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
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
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
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
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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