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 1519
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O |
72.107 |
109-99-9 |
Tetrahydrofuran |
| 2 |
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] |
y1 [mol/mol] |
| 102.045 |
0.03200 |
0.69700 |
| 120.590 |
0.07150 |
0.74500 |
| 122.710 |
0.14100 |
0.74900 |
| 122.657 |
0.24100 |
0.75000 |
| 123.003 |
0.33500 |
0.75100 |
| 123.350 |
0.42900 |
0.75400 |
| 124.323 |
0.55800 |
0.75800 |
| 125.256 |
0.62500 |
0.76800 |
| 126.216 |
0.75400 |
0.79000 |
| 126.443 |
0.80000 |
0.80500 |
| 126.056 |
0.85400 |
0.83000 |
| 125.256 |
0.88600 |
0.85500 |
| 123.390 |
0.92800 |
0.89300 |
| 120.097 |
0.96600 |
0.94500 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Matous J.; Novak J.P.; Sobr J.; Pick J.: Phase Equilibria in the System Tetrahydrofuran (1) -Water (2). Collect.Czech.Chem.Commun. 37 (1972) 2653-2663 |
Vapor-Liquid Equilibrium Data Set 1520
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O |
72.107 |
109-99-9 |
Tetrahydrofuran |
| 2 |
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] |
y1 [mol/mol] |
| 40.423 |
0.02800 |
0.70000 |
| 47.969 |
0.03850 |
0.74500 |
| 51.116 |
0.04600 |
0.76700 |
| 56.062 |
0.07500 |
0.78100 |
| 58.715 |
0.11650 |
0.79700 |
| 59.382 |
0.18300 |
0.80000 |
| 59.595 |
0.22800 |
0.80200 |
| 59.702 |
0.26400 |
0.80000 |
| 59.915 |
0.35400 |
0.80200 |
| 60.142 |
0.44100 |
0.80300 |
| 60.462 |
0.53100 |
0.80500 |
| 60.822 |
0.61100 |
0.81000 |
| 61.302 |
0.69800 |
0.82000 |
| 61.782 |
0.76500 |
0.83200 |
| 61.968 |
0.79800 |
0.84000 |
| 62.048 |
0.86800 |
0.86500 |
| 61.902 |
0.88800 |
0.87050 |
| 61.608 |
0.92200 |
0.90100 |
| 60.848 |
0.95600 |
0.93600 |
| 59.995 |
0.97900 |
0.96500 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Matous J.; Novak J.P.; Sobr J.; Pick J.: Phase Equilibria in the System Tetrahydrofuran (1) -Water (2). Collect.Czech.Chem.Commun. 37 (1972) 2653-2663 |
Vapor-Liquid Equilibrium Data Set 2391
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O |
72.107 |
109-99-9 |
Tetrahydrofuran |
| 2 |
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] |
y1 [mol/mol] |
| 346.15 |
0.02000 |
0.65230 |
| 339.65 |
0.04000 |
0.73810 |
| 338.73 |
0.06000 |
0.75160 |
| 338.47 |
0.08000 |
0.75620 |
| 338.09 |
0.10000 |
0.75870 |
| 337.85 |
0.15000 |
0.76180 |
| 337.47 |
0.20000 |
0.76250 |
| 337.45 |
0.25000 |
0.76290 |
| 337.42 |
0.30000 |
0.76350 |
| 337.40 |
0.35000 |
0.76390 |
| 337.38 |
0.40000 |
0.76430 |
| 337.35 |
0.45000 |
0.76490 |
| 337.31 |
0.50000 |
0.76580 |
| 337.21 |
0.55000 |
0.76840 |
| 337.09 |
0.60000 |
0.77200 |
| 336.97 |
0.65000 |
0.77650 |
| 336.85 |
0.70000 |
0.78310 |
| 336.76 |
0.75000 |
0.79150 |
| 336.69 |
0.80000 |
0.80850 |
| 336.68 |
0.82000 |
0.81800 |
| 336.72 |
0.84000 |
0.82600 |
| 336.79 |
0.86000 |
0.83680 |
| 336.88 |
0.88000 |
0.84980 |
| 337.02 |
0.90000 |
0.86600 |
| 337.20 |
0.92000 |
0.88550 |
| 337.44 |
0.94000 |
0.90700 |
| 337.76 |
0.96000 |
0.93250 |
| 338.22 |
0.98000 |
0.96250 |
| 338.54 |
0.99000 |
0.98050 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Shnitko V.A.; Kogan V.B.: Liquid-Vapor Equilibrium in the Systems Tetrahydrofuran-Water and Tetrahydrofuran-Ethylene Glycol and a Method for Dehydration of Tetrahydrofuran. J.Appl.Chem.USSR 41 (1968) 1236-1242 |
Diagrams
List of All References
| Source |
| Matous J.; Novak J.P.; Sobr J.; Pick J.: Phase Equilibria in the System Tetrahydrofuran (1) -Water (2). Collect.Czech.Chem.Commun. 37 (1972) 2653-2663 |
| Shnitko V.A.; Kogan V.B.: Liquid-Vapor Equilibrium in the Systems Tetrahydrofuran-Water and Tetrahydrofuran-Ethylene Glycol and a Method for Dehydration of Tetrahydrofuran. J.Appl.Chem.USSR 41 (1968) 1236-1242 |
Vapor-Liquid Equilibrium Data Overview
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