Dortmund Data Bank
Excess Enthalpy 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.
Enthalpy of Mixing Data Set 936
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
Miscibility gap: No
Constant Value
Data Table
| hE [J/mol] |
x1 [mol/mol] |
| 77.414 |
0.10330 |
| 124.180 |
0.19810 |
| 194.686 |
0.30190 |
| 244.216 |
0.40430 |
| 277.543 |
0.51740 |
| 271.053 |
0.58450 |
| 226.966 |
0.70130 |
| 184.470 |
0.80090 |
| 114.007 |
0.90230 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
| Source |
| Kesarwani V.S.; Chandak B.S.; Kher M.G.: Acetonitrile-Toluene Systems. Chem.Petro-Chem.J. 10 (1979) 3-8 |
Enthalpy of Mixing Data Set 6604
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
Miscibility gap: No
Constant Value
Data Table
| hE [J/mol] |
x1 [mol/mol] |
| 102.577 |
0.10000 |
| 186.313 |
0.20000 |
| 251.208 |
0.30000 |
| 301.450 |
0.40000 |
| 330.757 |
0.50000 |
| 337.037 |
0.60000 |
| 314.010 |
0.70000 |
| 251.208 |
0.80000 |
| 146.538 |
0.90000 |
(hE - excess enthalpy, x - liquid 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 |
Enthalpy of Mixing Data Set 10047
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
Miscibility gap: No
Constant Value
| Temperature |
363.150 |
K |
| Pressure |
18.910 |
bar |
Data Table
| hE [J/mol] |
x1 [mol/mol] |
| 46.466 |
0.03060 |
| 86.144 |
0.06010 |
| 163.576 |
0.11610 |
| 216.471 |
0.16820 |
| 279.255 |
0.21700 |
| 313.864 |
0.26280 |
| 359.668 |
0.30570 |
| 413.359 |
0.38410 |
| 444.063 |
0.45400 |
| 458.775 |
0.51670 |
| 458.525 |
0.57330 |
| 448.103 |
0.62450 |
| 430.628 |
0.67120 |
| 413.801 |
0.71390 |
| 380.844 |
0.75300 |
| 350.370 |
0.78910 |
| 318.566 |
0.82250 |
| 280.003 |
0.85340 |
| 238.451 |
0.88210 |
| 194.503 |
0.90890 |
| 148.572 |
0.93390 |
| 100.743 |
0.95740 |
| 51.209 |
0.97930 |
| 26.514 |
0.98980 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
| Source |
| Gmehling J.: unpublished data. Unpublished Data (2011) 1-43 |
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 |
| Gmehling J.: unpublished data. Unpublished Data (2011) 1-43 |
| Kesarwani V.S.; Chandak B.S.; Kher M.G.: Acetonitrile-Toluene Systems. Chem.Petro-Chem.J. 10 (1979) 3-8 |
Excess Enthalpy Data Overview
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