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 2723
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 354.15 |
0.01500 |
0.04200 |
| 353.25 |
0.03500 |
0.08800 |
| 352.15 |
0.05700 |
0.13800 |
| 351.25 |
0.07900 |
0.17900 |
| 350.15 |
0.10700 |
0.23200 |
| 348.75 |
0.14700 |
0.29300 |
| 347.75 |
0.17800 |
0.34100 |
| 346.85 |
0.21300 |
0.38500 |
| 345.75 |
0.25200 |
0.43500 |
| 344.85 |
0.29300 |
0.47600 |
| 343.95 |
0.33400 |
0.51900 |
| 343.15 |
0.37900 |
0.56000 |
| 342.35 |
0.42400 |
0.60100 |
| 341.75 |
0.46200 |
0.63100 |
| 341.05 |
0.50200 |
0.66300 |
| 340.45 |
0.54300 |
0.69500 |
| 339.85 |
0.57900 |
0.72300 |
| 339.25 |
0.61600 |
0.75000 |
| 338.75 |
0.64400 |
0.77100 |
| 338.55 |
0.66300 |
0.78400 |
| 338.25 |
0.68600 |
0.80300 |
| 337.75 |
0.71100 |
0.82200 |
| 337.45 |
0.74200 |
0.84000 |
| 337.05 |
0.76900 |
0.85700 |
| 336.95 |
0.78100 |
0.86500 |
| 336.95 |
0.78700 |
0.86600 |
| 336.65 |
0.80600 |
0.88000 |
| 336.15 |
0.86200 |
0.91300 |
| 335.85 |
0.88400 |
0.92800 |
| 335.05 |
0.96600 |
0.97600 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Mato F.; Sanchez M.: Equilibrio Liquido-Vapor de Mezclas Binarias de Acetonitrilo. Anal.Fis.Quim.Ser.B 63 (1967) 1-11 |
Vapor-Liquid Equilibrium Data Set 6184
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 22.958 |
0.00000 |
| 29.464 |
0.18230 |
| 32.731 |
0.30230 |
| 34.864 |
0.39900 |
| 37.397 |
0.50030 |
| 41.130 |
0.67350 |
| 43.530 |
0.76330 |
| 48.249 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Kreglewski A.: Influence of Donor-Acceptor Interactions on the Free Energy of Mixing. The Chloroform-Acetonitrile System at 40°C. Bull.Acad.Pol.Sci.Ser.Sci.Chim. 13 (1965) 723-727 |
Vapor-Liquid Equilibrium Data Set 6973
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 44.400 |
0.04000 |
0.09500 |
| 48.971 |
0.10900 |
0.23200 |
| 54.450 |
0.23000 |
0.39500 |
| 59.290 |
0.33800 |
0.50900 |
| 62.790 |
0.42400 |
0.58600 |
| 67.670 |
0.54900 |
0.69300 |
| 70.450 |
0.63800 |
0.75600 |
| 75.460 |
0.78500 |
0.86200 |
| 77.350 |
0.85900 |
0.91000 |
| 79.829 |
0.93400 |
0.95500 |
| 79.989 |
0.93800 |
0.95800 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.; Kawamura Y.: Excess Thermodynamic Functions and Complex Formation in Binary Liquid Mixtures Containing Acetonitrile. Fluid Phase Equilib. 3 (1979) 1-11 |
Diagrams
List of All References
| Source |
| Mato F.; Sanchez M.: Equilibrio Liquido-Vapor de Mezclas Binarias de Acetonitrilo. Anal.Fis.Quim.Ser.B 63 (1967) 1-11 |
| Kreglewski A.: Influence of Donor-Acceptor Interactions on the Free Energy of Mixing. The Chloroform-Acetonitrile System at 40°C. Bull.Acad.Pol.Sci.Ser.Sci.Chim. 13 (1965) 723-727 |
| Nagata I.; Kawamura Y.: Excess Thermodynamic Functions and Complex Formation in Binary Liquid Mixtures Containing Acetonitrile. Fluid Phase Equilib. 3 (1979) 1-11 |
Vapor-Liquid Equilibrium Data Overview
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