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 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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] |
Measurement Method |
Evaluation |
Source |
homPmax |
298.150 |
24.755 |
n.a.
|
0.73900 |
Phase equilibrium |
DDBST |
1 |
homPmax |
318.150 |
60.138 |
n.a.
|
0.67600 |
Phase equilibrium |
DDBST |
3 |
homPmax |
323.150 |
72.841 |
n.a.
|
0.65400 |
Phase equilibrium |
DDBST |
2 |
(yaz - vapor and liquid mole fraction)
List of Azeotrope Types
homPmax |
homogeneous pressure maximum |
List of References
1 |
Smith V.C.; Robinson, Jr.R.L.: Vapor-Liquid Equilibria at 25°C in the Binary Mixtures Formed by Hexane, Benzene and Ethanol. J.Chem.Eng.Data 15 (1970) 391-395 |
2 |
Diaz Pena M.; Rodriguez Cheda D.: I. Los Sistemas Benceno + Ciclohexano a 70 C y Metanol + n-Hexano a 50 C. Anal.Quim. 66 (1970) 721-735 |
3 |
O'Shea S.J.; Stokes R.H.: Activity Coefficients and Excess Partial Molar Enthalpies for (Ethanol + Hexane) from 283 to 318 K. J.Chem.Thermodyn. 18 (1986) 691-696 |
Diagrams
Azeotropic Data Overview
© DDBST GmbH