Electrochemical degradation of the reactive red 141 dye on a β-PbO2 anode assessed by the response surface methodology
Autor(a) principal: | |
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Data de Publicação: | 2010 |
Outros Autores: | , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Journal of the Brazilian Chemical Society (Online) |
Texto Completo: | http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0103-50532010000200019 |
Resumo: | The electrochemical degradation of the Reactive Red 141 dye using a filter-press reactor with a β-PbO2 anode was investigated through the application of the response surface methodology. The charge required for 90% decolorization (Q90) and the chemical oxygen demand removal percentage after 30 min electrolysis (COD30) were used to model the system. The investigated independent variables were the current density, pH, NaCl concentration, and temperature. Low values of Q90 (0.2-0.3 A h L-1) were obtained at acidic conditions (pH 1-3) and high concentrations of NaCl (1.0-2.0 g L-1), when Cl2 and HOCl are the predominant oxidant species. The best values of COD30 were obtained at high current densities and acidic to neutral conditions (pH 5-7); however, the consequent energy consumption makes the process not economically feasible under these conditions. For strongly acidic solutions, specific energy consumptions associated to Q90 as low as 0.79 kW h m-3 were attained. |
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Journal of the Brazilian Chemical Society (Online) |
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Electrochemical degradation of the reactive red 141 dye on a β-PbO2 anode assessed by the response surface methodologyelectrooxidationdye degradationReactive-Red 141 dyePbO2 anodefactorial designThe electrochemical degradation of the Reactive Red 141 dye using a filter-press reactor with a β-PbO2 anode was investigated through the application of the response surface methodology. The charge required for 90% decolorization (Q90) and the chemical oxygen demand removal percentage after 30 min electrolysis (COD30) were used to model the system. The investigated independent variables were the current density, pH, NaCl concentration, and temperature. Low values of Q90 (0.2-0.3 A h L-1) were obtained at acidic conditions (pH 1-3) and high concentrations of NaCl (1.0-2.0 g L-1), when Cl2 and HOCl are the predominant oxidant species. The best values of COD30 were obtained at high current densities and acidic to neutral conditions (pH 5-7); however, the consequent energy consumption makes the process not economically feasible under these conditions. For strongly acidic solutions, specific energy consumptions associated to Q90 as low as 0.79 kW h m-3 were attained.Sociedade Brasileira de Química2010-01-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0103-50532010000200019Journal of the Brazilian Chemical Society v.21 n.2 2010reponame:Journal of the Brazilian Chemical Society (Online)instname:Sociedade Brasileira de Química (SBQ)instacron:SBQ10.1590/S0103-50532010000200019info:eu-repo/semantics/openAccessAquino,José M.Rocha-Filho,Romeu C.Bocchi,NerilsoBiaggio,Sonia R.eng2010-03-17T00:00:00Zoai:scielo:S0103-50532010000200019Revistahttp://jbcs.sbq.org.brONGhttps://old.scielo.br/oai/scielo-oai.php||office@jbcs.sbq.org.br1678-47900103-5053opendoar:2010-03-17T00:00Journal of the Brazilian Chemical Society (Online) - Sociedade Brasileira de Química (SBQ)false |
dc.title.none.fl_str_mv |
Electrochemical degradation of the reactive red 141 dye on a β-PbO2 anode assessed by the response surface methodology |
title |
Electrochemical degradation of the reactive red 141 dye on a β-PbO2 anode assessed by the response surface methodology |
spellingShingle |
Electrochemical degradation of the reactive red 141 dye on a β-PbO2 anode assessed by the response surface methodology Aquino,José M. electrooxidation dye degradation Reactive-Red 141 dye PbO2 anode factorial design |
title_short |
Electrochemical degradation of the reactive red 141 dye on a β-PbO2 anode assessed by the response surface methodology |
title_full |
Electrochemical degradation of the reactive red 141 dye on a β-PbO2 anode assessed by the response surface methodology |
title_fullStr |
Electrochemical degradation of the reactive red 141 dye on a β-PbO2 anode assessed by the response surface methodology |
title_full_unstemmed |
Electrochemical degradation of the reactive red 141 dye on a β-PbO2 anode assessed by the response surface methodology |
title_sort |
Electrochemical degradation of the reactive red 141 dye on a β-PbO2 anode assessed by the response surface methodology |
author |
Aquino,José M. |
author_facet |
Aquino,José M. Rocha-Filho,Romeu C. Bocchi,Nerilso Biaggio,Sonia R. |
author_role |
author |
author2 |
Rocha-Filho,Romeu C. Bocchi,Nerilso Biaggio,Sonia R. |
author2_role |
author author author |
dc.contributor.author.fl_str_mv |
Aquino,José M. Rocha-Filho,Romeu C. Bocchi,Nerilso Biaggio,Sonia R. |
dc.subject.por.fl_str_mv |
electrooxidation dye degradation Reactive-Red 141 dye PbO2 anode factorial design |
topic |
electrooxidation dye degradation Reactive-Red 141 dye PbO2 anode factorial design |
description |
The electrochemical degradation of the Reactive Red 141 dye using a filter-press reactor with a β-PbO2 anode was investigated through the application of the response surface methodology. The charge required for 90% decolorization (Q90) and the chemical oxygen demand removal percentage after 30 min electrolysis (COD30) were used to model the system. The investigated independent variables were the current density, pH, NaCl concentration, and temperature. Low values of Q90 (0.2-0.3 A h L-1) were obtained at acidic conditions (pH 1-3) and high concentrations of NaCl (1.0-2.0 g L-1), when Cl2 and HOCl are the predominant oxidant species. The best values of COD30 were obtained at high current densities and acidic to neutral conditions (pH 5-7); however, the consequent energy consumption makes the process not economically feasible under these conditions. For strongly acidic solutions, specific energy consumptions associated to Q90 as low as 0.79 kW h m-3 were attained. |
publishDate |
2010 |
dc.date.none.fl_str_mv |
2010-01-01 |
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=S0103-50532010000200019 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0103-50532010000200019 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/S0103-50532010000200019 |
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 |
Sociedade Brasileira de Química |
publisher.none.fl_str_mv |
Sociedade Brasileira de Química |
dc.source.none.fl_str_mv |
Journal of the Brazilian Chemical Society v.21 n.2 2010 reponame:Journal of the Brazilian Chemical Society (Online) instname:Sociedade Brasileira de Química (SBQ) instacron:SBQ |
instname_str |
Sociedade Brasileira de Química (SBQ) |
instacron_str |
SBQ |
institution |
SBQ |
reponame_str |
Journal of the Brazilian Chemical Society (Online) |
collection |
Journal of the Brazilian Chemical Society (Online) |
repository.name.fl_str_mv |
Journal of the Brazilian Chemical Society (Online) - Sociedade Brasileira de Química (SBQ) |
repository.mail.fl_str_mv |
||office@jbcs.sbq.org.br |
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1750318170642579456 |