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Continuous separation of protein loaded nanoparticles by simulated moving bed chromatography
For scale up and efficient production of protein loaded nanoparticles continuous separation by size exclusion chromatography in simulated moving bed (SMB) mode helps do reduce unbound protein concentration and increase yields for perfectly covered particles. Silica nanoparticles were loaded with an...
Autores principales: | , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
Elsevier
2014
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4048465/ https://www.ncbi.nlm.nih.gov/pubmed/24866563 http://dx.doi.org/10.1016/j.chroma.2014.04.093 |
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author | Satzer, Peter Wellhoefer, Martin Jungbauer, Alois |
author_facet | Satzer, Peter Wellhoefer, Martin Jungbauer, Alois |
author_sort | Satzer, Peter |
collection | PubMed |
description | For scale up and efficient production of protein loaded nanoparticles continuous separation by size exclusion chromatography in simulated moving bed (SMB) mode helps do reduce unbound protein concentration and increase yields for perfectly covered particles. Silica nanoparticles were loaded with an excess of beta casein or bovine serum albumin (BSA) and the loaded particles purified by size exclusion chromatography using Sephacryl300 as stationary phase in a four zone SMB. We determined our working points for the SMB from batch separations and the triangle theory described by Mazzotti et al. with an SMB setup of one Sephacryl300 26/70 mm column per zone with switch times of 5 min for BSA and 7 min for beta casein. In the case of BSA the Raffinate contained loaded nanoparticles of 63% purity with 98% recovery and the extract was essentially particle free (95% purity). We showed that the low purity of the Raffinate was only due to BSA multimers present in the used protein solution. In the case of beta casein where no multimers are present we achieved 89% purity and 90% recovery of loaded nanoparticles in the Raffinate and an extract free of particles (92% purity). Using a tangential flow filtration unit with 5 kDa cutoff membrane we proved that the extract can be concentrated for recycling of protein and buffer. The calculated space–time-yield for loaded nanoparticles was 0.25 g of loaded nanoparticles per hour and liter of used resin. This proves that the presented process is suitable for large scale production for industrial purposes. |
format | Online Article Text |
id | pubmed-4048465 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2014 |
publisher | Elsevier |
record_format | MEDLINE/PubMed |
spelling | pubmed-40484652014-07-04 Continuous separation of protein loaded nanoparticles by simulated moving bed chromatography Satzer, Peter Wellhoefer, Martin Jungbauer, Alois J Chromatogr A Article For scale up and efficient production of protein loaded nanoparticles continuous separation by size exclusion chromatography in simulated moving bed (SMB) mode helps do reduce unbound protein concentration and increase yields for perfectly covered particles. Silica nanoparticles were loaded with an excess of beta casein or bovine serum albumin (BSA) and the loaded particles purified by size exclusion chromatography using Sephacryl300 as stationary phase in a four zone SMB. We determined our working points for the SMB from batch separations and the triangle theory described by Mazzotti et al. with an SMB setup of one Sephacryl300 26/70 mm column per zone with switch times of 5 min for BSA and 7 min for beta casein. In the case of BSA the Raffinate contained loaded nanoparticles of 63% purity with 98% recovery and the extract was essentially particle free (95% purity). We showed that the low purity of the Raffinate was only due to BSA multimers present in the used protein solution. In the case of beta casein where no multimers are present we achieved 89% purity and 90% recovery of loaded nanoparticles in the Raffinate and an extract free of particles (92% purity). Using a tangential flow filtration unit with 5 kDa cutoff membrane we proved that the extract can be concentrated for recycling of protein and buffer. The calculated space–time-yield for loaded nanoparticles was 0.25 g of loaded nanoparticles per hour and liter of used resin. This proves that the presented process is suitable for large scale production for industrial purposes. Elsevier 2014-07-04 /pmc/articles/PMC4048465/ /pubmed/24866563 http://dx.doi.org/10.1016/j.chroma.2014.04.093 Text en © 2014 The Authors http://creativecommons.org/licenses/by-nc-nd/3.0/ This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/3.0/). |
spellingShingle | Article Satzer, Peter Wellhoefer, Martin Jungbauer, Alois Continuous separation of protein loaded nanoparticles by simulated moving bed chromatography |
title | Continuous separation of protein loaded nanoparticles by simulated moving bed chromatography |
title_full | Continuous separation of protein loaded nanoparticles by simulated moving bed chromatography |
title_fullStr | Continuous separation of protein loaded nanoparticles by simulated moving bed chromatography |
title_full_unstemmed | Continuous separation of protein loaded nanoparticles by simulated moving bed chromatography |
title_short | Continuous separation of protein loaded nanoparticles by simulated moving bed chromatography |
title_sort | continuous separation of protein loaded nanoparticles by simulated moving bed chromatography |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4048465/ https://www.ncbi.nlm.nih.gov/pubmed/24866563 http://dx.doi.org/10.1016/j.chroma.2014.04.093 |
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