Pós-tratamento de efluente anaeróbio em lagoa de polimento

Detalhes bibliográficos
Ano de defesa: 2015
Autor(a) principal: Sousa, Tales Abreu Tavares de lattes
Orientador(a): Lopes, Wilton Silva lattes
Banca de defesa: Leite, Valderi Duarte lattes, Athayde Júnior, Gilson Barbosa lattes
Tipo de documento: Dissertação
Tipo de acesso: Acesso aberto
Idioma: por
Instituição de defesa: Universidade Estadual da Paraíba
Programa de Pós-Graduação: Programa de Pós-Graduação em Ciência e Tecnologia Ambiental - PPGCTA
Departamento: Pró-Reitoria de Pós-Graduação e Pesquisa - PRPGP
País: BR
Palavras-chave em Português:
Palavras-chave em Inglês:
Área do conhecimento CNPq:
Link de acesso: https://repositorio.uepb.edu.br/handle/123456789/72244
Resumo: The domestic sewage treatment in UASBs reactors followed by polishing pond is a sustainable alternative, especially to the northeast of Brazil. Therefore, the present study applied polishing ponds as anaerobic effluent post-treatment. Two treatment systems were constructed and operated: 1) compact station (UASB reactor with intermittent flow sand filter) followed by two 0.18 m deep shallow polishing ponds; 2) UASB reactor followed by two polishing ponds with different hydraulic systems (batch and continuous) and same depth (0.60 m). At system 1, at experimental conditions, with low organic concentration (87 mgO2.L -1 filtered COD and 49 mgSSV.L -1 ), high sunlight incidence (597 Wm ), high temperature (20 to 30 ºC) and carbon dioxide biological consumption sufficient to raise the average pH units; the pond 1, feed with the aerobic effluent from the compact system, reached a 9.6 pH and provided an average removal of 86% of the total kjeldahl nitrogen, 82% of total phosphorus and 88% ortho-phosphate and coliform less than 1000 UFC.100ml meeting the requirements of WHO (2006) for unrestricted irrigation. Also at system 1, the pond 2, feed with the anaerobic effluent from the compact system, reached a 8.6 pH and removed 80% NTK-N, 53% of total phosphorus and 44% ortho-phosphate, but did not obtain coliform final average less than 1000 UFC.100ml -1 . Both the 0.60 m deep ponds, 9 days batch and 12 days continuous hydraulic systems, achieved low nutrients removal and poor coliform efficiency, 96,85 and 97,21 %, equivalent to only two log units. Also achieved a negligible removal efficiency for both total phosphorus (efficiency <2%) and for ortho-phosphate (efficiency <25%); the NTK-N removal, compared to the ponds of 0.18 m were inefficient average values, 55% and 68% for PP3 and PP4 respectively.
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spelling 2016-03-03T13:32:02Z2026-02-25T13:03:59Z2015-02-27SOUSA, T. A. T. de. Pós-tratamento de efluente anaeróbio em lagoa de polimento. 2015. 80f. Dissertação (Programa de Pós-Graduação em Ciência e Tecnologia Ambiental - PPGCTA) - Universidade Estadual da Paraíba, Campina Grande, 2015.https://repositorio.uepb.edu.br/handle/123456789/7224424004014005P9The domestic sewage treatment in UASBs reactors followed by polishing pond is a sustainable alternative, especially to the northeast of Brazil. Therefore, the present study applied polishing ponds as anaerobic effluent post-treatment. Two treatment systems were constructed and operated: 1) compact station (UASB reactor with intermittent flow sand filter) followed by two 0.18 m deep shallow polishing ponds; 2) UASB reactor followed by two polishing ponds with different hydraulic systems (batch and continuous) and same depth (0.60 m). At system 1, at experimental conditions, with low organic concentration (87 mgO2.L -1 filtered COD and 49 mgSSV.L -1 ), high sunlight incidence (597 Wm ), high temperature (20 to 30 ºC) and carbon dioxide biological consumption sufficient to raise the average pH units; the pond 1, feed with the aerobic effluent from the compact system, reached a 9.6 pH and provided an average removal of 86% of the total kjeldahl nitrogen, 82% of total phosphorus and 88% ortho-phosphate and coliform less than 1000 UFC.100ml meeting the requirements of WHO (2006) for unrestricted irrigation. Also at system 1, the pond 2, feed with the anaerobic effluent from the compact system, reached a 8.6 pH