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)
0.7694 262.2
0.4343 314.0
0.3915 317.8
0.3443 323.0
0.2867 327.0
0.2366 330.7
0.2104 332.4
0.1654 333.7
0.1404 333.8
0.1243 334.0
0.0998 334.0
0.7291 271.0
0.0784 333.8
0.0625 333.4
0.0493 332.5
0.0378 331.2
0.0304 329.6
0.0210 325.7
0.0159 322.3
0.0090 315.1
0.7009 280.8
0.6676 284.9
0.6380 289.9
0.6002 294.8
0.5654 299.5
0.5277 303.4
0.4783 305.6
35592; 2-methyl-1-butanol + 1-butyl-1-methylpyrrolidinium bis[(trifluoromethyl)sulfonyl]imide; 00551:00759