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Previous issue date: 2011-10-24 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / Stabilization pond is the main technology used for treatment wastewater, in northeast Brazil, due to lower cost of deployment, operation and maintenance compared to other technologies. Most systems of stabilization ponds has been in operation for some time, on average 10 years of operation, receiving high organic loads and do not have good removal efficiencies of the main parameters for which have been designed. Therefore it is necessary to work to quantify the efficiency of current systems. This study evaluated the biodegradability of organic matter in raw sewage, the removal of organic matter in reactors and determination of the kinetic constant removal of organic matter (k), both in reactors and in raw sewage, based on the analysis made in the laboratory and through mathematical methods proposed in the literature, in nine systems stabilization ponds, located in Rio Grande do Norte. In relation the degradation kinetics in stabilization ponds, it was observed that many papers published in the literature were obtained in pilot-scale systems, which often, due to the action of external factors such as wind and temperature, these can t be considered as a reference in the analysis of the kinetic constant K, so the need for more research into systems of scale. This study had three distinct phases and simultaneous, routine monitoring, study of the daily cycle and the determination of kinetic constant of degradation of organic matter (K). The monitoring showed that the removal efficiencies of organic matter on most systems were lower than suggested by the literature, the best efficiencies of around 76% (BOD) and 72% (COD) and the worst of the order of 48% (BOD) and 55% (COD). The calculation of K in raw sewage (Ke) was within the range of variation expected in the literature (0.35 to 0.60 days-1). Already for the results obtained for K in the reactors (Kr), there were well below the values recommended in the literature (0.25 to 0.40 d-1 for complete mix and from 0.13 to 0.17 d-1 for flow dispersed), in line with the overloads that organic systems are subject / Lagoa de estabiliza??o ? a principal tecnologia utilizada para tratamento de esgotos dom?sticos no Nordeste brasileiro, devido ao menor custo de implanta??o, opera??o e manuten??o, quando comparada com outras tecnologias. A maioria dos sistemas de lagoas de estabiliza??o est? em opera??o h? bastante tempo, em m?dia 10 anos de opera??o, recebem altas cargas org?nicas e n?o apresentam boas efici?ncias de remo??o dos principais par?metros a qual foram projetadas. Portanto, faz-se necess?rio um trabalho que quantifique a efici?ncia atual desses sistemas. O presente estudo avaliou a biodegradabilidade da mat?ria org?nica no esgoto bruto, a remo??o da mat?ria org?nica nos reatores e a determina??o da constante cin?tica de remo??o de mat?ria org?nica (k), tanto nos reatores quanto no esgoto bruto, baseadas nas an?lises feitas em laborat?rio e atrav?s dos m?todos matem?ticos propostos pela literatura, em nove sistemas de lagoas de estabiliza??o, no Rio Grande do Norte. Em rela??o ? cin?tica de degrada??o em lagoas de estabiliza??o, observou-se que muitos trabalhos publicados na literatura foram obtidos em sistemas em escala piloto, o que muitas vezes, devido ? a??o de fatores externos, tais como vento e temperatura, esses n?o podem ser considerados como refer?ncia na an?lise da constante cin?tica K, por isso a necessidade de se pesquisar mais em sistemas de escala real. Essa pesquisa teve tr?s fases distintas e simult?neas: monitora??o de rotina, estudo do ciclo di?rio e a determina??o da constante cin?tica de degrada??o da mat?ria org?nica (K). O monitoramento mostrou que as efici?ncias de remo??o de mat?ria org?nica, na maioria dos sistemas, estavam abaixo do sugerido pela literatura, sendo as melhores efici?ncias da ordem de 76% (DBO) e de 72% (DQO) e as piores da ordem de 48% (DBO) e 55% (DQO). O calculo do K no esgoto bruto (Ke) mostrou-se dentro da faixa de varia??o prevista na literatura (0,35 a 0,60 dia-1). J? para os resultados obtidos para K nos reatores (Kr), verificaram-se valores bem abaixo do preconizado pela literatura (0,25 a 0,40 d-1 para mistura completa e 0,13 a 0,17 d-1 para fluxo disperso), em conson?ncia com as sobrecargas org?nicas a que os sistemas est?o sujeitos
| Identifer | oai:union.ndltd.org:IBICT/oai:repositorio.ufrn.br:123456789/15984 |
| Date | 24 October 2011 |
| Creators | Silva, Od?nia Alves de Lima |
| Contributors | CPF:37695045268, http://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4799320A6, Andrade Neto, C?cero Onofre de, CPF:05712939487, ANDRADE NETO, C?cero Onofre de, Ingunza, Maria Del Pilar Durante, CPF:00871819406, http://lattes.cnpq.br/1925954531585024, Ara?jo, Andr? Luis Calado |
| Publisher | Universidade Federal do Rio Grande do Norte, Programa de P?s-gradua??o em Engenharia Sanit?ria, UFRN, BR, Saneamento Ambiental; Meio Ambiente; Recursos H?dricos e Hidr?ulica |
| Source Sets | IBICT Brazilian ETDs |
| Language | Portuguese |
| Detected Language | English |
| Type | info:eu-repo/semantics/publishedVersion, info:eu-repo/semantics/masterThesis |
| Format | application/pdf |
| Source | reponame:Repositório Institucional da UFRN, instname:Universidade Federal do Rio Grande do Norte, instacron:UFRN |
| Rights | info:eu-repo/semantics/openAccess |
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