The influence of cell adsorbent interactions on protein adsorption in expanded beds

Autores
Fernandez Lahore, Hector; Geilenkirchen, S.; Boldt, K.; Nagel, A.; Kula, M. R.; Thömmes, J.
Año de publicación
2000
Idioma
inglés
Tipo de recurso
artículo
Estado
versión publicada
Descripción
Expanded bed adsorption (EBA) is a primary recovery operation allowing the adsorption of proteins directly from unclarified feedstock, e.g. culture suspensions, homogenates or crude extracts. Thus solid-liquid separation is combined with adsorptive purification in a single step. The concept of integration requires that the solid components of the feed solution are regarded as a part of the process, which influences stability, reproducibility, and overall performance. This aspect is investigated here at the example of the influence of presence and concentration of intact yeast cells (S. cerevisiae) on the adsorption of model proteins (hen egg white lysozyme and bovine serum albumin) to various stationary phases (cation and anion-exchange, hydrophobic interaction, immobilised metal affinity). The interaction of the cells with the adsorbents is determined qualitatively and quantitatively by a pulse response method as well as by a finite bath technique under different operating conditions. The consequence of these interactions for the stability of expanded beds in suspensions of varying cell concentration is measured by residence time distributions (RTDs) after tracer pulse injection (NaBr, LiCl). Analysis of the measured RTD by the PDE model allows the calculation of the fraction of perfectly fluidised bed (φ), a parameter which may be regarded as a critical quantity for the estimation of the quality of fluidisation of adsorbents in cell containing suspensions. The correlation between bed stability and performance is made by analysing the breakthrough of model proteins during adsorption from unclarified yeast culture broth. A clear relationship is found between the degree of cell/adsorbent interaction, bed stability in terms of the φ parameter, and the sorption efficiency. Only beds characterised by a φ; value larger than 0.8 in the presence of cells will show a conserved performance compared to adsorption from cell free solutions. A drop in φ, which is due to interactions of the fluidised adsorbent particles with cells from the feed, will directly result in a reduced breakthrough efficiency. The data presented highlight the importance of including the potential interaction of solid feedstock components and the expanded adsorbents into the design of EBA processes, as the interrelation found here is a key factor for the overall performance of EBA as a truly integrated operation. © 2000 Elsevier Science B.V.
Fil: Fernandez Lahore, Hector. Universitat Dusseldorf; Alemania. Consejo Nacional de Investigaciones Científicas y Técnicas; Argentina
Fil: Geilenkirchen, S.. Universitat Dusseldorf; Alemania
Fil: Boldt, K.. Universitat Dusseldorf; Alemania
Fil: Nagel, A.. Universitat Dusseldorf; Alemania
Fil: Kula, M. R.. Universitat Dusseldorf; Alemania
Fil: Thömmes, J.. Universitat Dusseldorf; Alemania
Materia
Adsorption
Cell Adhesion
Expanded Bed Adsorption
Proteins
Residence Time Distribution
Nivel de accesibilidad
acceso abierto
Condiciones de uso
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
Repositorio
CONICET Digital (CONICET)
Institución
Consejo Nacional de Investigaciones Científicas y Técnicas
OAI Identificador
oai:ri.conicet.gov.ar:11336/39158

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spelling The influence of cell adsorbent interactions on protein adsorption in expanded bedsFernandez Lahore, HectorGeilenkirchen, S.Boldt, K.Nagel, A.Kula, M. R.Thömmes, J.AdsorptionCell AdhesionExpanded Bed AdsorptionProteinsResidence Time DistributionExpanded bed adsorption (EBA) is a primary recovery operation allowing the adsorption of proteins directly from unclarified feedstock, e.g. culture suspensions, homogenates or crude extracts. Thus solid-liquid separation is combined with adsorptive purification in a single step. The concept of integration requires that the solid components of the feed solution are regarded as a part of the process, which influences stability, reproducibility, and overall performance. This aspect is investigated here at the example of the influence of presence and concentration of intact yeast cells (S. cerevisiae) on the adsorption of model proteins (hen egg white lysozyme and bovine serum albumin) to various stationary phases (cation and anion-exchange, hydrophobic interaction, immobilised metal affinity). The interaction of the cells with the adsorbents is determined qualitatively and quantitatively by a pulse response method as well as by a finite bath technique under different operating conditions. The consequence of these interactions for the stability of expanded beds in suspensions of varying cell concentration is measured by residence time distributions (RTDs) after tracer pulse injection (NaBr, LiCl). Analysis of the measured RTD by the PDE model allows the calculation of the fraction of perfectly fluidised bed (φ), a parameter which may be regarded as a critical quantity for the estimation of the quality of fluidisation of adsorbents in cell containing suspensions. The correlation between bed stability and performance is made by analysing the breakthrough of model proteins during adsorption from unclarified yeast culture broth. A clear relationship is found between the degree of cell/adsorbent interaction, bed stability in terms of the φ parameter, and the sorption efficiency. Only beds characterised by a φ; value larger than 0.8 in the presence of cells will