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 30763

Components

No. Formula Molar Mass CAS Registry Number Name
1 CHCl3 119.377 67-66-3 Chloroform
2 C4H8O 72.107 109-99-9 Tetrahydrofuran
3 C6H12 84.161 110-82-7 Cyclohexane
Search the DDB for all data of this mixture

Constant Value

Temperature 298.15 K

Data Table

x1 [mol/mol] x2 [mol/mol] y1 [mol/mol] y2 [mol/mol]
0.02560 0.04900 0.05750 0.11280
0.07430 0.04660 0.16050 0.08370
0.17430 0.04210 0.33230 0.04990
0.27550 0.03700 0.46610 0.03010
0.44040 0.02860 0.62020 0.01470
0.02470 0.10230 0.04190 0.21140
0.09950 0.09460 0.17390 0.14670
0.19690 0.08450 0.33090 0.09130
0.35010 0.06840 0.52280 0.04470
0.64580 0.03730 0.76290 0.01280
0.01850 0.20000 0.02110 0.35220
0.05420 0.19280 0.06510 0.31130
0.10140 0.18320 0.13090 0.26290
0.15660 0.17210 0.21440 0.21170
0.20800 0.16170 0.29210 0.17050
0.25390 0.15230 0.35350 0.13760
0.50210 0.10170 0.64580 0.04730
0.60480 0.08070 0.73210 0.03010
0.80010 0.04090 0.86950 0.01090
0.69250 0.06290 0.79560 0.02010
0.05310 0.38210 0.03840 0.50870
0.15090 0.34280 0.13560 0.41400
0.28690 0.28800 0.32120 0.27320
0.44990 0.22220 0.55170 0.14180
0.04450 0.48120 0.02420 0.59270
0.09880 0.45390 0.06340 0.55090
0.20700 0.39950 0.17680 0.44090
0.29650 0.35440 0.29880 0.34240
0.39840 0.30310 0.45240 0.23830
0.95070 0.02490 0.97420 0.00590
0.90630 0.04720 0.95020 0.01170
0.95080 0.02480 0.97470 0.00580
0.86680 0.06710 0.92840 0.01690
0.79580 0.10290 0.88150 0.03080
0.66040 0.17100 0.77200 0.07080
0.54770 0.22780 0.65050 0.12640
0.94010 0.04490 0.97680 0.01090
0.82720 0.12960 0.91880 0.04110
0.70180 0.22360 0.82020 0.10030
0.05030 0.71250 0.02070 0.76590
0.14940 0.63820 0.08140 0.70230
0.29750 0.52720 0.24160 0.55080
0.49900 0.37600 0.56080 0.28550
0.41630 0.18030 0.52700 0.12340
0.30550 0.39880 0.28690 0.40130
0.25390 0.50050 0.19540 0.53970
0.02550 0.94900 0.00820 0.96520
0.07550 0.84920 0.02790 0.89330
0.14960 0.70110 0.07570 0.76610
0.59650 0.25330 0.70380 0.14090
0.35930 0.55030 0.30620 0.57510
0.27220 0.65930 0.18180 0.73190
0.15870 0.80130 0.07710 0.87710
0.15810 0.80200 0.07370 0.87980
0.48700 0.48830 0.51550 0.44810
0.46140 0.46260 0.47910 0.41710
0.38280 0.38260 0.39220 0.34680
0.12720 0.19890 0.19890 0.18490
0.23450 0.28110 0.28110 0.25210

(x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Gianni P.; Lepori L.; Matteoli E.: Excess Gibbs energies and volumes of the ternary system chloroform + tetrahydrofuran + cyclohexane at 298.15 K. Fluid Phase Equilib. 297 (2010) 52-61

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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