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 1601

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H12 84.161 110-82-7 Cyclohexane
2 C3H8O 60.096 67-63-0 2-Propanol
Search the DDB for all data of this mixture

Miscibility gap: No

Constant Value

Temperature 298.150 K

Data Table

hE [J/mol] x1 [mol/mol]
45.200 0.01770
125.500 0.05030
234.100 0.09790
367.000 0.16140
493.300 0.23010
606.600 0.30260
685.400 0.36420
741.200 0.41680
781.600 0.46630
791.800 0.49200
818.100 0.55140
825.700 0.60880
809.500 0.67270
764.100 0.73810
692.200 0.79920
595.500 0.85770
467.700 0.91510
249.300 0.97800

(hE - excess enthalpy, x - liquid mole fraction)

Reference

Source
Nagata I.; Fujiwara K.; Ogasawara Y.: Excess Enthalpies of 2-Propanol + Cyclohexane and 2-Propanol + Benzene + Cyclohexane at 298.15 K. J.Chem.Thermodyn. 10 (1978) 1201-1203


Enthalpy of Mixing Data Set 1602

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H12 84.161 110-82-7 Cyclohexane
2 C3H8O 60.096 67-63-0 2-Propanol
Search the DDB for all data of this mixture

Miscibility gap: No

Constant Value

Temperature 308.150 K

Data Table

hE [J/mol] x1 [mol/mol]
318.200 0.10880
334.110 0.11400
671.560 0.26990
800.100 0.35110
897.650 0.40670
945.380 0.48280
951.660 0.51130
961.710 0.52420
981.390 0.61680
950.400 0.68680
931.560 0.71390
836.520 0.78740
754.880 0.83640
672.820 0.88230
617.550 0.89700

(hE - excess enthalpy, x - liquid mole fraction)

Reference

Source
Nagata I.; Ohta T.: Computation of Vapor-Liquid Equilibria Data from Binary and Ternary Vapor Pressure and Boiling Points Measurements. Ind.Eng.Chem. Process Des.Dev. 13 (1974) 304-309


Enthalpy of Mixing Data Set 1603

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H12 84.161 110-82-7 Cyclohexane
2 C3H8O 60.096 67-63-0 2-Propanol
Search the DDB for all data of this mixture

Miscibility gap: No

Constant Value

Temperature 318.150 K

Data Table

hE [J/mol] x1 [mol/mol]
198.870 0.05610
444.220 0.14180
457.200 0.14550
470.180 0.14800
612.950 0.20330
748.600 0.26570
744.410 0.26910
778.330 0.28720
856.200 0.32570
1026.600 0.44010
1101.130 0.50810
1131.690 0.58670
1098.200 0.68260
1097.360 0.70000
1029.950 0.75750
927.790 0.81840
856.200 0.85500
695.430 0.89600
606.250 0.91510

(hE - excess enthalpy, x - liquid mole fraction)

Reference

Source
Nagata I.; Ohta T.: Computation of Vapor-Liquid Equilibria Data from Binary and Ternary Vapor Pressure and Boiling Points Measurements. Ind.Eng.Chem. Process Des.Dev. 13 (1974) 304-309

Diagrams

Excess Enthalpies of Cyclohexane+2-Propanol
See larger image

List of All References

Source
Nagata I.; Ohta T.: Computation of Vapor-Liquid Equilibria Data from Binary and Ternary Vapor Pressure and Boiling Points Measurements. Ind.Eng.Chem. Process Des.Dev. 13 (1974) 304-309
Nagata I.; Fujiwara K.; Ogasawara Y.: Excess Enthalpies of 2-Propanol + Cyclohexane and 2-Propanol + Benzene + Cyclohexane at 298.15 K. J.Chem.Thermodyn. 10 (1978) 1201-1203

Excess Enthalpy Data Overview


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