Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol

Detalhes bibliográficos
Autor(a) principal: Martins, Michelly Freitas de Moraes
Data de Publicação: 2017
Tipo de documento: Dissertação
Idioma: por
Título da fonte: Repositório Institucional da UFG
dARK ID: ark:/38995/0013000009v44
Texto Completo: http://repositorio.bc.ufg.br/tede/handle/tede/10213
Resumo: Due to the need for more efficient technologies for the phenol elimination in effluents, the objective of this study was to evaluate the efficiency of the UV/H2O2/AC process and the adsobent behavior in the coupling to eliminate phenol. For a determination of the physical characteristics of the activated carbon, a textural analysis was carried out for isotherms of adsorption and desorption of N2 at 77 K, scanning electron microscopy, thermogravimetric analysis and differential thermal analysis. Regarding the chemical nature of the coal were carried out as techniques of infrared spectroscopy, elemental analysis, Boehm method and zero load point. Adsorption kinetics were used to determine the adsorption capacity, for each of the 11 tests, according to the experimental design 23 + 3 central points, where the pH, temperature and the quantity of carbon activated varied. The experimental data obtained in adsorption kinetics were adjusted to the kinetic models of pseudo-first order, pseudo-second order and intraparticle diffusion, with pseudo-second order being the best represent the adsorption process of all the tests. Adsorption isotherms (15, 30 and 45°C) were then adjusted, adjusting the values to the Langmuir and Freundlich models. All feared a better fit of the data to the Freundlich model. For the treatments H2O2/UV and H2O2/UV/AC a factorial design 22 + 3 central points was used, varying pH and H2O2 concentration and quantified response by rate of phenol removal. For both treatments the pH showed a negative release on elimination rate and a concentration of H2O2 showed positive effect. The best tests for H2O2/UV and H2O2/UV/AC processes were the central points (pH 7 and 20 mmol H2O2), with phenol elimination rates of 89% and 94.16%, respectively. With the presence of a free radical inhibitor (tert-butanol) the kinetic contribution of the hydroxyl radicals was calculated, showing that 77.64% of the phenol elimination in the H2O2/UV/AC treatment was caused by their action. The H2O2/UV/AC coupling process is acceptable, presenting a higher removal rate than the adsorption process with much shorter removal time.
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spelling Castiglioni, Gabriel Luishttp://lattes.cnpq.br/6050198962131737Oliveira, Tatianne Ferreira dehttp://lattes.cnpq.br/2017895913160804Castiglioni, Gabriel LuisOliveira, Tatianne Ferreira de OOstroski, Indianara ConceiçãoSá, Fernando Pereira dehttp://lattes.cnpq.br/5341453635380839Martins, Michelly Freitas de Moraes2019-11-29T12:01:09Z2017-06-30MARTINS, Michelly Freitas de Moraes. Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol. 2017. 102 f. Dissertação (Mestrado em Engenharia Química) - Universidade Federal de Goiás, Goiânia, 2017.http://repositorio.bc.ufg.br/tede/handle/tede/10213ark:/38995/0013000009v44Due to the need for more efficient technologies for the phenol elimination in effluents, the objective of this study was to evaluate the efficiency of the UV/H2O2/AC process and the adsobent behavior in the coupling to eliminate phenol. For a determination of the physical characteristics of the activated carbon, a textural analysis was carried out for isotherms of adsorption and desorption of N2 at 77 K, scanning electron microscopy, thermogravimetric analysis and differential thermal analysis. Regarding the chemical nature of the coal were carried out as techniques of infrared spectroscopy, elemental analysis, Boehm method and zero load point. Adsorption kinetics were used to determine the adsorption capacity, for each of the 11 tests, according to the experimental design 23 + 3 central points, where the pH, temperature and the quantity of carbon activated varied. The experimental data obtained in adsorption kinetics were adjusted to the kinetic models of pseudo-first order, pseudo-second order and intraparticle diffusion, with pseudo-second order being the best represent the adsorption process of all the tests. Adsorption isotherms (15, 30 and 45°C) were then adjusted, adjusting the values to the Langmuir and Freundlich models. All feared a better fit of the data to the Freundlich model. For the treatments H2O2/UV and H2O2/UV/AC a factorial design 22 + 3 central points was used, varying pH and H2O2 concentration and quantified response by rate of phenol removal. For both treatments the pH showed a negative release on elimination rate and a concentration of H2O2 showed positive effect. The best tests for H2O2/UV and H2O2/UV/AC processes were the central points (pH 7 and 20 mmol H2O2), with phenol elimination rates of 89% and 94.16%, respectively. With the