show a conserved performance compared to adsorption from cell free solutions. A drop in φ, which is due to interactions of the fluidised adsorbent particles with cells from the feed, will directly result in a reduced breakthrough efficiency. The data presented highlight the importance of including the potential interaction of solid feedstock components and the expanded adsorbents into the design of EBA processes, as the interrelation found here is a key factor for the overall performance of EBA as a truly integrated operation. © 2000 Elsevier Science B.V.Fil: Fernandez Lahore, Hector. Universitat Dusseldorf; Alemania. Consejo Nacional de Investigaciones Científicas y Técnicas; ArgentinaFil: Geilenkirchen, S.. Universitat Dusseldorf; AlemaniaFil: Boldt, K.. Universitat Dusseldorf; AlemaniaFil: Nagel, A.. Universitat Dusseldorf; AlemaniaFil: Kula, M. R.. Universitat Dusseldorf; AlemaniaFil: Thömmes, J.. Universitat Dusseldorf; AlemaniaElsevier Science2000-03info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/39158Fernandez Lahore, Hector; Geilenkirchen, S.; Boldt, K.; Nagel, A.; Kula, M. R.; et al.; The influence of cell adsorbent interactions on protein adsorption in expanded beds; Elsevier Science; Journal of Chromatography - A; 873; 2; 3-2000; 195-2080021-9673CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/url/https://www.sciencedirect.com/science/article/pii/S0021967399013084info:eu-repo/semantics/altIdentifier/doi/10.1016/S0021-9673(99)01308-4info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-29T09:59:44Zoai:ri.conicet.gov.ar:11336/39158instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982025-09-29 09:59:45.282CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse
dc.title.none.fl_str_mv The influence of cell adsorbent interactions on protein adsorption in expanded beds
title The influence of cell adsorbent interactions on protein adsorption in expanded beds
spellingShingle The influence of cell adsorbent interactions on protein adsorption in expanded beds
Fernandez Lahore, Hector
Adsorption
Cell Adhesion
Expanded Bed Adsorption
Proteins
Residence Time Distribution
title_short The influence of cell adsorbent interactions on protein adsorption in expanded beds
title_full The influence of cell adsorbent interactions on protein adsorption in expanded beds
title_fullStr The influence of cell adsorbent interactions on protein adsorption in expanded beds
title_full_unstemmed The influence of cell adsorbent interactions on protein adsorption in expanded beds
title_sort The influence of cell adsorbent interactions on protein adsorption in expanded beds
dc.creator.none.fl_str_mv Fernandez Lahore, Hector
Geilenkirchen, S.
Boldt, K.
Nagel, A.
Kula, M. R.
Thömmes, J.
author Fernandez Lahore, Hector
author_facet Fernandez Lahore, Hector
Geilenkirchen, S.
Boldt, K.
Nagel, A.
Kula, M. R.
Thömmes, J.
author_role author
author2 Geilenkirchen, S.
Boldt, K.
Nagel, A.
Kula, M. R.
Thömmes, J.
author2_role author
author
author
author
author
dc.subject.none.fl_str_mv Adsorption
Cell Adhesion
Expanded Bed Adsorption
Proteins
Residence Time Distribution
topic Adsorption
Cell Adhesion
Expanded Bed Adsorption
Proteins
Residence Time Distribution
dc.description.none.fl_txt_mv Expanded bed adsorption (EBA) is a primary recovery operation allowing the adsorption of proteins directly from unclarified feedstock, e.g. culture suspensions, homogenates or crude extracts. Thus solid-liquid separation is combined with adsorptive purification in a single step. The concept of integration requires that the solid components of the feed solution are regarded as a part of the process, which influences stability, reproducibility, and overall performance. This aspect is investigated here at the example of the influence of presence and concentration of intact yeast cells (S. cerevisiae) on the adsorption of model proteins (hen egg white lysozyme and bovine serum albumin) to various stationary phases (cation and anion-exchange, hydrophobic interaction, immobilised metal affinity). The interaction of the cells with the adsorbents is determined qualitatively and quantitatively by a pulse response method as well as by a finite bath technique under different operating conditions. The consequence of these interactions for the stability of expanded beds in suspensions of varying cell concentration is measured by residence time distributions (RTDs) after tracer pulse injection (NaBr, LiCl). Analysis of the measured RTD by the PDE model allows the calculation of the fraction of perfectly fluidised bed (φ), a parameter which may be regarded as a critical quantity for the estimation of the quality of fluidisation of adsorbents in cell containing suspensions. The correlation between bed stability and performance is made by analysing the breakthrough of model proteins during adsorption from unclarified yeast culture broth. A clear relationship is found between the degree of cell/adsorbent interaction, bed stability in terms of the φ parameter, and the sorption efficiency. Only beds characterised by a φ; value larger than 0.8 in the presence of cells will show a conserved performance compared to adsorption from cell free solutions. A drop in φ, which is due to interactions of the fluidised adsorbent particles with cells from the feed, will directly result in a reduced breakthrough efficiency. The data presented highlight the importance of including the potential interaction of solid feedstock components and the expanded adsorbents into the design of EBA processes, as the interrelation found here is a key factor for the overall performance of EBA as a truly integrated operation. © 2000 Elsevier Science B.V.
