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)
0.8852 288.0
0.6386 342.9
0.6002 348.0
0.5702 350.8
0.5108 358.2
0.4587 363.7
0.0155 357.1
0.0135 356.0
0.0102 352.7
0.0066 344.7
0.0044 325.3
0.8643 296.5
0.8394 303.3
0.8196 309.3
0.7970 315.6
0.7595 322.0
0.7473 327.1
0.7015 334.3
0.6824 337.4
35599; decan-1-ol + 1-hexyl-1-methylpyrrolidinium bis(trifluoromethanesulfonyl)imide; 00047:02465