Development and performance of a dynamic membrane for anaerobic wastewater treatment - an analysis with different mesh pore sizes and configurations.

Recent studies have focused on proposing materials with larger pores and lower cost to replace conventional membranes. This study aims to investigate the performance of an anaerobic dynamic membrane bioreactor (AnDMBR) at pilot scale, acting as a post-treatment for an Upflow Anaerobic Sludge Blanket (UASB) reactor treating sewage, for the removal of complementary organic matter, focusing on the module design, dynamic layer formation and process performance. The configurations tested on this study were: UASB followed by stone filter and three AnDMBRs in series with polyester pore sizes of 100 µm, 50 µm, and 5 µm; UASB followed by disc filter and the three AnDMBRs in series; UASB followed by the three AnDMBRs in series; and UASB reactor with only one AnDMBR module. Regarding the studied configurations, high removals of total suspended solids, chemical oxygen demand, and turbidity were achieved in all experimental setups. The use of stone and disc filters did not bring clear benefits to the system concerning the direct application of filtration with dynamic membranes, therefore, their removal in the system was favorable. The dynamic membrane formation was faster in the 50 µm mesh, and only a few hours were necessary to obtain a permeate quality with a total suspended solids concentration and a turbidity lower than 15 mg·L-1 and 30 NTU, respectively. Thus, the dynamic membrane technology proved to be a potential solution in the post-treatment of UASB reactor effluents.

Monitoramento do esgoto como ferramenta de vigilância epidemiológica para controle da COVID-19: estudo de caso na cidade de Belo Horizonte / Sewage monitoring as a surveillance epidemiological tool for COVID-19 control: a case study in the city of Belo Horizonte

RESUMO A recente detecção de material genético (RNA) do novo coronavírus em amostras de fezes e no esgoto aponta para a possibilidade de se identificar a circulação do vírus e até mesmo estimar o número de pessoas infectadas em determinada região pelo monitoramento sistemático do esgoto, configurando-se em importante ferramenta epidemiológica de testagem massiva indireta, incluindo portadores sintomáticos e assintomáticos. Nesse sentido, concebeu-se um projeto para a detecção e a quantificação do novo coronavírus em amostras de esgoto coletadas em 15 sub-bacias de esgotamento sanitário dos ribeirões Arrudas e Onça, visando entender a dinâmica de circulação e a prevalência do vírus nas regiões investigadas. Tais sub-bacias esgotam os efluentes gerados por uma população da ordem de 1,5 milhão de pessoas no município de Belo Horizonte e parte de Contagem. O plano de amostragem contemplou 17 pontos (15 sub-bacias + afluente às 2 estações de tratamento de esgoto) de monitoramento semanal, com coletas compostas durante todo o período da manhã. A detecção e a quantificação do RNA viral efetuaram-se em laboratório por meio de ensaios de RT-qPCR. Os resultados obtidos em quatro semanas de monitoramento (semanas epidemiológicas 21 a 24) mostraram um incremento da ocorrência do vírus, atingindo 100% das regiões investigadas na semana epidemiológica 24. A estimativa da população infectada pelo novo coronavírus pelo monitoramento do esgoto em Belo Horizonte apresentou tendência de crescimento exponencial, sendo até 20 vezes maior do que o número de casos confirmados acumulados. Quanto à circulação do vírus, as concentrações do RNA viral têm se mostrado bastante variáveis nas regiões monitoradas, com maiores porcentagens de população infectada estimada ao norte e nordeste da capital mineira.

