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 28634
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
| 2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 1.380 |
0.00000 |
| 1.4945 |
0.00810 |
| 2.0985 |
0.04940 |
| 3.5104 |
0.13080 |
| 5.412 |
0.21880 |
| 7.793 |
0.30840 |
| 10.666 |
0.39750 |
| 13.818 |
0.47970 |
| 16.935 |
0.55090 |
| 23.302 |
0.68120 |
| 27.646 |
0.77280 |
| 32.147 |
0.86340 |
| 36.666 |
0.94840 |
| 39.095 |
0.99130 |
| 39.661 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Schmid B.; Döker M.; Gmehling J.: Measurement of the thermodynamic properties for the reactive system ethylene glycol-acetic acid. Fluid Phase Equilib. 258 (2007) 115-124 |
Diagrams
List of All References
| Source |
| Schmid B.; Döker M.; Gmehling J.: Measurement of the thermodynamic properties for the reactive system ethylene glycol-acetic acid. Fluid Phase Equilib. 258 (2007) 115-124 |
Vapor-Liquid Equilibrium Data Overview
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