Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor

Detalhes bibliográficos
Autor(a) principal: dos Santos, Marcela Colombo
Data de Publicação: 2022
Outros Autores: Cerri, Marcel O. [UNESP], Bicas, Juliano Lemos
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Institucional da UNESP
Texto Completo: http://dx.doi.org/10.1007/s00449-022-02693-0
http://hdl.handle.net/11449/223322
Resumo: This study involved evaluating the effects of rotational impeller speed agitation (N) and specific air flow rate (Фair) on bikaverin production and on the growth of Fusarium oxysporum employing 11 bench-scale bioreactor assays. The results showed that the maximum bikaverin production (close to 300 mg L−1) was achieved after 48 h of fermentation in rice medium (20 g L−1 milled rice in water) at 28 °C with a volumetric oxygen transfer coefficient (KLa) and shear stress values of approximately 20 h−1 and 17 N m−2, respectively. We reached this combination of parameters using an N of 340 rpm and Фair of 0.935 vvm. These KLa and shear stress values can be used as references when upscaling this process. Thus, this study was important to demonstrate how the main parameters in bioreactors affect bikaverin production and it presented important indications for upscaling this bioprocess.
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spelling Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactorBlue pigmentOptimizationScale-upShear stressVolumetric oxygen transfer coefficient (KLa)This study involved evaluating the effects of rotational impeller speed agitation (N) and specific air flow rate (Фair) on bikaverin production and on the growth of Fusarium oxysporum employing 11 bench-scale bioreactor assays. The results showed that the maximum bikaverin production (close to 300 mg L−1) was achieved after 48 h of fermentation in rice medium (20 g L−1 milled rice in water) at 28 °C with a volumetric oxygen transfer coefficient (KLa) and shear stress values of approximately 20 h−1 and 17 N m−2, respectively. We reached this combination of parameters using an N of 340 rpm and Фair of 0.935 vvm. These KLa and shear stress values can be used as references when upscaling this process. Thus, this study was important to demonstrate how the main parameters in bioreactors affect bikaverin production and it presented important indications for upscaling this bioprocess.Department of Food Science Faculty of Food Engineering State University of Campinas, Rua Monteiro Lobato, 80, SPDepartment of Bioprocess and Biotechnology UNESP Universidade Estadual Paulista, SPDepartment of Bioprocess and Biotechnology UNESP Universidade Estadual Paulista, SPUniversidade Estadual de Campinas (UNICAMP)Universidade Estadual Paulista (UNESP)dos Santos, Marcela ColomboCerri, Marcel O. [UNESP]Bicas, Juliano Lemos2022-04-28T19:50:01Z2022-04-28T19:50:01Z2022-01-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articlehttp://dx.doi.org/10.1007/s00449-022-02693-0Bioprocess and Biosystems Engineering.1615-76051615-7591http://hdl.handle.net/11449/22332210.1007/s00449-022-02693-02-s2.0-85123463570Scopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengBioprocess and Biosystems Engineeringinfo:eu-repo/semantics/openAccess2022-04-28T19:50:01Zoai:repositorio.unesp.br:11449/223322Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T23:17:28.983877Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false
dc.title.none.fl_str_mv Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor
title Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor
spellingShingle Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor
dos Santos, Marcela Colombo
Blue pigment
Optimization
Scale-up
Shear stress
Volumetric oxygen transfer coefficient (KLa)
title_short Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor
title_full Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor
title_fullStr Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor
title_full_unstemmed Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor
title_sort Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor
author dos Santos, Marcela Colombo
author_facet dos Santos, Marcela Colombo
Cerri, Marcel O. [UNESP]
Bicas, Juliano Lemos
author_role author
author2 Cerri, Marcel O. [UNESP]
Bicas, Juliano Lemos
author2_role author
author
dc.contributor.none.fl_str_mv Universidade Estadual de Campinas (UNICAMP)
Universidade Estadual Paulista (UNESP)
dc.contributor.author.fl_str_mv dos Santos, Marcela Colombo
Cerri, Marcel O. [UNESP]
Bicas, Juliano Lemos
dc.subject.por.fl_str_mv Blue pigment
Optimization
Scale-up
Shear stress
Volumetric oxygen transfer coefficient (KLa)
topic Blue pigment
Optimization
Scale-up
Shear stress
Volumetric oxygen transfer coefficient (KLa)
description This study involved evaluating the effects of rotational impeller speed agitation (N) and specific air flow rate (Фair) on bikaverin production and on the growth of Fusarium oxysporum employing 11 bench-scale bioreactor assays. The results showed that the maximum bikaverin production (close to 300 mg L−1) was achieved after 48 h of fermentation in rice medium (20 g L−1 milled rice in water) at 28 °C with a volumetric oxygen transfer coefficient (KLa) and shear stress values of approximately 20 h−1 and 17 N m−2, respectively. We reached this combination of parameters using an N of 340 rpm and Фair of 0.935 vvm. These KLa and shear stress values can be used as references when upscaling this process. Thus, this study was important to demonstrate how the main parameters in bioreactors affect bikaverin production and it presented important indications for upscaling this bioprocess.
publishDate 2022
dc.date.none.fl_str_mv 2022-04-28T19:50:01Z
2022-04-28T19:50:01Z
2022-01-01
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://dx.doi.org/10.1007/s00449-022-02693-0
Bioprocess and Biosystems Engineering.
1615-7605
1615-7591
http://hdl.handle.net/11449/223322
10.1007/s00449-022-02693-0
2-s2.0-85123463570
url http://dx.doi.org/10.1007/s00449-022-02693-0
http://hdl.handle.net/11449/223322
identifier_str_mv Bioprocess and Biosystems Engineering.
1615-7605
1615-7591
10.1007/s00449-022-02693-0
2-s2.0-85123463570
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Bioprocess and Biosystems Engineering
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.source.none.fl_str_mv Scopus
reponame:Repositório Institucional da UNESP
instname:Universidade Estadual Paulista (UNESP)
instacron:UNESP
instname_str Universidade Estadual Paulista (UNESP)
instacron_str UNESP
institution UNESP
reponame_str Repositório Institucional da UNESP
collection Repositório Institucional da UNESP
repository.name.fl_str_mv Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)
repository.mail.fl_str_mv
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