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 2586
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 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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] |
| 334.72 |
0.10100 |
0.80000 |
0.07000 |
0.79500 |
| 335.04 |
0.20100 |
0.70000 |
0.17300 |
0.67100 |
| 333.99 |
0.10100 |
0.70100 |
0.08000 |
0.67800 |
| 335.24 |
0.30100 |
0.60000 |
0.29100 |
0.54200 |
| 334.06 |
0.20100 |
0.60000 |
0.18900 |
0.54200 |
| 333.81 |
0.10100 |
0.60000 |
0.09500 |
0.58500 |
| 334.14 |
0.40000 |
0.50200 |
0.42000 |
0.40500 |
| 333.37 |
0.30000 |
0.50000 |
0.31500 |
0.40100 |
| 333.30 |
0.20000 |
0.50100 |
0.21800 |
0.44000 |
| 333.74 |
0.10000 |
0.50000 |
0.13300 |
0.48600 |
| 333.31 |
0.49900 |
0.40200 |
0.53000 |
0.29400 |
| 331.70 |
0.40000 |
0.40100 |
0.42900 |
0.28200 |
| 332.00 |
0.30000 |
0.40000 |
0.34700 |
0.30300 |
| 332.55 |
0.19700 |
0.40000 |
0.26300 |
0.33800 |
| 333.66 |
0.10000 |
0.40000 |
0.13500 |
0.40300 |
| 330.97 |
0.60000 |
0.30000 |
0.63200 |
0.19000 |
| 330.26 |
0.50000 |
0.30000 |
0.53000 |
0.17900 |
| 329.77 |
0.40000 |
0.30100 |
0.46000 |
0.19000 |
| 330.46 |
0.30000 |
0.30000 |
0.39500 |
0.21500 |
| 331.61 |
0.19900 |
0.30100 |
0.32600 |
0.23600 |
| 333.48 |
0.09900 |
0.30000 |
0.17400 |
0.30400 |
| 329.25 |
0.70000 |
0.20100 |
0.71600 |
0.10600 |
| 327.75 |
0.60000 |
0.20000 |
0.60100 |
0.09900 |
| 327.37 |
0.50000 |
0.20000 |
0.56000 |
0.09500 |
| 327.69 |
0.39900 |
0.20200 |
0.51000 |
0.10200 |
| 328.05 |
0.29900 |
0.20100 |
0.45400 |
0.11600 |
| 330.28 |
0.19900 |
0.20000 |
0.37200 |
0.15100 |
| 333.80 |
0.09800 |
0.20000 |
0.20500 |
0.21600 |
| 327.01 |
0.80100 |
0.10000 |
0.77100 |
0.04700 |
| 325.65 |
0.70100 |
0.10100 |
0.66400 |
0.03900 |
| 325.05 |
0.60000 |
0.10000 |
0.61100 |
0.04000 |
| 325.16 |
0.49900 |
0.10000 |
0.57600 |
0.04300 |
| 325.61 |
0.40000 |
0.10000 |
0.54000 |
0.05200 |
| 326.78 |
0.29800 |
0.10000 |
0.48800 |
0.06100 |
| 328.65 |
0.19900 |
0.10000 |
0.41800 |
0.08100 |
| 332.33 |
0.09600 |
0.10000 |
0.27500 |
0.09000 |
| 333.94 |
0.06500 |
0.60000 |
0.06800 |
0.59900 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kudryavtseva L.S.; Susarev M.P.: Liquid-Vapor Equilibrium in the System Acetone-Chloroform-Hexane at Temperatures of 35,45,55° and a Pressure of 760mm Hg. J.Appl.Chem.USSR 36 (1963) 1654-1659 |
Vapor-Liquid Equilibrium Data Set 2587
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 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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] |
| 38.264 |
0.10900 |
0.79900 |
0.06000 |
0.79800 |
| 37.344 |
0.20700 |
0.70000 |
0.15800 |
0.67900 |
| 39.557 |
0.11000 |
0.70400 |
0.06700 |
0.69800 |
| 36.744 |
0.30500 |
0.60100 |
0.27600 |
0.54500 |
| 39.383 |
0.20400 |
0.60300 |
0.17500 |
0.54800 |
| 40.477 |
0.10700 |
0.60000 |
0.08300 |
0.58300 |
| 38.530 |
0.39900 |
0.51400 |
0.40900 |
0.41000 |
| 39.970 |
0.30100 |
0.50200 |
0.31000 |
0.40600 |
| 40.143 |
0.20000 |
0.50400 |
0.20900 |
0.43700 |
| 40.183 |
0.09800 |
0.50200 |
0.10500 |
0.49200 |
| 39.503 |
0.49500 |
0.41100 |
0.53500 |
0.28000 |
| 42.676 |
0.39900 |
0.40600 |
0.42500 |
0.27800 |
| 41.957 |
0.29700 |
0.40300 |
0.34200 |
0.29900 |
| 41.823 |
0.19000 |
0.40400 |
0.24900 |
0.34000 |
| 40.677 |
0.09700 |
0.40000 |
0.12500 |
0.40800 |
| 43.756 |
0.60000 |
0.30300 |
0.63900 |
0.18100 |
| 45.423 |
0.49800 |
0.30500 |
0.54100 |
0.17300 |
| 45.903 |
0.40000 |
0.30400 |
0.46200 |
0.18400 |
| 45.103 |
0.29700 |
0.30200 |
0.38600 |
0.21100 |
| 43.010 |
0.19400 |
0.30400 |
0.30000 |
