Desenvolvimento de um sistema de eletrocoagulação-flotação para o tratamento de água para abastecimento público

Detalhes bibliográficos
Autor(a) principal: Brächer, Gustavo Holz
Data de Publicação: 2022
Tipo de documento: Tese
Idioma: por
Título da fonte: Manancial - Repositório Digital da UFSM
Texto Completo: http://repositorio.ufsm.br/handle/1/26709
Resumo: Although essential for human life, health and dignity, there is a large proportion of people without access to services of water supply. Most of them are in regions with difficult access, low demographic density and/or high spatial dispersion, which makes unfeasible conventional solutions to serve them. Innovative solutions are also desired to complement public supply systems in face of the growing water scarcity and to supply the growing demand for water in a limited physical space. So, the objective of this study was developing an electrocoagulation-flotation system (ECF system), at pilot scale, for the surface water treatment for public supply and evaluating its performance. The ECF system was composed by two modular electrocoagulators followed by a helical tubular flocculator (HTF), with flowrate of 20 L∙min-1 . This configuration was developed for better use of the coagulants and microbubbles generated in the electrocoagulation by the formation of aerated flocs. The adopted conditions in the electrocoagulators were upward flow, aluminum electrodes, parallel monopolar connection, inter-electrodes distance of 3 mm, current density of 0.43-1.28 mA∙cm-2 , flow speed of 0.04 m∙s-1 , hydraulic detention time (HDT) of 51.0 s, and contact time with the electrodes of 43.3 s. The adopted conditions in the HTF were vertical orientation with upward flow, HDT of 6.36 min, speed gradient of 71.7-182.8 s -1 , Camp number of 27,366-69,770, and Reynolds number of 7,059. The study was performed at the water treatment plant of Santa Maria-RS, with water from the rivers Vacacaí-Mirim and Ibicuí-Mirim. The treatment was performed with pH adjustment of the water to 6.4. The ECF system was capable to provide turbidity of 1.3 ± 0.4 NTU and apparent color of 16.8 ± 5.8 uC to the treated water, which were appropriate for the further filtration step. Among the results of performance, the removal efficiency of total coliforms (95.6 ± 4.7%), E. coli (89.4 ± 8.8%), chlorophyll a (87.7 ± 10.9%), apparent color (73.0 ± 8.2%), and turbidity (79.9 ± 4.6%) were stand out, which shows the efficiency of the system in the water clarification and micro-organisms inactivation. The system had an energetic consumption of 0.02- 0.37 kWh∙m-3 , aluminum consumption of 3.0-9.0 mg∙L-1 , and hydrochloric acid of 2.5-21.5 mL∙m-3 . Operations of cleaning or electrodes change proved to be essential for keeping the energetic efficiency of the system. The energy consumption proved to be a good indicator for determining the moment to do it. The operation cost of the system was R$ 0.19 ± 0.07∙m-3 , where 49.1% referred to energy consumption, 44.1% to aluminum consumption, and 6.6% to hydrochloric acid consumption. The use of renewable energy sources can reduce the operational costs to R$ 0,10 ± 0,06∙m-3 . The ECF system showed potential of being diffused as an alternative technology for surface water treatment, compact, easily installable, operable, and automatable, especially attractive for decentralized supply systems (rural, riverside, peri-urban and/or hard-to-reach communities), as well as for coping with water scarcity and/or seasonal demands.
