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 16330
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 3 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
| 37.270 |
1.00000 |
0.00000 |
| 35.453 |
0.00000 |
1.00000 |
| 56.603 |
0.00000 |
0.00000 |
| 68.700 |
0.09370 |
0.10620 |
| 71.939 |
0.16540 |
0.09780 |
| 73.595 |
0.24730 |
0.08820 |
| 74.185 |
0.33250 |
0.07820 |
| 74.250 |
0.41260 |
0.06880 |
| 68.962 |
0.08390 |
0.18270 |
| 72.955 |
0.16330 |
0.16680 |
| 74.685 |
0.25110 |
0.14930 |
| 75.215 |
0.50130 |
0.09940 |
| 74.735 |
0.58040 |
0.08370 |
| 69.540 |
0.08420 |
0.25510 |
| 73.831 |
0.16710 |
0.23200 |
| 75.915 |
0.32800 |
0.18720 |
| 76.035 |
0.41520 |
0.16290 |
| 69.960 |
0.08490 |
0.32390 |
| 75.714 |
0.24930 |
0.26570 |
| 76.227 |
0.33230 |
0.23630 |
| 76.114 |
0.50180 |
0.17630 |
| 75.699 |
0.58700 |
0.14620 |
| 73.634 |
0.74790 |
0.08920 |
| 70.156 |
0.08440 |
0.38920 |
| 74.385 |
0.16040 |
0.35690 |
| 75.864 |
0.24830 |
0.31960 |
| 76.327 |
0.41190 |
0.25000 |
| 73.283 |
0.17140 |
0.14230 |
| 76.227 |
0.33300 |
0.32380 |
| 76.003 |
0.50220 |
0.24170 |
| 74.929 |
0.66770 |
0.16130 |
| 71.443 |
0.83370 |
0.08070 |
| 70.217 |
0.08460 |
0.51390 |
| 74.437 |
0.16660 |
0.46790 |
| 75.696 |
0.25150 |
0.42020 |
| 75.903 |
0.41850 |
0.32650 |
| 70.993 |
0.09700 |
0.58460 |
| 75.200 |
0.24950 |
0.48590 |
| 75.375 |
0.33140 |
0.43280 |
| 74.988 |
0.43350 |
0.32790 |
| 74.582 |
0.58850 |
0.26640 |
| 73.115 |
0.74630 |
0.16420 |
| 69.504 |
0.08500 |
0.66170 |
| 73.646 |
0.17010 |
0.60020 |
| 74.625 |
0.33260 |
0.48270 |
| 74.497 |
0.39720 |
0.43590 |
| 68.760 |
0.08480 |
0.73710 |
| 72.698 |
0.16550 |
0.67210 |
| 73.443 |
0.24810 |
0.60560 |
| 73.139 |
0.49910 |
0.40350 |
| 72.782 |
0.57840 |
0.33960 |
| 72.311 |
0.66360 |
0.27090 |
| 66.797 |
0.07960 |
0.81550 |
| 71.367 |
0.16690 |
0.73810 |
| 72.033 |
0.25220 |
0.66260 |
| 72.022 |
0.33370 |
0.59030 |
| 71.905 |
0.41650 |
0.51700 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Oracz P.; Warycha S.: VII: The ternary system hexane-methanol-acetone at 313.15 K. Fluid Phase Equilib. 108 (1995) 199-211 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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