Dortmund Data Bank
Solid-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.
Solid-Liquid Equilibrium Data Set 2972
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CO2 |
44.010 |
124-38-9 |
Carbon dioxide |
| 2 |
C16H34 |
226.446 |
544-76-3 |
Hexadecane |
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Data Table
| T [K] |
P [bar] |
xL1 [mol/mol] |
| 280.25 |
157.0 |
0.98882 |
| 286.75 |
498.0 |
0.98882 |
| 286.95 |
507.0 |
0.98882 |
| 289.85 |
654.0 |
0.98882 |
| 295.75 |
938.0 |
0.98882 |
| 300.75 |
1190.0 |
0.98882 |
| 304.75 |
1395.0 |
0.98882 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
| Source |
| Schneider G.; Alwani Z.; Heim W.; Horvath E.; Franck E.U.: CO2 mit n-Octan, n-Undecan, n-Tridecan und n-Hexadecan. Chem.Ing.Tech. CIT 39 (1967) 649-656 |
Solid-Liquid Equilibrium Data Set 2973
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CO2 |
44.010 |
124-38-9 |
Carbon dioxide |
| 2 |
C16H34 |
226.446 |
544-76-3 |
Hexadecane |
Search the DDB for all data of this mixture
Data Table
| T [K] |
P [bar] |
xL1 [mol/mol] |
| 284.25 |
243.0 |
0.98382 |
| 287.35 |
410.0 |
0.98382 |
| 290.85 |
590.0 |
0.98382 |
| 293.55 |
720.0 |
0.98382 |
| 296.05 |
863.0 |
0.98382 |
| 299.05 |
1015.0 |
0.98382 |
| 306.85 |
1419.0 |
0.98382 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
| Source |
| Schneider G.; Alwani Z.; Heim W.; Horvath E.; Franck E.U.: CO2 mit n-Octan, n-Undecan, n-Tridecan und n-Hexadecan. Chem.Ing.Tech. CIT 39 (1967) 649-656 |
Solid-Liquid Equilibrium Data Set 2977
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CO2 |
44.010 |
124-38-9 |
Carbon dioxide |
| 2 |
C16H34 |
226.446 |
544-76-3 |
Hexadecane |
Search the DDB for all data of this mixture
Data Table
| T [K] |
P [bar] |
xL1 [mol/mol] |
| 287.15 |
273.0 |
0.64146 |
| 296.15 |
761.0 |
0.64146 |
| 303.45 |
1135.0 |
0.64146 |
| 309.75 |
1463.0 |
0.64146 |
| 292.45 |
517.0 |
0.64146 |
| 308.45 |
1372.0 |
0.64146 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
| Source |
| Schneider G.; Alwani Z.; Heim W.; Horvath E.; Franck E.U.: CO2 mit n-Octan, n-Undecan, n-Tridecan und n-Hexadecan. Chem.Ing.Tech. CIT 39 (1967) 649-656 |
Diagrams
Solid-Liquid Equilibrium Data Overview
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