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 30032
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 3 |
C5H9NO |
99.133 |
872-50-4 |
N-Methyl-2-pyrrolidone |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
| 73.350 |
0.15670 |
0.63940 |
| 71.090 |
0.11700 |
0.47730 |
| 67.220 |
0.07820 |
0.31880 |
| 54.660 |
0.03960 |
0.16160 |
| 80.250 |
0.30850 |
0.49310 |
| 77.060 |
0.22920 |
0.36630 |
| 74.230 |
0.15330 |
0.24500 |
| 62.330 |
0.07880 |
0.12610 |
| 85.810 |
0.47340 |
0.31580 |
| 83.660 |
0.35530 |
0.23710 |
| 81.060 |
0.23450 |
0.15650 |
| 69.470 |
0.12060 |
0.08050 |
| 91.460 |
0.64130 |
0.16310 |
| 89.550 |
0.51630 |
0.13130 |
| 87.470 |
0.32380 |
0.08230 |
| 74.310 |
0.15280 |
0.03890 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Dojcansky J.; Bafrncova S; Surovy J.: Application of the Wilson Equation with Binary Parameters to the Prediction of the Isothermal Vapour-Liquid Equilibrium Data of Ternary and Quaternary Systems in the Assessment of the Polar Solvent in Extractive Distillation. Chem.Papers 55 (2001) 71-74 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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