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 15544

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
Search the DDB for all data of this mixture

Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] x2 [mol/mol] y1 [mol/mol] y2 [mol/mol]
338.45 0.17000 0.15000 0.25000 0.28000
335.95 0.13000 0.35000 0.17000 0.47700
334.95 0.08000 0.60000 0.11200 0.62400
335.45 0.04000 0.80000 0.06500 0.75500
335.75 0.34000 0.15100 0.43100 0.25100
333.95 0.26000 0.35000 0.32600 0.42300
333.85 0.16000 0.60000 0.21600 0.58100
335.15 0.08000 0.80000 0.12000 0.74200
332.85 0.51000 0.15000 0.60000 0.20500
332.35 0.39000 0.35100 0.45000 0.38000
333.15 0.24000 0.60000 0.31800 0.55000
334.15 0.11800 0.80100 0.20000 0.71500
330.65 0.67900 0.15100 0.71500 0.18200
330.45 0.51200 0.35000 0.58000 0.34000
332.15 0.31900 0.60100 0.42000 0.50700
333.55 0.15900 0.80100 0.25400 0.70000

(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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