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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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
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spelling crwiley:10.1002/elsc.201700159 2024-06-02T07:58:26+00:00 Continuous purification of Candida antarctica lipase B using 3‐membrane adsorber periodic counter‐current chromatography Brämer, Chantal Schreiber, Sarah Scheper, Thomas Beutel, Sascha Bundesministerium für Bildung und Forschung 2018 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 en eng Wiley http://onlinelibrary.wiley.com/termsAndConditions#vor Engineering in Life Sciences volume 18, issue 7, page 414-424 ISSN 1618-0240 1618-2863 journal-article 2018 crwiley https://doi.org/10.1002/elsc.201700159 2024-05-03T11:00:02Z 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. Article in Journal/Newspaper Antarc* Antarctica Wiley Online Library Engineering in Life Sciences 18 7 414 424
institution Open Polar
collection Wiley Online Library
op_collection_id crwiley
language English
description 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.
author2 Bundesministerium für Bildung und Forschung
format Article in Journal/Newspaper
author Brämer, Chantal
Schreiber, Sarah
Scheper, Thomas
Beutel, Sascha
spellingShingle Brämer, Chantal
Schreiber, Sarah
Scheper, Thomas
Beutel, Sascha
Continuous purification of Candida antarctica lipase B using 3‐membrane adsorber periodic counter‐current chromatography
author_facet Brämer, Chantal
Schreiber, Sarah
Scheper, Thomas
Beutel, Sascha
author_sort Brämer, Chantal
title Continuous purification of Candida antarctica lipase B using 3‐membrane adsorber periodic counter‐current chromatography
title_short Continuous purification of Candida antarctica lipase B using 3‐membrane adsorber periodic counter‐current chromatography
title_full Continuous purification of Candida antarctica lipase B using 3‐membrane adsorber periodic counter‐current chromatography
title_fullStr Continuous purification of Candida antarctica lipase B using 3‐membrane adsorber periodic counter‐current chromatography
title_full_unstemmed Continuous purification of Candida antarctica lipase B using 3‐membrane adsorber periodic counter‐current chromatography
title_sort continuous purification of candida antarctica lipase b using 3‐membrane adsorber periodic counter‐current chromatography
publisher Wiley
publishDate 2018
url 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
genre Antarc*
Antarctica
genre_facet Antarc*
Antarctica
op_source Engineering in Life Sciences
volume 18, issue 7, page 414-424
ISSN 1618-0240 1618-2863
op_rights http://onlinelibrary.wiley.com/termsAndConditions#vor
op_doi https://doi.org/10.1002/elsc.201700159
container_title Engineering in Life Sciences
container_volume 18
container_issue 7
container_start_page 414
op_container_end_page 424
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