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 3584
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 388.95 |
0.00000 |
0.00000 |
| 385.95 |
0.05500 |
0.10700 |
| 385.05 |
0.07300 |
0.14400 |
| 383.15 |
0.10300 |
0.19700 |
| 380.85 |
0.13300 |
0.27400 |
| 380.35 |
0.16600 |
0.31200 |
| 377.85 |
0.20700 |
0.39300 |
| 376.65 |
0.23300 |
0.43700 |
| 373.05 |
0.28200 |
0.52600 |
| 371.95 |
0.34700 |
0.59700 |
| 366.15 |
0.46000 |
0.75000 |
| 364.25 |
0.51600 |
0.79300 |
| 362.05 |
0.58700 |
0.85400 |
| 359.65 |
0.65900 |
0.90000 |
| 356.95 |
0.72800 |
0.93400 |
| 354.45 |
0.81600 |
0.96600 |
| 351.45 |
0.92400 |
0.99000 |
| 349.95 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Rius A.; Otero J.L.; Macarron A.: systèmes méthanol—acide acétique; éthanol—acide acétique; n-propanol—acide acétique; n-butanol—acide acétique. Chem.Eng.Sci. 10 (1959) 105-111 |
Vapor-Liquid Equilibrium Data Set 7651
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 3.5864 |
0.00000 |
| 3.866 |
0.06000 |
| 3.933 |
0.06800 |
| 4.000 |
0.08600 |
| 4.266 |
0.13100 |
| 4.746 |
0.19900 |
| 5.540 |
0.29600 |
| 6.413 |
0.40700 |
| 6.933 |
0.46000 |
| 7.239 |
0.50300 |
| 7.566 |
0.55000 |
| 8.559 |
0.59400 |
| 9.766 |
0.69400 |
| 10.630 |
0.76200 |
| 13.800 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Wagner M.; Apelblat A.; Tamir A.: Excess Gibbs Free Energy in Methanol + Acetic Acid and Ethanol + Acetic Acid. J.Chem.Thermodyn. 12 (1980) 181-186 |
Vapor-Liquid Equilibrium Data Set 7652
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 5.813 |
0.00000 |
| 6.366 |
0.06000 |
| 6.333 |
0.06800 |
| 6.599 |
0.08600 |
| 7.053 |
0.13100 |
| 7.886 |
0.19900 |
| 9.095 |
0.29600 |
| 10.590 |
0.40700 |
| 11.520 |
0.46000 |
| 12.330 |
0.50300 |
| 13.300 |
0.55000 |
| 14.280 |
0.59400 |
| 16.311 |
0.69400 |
| 17.651 |
0.76200 |
| 23.130 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Wagner M.; Apelblat A.; Tamir A.: Excess Gibbs Free Energy in Methanol + Acetic Acid and Ethanol + Acetic Acid. J.Chem.Thermodyn. 12 (1980) 181-186 |
Diagrams
List of All References
| Source |
| Rius A.; Otero J.L.; Macarron A.: systèmes méthanol—acide acétique; éthanol—acide acétique; n-propanol—acide acétique; n-butanol—acide acétique. Chem.Eng.Sci. 10 (1959) 105-111 |
| Wagner M.; Apelblat A.; Tamir A.: Excess Gibbs Free Energy in Methanol + Acetic Acid and Ethanol + Acetic Acid. J.Chem.Thermodyn. 12 (1980) 181-186 |
Vapor-Liquid Equilibrium Data Overview
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