Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor

Detalhes bibliográficos
Autor(a) principal: Wanderley, Carlos Ronald Pessoa
Data de Publicação: 2018
Outros Autores: Andrade, Marcus Vinícius, Pereira, Luciana, Silva, G., Pessoa, Kelly Rodrigues
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/1822/65840
Resumo: The mineralization of the azo dye congo red by the fungi Phanerochaete chrysosporium was studied in two sequential batch bioreactors (R1 and R2), operated in cycles of 48 h (step I) and 24 h (step II). In step I, glucose concentration was 1 g.L-1 in both reactors and in step II, 1 g.L-1 of glucose was maintained in R1, but R2 received no addition of glucose. In step I, the average dye removal efficiencies were 76 ± 29 % (R1) and 53 ± 15% (R2), while in step II the averages recorded for dye removal for R1 and R2 were 84 ± 15 and 70 ± 28%, respectively. The rates of dye removal were 0.04 h-1 in R1 and 0.03 h-1 in R2 in step I. Higher rates were obtained in step II, 0,07 h-1 and 0,02 h-1 for R1 and R2, respectively. The highest dye removal occurred in R1 and, in R2, the residual dye was further removed. Laccase was the oxidised at higher amount, in step I was 54 mol.min-1 for R1 and 38 molmin-1 for R2. The proposed treatment system was very effective in removing the azo dye, however the mineralization may not be complete and some by-products may have been formed, according to spectrofotometric analysis, were the peak corresponding to benzene, 220 nm, persisted.
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spelling Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactorBiodegradationCongo redPhanerochaete chrysosporiumSequential bioreactorsScience & TechnologyThe mineralization of the azo dye congo red by the fungi Phanerochaete chrysosporium was studied in two sequential batch bioreactors (R1 and R2), operated in cycles of 48 h (step I) and 24 h (step II). In step I, glucose concentration was 1 g.L-1 in both reactors and in step II, 1 g.L-1 of glucose was maintained in R1, but R2 received no addition of glucose. In step I, the average dye removal efficiencies were 76 ± 29 % (R1) and 53 ± 15% (R2), while in step II the averages recorded for dye removal for R1 and R2 were 84 ± 15 and 70 ± 28%, respectively. The rates of dye removal were 0.04 h-1 in R1 and 0.03 h-1 in R2 in step I. Higher rates were obtained in step II, 0,07 h-1 and 0,02 h-1 for R1 and R2, respectively. The highest dye removal occurred in R1 and, in R2, the residual dye was further removed. Laccase was the oxidised at higher amount, in step I was 54 mol.min-1 for R1 and 38 molmin-1 for R2. The proposed treatment system was very effective in removing the azo dye, however the mineralization may not be complete and some by-products may have been formed, according to spectrofotometric analysis, were the peak corresponding to benzene, 220 nm, persisted.Acknowledges to the National Council for Scientific and Technological Development (CNPq) - Brazil for financial assistance Process no. 479374/2012-0.info:eu-repo/semantics/publishedVersionInstituto de Tecnologia do Paraná - TECPARUniversidade do MinhoWanderley, Carlos Ronald PessoaAndrade, Marcus ViníciusPereira, LucianaSilva, G.Pessoa, Kelly Rodrigues2018-11-292018-11-29T00:00:00Zinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/1822/65840engWanderley, Carlos Ronald Pessoa; Andrade, Marcus Vinícius; Pereira, Luciana; Silva, G.; Pessoa, Kelly Rodrigues, Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor. Brazilian Archives of Biology and Technology, 61(e18180195), 20181516-891310.1590/1678-4324-2018180195http://www.scielo.br/revistas/babt/iaboutj.htminfo:eu-repo/semantics/openAccessreponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãoinstacron:RCAAP2023-07-21T12:06:19ZPortal AgregadorONG
dc.title.none.fl_str_mv Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor
title Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor
spellingShingle Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor
Wanderley, Carlos Ronald Pessoa
Biodegradation
Congo red
Phanerochaete chrysosporium
Sequential bioreactors
Science & Technology
title_short Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor
title_full Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor
title_fullStr Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor
title_full_unstemmed Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor
title_sort Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor
author Wanderley, Carlos Ronald Pessoa
author_facet Wanderley, Carlos Ronald Pessoa
Andrade, Marcus Vinícius
Pereira, Luciana
Silva, G.
Pessoa, Kelly Rodrigues
author_role author
author2 Andrade, Marcus Vinícius
Pereira, Luciana
Silva, G.
Pessoa, Kelly Rodrigues
author2_role author
author
author
author
dc.contributor.none.fl_str_mv Universidade do Minho
dc.contributor.author.fl_str_mv Wanderley, Carlos Ronald Pessoa
Andrade, Marcus Vinícius
Pereira, Luciana
Silva, G.
Pessoa, Kelly Rodrigues
dc.subject.por.fl_str_mv Biodegradation
Congo red
Phanerochaete chrysosporium
Sequential bioreactors
Science & Technology
topic Biodegradation
Congo red
Phanerochaete chrysosporium
Sequential bioreactors
Science & Technology
description The mineralization of the azo dye congo red by the fungi Phanerochaete chrysosporium was studied in two sequential batch bioreactors (R1 and R2), operated in cycles of 48 h (step I) and 24 h (step II). In step I, glucose concentration was 1 g.L-1 in both reactors and in step II, 1 g.L-1 of glucose was maintained in R1, but R2 received no addition of glucose. In step I, the average dye removal efficiencies were 76 ± 29 % (R1) and 53 ± 15% (R2), while in step II the averages recorded for dye removal for R1 and R2 were 84 ± 15 and 70 ± 28%, respectively. The rates of dye removal were 0.04 h-1 in R1 and 0.03 h-1 in R2 in step I. Higher rates were obtained in step II, 0,07 h-1 and 0,02 h-1 for R1 and R2, respectively. The highest dye removal occurred in R1 and, in R2, the residual dye was further removed. Laccase was the oxidised at higher amount, in step I was 54 mol.min-1 for R1 and 38 molmin-1 for R2. The proposed treatment system was very effective in removing the azo dye, however the mineralization may not be complete and some by-products may have been formed, according to spectrofotometric analysis, were the peak corresponding to benzene, 220 nm, persisted.
publishDate 2018
dc.date.none.fl_str_mv 2018-11-29
2018-11-29T00:00:00Z
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://hdl.handle.net/1822/65840
url http://hdl.handle.net/1822/65840
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Wanderley, Carlos Ronald Pessoa; Andrade, Marcus Vinícius; Pereira, Luciana; Silva, G.; Pessoa, Kelly Rodrigues, Azo dye mineralization by Phanerochaete chysosporium in a sequencing bath reactor. Brazilian Archives of Biology and Technology, 61(e18180195), 2018
1516-8913
10.1590/1678-4324-2018180195
http://www.scielo.br/revistas/babt/iaboutj.htm
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
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 reponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
instacron:RCAAP
instname_str Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
instacron_str RCAAP
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reponame_str Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
collection Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
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