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 11133
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 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] |
| 24.659 |
0.68540 |
0.29360 |
| 24.933 |
0.66500 |
0.28480 |
| 25.394 |
0.63050 |
0.27000 |
| 25.813 |
0.59480 |
0.25470 |
| 26.198 |
0.55970 |
0.23970 |
| 26.548 |
0.52430 |
0.22450 |
| 26.852 |
0.48950 |
0.20960 |
| 27.099 |
0.45440 |
0.19450 |
| 27.298 |
0.41940 |
0.17960 |
| 27.426 |
0.38420 |
0.16450 |
| 27.500 |
0.34830 |
0.14910 |
| 30.130 |
0.29550 |
0.68440 |
| 30.700 |
0.28630 |
0.66300 |
| 31.540 |
0.27110 |
0.62770 |
| 32.247 |
0.25580 |
0.59230 |
| 32.844 |
0.24100 |
0.55800 |
| 33.359 |
0.22570 |
0.52270 |
| 33.797 |
0.21060 |
0.48760 |
| 34.163 |
0.19550 |
0.45270 |
| 34.476 |
0.18040 |
0.41770 |
| 34.704 |
0.16530 |
0.38270 |
| 34.837 |
0.15020 |
0.34770 |
| 36.409 |
0.02030 |
0.29180 |
| 35.932 |
0.05000 |
0.28300 |
| 35.040 |
0.10020 |
0.26800 |
| 34.095 |
0.15010 |
0.25310 |
| 33.028 |
0.20040 |
0.23820 |
| 31.853 |
0.25040 |
0.22330 |
| 30.576 |
0.30020 |
0.20840 |
| 29.158 |
0.35030 |
0.19350 |
| 27.622 |
0.40040 |
0.17860 |
| 25.959 |
0.45030 |
0.16380 |
| 24.173 |
0.50030 |
0.14890 |
| 7.239 |
0.68560 |
0.01980 |
| 12.099 |
0.66470 |
0.04970 |
| 18.076 |
0.63000 |
0.09930 |
| 22.213 |
0.59540 |
0.14880 |
| 25.079 |
0.56030 |
0.19910 |
| 27.043 |
0.52540 |
0.24880 |
| 28.402 |
0.49090 |
0.29830 |
| 29.367 |
0.45590 |
0.34830 |
| 30.058 |
0.42100 |
0.39820 |
| 30.581 |
0.38590 |
0.44830 |
| 30.984 |
0.35100 |
0.49820 |
| 37.457 |
0.02030 |
0.68140 |
| 36.649 |
0.05000 |
0.66340 |
| 35.461 |
0.10120 |
0.62760 |
| 34.477 |
0.15090 |
0.59290 |
| 33.599 |
0.20080 |
0.55800 |
| 32.777 |
0.25080 |
0.52310 |
| 31.997 |
0.30090 |
0.48810 |
| 31.208 |
0.35100 |
0.45310 |
| 30.395 |
0.40110 |
0.41810 |
| 29.514 |
0.45110 |
0.38330 |
| 28.530 |
0.50100 |
0.34840 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Villamanan M.A.; Allawi A.J.; van Ness H.C.: 11. Total Pressure Data and GE for Ethylene Glycol/Acetone/Water and for Ethylene Glycol/Acetonitrile/Water at 50 °C. J.Chem.Eng.Data 29 (1984) 293-296 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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