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 21042
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
Search the DDB for all data of this mixture
Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
9.601 |
0.01400 |
0.39000 |
15.800 |
0.03600 |
0.59100 |
22.899 |
0.07200 |
0.70800 |
34.800 |
0.24800 |
0.81700 |
37.900 |
0.45700 |
0.84700 |
39.999 |
0.67200 |
0.88000 |
42.600 |
0.88900 |
0.94000 |
43.300 |
0.94500 |
0.96400 |
44.900 |
0.97800 |
0.98400 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Miyamoto S.; Nakamura S.; Iwai Y.; Arai Y.: Measurement of Isothermal Vapor-Liquid Equilibria for Hydrocarbon + Monocarboxylic Acid Binary Systems by a Flow-Type Apparatus. J.Chem.Eng.Data 45 (2000) 857-861 |
Diagrams
List of All References
Source |
Miyamoto S.; Nakamura S.; Iwai Y.; Arai Y.: Measurement of Isothermal Vapor-Liquid Equilibria for Hydrocarbon + Monocarboxylic Acid Binary Systems by a Flow-Type Apparatus. J.Chem.Eng.Data 45 (2000) 857-861 |
Vapor-Liquid Equilibrium Data Overview
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