Designing eutectic mixtures for the extraction of 2-phenylethanol (PEA) from aqueous phase Domań„ska, U.; Wič™ckowski, M.; Okuniewska, P.; Fluid Phase Equilibria 2017, 447, 84-94
Data
P = 101 kPa
x (mol mol-1) TLLE (K)
0.6287 271.3
0.1912 310.2
0.1592 310.9
0.1237 311.3
0.0967 311.4
0.0689 311.3
0.0517 310.9
0.0392 309.9
0.0285 308.0
0.0200 305.7
0.0137 302.9
0.5608 276.6
0.0014 289.4
0.5055 282.7
0.4663 286.4
0.4320 290.5
0.4024 293.5
0.3766 296.4
0.3040 303.4
0.2381 308.3
35600; 2-methyl-1-butanol + 1-hexyl-1-methylpyrrolidinium bis(trifluoromethanesulfonyl)imide; 00759:02465