Catalytic studies in wet oxidation of effluents from formaldehyde industry

Detalhes bibliográficos
Autor(a) principal: Silva, Adrián M. T.
Data de Publicação: 2003
Outros Autores: Castelo-Branco, Isabel M., Quinta-Ferreira, Rosa M., Levec, Janez
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/10316/3816
https://doi.org/10.1016/S0009-2509(02)00636-X
Resumo: Development and design of active catalysts for the oxidation of formaldehyde present in wastewaters is of great importance. In this context, catalytic performance studies for oxidation of high formaldehyde containing solutions (1500 ppm) were carried out in a semibatch high-pressure reactor at 190-220°C and 15-35 bar of oxygen partial pressure. The removal efficiency of total organic carbon (TOC) was evaluated experimentally under different solid catalysts, using several heterogeneous composite oxides prepared in our laboratory (Mn/Ce, Co/Ce and Ag/Ce), as well as a commercial catalyst (CuO-ZnO/Al2O3). The Mn/Ce catalyst was the more active leading to high TOC conversions (99.4%). The TOC reductions were lower using Co/Ce, Ag/Ce and CuO-ZnO/Al2O3, respectively, 71.3%, 54.2% and 78.7%. Attempts were made to identify the influence of different Mn/Ce ratios. A high molar fraction of Mn leads to high TOC abatements. During the preparation procedure of catalysts the drying temperature does not affect significantly the catalytic area while increasing calcination temperature leads to lower surface areas. Carbon capacity adsorption was not observed for the Mn/Ce and CuO-ZnO/Al2O3 catalyst and leaching of the correspondent metals, Mn, Cu and Zn, was not significant. The catalytic wet oxidation (CWO) process was studied with an industrial high formaldehyde concentration effluent (800 ppm). Using an Mn/Ce catalyst the formaldehyde concentration decreased from 800 to 0.1 ppm and ammoniacal nitrogen from 420 to 155 ppm while 91.7% in TOC reduction was observed. These conversions were higher than those obtained with the commercial CuO-ZnO/Al2O3 catalyst. Therefore, Mn/Ce catalysts seem to be interesting options for the treatment of effluents from formaldehyde industry by CWO process.
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spelling Catalytic studies in wet oxidation of effluents from formaldehyde industryEnvironmentPollutionFormaldehyde effluentsCatalytic wet oxidationMultiphase reactorsSlurriesDevelopment and design of active catalysts for the oxidation of formaldehyde present in wastewaters is of great importance. In this context, catalytic performance studies for oxidation of high formaldehyde containing solutions (1500 ppm) were carried out in a semibatch high-pressure reactor at 190-220°C and 15-35 bar of oxygen partial pressure. The removal efficiency of total organic carbon (TOC) was evaluated experimentally under different solid catalysts, using several heterogeneous composite oxides prepared in our laboratory (Mn/Ce, Co/Ce and Ag/Ce), as well as a commercial catalyst (CuO-ZnO/Al2O3). The Mn/Ce catalyst was the more active leading to high TOC conversions (99.4%). The TOC reductions were lower using Co/Ce, Ag/Ce and CuO-ZnO/Al2O3, respectively, 71.3%, 54.2% and 78.7%. Attempts were made to identify the influence of different Mn/Ce ratios. A high molar fraction of Mn leads to high TOC abatements. During the preparation procedure of catalysts the drying temperature does not affect significantly the catalytic area while increasing calcination temperature leads to lower surface areas. Carbon capacity adsorption was not observed for the Mn/Ce and CuO-ZnO/Al2O3 catalyst and leaching of the correspondent metals, Mn, Cu and Zn, was not significant. The catalytic wet oxidation (CWO) process was studied with an industrial high formaldehyde concentration effluent (800 ppm). Using an Mn/Ce catalyst the formaldehyde concentration decreased from 800 to 0.1 ppm and ammoniacal nitrogen from 420 to 155 ppm while 91.7% in TOC reduction was observed. These conversions were higher than those obtained with the commercial CuO-ZnO/Al2O3 catalyst. Therefore, Mn/Ce catalysts seem to be interesting options for the treatment of effluents from formaldehyde industry by CWO process.http://www.sciencedirect.com/science/article/B6TFK-47YGF5W-6/1/e0a79ca1a3c6dc28fdc3c33a6ce69ac82003info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleaplication/PDFhttp://hdl.handle.net/10316/3816http://hdl.handle.net/10316/3816https://doi.org/10.1016/S0009-2509(02)00636-XengChemical Engineering Science. 58:3-6 (2003) 963-970Silva, Adrián M. T.Castelo-Branco, Isabel M.Quinta-Ferreira, Rosa M.Levec, Janezinfo:eu-repo/semantics/openAccessreponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãoinstacron:RCAAP2020-11-06T16:59:28ZPortal AgregadorONG
dc.title.none.fl_str_mv Catalytic studies in wet oxidation of effluents from formaldehyde industry
title Catalytic studies in wet oxidation of effluents from formaldehyde industry
spellingShingle Catalytic studies in wet oxidation of effluents from formaldehyde industry
Silva, Adrián M. T.
