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 6675
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 3 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
| 340.45 |
0.12500 |
0.12500 |
| 340.05 |
0.12500 |
0.25000 |
| 340.25 |
0.12500 |
0.37500 |
| 341.05 |
0.12500 |
0.50000 |
| 342.65 |
0.12500 |
0.62500 |
| 346.25 |
0.12500 |
0.75000 |
| 341.15 |
0.25000 |
0.12500 |
| 341.35 |
0.25000 |
0.25000 |
| 341.95 |
0.25000 |
0.37500 |
| 343.85 |
0.25000 |
0.50000 |
| 347.75 |
0.25000 |
0.62500 |
| 342.25 |
0.37500 |
0.12500 |
| 342.85 |
0.37500 |
0.25000 |
| 344.65 |
0.37500 |
0.37500 |
| 349.15 |
0.37500 |
0.50000 |
| 343.85 |
0.50000 |
0.12500 |
| 345.45 |
0.50000 |
0.25000 |
| 350.55 |
0.50000 |
0.37500 |
| 345.65 |
0.62500 |
0.12500 |
| 351.15 |
0.62500 |
0.25000 |
| 351.65 |
0.75000 |
0.12500 |
| 357.35 |
0.85000 |
0.07500 |
| 375.75 |
0.95000 |
0.02500 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Gorbunova L.V.; Lutugina N.V.; Malenko Yu.I.: Boiling Point-Composition Relationships in Three Component Systems Formed From Acetic Acid Ethyl Acetate, Methyl Ethyl Ketone and n-Hexane. II.. J.Appl.Chem.USSR 38 (1965) 623-627 |
Vapor-Liquid Equilibrium Data Set 9065
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 |
| 3 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
Search the DDB for all data of this mixture
Constant Value
Data Table
| x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 0.09200 |
0.08100 |
0.55900 |
0.09600 |
| 0.28600 |
0.06200 |
0.70200 |
0.05500 |
| 0.49900 |
0.04400 |
0.75500 |
0.04000 |
| 0.71100 |
0.02500 |
0.81100 |
0.02900 |
| 0.04000 |
0.27500 |
0.24500 |
0.41100 |
| 0.18600 |
0.23400 |
0.57600 |
0.22200 |
| 0.38600 |
0.17800 |
0.69200 |
0.15300 |
| 0.59100 |
0.11800 |
0.75100 |
0.11400 |
| 0.79700 |
0.05900 |
0.82900 |
0.07200 |
| 0.95200 |
0.01300 |
0.93500 |
0.02400 |
| 0.09000 |
0.44700 |
0.36300 |
0.48400 |
| 0.29200 |
0.33100 |
0.58300 |
0.30200 |
| 0.49500 |
0.24500 |
0.68600 |
0.21900 |
| 0.70600 |
0.14000 |
0.76800 |
0.15200 |
| 0.05200 |
0.65500 |
0.17400 |
0.73300 |
| 0.18500 |
0.56400 |
0.42600 |
0.50600 |
| 0.39300 |
0.41900 |
0.58700 |
0.35600 |
| 0.60300 |
0.27500 |
0.68600 |
0.26300 |
| 0.80200 |
0.13600 |
0.79300 |
0.16900 |
| 0.90200 |
0.06800 |
0.87200 |
0.10000 |
| 0.09900 |
0.80900 |
0.24500 |
0.73500 |
| 0.29600 |
0.63100 |
0.46000 |
0.52200 |
| 0.49800 |
0.44900 |
0.59300 |
0.39100 |
| 0.70500 |
0.26400 |
0.70800 |
0.27600 |
(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 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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