and removed 80% NTK-N, 53% of total phosphorus and 44% ortho-phosphate, but did not obtain coliform final average less than 1000 UFC.100ml -1 . Both the 0.60 m deep ponds, 9 days batch and 12 days continuous hydraulic systems, achieved low nutrients removal and poor coliform efficiency, 96,85 and 97,21 %, equivalent to only two log units. Also achieved a negligible removal efficiency for both total phosphorus (efficiency <2%) and for ortho-phosphate (efficiency <25%); the NTK-N removal, compared to the ponds of 0.18 m were inefficient average values, 55% and 68% for PP3 and PP4 respectively.O tratamento de esgotos domésticos em reatores UASBs seguido de lagoa de polimento é uma alternativa sustentável, sobretudo para o nordeste do Brasil. Dessa forma, o presente trabalho utilizou lagoas de polimento como pós-tratamento de efluente de reator UASB. Foram construídos e operados dois sistemas de tratamento: 1) Estação compacta (reator UASB com filtro de areia de fluxo intermitente) seguido de duas lagoas de polimento rasas, com profundidade de 0,18 m; 2) Reator UASB seguido de duas lagoas de polimento, com diferentes regimes hidráulicos (batelada e contínuo) e mesma profundidade (0,60 m). No sistema 1, nas condições do experimento, com baixa concentração orgânica (83±25 mgO de DQO filtrada e 49±6 mgSSV.L -1 ), alta incidência de luz solar (597 W.m ) temperatura variando de 20 a 30 ºC, e consumo biológico de gás carbônico suficiente para elevar a média das unidades de pH; a lagoa 1, alimentada pelo efluente aeróbio da estação compacta, alcançou um pH 9,6 e garantiu remoção média de 86% de nitrogênio total kjeldahl, 82% de fósforo total e 88% de ortofosfato e coliformes termotolerantes menor que 1000 UFC.100ml atendendo a exigência da OMS (WHO, 2006) para irrigação irrestrita. Ainda no sistema 1, a lagoa 2, alimentada pelo efluente anaeróbio da estação compacta rasa de polimento, alcançou pH de 8,6 e removeu 80% de N-NTK, 53% de fósforo total e 44% de ortofosfato, e coliformes termotolerantes maior que 1000 UFC.100ml -1 . As lagoas 0,60 m de profundidade, operadas em batelada e em fluxo contínuo, respectivamente com TDH de 9 e 12 dias, apresentaram baixa remoção de nutrientes e pouca eficiência de remoção de coliformes, 96,85 e 97,21 %, equivalentes apenas duas unidades logs. Apresentam também uma insignificante eficiência de remoção, tanto para fósforo total (eficiência<2%) quanto para ortofosfato (eficiência < 25%), e as remoções de N-NTK, quando comparadas com as lagoas de 0,18 m, são de valores médios ineficientes, 55% e 68% para LP3 e LP4, respectivamente.Conselho Nacional de Pesquisa e Desenvolvimento Científico e Tecnológico - CNPqapplication/pdfUniversidade Estadual da ParaíbaPrograma de Pós-Graduação em Ciência e Tecnologia Ambiental - PPGCTAUEPBBRPró-Reitoria de Pós-Graduação e Pesquisa - PRPGPPró-Reitoria de Pós-Graduação e Pesquisa - PRPGPhttp://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/openAccessDisinfectionPolishing pondsENGENHARIASTratamento de efluenteLagoa de polimentoDesinfecçãoPós-tratamento de efluente anaeróbio em lagoa de polimentoinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesisHenrique, Israel Nuneshttp://lattes.cnpq.br/3418821931567495Leite, Valderi Duartehttp://lattes.cnpq.br/2319382787465258Athayde Júnior, Gilson Barbosahttp://lattes.cnpq.br/8220830326280125Lopes, Wilton Silvahttp://lattes.cnpq.br/1493216651945826http://lattes.cnpq.br/1214222841885518Sousa, Tales Abreu Tavares deporreponame:Repositório Institucional da Universidade Estadual da Paraíba (UEPB)instname:Universidade Estadual da Paraíba (UEPB)instacron:UEPBLICENSElicense.txtlicense.txttext/plain; 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dc.title.none.fl_str_mv Pós-tratamento de efluente anaeróbio em lagoa de polimento
title Pós-tratamento de efluente anaeróbio em lagoa de polimento
spellingShingle Pós-tratamento de efluente anaeróbio em lagoa de polimento
Sousa, Tales Abreu Tavares de
Disinfection
Polishing ponds
ENGENHARIAS
Tratamento de efluente
Lagoa de polimento
Desinfecção
title_short Pós-tratamento de efluente anaeróbio em lagoa de polimento
title_full Pós-tratamento de efluente anaeróbio em lagoa de polimento
