Table S8. Partition coefficients, efficiency extraction results and respective standard deviations obtained with the ternary system composed of methanol + K2HPO4/KH2PO4 (17.5 wt%) + H2O, at 298 (±1) K. Mass fraction percentage Kcaf ± std RB ± std of methanol (wt%) 0.606 ± 0.001 44.9 ± 0.1 40.0 0.351 ± 0.001 55.8 ± 0.1 45.0 0.2882 ± 0.0009 56.9 ± 0.1 50.0 0.2066 ± 0.0007 62.7 ± 0.1 55.0 0.202 ± 0.002 63.7 ± 0.2 60.0 Table S9. Partition coefficients, extraction efficiency results and respective standard deviations obtained with the ternary system composed of methanol (60.0 wt%) + K2HPO4/KH2PO4 (17.5 wt%) + H2O (22.5 wt%), at different temperatures. Temperature (±1) K Kcaf ± std RB ± std 0.0592 ± 0.0009 81.1 ± 0.2 278 0.079 ± 0.001 68.3 ± 0.3 293 0.095 ± 0.001 64.6 ± 0.3 298 0.123 ± 0.002 57.6 ± 0.3 308
Table S8. Partition coefficients, efficiency extraction results and respective standard deviations obtained with the ternary system composed of methanol + K2HPO4/KH2PO4 (17.5 wt%) + H2O, at 298 (±1) K. Mass fraction percentage of methanol (wt%) Kcaf ± std RB ± std 40.0 0.606 ± 0.001 44.9 ± 0.1 45.0 0.351 ± 0.001 55.8 ± 0.1 50.0 0.2882 ± 0.0009 56.9 ± 0.1 55.0 0.2066 ± 0.0007 62.7 ± 0.1 60.0 0.202 ± 0.002 63.7 ± 0.2 Table S9. Partition coefficients, extraction efficiency results and respective standard deviations obtained with the ternary system composed of methanol (60.0 wt%) + K2HPO4/KH2PO4 (17.5 wt%) + H2O (22.5 wt%), at different temperatures. Temperature (±1) K Kcaf ± std RB ± std 278 0.0592 ± 0.0009 81.1 ± 0.2 293 0.079 ± 0.001 68.3 ± 0.3 298 0.095 ± 0.001 64.6 ± 0.3 308 0.123 ± 0.002 57.6 ± 0.3
01496395.2016.1199569_SI.docx