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 17519
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 3 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 4 |
CH4O |
32.042 |
67-56-1 |
Methanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
x3 [mol/mol] |
| 24.625 |
1.00000 |
0.00000 |
0.00000 |
| 37.270 |
0.00000 |
1.00000 |
0.00000 |
| 56.603 |
0.00000 |
0.00000 |
1.00000 |
| 35.453 |
0.00000 |
0.00000 |
0.00000 |
| 65.680 |
0.01760 |
0.04400 |
0.74330 |
| 69.050 |
0.33240 |
0.22100 |
0.35370 |
| 65.871 |
0.20070 |
0.13340 |
0.09000 |
| 65.260 |
0.32720 |
0.21760 |
0.06150 |
| 62.150 |
0.01760 |
0.04400 |
0.12680 |
| 69.130 |
0.05400 |
0.13500 |
0.10960 |
| 69.430 |
0.08640 |
0.21610 |
0.09420 |
| 62.040 |
0.03530 |
0.02350 |
0.27430 |
| 67.670 |
0.09560 |
0.06360 |
0.24500 |
| 68.570 |
0.17280 |
0.11490 |
0.20760 |
| 68.100 |
0.27830 |
0.18500 |
0.15640 |
| 66.411 |
0.43200 |
0.28720 |
0.08180 |
| 69.060 |
0.03270 |
0.08190 |
0.25800 |
| 71.719 |
0.06590 |
0.16490 |
0.22410 |
| 70.939 |
0.16940 |
0.42370 |
0.11860 |
| 65.991 |
0.25250 |
0.63170 |
0.03370 |
| 61.560 |
0.54170 |
0.36030 |
0.04510 |
| 69.040 |
0.35010 |
0.23280 |
0.19180 |
| 69.970 |
0.22600 |
0.15030 |
0.28680 |
| 69.770 |
0.13370 |
0.08890 |
0.35750 |
| 67.100 |
0.06380 |
0.04240 |
0.41110 |
| 71.090 |
0.20630 |
0.51600 |
0.12770 |
| 72.910 |
0.13890 |
0.34760 |
0.23620 |
| 73.241 |
0.08640 |
0.21620 |
0.32070 |
| 72.090 |
0.04880 |
0.12200 |
0.38130 |
| 66.660 |
0.01980 |
0.04950 |
0.42800 |
| 63.980 |
0.25510 |
0.63820 |
0.06740 |
| 72.790 |
0.16910 |
0.42310 |
0.25750 |
| 73.630 |
0.11040 |
0.27610 |
0.38740 |
| 73.110 |
0.06610 |
0.16540 |
0.48530 |
| 69.940 |
0.03240 |
0.08110 |
0.55980 |
| 67.940 |
0.42840 |
0.28490 |
0.18100 |
| 70.210 |
0.27910 |
0.18560 |
0.33800 |
| 70.490 |
0.17090 |
0.11360 |
0.45190 |
| 69.130 |
0.09470 |
0.06300 |
0.53190 |
| 66.840 |
0.05840 |
0.03880 |
0.57010 |
| 69.380 |
0.21000 |
0.52530 |
0.20960 |
| 72.681 |
0.13770 |
0.34450 |
0.41010 |
| 72.830 |
0.08960 |
0.22420 |
0.54350 |
| 71.299 |
0.04950 |
0.12390 |
0.65470 |
| 62.020 |
0.05030 |
0.03340 |
0.12380 |
| 65.671 |
0.11430 |
0.07600 |
0.10940 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Goral M.; Oracz P.; Warycha S.: XI. The quaternary system cyclohexane + hexane + acetone + methanol at 313.15 K. Fluid Phase Equilib. 135 (1997) 51-61 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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