title_fullStr Pós-tratamento de efluente anaeróbio em lagoa de polimento
title_full_unstemmed Pós-tratamento de efluente anaeróbio em lagoa de polimento
title_sort Pós-tratamento de efluente anaeróbio em lagoa de polimento
author Sousa, Tales Abreu Tavares de
author_facet Sousa, Tales Abreu Tavares de
author_role author
dc.contributor.advisor-co1.fl_str_mv Henrique, Israel Nunes
dc.contributor.advisor-co1Lattes.fl_str_mv http://lattes.cnpq.br/3418821931567495
dc.contributor.referee1.fl_str_mv Leite, Valderi Duarte
dc.contributor.referee1Lattes.fl_str_mv http://lattes.cnpq.br/2319382787465258
dc.contributor.referee2.fl_str_mv Athayde Júnior, Gilson Barbosa
dc.contributor.referee2Lattes.fl_str_mv http://lattes.cnpq.br/8220830326280125
dc.contributor.advisor1.fl_str_mv Lopes, Wilton Silva
dc.contributor.advisor1Lattes.fl_str_mv http://lattes.cnpq.br/1493216651945826
dc.contributor.authorLattes.fl_str_mv http://lattes.cnpq.br/1214222841885518
dc.contributor.author.fl_str_mv Sousa, Tales Abreu Tavares de
contributor_str_mv Henrique, Israel Nunes
Leite, Valderi Duarte
Athayde Júnior, Gilson Barbosa
Lopes, Wilton Silva
dc.subject.eng.fl_str_mv Disinfection
Polishing ponds
topic Disinfection
Polishing ponds
ENGENHARIAS
Tratamento de efluente
Lagoa de polimento
Desinfecção
dc.subject.cnpq.fl_str_mv ENGENHARIAS
dc.subject.por.fl_str_mv Tratamento de efluente
Lagoa de polimento
Desinfecção
description The domestic sewage treatment in UASBs reactors followed by polishing pond is a sustainable alternative, especially to the northeast of Brazil. Therefore, the present study applied polishing ponds as anaerobic effluent post-treatment. Two treatment systems were constructed and operated: 1) compact station (UASB reactor with intermittent flow sand filter) followed by two 0.18 m deep shallow polishing ponds; 2) UASB reactor followed by two polishing ponds with different hydraulic systems (batch and continuous) and same depth (0.60 m). At system 1, at experimental conditions, with low organic concentration (87 mgO2.L -1 filtered COD and 49 mgSSV.L -1 ), high sunlight incidence (597 Wm ), high temperature (20 to 30 ºC) and carbon dioxide biological consumption sufficient to raise the average pH units; the pond 1, feed with the aerobic effluent from the compact system, reached a 9.6 pH and provided an average removal of 86% of the total kjeldahl nitrogen, 82% of total phosphorus and 88% ortho-phosphate and coliform less than 1000 UFC.100ml meeting the requirements of WHO (2006) for unrestricted irrigation. Also at system 1, the pond 2, feed with the anaerobic effluent from the compact system, reached a 8.6 pH and removed 80% NTK-N, 53% of total phosphorus and 44% ortho-phosphate, but did not obtain coliform final average less than 1000 UFC.100ml -1 . Both the 0.60 m deep ponds, 9 days batch and 12 days continuous hydraulic systems, achieved low nutrients removal and poor coliform efficiency, 96,85 and 97,21 %, equivalent to only two log units. Also achieved a negligible removal efficiency for both total phosphorus (efficiency <2%) and for ortho-phosphate (efficiency <25%); the NTK-N removal, compared to the ponds of 0.18 m were inefficient average values, 55% and 68% for PP3 and PP4 respectively.
publishDate 2015
dc.date.issued.fl_str_mv 2015-02-27
dc.date.accessioned.fl_str_mv 2016-03-03T13:32:02Z
2026-02-25T13:03:59Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
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dc.identifier.citation.fl_str_mv SOUSA, T. A. T. de. Pós-tratamento de efluente anaeróbio em lagoa de polimento. 2015. 80f. Dissertação (Programa de Pós-Graduação em Ciência e Tecnologia Ambiental - PPGCTA) - Universidade Estadual da Paraíba, Campina Grande, 2015.
dc.identifier.uri.fl_str_mv https://repositorio.uepb.edu.br/handle/123456789/72244
dc.identifier.capesdegreeprogramcode.none.fl_str_mv 24004014005P9
identifier_str_mv SOUSA, T. A. T. de. Pós-tratamento de efluente anaeróbio em lagoa de polimento. 2015. 80f. Dissertação (Programa de Pós-Graduação em Ciência e Tecnologia Ambiental - PPGCTA) - Universidade Estadual da Paraíba, Campina Grande, 2015.
24004014005P9
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