Dortmund Data Bank
Excess Enthalpy 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.
Enthalpy of Mixing Data Set 15580
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
Search the DDB for all data of this mixture
Miscibility gap: Yes
Constant Value
| Temperature |
363.150 |
K |
| Pressure |
16.520 |
bar |
Data Table
| hE [J/mol] |
x1 [mol/mol] |
| 94.000 |
0.01570 |
| 191.000 |
0.03170 |
| 353.000 |
0.06470 |
| 393.000 |
0.09900 |
| 403.000 |
0.13470 |
| 404.000 |
0.17190 |
| 405.000 |
0.21070 |
| 405.000 |
0.25110 |
| 406.000 |
0.29340 |
| 407.000 |
0.33750 |
| 409.000 |
0.38380 |
| 407.000 |
0.43220 |
| 407.000 |
0.48300 |
| 407.000 |
0.53630 |
| 408.000 |
0.59240 |
| 408.000 |
0.65140 |
| 411.000 |
0.71360 |
| 411.000 |
0.77920 |
| 411.000 |
0.84860 |
| 413.000 |
0.92210 |
| 413.000 |
0.96050 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
| Source |
| Wittig R.; Lohmann J.; Joh R.; Horstmann S.; Gmehling J.: Vapor-Liquid Equilibria and Enthalpies of Mixing in a Temperature Range from 298.15 to 413.15 K for the Further Development of Modified UNIFAC (Dortmund). Ind.Eng.Chem.Res. 40 (2001) 5831-5838 |
Enthalpy of Mixing Data Set 15581
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
Search the DDB for all data of this mixture
Miscibility gap: Yes
Constant Value
| Temperature |
413.150 |
K |
| Pressure |
13.760 |
bar |
Data Table
| hE [J/mol] |
x1 [mol/mol] |
| 138.000 |
0.01570 |
| 280.000 |
0.03170 |
| 557.000 |
0.06470 |
| 823.000 |
0.09900 |
| 972.000 |
0.13470 |
| 991.000 |
0.17190 |
| 1006.000 |
0.21060 |
| 1022.000 |
0.25110 |
| 1035.000 |
0.29330 |
| 1050.000 |
0.33750 |
| 1085.000 |
0.43220 |
| 1107.000 |
0.48290 |
| 1129.000 |
0.53630 |
| 1151.000 |
0.59230 |
| 1178.000 |
0.65130 |
| 1200.000 |
0.71350 |
| 1231.000 |
0.77920 |
| 1256.000 |
0.84860 |
| 1288.000 |
0.92210 |
| 815.000 |
0.96040 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
| Source |
| Wittig R.; Lohmann J.; Joh R.; Horstmann S.; Gmehling J.: Vapor-Liquid Equilibria and Enthalpies of Mixing in a Temperature Range from 298.15 to 413.15 K for the Further Development of Modified UNIFAC (Dortmund). Ind.Eng.Chem.Res. 40 (2001) 5831-5838 |
Enthalpy of Mixing Data Set 21678
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
Search the DDB for all data of this mixture
Miscibility gap: No
Constant Value
Data Table
| hE [cal/mol] |
x1 [mol/mol] |
| 16.710 |
0.04100 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
| Source |
| Könnecke H.-G.; Steinert H.; Leibnitz E.: Über die Mischungswärmen binärer flüssiger Systeme am Beispiel Benzol/Glykole und Wasser/Glykole. Z.Phys.Chem.(Leipzig) 208 (1957) 147-156 |
Diagrams
List of All References
| Source |
| Könnecke H.-G.; Steinert H.; Leibnitz E.: Über die Mischungswärmen binärer flüssiger Systeme am Beispiel Benzol/Glykole und Wasser/Glykole. Z.Phys.Chem.(Leipzig) 208 (1957) 147-156 |
| Wittig R.; Lohmann J.; Joh R.; Horstmann S.; Gmehling J.: Vapor-Liquid Equilibria and Enthalpies of Mixing in a Temperature Range from 298.15 to 413.15 K for the Further Development of Modified UNIFAC (Dortmund). Ind.Eng.Chem.Res. 40 (2001) 5831-5838 |
Excess Enthalpy Data Overview
© DDBST GmbH
