Relation of shear stress and K L a on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor
Autor(a) principal: | |
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Data de Publicação: | 2022 |
Outros Autores: | , |
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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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/requestrepositoriounesp@unesp.bropendoar:29462022-04-28T19:50:01Repositório 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 |
repositoriounesp@unesp.br |
_version_ |
1826304588206047232 |