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 33324
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 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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] |
| 335.16 |
0.16900 |
0.47100 |
0.20400 |
0.03500 |
| 335.68 |
0.13900 |
0.53100 |
0.19900 |
0.04100 |
| 337.06 |
0.13600 |
0.56200 |
0.19600 |
0.04200 |
| 342.85 |
0.11000 |
0.67900 |
0.18900 |
0.06100 |
| 342.78 |
0.23500 |
0.61500 |
0.24300 |
0.06800 |
| 345.90 |
0.21400 |
0.67700 |
0.25500 |
0.07900 |
| 353.40 |
0.17600 |
0.73900 |
0.32100 |
0.12600 |
| 358.44 |
0.21100 |
0.73700 |
0.43600 |
0.16500 |
| 358.58 |
0.19600 |
0.74700 |
0.42200 |
0.16500 |
| 364.09 |
0.16200 |
0.81300 |
0.50300 |
0.22300 |
| 353.27 |
0.36500 |
0.60400 |
0.42000 |
0.13400 |
| 342.51 |
0.17200 |
0.62300 |
0.22000 |
0.06500 |
| 342.59 |
0.12500 |
0.63400 |
0.18900 |
0.06900 |
| 338.33 |
0.06700 |
0.48700 |
0.16000 |
0.04600 |
| 343.65 |
0.07600 |
0.66600 |
0.14800 |
0.05900 |
| 340.45 |
0.05400 |
0.56500 |
0.12700 |
0.05300 |
| 342.79 |
0.05300 |
0.62300 |
0.13300 |
0.05600 |
| 348.90 |
0.03800 |
0.72300 |
0.10600 |
0.08400 |
| 352.25 |
0.03800 |
0.78400 |
0.10100 |
0.12300 |
| 355.08 |
0.03800 |
0.80900 |
0.09900 |
0.15900 |
| 358.83 |
0.04000 |
0.83600 |
0.11100 |
0.19700 |
| 363.46 |
0.03200 |
0.87600 |
0.10000 |
0.25700 |
| 367.29 |
0.03000 |
0.89000 |
0.10800 |
0.27900 |
| 371.50 |
0.03100 |
0.91200 |
0.11700 |
0.38200 |
| 374.26 |
0.03900 |
0.91600 |
0.16300 |
0.39500 |
| 382.48 |
0.04900 |
0.94400 |
0.28300 |
0.56500 |
| 371.94 |
0.17200 |
0.82300 |
0.57600 |
0.35100 |
| 374.22 |
0.14900 |
0.84800 |
0.56300 |
0.38500 |
| 378.51 |
0.10100 |
0.89700 |
0.51800 |
0.44400 |
| 359.87 |
0.09500 |
0.82700 |
0.24500 |
0.20500 |
| 355.07 |
0.08700 |
0.80500 |
0.19900 |
0.15400 |
| 353.94 |
0.08600 |
0.78800 |
0.18600 |
0.14500 |
| 344.55 |
0.10100 |
0.63000 |
0.16200 |
0.08100 |
| 348.57 |
0.09200 |
0.73300 |
0.17000 |
0.10600 |
| 347.90 |
0.13600 |
0.70800 |
0.21800 |
0.10000 |
| 349.27 |
0.19500 |
0.70700 |
0.28700 |
0.10700 |
| 351.21 |
0.24300 |
0.68300 |
0.33700 |
0.11000 |
| 348.35 |
0.34400 |
0.59400 |
0.33100 |
0.10100 |
| 347.88 |
0.33200 |
0.59100 |
0.32800 |
0.10200 |
| 345.11 |
0.30300 |
0.60600 |
0.28700 |
0.08400 |
| 350.58 |
0.30300 |
0.63900 |
0.35800 |
0.11800 |
| 354.67 |
0.29000 |
0.66100 |
0.42300 |
0.14000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Gornis V.; Font A.; Saquete M.D.; García-Cano J.: LLE, VLE and VLLE data for the water–n-butanol–n-hexane system at atmospheric pressure. Fluid Phase Equilib. 316 (2012) 135-140 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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