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 14701
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 4 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
x3 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
y3 [mol/mol] |
| 23.051 |
0.00000 |
1.00000 |
0.00000 |
0.00000 |
1.00000 |
0.00000 |
| 27.771 |
0.00000 |
0.00000 |
1.00000 |
0.00000 |
0.00000 |
1.00000 |
| 29.824 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 46.490 |
0.09400 |
0.10800 |
0.41400 |
0.18800 |
0.11400 |
0.31800 |
| 38.863 |
0.11800 |
0.57800 |
0.23400 |
0.14200 |
0.39500 |
0.29500 |
| 40.223 |
0.11800 |
0.60600 |
0.14300 |
0.14000 |
0.38500 |
0.19800 |
| 42.890 |
0.13600 |
0.41800 |
0.29200 |
0.16600 |
0.27900 |
0.29300 |
| 43.730 |
0.18100 |
0.25100 |
0.43800 |
0.23800 |
0.19700 |
0.36900 |
| 33.597 |
0.19200 |
0.73200 |
0.03900 |
0.26000 |
0.50900 |
0.10000 |
| 47.703 |
0.19700 |
0.21000 |
0.30200 |
0.25600 |
0.15900 |
0.25600 |
| 46.676 |
0.19700 |
0.31900 |
0.24900 |
0.24100 |
0.20500 |
0.23000 |
| 34.211 |
0.20100 |
0.71900 |
0.02200 |
0.25900 |
0.49100 |
0.05400 |
| 32.784 |
0.20300 |
0.70600 |
0.07100 |
0.26200 |
0.50900 |
0.16000 |
| 43.290 |
0.20900 |
0.30700 |
0.38100 |
0.25000 |
0.23000 |
0.35000 |
| 42.157 |
0.21000 |
0.54400 |
0.07100 |
0.23300 |
0.33200 |
0.10400 |
| 42.263 |
0.22900 |
0.37900 |
0.30900 |
0.26700 |
0.25900 |
0.32000 |
| 43.343 |
0.26600 |
0.49100 |
0.09900 |
0.28900 |
0.29000 |
0.13600 |
| 41.063 |
0.27500 |
0.45200 |
0.20100 |
0.30800 |
0.27500 |
0.25200 |
| 49.289 |
0.27900 |
0.28700 |
0.11800 |
0.32100 |
0.16900 |
0.11900 |
| 44.996 |
0.29500 |
0.44700 |
0.07000 |
0.31100 |
0.25000 |
0.09400 |
| 54.489 |
0.39800 |
0.11500 |
0.12800 |
0.44600 |
0.06600 |
0.10900 |
| 53.476 |
0.40000 |
0.10500 |
0.25300 |
0.43900 |
0.06200 |
0.19900 |
| 38.637 |
0.46400 |
0.44500 |
0.06800 |
0.51700 |
0.29200 |
0.12100 |
| 49.169 |
0.47700 |
0.24500 |
0.14800 |
0.46800 |
0.12500 |
0.16000 |
| 48.449 |
0.50500 |
0.18800 |
0.20200 |
0.49900 |
0.10200 |
0.20200 |
| 52.769 |
0.50700 |
0.21700 |
0.07300 |
0.48600 |
0.11100 |
0.07900 |
| 43.170 |
0.68000 |
0.23000 |
0.06800 |
0.69700 |
0.12300 |
0.11200 |
| 44.423 |
0.69400 |
0.22400 |
0.04400 |
0.69300 |
0.11600 |
0.07300 |
| 44.156 |
1.00000 |
0.00000 |
0.00000 |
1.00000 |
0.00000 |
0.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.: Isothermal Vapour-Liquid Equilibrium for the Methanol-Ethanol-Acetonitrile-Benzene System. Thermochim.Acta 157 (1990) 95-104 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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