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 14897
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
| 46.088 |
0.08660 |
0.10120 |
| 52.940 |
0.15720 |
0.09340 |
| 57.497 |
0.24570 |
0.08360 |
| 59.810 |
0.32110 |
0.07520 |
| 61.760 |
0.42480 |
0.06370 |
| 54.777 |
0.16990 |
0.16880 |
| 58.603 |
0.25360 |
0.15170 |
| 63.563 |
0.50110 |
0.10140 |
| 64.293 |
0.58010 |
0.08540 |
| 64.763 |
0.66840 |
0.06740 |
| 47.832 |
0.08790 |
0.25220 |
| 55.238 |
0.16650 |
0.23050 |
| 61.660 |
0.33460 |
0.18400 |
| 63.251 |
0.41760 |
0.16100 |
| 49.380 |
0.09410 |
0.32490 |
| 60.176 |
0.25190 |
0.26830 |
| 62.614 |
0.33790 |
0.23740 |
| 65.112 |
0.50280 |
0.17830 |
| 65.905 |
0.60420 |
0.14190 |
| 66.108 |
0.75400 |
0.08820 |
| 48.487 |
0.08290 |
0.39530 |
| 56.130 |
0.15800 |
0.36290 |
| 60.804 |
0.25000 |
0.32330 |
| 64.799 |
0.42020 |
0.24990 |
| 57.310 |
0.16520 |
0.42090 |
| 64.032 |
0.33810 |
0.33370 |
| 66.467 |
0.49950 |
0.25240 |
| 67.424 |
0.66760 |
0.16760 |
| 66.280 |
0.83420 |
0.08360 |
| 51.236 |
0.09310 |
0.50810 |
| 57.617 |
0.16150 |
0.46980 |
| 62.044 |
0.24880 |
0.42090 |
| 66.033 |
0.41950 |
0.32530 |
| 52.890 |
0.09960 |
0.58130 |
| 67.894 |
0.50210 |
0.32140 |
| 68.481 |
0.58270 |
0.26940 |
| 68.377 |
0.75390 |
0.15890 |
| 68.364 |
0.75390 |
0.15890 |
| 53.176 |
0.09560 |
0.66370 |
| 58.722 |
0.15460 |
0.62030 |
| 66.227 |
0.33920 |
0.48490 |
| 67.604 |
0.41660 |
0.42810 |
| 54.181 |
0.09850 |
0.71930 |
| 60.806 |
0.17550 |
0.65790 |
| 64.997 |
0.26920 |
0.58310 |
| 69.110 |
0.49470 |
0.40100 |
| 69.672 |
0.58020 |
0.33500 |
| 69.870 |
0.66640 |
0.26620 |
| 55.907 |
0.10610 |
0.79330 |
| 60.368 |
0.15900 |
0.74640 |
| 65.184 |
0.25010 |
0.66560 |
| 67.562 |
0.33210 |
0.59280 |
| 69.233 |
0.43000 |
0.50590 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Goral M.; Oracz P.; Warycha S.: VI. The Ternary System Acetone-Hexane-Cyclohexane at 313.15 K. Fluid Phase Equilib. 81 (1992) 261-272 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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