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 756
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Miscibility gap: No
Constant Value
Data Table
hE [J/mol] |
x1 [mol/mol] |
800.000 |
0.38100 |
545.000 |
0.65800 |
545.000 |
0.65900 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
Source |
Brown I.; Fock W.: IV. Systems of n-Alcohols with Benzene at 25, 35, and 45° C. Aust.J.Chem. 14 (1961) 387-396 |
Enthalpy of Mixing Data Set 757
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Miscibility gap: No
Constant Value
Data Table
hE [J/mol] |
x1 [mol/mol] |
435.427 |
0.05010 |
539.260 |
0.07920 |
589.920 |
0.10670 |
632.207 |
0.13260 |
656.909 |
0.15700 |
692.915 |
0.20190 |
711.337 |
0.26090 |
707.150 |
0.32730 |
690.403 |
0.37950 |
658.583 |
0.43770 |
625.927 |
0.48600 |
575.266 |
0.54800 |
525.025 |
0.60150 |
400.677 |
0.70740 |
347.504 |
0.75110 |
279.678 |
0.80510 |
224.831 |
0.84470 |
162.866 |
0.89050 |
72.850 |
0.95230 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
Source |
Coca Prados J.: Propiedades Fisico - Quimicas de Mezclas Liquidas Binarias: Viscosidad y Calor de Mezcla. Thesis (1969) |
Enthalpy of Mixing Data Set 758
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Miscibility gap: No
Constant Value
Data Table
hE [J/mol] |
x1 [mol/mol] |
483.156 |
0.06180 |
622.577 |
0.11780 |
694.171 |
0.19020 |
731.853 |
0.25580 |
719.292 |
0.35010 |
681.192 |
0.42810 |
647.698 |
0.49370 |
560.194 |
0.55750 |
588.245 |
0.57320 |
513.302 |
0.61500 |
512.045 |
0.63830 |
466.828 |
0.65620 |
413.656 |
0.69930 |
369.694 |
0.73170 |
327.408 |
0.76410 |
281.771 |
0.79750 |
238.229 |
0.83080 |
194.267 |
0.86430 |
144.863 |
0.89830 |
91.272 |
0.93220 |
43.124 |
0.96010 |
14.235 |
0.98620 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
Source |
Deshpande D.D.; Pandya M.V.: Part 1. Heats of Mixing of Aniline in Benzene, Carbontetrachloride and Chlorobenzene. Trans.Faraday Soc. 61 (1965) 1858-1868 |
Diagrams
List of All References
Source |
Deshpande D.D.; Pandya M.V.: Part 1. Heats of Mixing of Aniline in Benzene, Carbontetrachloride and Chlorobenzene. Trans.Faraday Soc. 61 (1965) 1858-1868 |
Brown I.; Fock W.: IV. Systems of n-Alcohols with Benzene at 25, 35, and 45° C. Aust.J.Chem. 14 (1961) 387-396 |
Coca Prados J.: Propiedades Fisico - Quimicas de Mezclas Liquidas Binarias: Viscosidad y Calor de Mezcla. Thesis (1969) |
Excess Enthalpy Data Overview
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