ABSTRACT The recent detection of SARS-CoV-2 RNA in stool and sewage samples highlights the possibility of mapping the circulation of the virus and even estimating the number of infected people through the systematic monitoring of sewage in a specific region. Therefore, this is an important epidemiological tool for large-scale indirect testing, including symptomatic and asymptomatic carriers. This project was conceived for the detection and quantification of the SARS-CoV-2 in sewage samples collected in 15 watersheds of the Arrudas and Onça streams, aiming to understand the dynamics of spread and the prevalence of the virus in these regions/watersheds. These sub-basins exhaust the effluents generated by a population of approximately 1.5 million people in the municipality of Belo Horizonte and part of Contagem. Weekly composite samples were collected during the morning periods in seventeen monitoring points (15 water sheds + influent to 2 sewage treatment plants). RNA detection and quantification were performed in the laboratory using RT-qPCR. The results obtained in four weeks of monitoring (epidemiological weeks 21 to 24) showed an increase in the occurrence of the virus, reaching 100% of the monitored regions investigated in epidemiological week 24. The infected population, estimated by sewage monitoring in Belo Horizonte, showed exponential growth, being up to 20 times higher than those of accumulated confirmed cases. As for the dynamics of virus spread, RNA concentrations have shown to be quite variable in the monitored regions with higher percentages of the estimated infected population in the northern and north-eastern portions of Belo Horizonte.

Detecção e quantificação de bactérias resistentes aos antibióticos ampicilina e cloranfenicol em estações de tratamento de esgoto doméstico / Detection and quantification of bacteria resistant to ampicillin and chloranphenicol in domestic sewage treatment plants

RESUMO Estações de tratamento de esgotos (ETEs) estão entre as principais fontes de disseminação de bactérias resistentes a antibióticos (BRAs) e genes de resistência (GRAs) no ambiente. Este trabalho quantificou a ocorrência de bactérias resistentes aos antibióticos ampicilina e cloranfenicol no esgoto bruto (EB), no efluente tratado (ET) e no lodo de duas ETEs em escala plena por um período de nove meses. As unidades investigadas utilizavam os seguintes sistemas de tratamento: ETE-A, sistema de lodos ativados convencional; e a ETE-B, reatores anaeróbios (UASB) seguidos de filtros biológicos percoladores (FBP). Os resultados evidenciaram que a ETE-A foi mais eficiente na redução das concentrações de bactérias resistentes à ampicilina e ao cloranfenicol (cerca de 1,1 e 0,7 log10UFC.mL−1 de remoção, respectivamente), quando comparada com a ETE-B (0,5log10 UFC.mL−1 de remoção para as bactérias resistentes ao cloranfenicol e nenhuma remoção para as resistentes à ampicilina). As amostras de lodo, de ambas ETEs, apresentaram elevadas concentrações de bactérias heterotróficas totais — BHTs (4,8-7,6 log10UFC.mL−1) e de BRAs (3,0-6,3 log10UFC.mL−1). A maioria das cepas resistentes à ampicilina e ao cloranfenicol isoladas foi identificada como sendo da família Enterobacteriaceae. Algumas das espécies identificadas são bactérias potencialmente patogênicas, tais como: Klebsiella pneumoniae, Aeromonas hydrophila, Escherichia coli, Enterococcus faecium, Salmonella spp. Os resultados chamam a atenção para a disseminação de BRAs, potencialmente patogênicas, no meio ambiente a partir do efluente final (proveniente do tratamento secundário) das ETEs, independentemente do tipo de sistema adotado. Fica evidente que para reduzir significativamente a concentração das BRAs no ET, este deveria passar por tratamento adicional e desinfecção.

ABSTRACT Sewage treatment plants (STP) are among the main sources of dissemination of antibiotic-resistant bacteria (ARB) and antibiotic-resistance genes (ARG) into the environment. This work quantified the occurrence of cultivable ampicilin-resistant and chloramphenicol-resistant bacteria in raw sewage, treated effluent and sludge samples from two full-scale STP over nine months. The STP investigated used the following treatment systems: STP-A used conventional activated sludge system; and STP-B, anaerobic reactors (UASB) followed by percolating biological filters (PBF). Results showed that was more efficient in reducing the concentrations of ampicilin- and chloramphenicol-resistant bacteria (around 1.1 and 0.7 log10UFC.mL−1, respectively) when compared to STP-B (0.5 log10 UFC.mL−1 removal of cloramphenicol-resistant bacteria and no-removal of ampicilin-resistant bacteria). Sludge samples, from both STP, showed high concentrations of total heterotrophic bacteria (THB; 4.8-7.6 log10UFC.mL−1) and ARB (3.0-6.3 log10UFC.mL−1). Most of the isolated ampicilin- and chloramphenicol-resistant strains were identified as members of the Enterobacteriaceae family. Some of the identified species are potential pathogenic bacteria, such as Klebsiella pneumoniae, Aeromonas hydrophila, Escherichia coli, Enterococcus faecium, Salmonella spp. These results call attention to the spread of ARB, potentially pathogenic, in the environment from the final effluent (from secondary effluent) on the STP, regardless of the type of system adopted. It is evident that in order to significantly reduce the concentration of ARB in the treated effluent, it should undergo additional treatment and disinfection.

