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 6748
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
387.85 |
0.05250 |
0.18200 |
386.25 |
0.08800 |
0.27500 |
385.35 |
0.10500 |
0.31500 |
381.95 |
0.17500 |
0.45500 |
380.75 |
0.19100 |
0.49900 |
378.85 |
0.23900 |
0.55900 |
376.45 |
0.29300 |
0.61100 |
372.35 |
0.37500 |
0.69500 |
370.85 |
0.42600 |
0.74100 |
367.95 |
0.49800 |
0.79900 |
365.35 |
0.57300 |
0.83900 |
362.05 |
0.68900 |
0.89600 |
360.25 |
0.76100 |
0.92300 |
357.45 |
0.88500 |
0.96700 |
356.35 |
0.94600 |
0.98200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Morozov A.V.; Sarkisov A.G.; Turovskii V.B.; Ilyaskin V.I.: . Viniti (1978) 1-7 |
Vapor-Liquid Equilibrium Data Set 11486
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
383.75 |
0.12050 |
378.25 |
0.23570 |
373.85 |
0.34590 |
370.15 |
0.44820 |
366.52 |
0.55240 |
363.77 |
0.64930 |
361.30 |
0.74120 |
359.08 |
0.83150 |
357.05 |
0.91750 |
(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 11487
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
T [K] |
x1 [mol/mol] |
366.73 |
0.12050 |
361.43 |
0.23570 |
357.27 |
0.34590 |
353.73 |
0.44820 |
350.72 |
0.55210 |
348.13 |
0.64930 |
345.75 |
0.74120 |
343.78 |
0.83150 |
341.86 |
0.91750 |
(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) |
Diagrams
List of All References
Source |
Morozov A.V.; Sarkisov A.G.; Turovskii V.B.; Ilyaskin V.I.: . Viniti (1978) 1-7 |
Villa Rivera J.E.: Application a la Deshydratation par Distillation des Melanges d'Alcools de Synthese. Thesis (1983) |
Vapor-Liquid Equilibrium Data Overview
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