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 6781
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O |
72.107 |
109-99-9 |
Tetrahydrofuran |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 12.586 |
0.00000 |
| 13.039 |
0.06740 |
| 13.492 |
0.15590 |
| 14.052 |
0.23650 |
| 14.465 |
0.30530 |
| 15.079 |
0.36470 |
| 15.599 |
0.42930 |
| 16.079 |
0.48350 |
| 16.585 |
0.55120 |
| 17.105 |
0.59830 |
| 17.852 |
0.67030 |
| 18.545 |
0.73710 |
| 19.438 |
0.81250 |
| 20.172 |
0.88370 |
| 21.025 |
0.95450 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Deshpande D.D.; Oswal S.L.: 1. Excess Gibbs Free Energies and Excess Volumes. J.Chem.Thermodyn. 7 (1975) 155-159 |
Vapor-Liquid Equilibrium Data Set 6782
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O |
72.107 |
109-99-9 |
Tetrahydrofuran |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 24.478 |
0.00000 |
| 25.025 |
0.06740 |
| 25.891 |
0.15590 |
| 26.864 |
0.23650 |
| 27.771 |
0.30530 |
| 28.731 |
0.36470 |
| 29.638 |
0.42930 |
| 30.597 |
0.48350 |
| 31.624 |
0.55120 |
| 32.411 |
0.59830 |
| 33.877 |
0.67030 |
| 34.890 |
0.73710 |
| 36.517 |
0.81250 |
| 37.850 |
0.88370 |
| 39.370 |
0.95450 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Deshpande D.D.; Oswal S.L.: 1. Excess Gibbs Free Energies and Excess Volumes. J.Chem.Thermodyn. 7 (1975) 155-159 |
Vapor-Liquid Equilibrium Data Set 8429
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O |
72.107 |
109-99-9 |
Tetrahydrofuran |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 16.025 |
0.00000 |
0.00000 |
| 16.345 |
0.05000 |
0.06800 |
| 16.839 |
0.12500 |
0.16500 |
| 17.599 |
0.22800 |
0.30300 |
| 18.398 |
0.32700 |
0.42300 |
| 19.265 |
0.42300 |
0.53800 |
| 19.998 |
0.49500 |
0.61400 |
| 20.398 |
0.53000 |
0.65700 |
| 20.625 |
0.55000 |
0.67500 |
| 21.572 |
0.62000 |
0.74200 |
| 22.038 |
0.65500 |
0.77200 |
| 23.398 |
0.75000 |
0.84800 |
| 25.318 |
0.88800 |
0.93600 |
| 26.331 |
0.95000 |
0.97400 |
| 27.011 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Geier K.; Bittrich H.-J.: Zur Thermodynamik der Flüssig-Dampf-Gleichgewichte der binären Systeme n-Hexan-Benzol, Cyclohexan-Benzol und Tetrahydrofuran mit n-Hexan, Cyclohexan, Benzol und Dimethylformamid. Z.Phys.Chem.(Leipzig) 260 (1979) 705-718 |
Diagrams
List of All References
| Source |
| Deshpande D.D.; Oswal S.L.: 1. Excess Gibbs Free Energies and Excess Volumes. J.Chem.Thermodyn. 7 (1975) 155-159 |
| Geier K.; Bittrich H.-J.: Zur Thermodynamik der Flüssig-Dampf-Gleichgewichte der binären Systeme n-Hexan-Benzol, Cyclohexan-Benzol und Tetrahydrofuran mit n-Hexan, Cyclohexan, Benzol und Dimethylformamid. Z.Phys.Chem.(Leipzig) 260 (1979) 705-718 |
Vapor-Liquid Equilibrium Data Overview
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