Nitrogen removal from food waste digestate using partial nitritation-anammox process: Effect of different aeration strategies on performance and microbial community dynamics.

The feasibility of employing anammox and partial nitritation-anammox (PN/A) processes for nitrogen removal from food waste (FW) digestate was investigated in this study. The effects of different aeration strategies on the microbial community were also investigated. To achieve this, after anammox enrichment (Phase 1), the reactor was fed with digestate supplemented with nitrite (Phase 2), and subsequently different aeration strategies were evaluated to establish PN/A. Aeration strategies with high anoxic periods (30 and 45 min) in relation to aerobic periods (15 min) coupled with low air flow rates (0.026 L  min-1. Lreator-1) were found to be better for establishing PN/A, as coefficients of produced nitrate/removed ammonium were closer to those reported previously (0.17 and 0.21). Aeration conditions considerably altered the microbial community. Candidatus Brocadia was replaced by Candidatus Jettenia, after the first aeration strategies. These results support the feasibility of FW digestate treatment using anammox and PN/A processes and provide a better understanding of the effect of aeration on microbial dynamics in PN/A reactors.

Planning for achieving low carbon and integrated resources recovery from sewage treatment plants in Minas Gerais, Brazil.

There is an enormous deficit in sanitation infrastructure in most Brazilian cities. To tackle this challenge, it is crucial to conceive the new sanitation infrastructure based on sustainability principles, including an integrated approach for the management of the liquid, solid and gaseous phases. This study aimed at developing sustainable sewage treatment flowsheets for different scales and regional scenarios in the state of Minas Gerais. Two watersheds were chosen as study areas, due to their remarkable regional importance and socioeconomic and environmental diversity, i.e. Rio das Velhas and Jequitaí-Pacuí. Currently available processes for sewage treatment and resources recovery were assessed based on: literature review and benchmarking of operational practices, experiences reported by sanitation companies, techno-economic feasibility of resource recovery and carbon footprint assessment of anaerobic-based technologies. Social acceptance was also considered. A total of 15 sustainable flowsheets were proposed, comprising passive/natural systems (stabilization ponds, constructed wetlands and controlled land application), anaerobic process combined with natural systems (UASB reactors followed by controlled land application, constructed wetlands or polishing ponds) and compact anaerobic/aerobic systems (UASB reactors followed by activated sludge or trickling filters). Processes selected for small-scale sewage treatment plants (STPs) (people-equivalent - PE < 10,000 inhab.) intended to be integrated into local communities and economic activities. Large-scale STPs (especially those with PE > 100,000 inhab.) were conceived as industries, where a wide range of resources (e.g. sand for non-structural concrete, biogas for electricity, sludge for thermal energy) could be recovered from the influent sewage. Results obtained from the current study could serve as support for decision-making on the planning and implementation of new sustainable sanitation solutions in the state of Minas Gerais and possibly in other regions of Brazil and other developing countries.

Ocorrência de fármacos e desreguladores endócrinos em esgoto bruto e tratado na cidade de Belo Horizonte (MG) / Occurrence of drugs and endocrine disrupters in raw and treatment sewage in the city of Belo Horizonte / MG, Brazil

RESUMO Os compostos de preocupação emergente (contaminants of emerging concern - CECs) atingem constantemente os corpos d'água via lançamento de esgoto sanitário, efluentes industriais e lixiviados de aterro, disposição inadequada de resíduos sólidos e escoamento superficial, ocasionando a poluição dos cursos d'água. Geralmente estes se encontram em concentrações da ordem de nanograma por litro ou micrograma por litro, dificultando sua análise ou onerando esse processo, demandando, assim, o desenvolvimento de técnicas de preparo e extração. Nesse contexto, destaca-se a Partição a Baixa Temperatura (EPBT), que se baseia na partição do analito de interesse entre fase aquosa e fase orgânica. Face ao exposto e à relevância do tema, o presente trabalho teve como objetivo avaliar, pelo uso da EPBT e cromatografia gasosa acoplada à espectrometria de massas, a ocorrência de 16 CECs no esgoto bruto e no tratado de Belo Horizonte (MG).

