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 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
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 |
323.150 |
n.a. |
n.a.
|
n.a.
|
Phase equilibrium |
DDBST |
2 |
homPmax |
333.950 |
101.325 |
0.92100 |
n.a.
|
n.a. |
Author |
1 |
homPmax |
334.150 |
101.325 |
0.95000 |
n.a.
|
Phase equilibrium |
DDBST from VLE by regression |
3 |
(yaz - vapor and liquid mole fraction)
List of Azeotrope Types
homPmax |
homogeneous pressure maximum |
List of References
1 |
Hanumantharao G.; Subbarao B.V.: Isobaric Vapor-Liquid Equilibria-Chloroform-Isopropanol, Tertiary Butanol-Toluene and Ternary Butanol-Trichloroethylene Systems. Indian J.Technol. 12 (1974) 292-295 |
2 |
Nagata I.: Vapor-Liquid Equilibria for the Ternary System 2-Propanol-Chloroform-Benzene. J.Chem.Eng.Data 30 (1985) 80-82 |
3 |
Nagata I.: Isobaric Vapor-Liquid Equilibrium Data for Binary Systems. Can.J.Chem.Eng. 41 (1963) 21-23 |
Diagrams
Azeotropic Data Overview
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