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 6708

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H14 86.177 110-54-3 Hexane
2 C4H8O2 88.106 141-78-6 Ethyl acetate
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Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol]
350.30 0.00000
345.65 0.09000
342.35 0.20200
340.55 0.30200
339.45 0.40400
338.75 0.50000
338.45 0.59300
338.35 0.70200
338.75 0.80300
339.75 0.90000
342.00 1.00000

(T - temperature, x - liquid mole fraction)

Reference

Source
Gorbunova L.V.; Lutugina N.V.; Malenko Yu.I.: Relationship Between Boiling Point and Composition in the Binary Systems Formed by Acetic Acid Ethyl Acetate Methyl Ethyl Ketone and n-Hexane.I.. J.Appl.Chem.USSR 38 (1965) 368-370


Vapor-Liquid Equilibrium Data Set 9062

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H14 86.177 110-54-3 Hexane
2 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

x1 [mol/mol] y1 [mol/mol]
0.04000 0.09400
0.09100 0.19100
0.17400 0.31400
0.26600 0.40300
0.36100 0.47900
0.45800 0.53400
0.55700 0.59900
0.64300 0.64900
0.69200 0.67900
0.79800 0.75200
0.90000 0.84900
0.95200 0.92200

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

Reference

Source
Lutugina N.V.; Pukinskii I.B.; Kaliev S.G.: Dampf-Flüssig-Gleichgewicht in binären und ternären Systemen aus Essigsäure, Methylethylketon, Ethylacetat und n-Hexan. Vestn.Leningr.Univ.Fiz.Khim. (1972) 102-105


Vapor-Liquid Equilibrium Data Set 22908

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H14 86.177 110-54-3 Hexane
2 C4H8O2 88.106 141-78-6 Ethyl acetate
Search the DDB for all data of this mixture

Constant Value

Temperature 353.15 K

Data Table

x1 [mol/mol] y1 [mol/mol]
0.01890 0.06420
0.03920 0.11830
0.05830 0.15610
0.11960 0.29730
0.16530 0.34170
0.22750 0.41740
0.28560 0.45800
0.34620 0.51710
0.39690 0.52080
0.46730 0.55700
0.52870 0.58640
0.58870 0.61710
0.65180 0.63700
0.70860 0.66910
0.77040 0.71080
0.88120 0.79330
0.91470 0.83230
0.94100 0.87840
0.96130 0.91370
0.97840 0.94880

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

Reference

Source
Park S.-J.; Han K.-J.; Choi M.-J.; Gmehling J.: Isothermal vapor-liquid equilibria and excess molar volumes for the ternary mixtures containing 2-methyl pyrazine. Fluid Phase Equilib. 193 (2002) 109-121

Diagrams

Vapor-Liquid Equilibrium of Ethyl acetate+Hexane
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Vapor-Liquid Equilibrium of Ethyl acetate+Hexane
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Vapor-Liquid Equilibrium of Ethyl acetate+Hexane
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List of All References

Source
Lutugina N.V.; Pukinskii I.B.; Kaliev S.G.: Dampf-Flüssig-Gleichgewicht in binären und ternären Systemen aus Essigsäure, Methylethylketon, Ethylacetat und n-Hexan. Vestn.Leningr.Univ.Fiz.Khim. (1972) 102-105
Gorbunova L.V.; Lutugina N.V.; Malenko Yu.I.: Relationship Between Boiling Point and Composition in the Binary Systems Formed by Acetic Acid Ethyl Acetate Methyl Ethyl Ketone and n-Hexane.I.. J.Appl.Chem.USSR 38 (1965) 368-370
Park S.-J.; Han K.-J.; Choi M.-J.; Gmehling J.: Isothermal vapor-liquid equilibria and excess molar volumes for the ternary mixtures containing 2-methyl pyrazine. Fluid Phase Equilib. 193 (2002) 109-121

Vapor-Liquid Equilibrium Data Overview


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