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 1140
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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Miscibility gap: No
Constant Value
Data Table
hE [J/mol] |
x1 [mol/mol] |
421.192 |
0.08700 |
457.617 |
0.10560 |
571.498 |
0.17560 |
625.089 |
0.25360 |
637.231 |
0.30610 |
643.092 |
0.31220 |
655.234 |
0.37580 |
652.722 |
0.45510 |
612.947 |
0.56110 |
543.447 |
0.68120 |
469.759 |
0.75060 |
416.586 |
0.80290 |
289.308 |
0.88910 |
271.723 |
0.89160 |
154.074 |
0.94310 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
Source |
Goates J.R.; Snow R.L.; James M.R.: Application of Quasi-Lattice Theory to Heats of Mixing in some Alcohol-Hydrocarbon Systems. J.Phys.Chem. 65 (1961) 335-336 |
Enthalpy of Mixing Data Set 1141
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
Search the DDB for all data of this mixture
Miscibility gap: No
Constant Value
Data Table
hE [J/mol] |
x1 [mol/mol] |
429.917 |
0.13240 |
543.486 |
0.26000 |
580.151 |
0.34000 |
590.044 |
0.50000 |
519.043 |
0.66830 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
Source |
Grosse-Wortmann H.; Jost W.; Wagner H.G.: Kalorimetrische Messungen am System Äthanol-Cyclohexan-n-Heptan. Z.Phys.Chem.(München) 49 (1966) 74-93 |
Enthalpy of Mixing Data Set 1142
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
Search the DDB for all data of this mixture
Miscibility gap: No
Constant Value
Data Table
hE [J/mol] |
x1 [mol/mol] |
274.500 |
0.03520 |
426.000 |
0.10270 |
537.500 |
0.18960 |
607.100 |
0.28790 |
627.100 |
0.33810 |
638.300 |
0.38830 |
642.200 |
0.43550 |
638.400 |
0.48230 |
629.000 |
0.52670 |
614.500 |
0.56840 |
538.300 |
0.68650 |
520.000 |
0.70660 |
494.300 |
0.73240 |
464.600 |
0.75990 |
426.700 |
0.78980 |
384.500 |
0.81960 |
316.400 |
0.86110 |
239.700 |
0.90150 |
154.600 |
0.94070 |
60.300 |
0.97790 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
Source |
Nagata I.; Kazuma K.: Heats of Mixing for the Ternary System Ethanol-1-Propanol-Cyclohexane at 25° C. J.Chem.Eng.Data 22 (1977) 79-84 |
Diagrams
List of All References
Source |
Grosse-Wortmann H.; Jost W.; Wagner H.G.: Kalorimetrische Messungen am System Äthanol-Cyclohexan-n-Heptan. Z.Phys.Chem.(München) 49 (1966) 74-93 |
Goates J.R.; Snow R.L.; James M.R.: Application of Quasi-Lattice Theory to Heats of Mixing in some Alcohol-Hydrocarbon Systems. J.Phys.Chem. 65 (1961) 335-336 |
Nagata I.; Kazuma K.: Heats of Mixing for the Ternary System Ethanol-1-Propanol-Cyclohexane at 25° C. J.Chem.Eng.Data 22 (1977) 79-84 |
Excess Enthalpy Data Overview
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