Dortmund Data Bank
Azeotropic 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.
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
3 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Data Table
Azeotropic Type |
T [K] |
P [kPa] |
yaz,1 [mol/mol] |
yaz,2 [mol/mol] |
yaz,3 [mol/mol] |
Measurement Method |
Evaluation |
Source |
homPmaxMisGap |
n.a. |
101.300 |
n.a.
|
n.a.
|
n.a.
|
Phase equilibrium |
Author |
2 |
homPmaxMisGap |
334.030 |
49.400 |
0.77700 |
0.16000 |
n.a.
|
Phase equilibrium |
Author from VLE by regression |
1 |
homPmaxMisGap |
348.370 |
90.400 |
0.77200 |
0.17000 |
n.a.
|
Phase equilibrium |
Author from VLE by regression |
1 |
(yaz - vapor and liquid mole fraction)
List of Azeotrope Types
homPmaxMisGap |
homogeneous pressure maximum miscibility gap |
List of References
1 |
Fele L.; Stemberger N.Z.; Grilc V.: Separation of Water + Ethanol + (o-, m-, p-) Xylene Systems. J.Chem.Eng.Data 45 (2000) 784-791 |
2 |
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 |
Azeotropic Data Overview
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