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spelling Desenvolvimento de um sistema de eletrocoagulação-flotação para o tratamento de água para abastecimento públicoDevelopment of an electrocoagulation-flotation system for the treatment of water for public supplySaneamentoTratamento de águaÁgua potávelProcessos eletroquímicosEletrocoagulação-flotaçãoSanitationWater treatmentDrinking waterElectrochemical processElectrocoagulation-flotationCNPQ::ENGENHARIAS::ENGENHARIA CIVILAlthough essential for human life, health and dignity, there is a large proportion of people without access to services of water supply. Most of them are in regions with difficult access, low demographic density and/or high spatial dispersion, which makes unfeasible conventional solutions to serve them. Innovative solutions are also desired to complement public supply systems in face of the growing water scarcity and to supply the growing demand for water in a limited physical space. So, the objective of this study was developing an electrocoagulation-flotation system (ECF system), at pilot scale, for the surface water treatment for public supply and evaluating its performance. The ECF system was composed by two modular electrocoagulators followed by a helical tubular flocculator (HTF), with flowrate of 20 L∙min-1 . This configuration was developed for better use of the coagulants and microbubbles generated in the electrocoagulation by the formation of aerated flocs. The adopted conditions in the electrocoagulators were upward flow, aluminum electrodes, parallel monopolar connection, inter-electrodes distance of 3 mm, current density of 0.43-1.28 mA∙cm-2 , flow speed of 0.04 m∙s-1 , hydraulic detention time (HDT) of 51.0 s, and contact time with the electrodes of 43.3 s. The adopted conditions in the HTF were vertical orientation with upward flow, HDT of 6.36 min, speed gradient of 71.7-182.8 s -1 , Camp number of 27,366-69,770, and Reynolds number of 7,059. The study was performed at the water treatment plant of Santa Maria-RS, with water from the rivers Vacacaí-Mirim and Ibicuí-Mirim. The treatment was performed with pH adjustment of the water to 6.4. The ECF system was capable to provide turbidity of 1.3 ± 0.4 NTU and apparent color of 16.8 ± 5.8 uC to the treated water, which were appropriate for the further filtration step. Among the results of performance, the removal efficiency of total coliforms (95.6 ± 4.7%), E. coli (89.4 ± 8.8%), chlorophyll a (87.7 ± 10.9%), apparent color (73.0 ± 8.2%), and turbidity (79.9 ± 4.6%) were stand out, which shows the efficiency of the system in the water clarification and micro-organisms inactivation. The system had an energetic consumption of 0.02- 0.37 kWh∙m-3 , aluminum consumption of 3.0-9.0 mg∙L-1 , and hydrochloric acid of 2.5-21.5 mL∙m-3 . Operations of cleaning or electrodes change proved to be essential for keeping the energetic efficiency of the system. The energy consumption proved to be a good indicator for determining the moment to do it. The operation cost of the system was R$ 0.19 ± 0.07∙m-3 , where 49.1% referred to energy consumption, 44.1% to aluminum consumption, and 6.6% to hydrochloric acid consumption. The use of renewable energy sources can reduce the operational costs to R$ 0,10 ± 0,06∙m-3 . The ECF system showed potential of being diffused as an alternative technology for surface water treatment, compact, easily installable, operable, and automatable, especially attractive for decentralized supply systems (rural, riverside, peri-urban and/or hard-to-reach communities), as well as for coping with water scarcity and/or seasonal demands.Embora essencial para a vida, saúde e dignidade humana, existe uma grande parcela da população sem acesso a serviços de abastecimento de água. A maioria está situada em regiões de difícil acesso, baixa densidade demográfica e/ou alta dispersão espacial, inviabilizando soluções convencionais para o seu atendimento. Soluções inovadoras também são desejadas para complementar sistemas de abastecimento público frente à crescente escassez de água e suprir a crescente demanda por água em um espaço físico limitado. Assim, o objetivo deste estudo foi desenvolver um sistema de eletrocoagulação-flotação (sistema ECF), em escala piloto, para o tratamento de águas superficiais para abastecimento público e avaliar o seu desempenho. O sistema ECF foi composto por dois eletrocoaguladores modulares seguidos por um floculador tubular helicoidal (FTH), com vazão de 20 L∙min-1 . Esta configuração foi desenvolvida para melhor aproveitamento de coagulantes e microbolhas gerados na eletrocoagulação através da formação de flocos aerados. As condições adotadas para os eletrocoaguladores foram de fluxo ascendente, eletrodos de alumínio, conexão monopolar em paralelo, distância entre os eletrodos de 3 mm, densidade de corrente de 0,43-1,28 mA∙cm-2 , velocidade de escoamento de 0,04 m∙s -1 , tempo de detenção hidráulico (TDH) de 51,0 s e tempo de contato