RESUMO

Although anaerobic reactors are an excellent alternative in the treatment of domestic effluents, they have the disadvantage of requiring post-treatment. Many technologies have been studied and, recently, rapid filtration systems have been presented as a viable alternative for post-treatment. This work compared post-treatment techniques for anaerobic upflow sludge blanket (UASB) reactors by rapid filtration systems (double filtration (DF); triple filtration with clinoptilolite (TFc); and triple filtration with activated carbon (TFac)) to conventional systems (facultative pond (FP); biological filter (BF); biological filter with recirculation and decantation (BFD)), verifying their potential for improvement of the final effluent quality. The UASB effluent post-treatments by FP, BF, BFD, DF, TFc, and TFac were evaluated. The removal of turbidity in both BFD and FP post-treatments was below 75%. The DF, TFc, and TFac treatments showed over 99% removal of the same parameters. COD removal in the FP, BF, and BFD post-treatments was over 10%, while in the DF, TFc, and TFac treatments, it was over 80%. The greatest total phosphorus removal was observed in TFc and TFac, whose values were over 99%. The best removal of ammoniacal nitrogen, 99% was observed in the TFc treatment. Regarding Al, Cd, Cr, Cu, Mn, Ni, Pb, and Zn removal, all rapid filtration systems showed better performance when compared to conventional systems. The DF, TFc, and TFac systems showed over 90% removal of most metals evaluated, while the FP and BF treatments presented values below 50% for most metals, and in the BFD system, the removal values were below 80% for most metals. The results indicate that rapid filtration systems were better at removing all evaluated parameters when compared to conventional systems.

Assuntos

RESUMO

This study evaluates the efficacy of a sanitary sewage treatment system, proposing post-treatment of the effluent generated by the upflow anaerobic sludge blanket UASB reactor, through a Fenton coagulation/oxidation ((ferric chloride (FC) or ferrous sulfate (FS) and peracetic acid (PAA)), followed by a double filtration system, composed of a gravel ascending drainage filter and a sand descending filter. Following the assessment of treatability, the system efficiency was evaluated using physicochemical and microbiological parameters. In all treatments performed in the pilot unit, total suspended solids (TSS) were completely removed, leading to a decrease in turbidity greater than 90% and close to 100% removal of total phosphorous. In the FC and PAA combination, the effluent was oxygenated prior to filtration, enabling a more significant removal of biochemical oxygen demand (BOD), which characterizes aerobic degradation even in a quick sand filter. The treatments carried out in the presence of the PAA oxidizing agent showed a more significant bleaching of the effluent. Concerning the microbiological parameters, the simultaneous use of PAA and FC contributed to the partial inactivation of the assessed microorganisms. A 65% recovery of the effluent was obtained with the proposed treatment system, considering the volume employed in filter backwashing.

Assuntos

RESUMO

A implantação de uma unidade de pré-tratamento a montante de um filtro ascendente (FA) existente objetiva condicionar a água bruta eutrofizada à capacidade de tratamento do FA. Essa solução esbarra na necessidade de se instalar essa unidade de pré-tratamento com cota mais elevada que o filtro a jusante. Nesta pesquisa, a instalação de um filtro de pressão de fluxo descendente possibilitou a eliminação do problema do desnível geométrico e a adequação da água bruta com elevada presença de fitoplâncton às limitações da filtração direta ascendente (FDA). O pré-filtro de pressão com melhor eficiência, o PFP1, apresentou uma remoção de 50% de cor aparente e 63% de turbidez. A eficiência global do sistema PFP/FA foi satisfatória, apresentando turbidez final inferior a 0,5 uT, cor aparente em torno de 5 uH, além de reduzir as perdas da água tratada de 11,7 para 4,5%.