0.24700 |
| 40.103 |
0.09400 |
0.29900 |
0.17400 |
0.30000 |
| 47.209 |
0.69700 |
0.20800 |
0.70900 |
0.10400 |
| 50.209 |
0.59900 |
0.20300 |
0.62300 |
0.09000 |
| 49.823 |
0.49700 |
0.20400 |
0.56100 |
0.09900 |
| 49.956 |
0.39600 |
0.20800 |
0.49600 |
0.11400 |
| 48.076 |
0.29000 |
0.20700 |
0.43500 |
0.12700 |
| 44.623 |
0.19300 |
0.20200 |
0.35200 |
0.16300 |
| 40.223 |
0.08600 |
0.19700 |
0.20300 |
0.21900 |
| 51.089 |
0.80700 |
0.10400 |
0.75200 |
0.04400 |
| 53.556 |
0.71000 |
0.10700 |
0.66900 |
0.04300 |
| 55.182 |
0.59900 |
0.10300 |
0.62100 |
0.04200 |
| 54.569 |
0.49100 |
0.10200 |
0.59500 |
0.03700 |
| 54.102 |
0.39600 |
0.10300 |
0.54400 |
0.04300 |
| 51.916 |
0.28300 |
0.10200 |
0.49100 |
0.05300 |
| 48.209 |
0.19300 |
0.10000 |
0.41000 |
0.07000 |
| 42.783 |
0.08700 |
0.10000 |
0.26700 |
0.08900 |
| 40.063 |
0.06500 |
0.60000 |
0.06000 |
0.60000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kudryavtseva L.S.; Susarev M.P.: Liquid-Vapor Equilibrium in the System Acetone-Chloroform-Hexane at Temperatures of 35,45,55° and a Pressure of 760mm Hg. J.Appl.Chem.USSR 36 (1963) 1654-1659 |
Vapor-Liquid Equilibrium Data Set 2588
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 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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] |
| 56.849 |
0.10300 |
0.80000 |
0.06200 |
0.80600 |
| 55.769 |
0.20500 |
0.70000 |
0.15700 |
0.67800 |
| 60.395 |
0.10700 |
0.70300 |
0.07100 |
0.69200 |
| 54.955 |
0.30400 |
0.60100 |
0.27900 |
0.54500 |
| 58.155 |
0.20300 |
0.60200 |
0.17900 |
0.54800 |
| 59.648 |
0.10500 |
0.60000 |
0.09200 |
0.58300 |
| 57.795 |
0.39900 |
0.51000 |
0.41400 |
0.40800 |
| 59.235 |
0.30100 |
0.50100 |
0.30600 |
0.40500 |
| 59.635 |
0.20000 |
0.50300 |
0.21200 |
0.44200 |
| 56.209 |
0.09800 |
0.50200 |
0.10500 |
0.49500 |
| 60.488 |
0.49600 |
0.40800 |
0.52600 |
0.28800 |
| 62.608 |
0.40000 |
0.40400 |
0.43400 |
0.27600 |
| 62.008 |
0.29800 |
0.40200 |
0.34800 |
0.29900 |
| 61.262 |
0.19300 |
0.40200 |
0.25100 |
0.34500 |
| 59.915 |
0.09800 |
0.40000 |
0.13200 |
0.40600 |
| 64.155 |
0.60000 |
0.30200 |
0.62700 |
0.18300 |
| 66.355 |
0.49900 |
0.30300 |
0.53000 |
0.18600 |
| 66.875 |
0.40000 |
0.30300 |
0.46000 |
0.19300 |
| 66.408 |
0.29800 |
0.30100 |
0.40200 |
0.21500 |
| 63.475 |
0.19600 |
0.30200 |
0.29000 |
0.25500 |
| 59.222 |
0.09600 |
0.29900 |
0.17000 |
0.31000 |
| 69.328 |
0.69800 |
0.20600 |
0.71000 |
0.09900 |
| 72.447 |
0.59900 |
0.20200 |
0.61800 |
0.09300 |
| 72.327 |
0.49800 |
0.20200 |
0.55900 |
0.09900 |
| 71.287 |
0.39700 |
0.20600 |
0.51000 |
0.10600 |
| 70.834 |
0.29300 |
0.20500 |
0.43000 |
0.12800 |
| 66.635 |
0.19500 |
0.20100 |
0.34800 |
0.15600 |
| 58.995 |
0.09000 |
0.19800 |
0.20000 |
0.21900 |
| 73.967 |
0.80500 |
0.10300 |
0.75500 |
0.04000 |
| 77.580 |
0.70700 |
0.10500 |
0.67000 |
0.03700 |
| 80.380 |
0.59900 |
0.10200 |
0.62000 |
0.03600 |
| 79.327 |
0.49400 |
0.10100 |
0.58700 |
0.03900 |
| 78.914 |
0.39700 |
0.10200 |
0.55200 |
0.04200 |
| 75.434 |
0.28800 |
0.10100 |
0.48700 |
0.05400 |
| 69.888 |
0.19500 |
0.10000 |
0.41100 |
0.06900 |
| 62.142 |
0.09000 |
0.10000 |
0.26100 |
0.09600 |
| 59.182 |
0.06500 |
0.60000 |
0.06500 |
0.60000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kudryavtseva L.S.; Susarev M.P.: Liquid-Vapor Equilibrium in the System Acetone-Chloroform-Hexane at Temperatures of 35,45,55° and a Pressure of 760mm Hg. J.Appl.Chem.USSR 36 (1963) 1654-1659 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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