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 11510
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
| 404.55 |
0.07940 |
| 388.95 |
0.18330 |
| 378.35 |
0.28730 |
| 372.95 |
0.39100 |
| 369.18 |
0.49350 |
| 366.11 |
0.59650 |
| 363.38 |
0.69890 |
| 360.74 |
0.80000 |
| 358.29 |
0.89990 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Villa Rivera J.E.: Application a la Deshydratation par Distillation des Melanges d'Alcools de Synthese. Thesis (1983) |
Vapor-Liquid Equilibrium Data Set 11511
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
| 386.95 |
0.07900 |
| 369.55 |
0.18300 |
| 360.40 |
0.28710 |
| 355.83 |
0.39090 |
| 352.38 |
0.49340 |
| 349.65 |
0.59650 |
| 347.16 |
0.69880 |
| 344.90 |
0.80000 |
| 342.87 |
0.89990 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Villa Rivera J.E.: Application a la Deshydratation par Distillation des Melanges d'Alcools de Synthese. Thesis (1983) |
Vapor-Liquid Equilibrium Data Set 15087
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 426.15 |
0.04500 |
0.73300 |
| 413.15 |
0.07000 |
0.85500 |
| 401.15 |
0.11000 |
0.91200 |
| 387.15 |
0.15200 |
0.96000 |
| 380.15 |
0.19000 |
0.99200 |
| 375.15 |
0.26000 |
0.99400 |
| 371.15 |
0.40200 |
0.99950 |
| 363.15 |
0.65100 |
0.99700 |
| 355.75 |
0.96000 |
0.99900 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Liu F.; Huang F.; Zhang C.; Zhang C.: Mathematical Modelling and Identification in Extractive Distillation of Alcohol-Water with Glycol and Diethylene Glycol. Huadong-Huagong-Xueyuan-Xuebao 19 (1993) 254-262 |
Diagrams
List of All References
| Source |
| Villa Rivera J.E.: Application a la Deshydratation par Distillation des Melanges d'Alcools de Synthese. Thesis (1983) |
| Liu F.; Huang F.; Zhang C.; Zhang C.: Mathematical Modelling and Identification in Extractive Distillation of Alcohol-Water with Glycol and Diethylene Glycol. Huadong-Huagong-Xueyuan-Xuebao 19 (1993) 254-262 |
Vapor-Liquid Equilibrium Data Overview
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