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 2579
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 3 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 332.80 |
0.90000 |
0.00000 |
0.87500 |
0.00000 |
| 334.05 |
0.80000 |
0.10000 |
0.80000 |
0.05500 |
| 334.05 |
0.70000 |
0.10000 |
0.74000 |
0.06000 |
| 334.55 |
0.60000 |
0.10000 |
0.69000 |
0.07000 |
| 335.70 |
0.50000 |
0.10000 |
0.64000 |
0.08500 |
| 336.95 |
0.40000 |
0.10000 |
0.57500 |
0.10000 |
| 338.55 |
0.30000 |
0.10000 |
0.47500 |
0.13000 |
| 340.75 |
0.20000 |
0.10000 |
0.34500 |
0.17000 |
| 335.20 |
0.70000 |
0.20000 |
0.73000 |
0.14000 |
| 335.35 |
0.60000 |
0.20000 |
0.65000 |
0.16000 |
| 336.10 |
0.50000 |
0.20000 |
0.57000 |
0.17500 |
| 337.05 |
0.40000 |
0.20000 |
0.49000 |
0.22000 |
| 338.30 |
0.30000 |
0.20000 |
0.39000 |
0.25000 |
| 339.65 |
0.20000 |
0.20000 |
0.27000 |
0.30000 |
| 336.15 |
0.60000 |
0.30000 |
0.61000 |
0.25500 |
| 336.25 |
0.50000 |
0.30000 |
0.51500 |
0.28500 |
| 336.70 |
0.40000 |
0.30000 |
0.44000 |
0.31500 |
| 337.45 |
0.30000 |
0.30000 |
0.33500 |
0.36000 |
| 336.35 |
0.50000 |
0.40000 |
0.46500 |
0.40500 |
| 336.50 |
0.30000 |
0.40000 |
0.29400 |
0.46000 |
| 336.25 |
0.40000 |
0.40000 |
0.37500 |
0.43000 |
| 336.65 |
0.20000 |
0.40000 |
0.20000 |
0.49500 |
| 334.55 |
0.30000 |
0.60000 |
0.20000 |
0.68000 |
| 334.20 |
0.20000 |
0.60000 |
0.13000 |
0.69500 |
| 333.85 |
0.10000 |
0.60000 |
0.06500 |
0.70500 |
| 331.60 |
0.10000 |
0.80000 |
0.07000 |
0.86500 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Morachevskii A.G.; Leontev N.P.: Liquid-Vapor Equilibrium in the Ternary System Acetone-Chloroform Ethanol. Russ.J.Phys.Chem. 34 (1960) 1114-1115 |
Vapor-Liquid Equilibrium Data Set 8511
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 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 334.16 |
0.10000 |
0.80000 |
0.06000 |
0.82500 |
| 334.20 |
0.10000 |
0.70000 |
0.06100 |
0.74900 |
| 335.44 |
0.20000 |
0.70000 |
0.14900 |
0.72900 |
| 334.74 |
0.10000 |
0.60000 |
0.07100 |
0.69100 |
| 335.63 |
0.20000 |
0.60000 |
0.16500 |
0.64500 |
| 336.65 |
0.30000 |
0.60000 |
0.26700 |
0.61600 |
| 335.65 |
0.10000 |
0.50000 |
0.08400 |
0.63700 |
| 336.24 |
0.20000 |
0.50000 |
0.18100 |
0.57700 |
| 336.43 |
0.30000 |
0.50000 |
0.28500 |
0.52000 |
| 336.55 |
0.40000 |
0.50000 |
0.41300 |
0.46700 |
| 337.06 |
0.10000 |
0.40000 |
0.10000 |
0.57100 |
| 337.10 |
0.20000 |
0.40000 |
0.20800 |
0.49700 |
| 336.85 |
0.30000 |
0.40000 |
0.31400 |
0.43100 |
| 336.45 |
0.40000 |
0.40000 |
0.43300 |
0.38400 |
| 335.95 |
0.50000 |
0.40000 |
0.55800 |
0.34000 |
| 338.70 |
0.10000 |
0.30000 |
0.13000 |
0.47500 |
| 338.45 |
0.20000 |
0.30000 |
0.25000 |
0.40000 |
| 337.54 |
0.30000 |
0.30000 |
0.35800 |
0.34400 |
| 336.55 |
0.40000 |
0.30000 |
0.46200 |
0.30000 |
| 335.72 |
0.50000 |
0.30000 |
0.57500 |
0.26500 |
| 334.15 |
0.60000 |
0.30000 |
0.68000 |
0.23300 |
| 340.93 |
0.10000 |
0.20000 |
0.16300 |
0.36200 |
| 339.78 |
0.20000 |
0.20000 |
0.30000 |
0.28500 |
| 338.13 |
0.30000 |
0.20000 |
0.40600 |
0.24600 |
| 336.75 |
0.40000 |
