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 4993
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 409.25 |
0.01100 |
0.06900 |
| 403.15 |
0.04200 |
0.22500 |
| 391.45 |
0.12300 |
0.48700 |
| 385.25 |
0.16500 |
0.58700 |
| 382.95 |
0.19200 |
0.62500 |
| 369.45 |
0.33900 |
0.78500 |
| 364.45 |
0.40900 |
0.83100 |
| 359.75 |
0.49700 |
0.86700 |
| 356.05 |
0.57800 |
0.89800 |
| 351.35 |
0.70100 |
0.94100 |
| 347.95 |
0.79700 |
0.96600 |
| 345.75 |
0.86800 |
0.97800 |
| 343.15 |
0.95300 |
0.99300 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Saito S.: Separation of Hydrocarbons. Asahi-Garasu-Kogyo-Gijutsu-Shoreikai-Kenkyu-Hokuku 15 (1969) 397-407 |
Vapor-Liquid Equilibrium Data Set 16373
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 2.6544 |
0.00000 |
| 5.440 |
0.05600 |
| 9.239 |
0.14330 |
| 11.848 |
0.20710 |
| 15.871 |
0.31550 |
| 17.503 |
0.36270 |
| 19.438 |
0.42510 |
| 22.362 |
0.52000 |
| 24.511 |
0.58610 |
| 26.278 |
0.64540 |
| 28.111 |
0.71070 |
| 28.678 |
0.72520 |
| 30.553 |
0.79040 |
| 33.031 |
0.87180 |
| 34.982 |
0.93290 |
| 37.250 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Goral M.: III. Binary Mixtures of Alkylbenzenes and n-Alkanes at 313.15 K. Fluid Phase Equilib. 102 (1994) 275-286 |
Vapor-Liquid Equilibrium Data Set 25809
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
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] |
| 409.35 |
0.00000 |
| 378.75 |
0.15880 |
| 361.81 |
0.43030 |
| 352.55 |
0.63380 |
| 347.25 |
0.77560 |
| 342.75 |
0.91220 |
| 340.25 |
1.00000 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Vittal Prasad T.E.; Prasad D.H.L.; Patanjali V.: Bubble Temperature Measurements on Seven Binary Mixtures Containing 1-4-Dimethylbenzene at 95.8 kPa. Chem.Eng.Commun. 192 (2005) 18-22 |
Diagrams
List of All References
| Source |
| Saito S.: Separation of Hydrocarbons. Asahi-Garasu-Kogyo-Gijutsu-Shoreikai-Kenkyu-Hokuku 15 (1969) 397-407 |
| Goral M.: III. Binary Mixtures of Alkylbenzenes and n-Alkanes at 313.15 K. Fluid Phase Equilib. 102 (1994) 275-286 |
| Vittal Prasad T.E.; Prasad D.H.L.; Patanjali V.: Bubble Temperature Measurements on Seven Binary Mixtures Containing 1-4-Dimethylbenzene at 95.8 kPa. Chem.Eng.Commun. 192 (2005) 18-22 |
Vapor-Liquid Equilibrium Data Overview
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