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 9756
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 2.648 |
0.00000 |
0.00000 |
| 9.842 |
0.06340 |
0.74370 |
| 13.768 |
0.10820 |
0.82610 |
| 18.398 |
0.16850 |
0.87620 |
| 22.602 |
0.23380 |
0.90470 |
| 25.847 |
0.29110 |
0.92070 |
| 28.680 |
0.34840 |
0.93250 |
| 31.424 |
0.40540 |
0.94170 |
| 33.971 |
0.46520 |
0.94970 |
| 39.030 |
0.58650 |
0.96270 |
| 46.604 |
0.70230 |
0.97310 |
| 46.111 |
0.76580 |
0.97850 |
| 48.576 |
0.82570 |
0.98360 |
| 51.049 |
0.88340 |
0.98860 |
| 53.645 |
0.94100 |
0.99400 |
| 56.603 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kolasinska G.; Goral M.; Giza J.: Vapour-Liquid Equilibria and Excess Gibbs Free Energy in Binary Systems of Acetone with Aliphatic and Aromatic Hydrocarbons at 313.15 K. Z.Phys.Chem.(Leipzig) 263 (1982) 151-160 |
Vapor-Liquid Equilibrium Data Set 13827
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 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] |
y1 [mol/mol] |
| 9.900 |
0.04730 |
0.62170 |
| 19.000 |
0.14270 |
0.85000 |
| 29.200 |
0.29430 |
0.91480 |
| 40.700 |
0.57350 |
0.95430 |
| 50.300 |
0.86800 |
0.98440 |
| 53.500 |
0.94860 |
0.98510 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Leu A.D.; Chen C.J.; Robinson D.B.: Vapor-Liquid Equilibrium in Selected Binary Systems. AIChE Symp.Ser. 85 (1989) 11-16 |
Vapor-Liquid Equilibrium Data Set 13828
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 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] |
y1 [mol/mol] |
| 33.600 |
0.03270 |
0.45350 |
| 75.400 |
0.14310 |
0.76400 |
| 144.700 |
0.55490 |
0.93420 |
| 171.101 |
0.72420 |
0.95670 |
| 188.101 |
0.87160 |
0.97940 |
| 205.400 |
0.97120 |
0.99430 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Leu A.D.; Chen C.J.; Robinson D.B.: Vapor-Liquid Equilibrium in Selected Binary Systems. AIChE Symp.Ser. 85 (1989) 11-16 |
Diagrams
List of All References
| Source |
| Kolasinska G.; Goral M.; Giza J.: Vapour-Liquid Equilibria and Excess Gibbs Free Energy in Binary Systems of Acetone with Aliphatic and Aromatic Hydrocarbons at 313.15 K. Z.Phys.Chem.(Leipzig) 263 (1982) 151-160 |
| Leu A.D.; Chen C.J.; Robinson D.B.: Vapor-Liquid Equilibrium in Selected Binary Systems. AIChE Symp.Ser. 85 (1989) 11-16 |
Vapor-Liquid Equilibrium Data Overview
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