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 11131
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
| 2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 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] |
| 19.002 |
0.29390 |
0.01940 |
| 31.688 |
0.28490 |
0.04970 |
| 45.022 |
0.27010 |
0.09890 |
| 53.113 |
0.25530 |
0.14830 |
| 58.269 |
0.24030 |
0.19830 |
| 61.694 |
0.22530 |
0.24830 |
| 64.088 |
0.21030 |
0.29840 |
| 65.872 |
0.19530 |
0.34840 |
| 67.296 |
0.18020 |
0.39860 |
| 68.458 |
0.16520 |
0.44870 |
| 69.512 |
0.15020 |
0.49880 |
| 12.355 |
0.68440 |
0.02050 |
| 23.113 |
0.66380 |
0.05000 |
| 36.441 |
0.62920 |
0.09950 |
| 45.598 |
0.59510 |
0.14830 |
| 52.070 |
0.56030 |
0.19800 |
| 56.629 |
0.52540 |
0.24810 |
| 59.892 |
0.49050 |
0.29790 |
| 62.291 |
0.45590 |
0.34760 |
| 64.147 |
0.42060 |
0.39800 |
| 65.616 |
0.38580 |
0.44780 |
| 66.861 |
0.35070 |
0.49810 |
| 74.214 |
0.02120 |
0.68470 |
| 73.393 |
0.04990 |
0.66460 |
| 72.065 |
0.09980 |
0.62960 |
| 71.490 |
0.12430 |
0.61250 |
| 70.922 |
0.14730 |
0.59640 |
| 69.622 |
0.20360 |
0.55700 |
| 68.342 |
0.25970 |
0.51780 |
| 67.066 |
0.31550 |
0.47870 |
| 65.692 |
0.37060 |
0.44020 |
| 64.147 |
0.42550 |
0.40180 |
| 62.391 |
0.47980 |
0.36380 |
| 61.618 |
0.50040 |
0.34940 |
| 65.781 |
0.02000 |
0.29390 |
| 65.213 |
0.05060 |
0.28460 |
| 64.152 |
0.10010 |
0.26980 |
| 62.939 |
0.15020 |
0.25480 |
| 61.503 |
0.20060 |
0.23970 |
| 59.903 |
0.25030 |
0.22480 |
| 58.039 |
0.30030 |
0.20980 |
| 55.949 |
0.35040 |
0.19480 |
| 53.592 |
0.40020 |
0.17990 |
| 50.936 |
0.45030 |
0.16490 |
| 47.981 |
0.50030 |
0.15000 |
| 69.372 |
0.29410 |
0.68490 |
| 69.412 |
0.28540 |
0.66450 |
| 69.425 |
0.27030 |
0.62920 |
| 69.322 |
0.25510 |
0.59380 |
| 69.166 |
0.24020 |
0.55910 |
| 68.598 |
0.21010 |
0.48920 |
| 68.281 |
0.19510 |
0.45400 |
| 67.726 |
0.18010 |
0.41910 |
| 67.074 |
0.16420 |
0.38210 |
| 66.371 |
0.15000 |
0.34910 |
| 56.049 |
0.68630 |
0.29290 |
| 55.990 |
0.66590 |
0.28410 |
| 55.850 |
0.63070 |
0.26900 |
| 55.639 |
0.59570 |
0.25410 |
| 55.323 |
0.56100 |
0.23920 |
| 54.915 |
0.52520 |
0.22400 |
| 54.436 |
0.49020 |
0.20900 |
| 53.844 |
0.45540 |
0.19420 |
| 53.142 |
0.42030 |
0.17920 |
| 52.185 |
0.38530 |
0.16430 |
| 51.186 |
0.35020 |
0.14930 |
| 56.055 |
0.68760 |
0.29280 |
| 55.995 |
0.66640 |
0.28370 |
| 55.850 |
0.63130 |
0.26880 |
| 55.622 |
0.59590 |
0.25370 |
| 55.315 |
0.56080 |
0.23870 |
| 54.917 |
0.52580 |
0.22370 |
(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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