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Stabilized leachates: Ozone-activated carbon treatment and kinetics

Bibliographic Details
Main Author: Javier Rivas, F.
Publication Date: 2003
Other Authors: Beltrán, F., Gimeno, O., Acedo, B., Carvalho, Fátima
Format: Article
Language: eng
Source: Repositórios Científicos de Acesso Aberto de Portugal (RCAAP)
Download full: http://hdl.handle.net/20.500.12207/5599
Summary: Ozone has been used as a pre-oxidation step for the treatment of stabilized leachates. Given the refractory nature of this type of effluents, the conversion of some wastewater quality parameters has been moderate after 1 h of ozonation (i.e. 30% chemical oxygen demand (COD) depletion). Ozone uptake was calculated in the interval 1.3–1:5 g of ozone per gram of COD degraded. An optimum dose of ozone has been experienced in terms of biodegradability of the processed effluent (60 min of treatment, 1 103 mol L1 ozone inlet feeding concentration and 50 L h1 gas flowrate). pH and other typical hydroxyl radical generator systems exerted no influence on the efficiency of the process, suggesting the negligible role played by the indirect route of oxidation (generation of hydroxyl radicals). The ozonated effluent was thereafter treated in a second adsorption stage by using a commercial activated carbon. Removal levels up to 90% of COD in approximately 120 h were experienced for adsorbent dosages of 30 g L1 : Both steps, the single ozonation and the adsorption stage have been modelled by using different pseudoempirical models. r 2003 Elsevier Ltd. All rights reserved.
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spelling Stabilized leachates: Ozone-activated carbon treatment and kineticsLeachateLandfillOzoneActivated carbonWastewaterOzone has been used as a pre-oxidation step for the treatment of stabilized leachates. Given the refractory nature of this type of effluents, the conversion of some wastewater quality parameters has been moderate after 1 h of ozonation (i.e. 30% chemical oxygen demand (COD) depletion). Ozone uptake was calculated in the interval 1.3–1:5 g of ozone per gram of COD degraded. An optimum dose of ozone has been experienced in terms of biodegradability of the processed effluent (60 min of treatment, 1 103 mol L1 ozone inlet feeding concentration and 50 L h1 gas flowrate). pH and other typical hydroxyl radical generator systems exerted no influence on the efficiency of the process, suggesting the negligible role played by the indirect route of oxidation (generation of hydroxyl radicals). The ozonated effluent was thereafter treated in a second adsorption stage by using a commercial activated carbon. Removal levels up to 90% of COD in approximately 120 h were experienced for adsorbent dosages of 30 g L1 : Both steps, the single ozonation and the adsorption stage have been modelled by using different pseudoempirical models. r 2003 Elsevier Ltd. All rights reserved.Elsevier2022-07-19T13:01:37Z2003-08-01T00:00:00Z2003-08-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/20.500.12207/5599eng0043-1354https://doi.org/10.1016/j.watres.2003.08.007Javier Rivas, F.Beltrán, F.Gimeno, O.Acedo, B.Carvalho, FátimaCarvalho, Fátimainfo:eu-repo/semantics/openAccessreponame:Repositórios Científicos de Acesso Aberto de Portugal (RCAAP)instname:FCCN, serviços digitais da FCT – Fundação para a Ciência e a Tecnologiainstacron:RCAAP2025-04-24T11:57:54Zoai:repositorio.ipbeja.pt:20.500.12207/5599Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireinfo@rcaap.ptopendoar:https://opendoar.ac.uk/repository/71602025-05-29T06:33:13.075295Repositórios Científicos de Acesso Aberto de Portugal (RCAAP) - FCCN, serviços digitais da FCT – Fundação para a Ciência e a Tecnologiafalse
dc.title.none.fl_str_mv Stabilized leachates: Ozone-activated carbon treatment and kinetics
title Stabilized leachates: Ozone-activated carbon treatment and kinetics
spellingShingle Stabilized leachates: Ozone-activated carbon treatment and kinetics
Javier Rivas, F.
Leachate
Landfill
Ozone
Activated carbon
Wastewater
title_short Stabilized leachates: Ozone-activated carbon treatment and kinetics
title_full Stabilized leachates: Ozone-activated carbon treatment and kinetics
title_fullStr Stabilized leachates: Ozone-activated carbon treatment and kinetics
title_full_unstemmed Stabilized leachates: Ozone-activated carbon treatment and kinetics
title_sort Stabilized leachates: Ozone-activated carbon treatment and kinetics
author Javier Rivas, F.
author_facet Javier Rivas, F.
Beltrán, F.
Gimeno, O.
Acedo, B.
Carvalho, Fátima
author_role author
author2 Beltrán, F.
Gimeno, O.
Acedo, B.
Carvalho, Fátima
author2_role author
author
author
author
dc.contributor.author.fl_str_mv Javier Rivas, F.
Beltrán, F.
Gimeno, O.
Acedo, B.
Carvalho, Fátima
Carvalho, Fátima
dc.subject.por.fl_str_mv Leachate
Landfill
Ozone
Activated carbon
Wastewater
topic Leachate
Landfill
Ozone
Activated carbon
Wastewater
description Ozone has been used as a pre-oxidation step for the treatment of stabilized leachates. Given the refractory nature of this type of effluents, the conversion of some wastewater quality parameters has been moderate after 1 h of ozonation (i.e. 30% chemical oxygen demand (COD) depletion). Ozone uptake was calculated in the interval 1.3–1:5 g of ozone per gram of COD degraded. An optimum dose of ozone has been experienced in terms of biodegradability of the processed effluent (60 min of treatment, 1 103 mol L1 ozone inlet feeding concentration and 50 L h1 gas flowrate). pH and other typical hydroxyl radical generator systems exerted no influence on the efficiency of the process, suggesting the negligible role played by the indirect route of oxidation (generation of hydroxyl radicals). The ozonated effluent was thereafter treated in a second adsorption stage by using a commercial activated carbon. Removal levels up to 90% of COD in approximately 120 h were experienced for adsorbent dosages of 30 g L1 : Both steps, the single ozonation and the adsorption stage have been modelled by using different pseudoempirical models. r 2003 Elsevier Ltd. All rights reserved.
publishDate 2003
dc.date.none.fl_str_mv 2003-08-01T00:00:00Z
2003-08-01
2022-07-19T13:01:37Z
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dc.identifier.uri.fl_str_mv http://hdl.handle.net/20.500.12207/5599
url http://hdl.handle.net/20.500.12207/5599
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 0043-1354
https://doi.org/10.1016/j.watres.2003.08.007
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