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 49
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 12.999 |
0.00000 |
| 17.505 |
0.10000 |
| 20.332 |
0.20000 |
| 22.305 |
0.30000 |
| 23.825 |
0.40000 |
| 25.105 |
0.50000 |
| 25.371 |
0.52230 |
| 26.278 |
0.60000 |
| 27.371 |
0.70000 |
| 27.571 |
0.73990 |
| 28.411 |
0.80000 |
| 29.371 |
0.90000 |
| 30.331 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Litvinov N.D.: Dampfdruck der Flüssigkeiten und binären flüssigen Mischungen. Zh.Fiz.Khim. 14 (1940) 782-788 |
Vapor-Liquid Equilibrium Data Set 50
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 20.012 |
0.00000 |
| 26.105 |
0.10000 |
| 30.158 |
0.20000 |
| 33.091 |
0.30000 |
| 35.410 |
0.40000 |
| 37.437 |
0.50000 |
| 37.824 |
0.52230 |
| 39.277 |
0.60000 |
| 41.010 |
0.70000 |
| 41.677 |
0.73990 |
| 42.676 |
0.80000 |
| 44.623 |
0.90000 |
| 45.943 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Litvinov N.D.: Dampfdruck der Flüssigkeiten und binären flüssigen Mischungen. Zh.Fiz.Khim. 14 (1940) 782-788 |
Vapor-Liquid Equilibrium Data Set 559
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 33.428 |
0.04700 |
0.14440 |
| 36.666 |
0.09630 |
0.25740 |
| 43.230 |
0.22070 |
0.44170 |
| 46.450 |
0.29360 |
0.52040 |
| 50.647 |
0.40110 |
0.61390 |
| 53.293 |
0.47590 |
0.66970 |
| 57.722 |
0.61250 |
0.76140 |
| 60.527 |
0.70450 |
0.82010 |
| 63.380 |
0.80810 |
0.88050 |
| 66.037 |
0.90840 |
0.94180 |
| 67.189 |
0.95290 |
0.96990 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Brown I.; Smith F.: VIII. The Systems Acetone + Benzene and Acetone + Carbon tetrachloride at 45°C. Aust.J.Chem. 10 (1957) 423-428 |
Diagrams
List of All References
| Source |
| Brown I.; Smith F.: VIII. The Systems Acetone + Benzene and Acetone + Carbon tetrachloride at 45°C. Aust.J.Chem. 10 (1957) 423-428 |
| Litvinov N.D.: Dampfdruck der Flüssigkeiten und binären flüssigen Mischungen. Zh.Fiz.Khim. 14 (1940) 782-788 |
Vapor-Liquid Equilibrium Data Overview
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