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 18034
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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] |
| 353.24 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 337.70 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
| 329.26 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
| 331.14 |
0.02300 |
0.51100 |
0.02300 |
0.58400 |
| 333.60 |
0.02400 |
0.90400 |
0.04100 |
0.78400 |
| 332.27 |
0.06000 |
0.83100 |
0.09100 |
0.70300 |
| 335.04 |
0.06600 |
0.10300 |
0.09100 |
0.41900 |
| 333.28 |
0.06600 |
0.87600 |
0.11300 |
0.75500 |
| 330.87 |
0.09400 |
0.62300 |
0.10800 |
0.58500 |
| 332.54 |
0.11800 |
0.21000 |
0.13200 |
0.45600 |
| 330.73 |
0.13600 |
0.53300 |
0.14800 |
0.54300 |
| 333.95 |
0.14600 |
0.13300 |
0.18200 |
0.38700 |
| 331.20 |
0.14900 |
0.72700 |
0.19900 |
0.61600 |
| 330.65 |
0.15400 |
0.58400 |
0.17400 |
0.55300 |
| 330.60 |
0.17500 |
0.50800 |
0.19100 |
0.52100 |
| 330.71 |
0.19100 |
0.43400 |
0.20300 |
0.49400 |
| 330.45 |
0.20100 |
0.54600 |
0.22500 |
0.52400 |
| 331.65 |
0.20900 |
0.25700 |
0.22500 |
0.42700 |
| 331.36 |
0.21400 |
0.73500 |
0.30400 |
0.61200 |
| 330.72 |
0.21800 |
0.66800 |
0.27800 |
0.56900 |
| 332.96 |
0.21900 |
0.16400 |
0.25500 |
0.36800 |
| 330.35 |
0.22900 |
0.56900 |
0.26400 |
0.52200 |
| 333.23 |
0.25000 |
0.14200 |
0.29600 |
0.33300 |
| 330.34 |
0.25400 |
0.45900 |
0.27200 |
0.47700 |
| 334.78 |
0.27400 |
0.08500 |
0.35700 |
0.24900 |
| 330.18 |
0.27400 |
0.55500 |
0.31400 |
0.50300 |
| 330.34 |
0.27500 |
0.61900 |
0.33700 |
0.53200 |
| 330.13 |
0.29700 |
0.45700 |
0.32100 |
0.46100 |
| 330.67 |
0.31000 |
0.31600 |
0.32300 |
0.40700 |
| 331.71 |
0.32000 |
0.20400 |
0.34800 |
0.34500 |
| 330.04 |
0.32300 |
0.57800 |
0.38600 |
0.49900 |
| 329.98 |
0.32700 |
0.46800 |
0.35500 |
0.45600 |
| 329.82 |
0.35000 |
0.49900 |
0.38900 |
0.46000 |
| 334.41 |
0.35100 |
0.07700 |
0.44400 |
0.20100 |
| 329.92 |
0.36100 |
0.41500 |
0.38300 |
0.42500 |
| 330.05 |
0.37200 |
0.37800 |
0.39100 |
0.40500 |
| 329.97 |
0.39800 |
0.35200 |
0.41600 |
0.38800 |
| 329.64 |
0.40000 |
0.51300 |
0.45500 |
0.45200 |
| 330.89 |
0.40500 |
0.22400 |
0.42800 |
0.32800 |
| 329.61 |
0.41300 |
0.43400 |
0.44200 |
0.41700 |
| 333.93 |
0.42600 |
0.06700 |
0.52300 |
0.16000 |
| 329.61 |
0.43900 |
0.38000 |
0.46100 |
0.38700 |
| 330.81 |
0.44700 |
0.20700 |
0.47200 |
0.30100 |
| 334.48 |
0.46700 |
0.04100 |
0.59100 |
0.10000 |
| 329.35 |
0.47800 |
0.39500 |
0.50600 |
0.38200 |
| 330.72 |
0.48900 |
0.19200 |
0.51400 |
0.27600 |
| 329.47 |
0.49200 |
0.34200 |
0.51100 |
0.35500 |
| 334.16 |
0.49800 |
0.03800 |
0.62000 |
0.08900 |
| 329.79 |
0.50400 |
0.27500 |
0.51800 |
0.31900 |
| 329.18 |
0.50800 |
0.42000 |
0.54800 |
0.38400 |
| 331.07 |
0.52300 |
0.14800 |
0.55900 |
0.22800 |
| 331.73 |
0.53200 |
0.10800 |
0.58600 |
0.18600 |
| 329.69 |
0.53700 |
0.26100 |
0.55000 |
0.30200 |
| 333.66 |
0.55300 |
0.03300 |
0.66900 |
0.07000 |
| 329.66 |
0.56200 |
0.24500 |
0.57300 |
0.28700 |
| 330.50 |
0.57900 |
0.15600 |
0.60500 |
0.21900 |
| 328.98 |
0.58700 |
0.33100 |
0.60700 |
0.32400 |
| 328.82 |
0.61000 |
0.35100 |
0.63700 |
0.32800 |
| 328.96 |
0.61700 |
0.29700 |
0.63100 |
0.30000 |
| 330.40 |
0.62100 |
0.14000 |
0.64600 |
0.19600 |
| 328.96 |
0.64600 |
0.26300 |
0.65600 |
0.27400 |
| 330.31 |
0.65800 |
0.12500 |
0.68100 |
0.17600 |
| 328.66 |
0.66900 |
0.29200 |
0.68200 |
0.28600 |
| 329.01 |
0.68200 |
0.22200 |
0.68600 |
0.24300 |
| 330.20 |
0.70700 |
0.10500 |
0.73000 |
0.14700 |
| 328.60 |
0.72800 |
0.24000 |
0.73100 |
0.24400 |
| 328.60 |
0.75000 |
0.22000 |
0.74900 |
0.22800 |
| 329.47 |
0.76500 |
0.12200 |
0.77000 |
0.15300 |
| 329.21 |
0.81600 |
0.11000 |
0.81700 |
0.13200 |
| 329.24 |
0.84400 |
0.09200 |
0.84400 |
0.11200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kurihara K.; Hori H.; Kojima K.: Vapor-Liquid Equilibrium Data for Acetone + Methanol + Benzene, Chloroform + Methanol + Benzene, and Constituent Binary Systems at 101.3 kPa. J.Chem.Eng.Data 43 (1998) 264-268 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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