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 2115
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 3 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 331.25 |
0.29200 |
0.36800 |
0.35700 |
0.33700 |
| 332.65 |
0.14600 |
0.43600 |
0.23500 |
0.41100 |
| 329.85 |
0.40000 |
0.18800 |
0.41900 |
0.14300 |
| 330.55 |
0.40300 |
0.42800 |
0.40600 |
0.44600 |
| 330.85 |
0.49500 |
0.26400 |
0.47500 |
0.26400 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Willock J.M.; van Winkle M.: Binary and Ternary Vapor-Liquid Equilibria of Methanol-Acetone-2,3-Dimethylbutane. J.Chem.Eng.Data 15 (1970) 281-286 |
Vapor-Liquid Equilibrium Data Set 2577
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 3 |
CH4O |
32.042 |
67-56-1 |
Methanol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 334.15 |
0.10000 |
0.10000 |
0.11500 |
0.17000 |
| 331.85 |
0.10000 |
0.20000 |
0.10000 |
0.31000 |
| 330.15 |
0.10000 |
0.30000 |
0.09500 |
0.42500 |
| 329.15 |
0.10000 |
0.40000 |
0.07800 |
0.49000 |
| 329.15 |
0.10000 |
0.50000 |
0.08700 |
0.53000 |
| 329.15 |
0.10000 |
0.60000 |
0.09000 |
0.57000 |
| 329.65 |
0.10000 |
0.70000 |
0.08000 |
0.64500 |
| 332.95 |
0.10000 |
0.80000 |
0.09000 |
0.77000 |
| 332.35 |
0.20000 |
0.10000 |
0.27000 |
0.13000 |
| 332.15 |
0.20000 |
0.20000 |
0.20000 |
0.25000 |
| 330.35 |
0.20000 |
0.30000 |
0.19000 |
0.35000 |
| 329.85 |
0.20000 |
0.40000 |
0.18000 |
0.42000 |
| 331.15 |
0.20000 |
0.50000 |
0.17000 |
0.49000 |
| 332.15 |
0.20000 |
0.60000 |
0.19000 |
0.58000 |
| 333.65 |
0.20000 |
0.70000 |
0.18000 |
0.68000 |
| 332.05 |
0.30000 |
0.10000 |
0.38000 |
0.11000 |
| 331.95 |
0.30000 |
0.20000 |
0.32000 |
0.21500 |
| 331.15 |
0.30000 |
0.30000 |
0.30000 |
0.29000 |
| 331.85 |
0.30000 |
0.40000 |
0.30000 |
0.37500 |
| 332.65 |
0.30000 |
0.50000 |
0.27000 |
0.47500 |
| 334.65 |
0.30000 |
0.60000 |
0.28600 |
0.58500 |
| 331.15 |
0.40000 |
0.10000 |
0.47500 |
0.11000 |
| 331.35 |
0.40000 |
0.20000 |
0.41000 |
0.19000 |
| 332.05 |
0.40000 |
0.30000 |
0.42000 |
0.26000 |
| 333.15 |
0.40000 |
0.40000 |
0.40000 |
0.36200 |
| 334.65 |
0.40000 |
0.50000 |
0.41000 |
0.46000 |
| 330.95 |
0.50000 |
0.10000 |
0.52000 |
0.09000 |
| 331.45 |
0.50000 |
0.20000 |
0.52500 |
0.16500 |
| 332.35 |
0.50000 |
0.30000 |
0.55000 |
0.23000 |
| 334.35 |
0.50000 |
0.40000 |
0.54500 |
0.33000 |
| 330.45 |
0.60000 |
0.10000 |
0.62000 |
0.08500 |
| 332.15 |
0.60000 |
0.20000 |
0.63500 |
0.15500 |
| 333.15 |
0.60000 |
0.30000 |
0.67500 |
0.19500 |
| 330.65 |
0.70000 |
0.10000 |
0.71000 |
0.08000 |
| 333.15 |
0.70000 |
0.20000 |
0.75500 |
0.13500 |
| 331.15 |
0.80000 |
0.10000 |
0.82000 |
0.07500 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Shishkin K.N.; Kotsyuba A.A.: Investigation in the area of rectification of binary and ternary azeotropic mixtures. III. Tr.Dnepropetr.Khim.Tekhnol.Inst. 4 (1955) 18-24 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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