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 18099
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
Search the DDB for all data of this mixture
Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
399.10 |
0.00000 |
0.00000 |
397.78 |
0.00730 |
0.03990 |
395.68 |
0.02050 |
0.10600 |
390.87 |
0.05200 |
0.24400 |
384.30 |
0.10150 |
0.40400 |
380.32 |
0.13630 |
0.49470 |
376.14 |
0.17790 |
0.57760 |
372.34 |
0.22130 |
0.64290 |
369.97 |
0.25180 |
0.68310 |
366.50 |
0.30200 |
0.73470 |
365.69 |
0.31490 |
0.74620 |
363.70 |
0.34840 |
0.77290 |
359.99 |
0.41980 |
0.81840 |
358.14 |
0.46060 |
0.84020 |
356.19 |
0.50760 |
0.86240 |
354.48 |
0.55250 |
0.88000 |
352.55 |
0.60160 |
0.89900 |
351.35 |
0.64410 |
0.91030 |
349.78 |
0.69440 |
0.92490 |
348.28 |
0.74530 |
0.93860 |
346.19 |
0.81980 |
0.95740 |
345.14 |
0.85800 |
0.96650 |
342.69 |
0.94750 |
0.98760 |
342.12 |
0.96750 |
0.99230 |
341.95 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Feng L.-C.; Chou C.-H.; Tang M.; Chen Y.-P.: Vapor-Liquid Equilibria of Binary Mixtures 2-Butanol + Butyl Acetate, Hexane + Butyl Acetate, and Cyclohexane + 2-Butanol at 101.3 kPa. J.Chem.Eng.Data 43 (1998) 658-661 |
Diagrams
List of All References
Source |
Feng L.-C.; Chou C.-H.; Tang M.; Chen Y.-P.: Vapor-Liquid Equilibria of Binary Mixtures 2-Butanol + Butyl Acetate, Hexane + Butyl Acetate, and Cyclohexane + 2-Butanol at 101.3 kPa. J.Chem.Eng.Data 43 (1998) 658-661 |
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH