Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatment

Detalhes bibliográficos
Autor(a) principal: Sbizzaro Filho, Daniel [UNESP]
Data de Publicação: 2012
Outros Autores: Bota, Guilherme Bonfatti [UNESP], Borri, Rodrigo Babora [UNESP], Teran, Francisco Javier Cuba [UNESP]
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Institucional da UNESP
Texto Completo: http://dx.doi.org/10.1080/19443994.2012.661292
http://hdl.handle.net/11449/220884
Resumo: A series operation of electrocoagulation/flotation (ECF) and fluidized bed anaerobic reactor (FBR) was conducted to treat tannery wastewater. Although both reactors were operated in fill- and-draw (batch) mode, effluent from ECF was fed to FBR in order to remove the remaining soluble biodegradable organic matter. Operating with a hydraulic residence time of 65 min, the ECF reactor reached 59% COD removal and FBR reached 74% COD removal with an 8 h residence time. Time profiles for wastewater treatment of 65 min in ECF plus 12 h in FBR, showed 39% removal of COD in the first 10 min and 84% in the remaining 775 min of the overall operation cycle. Although turbidity in the raw influent reached levels beyond the upper limit of detection for the turbidimeter, values as low as 10 uT were detected after 65 min treatment in ECF. However, after being treated for 8 h in FBR, the efficiency of turbidity removal was affected by solids settling in the recirculation basin. © 2012, Taylor & Francis Group, LLC.
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spelling Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatmentAnaerobic treatmentBiofilmElectrocoagulationFlotationFluidized bedTannery effluentA series operation of electrocoagulation/flotation (ECF) and fluidized bed anaerobic reactor (FBR) was conducted to treat tannery wastewater. Although both reactors were operated in fill- and-draw (batch) mode, effluent from ECF was fed to FBR in order to remove the remaining soluble biodegradable organic matter. Operating with a hydraulic residence time of 65 min, the ECF reactor reached 59% COD removal and FBR reached 74% COD removal with an 8 h residence time. Time profiles for wastewater treatment of 65 min in ECF plus 12 h in FBR, showed 39% removal of COD in the first 10 min and 84% in the remaining 775 min of the overall operation cycle. Although turbidity in the raw influent reached levels beyond the upper limit of detection for the turbidimeter, values as low as 10 uT were detected after 65 min treatment in ECF. However, after being treated for 8 h in FBR, the efficiency of turbidity removal was affected by solids settling in the recirculation basin. © 2012, Taylor & Francis Group, LLC.Faculdade de Ciências e Tecnologia UNESP Univ Estadual Paulista, Presidente Prudente, SPFaculdade de Ciências e Tecnologia UNESP Univ Estadual Paulista, Presidente Prudente, SPUniversidade Estadual Paulista (UNESP)Sbizzaro Filho, Daniel [UNESP]Bota, Guilherme Bonfatti [UNESP]Borri, Rodrigo Babora [UNESP]Teran, Francisco Javier Cuba [UNESP]2022-04-28T19:06:38Z2022-04-28T19:06:38Z2012-01-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article359-363http://dx.doi.org/10.1080/19443994.2012.661292Desalination and Water Treatment, v. 37, n. 1-3, p. 359-363, 2012.1944-39861944-3994http://hdl.handle.net/11449/22088410.1080/19443994.2012.6612922-s2.0-85025345698Scopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengDesalination and Water Treatmentinfo:eu-repo/semantics/openAccess2022-04-28T19:06:38Zoai:repositorio.unesp.br:11449/220884Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T13:46:13.653904Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false
dc.title.none.fl_str_mv Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatment
title Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatment
spellingShingle Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatment
Sbizzaro Filho, Daniel [UNESP]
Anaerobic treatment
Biofilm
Electrocoagulation
Flotation
Fluidized bed
Tannery effluent
title_short Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatment
title_full Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatment
title_fullStr Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatment
title_full_unstemmed Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatment
title_sort Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatment
author Sbizzaro Filho, Daniel [UNESP]
author_facet Sbizzaro Filho, Daniel [UNESP]
Bota, Guilherme Bonfatti [UNESP]
Borri, Rodrigo Babora [UNESP]
Teran, Francisco Javier Cuba [UNESP]
author_role author
author2 Bota, Guilherme Bonfatti [UNESP]
Borri, Rodrigo Babora [UNESP]
Teran, Francisco Javier Cuba [UNESP]
author2_role author
author
author
dc.contributor.none.fl_str_mv Universidade Estadual Paulista (UNESP)
dc.contributor.author.fl_str_mv Sbizzaro Filho, Daniel [UNESP]
Bota, Guilherme Bonfatti [UNESP]
Borri, Rodrigo Babora [UNESP]
Teran, Francisco Javier Cuba [UNESP]
dc.subject.por.fl_str_mv Anaerobic treatment
Biofilm
Electrocoagulation
Flotation
Fluidized bed
Tannery effluent
topic Anaerobic treatment
Biofilm
Electrocoagulation
Flotation
Fluidized bed
Tannery effluent
description A series operation of electrocoagulation/flotation (ECF) and fluidized bed anaerobic reactor (FBR) was conducted to treat tannery wastewater. Although both reactors were operated in fill- and-draw (batch) mode, effluent from ECF was fed to FBR in order to remove the remaining soluble biodegradable organic matter. Operating with a hydraulic residence time of 65 min, the ECF reactor reached 59% COD removal and FBR reached 74% COD removal with an 8 h residence time. Time profiles for wastewater treatment of 65 min in ECF plus 12 h in FBR, showed 39% removal of COD in the first 10 min and 84% in the remaining 775 min of the overall operation cycle. Although turbidity in the raw influent reached levels beyond the upper limit of detection for the turbidimeter, values as low as 10 uT were detected after 65 min treatment in ECF. However, after being treated for 8 h in FBR, the efficiency of turbidity removal was affected by solids settling in the recirculation basin. © 2012, Taylor & Francis Group, LLC.
publishDate 2012
dc.date.none.fl_str_mv 2012-01-01
2022-04-28T19:06:38Z
2022-04-28T19:06:38Z
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/10.1080/19443994.2012.661292
Desalination and Water Treatment, v. 37, n. 1-3, p. 359-363, 2012.
1944-3986
1944-3994
http://hdl.handle.net/11449/220884
10.1080/19443994.2012.661292
2-s2.0-85025345698
url http://dx.doi.org/10.1080/19443994.2012.661292
http://hdl.handle.net/11449/220884
identifier_str_mv Desalination and Water Treatment, v. 37, n. 1-3, p. 359-363, 2012.
1944-3986
1944-3994
10.1080/19443994.2012.661292
2-s2.0-85025345698
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Desalination and Water Treatment
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv 359-363
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
_version_ 1808128274310627328