com os eletrodos de 43,3 s. As condições adotadas para o FTH foram de orientação vertical com fluxo ascendente, TDH de 6,36 min, gradiente de velocidade de 71,7-182,8 s-1 , número de Camp de 27.366-69.770 e número de Reynolds de 7.059. O estudo foi realizado na estação de tratamento de água de Santa Maria-RS, com água dos rios Vacacaí-Mirim e Ibicuí-Mirim. O tratamento foi realizado com ajuste do pH inicial da água para 6,4. O sistema ECF foi capaz de conferir turbidez de 1,3 ± 0,4 NTU e cor aparente de 16,8 ± 5,8 uC à água tratada, valores adequados para posterior etapa de filtração. Dentre os resultados de desempenho, destacam-se a eficiência de remoção de coliformes totais (95,6 ± 4,7%), E. coli (89,4 ± 8,8%), clorofila a (87,7 ± 10,9%), cor aparente (73,0 ± 8,2%) e turbidez (79,9 ± 4,6%), demonstrando a eficiência do sistema na clarificação da água e inativação de micro-organismos. O sistema apresentou consumo energético de 0,02-0,37 kWh∙m-3 , consumo de alumínio de 3,0-9,0 mg∙L-1 e consumo de ácido clorídrico de 2,5-21,5 mL∙m-3 . Operações de limpeza ou troca dos eletrodos se mostraram essenciais para manter a eficiência energética do sistema. O consumo energético se mostrou um bom indicador para determinar o momento de realizá-las. O custo operacional do sistema foi de R$ 0,19 ± 0,07∙m-3 , dos quais 49,1% foram referentes ao consumo energético, 44,1% ao consumo de alumínio e 6,6% ao consumo de ácido clorídrico. O uso de fontes de energia renovável pode reduzir os custos operacionais para R$ 0,10 ± 0,06∙m-3 . O sistema ECF demonstrou potencial de ser difundido como uma tecnologia alternativa de tratamento de águas superficiais, compacta, de fácil instalação, operação e automação, especialmente atrativo para sistemas de abastecimento descentralizados (comunidades rurais, ribeirinhas, de difícil acesso e/ou periurbanas), assim como para enfrentamento de escassez de água e/ou suprimento de demandas sazonais.Universidade Federal de Santa MariaBrasilEngenharia CivilUFSMPrograma de Pós-Graduação em Engenharia CivilCentro de TecnologiaCarissimi, Elvishttp://lattes.cnpq.br/4642912749433316Oyanedel-Craver, VinkaAzevedo, André Camargo deOliveira, Danieli Soares deMachado, Ênio LeandroRuotolo, Luis Augusto MartinsBrächer, Gustavo Holz2022-10-31T15:50:52Z2022-10-31T15:50:52Z2022-08-23info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/doctoralThesisapplication/pdfhttp://repositorio.ufsm.br/handle/1/26709porAttribution-NonCommercial-NoDerivatives 4.0 Internationalhttp://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/openAccessreponame:Manancial - Repositório Digital da UFSMinstname:Universidade Federal de Santa Maria (UFSM)instacron:UFSM2022-10-31T15:50:52Zoai:repositorio.ufsm.br:1/26709Biblioteca Digital de Teses e Dissertaçõeshttps://repositorio.ufsm.br/ONGhttps://repositorio.ufsm.br/oai/requestatendimento.sib@ufsm.br||tedebc@gmail.comopendoar:2022-10-31T15:50:52Manancial - Repositório Digital da UFSM - Universidade Federal de Santa Maria (UFSM)false
dc.title.none.fl_str_mv Desenvolvimento de um sistema de eletrocoagulação-flotação para o tratamento de água para abastecimento público
Development of an electrocoagulation-flotation system for the treatment of water for public supply
title Desenvolvimento de um sistema de eletrocoagulação-flotação para o tratamento de água para abastecimento público
spellingShingle Desenvolvimento de um sistema de eletrocoagulação-flotação para o tratamento de água para abastecimento público
Brächer, Gustavo Holz
Saneamento
Tratamento de água
Água potável
Processos eletroquímicos
Eletrocoagulação-flotação
Sanitation
Water treatment
Drinking water
Electrochemical process
Electrocoagulation-flotation
CNPQ::ENGENHARIAS::ENGENHARIA CIVIL
title_short Desenvolvimento de um sistema de eletrocoagulação-flotação para o tratamento de água para abastecimento público
title_full Desenvolvimento de um sistema de eletrocoagulação-flotação para o tratamento de água para abastecimento público
title_fullStr Desenvolvimento de um sistema de eletrocoagulação-flotação para o tratamento de água para abastecimento público
title_full_unstemmed Desenvolvimento de um sistema de eletrocoagulação-flotação para o tratamento de água para abastecimento público
title_sort Desenvolvimento de um sistema de eletrocoagulação-flotação para o tratamento de água para abastecimento público
author Brächer, Gustavo Holz
author_facet Brächer, Gustavo Holz
author_role author
dc.contributor.none.fl_str_mv Carissimi, Elvis
http://lattes.cnpq.br/4642912749433316
Oyanedel-Craver, Vinka
Azevedo, André Camargo de
Oliveira, Danieli Soares de
Machado, Ênio Leandro
Ruotolo, Luis Augusto Martins
dc.contributor.author.fl_str_mv Brächer, Gustavo Holz
dc.subject.por.fl_str_mv Saneamento
Tratamento de água
Água potável
Processos eletroquímicos
Eletrocoagulação-flotação
Sanitation
Water treatment
Drinking water
Electrochemical process
Electrocoagulation-flotation
CNPQ::ENGENHARIAS::ENGENHARIA CIVIL
topic Saneamento
