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 2552
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 349.25 |
0.24400 |
0.00420 |
0.50300 |
0.13800 |
| 348.90 |
0.24500 |
0.00500 |
0.47000 |
0.15200 |
| 348.15 |
0.24800 |
0.00620 |
0.44900 |
0.19100 |
| 347.15 |
0.24950 |
0.00730 |
0.42500 |
0.22700 |
| 346.40 |
0.25000 |
0.00850 |
0.40700 |
0.27500 |
| 345.90 |
0.25000 |
0.00970 |
0.38200 |
0.30100 |
| 345.40 |
0.25000 |
0.01100 |
0.36500 |
0.33500 |
| 344.90 |
0.25100 |
0.01260 |
0.34800 |
0.37800 |
| 344.40 |
0.25100 |
0.01400 |
0.32800 |
0.41000 |
| 343.40 |
0.25100 |
0.01570 |
0.31200 |
0.42400 |
| 343.70 |
0.27000 |
0.01800 |
0.35400 |
0.36600 |
| 343.40 |
0.27050 |
0.01950 |
0.33600 |
0.40300 |
| 342.90 |
0.27080 |
0.02120 |
0.32400 |
0.42700 |
| 342.40 |
0.27080 |
0.02320 |
0.29400 |
0.45800 |
| 340.40 |
0.27150 |
0.03220 |
0.25800 |
0.53000 |
| 339.90 |
0.27150 |
0.03430 |
0.25800 |
0.53000 |
| 341.65 |
0.27200 |
0.02700 |
0.29200 |
0.47700 |
| 340.90 |
0.27200 |
0.03050 |
0.27900 |
0.50100 |
| 339.15 |
0.38540 |
0.53900 |
0.33100 |
0.53700 |
| 339.20 |
0.38700 |
0.54000 |
0.33400 |
0.53700 |
| 339.25 |
0.38800 |
0.54000 |
0.33700 |
0.53700 |
| 339.30 |
0.39100 |
0.54100 |
0.34300 |
0.53700 |
| 339.35 |
0.39400 |
0.54100 |
0.34600 |
0.53750 |
| 339.35 |
0.39500 |
0.54200 |
0.34700 |
0.53700 |
| 339.40 |
0.39700 |
0.54150 |
0.34950 |
0.53700 |
| 343.80 |
0.45640 |
0.04160 |
0.40600 |
0.35300 |
| 344.90 |
0.45800 |
0.03420 |
0.43000 |
0.31900 |
| 349.15 |
0.46610 |
0.01390 |
0.54750 |
0.13550 |
| 349.15 |
0.46650 |
0.01350 |
0.55000 |
0.12350 |
| 348.15 |
0.46750 |
0.01980 |
0.49200 |
0.20300 |
| 348.90 |
0.46760 |
0.01540 |
0.52900 |
0.13800 |
| 348.65 |
0.46760 |
0.01740 |
0.49900 |
0.18350 |
| 348.75 |
0.86470 |
0.03170 |
0.76950 |
0.12600 |
| 349.00 |
0.86640 |
0.02960 |
0.77600 |
0.11750 |
| 349.15 |
0.86950 |
0.02650 |
0.78650 |
0.10550 |
| 349.40 |
0.87400 |
0.02400 |
0.79600 |
0.09600 |
| 349.65 |
0.87580 |
0.02220 |
0.80550 |
0.08750 |
| 349.65 |
0.87700 |
0.02000 |
0.81200 |
0.08100 |
| 349.75 |
0.87800 |
0.01800 |
0.82000 |
0.07200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Norman W.S.: The Dehydration of Ethanol by Azeotropic Distillation. Trans.Inst.Chem.Engr. 23 (1945) 66-75 |
Vapor-Liquid Equilibrium Data Set 7234
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 25.598 |
0.98200 |
0.01400 |
0.74500 |
0.09200 |
| 28.264 |
0.89900 |
0.08000 |
0.69200 |
0.17900 |
| 28.798 |
0.81600 |
0.14500 |
0.66000 |
0.20000 |
| 29.198 |
0.74600 |
0.19700 |
0.65200 |
0.20800 |
| 28.931 |
0.64900 |
0.25500 |
0.64400 |
0.21600 |
| 28.531 |
0.50800 |
0.32000 |
0.64000 |
0.22000 |
| 25.598 |
0.00100 |
0.05600 |
0.74500 |
0.09200 |
| 28.264 |
0.00300 |
0.15400 |
0.69200 |
0.17900 |
| 28.798 |
0.01500 |
0.24100 |
0.66000 |
0.20000 |
| 29.198 |
0.03300 |
0.29800 |
0.65200 |
0.20800 |
| 28.931 |
0.06400 |
0.34800 |
0.64400 |
0.21600 |
| 28.531 |
0.12400 |
0.38600 |
0.64000 |
0.22000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Morachevskii A.G.; Belousov V.P.: Untersuchung der dreiphasigen Gleichgewicht im System Benzol-Ethanol-Wasser. Vestn.Leningr.Univ.Fiz.Khim. (1958) 117-125 |
Vapor-Liquid Equilibrium Data Set 7235
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 39.730 |
0.97900 |
0.01700 |
0.73200 |
0.09600 |
| 44.796 |
0.88900 |
0.08600 |
0.63600 |
0.19300 |
| 45.863 |
0.80100 |
0.15600 |
0.64500 |
0.20500 |
| 46.130 |
0.72700 |
0.21300 |
0.63000 |
0.21500 |
| 45.863 |
0.61900 |
0.27000 |
0.63500 |
0.22000 |
| 39.730 |
0.00100 |
0.05100 |
0.73200 |
0.09600 |
| 44.796 |
0.00300 |
0.14000 |
0.63600 |
0.19300 |
| 45.863 |
0.01200 |
0.21700 |
0.64500 |
0.20500 |
| 46.130 |
0.02700 |
0.27000 |
0.63000 |
0.21500 |
| 45.863 |
0.05300 |
0.32000 |
0.63500 |
0.22000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Morachevskii A.G.; Belousov V.P.: Untersuchung der dreiphasigen Gleichgewicht im System Benzol-Ethanol-Wasser. Vestn.Leningr.Univ.Fiz.Khim. (1958) 117-125 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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