Using Ionic Liquids To Tune the Performance of Aqueous Biphasic Systems Based on Pluronic L‑35 for the Purification of Naringin and Rutin

Aqueous biphasic systems (ABS) based on Pluronic L-35, a (EO) x -(PO) y -(EO) x triblock copolymer, were determined and applied in the separation of two structurally similar flavonoids (naringin and rutin). Two sets of phase formers were paired with Pluronic L-35, one comprising conventional salts/b...

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Bibliographic Details
Published in:	ACS sustainable chemistry & engineering Vol. 5; no. 8; pp. 6409 - 6419
Main Authors:	e Silva, Francisca A, Carmo, Rui M. C, Fernandes, Andreia P. M, Kholany, Mariam, Coutinho, João A. P, Ventura, Sónia P. M
Format:	Journal Article
Language:	English
Published:	American Chemical Society 07-08-2017
Subjects:	Aqueous biphasic systems Purification Naringin Ionic liquids Copolymer Rutin Flavonoid
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Summary:	Aqueous biphasic systems (ABS) based on Pluronic L-35, a (EO) x -(PO) y -(EO) x triblock copolymer, were determined and applied in the separation of two structurally similar flavonoids (naringin and rutin). Two sets of phase formers were paired with Pluronic L-35, one comprising conventional salts/buffer and other including cholinium-based ionic liquids (ILs). It is shown that while the conventional salts induce an unbalanced and strong salting out leading to complete extraction of flavonoids to the same phase in most of the cases (84.7 ± 0.6% ≤ R NAR ≤ 100% and 53.2 ± 0.5% ≤ R RUT ≤ 99.7 ± 0.1% with selectivities ranging from 1 to 11.8), the cholinium-based ILs provide an enhanced extractive performance. Indeed, these novel cholinium ILs/Pluronic L-35-based ABS allowed the manipulation of the affinity of both naringin and rutin to opposite phases, thus yielding a selective separation. The best results were achieved for the system using [Ch][Bic] as phase former (R NAR = 89.6 ± 0.3 and R RUT = 32 ± 2 with a selectivity of 18.9). An integrated approach based on the sequential implementation of Na2SO4/Pluronic L-35- (step 1) and [Ch][Bic]/Pluronic L-35-based (step 2) ABS was designed to purify the flavonoids from a complex synthetic mixture simulating natural extracts. Remarkably, glucose (the main contaminant) was removed during step 1 with an extraction efficiency of 60 ± 4% to the Na2SO4-rich phase, while step 2 has enabled the efficient separation of naringin from rutin.
ISSN:	2168-0485 2168-0485
DOI:	10.1021/acssuschemeng.7b00178