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 3862
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 327.48 |
0.12200 |
0.12200 |
0.24400 |
0.20000 |
| 325.83 |
0.24900 |
0.12400 |
0.36900 |
0.15400 |
| 324.27 |
0.37400 |
0.12500 |
0.46900 |
0.10300 |
| 323.70 |
0.50000 |
0.12500 |
0.52200 |
0.09000 |
| 325.18 |
0.62700 |
0.12500 |
0.65500 |
0.10900 |
| 325.18 |
0.75200 |
0.12500 |
0.65500 |
0.10900 |
| 327.76 |
0.12200 |
0.25000 |
0.21000 |
0.24300 |
| 325.93 |
0.24900 |
0.25100 |
0.33300 |
0.19200 |
| 324.98 |
0.37400 |
0.25200 |
0.41700 |
0.15500 |
| 324.91 |
0.50000 |
0.25200 |
0.48500 |
0.15800 |
| 326.18 |
0.62500 |
0.25300 |
0.60600 |
0.13000 |
| 328.07 |
0.12200 |
0.37800 |
0.20200 |
0.26800 |
| 326.52 |
0.24800 |
0.37900 |
0.32000 |
0.21800 |
| 326.06 |
0.37400 |
0.37900 |
0.41800 |
0.19900 |
| 327.23 |
0.50000 |
0.38000 |
0.52400 |
0.18000 |
| 328.75 |
0.12400 |
0.50500 |
0.19000 |
0.28600 |
| 327.73 |
0.24800 |
0.50500 |
0.31000 |
0.26700 |
| 328.73 |
0.37400 |
0.50600 |
0.44600 |
0.23700 |
| 330.13 |
0.12300 |
0.63200 |
0.18600 |
0.32200 |
| 331.23 |
0.24800 |
0.63200 |
0.33700 |
0.32000 |
| 333.61 |
0.12300 |
0.76000 |
0.21000 |
0.38300 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Vinichenko I.G.; Susarev M.P.: Investigation and Calculation of Liquid-Vapor Equilibrium in the System acetone-Ethanol-n-Hexane. J.Appl.Chem.USSR 39 (1966) 1475-1478 |
Vapor-Liquid Equilibrium Data Set 3863
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 103.965 |
0.12500 |
0.12400 |
0.24100 |
0.20100 |
| 110.911 |
0.25000 |
0.12500 |
0.36500 |
0.15700 |
| 115.684 |
0.37500 |
0.12500 |
0.46700 |
0.10700 |
| 117.830 |
0.50000 |
0.12500 |
0.52500 |
0.09000 |
| 117.164 |
0.62600 |
0.12500 |
0.58400 |
0.08200 |
| 111.937 |
0.75100 |
0.12500 |
0.66500 |
0.08500 |
| 102.672 |
0.12400 |
0.25000 |
0.21600 |
0.23700 |
| 109.178 |
0.25000 |
0.25000 |
0.33400 |
0.19200 |
| 113.071 |
0.37500 |
0.25000 |
0.42300 |
0.15400 |
| 113.444 |
0.50000 |
0.25100 |
0.49000 |
0.15500 |
| 108.498 |
0.62500 |
0.25100 |
0.60500 |
0.12700 |
| 101.752 |
0.12400 |
0.37600 |
0.20400 |
0.27300 |
| 105.645 |
0.25000 |
0.37500 |
0.31800 |
0.22000 |
| 108.964 |
0.37500 |
0.37600 |
0.41300 |
0.19800 |
| 104.698 |
0.50000 |
0.37600 |
0.51500 |
0.19000 |
| 99.165 |
0.12400 |
0.50100 |
0.19500 |
0.28000 |
| 103.058 |
0.25000 |
0.50100 |
0.31600 |
0.25300 |
| 99.818 |
0.37500 |
0.50200 |
0.44200 |
0.23500 |
| 95.112 |
0.12500 |
0.62700 |
0.19500 |
0.31000 |
| 92.219 |
0.24900 |
0.62800 |
0.34700 |
0.30000 |
| 84.820 |
0.12400 |
0.75300 |
0.21600 |
0.36300 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Vinichenko I.G.; Susarev M.P.: Investigation and Calculation of Liquid-Vapor Equilibrium in the System acetone-Ethanol-n-Hexane. J.Appl.Chem.USSR 39 (1966) 1475-1478 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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