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 4802
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 |
3 |
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] |
x2 [mol/mol] |
333.43 |
0.66600 |
0.06500 |
334.77 |
0.49200 |
0.05500 |
335.96 |
0.36500 |
0.04700 |
337.57 |
0.26800 |
0.04200 |
340.00 |
0.19200 |
0.03700 |
343.03 |
0.13000 |
0.03400 |
347.57 |
0.07900 |
0.03100 |
353.04 |
0.03600 |
0.02900 |
335.59 |
0.59400 |
0.13300 |
337.37 |
0.42800 |
0.11200 |
339.11 |
0.30800 |
0.09700 |
341.92 |
0.21600 |
0.08500 |
345.25 |
0.14500 |
0.07600 |
349.71 |
0.08700 |
0.06800 |
357.20 |
0.04000 |
0.06200 |
338.38 |
0.51800 |
0.20300 |
340.15 |
0.36300 |
0.17000 |
343.05 |
0.25000 |
0.14700 |
346.48 |
0.16400 |
0.12900 |
351.26 |
0.09800 |
0.11500 |
357.43 |
0.04400 |
0.10400 |
341.31 |
0.43800 |
0.27800 |
344.15 |
0.29400 |
0.23100 |
348.79 |
0.18900 |
0.19800 |
352.04 |
0.11000 |
0.17400 |
358.01 |
0.04900 |
0.15700 |
344.86 |
0.35900 |
0.35200 |
348.50 |
0.22200 |
0.29300 |
353.05 |
0.12800 |
0.25200 |
358.12 |
0.05600 |
0.22000 |
348.55 |
0.27500 |
0.43000 |
353.46 |
0.15200 |
0.35800 |
358.40 |
0.06700 |
0.30500 |
353.87 |
0.18700 |
0.51200 |
359.45 |
0.07700 |
0.42500 |
361.06 |
0.09500 |
0.59800 |
(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 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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