Environment
Pollution
Formaldehyde effluents
Catalytic wet oxidation
Multiphase reactors
Slurries
title_short Catalytic studies in wet oxidation of effluents from formaldehyde industry
title_full Catalytic studies in wet oxidation of effluents from formaldehyde industry
title_fullStr Catalytic studies in wet oxidation of effluents from formaldehyde industry
title_full_unstemmed Catalytic studies in wet oxidation of effluents from formaldehyde industry
title_sort Catalytic studies in wet oxidation of effluents from formaldehyde industry
author Silva, Adrián M. T.
author_facet Silva, Adrián M. T.
Castelo-Branco, Isabel M.
Quinta-Ferreira, Rosa M.
Levec, Janez
author_role author
author2 Castelo-Branco, Isabel M.
Quinta-Ferreira, Rosa M.
Levec, Janez
author2_role author
author
author
dc.contributor.author.fl_str_mv Silva, Adrián M. T.
Castelo-Branco, Isabel M.
Quinta-Ferreira, Rosa M.
Levec, Janez
dc.subject.por.fl_str_mv Environment
Pollution
Formaldehyde effluents
Catalytic wet oxidation
Multiphase reactors
Slurries
topic Environment
Pollution
Formaldehyde effluents
Catalytic wet oxidation
Multiphase reactors
Slurries
description Development and design of active catalysts for the oxidation of formaldehyde present in wastewaters is of great importance. In this context, catalytic performance studies for oxidation of high formaldehyde containing solutions (1500 ppm) were carried out in a semibatch high-pressure reactor at 190-220°C and 15-35 bar of oxygen partial pressure. The removal efficiency of total organic carbon (TOC) was evaluated experimentally under different solid catalysts, using several heterogeneous composite oxides prepared in our laboratory (Mn/Ce, Co/Ce and Ag/Ce), as well as a commercial catalyst (CuO-ZnO/Al2O3). The Mn/Ce catalyst was the more active leading to high TOC conversions (99.4%). The TOC reductions were lower using Co/Ce, Ag/Ce and CuO-ZnO/Al2O3, respectively, 71.3%, 54.2% and 78.7%. Attempts were made to identify the influence of different Mn/Ce ratios. A high molar fraction of Mn leads to high TOC abatements. During the preparation procedure of catalysts the drying temperature does not affect significantly the catalytic area while increasing calcination temperature leads to lower surface areas. Carbon capacity adsorption was not observed for the Mn/Ce and CuO-ZnO/Al2O3 catalyst and leaching of the correspondent metals, Mn, Cu and Zn, was not significant. The catalytic wet oxidation (CWO) process was studied with an industrial high formaldehyde concentration effluent (800 ppm). Using an Mn/Ce catalyst the formaldehyde concentration decreased from 800 to 0.1 ppm and ammoniacal nitrogen from 420 to 155 ppm while 91.7% in TOC reduction was observed. These conversions were higher than those obtained with the commercial CuO-ZnO/Al2O3 catalyst. Therefore, Mn/Ce catalysts seem to be interesting options for the treatment of effluents from formaldehyde industry by CWO process.
publishDate 2003
dc.date.none.fl_str_mv 2003
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dc.identifier.uri.fl_str_mv http://hdl.handle.net/10316/3816
http://hdl.handle.net/10316/3816
https://doi.org/10.1016/S0009-2509(02)00636-X
url http://hdl.handle.net/10316/3816
https://doi.org/10.1016/S0009-2509(02)00636-X
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Chemical Engineering Science. 58:3-6 (2003) 963-970
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