Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling Domań„ska, U.; Zawadzki, M.; Królikowski, M.; González, J.; Fluid Phase Equilibria 2014, 361, 116-129
Data
P = 101 kPa, T = 298.15 K
x (mol mol-1) HmE (kJ mol-1)
0.0150 0.2344
0.1543 1.0282
0.1692 1.068
0.1840 1.1035
0.1989 1.1369
0.2139 1.1672
0.2288 1.1952
0.2437 1.2204
0.2587 1.2437
0.2737 1.2648
0.2887 1.2841
0.0300 0.4145
0.3037 1.302
0.3186 1.3179
0.3337 1.3356
0.3485 1.3478
0.3677 1.3673
0.3829 1.3797
0.3982 1.3922
0.4135 1.402
0.4287 1.4099
0.4440 1.4162
0.0451 0.5479
0.4592 1.4212
0.4745 1.4247
0.4898 1.4268
0.5050 1.4275
0.5203 1.4267
0.5355 1.4244
0.5507 1.4207
0.5660 1.4152
0.5812 1.4083
0.5964 1.3996
0.0601 0.65
0.6116 1.3889
0.6269 1.3761
0.6421 1.3614
0.6573 1.3447
0.6725 1.3259
0.6878 1.3038
0.7030 1.2788
0.7182 1.245
0.7310 1.2101
0.7468 1.171
0.0752 0.7315
0.7627 1.127
0.7786 1.0844
0.7945 1.0378
0.8104 0.9871
0.8263 0.9323
0.8421 0.8731
0.8580 0.8083
0.8740 0.739
0.8899 0.6637
0.9058 0.583
0.0905 0.8041
0.9218 0.4959
0.9377 0.4027
0.9537 0.3036
0.9691 0.2013
0.9846 0.0929
0.1057 0.8674
0.1208 0.9243
0.1358 0.9731
5682; 1H-pyrrole + cyclohexane; 00031:01478