Scale-Up of Capsular Polysaccharide Production Process by Haemophilus influenzae Type b Using kLa Criterion

Descripción del Articulo

Polyribosyl-ribitol-phosphate (PRP) from Haemophilus influenzae type b (Hib) is an active immunizing molecule used in the production of the vaccine against H. influenzae, and industrial production could contribute to satisfying a world demand especially in developing countries. In this sense, the ai...

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Detalles Bibliográficos
Autores: Pillaca-Pullo, Omar, Dias Vieira , Lucas, Takagi , Mickie
Formato: artículo
Fecha de Publicación:2022
Institución:Universidad Privada Norbert Wiener
Repositorio:UWIENER-Institucional
Lenguaje:inglés
OAI Identifier:oai:repositorio.uwiener.edu.pe:20.500.13053/7192
Enlace del recurso:https://hdl.handle.net/20.500.13053/7192
https://doi.org/10.3390/bioengineering9090415
Nivel de acceso:acceso abierto
Materia:Haemophilus influenzae; polysaccharide; kLa; batch mode; fed-batch mode
http://purl.org/pe-repo/ocde/ford#3.03.00
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dc.title.es_ES.fl_str_mv Scale-Up of Capsular Polysaccharide Production Process by Haemophilus influenzae Type b Using kLa Criterion
title Scale-Up of Capsular Polysaccharide Production Process by Haemophilus influenzae Type b Using kLa Criterion
spellingShingle Scale-Up of Capsular Polysaccharide Production Process by Haemophilus influenzae Type b Using kLa Criterion
Pillaca-Pullo, Omar
Haemophilus influenzae; polysaccharide; kLa; batch mode; fed-batch mode
http://purl.org/pe-repo/ocde/ford#3.03.00
title_short Scale-Up of Capsular Polysaccharide Production Process by Haemophilus influenzae Type b Using kLa Criterion
title_full Scale-Up of Capsular Polysaccharide Production Process by Haemophilus influenzae Type b Using kLa Criterion
title_fullStr Scale-Up of Capsular Polysaccharide Production Process by Haemophilus influenzae Type b Using kLa Criterion
title_full_unstemmed Scale-Up of Capsular Polysaccharide Production Process by Haemophilus influenzae Type b Using kLa Criterion
title_sort Scale-Up of Capsular Polysaccharide Production Process by Haemophilus influenzae Type b Using kLa Criterion
author Pillaca-Pullo, Omar
author_facet Pillaca-Pullo, Omar
Dias Vieira , Lucas
Takagi , Mickie
author_role author
author2 Dias Vieira , Lucas
Takagi , Mickie
author2_role author
author
dc.contributor.author.fl_str_mv Pillaca-Pullo, Omar
Dias Vieira , Lucas
Takagi , Mickie
dc.subject.es_ES.fl_str_mv Haemophilus influenzae; polysaccharide; kLa; batch mode; fed-batch mode
topic Haemophilus influenzae; polysaccharide; kLa; batch mode; fed-batch mode
http://purl.org/pe-repo/ocde/ford#3.03.00
dc.subject.ocde.es_ES.fl_str_mv http://purl.org/pe-repo/ocde/ford#3.03.00
description Polyribosyl-ribitol-phosphate (PRP) from Haemophilus influenzae type b (Hib) is an active immunizing molecule used in the production of the vaccine against H. influenzae, and industrial production could contribute to satisfying a world demand especially in developing countries. In this sense, the aim of this study was to establish a scale-up process using the constant oxygen mass transfer coefficient (kLa) such as the criterion for production of PRP in three different sizes of bioreactor systems. Three different kLa values (24, 52 and 80 h−1) were evaluated in which the biological influence in a 1.5 L bioreactor and 52 h−1 was selected to scale-up the production process until a 75 L pilot-scale bioreactor was achieved. Finally, the fed-batch phase was started under a dissolved oxygen concentration (pO2) at 30% of the saturation in the 75 L bioreactor to avoid oxygen limitation; the performance of production presented high efficiency (9.0 g/L DCW-dry cell weight and 1.4 g/L PRP) in comparison with previous scale-up studies. The yields, productivity and kinetic behavior were similar in the three-size bioreactor systems in the batch mode indicating that kLa is possible to use for PRP production at large scales. This process operated under two stages and successfully produced DCW and PRP in the pilot scale and could be beneficial for future bioprocess operations that may lead to higher production and less operative cost. View Full-Text
publishDate 2022
dc.date.accessioned.none.fl_str_mv 2022-11-22T22:12:05Z
dc.date.available.none.fl_str_mv 2022-11-22T22:12:05Z
dc.date.issued.fl_str_mv 2022-08-25
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url https://hdl.handle.net/20.500.13053/7192
https://doi.org/10.3390/bioengineering9090415
dc.language.iso.es_ES.fl_str_mv eng
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spelling Pillaca-Pullo, OmarDias Vieira , LucasTakagi , Mickie2022-11-22T22:12:05Z2022-11-22T22:12:05Z2022-08-25https://hdl.handle.net/20.500.13053/7192https://doi.org/10.3390/bioengineering9090415Polyribosyl-ribitol-phosphate (PRP) from Haemophilus influenzae type b (Hib) is an active immunizing molecule used in the production of the vaccine against H. influenzae, and industrial production could contribute to satisfying a world demand especially in developing countries. In this sense, the aim of this study was to establish a scale-up process using the constant oxygen mass transfer coefficient (kLa) such as the criterion for production of PRP in three different sizes of bioreactor systems. Three different kLa values (24, 52 and 80 h−1) were evaluated in which the biological influence in a 1.5 L bioreactor and 52 h−1 was selected to scale-up the production process until a 75 L pilot-scale bioreactor was achieved. Finally, the fed-batch phase was started under a dissolved oxygen concentration (pO2) at 30% of the saturation in the 75 L bioreactor to avoid oxygen limitation; the performance of production presented high efficiency (9.0 g/L DCW-dry cell weight and 1.4 g/L PRP) in comparison with previous scale-up studies. The yields, productivity and kinetic behavior were similar in the three-size bioreactor systems in the batch mode indicating that kLa is possible to use for PRP production at large scales. This process operated under two stages and successfully produced DCW and PRP in the pilot scale and could be beneficial for future bioprocess operations that may lead to higher production and less operative cost. 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