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 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 3 |
CH4O |
32.042 |
67-56-1 |
Methanol |
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 |
| homSaddle |
323.150 |
75.570 |
0.31300 |
0.25390 |
n.a.
|
n.a. |
Author from VLE by regression |
3 |
| homSaddle |
330.650 |
n.a. |
0.31726 |
0.24182 |
n.a.
|
n.a. |
Author |
1 |
| homSaddle |
330.820 |
101.325 |
0.31800 |
0.24100 |
n.a.
|
n.a. |
Author |
2 |
(yaz - vapor and liquid mole fraction)
List of Azeotrope Types
| homSaddle |
homogeneous saddle |
List of References
| 1 |
Ewell R.H.; Welch L.M.: Rectification in Ternary Systems Containing Binary Azeotropes. Ind.Eng.Chem. 37 (1945) 1224-1231 |
| 2 |
Hiaki T.; Kurihara K.; Kojima K.: Vapor-Liquid Equilibria for Acetone + Chloroform + Methanol and Constituent Binary Systems at 101.3kPa. J.Chem.Eng.Data 39 (1994) 714-719 |
| 3 |
Goral M.; Kolasinska G.; Oracz P.; Warycha S.: Vapor-Liquid Equilibria. II. The Ternary System Methanol-Chloroform-Acetone at 313.15 and 323.15 K. Fluid Phase Equilib. 23 (1985) 89-116 |
Azeotropic Data Overview
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