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 564
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 9.733 |
0.16000 |
0.91400 |
| 15.465 |
0.43500 |
0.96100 |
| 19.865 |
0.65000 |
0.97500 |
| 21.865 |
0.79000 |
0.98400 |
| 24.265 |
0.90500 |
0.98900 |
| 25.331 |
0.95100 |
0.99100 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Fordyce C.R.; Simonsen D.R.: Evaporation in Binary Solvent Mixtures. Ind.Eng.Chem. 41 (1949) 104-111 |
Vapor-Liquid Equilibrium Data Set 565
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 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] |
| 388.15 |
0.01000 |
0.10500 |
| 385.15 |
0.02500 |
0.22500 |
| 380.25 |
0.05000 |
0.40500 |
| 376.95 |
0.07000 |
0.47200 |
| 364.85 |
0.15400 |
0.69800 |
| 360.05 |
0.19800 |
0.75000 |
| 358.55 |
0.21500 |
0.77300 |
| 354.85 |
0.26500 |
0.80900 |
| 351.95 |
0.31200 |
0.83700 |
| 341.75 |
0.53500 |
0.93000 |
| 339.35 |
0.60700 |
0.94300 |
| 337.65 |
0.65900 |
0.95100 |
| 334.75 |
0.76300 |
0.97200 |
| 333.15 |
0.81900 |
0.97800 |
| 331.25 |
0.89700 |
0.98800 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Michalski H.; Michalowski S.; Serwinski M.; Strumillo C.: Vapour - Liquid Equilibria for the System Acetone - n-Butanol. Zesz.Nauk.Politech.Lodz.Chem. 10=36 (1961) 73-84 |
Vapor-Liquid Equilibrium Data Set 4801
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 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] |
| 374.50 |
0.12400 |
| 361.64 |
0.24200 |
| 353.15 |
0.35400 |
| 347.36 |
0.46000 |
| 343.18 |
0.56100 |
| 339.49 |
0.65700 |
| 336.47 |
0.74900 |
| 334.05 |
0.83600 |
| 331.83 |
0.92000 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Ernst R.C.; Litkenhous E.E.; Spanyer J.W.: The Physical Properties of the Ternary System Acetone-n-Butyl Alcohol-Water. J.Phys.Chem. 36 (1932) 842-854 |
Diagrams
List of All References
| Source |
| Fordyce C.R.; Simonsen D.R.: Evaporation in Binary Solvent Mixtures. Ind.Eng.Chem. 41 (1949) 104-111 |
| Michalski H.; Michalowski S.; Serwinski M.; Strumillo C.: Vapour - Liquid Equilibria for the System Acetone - n-Butanol. Zesz.Nauk.Politech.Lodz.Chem. 10=36 (1961) 73-84 |
| Ernst R.C.; Litkenhous E.E.; Spanyer J.W.: The Physical Properties of the Ternary System Acetone-n-Butyl Alcohol-Water. J.Phys.Chem. 36 (1932) 842-854 |
Vapor-Liquid Equilibrium Data Overview
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