ABSTRACT Contaminants of Emerging Concern (CECs) constantly reach water bodies through the discharge of sanitary sewage, industrial effluents and landfill leachate, inadequate disposal of solid waste and surface runoff, causing the pollution of watercourses. In general, these are in concentrations of the order of mg / L or ng / L, making it difficult to analyze or burden this process, thus requiring the development of preparation and extraction techniques. In this context, it stands out the Low Temperature Patitioning Extraction (LTPE), which is based on the partition of the analyte of interest between aqueous phase and organic phase. Bearing this and the relevance of the subject in mind, the present work had the objective of evaluating the occurrence of 16 CECs in the crude and treated sewage of Belo Horizonte / MG, by using LTPE and gas chromatography coupled to mass spectrometry.

Comparação de métodos para quantificação de bactérias nitrificantes / Comparison of methods for quantification of nitrifying bacteria

RESUMO A quantificação de bactérias nitrificantes é de extrema importância para o monitoramento de sistemas biológicos de tratamento que promovam a nitrificação. Neste trabalho, 15 amostras de efluentes coletadas em sistema de tratamento por lodos ativados (LA) foram analisadas de modo a quantificar bactérias nitrificantes por meio de duas técnicas: tubos múltiplos ou técnica do número mais provável (NMP); e hibridação in situ fluorescente (FISH). Os resultados sugerem que houve uma tendência de se obter valores diferentes para bactérias oxidadoras de amônia por meio da NMP em comparação com a FISH. Não obstante, a análise estatística revelou que a diferença de quantificação encontrada entre as técnicas não foi significativa, indicando que ambas podem ser usadas. Para as oxidadoras de nitrito, não foi possível realizar comparação, uma vez que os gêneros que estavam sendo determinados em cada uma das técnicas provavelmente eram diferentes. Sendo assim, as técnicas NMP e FISH se mostraram métodos relativamente simples e adequados para quantificação de microrganismos nitrificantes, com vantagens e limitações inerentes a cada uma.

ABSTRACT The quantification of nitrifying bacteria is of utmost importance for monitoring biological treatment systems designed to promote nitrification. In this study, 15 activated sludge samples were analyzed in order to quantify nitrifying bacteria by two different methods: the most-probable number (MPN); and the fluorescence in situ hybridization (FISH). The results suggest that there was a tendency to obtain different values for ammonia-oxidizing bacteria by MPN compared to FISH. However, statistical analysis of these data revealed that the difference found between the two techniques was not significant, indicating that both can be used for quantification of ammonia-oxidizing bacteria. For nitrite-oxidizing bacteria it was not possible to make this comparison, since the bacterial genera that were being determined in each technique were likely different. Thus, MPN and FISH techniques proved to be relatively simple and suitable for quantification of nitrifying microorganisms in sludge samples, each of them with advantages and limitations.

Behavior of pharmaceuticals in UV photoreactors fed with sewage treated by anaerobic/aerobic system.

This work has assessed the seasonal changes and the dynamics in the concentration of six pharmaceutical compounds during photolysis as a tertiary treatment of sewage previously treated by an anaerobic/aerobic system comprising a UASB (Upflow Anaerobic Sludge Blanket) reactor and a trickling filter (TF). The target compounds were four antibiotics (ciprofloxacin (CPF), clindamycin (CLM), sulfamethoxazole (SMX), and trimetoprim), one ß-blocker (atenolol), and one anti-inflammatory (diclofenac (DCF)). Six hydraulic retention times (HRTs) were evaluated (5, 10, 20, 40, 80, and 160 min) with the intent of varying the ultraviolet C (UVC) radiation doses applied to the effluent from biological treatment containing the target contaminants. The concentrations of pharmaceutical compounds in the effluent of the UASB/TF system were in agreement with the concentration levels reported in the literature. Aside from DCF, the seasonality seems to be a preponderant characteristic regarding the pharmaceutical concentration found in the effluent of biological treatment systems. The radiation dose of 117 mJ cm-2 seemed to be most suited for the photolysis application to tertiary treatment of domestic effluents. It was observed that lower UVC doses led to deconjugation of pharmaceuticals, which can result in increased concentrations of target pollutants in the photoreactor effluent.