Tratamento de água
Água potável
Processos eletroquímicos
Eletrocoagulação-flotação
Sanitation
Water treatment
Drinking water
Electrochemical process
Electrocoagulation-flotation
CNPQ::ENGENHARIAS::ENGENHARIA CIVIL
description Although essential for human life, health and dignity, there is a large proportion of people without access to services of water supply. Most of them are in regions with difficult access, low demographic density and/or high spatial dispersion, which makes unfeasible conventional solutions to serve them. Innovative solutions are also desired to complement public supply systems in face of the growing water scarcity and to supply the growing demand for water in a limited physical space. So, the objective of this study was developing an electrocoagulation-flotation system (ECF system), at pilot scale, for the surface water treatment for public supply and evaluating its performance. The ECF system was composed by two modular electrocoagulators followed by a helical tubular flocculator (HTF), with flowrate of 20 L∙min-1 . This configuration was developed for better use of the coagulants and microbubbles generated in the electrocoagulation by the formation of aerated flocs. The adopted conditions in the electrocoagulators were upward flow, aluminum electrodes, parallel monopolar connection, inter-electrodes distance of 3 mm, current density of 0.43-1.28 mA∙cm-2 , flow speed of 0.04 m∙s-1 , hydraulic detention time (HDT) of 51.0 s, and contact time with the electrodes of 43.3 s. The adopted conditions in the HTF were vertical orientation with upward flow, HDT of 6.36 min, speed gradient of 71.7-182.8 s -1 , Camp number of 27,366-69,770, and Reynolds number of 7,059. The study was performed at the water treatment plant of Santa Maria-RS, with water from the rivers Vacacaí-Mirim and Ibicuí-Mirim. The treatment was performed with pH adjustment of the water to 6.4. The ECF system was capable to provide turbidity of 1.3 ± 0.4 NTU and apparent color of 16.8 ± 5.8 uC to the treated water, which were appropriate for the further filtration step. Among the results of performance, the removal efficiency of total coliforms (95.6 ± 4.7%), E. coli (89.4 ± 8.8%), chlorophyll a (87.7 ± 10.9%), apparent color (73.0 ± 8.2%), and turbidity (79.9 ± 4.6%) were stand out, which shows the efficiency of the system in the water clarification and micro-organisms inactivation. The system had an energetic consumption of 0.02- 0.37 kWh∙m-3 , aluminum consumption of 3.0-9.0 mg∙L-1 , and hydrochloric acid of 2.5-21.5 mL∙m-3 . Operations of cleaning or electrodes change proved to be essential for keeping the energetic efficiency of the system. The energy consumption proved to be a good indicator for determining the moment to do it. The operation cost of the system was R$ 0.19 ± 0.07∙m-3 , where 49.1% referred to energy consumption, 44.1% to aluminum consumption, and 6.6% to hydrochloric acid consumption. The use of renewable energy sources can reduce the operational costs to R$ 0,10 ± 0,06∙m-3 . The ECF system showed potential of being diffused as an alternative technology for surface water treatment, compact, easily installable, operable, and automatable, especially attractive for decentralized supply systems (rural, riverside, peri-urban and/or hard-to-reach communities), as well as for coping with water scarcity and/or seasonal demands.
publishDate 2022
dc.date.none.fl_str_mv 2022-10-31T15:50:52Z
2022-10-31T15:50:52Z
2022-08-23
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/doctoralThesis
format doctoralThesis
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://repositorio.ufsm.br/handle/1/26709
url http://repositorio.ufsm.br/handle/1/26709
dc.language.iso.fl_str_mv por
language por
dc.rights.driver.fl_str_mv Attribution-NonCommercial-NoDerivatives 4.0 International
http://creativecommons.org/licenses/by-nc-nd/4.0/
info:eu-repo/semantics/openAccess
rights_invalid_str_mv Attribution-NonCommercial-NoDerivatives 4.0 International
http://creativecommons.org/licenses/by-nc-nd/4.0/
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
dc.publisher.none.fl_str_mv Universidade Federal de Santa Maria
Brasil
Engenharia Civil
UFSM
Programa de Pós-Graduação em Engenharia Civil
Centro de Tecnologia
publisher.none.fl_str_mv Universidade Federal de Santa Maria
Brasil
Engenharia Civil
UFSM
Programa de Pós-Graduação em Engenharia Civil
Centro de Tecnologia
dc.source.none.fl_str_mv reponame:Manancial - Repositório Digital da UFSM
instname:Universidade Federal de Santa Maria (UFSM)
instacron:UFSM
instname_str Universidade Federal de Santa Maria (UFSM)
instacron_str UFSM
institution UFSM
reponame_str Manancial - Repositório Digital da UFSM
collection Manancial - Repositório Digital da UFSM
repository.name.fl_str_mv Manancial - Repositório Digital da UFSM - Universidade Federal de Santa Maria (UFSM)
repository.mail.fl_str_mv atendimento.sib@ufsm.br||tedebc@gmail.com
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