presence of a free radical inhibitor (tert-butanol) the kinetic contribution of the hydroxyl radicals was calculated, showing that 77.64% of the phenol elimination in the H2O2/UV/AC treatment was caused by their action. The H2O2/UV/AC coupling process is acceptable, presenting a higher removal rate than the adsorption process with much shorter removal time.Tendo em vista a necessidade de tecnologias mais eficazes para eliminação de fenol em efluentes, objetivou-se com este trabalho avaliar a eficiência do processo UV/H2O2/CA e o comportamento do adsorvente na acoplagem na eliminação de fenol. Para a determinação das características físicas do carvão ativado foram realizadas a análise textural por isotermas de adsorção e dessorção de N2 a 77 K, microscopia eletrônica de varredura, análise termogravimétrica e análise térmica diferencial. No que tange à natureza química do carvão foram realizadas as técnicas de espectroscopia no infravermelho, análise elementar, método de Boehm e ponto de carga zero. Realizou-se as cinéticas de adsorção para a determinação da capacidade de adsorção, para cada um dos 11 ensaios, conforme o delineamento experimental 23 + 3 pontos centrais, em que foram variados o pH, a temperatura e a quantidade de carvão ativado. Os dados experimentais obtidos nas cinéticas de adsorção foram ajustados aos modelos cinéticos de pseudo-primeira ordem, pseudo-segunda ordem e difusão intrapartícula, sendo o pseudo-segunda ordem o que melhor representou o processo de adsorção de todos os ensaios. Realizou-se então experimentos para a obtenção das isotermas de adsorção (15, 30 e 45°C) e os valores foram ajustados aos modelos de Langmuir e Freundlich. Todas tiveram uma melhor adequação dos dados ao modelo de Freundlich. Para os tratamentos H2O2/UV e H2O2/UV/CA utilizou-se um delineamento fatorial 22 + 3 pontos centrais, variando pH e concentração de H2O2 e a resposta quantificada pela taxa de remoção de fenol. Para ambos os tratamentos o pH mostrou efeito negativo sobre a taxa de eliminação e a concentração de H2O2 mostrou efeito positivo. Os melhores ensaios para os processos H2O2/UV e H2O2/UV/CA foram os pontos centrais (pH 7 e 20 mmol de H2O2), obtiveram taxas de eliminação de fenol de 89% e 94,16%, respectivamente. Com a presença de um inibidor de radicais livres (tert-butanol) foi calculada a contribuição cinética dos radicais hidroxila, mostrando que 77,64% da eliminação de fenol no tratamento H2O2/UV/CA foi ocasionado pela ação dos radicais hidroxila. O processo de acoplagem H2O2/UV/CA se mostrou aceitável, apresentando uma taxa de remoção maior que para o processo de adsorção sozinho com o tempo de remoção bem menor.Submitted by Marlene Santos (marlene.bc.ufg@gmail.com) on 2019-11-28T18:09:36Z No. of bitstreams: 2 Dissertação - Michelly Freitas de Moraes Martins - 2017.pdf: 12092838 bytes, checksum: e7c6481fe807d5aa71bd2e84e63ef107 (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5)Approved for entry into archive by Luciana Ferreira (lucgeral@gmail.com) on 2019-11-29T12:01:09Z (GMT) No. of bitstreams: 2 Dissertação - Michelly Freitas de Moraes Martins - 2017.pdf: 12092838 bytes, checksum: e7c6481fe807d5aa71bd2e84e63ef107 (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5)Made available in DSpace on 2019-11-29T12:01:09Z (GMT). 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dc.title.eng.fl_str_mv Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol
dc.title.alternative.eng.fl_str_mv Investigation of the advanced oxidative process (UV/H2O2/activated carbon) in the treatment of industrial effluents: phenol elimination
title Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol
spellingShingle Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol
Martins, Michelly Freitas de Moraes
Modelagem cinética
Tert-butanol
Acoplagem
Adsorção
Kinectics modeling
Tert-butanol
Coupling
Adsortion
CIENCIAS EXATAS E DA TERRA::QUIMICA
title_short Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol
title_full Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol
title_fullStr Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol
title_full_unstemmed Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol
title_sort Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol
author Martins, Michelly Freitas de Moraes
author_facet Martins, Michelly Freitas de Moraes
author_role author
dc.contributor.advisor1.fl_str_mv Castiglioni, Gabriel Luis
dc.contributor.advisor1Lattes.fl_str_mv http://lattes.cnpq.br/6050198962131737
dc.contributor.advisor-co1.fl_str_mv Oliveira, Tatianne Ferreira de
dc.contributor.advisor-co1Lattes.fl_str_mv http://lattes.cnpq.br/2017895913160804
dc.contributor.referee1.fl_str_mv Castiglioni, Gabriel Luis
dc.contributor.referee2.fl_str_mv Oliveira, Tatianne Ferreira de O
dc.contributor.referee3.fl_str_mv Ostroski, Indianara Conceição
dc.contributor.referee4.fl_str_mv Sá, Fernando Pereira de
dc.contributor.authorLattes.fl_str_mv http://lattes.cnpq.br/5341453635380839
