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 12855
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 3 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
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] |
| 41.037 |
0.36900 |
0.17200 |
0.21800 |
0.12200 |
| 28.558 |
0.15900 |
0.76100 |
0.23100 |
0.63000 |
| 28.931 |
0.15400 |
0.76700 |
0.21700 |
0.62800 |
| 40.343 |
0.25500 |
0.27700 |
0.19300 |
0.18000 |
| 43.143 |
0.11700 |
0.22100 |
0.11500 |
0.12800 |
| 39.250 |
0.41100 |
0.22500 |
0.25200 |
0.17700 |
| 30.398 |
0.62800 |
0.25100 |
0.42100 |
0.32600 |
| 30.691 |
0.36200 |
0.54400 |
0.34000 |
0.50000 |
| 27.864 |
0.03500 |
0.86200 |
0.06800 |
0.71300 |
| 36.304 |
0.58400 |
0.14400 |
0.32500 |
0.15800 |
| 35.504 |
0.61300 |
0.13100 |
0.34300 |
0.15500 |
| 35.490 |
0.47200 |
0.27600 |
0.31600 |
0.26000 |
| 35.170 |
0.45200 |
0.29700 |
0.30200 |
0.27000 |
| 35.544 |
0.38300 |
0.36700 |
0.28100 |
0.30900 |
| 35.170 |
0.28200 |
0.45800 |
0.24500 |
0.36100 |
| 34.677 |
0.27700 |
0.48200 |
0.24400 |
0.37400 |
| 34.704 |
0.19400 |
0.54900 |
0.20100 |
0.40100 |
| 34.744 |
0.14100 |
0.58200 |
0.16400 |
0.41200 |
| 33.024 |
0.07000 |
0.66500 |
0.10200 |
0.47800 |
| 41.437 |
0.42500 |
0.13000 |
0.24100 |
0.10000 |
| 41.677 |
0.35300 |
0.18400 |
0.22000 |
0.13000 |
| 40.010 |
0.26000 |
0.29700 |
0.19800 |
0.20100 |
| 40.770 |
0.24400 |
0.29200 |
0.18700 |
0.19200 |
| 38.117 |
0.08700 |
0.46400 |
0.10400 |
0.29900 |
| 46.103 |
0.32000 |
0.05500 |
0.18500 |
0.03300 |
| 45.356 |
0.17400 |
0.15700 |
0.13900 |
0.08600 |
| 42.983 |
0.07900 |
0.26200 |
0.09200 |
0.15200 |
| 32.637 |
0.60900 |
0.21900 |
0.38800 |
0.26800 |
| 33.651 |
0.42700 |
0.37300 |
0.32600 |
0.34300 |
| 32.717 |
0.20100 |
0.62100 |
0.22400 |
0.47700 |
| 38.570 |
0.41800 |
0.22800 |
0.25900 |
0.18700 |
| 40.157 |
0.17600 |
0.34500 |
0.15900 |
0.21800 |
| 41.570 |
0.50400 |
0.07800 |
0.25200 |
0.06500 |
| 34.171 |
0.29600 |
0.45700 |
0.25200 |
0.35900 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.: Isothermal Vapor-Liquid Equilibria for the Ternary Ethanol-Acetonitrile-Chloroform System. J.Chem.Eng.Data 33 (1988) 286-288 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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