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 547
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| x1 [mol/mol] |
y1 [mol/mol] |
| 0.00350 |
0.02050 |
| 0.00450 |
0.02750 |
| 0.01750 |
0.13150 |
| 0.05850 |
0.30500 |
| 0.06800 |
0.36150 |
| 0.09350 |
0.41100 |
| 0.16500 |
0.52000 |
| 0.21250 |
0.54550 |
| 0.24100 |
0.56750 |
| 0.36150 |
0.60600 |
| 0.47400 |
0.65050 |
| 0.49850 |
0.65550 |
| 0.58150 |
0.69700 |
| 0.64600 |
0.72900 |
| 0.65400 |
0.73100 |
| 0.72300 |
0.77600 |
| 0.79000 |
0.82000 |
| 0.83700 |
0.85200 |
| 0.87310 |
0.88170 |
| 0.88300 |
0.88850 |
| 0.88800 |
0.89300 |
| 0.89730 |
0.90120 |
| 0.94890 |
0.95020 |
| 0.97070 |
0.97150 |
| 0.98250 |
0.98350 |
(x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Beebe A.H.; Coulter K.E.; Lindsay R.A.; Baker E.M.: Equilibria in Ethanol-Water System at Pressures Less Than Atmospheric. Ind.Eng.Chem. Ind.Ed. 34 (1942) 1501-1504 |
Vapor-Liquid Equilibrium Data Set 548
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| x1 [mol/mol] |
y1 [mol/mol] |
| 0.01600 |
0.14600 |
| 0.03700 |
0.27550 |
| 0.06500 |
0.36500 |
| 0.09000 |
0.41250 |
| 0.15800 |
0.50150 |
| 0.20900 |
0.54550 |
| 0.23850 |
0.56500 |
| 0.35350 |
0.60450 |
| 0.47050 |
0.64450 |
| 0.49700 |
0.65400 |
| 0.58050 |
0.69250 |
| 0.65250 |
0.72600 |
| 0.70000 |
0.75500 |
| 0.72000 |
0.76850 |
| 0.78950 |
0.81520 |
| 0.84160 |
0.85020 |
| 0.87350 |
0.87900 |
| 0.89700 |
0.89900 |
| 0.94850 |
0.94660 |
| 0.96000 |
0.95800 |
| 0.97190 |
0.97000 |
| 0.98120 |
0.97980 |
(x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Beebe A.H.; Coulter K.E.; Lindsay R.A.; Baker E.M.: Equilibria in Ethanol-Water System at Pressures Less Than Atmospheric. Ind.Eng.Chem. Ind.Ed. 34 (1942) 1501-1504 |
Vapor-Liquid Equilibrium Data Set 549
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| x1 [mol/mol] |
y1 [mol/mol] |
| 0.01600 |
0.14700 |
| 0.03150 |
0.25050 |
| 0.06000 |
0.37650 |
| 0.08550 |
0.43000 |
| 0.14650 |
0.50050 |
| 0.20600 |
0.54150 |
| 0.23600 |
0.56000 |
| 0.34950 |
0.59450 |
| 0.46750 |
0.64100 |
| 0.48750 |
0.64250 |
| 0.58000 |
0.68900 |
| 0.65250 |
0.72500 |
| 0.70000 |
0.74950 |
| 0.71750 |
0.76800 |
| 0.78900 |
0.81110 |
| 0.84200 |
0.84880 |
| 0.87490 |
0.87680 |
| 0.89670 |
0.89730 |
| 0.94850 |
0.94400 |
| 0.97270 |
0.96920 |
(x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Beebe A.H.; Coulter K.E.; Lindsay R.A.; Baker E.M.: Equilibria in Ethanol-Water System at Pressures Less Than Atmospheric. Ind.Eng.Chem. Ind.Ed. 34 (1942) 1501-1504 |
Diagrams
List of All References
| Source |
| Beebe A.H.; Coulter K.E.; Lindsay R.A.; Baker E.M.: Equilibria in Ethanol-Water System at Pressures Less Than Atmospheric. Ind.Eng.Chem. Ind.Ed. 34 (1942) 1501-1504 |
Vapor-Liquid Equilibrium Data Overview
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