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 18363
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 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] |
| 342.40 |
0.00000 |
0.98800 |
0.00000 |
0.70400 |
| 342.40 |
0.00000 |
0.00060 |
0.00000 |
0.70400 |
| 336.60 |
0.22200 |
0.74500 |
0.33670 |
0.51770 |
| 336.60 |
0.03100 |
0.00100 |
0.33670 |
0.51770 |
| 335.89 |
0.26600 |
0.69600 |
0.36570 |
0.48360 |
| 335.89 |
0.04200 |
0.00200 |
0.36570 |
0.48360 |
| 335.03 |
0.32100 |
0.60900 |
0.44250 |
0.42780 |
| 335.03 |
0.06200 |
0.00400 |
0.44250 |
0.42780 |
| 333.77 |
0.42000 |
0.46700 |
0.52560 |
0.32230 |
| 333.77 |
0.08200 |
0.00300 |
0.52560 |
0.32230 |
| 334.20 |
0.40600 |
0.48700 |
0.48930 |
0.37840 |
| 334.20 |
0.08070 |
0.00440 |
0.48930 |
0.37840 |
| 333.30 |
0.44900 |
0.41900 |
0.50620 |
0.33690 |
| 333.30 |
0.08800 |
0.00300 |
0.50620 |
0.33690 |
| 332.94 |
0.50000 |
0.31900 |
0.57060 |
0.27770 |
| 332.94 |
0.10500 |
0.00300 |
0.57060 |
0.27770 |
| 332.64 |
0.52100 |
0.17900 |
0.62990 |
0.22300 |
| 332.94 |
0.14300 |
0.00400 |
0.62990 |
0.22300 |
| 332.72 |
0.60000 |
0.32000 |
0.67430 |
0.24460 |
| 331.12 |
0.80000 |
0.16000 |
0.85350 |
0.11340 |
| 332.39 |
0.60000 |
0.24000 |
0.67900 |
0.21360 |
| 330.93 |
0.80000 |
0.12000 |
0.84590 |
0.09530 |
| 331.44 |
0.60000 |
0.16000 |
0.71020 |
0.18100 |
| 330.68 |
0.80000 |
0.08000 |
0.86000 |
0.07900 |
| 332.21 |
0.60000 |
0.08000 |
0.75270 |
0.11920 |
| 330.66 |
0.80000 |
0.04000 |
0.87970 |
0.03580 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Polyakova E.V.; Rudakovskaya T.S.; Pavlenko T.G.; Timofeev V.S.; Serafimov L.A.: Experimentelle Untersuchung und Gleichgewichtsberechnung in Systemen mit verschließender Binodal. Fiziko-chimiceskie osnovy rektifikacii (1977) 51-69 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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