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 3072
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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] |
193.100 |
0.25310 |
210.800 |
0.31640 |
222.200 |
0.41910 |
217.400 |
0.49700 |
214.500 |
0.52240 |
198.900 |
0.59000 |
186.200 |
0.63860 |
170.900 |
0.68680 |
136.000 |
0.76290 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
Source |
Ahmed A.: Enthalpy of Mixing of n-Hexane and Cyclohexane. J.Chem.Soc.Faraday Trans.1 69 (1973) 387-389 |
Enthalpy of Mixing Data Set 3073
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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] |
55.200 |
0.09000 |
158.100 |
0.23000 |
187.900 |
0.30000 |
208.200 |
0.39000 |
217.800 |
0.46000 |
219.100 |
0.50000 |
188.200 |
0.67000 |
133.800 |
0.79000 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
Source |
Alessi P.; Kikic I.; Longo V.: The Heats of Mixing of Paraffin-Cycloparaffin Systems. Ist.Chim.Appl./Fac.Ing.,Univ.Studi Trieste 49 (1974) 1-10 |
Enthalpy of Mixing Data Set 3074
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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] |
61.000 |
0.05720 |
81.000 |
0.07700 |
108.000 |
0.10910 |
134.000 |
0.14300 |
168.000 |
0.19850 |
186.000 |
0.23890 |
193.000 |
0.25460 |
199.000 |
0.27260 |
206.000 |
0.29920 |
208.000 |
0.30560 |
214.000 |
0.33550 |
215.000 |
0.34190 |
215.000 |
0.34220 |
218.000 |
0.35890 |
217.000 |
0.36120 |
218.000 |
0.37470 |
219.000 |
0.37770 |
220.000 |
0.37850 |
220.000 |
0.38340 |
219.000 |
0.38600 |
220.000 |
0.38730 |
220.000 |
0.39860 |
221.000 |
0.40060 |
221.000 |
0.40930 |
221.000 |
0.40990 |
221.000 |
0.41050 |
221.000 |
0.41630 |
221.000 |
0.42630 |
221.000 |
0.42970 |
221.000 |
0.43130 |
221.000 |
0.43650 |
221.000 |
0.44090 |
221.000 |
0.44800 |
221.000 |
0.44860 |
220.000 |
0.45380 |
220.000 |
0.46600 |
220.000 |
0.46830 |
219.000 |
0.47070 |
218.000 |
0.48430 |
218.000 |
0.49110 |
217.000 |
0.49690 |
216.000 |
0.49880 |
215.000 |
0.50910 |
214.000 |
0.51900 |
213.000 |
0.52080 |
211.000 |
0.53380 |
211.000 |
0.53490 |
209.000 |
0.54380 |
207.000 |
0.55610 |
205.000 |
0.56290 |
202.000 |
0.57770 |
197.000 |
0.59440 |
197.000 |
0.59860 |
189.000 |
0.62360 |
188.000 |
0.62850 |
182.000 |
0.64800 |
178.000 |
0.66110 |
168.000 |
0.68840 |
162.000 |
0.70200 |
161.000 |
0.70600 |
141.000 |
0.75300 |
137.000 |
0.76080 |
130.000 |
0.77630 |
118.000 |
0.80140 |
95.000 |
0.84530 |
92.000 |
0.84920 |
87.000 |
0.85990 |
48.000 |
0.92650 |
42.000 |
0.93580 |
37.000 |
0.94350 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
Source |
Arenosa R.L.; Menduina C.; Tardajos G.; Diaz Pena M.: Excess Enthalpies at 298.15 K of Binary Mixtures of Cyclohexane with n-Alkanes. J.Chem.Thermodyn. 11 (1979) 159-166 |
Diagrams
List of All References
Source |
Ahmed A.: Enthalpy of Mixing of n-Hexane and Cyclohexane. J.Chem.Soc.Faraday Trans.1 69 (1973) 387-389 |
Alessi P.; Kikic I.; Longo V.: The Heats of Mixing of Paraffin-Cycloparaffin Systems. Ist.Chim.Appl./Fac.Ing.,Univ.Studi Trieste 49 (1974) 1-10 |
Arenosa R.L.; Menduina C.; Tardajos G.; Diaz Pena M.: Excess Enthalpies at 298.15 K of Binary Mixtures of Cyclohexane with n-Alkanes. J.Chem.Thermodyn. 11 (1979) 159-166 |
Excess Enthalpy Data Overview
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