Potencial energético e alternativas para o aproveitamento do biogás e lodo de reatores UASB: estudo de caso Estação de tratamento de efluentes Laboreaux (Itabira) / Energy potential and alternative usages of biogas and sludge from UASB reactors: case study of the Laboreaux wastewater treatment plant (Itabira)

RESUMO: Este trabalho estuda o potencial de aproveitamento energético dos subprodutos biogás e lodo gerados na estação de tratamento de efluentes (ETE) Laboreaux em Itabira (MG), composta de reatores UASB, filtros biológicos percoladores e unidade de desaguamento do lodo por filtro prensa. Os subprodutos biogás e lodo foram caracterizados em termos quantitativos (produção) e qualitativos (composição e poder calorífico) durante 12 meses de monitoramento. Foram estudados dois cenários de aproveitamento energético dos subprodutos: (i) uso prioritário do biogás para a secagem térmica do lodo e o excedente de biogás para geração de eletricidade em motor de combustão interna; e (ii) uso prioritário do biogás visando à geração de eletricidade e ao aproveitamento do calor dos gases de exaustão para a secagem térmica de lodo. Para a análise desses cenários, utilizou-se o software CHEMCAD(r) a fim de determinar as condições de queima do biogás em câmara de combustão e em motor de combustão interna, assim como na determinação dos balanços de massa e energia. O estudo analisou o potencial de aproveitamento dos subprodutos do tratamento como fonte de energia renovável para uso na própria ETE e para fornecimento a terceiros. No cenário 1, a geração de eletricidade é menor (atendendo 22,2% da demanda de energia da ETE), mas a secagem térmica possibilita maior redução no volume final de lodo a ser disposto ou a eliminação completa de disposição final se o lodo seco final (com 10% de umidade) for utilizado como combustível por terceiros. No cenário 2, a geração de eletricidade é capaz de suprir 57,6% da demanda de energia da ETE, todavia o calor contido nos gases de exaustão não é suficiente para a secagem de todo o lodo desaguado, configurando uma menor redução na quantidade de lodo a ser disposto (13,5 ou 24,9% de redução em massa, conforme a alternativa de remoção de umidade selecionada).

ABSTRACT: This work assesses the potential of energy recovery of the byproducts biogas and sludge produced at the Laboreaux wastewater treatment plant (WWTP), in Itabira (MG), which is integrated by UASB reactors, trickling filters and sludge dehydration unit (filter press). The byproducts biogas and sludge were quantitatively (production) and qualitatively (composition and calorific value) characterized during a monitoring period of 12 months. Two scenarios for energy recovery from the byproducts were considered: (i) priority use of biogas for sludge thermal drying and the excess of biogas being used for power generation in an internal combustion engine (ICE); and (ii) primary use of biogas for power generation and the heat of the engine exhaustion gases being used for sludge thermal drying. Biogas burning conditions into a combustion chamber and in an internal combustion engine, as well as mass and energy balances for each scenario, were assessed with the CHEMCAD(r) software. The study analysed the potential use of the byproducts as sources of renewable energy for use in the WWTP itself and to be offered to third party. In scenario 1, the electricity generation is lower (fulfilling 22.2% of the WWTP energy demand), but thermal drying allows greater reduction of sludge volume to be disposed of, or the entire elimination of final disposal if the dry sludge (with 10% moisture content) is used as fuel by the third party. As for scenario 2, the electricity generation is sufficient to supply 57.6% of the WWTP energy demand, nevertheless the heat contained in exhausted gases is not enough to dry the whole dehydrated sludge, configuring a lower reduction of sludge amount to be disposed of (13.5 or 24.9% of mass reduction, depending on the moisture reduction alternative chosen).

