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 14072
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 4 |
CH4O |
32.042 |
67-56-1 |
Methanol |
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] |
| 68.314 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 43.583 |
0.00000 |
0.00000 |
1.00000 |
0.00000 |
0.00000 |
1.00000 |
| 40.877 |
0.00000 |
1.00000 |
0.00000 |
0.00000 |
1.00000 |
0.00000 |
| 5.940 |
1.00000 |
0.00000 |
0.00000 |
1.00000 |
0.00000 |
0.00000 |
| 51.769 |
0.41000 |
0.15300 |
0.10000 |
0.06100 |
0.24700 |
0.21000 |
| 49.063 |
0.43700 |
0.18300 |
0.19200 |
0.07000 |
0.27800 |
0.34000 |
| 49.969 |
0.32700 |
0.35900 |
0.20400 |
0.06100 |
0.41400 |
0.31600 |
| 54.196 |
0.32200 |
0.21800 |
0.31100 |
0.05200 |
0.26200 |
0.41900 |
| 69.141 |
0.16200 |
0.17600 |
0.10500 |
0.01900 |
0.18800 |
0.19000 |
| 55.622 |
0.10400 |
0.20300 |
0.65800 |
0.03300 |
0.23500 |
0.59900 |
| 64.888 |
0.16000 |
0.35000 |
0.26800 |
0.02500 |
0.29700 |
0.32000 |
| 63.208 |
0.30200 |
0.09500 |
0.19300 |
0.03700 |
0.12400 |
0.32000 |
| 74.261 |
0.15900 |
0.09100 |
0.17400 |
0.01700 |
0.10200 |
0.28100 |
| 64.208 |
0.21500 |
0.19200 |
0.36500 |
0.03000 |
0.19300 |
0.40900 |
| 64.315 |
0.07800 |
0.26000 |
0.57300 |
0.01700 |
0.24000 |
0.48700 |
| 41.370 |
0.56700 |
0.09900 |
0.20400 |
0.10000 |
0.21400 |
0.43300 |
| 66.128 |
0.12100 |
0.23400 |
0.49300 |
0.02100 |
0.21100 |
0.45000 |
| 66.568 |
0.09100 |
0.50000 |
0.20900 |
0.01700 |
0.37200 |
0.26600 |
| 65.821 |
0.11200 |
0.22900 |
0.52500 |
0.02000 |
0.20800 |
0.46500 |
| 61.782 |
0.07500 |
0.49800 |
0.33900 |
0.01800 |
0.39800 |
0.36900 |
| 61.782 |
0.07900 |
0.48600 |
0.34400 |
0.01800 |
0.39000 |
0.37200 |
| 46.929 |
0.15500 |
0.70000 |
0.11100 |
0.04800 |
0.66300 |
0.19800 |
| 49.103 |
0.14900 |
0.66100 |
0.14900 |
0.04400 |
0.60700 |
0.24300 |
| 51.956 |
0.20800 |
0.53800 |
0.15400 |
0.04600 |
0.50800 |
0.24200 |
| 39.997 |
0.54400 |
0.21400 |
0.14400 |
0.10300 |
0.39800 |
0.30800 |
| 51.809 |
0.13800 |
0.63300 |
0.17400 |
0.03700 |
0.55800 |
0.26500 |
| 42.290 |
0.56700 |
0.06400 |
0.15200 |
0.09200 |
0.15300 |
0.36400 |
| 54.182 |
0.13800 |
0.63500 |
0.11100 |
0.03300 |
0.53900 |
0.18400 |
| 74.421 |
0.14700 |
0.06100 |
0.16400 |
0.01500 |
0.07000 |
0.28100 |
| 63.221 |
0.23400 |
0.20000 |
0.33100 |
0.03400 |
0.20400 |
0.39200 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.: Isothermal (vapour + liquid) equilibria of (methanol + butan-1-ol + acetonitrile + benzene). J.Chem.Thermodyn. 23 (1991) 293-296 |
List of All References
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH