Effect of the initial pH and the catalyst concentration on TiO2-based photocatalytic degradation of three commercial pesticides
The photocatalytic degradations of three pesticides: 2,4-D, diuron, ametryne and a specific mixture of these ones, were carried out in a lab-scale reactor with artificial ultraviolet radiation. The effects of initial pH and catalyst concentration for each substrate were analyzed, and the degradation...
- Autores:
-
Fiderman Machuca-Martínez; Universidad del Valle, Colombia
José Ángel Colina-Márquez; Universidad de Cartagena, Colombia
- Tipo de recurso:
- Fecha de publicación:
- 2011
- Institución:
- Universidad del Norte
- Repositorio:
- Repositorio Uninorte
- Idioma:
- spa
- OAI Identifier:
- oai:manglar.uninorte.edu.co:10584/4161
- Acceso en línea:
- http://rcientificas.uninorte.edu.co/index.php/ingenieria/article/view/3306
http://hdl.handle.net/10584/4161
- Palabra clave:
- Rights
- License
- http://purl.org/coar/access_right/c_abf2
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Fiderman Machuca-Martínez; Universidad del Valle, ColombiaJosé Ángel Colina-Márquez; Universidad de Cartagena, ColombiaColombia2013-08-31T23:11:04Z2013-08-31T23:11:04Z2011-08-09http://rcientificas.uninorte.edu.co/index.php/ingenieria/article/view/3306http://hdl.handle.net/10584/4161The photocatalytic degradations of three pesticides: 2,4-D, diuron, ametryne and a specific mixture of these ones, were carried out in a lab-scale reactor with artificial ultraviolet radiation. The effects of initial pH and catalyst concentration for each substrate were analyzed, and the degradation kinetics was modeled at the optimal operating conditions for each mineralization process. The parameters of the Langmuir-Hinselwood models fitted satisfactorily to the experimental data. The incidence of the studied variable was evaluated by analysis of variance (ANOVA). The catalyst concentration was the most important variable for the 2,4-D degradation, whereas for diuron, ametryne and the considered mixture was the initial pH. The degradations of the pesticides mixture were favored at an initial pH of 7 and 0.6 g/L of TiO2 concentration.En este trabajo se evaluó la degradación fotocatalítica de tres pesticidas y su mezcla: 2,4 D, diurón y ametrina, en un reactor a escala de laboratorio con luz ultravioleta artificial. Se estudiaron los efectos del pH inicial y la concentración del catalizador y se modeló la cinética en las mejores condiciones de degradación para cada sustrato empleado en este estudio. Se calcularon las constantes cinéticas y de adsorción de Langmuir-Hinselwood por ajuste de parámetros. Por otro lado, se evaluó el efecto de cada una de las variables mediante un análisis de varianza. Se encontró que la variable más importante para la degradación del 2,4-D, fue la concentración del catalizador; mientras que para el diuron, la ametrina y la mezcla fue el pH inicial de la suspensión. La degradación de la mezcla se favoreció con un pH inicial de 7 y una concentración de catalizador de 0.6 g/L.application/pdfspaUniversidad del NorteRevista Científica Ingeniería y Desarrollo; Vol 29, No 1 (2011): Enero - Junio; 84-100instname:Universidad del Nortereponame:Repositorio Digital de la Universidad del NorteEffect of the initial pH and the catalyst concentration on TiO2-based photocatalytic degradation of three commercial pesticidesEfecto del pH inicial y la concentración del catalizador en la fotodegradación de tres pesticidas comercialesarticlepublishedVersionhttp://purl.org/coar/version/c_970fb48d4fbd8a85http://purl.org/coar/resource_type/c_6501http://purl.org/coar/access_right/c_abf210584/4161oai:172.16.14.36:10584/41612015-10-07 01:47:19.907Repositorio Digital de la Universidad del Nortemauribe@uninorte.edu.co |
dc.title.none.fl_str_mv |
Effect of the initial pH and the catalyst concentration on TiO2-based photocatalytic degradation of three commercial pesticides Efecto del pH inicial y la concentración del catalizador en la fotodegradación de tres pesticidas comerciales |
title |
Effect of the initial pH and the catalyst concentration on TiO2-based photocatalytic degradation of three commercial pesticides |
spellingShingle |
Effect of the initial pH and the catalyst concentration on TiO2-based photocatalytic degradation of three commercial pesticides |
title_short |
Effect of the initial pH and the catalyst concentration on TiO2-based photocatalytic degradation of three commercial pesticides |
title_full |
Effect of the initial pH and the catalyst concentration on TiO2-based photocatalytic degradation of three commercial pesticides |
title_fullStr |
Effect of the initial pH and the catalyst concentration on TiO2-based photocatalytic degradation of three commercial pesticides |
title_full_unstemmed |
Effect of the initial pH and the catalyst concentration on TiO2-based photocatalytic degradation of three commercial pesticides |
title_sort |
Effect of the initial pH and the catalyst concentration on TiO2-based photocatalytic degradation of three commercial pesticides |
dc.creator.fl_str_mv |
Fiderman Machuca-Martínez; Universidad del Valle, Colombia José Ángel Colina-Márquez; Universidad de Cartagena, Colombia |
dc.contributor.author.none.fl_str_mv |
Fiderman Machuca-Martínez; Universidad del Valle, Colombia José Ángel Colina-Márquez; Universidad de Cartagena, Colombia |
description |
The photocatalytic degradations of three pesticides: 2,4-D, diuron, ametryne and a specific mixture of these ones, were carried out in a lab-scale reactor with artificial ultraviolet radiation. The effects of initial pH and catalyst concentration for each substrate were analyzed, and the degradation kinetics was modeled at the optimal operating conditions for each mineralization process. The parameters of the Langmuir-Hinselwood models fitted satisfactorily to the experimental data. The incidence of the studied variable was evaluated by analysis of variance (ANOVA). The catalyst concentration was the most important variable for the 2,4-D degradation, whereas for diuron, ametryne and the considered mixture was the initial pH. The degradations of the pesticides mixture were favored at an initial pH of 7 and 0.6 g/L of TiO2 concentration. |
publishDate |
2011 |
dc.date.issued.none.fl_str_mv |
2011-08-09 |
dc.date.accessioned.none.fl_str_mv |
2013-08-31T23:11:04Z |
dc.date.available.none.fl_str_mv |
2013-08-31T23:11:04Z |
dc.type.none.fl_str_mv |
article |
dc.type.coarversion.fl_str_mv |
http://purl.org/coar/version/c_970fb48d4fbd8a85 |
dc.type.coar.fl_str_mv |
http://purl.org/coar/resource_type/c_6501 |
dc.type.hasVersion.none.fl_str_mv |
publishedVersion |
dc.identifier.other.none.fl_str_mv |
http://rcientificas.uninorte.edu.co/index.php/ingenieria/article/view/3306 |
dc.identifier.uri.none.fl_str_mv |
http://hdl.handle.net/10584/4161 |
url |
http://rcientificas.uninorte.edu.co/index.php/ingenieria/article/view/3306 http://hdl.handle.net/10584/4161 |
dc.language.iso.none.fl_str_mv |
spa |
language |
spa |
dc.relation.ispartof.none.fl_str_mv |
Revista Científica Ingeniería y Desarrollo; Vol 29, No 1 (2011): Enero - Junio; 84-100 |
dc.rights.coar.fl_str_mv |
http://purl.org/coar/access_right/c_abf2 |
rights_invalid_str_mv |
http://purl.org/coar/access_right/c_abf2 |
dc.format.none.fl_str_mv |
application/pdf |
dc.coverage.spatial.none.fl_str_mv |
Colombia |
dc.publisher.none.fl_str_mv |
Universidad del Norte |
publisher.none.fl_str_mv |
Universidad del Norte |
dc.source.none.fl_str_mv |
instname:Universidad del Norte reponame:Repositorio Digital de la Universidad del Norte |
instname_str |
Universidad del Norte |
institution |
Universidad del Norte |
reponame_str |
Repositorio Digital de la Universidad del Norte |
collection |
Repositorio Digital de la Universidad del Norte |
repository.name.fl_str_mv |
Repositorio Digital de la Universidad del Norte |
repository.mail.fl_str_mv |
mauribe@uninorte.edu.co |
_version_ |
1828169925589467136 |