REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR
Autor(a) principal: | |
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Data de Publicação: | 2018 |
Tipo de documento: | Dissertação |
Idioma: | por |
Título da fonte: | Biblioteca Digital de Teses e Dissertações do UNICENTRO |
Texto Completo: | http://tede.unicentro.br:8080/jspui/handle/jspui/1110 |
Resumo: | This study evaluated the removal efficiency of ammoniacal nitrogen (NH4 +) and phosphorus (PO4 3) during operation of a moving bed membrane bioreactor (MBR) for wastewater treatment. The experimental system was operated in sequential batches in four different strategies, E1, E2, E3 and E4, in which the order of the aerobic and anaerobic phases and the presence or absence of the moving bed varied. The concentration of total suspended solids (TSS) in the MBR mixed liquor was controlled between 2 g L-1 and 4 g L-1. The average removal efficiency of NH4 +-N was 82.8%, and the E1 strategy had better performance reaching 93.4% removal. In this strategy, the aerobic stage precedes the anaerobic stage and the moving bed was present. The statistical analysis showed that the order of the aerobic and anaerobic stages influences meaningfully in the removal efficiency of NH4 +-N with p-value of 0.000278. The E4 strategy, operated without the moving bed and with the aerobic stage followed by anaerobic, obtained the best denitrification values, the average efficiency was 90.7%, without addition of external carbon source. The average removal efficiency of PO4 3-P was 61.2% for its soluble form and 57% for total PO4 3-P, and there was no statistically significant difference in the means of phosphorus removal rates from one strategy to another. There was no variation in the concentration of PO4 3--P in the mixed liquor during the aerobic and anaerobic stages, therefore the main mechanism phosphorus removal was not biological, but physical by the selectivity of the membranes. |
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Vidal, Carlos Magno de Sousahttp://lattes.cnpq.br/1554298849674091Jungles, Mariele Katherinehttp://lattes.cnpq.br/5147528194257932040.519.619-90http://lattes.cnpq.br/7989371781589068Rodrigues, Hiromi Umezawa2019-06-04T11:27:30Z2018-09-28Rodrigues, Hiromi Umezawa. REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR. 2018. 95 f. Dissertação (Programa de Pós-Graduação em Engenharia Sanitária e Ambiental - Mestrado / Associação Ampla com UEPG) - Universidade Estadual do Centro-Oeste, Irati - PR.http://tede.unicentro.br:8080/jspui/handle/jspui/1110This study evaluated the removal efficiency of ammoniacal nitrogen (NH4 +) and phosphorus (PO4 3) during operation of a moving bed membrane bioreactor (MBR) for wastewater treatment. The experimental system was operated in sequential batches in four different strategies, E1, E2, E3 and E4, in which the order of the aerobic and anaerobic phases and the presence or absence of the moving bed varied. The concentration of total suspended solids (TSS) in the MBR mixed liquor was controlled between 2 g L-1 and 4 g L-1. The average removal efficiency of NH4 +-N was 82.8%, and the E1 strategy had better performance reaching 93.4% removal. In this strategy, the aerobic stage precedes the anaerobic stage and the moving bed was present. The statistical analysis showed that the order of the aerobic and anaerobic stages influences meaningfully in the removal efficiency of NH4 +-N with p-value of 0.000278. The E4 strategy, operated without the moving bed and with the aerobic stage followed by anaerobic, obtained the best denitrification values, the average efficiency was 90.7%, without addition of external carbon source. The average removal efficiency of PO4 3-P was 61.2% for its soluble form and 57% for total PO4 3-P, and there was no statistically significant difference in the means of phosphorus removal rates from one strategy to another. There was no variation in the concentration of PO4 3--P in the mixed liquor during the aerobic and anaerobic stages, therefore the main mechanism phosphorus removal was not biological, but physical by the selectivity of the membranes.Este trabalho avaliou a eficiência de remoção de nitrogênio amoniacal (NH4 +) e fósforo (PO4 3-) durante a operação de um biorreator à membrana (BRM) com leito móvel aplicado ao tratamento de esgoto sanitário. O sistema experimental foi operado em bateladas sequenciais em quatro estratégias diferentes, E1, E2, E3 e E4, nas quais variavam-se a ordem das fases aeróbia e anaeróbia e a presença ou não de leito móvel. A concentração de sólidos suspensos totais (SST) no licor misto do BRM foi controlada entre 2 g L-1 e 4 g L-1. A eficiência média de remoção de NH4 +-N foi de 82,8%, sendo que a estratégia E1 teve melhor desempenho neste quesito alcançando 93,4% de remoção. Nesta estratégia, a etapa aeróbia precede a etapa anaeróbia e há a presença de leito móvel. A análise estatística apontou que a ordem das etapas aeróbia e anaeróbia influencia de forma significativa na eficiência de remoção de NH4 +-N com p-valor de 0,000278. Na estratégia E4, operada sem leito móvel e com ciclo aeróbio seguido de anaeróbio, se obteve a melhor eficiência média de desnitrificação de 90,7%, sem adição de fonte externa de carbono. As médias de eficiência de remoção de PO4 3--P solúvel e total foram de 61,2% e 57% respectivamente, não havendo diferença estatisticamente significativa nas médias de remoção de fósforo de uma estratégia para outra. Não se observou variação na concentração de PO4 3--P no licor misto durante as etapas aeróbia e anaeróbia, portanto o principal mecanismo de remoção de fósforo não foi biológico, e sim físico pela seletividade das membranas.Submitted by Fabiano Jucá (fjuca@unicentro.br) on 2019-06-04T11:27:30Z No. of bitstreams: 1 Hiromi Umezawa Rodrigues.pdf: 5128730 bytes, checksum: d466a8647adcab83225605018bbe3d85 (MD5)Made available in DSpace on 2019-06-04T11:27:30Z (GMT). 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dc.title.por.fl_str_mv |
REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR |
title |
REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR |
spellingShingle |
REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR Rodrigues, Hiromi Umezawa biomídias remoção de nutrientes nitrificação-desnitrificação EPBR BRM biomedias nutrient removal nitrification-denitrification EPBR MBR ENGENHARIAS::ENGENHARIA SANITARIA |
title_short |
REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR |
title_full |
REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR |
title_fullStr |
REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR |
title_full_unstemmed |
REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR |
title_sort |
REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR |
author |
Rodrigues, Hiromi Umezawa |
author_facet |
Rodrigues, Hiromi Umezawa |
author_role |
author |
dc.contributor.advisor1.fl_str_mv |
Vidal, Carlos Magno de Sousa |
dc.contributor.advisor1Lattes.fl_str_mv |
http://lattes.cnpq.br/1554298849674091 |
dc.contributor.advisor-co1.fl_str_mv |
Jungles, Mariele Katherine |
dc.contributor.advisor-co1Lattes.fl_str_mv |
http://lattes.cnpq.br/5147528194257932 |
dc.contributor.authorID.fl_str_mv |
040.519.619-90 |
dc.contributor.authorLattes.fl_str_mv |
http://lattes.cnpq.br/7989371781589068 |
dc.contributor.author.fl_str_mv |
Rodrigues, Hiromi Umezawa |
contributor_str_mv |
Vidal, Carlos Magno de Sousa Jungles, Mariele Katherine |
dc.subject.por.fl_str_mv |
biomídias remoção de nutrientes nitrificação-desnitrificação EPBR BRM |
topic |
biomídias remoção de nutrientes nitrificação-desnitrificação EPBR BRM biomedias nutrient removal nitrification-denitrification EPBR MBR ENGENHARIAS::ENGENHARIA SANITARIA |
dc.subject.eng.fl_str_mv |
biomedias nutrient removal nitrification-denitrification EPBR MBR |
dc.subject.cnpq.fl_str_mv |
ENGENHARIAS::ENGENHARIA SANITARIA |
description |
This study evaluated the removal efficiency of ammoniacal nitrogen (NH4 +) and phosphorus (PO4 3) during operation of a moving bed membrane bioreactor (MBR) for wastewater treatment. The experimental system was operated in sequential batches in four different strategies, E1, E2, E3 and E4, in which the order of the aerobic and anaerobic phases and the presence or absence of the moving bed varied. The concentration of total suspended solids (TSS) in the MBR mixed liquor was controlled between 2 g L-1 and 4 g L-1. The average removal efficiency of NH4 +-N was 82.8%, and the E1 strategy had better performance reaching 93.4% removal. In this strategy, the aerobic stage precedes the anaerobic stage and the moving bed was present. The statistical analysis showed that the order of the aerobic and anaerobic stages influences meaningfully in the removal efficiency of NH4 +-N with p-value of 0.000278. The E4 strategy, operated without the moving bed and with the aerobic stage followed by anaerobic, obtained the best denitrification values, the average efficiency was 90.7%, without addition of external carbon source. The average removal efficiency of PO4 3-P was 61.2% for its soluble form and 57% for total PO4 3-P, and there was no statistically significant difference in the means of phosphorus removal rates from one strategy to another. There was no variation in the concentration of PO4 3--P in the mixed liquor during the aerobic and anaerobic stages, therefore the main mechanism phosphorus removal was not biological, but physical by the selectivity of the membranes. |
publishDate |
2018 |
dc.date.issued.fl_str_mv |
2018-09-28 |
dc.date.accessioned.fl_str_mv |
2019-06-04T11:27:30Z |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
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info:eu-repo/semantics/masterThesis |
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masterThesis |
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publishedVersion |
dc.identifier.citation.fl_str_mv |
Rodrigues, Hiromi Umezawa. REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR. 2018. 95 f. Dissertação (Programa de Pós-Graduação em Engenharia Sanitária e Ambiental - Mestrado / Associação Ampla com UEPG) - Universidade Estadual do Centro-Oeste, Irati - PR. |
dc.identifier.uri.fl_str_mv |
http://tede.unicentro.br:8080/jspui/handle/jspui/1110 |
identifier_str_mv |
Rodrigues, Hiromi Umezawa. REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR. 2018. 95 f. Dissertação (Programa de Pós-Graduação em Engenharia Sanitária e Ambiental - Mestrado / Associação Ampla com UEPG) - Universidade Estadual do Centro-Oeste, Irati - PR. |
url |
http://tede.unicentro.br:8080/jspui/handle/jspui/1110 |
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por |
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por |
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8192256085508296768 |
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Universidade Estadual do Centro-Oeste |
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Programa de Pós-Graduação em Engenharia Sanitária e Ambiental (Mestrado / Associação Ampla com UEPG) |
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UNICENTRO |
dc.publisher.country.fl_str_mv |
Brasil |
dc.publisher.department.fl_str_mv |
Unicentro::Departamento de Ciências Agrárias e Ambientais |
publisher.none.fl_str_mv |
Universidade Estadual do Centro-Oeste |
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