Recovery of phytase produced by solid-state fermentation on citrus peel
Autor(a) principal: | |
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Data de Publicação: | 2010 |
Outros Autores: | , , , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Brazilian Archives of Biology and Technology |
Texto Completo: | http://old.scielo.br/scielo.php?script=sci_arttext&pid=S1516-89132010000600026 |
Resumo: | The extraction of phytase produced by solid-state fermentation of citrus peel was studied employing a multistage leaching process. It was observed that the extracts containing EDTA retained over 90% of phytase activity at room temperature after 24 h after the leaching. A fractional design 2² (with 4 replicates at the central point) was carried out for testing the pH and agitation as process independent factors. Only the interaction between the pH and agitation showed a significant influence. These factors were optimized with a central composite design. Agitation at 300 rpm and pH at 5.0 were the best conditions to extract the enzyme from solid matrix. The modeling of the process indicated that diffusivity of the enzyme in the solvent was the controlling mechanism. The corresponding kinetic constant and saturation concentration in this process were 0.89 min-1 and 4.0 IU/mL, respectively. The multistage process indicated that after two steps, it was possible to recover 85% of total enzyme produced. |
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Brazilian Archives of Biology and Technology |
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Recovery of phytase produced by solid-state fermentation on citrus peelleachingrecovery multistagephytasesolid state fermentationkinetic modelsThe extraction of phytase produced by solid-state fermentation of citrus peel was studied employing a multistage leaching process. It was observed that the extracts containing EDTA retained over 90% of phytase activity at room temperature after 24 h after the leaching. A fractional design 2² (with 4 replicates at the central point) was carried out for testing the pH and agitation as process independent factors. Only the interaction between the pH and agitation showed a significant influence. These factors were optimized with a central composite design. Agitation at 300 rpm and pH at 5.0 were the best conditions to extract the enzyme from solid matrix. The modeling of the process indicated that diffusivity of the enzyme in the solvent was the controlling mechanism. The corresponding kinetic constant and saturation concentration in this process were 0.89 min-1 and 4.0 IU/mL, respectively. The multistage process indicated that after two steps, it was possible to recover 85% of total enzyme produced.Instituto de Tecnologia do Paraná - Tecpar2010-12-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S1516-89132010000600026Brazilian Archives of Biology and Technology v.53 n.6 2010reponame:Brazilian Archives of Biology and Technologyinstname:Instituto de Tecnologia do Paraná (Tecpar)instacron:TECPAR10.1590/S1516-89132010000600026info:eu-repo/semantics/openAccessRodríguez-Fernández,Daniel ErnestoRodríguez-León,José AngelCarvalho,Júlio Cesar deThomaz-Soccol,VaneteParada,José LuisSoccol,Carlos Ricardoeng2011-01-18T00:00:00Zoai:scielo:S1516-89132010000600026Revistahttps://www.scielo.br/j/babt/https://old.scielo.br/oai/scielo-oai.phpbabt@tecpar.br||babt@tecpar.br1678-43241516-8913opendoar:2011-01-18T00:00Brazilian Archives of Biology and Technology - Instituto de Tecnologia do Paraná (Tecpar)false |
dc.title.none.fl_str_mv |
Recovery of phytase produced by solid-state fermentation on citrus peel |
title |
Recovery of phytase produced by solid-state fermentation on citrus peel |
spellingShingle |
Recovery of phytase produced by solid-state fermentation on citrus peel Rodríguez-Fernández,Daniel Ernesto leaching recovery multistage phytase solid state fermentation kinetic models |
title_short |
Recovery of phytase produced by solid-state fermentation on citrus peel |
title_full |
Recovery of phytase produced by solid-state fermentation on citrus peel |
title_fullStr |
Recovery of phytase produced by solid-state fermentation on citrus peel |
title_full_unstemmed |
Recovery of phytase produced by solid-state fermentation on citrus peel |
title_sort |
Recovery of phytase produced by solid-state fermentation on citrus peel |
author |
Rodríguez-Fernández,Daniel Ernesto |
author_facet |
Rodríguez-Fernández,Daniel Ernesto Rodríguez-León,José Angel Carvalho,Júlio Cesar de Thomaz-Soccol,Vanete Parada,José Luis Soccol,Carlos Ricardo |
author_role |
author |
author2 |
Rodríguez-León,José Angel Carvalho,Júlio Cesar de Thomaz-Soccol,Vanete Parada,José Luis Soccol,Carlos Ricardo |
author2_role |
author author author author author |
dc.contributor.author.fl_str_mv |
Rodríguez-Fernández,Daniel Ernesto Rodríguez-León,José Angel Carvalho,Júlio Cesar de Thomaz-Soccol,Vanete Parada,José Luis Soccol,Carlos Ricardo |
dc.subject.por.fl_str_mv |
leaching recovery multistage phytase solid state fermentation kinetic models |
topic |
leaching recovery multistage phytase solid state fermentation kinetic models |
description |
The extraction of phytase produced by solid-state fermentation of citrus peel was studied employing a multistage leaching process. It was observed that the extracts containing EDTA retained over 90% of phytase activity at room temperature after 24 h after the leaching. A fractional design 2² (with 4 replicates at the central point) was carried out for testing the pH and agitation as process independent factors. Only the interaction between the pH and agitation showed a significant influence. These factors were optimized with a central composite design. Agitation at 300 rpm and pH at 5.0 were the best conditions to extract the enzyme from solid matrix. The modeling of the process indicated that diffusivity of the enzyme in the solvent was the controlling mechanism. The corresponding kinetic constant and saturation concentration in this process were 0.89 min-1 and 4.0 IU/mL, respectively. The multistage process indicated that after two steps, it was possible to recover 85% of total enzyme produced. |
publishDate |
2010 |
dc.date.none.fl_str_mv |
2010-12-01 |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S1516-89132010000600026 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S1516-89132010000600026 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/S1516-89132010000600026 |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
text/html |
dc.publisher.none.fl_str_mv |
Instituto de Tecnologia do Paraná - Tecpar |
publisher.none.fl_str_mv |
Instituto de Tecnologia do Paraná - Tecpar |
dc.source.none.fl_str_mv |
Brazilian Archives of Biology and Technology v.53 n.6 2010 reponame:Brazilian Archives of Biology and Technology instname:Instituto de Tecnologia do Paraná (Tecpar) instacron:TECPAR |
instname_str |
Instituto de Tecnologia do Paraná (Tecpar) |
instacron_str |
TECPAR |
institution |
TECPAR |
reponame_str |
Brazilian Archives of Biology and Technology |
collection |
Brazilian Archives of Biology and Technology |
repository.name.fl_str_mv |
Brazilian Archives of Biology and Technology - Instituto de Tecnologia do Paraná (Tecpar) |
repository.mail.fl_str_mv |
babt@tecpar.br||babt@tecpar.br |
_version_ |
1750318274384494592 |