The implementation of a pretreatment unit before existing upward filter, to condition the eutrophic raw waters to its capacity, is an option which runs into a problem of technical nature, the need of a pretreatment unit with enough hydraulic load to properly feed the existing filter. Typically, the available studies on double filtration present upward filters followed by descendant ones. In this study, the installation of a pressure filter downflow adapted the raw water with high algae concentration to the upward direct filtration system limitations, improving the quality of water produced and reducing losses by washing. The pressure filter with better efficiency was the PFP1 filter showed a removal of 50% of apparent color and 63% of turbidity. The overall efficiency of the PFP/FA system was satisfactory, presenting final turbidity of less than 0.5 uT, apparent color around 5 uH and reducing losses from 11.7 to 4.5% of the total treated water.

RESUMO

Este trabalho teve como objetivo avaliar o tratamento de água bruta proveniente de um reservatório de água, utilizando instalação piloto de dupla filtração (DF), composta por filtro ascendente de pedregulho (FAP) e filtro rápido descendente de areia (FRD), seguida de uma unidade de pós-tratamento com carvão ativado granular (CAG). Adicionalmente, foi verificado o efeito da pré e interoxidação (entre o FAP e o FRD) na eficiência global do tratamento e na formação de subprodutos orgânicos halogenados (SOH). Em função dos resultados obtidos, foi observado que a pré-oxidação melhorou a qualidade do efluente do FAP e a interoxidação favoreceu que resultassem valores menores de turbidez e cor no efluente do FRD. O processo de tratamento por adsorção em carvão ativado granular, utilizado como pós-tratamento, mostrou-se eficiente para assegurar a qualidade dos efluentes finais nos ensaios realizados, especialmente, em relação à remoção de matéria orgânica, cianobactérias e cor. As concentrações máximas de SOH encontrados nos efluentes do FRD e do FCAG não ultrapassaram os valores limites da Portaria nº 2.914/2011 do Ministério da Saúde.

This study evaluated the treatment of raw lake water using a double filtration (DF) pilot plant consisting of an up-flow gravel filter (UGF) in series with a down-flow sand filter (DSF) and followed by a post-treatment granular activated carbon (GAC) unit. Additionally, the study examines the effect of pre and inter-oxidation (between UGF and DSF) on overall efficiency in the treatment and the formation of halogenated organic byproducts (HOB). According to the results obtained, it was observed that the pre-oxidation improved the quality of the UGF effluent and the inter-oxidation favored lower values of turbidity and color in the DSF effluent. Also, the treatment process by adsorption on granular activated carbon, used as a post-treatment, was efficient to ensure the quality of final effluent in the tests, especially regarding the removal of organic matter, cyanobacteria, and color. The maximum concentrations of HOB found in the effluents from the DSF and GAC did not exceed the limits of the Brazilian drinking water standards (Portaria nº 2.914/2011).

RESUMO

A utilização de um modelo matemático permite a obtenção de condições otimizadas de operação, o que conduz à melhoria do controle e da previsão do processo de filtração. Os modelos matemáticos descrevem o processo de filtração através dos mecanismos de remoção de partículas que ocorre no meio filtrante. Este trabalho propõe a modelação matemática baseada nos modelos que descrevem macroscopicamente o processo de filtração e que incluem, por exemplo, o mecanismo de desprendimento de partículas do meio filtrante e a alteração da porosidade do material retido durante a filtração. O modelo desenvolvido foi adaptado para a aplicação à filtração direta ascendente em material granular de areia grossa inserido no processo de dupla filtração.

The use of a mathematical model allows optimization of the operation conditions, what drives to the improvement of the control and predicting of the filtration process. The mathematical models describe the filtration process through the mechanisms of removal of particles that it happens in the porous media. This work proposes the mathematical modeling based on the models that describe macroscopically the filtration process and that they include, for example, the mechanism of particles detachment from porous media and the alteration of the porosity of retained particles during the filtration. The model developed out adapted for the application to the up flow direct filtration in material to granulate of thick sand inserted in the process of double filtration.

Assuntos