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 11564

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H12 84.161 110-82-7 Cyclohexane
2 CH4O 32.042 67-56-1 Methanol
3 C6H14 86.177 110-54-3 Hexane
Search the DDB for all data of this mixture

Constant Value

Temperature 293.15 K

Data Table

P [kPa] x1 [mol/mol] x2 [mol/mol]
23.065 0.76270 0.05750
23.509 0.71780 0.11300
23.625 0.68320 0.15570
23.651 0.65260 0.19350
23.666 0.21200 0.73800
23.661 0.16510 0.79600
23.635 0.13440 0.83390
23.410 0.10320 0.87110
21.794 0.05470 0.93160
24.239 0.59530 0.08250
24.550 0.54520 0.15970
24.614 0.51900 0.20010
24.667 0.16690 0.74270
24.678 0.12930 0.80070
24.658 0.12170 0.81290
24.542 0.09920 0.84710
24.315 0.08460 0.87000
22.695 0.04590 0.92940
25.378 0.09820 0.81280
25.079 0.07050 0.86560
23.483 0.03830 0.92690
25.011 0.45500 0.07950
25.358 0.43130 0.12740
25.451 0.41440 0.16170
25.451 0.11920 0.75890
25.565 0.10050 0.79670
25.003 0.05730 0.88410
25.851 0.31860 0.09380
26.105 0.30720 0.12620
26.171 0.29400 0.16380
26.334 0.07230 0.79440
26.375 0.06410 0.81570
26.017 0.04530 0.86980
24.195 0.02420 0.93040
24.131 0.02460 0.93130
26.424 0.19220 0.07970
26.803 0.18170 0.12970
26.859 0.17930 0.14120
26.879 0.03140 0.84960
26.758 0.02590 0.87070
24.854 0.01380 0.93130

(P - pressure, x - liquid mole fraction)

Reference

Source
Goral M.; Oracz P.; Warycha S.: XIV. The ternary system cyclohexane-methanol-hexane at 293.15 K. Fluid Phase Equilib. 169 (2000) 85-99


Vapor-Liquid Equilibrium Data Set 11565

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 CH4O 32.042 67-56-1 Methanol
Search the DDB for all data of this mixture

Constant Value

Temperature 303.15 K

Data Table

P [kPa] x1 [mol/mol] x2 [mol/mol]
35.090 0.77400 0.19280
36.917 0.75080 0.18700
37.597 0.72370 0.18300
38.122 0.66930 0.16670
38.230 0.20180 0.05030
38.214 0.17710 0.04410
38.121 0.15020 0.03740
37.565 0.10650 0.02660
34.901 0.05510 0.01370
35.597 0.63550 0.33900
37.490 0.61610 0.32870
38.570 0.59630 0.31810
39.130 0.56950 0.30380
39.423 0.53870 0.28740
39.497 0.51610 0.27530
39.503 0.51320 0.27380
39.615 0.16250 0.08730
39.562 0.14390 0.07680
39.493 0.12350 0.06630
38.831 0.08420 0.04520
35.600 0.04150 0.02230
36.464 0.48070 0.49200
39.170 0.46120 0.47210
40.210 0.44200 0.45240
40.597 0.42630 0.43630
40.858 0.38600 0.39500
40.958 0.13190 0.13500
40.934 0.11590 0.11860
32.004 0.01540 0.01580
40.558 0.09780 0.08870
39.922 0.06790 0.06160
37.170 0.03790 0.03440
37.864 0.34240 0.63080
40.357 0.33040 0.60880
41.063 0.32020 0.59000
41.623 0.30640 0.56460
41.890 0.29080 0.53570
42.009 0.27800 0.51220
42.049 0.26150 0.48180
42.130 0.09210 0.16960
42.002 0.06420 0.12040
41.463 0.04500 0.08430
38.237 0.02350 0.04400
40.131 0.19670 0.76340
41.650 0.19110 0.74160
42.596 0.18030 0.71030
42.663 0.17650 0.68510
43.106 0.16980 0.65880
43.190 0.15910 0.61730
43.296 0.05700 0.22110
43.263 0.04930 0.19150
43.207 0.03910 0.15600
42.423 0.02590 0.10320
39.410 0.01380 0.05510

(P - pressure, x - liquid mole fraction)

Reference

Source
Goral M.; Oracz P.; Warycha S.: XIII. The Ternary System Cyclohexane-Methanol-Hexane at 303.15 K. Fluid Phase Equilib. 152 (1998) 109-120


Vapor-Liquid Equilibrium Data Set 11566

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 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]
24.625 1.00000 0.00000
37.270 0.00000 1.00000
35.453 0.00000 0.00000
58.609 0.69390 0.17300
59.379 0.62780 0.15660
59.490 0.57740 0.14400
59.500 0.52150 0.13000
59.518 0.27990 0.06980
59.474 0.20020 0.04990
59.108 0.14610 0.03640
58.022 0.10350 0.02580
54.377 0.05620 0.01400
59.675 0.59150 0.31760
60.483 0.56240 0.30200
61.195 0.52140 0.28000
61.338 0.48680 0.26140
61.439 0.32540 0.17480
61.446 0.29020 0.15590
61.454 0.26030 0.13980
61.382 0.16160 0.08680
61.122 0.12340 0.06630
59.982 0.08490 0.04560
55.903 0.04580 0.02460
62.078 0.45200 0.40990
62.755 0.41830 0.37930
62.848 0.39640 0.35950
63.024 0.23060 0.20920
63.039 0.21200 0.19230
63.024 0.18850 0.17100
62.963 0.13160 0.11930
62.684 0.09850 0.08930
61.515 0.06780 0.06140
57.249 0.03670 0.03330
62.435 0.32110 0.60240
64.261 0.29920 0.56130
64.755 0.27670 0.51910
65.007 0.26100 0.48970
65.161 0.13890 0.26060
65.163 0.12190 0.22860
65.156 0.11480 0.21530
65.117 0.08520 0.15990
64.836 0.06700 0.12560
63.661 0.04560 0.08560
59.008 0.02420 0.04530
63.268 0.18630 0.74230
65.061 0.18030 0.71830
65.756 0.17330 0.69050
66.495 0.16020 0.63850
66.636 0.15180 0.60490
66.801 0.07010 0.27920
66.801 0.06430 0.25640
66.801 0.06080 0.24230
65.155 0.02600 0.10360
60.475 0.01410 0.05630

(P - pressure, x - liquid mole fraction)

Reference

Source
Goral M.; Oracz P.; Warycha S.: IX. The ternary system cyclohexane-methanol-hexane at 313.15 K. Fluid Phase Equilib. 129 (1997) 223-233

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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