0.20000 |
0.50200 |
0.20700 |
| 335.56 |
0.50000 |
0.20000 |
0.59900 |
0.18100 |
| 334.43 |
0.60000 |
0.20000 |
0.70000 |
0.15800 |
| 333.72 |
0.70000 |
0.20000 |
0.79700 |
0.13200 |
| 343.55 |
0.10000 |
0.10000 |
0.21100 |
0.20900 |
| 341.00 |
0.20000 |
0.10000 |
0.35400 |
0.15600 |
| 338.88 |
0.30000 |
0.10000 |
0.46700 |
0.13000 |
| 337.03 |
0.40000 |
0.10000 |
0.56300 |
0.10700 |
| 335.40 |
0.50000 |
0.10000 |
0.63500 |
0.09500 |
| 334.15 |
0.60000 |
0.10000 |
0.72000 |
0.08000 |
| 332.86 |
0.70000 |
0.10000 |
0.80200 |
0.07100 |
| 331.95 |
0.80000 |
0.10000 |
0.87700 |
0.05700 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Susarev M.P.; Zapolskaya M.A.; Vinichenko I.G.: Liquid-Vapor Equilibrium in the System Acetone-Chloroform-Ethanol. Russ.J.Phys.Chem. 39 (1965) 1279-1282 |
Vapor-Liquid Equilibrium Data Set 8512
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 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 82.033 |
0.10000 |
0.80000 |
0.06500 |
0.81500 |
| 81.687 |
0.10000 |
0.70000 |
0.06300 |
0.75300 |
| 77.300 |
0.20000 |
0.70000 |
0.14600 |
0.74000 |
| 80.100 |
0.10000 |
0.60000 |
0.07100 |
0.70100 |
| 77.247 |
0.20000 |
0.60000 |
0.16500 |
0.65800 |
| 75.407 |
0.30000 |
0.60000 |
0.26500 |
0.62500 |
| 75.874 |
0.10000 |
0.50000 |
0.08200 |
0.65100 |
| 75.380 |
0.20000 |
0.50000 |
0.18200 |
0.59300 |
| 75.114 |
0.30000 |
0.50000 |
0.28700 |
0.53600 |
| 74.941 |
0.40000 |
0.50000 |
0.42000 |
0.47700 |
| 73.087 |
0.10000 |
0.40000 |
0.09800 |
0.59300 |
| 72.007 |
0.20000 |
0.40000 |
0.20700 |
0.51700 |
| 73.581 |
0.30000 |
0.40000 |
0.32400 |
0.44900 |
| 74.994 |
0.40000 |
0.40000 |
0.44000 |
0.39000 |
| 76.487 |
0.50000 |
0.40000 |
0.54800 |
0.35200 |
| 69.808 |
0.10000 |
0.30000 |
0.12200 |
0.50300 |
| 70.781 |
0.20000 |
0.30000 |
0.24600 |
0.42500 |
| 71.167 |
0.30000 |
0.30000 |
0.37400 |
0.35400 |
| 74.301 |
0.40000 |
0.30000 |
0.47400 |
0.30700 |
| 76.994 |
0.50000 |
0.30000 |
0.58100 |
0.26800 |
| 80.153 |
0.60000 |
0.30000 |
0.68500 |
0.22900 |
| 63.728 |
0.10000 |
0.20000 |
0.16300 |
0.37900 |
| 67.261 |
0.20000 |
0.20000 |
0.29800 |
0.29800 |
| 69.928 |
0.30000 |
0.20000 |
0.43100 |
0.25600 |
| 73.661 |
0.40000 |
0.20000 |
0.52500 |
0.21100 |
| 77.007 |
0.50000 |
0.20000 |
0.62000 |
0.17800 |
| 80.793 |
0.60000 |
0.20000 |
0.70800 |
0.15700 |
| 83.140 |
0.70000 |
0.20000 |
0.79800 |
0.13200 |
| 55.502 |
0.10000 |
0.10000 |
0.23300 |
0.20400 |
| 61.822 |
0.20000 |
0.10000 |
0.36400 |
0.16100 |
| 67.874 |
0.30000 |
0.10000 |
0.50400 |
0.12900 |
| 73.327 |
0.40000 |
0.10000 |
0.58800 |
0.10600 |
| 77.834 |
0.50000 |
0.10000 |
0.66200 |
0.09400 |
| 81.793 |
0.60000 |
0.10000 |
0.73500 |
0.08500 |
| 85.753 |
0.70000 |
0.10000 |
0.80700 |
0.07300 |
| 88.659 |
0.80000 |
0.10000 |
0.87800 |
0.05600 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Susarev M.P.; Zapolskaya M.A.; Vinichenko I.G.: Liquid-Vapor Equilibrium in the System Acetone-Chloroform-Ethanol. Russ.J.Phys.Chem. 39 (1965) 1279-1282 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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