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 14057
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 386.75 |
0.02600 |
0.08800 |
| 383.35 |
0.08900 |
0.23900 |
| 381.05 |
0.11900 |
0.31200 |
| 379.35 |
0.14500 |
0.35700 |
| 375.05 |
0.20200 |
0.45700 |
| 373.45 |
0.24700 |
0.52800 |
| 371.55 |
0.28500 |
0.57900 |
| 369.15 |
0.35500 |
0.65300 |
| 367.45 |
0.40400 |
0.70500 |
| 365.45 |
0.46700 |
0.76200 |
| 363.85 |
0.53200 |
0.80700 |
| 363.55 |
0.55700 |
0.82300 |
| 362.95 |
0.57800 |
0.82800 |
| 362.35 |
0.60200 |
0.85300 |
| 359.75 |
0.73800 |
0.91500 |
| 358.45 |
0.81800 |
0.94500 |
| 357.15 |
0.89100 |
0.97000 |
| 355.65 |
0.97200 |
0.99200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Mato F.; Sanchez M.: Equilibrio Liquido-Vapor de Mezclas Binarias de Acetonitrilio. II.. Anal.Fis.Quim.Ser.B 63 (1967) 971-980 |
Vapor-Liquid Equilibrium Data Set 15393
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 2.080 |
0.00000 |
| 4.518 |
0.11670 |
| 5.832 |
0.20990 |
| 6.871 |
0.29850 |
| 7.687 |
0.36190 |
| 8.326 |
0.41880 |
| 8.639 |
0.47950 |
| 8.905 |
0.54610 |
| 9.415 |
0.62720 |
| 9.685 |
0.68690 |
| 10.220 |
0.76330 |
| 10.627 |
0.80980 |
| 10.766 |
0.85140 |
| 11.164 |
0.91040 |
| 11.864 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Banipal T.S.; Lark B.S.; Singh S.: Excess Gibbs for binary mixtures of acetonitrile with acetic acid, propionic acid, isobutyric acid, and trimethylacetic acid. Can.J.Chem. 69 (1991) 2117-2121 |
Vapor-Liquid Equilibrium Data Set 15394
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 5.780 |
0.00000 |
| 11.115 |
0.11670 |
| 13.983 |
0.20990 |
| 16.297 |
0.29850 |
| 18.235 |
0.36190 |
| 19.464 |
0.41880 |
| 20.414 |
0.47950 |
| 21.256 |
0.54610 |
| 22.327 |
0.62720 |
| 23.182 |
0.68690 |
| 24.194 |
0.76330 |
| 24.905 |
0.80980 |
| 25.675 |
0.85140 |
| 26.575 |
0.91040 |
| 28.242 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Banipal T.S.; Lark B.S.; Singh S.: Excess Gibbs for binary mixtures of acetonitrile with acetic acid, propionic acid, isobutyric acid, and trimethylacetic acid. Can.J.Chem. 69 (1991) 2117-2121 |
Diagrams
List of All References
| Source |
| Mato F.; Sanchez M.: Equilibrio Liquido-Vapor de Mezclas Binarias de Acetonitrilio. II.. Anal.Fis.Quim.Ser.B 63 (1967) 971-980 |
| Banipal T.S.; Lark B.S.; Singh S.: Excess Gibbs for binary mixtures of acetonitrile with acetic acid, propionic acid, isobutyric acid, and trimethylacetic acid. Can.J.Chem. 69 (1991) 2117-2121 |
Vapor-Liquid Equilibrium Data Overview
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