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 10768
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
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
P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
43.570 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
40.861 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
68.300 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
77.750 |
0.39700 |
0.20300 |
0.26200 |
0.39100 |
83.690 |
0.25500 |
0.33000 |
0.17300 |
0.47500 |
76.990 |
0.51300 |
0.28700 |
0.32000 |
0.43900 |
86.690 |
0.20900 |
0.49500 |
0.14700 |
0.53900 |
78.060 |
0.31300 |
0.16600 |
0.22300 |
0.38000 |
88.970 |
0.07800 |
0.43400 |
0.06000 |
0.54800 |
63.929 |
0.49700 |
0.04900 |
0.40800 |
0.15800 |
80.829 |
0.25000 |
0.65400 |
0.19800 |
0.63400 |
83.900 |
0.11800 |
0.19300 |
0.09500 |
0.46400 |
64.269 |
0.66900 |
0.09300 |
0.47300 |
0.23300 |
90.210 |
0.05800 |
0.64400 |
0.05000 |
0.60200 |
67.300 |
0.67100 |
0.27500 |
0.44900 |
0.45500 |
84.690 |
0.10100 |
0.76500 |
0.09300 |
0.66900 |
61.670 |
0.76700 |
0.14000 |
0.53900 |
0.30700 |
51.010 |
0.89300 |
0.04200 |
0.73900 |
0.12800 |
64.229 |
0.50100 |
0.05600 |
0.40200 |
0.17500 |
78.820 |
0.05300 |
0.89900 |
0.06400 |
0.81100 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Ohta T.; Nagata I.: Vapor-Liquid Equilibria for the Ternary Systems Acetonitrile-2-Butanone-Benzene and Acetonitrile-Methanol-Benzene at 328.15 K. J.Chem.Eng.Data 28 (1983) 398-402 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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