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 1615
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 399.35 |
0.00000 |
0.00000 |
| 395.65 |
0.01000 |
0.05700 |
| 393.65 |
0.01800 |
0.10200 |
| 390.25 |
0.03000 |
0.16500 |
| 388.15 |
0.04000 |
0.21500 |
| 386.15 |
0.05000 |
0.25500 |
| 382.90 |
0.08000 |
0.34000 |
| 378.55 |
0.13300 |
0.46000 |
| 375.65 |
0.17200 |
0.53500 |
| 373.45 |
0.21500 |
0.59500 |
| 367.55 |
0.37500 |
0.74000 |
| 364.85 |
0.46500 |
0.79600 |
| 363.90 |
0.50800 |
0.81700 |
| 362.05 |
0.56700 |
0.84700 |
| 360.90 |
0.61200 |
0.86500 |
| 359.65 |
0.68000 |
0.89800 |
| 358.65 |
0.74200 |
0.91500 |
| 357.65 |
0.79300 |
0.92700 |
| 356.90 |
0.84600 |
0.94500 |
| 356.25 |
0.89000 |
0.96000 |
| 355.85 |
0.91700 |
0.96900 |
| 355.25 |
0.95000 |
0.98000 |
| 354.85 |
0.97900 |
0.98900 |
| 354.65 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Mato F.; Cabezas J.L.; Coca J.: Equilibrio Liquido-Vapor Isobarico y Calor de Mezcla. Anal.Quim. 69 (1973) 123-128 |
Vapor-Liquid Equilibrium Data Set 7782
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 398.55 |
0.00000 |
0.00000 |
| 388.45 |
0.08600 |
0.33800 |
| 378.80 |
0.20800 |
0.58800 |
| 375.75 |
0.23400 |
0.60400 |
| 370.05 |
0.35200 |
0.74100 |
| 366.50 |
0.46100 |
0.79900 |
| 364.95 |
0.51800 |
0.82900 |
| 363.20 |
0.58800 |
0.84800 |
| 362.15 |
0.64500 |
0.87100 |
| 358.35 |
0.80400 |
0.93000 |
| 358.25 |
0.79400 |
0.92900 |
| 354.75 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Ravi Prasad A.: Data, Measurement, Correlation and Prediction. Thesis (2004) |
Vapor-Liquid Equilibrium Data Set 8971
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 398.85 |
0.00000 |
0.00000 |
| 389.55 |
0.05100 |
0.28950 |
| 385.15 |
0.08500 |
0.43810 |
| 380.55 |
0.14900 |
0.53220 |
| 376.75 |
0.19400 |
0.60200 |
| 371.25 |
0.29200 |
0.69850 |
| 366.65 |
0.42100 |
0.78680 |
| 363.15 |
0.50000 |
0.82840 |
| 358.45 |
0.78700 |
0.92080 |
| 356.55 |
0.91000 |
0.96410 |
| 354.65 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kesarwani V.S.; Chandak B.S.; Kher M.G.: Acetonitrile-Toluene Systems. Chem.Petro-Chem.J. 10 (1979) 3-8 |
Diagrams
List of All References
| Source |
| Mato F.; Cabezas J.L.; Coca J.: Equilibrio Liquido-Vapor Isobarico y Calor de Mezcla. Anal.Quim. 69 (1973) 123-128 |
| Kesarwani V.S.; Chandak B.S.; Kher M.G.: Acetonitrile-Toluene Systems. Chem.Petro-Chem.J. 10 (1979) 3-8 |
| Ravi Prasad A.: Data, Measurement, Correlation and Prediction. Thesis (2004) |
Vapor-Liquid Equilibrium Data Overview
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