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 21061
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 334.13 |
0.12290 |
0.85690 |
0.12270 |
0.85390 |
| 334.03 |
0.12950 |
0.82860 |
0.13550 |
0.82130 |
| 333.96 |
0.13120 |
0.80270 |
0.14430 |
0.79590 |
| 333.86 |
0.13630 |
0.77340 |
0.15540 |
0.77160 |
| 334.04 |
0.13780 |
0.74640 |
0.16680 |
0.75000 |
| 334.16 |
0.14960 |
0.70400 |
0.18680 |
0.72010 |
| 334.08 |
0.14680 |
0.67620 |
0.19590 |
0.70470 |
| 334.22 |
0.18110 |
0.80890 |
0.16940 |
0.81690 |
| 334.12 |
0.18610 |
0.78350 |
0.18030 |
0.77940 |
| 334.05 |
0.19000 |
0.75800 |
0.19240 |
0.75150 |
| 334.04 |
0.19170 |
0.73570 |
0.20550 |
0.72500 |
| 334.04 |
0.19790 |
0.70360 |
0.21500 |
0.70190 |
| 334.07 |
0.20620 |
0.66880 |
0.23100 |
0.67510 |
| 334.12 |
0.21050 |
0.63590 |
0.24610 |
0.65190 |
| 334.06 |
0.23150 |
0.75010 |
0.20600 |
0.76530 |
| 333.88 |
0.23460 |
0.72690 |
0.21410 |
0.73530 |
| 333.90 |
0.24180 |
0.69790 |
0.22970 |
0.70100 |
| 333.90 |
0.24630 |
0.67430 |
0.24170 |
0.67430 |
| 333.96 |
0.26910 |
0.62610 |
0.26670 |
0.63970 |
| 334.35 |
0.35600 |
0.62800 |
0.28810 |
0.67880 |
| 334.14 |
0.34860 |
0.61730 |
0.28680 |
0.65210 |
| 333.96 |
0.35900 |
0.58860 |
0.30330 |
0.61580 |
| 334.56 |
0.40790 |
0.57640 |
0.29960 |
0.65800 |
| 334.35 |
0.40660 |
0.56200 |
0.30390 |
0.62450 |
| 334.86 |
0.47510 |
0.51120 |
0.32380 |
0.62470 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Fele L.; Stemberger N.Z.; Grilc V.: Separation of Water + Ethanol + (o-, m-, p-) Xylene Systems. J.Chem.Eng.Data 45 (2000) 784-791 |
Vapor-Liquid Equilibrium Data Set 21062
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 348.39 |
0.12730 |
0.82900 |
0.13530 |
0.82370 |
| 348.41 |
0.13030 |
0.80370 |
0.14460 |
0.79960 |
| 348.44 |
0.13580 |
0.77200 |
0.15710 |
0.77510 |
| 348.53 |
0.13610 |
0.72560 |
0.16830 |
0.75170 |
| 348.59 |
0.14230 |
0.71300 |
0.18250 |
0.73030 |
| 348.69 |
0.14270 |
0.67520 |
0.19470 |
0.71100 |
| 348.52 |
0.18430 |
0.80570 |
0.17430 |
0.81300 |
| 348.44 |
0.18890 |
0.77770 |
0.20110 |
0.76610 |
| 348.42 |
0.19320 |
0.75560 |
0.19490 |
0.75360 |
| 348.42 |
0.19700 |
0.72780 |
0.20700 |
0.72690 |
| 348.47 |
0.19870 |
0.70520 |
0.21250 |
0.70970 |
| 348.52 |
0.20260 |
0.67060 |
0.23220 |
0.68070 |
| 348.59 |
0.20170 |
0.64820 |
0.24270 |
0.66410 |
| 348.42 |
0.22440 |
0.75720 |
0.20610 |
0.76850 |
| 348.39 |
0.23700 |
0.73110 |
0.22190 |
0.73100 |
| 348.34 |
0.23940 |
0.70010 |
0.22700 |
0.70810 |
| 348.35 |
0.24470 |
0.67260 |
0.24630 |
0.67590 |
| 348.39 |
0.25170 |
0.63960 |
0.28210 |
0.63070 |
| 348.70 |
0.35130 |
0.63240 |
0.29190 |
0.67810 |
| 348.57 |
0.34090 |
0.62440 |
0.28800 |
0.65680 |
| 348.47 |
0.35500 |
0.59220 |
0.30500 |
0.62120 |
| 348.99 |
0.40670 |
0.57790 |
0.30770 |
0.65440 |
| 348.78 |
0.41610 |
0.55170 |
0.32170 |
0.61710 |
| 349.27 |
0.46990 |
0.51620 |
0.33440 |
0.62210 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Fele L.; Stemberger N.Z.; Grilc V.: Separation of Water + Ethanol + (o-, m-, p-) Xylene Systems. J.Chem.Eng.Data 45 (2000) 784-791 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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