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 12305
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 |
H2O |
18.015 |
7732-18-5 |
Water |
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] |
| 326.35 |
0.78200 |
0.03500 |
0.77600 |
0.15300 |
| 324.85 |
0.69200 |
0.03500 |
0.69700 |
0.24900 |
| 326.65 |
0.88400 |
0.03600 |
0.83700 |
0.10500 |
| 326.05 |
0.84500 |
0.04300 |
0.79700 |
0.15200 |
| 324.75 |
0.73700 |
0.04700 |
0.70200 |
0.23600 |
| 325.35 |
0.76100 |
0.05000 |
0.72800 |
0.21100 |
| 326.15 |
0.90100 |
0.05600 |
0.81600 |
0.15300 |
| 322.85 |
0.75500 |
0.07100 |
0.65300 |
0.27400 |
| 322.95 |
0.71000 |
0.08200 |
0.62500 |
0.29700 |
| 324.55 |
0.79600 |
0.08300 |
0.70200 |
0.22600 |
| 323.95 |
0.84700 |
0.08600 |
0.70100 |
0.22300 |
| 322.75 |
0.71900 |
0.12000 |
0.58000 |
0.33600 |
| 323.45 |
0.81300 |
0.12100 |
0.67800 |
0.27100 |
| 323.95 |
0.85200 |
0.12100 |
0.70500 |
0.25600 |
| 322.95 |
0.76200 |
0.13000 |
0.63400 |
0.29000 |
| 323.15 |
0.80800 |
0.15100 |
0.64700 |
0.29900 |
| 322.55 |
0.75000 |
0.17600 |
0.62500 |
0.33100 |
| 322.35 |
0.71500 |
0.18100 |
0.57200 |
0.33800 |
| 322.25 |
0.76300 |
0.19900 |
0.63300 |
0.32600 |
| 321.95 |
0.70800 |
0.23300 |
0.58500 |
0.34600 |
| 321.75 |
0.66600 |
0.23900 |
0.55900 |
0.37800 |
| 321.75 |
0.68600 |
0.28600 |
0.59900 |
0.36000 |
| 321.85 |
0.64300 |
0.29100 |
0.55200 |
0.37200 |
| 321.95 |
0.65600 |
0.30300 |
0.57600 |
0.37900 |
| 321.45 |
0.61800 |
0.33600 |
0.57600 |
0.38600 |
| 321.85 |
0.59300 |
0.34600 |
0.53500 |
0.41200 |
| 321.65 |
0.58500 |
0.37300 |
0.53800 |
0.41900 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Srinivasan D.; Lakshman C.M.; Laddha G.S.: Isothermal Vapor-Liquid Equilibrium Data at Atmospheric Pressure for the Ternary System Acetone-n-Hexane-Water. Indian J.Technol. 13 (1975) 431-434 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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