 0.11000 0.36100 0.09600 0.27300 0.36300 0.23600
334.95 0.34000 0.11300 0.09900 0.62500 0.09900 0.14800

(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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