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 28194
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 3 |
C4H8O |
72.107 |
109-99-9 |
Tetrahydrofuran |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 32.479 |
0.14750 |
0.75430 |
0.23090 |
0.61600 |
| 33.924 |
0.28550 |
0.59000 |
0.32460 |
0.50860 |
| 33.982 |
0.44990 |
0.43170 |
0.42040 |
0.43590 |
| 33.217 |
0.61100 |
0.27550 |
0.51440 |
0.34760 |
| 32.224 |
0.70500 |
0.18770 |
0.57900 |
0.28210 |
| 34.115 |
0.12820 |
0.66840 |
0.17100 |
0.52880 |
| 35.038 |
0.25510 |
0.51500 |
0.26400 |
0.44560 |
| 34.921 |
0.39930 |
0.37650 |
0.35590 |
0.37890 |
| 34.187 |
0.53910 |
0.23880 |
0.36450 |
0.24850 |
| 33.044 |
0.64610 |
0.16440 |
0.52070 |
0.24180 |
| 35.540 |
0.11260 |
0.57290 |
0.13030 |
0.45180 |
| 36.156 |
0.21870 |
0.43810 |
0.20880 |
0.38160 |
| 35.883 |
0.34150 |
0.32350 |
0.29060 |
0.32310 |
| 34.024 |
0.55940 |
0.14360 |
0.43760 |
0.20330 |
| 36.748 |
0.09610 |
0.48510 |
0.10210 |
0.38680 |
| 37.140 |
0.18350 |
0.36150 |
0.16550 |
0.31890 |
| 36.808 |
0.28600 |
0.26640 |
0.23200 |
0.26710 |
| 36.022 |
0.39260 |
0.16680 |
0.30040 |
0.19920 |
| 35.060 |
0.46660 |
0.12010 |
0.35710 |
0.16170 |
| 37.850 |
0.07910 |
0.39440 |
0.07510 |
0.32480 |
| 37.993 |
0.15230 |
0.28960 |
0.12750 |
0.26310 |
| 37.609 |
0.23130 |
0.21340 |
0.18260 |
0.21460 |
| 36.830 |
0.31240 |
0.13690 |
0.23940 |
0.15700 |
| 36.061 |
0.37910 |
0.09560 |
0.28120 |
0.12340 |
| 38.652 |
0.06440 |
0.31210 |
0.05600 |
0.26730 |
| 38.573 |
0.12070 |
0.23190 |
0.09690 |
0.21460 |
| 38.213 |
0.18810 |
0.16690 |
0.14040 |
0.17100 |
| 37.528 |
0.25310 |
0.10680 |
0.18520 |
0.12300 |
| 36.905 |
0.30140 |
0.07370 |
0.22020 |
0.09220 |
| 39.257 |
0.05130 |
0.24480 |
0.04200 |
0.21750 |
| 39.050 |
0.09790 |
0.18400 |
0.07610 |
0.17650 |
| 39.350 |
0.09200 |
0.07840 |
0.06700 |
0.08490 |
| 38.122 |
0.19980 |
0.08140 |
0.14650 |
0.09290 |
| 37.620 |
0.24340 |
0.05450 |
0.17780 |
0.06740 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Wu H.S.; Sandler S.I.: Vapor-Liquid Equilibria of Tetrahydrofuran Systems. J.Chem.Eng.Data 33 (1988) 157-162 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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