Electrocoagulation/flotation followed by fluidized bed anaerobic reactor applied to tannery effluent treatment
Autor(a) principal: | |
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Data de Publicação: | 2012 |
Outros Autores: | , , |
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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Repositório Institucional da UNESP |
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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 |