Journal
BIOTECHNOLOGY PROGRESS
Volume 34, Issue 5, Pages 1149-1166Publisher
WILEY
DOI: 10.1002/btpr.2657
Keywords
aqueous biphasic system; polyethylene glycol; tri-potassium citrate; ionic liquid; extraction
Funding
- Iran National Science Foundation (INSF) [92018043]
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The potential of (polyethylene glycol 400 + potassium citrate} aqueous biphasic system (ABS) with ionic liquid (IL) 1-butyl-3-methylimidazolium bromide ([C(4)C(1)im]Br) as an adjuvant is examined for the extraction of c-phenylalanine (Phe), as a model biomolecule, at different temperatures and system compositions. The binodal curves and liquid-liquid equilibrium data were determined by the addition of 5 wt% IL to investigate its effect on phase diagrams and Phe partition coefficients. The results indicate that binodal curves of systems with and without IL are more deviated from each other with decreasing temperature. Moreover, IL has a high tendency to partition into the PEG-rich phase. This tendency increases with increasing temperature and system compositions. For Phe, the partition coefficients obtained in this work (K-phe approximate to 5.5-81.2) are significantly higher than those observed in other conventional PEG-inorganic salt ABS (K-phe approximate to 0.5-2.5), water-immiscible ILs twophase extraction systems (K-phe approximate to 0.02-1.2), or even, in the IL-based ABS with the same IL as the main phase-forming component (K-phe approximate to 3.2). The phase hydrophobicity, salting-out and t it stacking seem to be the main driving forces to affect the extraction aptitude of the studied ABS for Phe. Furthermore, the performance of using [C(4)C(1)im]Br as adjuvant to improve the partition of Phe in the studied ABS at different temperatures seems to be ruled by the differences in the phases hydrophobicities. Finally, the experimental tie lines and partition coefficients are accurately correlated using the NRTL model. (C) 2018 American Institute of Chemical Engineers
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