Efficient purification of the antimicrobial peptide ε-poly-L-lysine from microbial culture medium with continuous ion-exchange chromatography
•Strong acid cation resin was introduced to adsorb ε-PL for the first time.•Continuous ion-chromatography was successfully developed to purify ε-PL.•ε-PL purity was attained by 96.57% with recovery ratio of 73.10% after purification.•This novel strategy provides a sustainable approach for ε-PL bioma...
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Veröffentlicht in: | Separation and purification technology 2024-07, Vol.339, p.126608, Article 126608 |
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Sprache: | eng |
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Zusammenfassung: | •Strong acid cation resin was introduced to adsorb ε-PL for the first time.•Continuous ion-chromatography was successfully developed to purify ε-PL.•ε-PL purity was attained by 96.57% with recovery ratio of 73.10% after purification.•This novel strategy provides a sustainable approach for ε-PL biomanufacturing.
ε-Poly-L-lysine (ε-PL) is an added-value biopolymer for wide potential applications in food, pharmaceutical, biomaterial, and other industries, which is primarily manufactured through ion-exchange chromatography adsorption from a microbial culture medium. However, the high production cost in the ε-PL downstream limits its application. In this study, the strong acid cation resin SQD-04 was first developed to recover ε-PL from a clarified microbial culture medium. Subsequently, efficient sequential four-column chromatography (SFCC) rather than batch (single-column) chromatography was developed to purify ε-PL. During SFCC adsorption, specific optimal adsorption conditions (ε-PL concentration of 35 g/L, flow rate of 1 BV/h, and ε-PL breakthrough percentage of 60 %) were optimized through orthogonal experiments. Finally, the constructed SFCC process achieved 75.11 % purity with 94.25 % recovery for separating ε-PL from clarified microbial culture medium and offered several advantages, including higher inlet ε-PL concentration (35 g/L), higher adsorption capacity (244.34 mg/g), higher resin utilization (84.69 %), lower water consumption (51.60 % saving), and lower alkali consumption (58.86 % saving) over batch ion-exchange chromatography. After further purification through decoloration and ultrafiltration, a final ε-PL purity of 96.57 % was attained with a total recovery ratio of 73.10 %. The study demonstrated that continuous ion-exchange chromatography could provide great industrial benefits for ε-PL and other biological products. |
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ISSN: | 1383-5866 1873-3794 |
DOI: | 10.1016/j.seppur.2024.126608 |