Avaliação de lavador de gases do tipo Venturi, operando com solução de hidróxido de sódio, para dessulfuração de biogás com altas concentrações de H2S / Evaluation of a Venturi gas scrubber operating with sodium hydroxide solution for desulphurization of biogas with high H2S concentrations

RESUMO O processo de metanização tem sido empregado com sucesso como tratamento biológico de distintas tipologias de efluentes orgânicos. Para conversão do biogás em energia, o sulfeto de hidrogênio (H2S) é o principal composto a ser removido. A metanização da vinhaça, principal efluente do setor sucroenergético, gera um biogás com concentrações de H2S que podem ultrapassar os 30.000 ppmV, com grande variação devido às condições operacionais das usinas. Processos químicos de dessulfuração apresentam-se como uma alternativa que alia robustez e maior controle operacional do processo, além de não resultarem em diluição da concentração de metano, como ocorre em processos biológicos. Entretanto, a principal desvantagem desses processos é a demanda de compostos químicos, resultando em custos operacionais elevados. Esse trabalho teve como objetivo avaliar a viabilidade técnica de se realizar uma dessulfuração química de biogás com altas concentrações de H2S, além de determinar as concentrações de hidróxido de sódio (NaOH) em meio aquoso que proporcionassem altas eficiências de remoção de H2S e que possibilite que o efluente desse processo seja passível de regeneração por microrganismos sulfo-oxidantes. Foi utilizado um lavador do tipo Venturi, com uma solução de 5,00 x 10-2 mol.L-1 de NaOH. Na faixa de pH de crescimento desses microrganismos, as eficiências de remoção de H2S variaram de 99,3 a 99,9%. Constatou-se que é possível atingir eficiências máximas de remoção de H2S utilizando soluções de 5,00 x 10-3 mol.L-1 de NaOH, obtendo um efluente com pH adequado ao crescimento de microrganismos sulfo-oxidantes. Verificou-se, ainda, que o CO2 exerce grande influência na competição pelas hidroxilas presentes no meio.

ABSTRACT The methanation process has been successfully used as a biological treatment method for different effluent typologies. For biogas to energy conversion, the hydrogen sulfide (H2S) is the most important compound that must be removed. The methanation of vinasse, which is the major effluent of the sugar and ethanol industry, results in a biogas with hydrogen sulfide concentrations that might exceed 30,000 ppmV. The concentrations may vary considerably according to the operational conditions of the production process. Chemical desulphurization processes are presented as an alternative that combines robustness and provides better operational process control. Moreover, the chemical desulphurization does not result in dilution of the methane concentration, which is side effect noticed in the biological desulphurization processes. However, the main disadvantage of the chemical desulphurization is exactly the high demand for chemical compounds, which results in high operational costs. The present research investigated the technical feasibility of applying a chemical desulphurization process to treat biogas with high hydrogen sulfide concentrations; the research also aimed to determine the sodium hydroxide (NaOH) concentration in the aqueous medium, as the NaOH presence enables high efficiency of hydrogen sulfide removal and allows the effluent regeneration by sulfo-oxidant microorganisms. The experiments were carried out using a Venturi absorption tower with a NaOH chemical solution of 5.00 x 10-2 mol.L-1. In the pH range favorable to this microorganisms, the H2S removal efficiency varied from 99.3 to 99.9%. It was observed that it is possible to achieve maximum efficiency of removal of H2S using solutions of 5.00 x 10-3 mol.L-1 NaOH, obtaining an effluent with proper pH to grow sulfo oxidant microorganisms. Moreover, it was verified that carbon dioxide significantly influenced the competition for the hydroxyls present in the solution.

