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 4884
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C16H34 |
226.446 |
544-76-3 |
Hexadecane |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 73.674 |
0.29150 |
| 84.886 |
0.35800 |
| 86.406 |
0.36700 |
| 89.793 |
0.41080 |
| 93.632 |
0.45600 |
| 94.606 |
0.46020 |
| 96.539 |
0.49250 |
| 99.965 |
0.54400 |
| 115.177 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Messow U.; Doye U.; Kuntzsch S.; Kuchenbecker D.: V. Die Systeme Aceton/n-Decan, Aceton/n-Dodecan, Aceton/n-Tetradecan und Aceton/n-Hexadecan. Z.Phys.Chem.(Leipzig) 258 (1977) 90-96 |
Vapor-Liquid Equilibrium Data Set 23754
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C16H34 |
226.446 |
544-76-3 |
Hexadecane |
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Data Table
| P [kPa] |
T [K] |
x1 [mol/mol] |
| 2.9464 |
295.25 |
0.01810 |
| 3.640 |
295.25 |
0.02420 |
| 4.106 |
306.85 |
0.01680 |
| 3.933 |
306.85 |
0.01720 |
| 4.266 |
307.65 |
0.01950 |
| 5.040 |
314.75 |
0.01770 |
| 6.279 |
314.75 |
0.02290 |
| 9.053 |
332.95 |
0.01980 |
| 10.892 |
332.95 |
0.02480 |
(P - pressure, T - temperature, x - liquid mole fraction)
Reference
| Source |
| Pierotti G.J.; Deal C.H.; Derr E.L.: (Addendum included). Ind.Eng.Chem. 51 (1959) 95-102 |
Vapor-Liquid Equilibrium Data Set 23755
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C16H34 |
226.446 |
544-76-3 |
Hexadecane |
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Data Table
| P [kPa] |
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 13.786 |
362.55 |
0.01710 |
0.99600 |
| 17.559 |
362.55 |
0.02160 |
0.99600 |
| 14.172 |
366.75 |
0.01700 |
0.99500 |
| 13.319 |
366.75 |
0.01680 |
0.99500 |
(P - pressure, T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Pierotti G.J.; Deal C.H.; Derr E.L.: (Addendum included). Ind.Eng.Chem. 51 (1959) 95-102 |
Diagrams
List of All References
| Source |
| Messow U.; Doye U.; Kuntzsch S.; Kuchenbecker D.: V. Die Systeme Aceton/n-Decan, Aceton/n-Dodecan, Aceton/n-Tetradecan und Aceton/n-Hexadecan. Z.Phys.Chem.(Leipzig) 258 (1977) 90-96 |
| Pierotti G.J.; Deal C.H.; Derr E.L.: (Addendum included). Ind.Eng.Chem. 51 (1959) 95-102 |
Vapor-Liquid Equilibrium Data Overview
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