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 179
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 349.25 |
0.07900 |
0.15500 |
| 347.75 |
0.16400 |
0.26700 |
| 346.45 |
0.26400 |
0.37200 |
| 345.45 |
0.37200 |
0.43800 |
| 345.15 |
0.44200 |
0.48300 |
| 345.05 |
0.47300 |
0.49900 |
| 345.55 |
0.69100 |
0.64000 |
| 345.85 |
0.72800 |
0.66800 |
| 347.05 |
0.84500 |
0.77200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Griswold J.; Chu P.L.; Winsauer W.O.: (Separation of Synthesis Mixtures) Phase Equilibria in Ethyl Alcohol-Ethyl Acetate-Water System. Ind.Eng.Chem. 41 (1949) 2352-2358 |
Vapor-Liquid Equilibrium Data Set 513
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 19.465 |
0.02240 |
0.08080 |
| 20.198 |
0.03640 |
0.11320 |
| 21.065 |
0.06880 |
0.18360 |
| 21.998 |
0.09910 |
0.24560 |
| 23.465 |
0.13620 |
0.30790 |
| 24.531 |
0.17400 |
0.35580 |
| 25.531 |
0.22850 |
0.41700 |
| 25.531 |
0.24240 |
0.42400 |
| 26.731 |
0.28340 |
0.46850 |
| 27.264 |
0.36410 |
0.50900 |
| 28.131 |
0.45900 |
0.56830 |
| 28.798 |
0.56110 |
0.59780 |
| 28.731 |
0.64460 |
0.66930 |
| 28.798 |
0.65590 |
0.65860 |
| 28.798 |
0.76840 |
0.73860 |
| 28.464 |
0.77440 |
0.72550 |
| 28.264 |
0.87150 |
0.81260 |
| 27.464 |
0.92430 |
0.87740 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Murti P.S.; van Winkle M.: Vapor-Liquid Equilibria for Binary Systems of Methanol, Ethyl Alcohol, 1-Propanol, and 2-Propanol with Ethyl Acetate and 1-Propanol-Water. Ind.Eng.Chem. Chem.Eng.Data Series 3 (1958) 72-81 |
Vapor-Liquid Equilibrium Data Set 514
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 49.996 |
0.04350 |
0.11510 |
| 48.196 |
0.02400 |
0.06070 |
| 51.862 |
0.07530 |
0.15090 |
| 54.795 |
0.10600 |
0.22700 |
| 56.195 |
0.14410 |
0.27400 |
| 59.262 |
0.19360 |
0.32000 |
| 60.528 |
0.24590 |
0.37150 |
| 62.128 |
0.31300 |
0.41200 |
| 63.061 |
0.38000 |
0.47060 |
| 63.195 |
0.41400 |
0.51350 |
| 63.928 |
0.47710 |
0.53750 |
| 64.128 |
0.49890 |
0.54220 |
| 64.661 |
0.55630 |
0.57560 |
| 64.595 |
0.67210 |
0.67430 |
| 63.795 |
0.77140 |
0.71110 |
| 63.728 |
0.77140 |
0.71990 |
| 61.862 |
0.86810 |
0.79770 |
| 59.262 |
0.94050 |
0.89000 |
| 59.195 |
0.94950 |
0.88930 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Murti P.S.; van Winkle M.: Vapor-Liquid Equilibria for Binary Systems of Methanol, Ethyl Alcohol, 1-Propanol, and 2-Propanol with Ethyl Acetate and 1-Propanol-Water. Ind.Eng.Chem. Chem.Eng.Data Series 3 (1958) 72-81 |
Diagrams
List of All References
| Source |
| Murti P.S.; van Winkle M.: Vapor-Liquid Equilibria for Binary Systems of Methanol, Ethyl Alcohol, 1-Propanol, and 2-Propanol with Ethyl Acetate and 1-Propanol-Water. Ind.Eng.Chem. Chem.Eng.Data Series 3 (1958) 72-81 |
| Griswold J.; Chu P.L.; Winsauer W.O.: (Separation of Synthesis Mixtures) Phase Equilibria in Ethyl Alcohol-Ethyl Acetate-Water System. Ind.Eng.Chem. 41 (1949) 2352-2358 |
Vapor-Liquid Equilibrium Data Overview
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