Enriquecimento de microrganismos metanotróficos a partir de lodo de reator UASB tratando esgotos domésticos / Enrichment of methanotrophic microorganisms from sludge of UASB reactor treating domestic sewage

RESUMO Nesse estudo, microrganismos metanotróficos foram enriquecidos a partir de lodo proveniente de um reator UASB tratando esgotos domésticos em reator em batelada sequencial (RBS) com meio autotrófico contendo nitrito e nitrato. As eficiências médias de remoção de nitrito e nitrato foram de 68% e 53%, respectivamente, provavelmente devido à atividade heterotrófica desnitrificante. A detecção de arquéias dos grupos ANME-I e ANME-II foram realizadas por PCR durante todo período de cultivo. A estrutura da comunidade microbiana presente no inóculo e enriquecida no RBS após 100 dias de operação foi estudada por pirosequenciamento. Os resultados das análises demonstraram que a comunidade enriquecida no reator foi diferente à inoculada. Os filos dominantes no inóculo foram Synergistestes , Firmicutes e Euryarchaeota , ao passo que na biomassa enriquecida Planctomycetes, Verrucomicrobia, Chloroflexi e Proteobacteria predominaram. As condições de cultivo do RBS reduziram a abundância de Methanobacterium (8% para 1%) e selecionaram bactérias metanotróficas como Methylocaldum , Methylocistis e Methylosinus . As sequências de Methylocaldum sp. apresentaram abundância relativa de 2.5%. A presença e elevada predominância do filo Verrucomicrobia na biomassa enriquecida do RBS sugere que outras espécies de metanotróficas, ainda pouco conhecidas, relacionadas a este filo podem estar presentes no reator. O potencial de oxidação anaeróbia do metano foi determinado para ambas amostras e revelaram que a atividade metanotrófica da biomassa foi aproximadamente três vezes maior que a do inóculo. Em suma, estes resultados sugerem que o inóculo usado e as condições de cultivo aplicadas foram adequados para o enriquecimento de metanotróficas.

ABSTRACT In this study, methanotrophic microorganisms were enriched from sludge derived from a UASB reactor treating domestic sewage. The enrichment was performed in a sequencing batch reactor (RBS) with an autotrophic medium containing nitrite and nitrate. The nitrite and nitrate removal efficiencies were 68% and 53%, respectively, probably due to heterotrophic denitrification. Archaeal cells of the ANME-I and ANME-II groups were detected by PCR throughout the whole cultivation period. The microbial community composition of the biomass present in the inoculum and enriched in RBS after 100 days of operation was investigated and compared with the help of data obtained from pyrosequencing analyses. Pyrosequencing analysis demonstrated that the community enriched in the reactor had differing composition from the inoculum. The dominant phyla detected in the inoculum were Synergistestes , Firmicutes and Euryarchaeota while in the enriched biomass Planctomycetes, Verrucomicrobia, Chloroflexi and Proteobacteria predominated. The cultivation conditions applied decreased the abundance of Methanobacterium (from 8 to 1%) and selected for methanotrophic bacteria such as Methylocaldum , Methylocistis and Methylosinus . Sequences of Methylocaldum sp. accounted for 2.5% of the total reads. The presence and high predominance of Verrucomicrobia in the enriched biomass suggest that other unknown methanotrophic species related to this phylum might also have occurred in the reactor. The potential for anaerobic oxidation of methane was determined for both samples and revealed that the methanotrophic activity of the enriched biomass was almost three times greater than in the inoculum. Taken together these results indicated that the inoculum used and the cultivation conditions applied were adequate for the methanotrophic enrichment.

Uso de fotorreatores UV para a remoção de diclofenaco, bezafibrato e etinilestradiol de esgoto tratado em sistema UASB-FBP / Use of UV photoreactors to remove diclofenac, bezafibrate and ethynylestradiol from sewage treated in UASB-TF system

RESUMOEste trabalho avaliou a remoção de diclofenaco (DCF), bezafibrato (BZF) e etinilestradiol (EE2) de efluentes de sistema UASB-FBP (reator anaeróbio de manta de lodo seguido de filtro biológico percolador) em fotorreatores UV de lâmpadas imersas (FRI) e emersas (FRE). Os resultados mostram que baixa eficiência de remoção de tais compostos foi obtida em ambos fotorreatores quando se utilizou baixo tempo de contato (~10 min) e baixa concentração inicial de fármacos (0,5 µg.L-1 para EE2, e 21 µg.L-1 para DCF e BZF). O aumento da concentração inicial de DCF (para 20 mg.L-1) e do tempo de contato (para 20 min) resultaram em aumento da eficiência de remoção (de 31 para 83% no FRI e de 36 para 86% no FRE), indicando que compostos dissolvidos presentes no efluente biológico afetaram adversamente a remoção de fármacos nos fotorreatores devido a competição pela radiação UV incidente.

