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

Temperature 313.15 K

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

Source

Vapor-Liquid Equilibrium Data Overview


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