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 1951
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
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] |
| 351.05 |
0.48300 |
0.25600 |
0.68500 |
0.27000 |
| 354.35 |
0.43400 |
0.22000 |
0.68100 |
0.25000 |
| 361.85 |
0.32600 |
0.17000 |
0.64900 |
0.23000 |
| 353.95 |
0.24400 |
0.50100 |
0.41500 |
0.53300 |
| 353.75 |
0.18400 |
0.60000 |
0.33100 |
0.63000 |
| 353.45 |
0.13700 |
0.69400 |
0.25500 |
0.71500 |
| 353.05 |
0.16400 |
0.65700 |
0.29600 |
0.67200 |
| 353.05 |
0.15100 |
0.68100 |
0.27500 |
0.69600 |
| 360.65 |
0.11200 |
0.52900 |
0.25100 |
0.66500 |
| 367.55 |
0.08500 |
0.41900 |
0.22500 |
0.63100 |
| 372.85 |
0.07400 |
0.33000 |
0.22100 |
0.57200 |
| 355.95 |
0.26300 |
0.40400 |
0.48300 |
0.44900 |
| 361.85 |
0.21000 |
0.33400 |
0.44800 |
0.43400 |
| 366.05 |
0.17800 |
0.28800 |
0.42600 |
0.42100 |
| 362.85 |
0.20300 |
0.32100 |
0.44700 |
0.42700 |
| 368.85 |
0.16000 |
0.26500 |
0.41000 |
0.41300 |
| 372.25 |
0.13700 |
0.23500 |
0.38600 |
0.40200 |
| 365.85 |
0.23400 |
0.19800 |
0.55100 |
0.29600 |
| 381.65 |
0.12300 |
0.11000 |
0.41300 |
0.23500 |
| 376.55 |
0.19800 |
0.06800 |
0.57500 |
0.13000 |
| 369.65 |
0.28500 |
0.06000 |
0.69100 |
0.10000 |
| 361.75 |
0.41300 |
0.04800 |
0.79200 |
0.06800 |
| 349.85 |
0.34400 |
0.51000 |
0.50600 |
0.47000 |
| 349.35 |
0.24900 |
0.63900 |
0.39600 |
0.58700 |
| 343.25 |
0.86200 |
0.09000 |
0.90400 |
0.09000 |
| 343.85 |
0.82100 |
0.11200 |
0.88000 |
0.11100 |
| 344.55 |
0.77700 |
0.13400 |
0.85500 |
0.13200 |
| 344.95 |
0.75300 |
0.14600 |
0.84200 |
0.14400 |
| 344.85 |
0.76200 |
0.14200 |
0.84500 |
0.14000 |
| 347.15 |
0.70400 |
0.12800 |
0.84000 |
0.13300 |
| 347.15 |
0.65400 |
0.18300 |
0.79100 |
0.18400 |
| 347.15 |
0.64700 |
0.19000 |
0.78300 |
0.19200 |
| 347.55 |
0.62400 |
0.19900 |
0.77000 |
0.20200 |
| 349.25 |
0.58400 |
0.18700 |
0.76200 |
0.19700 |
| 348.95 |
0.47100 |
0.33900 |
0.63500 |
0.33600 |
| 348.35 |
0.52700 |
0.29300 |
0.68100 |
0.29100 |
| 350.85 |
0.48200 |
0.26400 |
0.67800 |
0.27700 |
| 352.95 |
0.44900 |
0.24300 |
0.67400 |
0.26700 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Michishita T.; Arai Y.; Saito S.: Vapor-Liquid Equilibria of Hydrocarbons at Atmospheric Pressure. Kagaku Kogaku 35 (1971) 111 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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