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 22870
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
| 44.978 |
1.00000 |
0.00000 |
| 41.005 |
0.70030 |
0.29970 |
| 40.697 |
0.68320 |
0.29230 |
| 40.317 |
0.66360 |
0.28400 |
| 39.643 |
0.62920 |
0.26920 |
| 38.967 |
0.59480 |
0.25450 |
| 38.261 |
0.55940 |
0.23930 |
| 37.565 |
0.52500 |
0.22460 |
| 36.844 |
0.48970 |
0.20950 |
| 36.104 |
0.45480 |
0.19450 |
| 35.366 |
0.41880 |
0.17910 |
| 34.642 |
0.38490 |
0.16460 |
| 33.873 |
0.35010 |
0.14970 |
| 24.655 |
0.00000 |
0.00000 |
| 31.861 |
0.30530 |
0.00000 |
| 31.925 |
0.29770 |
0.02490 |
| 31.976 |
0.29000 |
0.05010 |
| 32.033 |
0.27450 |
0.10070 |
| 32.041 |
0.25930 |
0.15070 |
| 32.017 |
0.24780 |
0.18840 |
| 31.925 |
0.22890 |
0.25030 |
| 31.809 |
0.21360 |
0.30040 |
| 31.649 |
0.19830 |
0.35060 |
| 31.449 |
0.18300 |
0.40050 |
| 31.211 |
0.16790 |
0.45010 |
| 30.932 |
0.15270 |
0.50010 |
| 24.398 |
0.00000 |
1.00000 |
| 33.923 |
0.30420 |
0.69580 |
| 33.787 |
0.29640 |
0.67800 |
| 33.657 |
0.28840 |
0.65960 |
| 33.393 |
0.27350 |
0.62560 |
| 33.119 |
0.25880 |
0.59180 |
| 32.801 |
0.24270 |
0.55490 |
| 32.501 |
0.22810 |
0.52150 |
| 32.173 |
0.21290 |
0.48660 |
| 31.831 |
0.19780 |
0.45220 |
| 31.468 |
0.18250 |
0.41710 |
| 31.087 |
0.16730 |
0.38230 |
| 30.688 |
0.15220 |
0.34770 |
| 24.411 |
0.00000 |
1.00000 |
| 27.151 |
0.00000 |
0.70120 |
| 28.084 |
0.03530 |
0.67650 |
| 28.664 |
0.05780 |
0.66070 |
| 29.759 |
0.10340 |
0.62870 |
| 30.917 |
0.15380 |
0.59330 |
| 31.921 |
0.20040 |
0.56070 |
| 32.980 |
0.25140 |
0.52490 |
| 33.933 |
0.30020 |
0.49070 |
| 34.881 |
0.35010 |
0.45570 |
| 35.806 |
0.40080 |
0.42020 |
| 36.682 |
0.45000 |
0.38560 |
| 37.548 |
0.50050 |
0.35020 |
| 44.950 |
1.00000 |
0.00000 |
| 39.798 |
0.71400 |
0.00000 |
| 39.667 |
0.69870 |
0.02140 |
| 39.477 |
0.67780 |
0.05070 |
| 39.110 |
0.64150 |
0.10150 |
| 38.717 |
0.60620 |
0.15100 |
| 38.292 |
0.57070 |
0.20070 |
| 37.834 |
0.53470 |
0.25110 |
| 37.340 |
0.49920 |
0.30090 |
| 36.829 |
0.46400 |
0.35020 |
| 36.274 |
0.42810 |
0.40040 |
| 35.672 |
0.39230 |
0.45060 |
| 35.048 |
0.35690 |
0.50020 |
| 24.654 |
0.00000 |
0.00000 |
| 27.135 |
0.00000 |
0.30030 |
| 27.786 |
0.02950 |
0.29140 |
| 28.270 |
0.05230 |
0.28450 |
| 29.327 |
0.10290 |
0.26940 |
| 30.322 |
0.15190 |
0.25470 |
| 31.283 |
0.20080 |
0.24000 |
| 32.232 |
0.25050 |
0.22510 |
| 33.199 |
0.30130 |
0.20980 |
| 34.097 |
0.35030 |
0.19510 |
| 34.994 |
0.40000 |
0.18020 |
| 35.878 |
0.44990 |
0.16520 |
| 36.761 |
0.50000 |
0.15010 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Chamorro C.R.; Segovia J.J.; Martin M.C.; Villamanan M.A.: Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor-Liquid Equilibrium of Ternary Mixtures Containing Di-isopropyl Ether of Cyclohexane and 1-Hexene + Benzene at 313.15 K. J.Chem.Eng.Data 47 (2002) 316-321 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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