Fil: Fernandez Lahore, Hector. Universitat Dusseldorf; Alemania. Consejo Nacional de Investigaciones Científicas y Técnicas; Argentina
Fil: Geilenkirchen, S.. Universitat Dusseldorf; Alemania
Fil: Boldt, K.. Universitat Dusseldorf; Alemania
Fil: Nagel, A.. Universitat Dusseldorf; Alemania
Fil: Kula, M. R.. Universitat Dusseldorf; Alemania
Fil: Thömmes, J.. Universitat Dusseldorf; Alemania
description Expanded bed adsorption (EBA) is a primary recovery operation allowing the adsorption of proteins directly from unclarified feedstock, e.g. culture suspensions, homogenates or crude extracts. Thus solid-liquid separation is combined with adsorptive purification in a single step. The concept of integration requires that the solid components of the feed solution are regarded as a part of the process, which influences stability, reproducibility, and overall performance. This aspect is investigated here at the example of the influence of presence and concentration of intact yeast cells (S. cerevisiae) on the adsorption of model proteins (hen egg white lysozyme and bovine serum albumin) to various stationary phases (cation and anion-exchange, hydrophobic interaction, immobilised metal affinity). The interaction of the cells with the adsorbents is determined qualitatively and quantitatively by a pulse response method as well as by a finite bath technique under different operating conditions. The consequence of these interactions for the stability of expanded beds in suspensions of varying cell concentration is measured by residence time distributions (RTDs) after tracer pulse injection (NaBr, LiCl). Analysis of the measured RTD by the PDE model allows the calculation of the fraction of perfectly fluidised bed (φ), a parameter which may be regarded as a critical quantity for the estimation of the quality of fluidisation of adsorbents in cell containing suspensions. The correlation between bed stability and performance is made by analysing the breakthrough of model proteins during adsorption from unclarified yeast culture broth. A clear relationship is found between the degree of cell/adsorbent interaction, bed stability in terms of the φ parameter, and the sorption efficiency. Only beds characterised by a φ; value larger than 0.8 in the presence of cells will show a conserved performance compared to adsorption from cell free solutions. A drop in φ, which is due to interactions of the fluidised adsorbent particles with cells from the feed, will directly result in a reduced breakthrough efficiency. The data presented highlight the importance of including the potential interaction of solid feedstock components and the expanded adsorbents into the design of EBA processes, as the interrelation found here is a key factor for the overall performance of EBA as a truly integrated operation. © 2000 Elsevier Science B.V.
publishDate 2000
dc.date.none.fl_str_mv 2000-03
dc.type.none.fl_str_mv info:eu-repo/semantics/article
info:eu-repo/semantics/publishedVersion
http://purl.org/coar/resource_type/c_6501
info:ar-repo/semantics/articulo
format article
status_str publishedVersion
dc.identifier.none.fl_str_mv http://hdl.handle.net/11336/39158
Fernandez Lahore, Hector; Geilenkirchen, S.; Boldt, K.; Nagel, A.; Kula, M. R.; et al.; The influence of cell adsorbent interactions on protein adsorption in expanded beds; Elsevier Science; Journal of Chromatography - A; 873; 2; 3-2000; 195-208
0021-9673
CONICET Digital
CONICET
url http://hdl.handle.net/11336/39158
identifier_str_mv Fernandez Lahore, Hector; Geilenkirchen, S.; Boldt, K.; Nagel, A.; Kula, M. R.; et al.; The influence of cell adsorbent interactions on protein adsorption in expanded beds; Elsevier Science; Journal of Chromatography - A; 873; 2; 3-2000; 195-208
0021-9673
CONICET Digital
CONICET
dc.language.none.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv info:eu-repo/semantics/altIdentifier/url/https://www.sciencedirect.com/science/article/pii/S0021967399013084
info:eu-repo/semantics/altIdentifier/doi/10.1016/S0021-9673(99)01308-4
dc.rights.none.fl_str_mv info:eu-repo/semantics/openAccess
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
eu_rights_str_mv openAccess
rights_invalid_str_mv https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.format.none.fl_str_mv application/pdf
application/pdf
dc.publisher.none.fl_str_mv Elsevier Science
publisher.none.fl_str_mv Elsevier Science
dc.source.none.fl_str_mv reponame:CONICET Digital (CONICET)
instname:Consejo Nacional de Investigaciones Científicas y Técnicas
reponame_str CONICET Digital (CONICET)
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instname_str Consejo Nacional de Investigaciones Científicas y Técnicas
repository.name.fl_str_mv CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas
repository.mail.fl_str_mv dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar
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