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 21063
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 |
106-42-3 |
p-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] |
| 334.07 |
0.12670 |
0.85320 |
0.12660 |
0.84950 |
| 333.97 |
0.12800 |
0.82920 |
0.13610 |
0.81990 |
| 334.02 |
0.13150 |
0.80250 |
0.14460 |
0.79410 |
| 334.04 |
0.13400 |
0.77440 |
0.15320 |
0.77290 |
| 334.04 |
0.13800 |
0.74320 |
0.16590 |
0.74890 |
| 334.02 |
0.14030 |
0.71470 |
0.17930 |
0.72600 |
| 334.16 |
0.14300 |
0.68040 |
0.19350 |
0.70420 |
| 334.29 |
0.18050 |
0.81020 |
0.17920 |
0.80690 |
| 334.15 |
0.18470 |
0.78600 |
0.17670 |
0.78750 |
| 334.13 |
0.18620 |
0.76230 |
0.18630 |
0.75700 |
| 334.08 |
0.19030 |
0.73410 |
0.19830 |
0.72650 |
| 334.08 |
0.19430 |
0.70690 |
0.21030 |
0.70510 |
| 334.07 |
0.20070 |
0.67710 |
0.22740 |
0.67650 |
| 334.10 |
0.20570 |
0.64330 |
0.24280 |
0.65040 |
| 334.03 |
0.22420 |
0.69950 |
0.22290 |
0.69790 |
| 334.19 |
0.23260 |
0.74890 |
0.20590 |
0.76560 |
| 333.97 |
0.23530 |
0.72590 |
0.21400 |
0.73340 |
| 334.06 |
0.24240 |
0.69690 |
0.23080 |
0.69750 |
| 334.02 |
0.24490 |
0.68460 |
0.23660 |
0.68460 |
| 333.91 |
0.24750 |
0.66980 |
0.24380 |
0.66940 |
| 333.86 |
0.25310 |
0.64060 |
0.25650 |
0.64520 |
| 334.39 |
0.32290 |
0.66040 |
0.26560 |
0.69930 |
| 334.14 |
0.33060 |
0.63470 |
0.27180 |
0.66720 |
| 333.93 |
0.33730 |
0.60740 |
0.27740 |
0.63450 |
| 334.61 |
0.40780 |
0.57860 |
0.30690 |
0.65920 |
| 334.32 |
0.41370 |
0.55430 |
0.31560 |
0.61230 |
| 334.78 |
0.47860 |
0.51020 |
0.32750 |
0.62070 |
(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 21064
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 |
106-42-3 |
p-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] |
| 348.38 |
0.12360 |
0.85570 |
0.12590 |
0.85210 |
| 348.36 |
0.12930 |
0.82830 |
0.13780 |
0.82140 |
| 348.40 |
0.12660 |
0.80670 |
0.14420 |
0.79920 |
| 348.44 |
0.13440 |
0.77340 |
0.15510 |
0.77590 |
| 348.51 |
0.13810 |
0.74290 |
0.16740 |
0.75270 |
| 348.59 |
0.13990 |
0.71220 |
0.18070 |
0.72880 |
| 348.64 |
0.14270 |
0.67710 |
0.19440 |
0.70650 |
| 348.53 |
0.17780 |
0.81180 |
0.16980 |
0.81650 |
| 348.44 |
0.18360 |
0.78520 |
0.17840 |
0.78680 |
| 348.40 |
0.18700 |
0.76180 |
0.18850 |
0.75920 |
| 348.38 |
0.19090 |
0.73290 |
0.20010 |
0.73100 |
| 348.44 |
0.19810 |
0.70030 |
0.21740 |
0.70200 |
| 348.47 |
0.20180 |
0.67280 |
0.23050 |
0.68070 |
| 348.50 |
0.20800 |
0.63850 |
0.24900 |
0.65300 |
| 348.48 |
0.22650 |
0.75530 |
0.21120 |
0.76320 |
| 348.38 |
0.23530 |
0.72640 |
0.22050 |
0.73310 |
| 348.36 |
0.24350 |
0.69570 |
0.23480 |
0.69950 |
| 348.34 |
0.24660 |
0.66870 |
0.24770 |
0.67080 |
| 348.37 |
0.25410 |
0.63890 |
0.26180 |
0.64560 |
| 348.71 |
0.32360 |
0.66010 |
0.26290 |
0.70340 |
| 348.55 |
0.33080 |
0.63380 |
0.27460 |
0.66910 |
| 348.47 |
0.33790 |
0.60690 |
0.28900 |
0.63320 |
| 348.99 |
0.40250 |
0.58150 |
0.30570 |
0.65400 |
| 348.79 |
0.41630 |
0.55400 |
0.30540 |
0.62580 |
| 349.27 |
0.47750 |
0.50910 |
0.33700 |
0.61740 |
(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 29726
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 |
106-42-3 |
p-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] |
| 351.51 |
0.34600 |
0.50300 |
0.33200 |
0.54800 |
| 351.56 |
0.22900 |
0.49900 |
0.31200 |
0.57000 |
| 351.53 |
0.15700 |
0.65500 |
0.20800 |
0.69600 |
| 351.27 |
0.24300 |
0.62600 |
0.25800 |
0.64200 |
| 351.59 |
0.46700 |
0.47200 |
0.33900 |
0.54700 |
| 351.83 |
0.45900 |
0.51400 |
0.31800 |
0.60900 |
| 351.23 |
0.28700 |
0.63400 |
0.26400 |
0.65200 |
| 351.19 |
0.22400 |
0.73400 |
0.20400 |
0.74700 |
| 351.16 |
0.19600 |
0.73500 |
0.19400 |
0.73900 |
| 351.27 |
0.17700 |
0.70400 |
0.19800 |
0.71600 |
| 351.26 |
0.10200 |
0.83000 |
0.11500 |
0.83100 |
| 351.65 |
0.11900 |
0.70100 |
0.16300 |
0.74100 |
| 352.19 |
0.09700 |
0.58100 |
0.18500 |
0.70700 |
| 352.59 |
0.08200 |
0.49500 |
0.19900 |
0.68800 |
| 351.41 |
0.31400 |
0.66000 |
0.25800 |
0.69800 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Gomis V.; Pequenin A.; Asensi J.C.: Isobaric vapor-liquid-liquid equilibrium and vapor-liquid equilibrium for the system water-ethanol-1,4-dimethylbenzene at 101.3 kPa. Fluid Phase Equilib. 281 (2009) 1-4 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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