Dortmund Data Bank
Vapor-Liquid Equilibrium 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.
Vapor-Liquid Equilibrium Data Set 24291
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
3 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
330.05 |
0.62674 |
0.07040 |
0.73298 |
0.12494 |
324.65 |
0.66753 |
0.22494 |
0.72126 |
0.24948 |
336.05 |
0.31670 |
0.07115 |
0.52216 |
0.15364 |
335.15 |
0.11337 |
0.22922 |
0.24203 |
0.39604 |
325.25 |
0.37452 |
0.50483 |
0.56698 |
0.35913 |
331.15 |
0.12589 |
0.50909 |
0.27769 |
0.47790 |
334.65 |
0.60816 |
0.00000 |
0.80540 |
0.00000 |
339.05 |
0.40822 |
0.00000 |
0.67453 |
0.00000 |
337.75 |
0.00000 |
0.31736 |
0.00000 |
0.52170 |
335.85 |
0.00000 |
0.51125 |
0.00000 |
0.60040 |
322.75 |
0.68998 |
0.31001 |
0.74399 |
0.25601 |
322.85 |
0.49728 |
0.50272 |
0.68820 |
0.31180 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Kozhenkov A.V.; Sobolev D.M.; Malenko Yu.I.: Liquid-Vapor Equilibrium in the Four-Component Acetone-Hexane-Isopropanol-Toluene System. Zh.Prikl.Khim. 62 (1989) 1319-1322 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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