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 34827
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 348.67 |
0.31600 |
0.57000 |
0.29200 |
0.09400 |
| 350.09 |
0.30100 |
0.57800 |
0.29400 |
0.11900 |
| 353.41 |
0.25200 |
0.65800 |
0.41400 |
0.12500 |
| 358.41 |
0.20900 |
0.71600 |
0.43300 |
0.16400 |
| 361.49 |
0.17700 |
0.75500 |
0.44000 |
0.19400 |
| 365.54 |
0.14200 |
0.81000 |
0.43000 |
0.23800 |
| 373.12 |
0.11000 |
0.84600 |
0.38700 |
0.36400 |
| 379.92 |
0.05900 |
0.92300 |
0.28300 |
0.56300 |
| 364.57 |
0.31900 |
0.66800 |
0.64100 |
0.23700 |
| 365.33 |
0.30800 |
0.67900 |
0.64500 |
0.24700 |
| 366.85 |
0.29600 |
0.69200 |
0.63600 |
0.26800 |
| 368.77 |
0.23600 |
0.75500 |
0.62600 |
0.30100 |
| 372.04 |
0.18400 |
0.81100 |
0.58800 |
0.36100 |
| 374.71 |
0.15000 |
0.84700 |
0.54700 |
0.41600 |
| 377.93 |
0.11400 |
0.88400 |
0.48000 |
0.49800 |
| 377.82 |
0.07900 |
0.90200 |
0.32800 |
0.53100 |
| 377.96 |
0.05600 |
0.91200 |
0.23200 |
0.54300 |
| 376.19 |
0.05700 |
0.89500 |
0.20400 |
0.48600 |
| 373.92 |
0.03500 |
0.89100 |
0.13400 |
0.43400 |
| 368.69 |
0.04600 |
0.85000 |
0.17000 |
0.33900 |
| 363.77 |
0.06700 |
0.79500 |
0.19600 |
0.26000 |
| 358.64 |
0.09600 |
0.73000 |
0.24400 |
0.19200 |
| 352.99 |
0.13900 |
0.64400 |
0.27500 |
0.12800 |
| 351.06 |
0.14400 |
0.63100 |
0.28500 |
0.10600 |
| 348.12 |
0.16100 |
0.54100 |
0.28000 |
0.08700 |
| 347.19 |
0.12900 |
0.51100 |
0.25600 |
0.08500 |
| 348.06 |
0.08600 |
0.50800 |
0.22600 |
0.09100 |
| 351.66 |
0.06300 |
0.59600 |
0.18100 |
0.11800 |
| 353.66 |
0.04500 |
0.62200 |
0.13800 |
0.13800 |
| 356.26 |
0.05100 |
0.67200 |
0.13800 |
0.16300 |
| 360.17 |
0.03500 |
0.73600 |
0.11500 |
0.19700 |
| 358.61 |
0.38400 |
0.57800 |
0.53700 |
0.17700 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Gomis V.; Font A.; Saquete M.D.; Garcia-Cano J.: Experimental Determination and Correlation. J.Chem.Eng.Data 58 (2013) 3320-3326 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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