dc.contributor.author.fl_str_mv Martins, Michelly Freitas de Moraes
contributor_str_mv Castiglioni, Gabriel Luis
Oliveira, Tatianne Ferreira de
Castiglioni, Gabriel Luis
Oliveira, Tatianne Ferreira de O
Ostroski, Indianara Conceição
Sá, Fernando Pereira de
dc.subject.por.fl_str_mv Modelagem cinética
Tert-butanol
Acoplagem
Adsorção
topic Modelagem cinética
Tert-butanol
Acoplagem
Adsorção
Kinectics modeling
Tert-butanol
Coupling
Adsortion
CIENCIAS EXATAS E DA TERRA::QUIMICA
dc.subject.eng.fl_str_mv Kinectics modeling
Tert-butanol
Coupling
Adsortion
dc.subject.cnpq.fl_str_mv CIENCIAS EXATAS E DA TERRA::QUIMICA
description Due to the need for more efficient technologies for the phenol elimination in effluents, the objective of this study was to evaluate the efficiency of the UV/H2O2/AC process and the adsobent behavior in the coupling to eliminate phenol. For a determination of the physical characteristics of the activated carbon, a textural analysis was carried out for isotherms of adsorption and desorption of N2 at 77 K, scanning electron microscopy, thermogravimetric analysis and differential thermal analysis. Regarding the chemical nature of the coal were carried out as techniques of infrared spectroscopy, elemental analysis, Boehm method and zero load point. Adsorption kinetics were used to determine the adsorption capacity, for each of the 11 tests, according to the experimental design 23 + 3 central points, where the pH, temperature and the quantity of carbon activated varied. The experimental data obtained in adsorption kinetics were adjusted to the kinetic models of pseudo-first order, pseudo-second order and intraparticle diffusion, with pseudo-second order being the best represent the adsorption process of all the tests. Adsorption isotherms (15, 30 and 45°C) were then adjusted, adjusting the values to the Langmuir and Freundlich models. All feared a better fit of the data to the Freundlich model. For the treatments H2O2/UV and H2O2/UV/AC a factorial design 22 + 3 central points was used, varying pH and H2O2 concentration and quantified response by rate of phenol removal. For both treatments the pH showed a negative release on elimination rate and a concentration of H2O2 showed positive effect. The best tests for H2O2/UV and H2O2/UV/AC processes were the central points (pH 7 and 20 mmol H2O2), with phenol elimination rates of 89% and 94.16%, respectively. With the presence of a free radical inhibitor (tert-butanol) the kinetic contribution of the hydroxyl radicals was calculated, showing that 77.64% of the phenol elimination in the H2O2/UV/AC treatment was caused by their action. The H2O2/UV/AC coupling process is acceptable, presenting a higher removal rate than the adsorption process with much shorter removal time.
publishDate 2017
dc.date.issued.fl_str_mv 2017-06-30
dc.date.accessioned.fl_str_mv 2019-11-29T12:01:09Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/masterThesis
format masterThesis
status_str publishedVersion
dc.identifier.citation.fl_str_mv MARTINS, Michelly Freitas de Moraes. Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol. 2017. 102 f. Dissertação (Mestrado em Engenharia Química) - Universidade Federal de Goiás, Goiânia, 2017.
dc.identifier.uri.fl_str_mv http://repositorio.bc.ufg.br/tede/handle/tede/10213
dc.identifier.dark.fl_str_mv ark:/38995/0013000009v44
identifier_str_mv MARTINS, Michelly Freitas de Moraes. Investigação do processo oxidativo avançado (UV/H2O2/carvão ativado) no tratamento de efluentes industriais: eliminação de fenol. 2017. 102 f. Dissertação (Mestrado em Engenharia Química) - Universidade Federal de Goiás, Goiânia, 2017.
ark:/38995/0013000009v44
url http://repositorio.bc.ufg.br/tede/handle/tede/10213
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language por
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600
600
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dc.relation.department.fl_str_mv 7826066743741197278
dc.relation.cnpq.fl_str_mv 1571700325303117195
dc.relation.sponsorship.fl_str_mv -961409807440757778
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info:eu-repo/semantics/openAccess
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dc.publisher.none.fl_str_mv Universidade Federal de Goiás
dc.publisher.program.fl_str_mv Programa de Pós-graduação em Engenharia Química (IQ)
dc.publisher.initials.fl_str_mv UFG
dc.publisher.country.fl_str_mv Brasil
dc.publisher.department.fl_str_mv Instituto de Química - IQ (RG)
publisher.none.fl_str_mv Universidade Federal de Goiás
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http://repositorio.bc.ufg.br/tede/bitstreams/cbaf9603-0f65-4492-8bfa-e3f54c8145f8/download
http://repositorio.bc.ufg.br/tede/bitstreams/48d90204-0262-4baa-b993-6256514d3b93/download
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repository.name.fl_str_mv Repositório Institucional da UFG - Universidade Federal de Goiás (UFG)
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