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 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CO2 |
44.010 |
124-38-9 |
Carbon dioxide |
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 |
| none |
298.150 |
n.a. |
n.a.
|
n.a.
|
n.a. |
Author |
1 |
| nonesupercrit |
333.150 |
n.a. |
n.a.
|
n.a.
|
Phase equilibrium |
Author from VLE |
2 |
| nonesupercrit |
353.150 |
n.a. |
n.a.
|
n.a.
|
Phase equilibrium |
Author from VLE |
2 |
(yaz - vapor and liquid mole fraction)
List of Azeotrope Types
| none |
zeotropic |
| nonesupercrit |
zeotropic supercritical |
List of References
| 1 |
Katayama T.; Ohgaki K.; Maekawa G.; Goto M.; Nagano T.: Isothermal Vapor-Liquid Equilibria of Acetone-Carbon Dioxide and Methanol-Carbon Dioxide Systems at High Pressures. J.Chem.Eng.Japan 8 (1975) 89-92 |
| 2 |
Han F.; Xue Y.; Tian Y.; Zhao X.; Chen L.: Vapor-Liquid Equilibria of the Carbon Dioxide + Acetone System at Pressures from (2.36 to 11.77) MPa and Temperatures from (333.15 to 393.15) K. J.Chem.Eng.Data 50 (2005) 36-39 |
Azeotropic Data Overview
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