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 9142
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
| 3 |
C5H9NO |
99.133 |
872-50-4 |
N-Methyl-2-pyrrolidone |
Search the DDB for all data of this mixture
Miscibility gap: No
Constant Value
| Temperature |
416.290 |
K |
| Pressure |
24.000 |
bar |
Data Table
| hE [J/mol] |
x1 [mol/mol] |
x2 [mol/mol] |
| -3.740 |
0.03450 |
0.14040 |
| 154.630 |
0.06330 |
0.24340 |
| 156.570 |
0.06350 |
0.24340 |
| 187.370 |
0.07020 |
0.13520 |
| 191.368 |
0.07020 |
0.13520 |
| 191.348 |
0.07020 |
0.13520 |
| 351.070 |
0.09720 |
0.23460 |
| 356.580 |
0.09720 |
0.23460 |
| 360.916 |
0.10710 |
0.12980 |
| 576.320 |
0.13240 |
0.22550 |
| 520.053 |
0.14520 |
0.12430 |
| 725.480 |
0.16910 |
0.21590 |
| 726.680 |
0.16910 |
0.21590 |
| 648.456 |
0.18470 |
0.11850 |
| 891.750 |
0.20730 |
0.20600 |
| 774.122 |
0.22560 |
0.11260 |
| 1127.150 |
0.28920 |
0.18470 |
| 960.021 |
0.31180 |
0.10010 |
| 1270.180 |
0.37900 |
0.16140 |
| 1077.780 |
0.40460 |
0.08660 |
| 1339.290 |
0.47790 |
0.13570 |
| 1119.010 |
0.50480 |
0.07200 |
| 1330.450 |
0.58750 |
0.10720 |
| 1085.390 |
0.61330 |
0.05620 |
| 1210.960 |
0.70920 |
0.07570 |
| 963.781 |
0.73110 |
0.03910 |
| 1068.320 |
0.77570 |
0.05830 |
| 823.484 |
0.79380 |
0.03000 |
| 823.293 |
0.79380 |
0.03000 |
| 883.140 |
0.84600 |
0.04000 |
| 888.220 |
0.84600 |
0.04000 |
| 667.124 |
0.85950 |
0.02040 |
| 655.403 |
0.85950 |
0.02040 |
| 545.550 |
0.92060 |
0.02060 |
| 538.610 |
0.92060 |
0.02060 |
| 401.438 |
0.92810 |
0.01050 |
| 395.999 |
0.92810 |
0.01050 |
| 330.330 |
0.95970 |
0.01050 |
| 220.814 |
0.96360 |
0.00530 |
| 224.610 |
0.96360 |
0.00530 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
| Source |
| Fischer K.; Gmehling J.: Influence of Water on the Vapor-Liquid Equilibria, Activity Coefficients at Infinite Dilution and Enthalpies of Mixing for Mixtures of n-Methyl-2-Pyrrolidone with C5 or C6 Hydrocarbons. Fluid Phase Equilib. 218 (2004) 69-76 |
Enthalpy of Mixing Data Set 9143
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
592-41-6 |
1-Hexene |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
| 3 |
C5H9NO |
99.133 |
872-50-4 |
N-Methyl-2-pyrrolidone |
Search the DDB for all data of this mixture
Miscibility gap: No
Constant Value
| Temperature |
363.150 |
K |
| Pressure |
8.000 |
bar |
Data Table
| hE [J/mol] |
x1 [mol/mol] |
x2 [mol/mol] |
| -345.778 |
0.06260 |
0.24360 |
| -71.903 |
0.06940 |
0.13530 |
| 80.984 |
0.13050 |
0.22600 |
| 262.221 |
0.14370 |
0.12450 |
| 394.073 |
0.20470 |
0.20670 |
| 515.448 |
0.22350 |
0.11290 |
| 628.568 |
0.28590 |
0.18560 |
| 707.653 |
0.30930 |
0.10040 |
| 773.789 |
0.37520 |
0.16240 |
| 811.451 |
0.40170 |
0.08700 |
| 832.090 |
0.47400 |
0.13670 |
| 829.729 |
0.50180 |
0.07240 |
| 778.684 |
0.58360 |
0.10820 |
| 776.737 |
0.61050 |
0.05660 |
| 644.827 |
0.70610 |
0.07640 |
| 624.737 |
0.72880 |
0.03940 |
| 460.536 |
0.84390 |
0.04060 |
| 393.673 |
0.85810 |
0.02060 |
| 357.288 |
0.91950 |
0.02090 |
| 234.904 |
0.92730 |
0.01060 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
| Source |
| Fischer K.; Gmehling J.: Influence of Water on the Vapor-Liquid Equilibria, Activity Coefficients at Infinite Dilution and Enthalpies of Mixing for Mixtures of n-Methyl-2-Pyrrolidone with C5 or C6 Hydrocarbons. Fluid Phase Equilib. 218 (2004) 69-76 |
List of All References
| Source |
| Fischer K.; Gmehling J.: Influence of Water on the Vapor-Liquid Equilibria, Activity Coefficients at Infinite Dilution and Enthalpies of Mixing for Mixtures of n-Methyl-2-Pyrrolidone with C5 or C6 Hydrocarbons. Fluid Phase Equilib. 218 (2004) 69-76 |
Excess Enthalpy Data Overview
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