Simultaneous extraction of basic and non-basic N-compounds
from
oil is still a big challenge. Triethylene glycol (TEG) encounters
very weak Brønsted acidity. Its N-distribution coefficient [D
N, (mmol·gEx
–1)/(mmol·gOil
–1)] for the basic
was below 7.0. In this work, metals dissolved in TEG can improve the
Lewis acidity of the extractant and bring about the simultaneous removal.
For example, D
N of TEG–Ag(I) can
increase to 40.5 for quinoline and 57.9 for pyridine, respectively.
For the non-basic, it still remained higher than 70.0. The promoted
performance was ascribed to the improvement of extractive behavior
of the basic. From TEG to TEG–Ag(I), first, the distribution
of equilibrium N-concentrations between two phases was significantly
changed from the straight line to the non-linear curve with the plateau.
Second, the interaction type inside the system was optimized. The
Ag(I)-based complexation coupled with the TEG-based H-bonding was
identified. Third, the interaction intensity was increased as well.
Ag(I) contributed much to reduction of Gibbs free energy change for
the basic. Therefore, enhancing Lewis acidity of the extractant was
a feasible way for the extraction of the N-compounds.