Continuous purification of Candida antarctica lipase B using 3‐membrane adsorber periodic counter‐current chromatography

Abstract Batch chromatography has several disadvantages, such as insufficient utilization of the capacity of the resin, high buffer consumption and discontinuity. Considering the high costs for downstream processing, a continuously working chromatographic system with three membrane adsorber units wa...

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Bibliographic Details
Published in:Engineering in Life Sciences
Main Authors: Brämer, Chantal, Schreiber, Sarah, Scheper, Thomas, Beutel, Sascha
Other Authors: Bundesministerium für Bildung und Forschung
Format: Article in Journal/Newspaper
Language:English
Published: Wiley 2018
Subjects:
Online Access:http://dx.doi.org/10.1002/elsc.201700159
https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Felsc.201700159
https://onlinelibrary.wiley.com/doi/pdf/10.1002/elsc.201700159
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Summary:Abstract Batch chromatography has several disadvantages, such as insufficient utilization of the capacity of the resin, high buffer consumption and discontinuity. Considering the high costs for downstream processing, a continuously working chromatographic system with three membrane adsorber units was designed, tested and put into operation. The basic principle of the setup is periodic counter‐current chromatography (PCCC). The PCCC system was used for capturing and purifying Candida antarctica lipase B (CalB) directly from cell lysate in one single unit operation. The best purification result was achieved by means of anion‐exchange chromatography. The dynamic binding capacity with Sartobind® Q 75 amounted to 4.2 mg (56 g/cm 2 ). After transferring the method to the 3MA‐PCCC, 0.22 g CalB (73 U/mg) were obtained from 0.9 L E. coli lysate within 6 h and a recovery of 80%. Compared to the batch process, the productivity could be increased by 36% and the buffer consumption could be reduced by about 20%. Although the purification of CalB from lysate by means of anion‐exchange chromatography was not selective and quantitative using the 3MA‐PCCC device, it could be shown that the concept of the system was successfully implemented and led to a significant improvement of CalB purification.