REMOÇÃO DE NITROGÊNIO AMONIACAL E FÓSFORO DE ESGOTO SANITÁRIO EM BIORREATOR À MEMBRANA COM LEITO MÓVEL IRATI, PR

Detalhes bibliográficos
Autor(a) principal: Rodrigues, Hiromi Umezawa
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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spelling 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
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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.
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dc.publisher.initials.fl_str_mv UNICENTRO
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dc.publisher.department.fl_str_mv Unicentro::Departamento de Ciências Agrárias e Ambientais
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