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 2051
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 |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 94.766 |
0.30200 |
0.46400 |
0.43300 |
0.38800 |
| 77.034 |
0.03500 |
0.92300 |
0.08700 |
0.86300 |
| 71.781 |
0.01200 |
0.56200 |
0.05500 |
0.66200 |
| 88.633 |
0.16200 |
0.48200 |
0.32600 |
0.42600 |
| 99.032 |
0.73800 |
0.24600 |
0.69400 |
0.25600 |
| 93.619 |
0.16300 |
0.19000 |
0.50300 |
0.18600 |
| 76.260 |
0.03400 |
0.23100 |
0.26000 |
0.39600 |
| 96.325 |
0.79800 |
0.12600 |
0.71300 |
0.16200 |
| 92.779 |
0.30400 |
0.65700 |
0.41200 |
0.56000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Mertl I.: II. Phase Equilibria in the Ternary System Ethyl Acetate-Ethanol-Water. Collect.Czech.Chem.Commun. 37 (1972) 366-374 |
Vapor-Liquid Equilibrium Data Set 2052
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 |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 51.356 |
0.27400 |
0.51200 |
0.44100 |
0.38700 |
| 39.370 |
0.02000 |
0.93900 |
0.07300 |
0.91000 |
| 36.957 |
0.01000 |
0.60500 |
0.03700 |
0.69300 |
| 35.690 |
0.15600 |
0.44600 |
0.39400 |
0.39000 |
| 55.515 |
0.67300 |
0.21000 |
0.65500 |
0.21400 |
| 51.289 |
0.13700 |
0.21300 |
0.50500 |
0.22600 |
| 39.370 |
0.02400 |
0.22300 |
0.25400 |
0.40700 |
| 23.651 |
0.00130 |
0.05700 |
0.01430 |
0.35100 |
| 53.969 |
0.84900 |
0.09100 |
0.76700 |
0.12800 |
| 49.983 |
0.34400 |
0.60300 |
0.46100 |
0.48000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Mertl I.: II. Phase Equilibria in the Ternary System Ethyl Acetate-Ethanol-Water. Collect.Czech.Chem.Commun. 37 (1972) 366-374 |
Vapor-Liquid Equilibrium Data Set 2053
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 |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 25.958 |
0.21100 |
0.50800 |
0.44800 |
0.38100 |
| 21.532 |
0.00320 |
0.61800 |
0.03400 |
0.73100 |
| 24.785 |
0.15200 |
0.46800 |
0.41400 |
0.38000 |
| 29.278 |
0.70000 |
0.19900 |
0.68900 |
0.20100 |
| 26.371 |
0.10300 |
0.20000 |
0.50100 |
0.22900 |
| 18.972 |
0.01900 |
0.20600 |
0.21700 |
0.40000 |
| 28.664 |
0.88000 |
0.07400 |
0.78900 |
0.10100 |
| 26.758 |
0.30700 |
0.61400 |
0.48800 |
0.44900 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Mertl I.: II. Phase Equilibria in the Ternary System Ethyl Acetate-Ethanol-Water. Collect.Czech.Chem.Commun. 37 (1972) 366-374 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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