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 José, Silva,Gloria Maria Marinho, Pessoa,Kelly Rodrigues
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=S1516-89132018000100606
Resumo: ABSTRACT 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 μmol.min-1 for R1 and 38 μmolmin-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 bioreactorsABSTRACT 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 μmol.min-1 for R1 and 38 μmolmin-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.Instituto de Tecnologia do Paraná - Tecpar2018-01-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S1516-89132018000100606Brazilian Archives of Biology and Technology v.61 2018reponame:Brazilian Archives of Biology and Technologyinstname:Instituto de Tecnologia do Paraná (Tecpar)instacron:TECPAR10.1590/1678-4324-2018180195info:eu-repo/semantics/openAccessWanderley,Carlos Ronald PessoaAndrade,Marcus ViníciusPereira,Luciana JoséSilva,Gloria Maria MarinhoPessoa,Kelly Rodrigueseng2019-09-11T00:00:00Zoai:scielo:S1516-89132018000100606Revistahttps://www.scielo.br/j/babt/https://old.scielo.br/oai/scielo-oai.phpbabt@tecpar.br||babt@tecpar.br1678-43241516-8913opendoar:2019-09-11T00:00Brazilian Archives of Biology and Technology - Instituto de Tecnologia do Paraná (Tecpar)false
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
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 José
Silva,Gloria Maria Marinho
Pessoa,Kelly Rodrigues
author_role author
author2 Andrade,Marcus Vinícius
Pereira,Luciana José
Silva,Gloria Maria Marinho
Pessoa,Kelly Rodrigues
author2_role author
author
author
author
dc.contributor.author.fl_str_mv Wanderley,Carlos Ronald Pessoa
Andrade,Marcus Vinícius
Pereira,Luciana José
Silva,Gloria Maria Marinho
Pessoa,Kelly Rodrigues
dc.subject.por.fl_str_mv Biodegradation
Congo red
Phanerochaete chrysosporium
Sequential bioreactors
topic Biodegradation
Congo red
Phanerochaete chrysosporium
Sequential bioreactors
description ABSTRACT 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 μmol.min-1 for R1 and 38 μmolmin-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 2018-01-01
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=S1516-89132018000100606
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S1516-89132018000100606
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 10.1590/1678-4324-2018180195
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.61 2018
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
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