ABSTRACTThis paper evaluated the removal of diclophenac (DCF), bezafibrate (BZF) and ethynylestradiol (EE2) from effluent of an anaerobic reactor coupled to a trickling filter (UASB-TF) in two types of UV photoreactors (immerse UV lamps - FRI and emmersed UV lamps - FRE). The results showed low removal efficiencies in both photoreactors when low contact times (10 min) and low initial concentration of such compounds was used (0.5 µg.L-1 for EE2 and 21 µg.L-1 for DCF and BZF). An increase in the initial concentration of DCF (to 20 mg.L-1) and of the contact time (to 20 min) led to an increase in the removal efficiency (from 31 to 83% in FRI and from 36 to 86% in FRE), suggesting that dissolved compounds present in the biological effluent adversely affected the removal of the pharmaceutical tested due to competition for the incident UV radiation.

Remocao de farmacos e desreguladores endocrinos em estacoes de tratamento de esgoto: revisao da literatura / Removal of pharmaceuticals and endocrine disrupters in sewage treatment plants: literature review

O monitoramento ambiental dos chamados microcontaminantes ou micropoluentes vem ganhando grande interesse da comunidade científica desde os anos 1970. Nesse grupo de contaminantes estão incluídos fármacos de diversas classes, produtos de limpeza e higiene pessoal, substâncias aplicadas na produção de plásticos e resinas, pesticidas, hormônios naturais e seus subprodutos, entre outros compostos. A principal via de contaminação do meio ambiente com fármacos e desreguladores endócrinos (DE) é o lançamento de esgotos in natura e tratado. Nesse contexto, este artigo compila dados de ocorrência de fármacos e DE no afluente e efluente de estações de tratamento de esgoto (ETE), discute os mecanismos envolvidos na sua remoção em ETE e faz uma análise comparativa da remoção de tais compostos em diferentes sistemas de tratamento.

The environmental monitoring of the so-called micropollutants has gained great interest since the 1970s. In this group of compounds are included several classes of pharmaceuticals, cleaning and personal care products, substances applied in plastics and resins, pesticides, natural hormones and their by-products, among others. The main route of contamination of the environment with pharmaceuticals and endocrine disrupting compounds (EDC) is through the discharge of raw and treated sewage. Thus, this paper summarizes data on the occurrence of pharmaceuticals and EDC in raw and treated sewage, provides information regarding the mechanisms involved in their removal and compares their removal in different treatment processes.

Operação de filtros biológicos percoladores pós-reatores UASB sem a etapa de decantação secundária / Operation of trickling filters post-UASB reactors without the secondary sedimentation stage

A pesquisa teve por objetivo avaliar filtros biológicos percoladores (FBP) pós-reatores UASB operando sem a etapa de decantação secundária, em termos da remoção da demanda bioquímica e química de oxigênio (DBO e DQO) e sólidos suspensos totais (SST). O aparato experimental consistia em um reator UASB que alimentava quatro FBP em paralelo, preenchidos com diferentes materiais suporte. O reator UASB operou em regime hidráulico permanente, e três condições operacionais foram impostas aos FBP durante o período experimental. Em geral, os sistemas UASB/FBP foram capazes de promover o atendimento aos padrões de lançamento. Em condições de baixas cargas orgânicas volumétricas (COV), o uso de materiais de enchimento de maior área superficial específica não proporcionou ganhos expressivos em termos de desempenho. Contudo, o uso de meio suporte baseado em espumas de poliuretano propiciou melhoria significativa na qualidade do efluente final. O uso de sistemas UASB/FBP sem decantadores secundários parece ser uma promissora alternativa para a simplificação operacional da tecnologia, e uma importante estratégia para o tratamento de efluentes domésticos em países em desenvolvimento. No entanto, o sucesso do emprego desta tecnologia fica condicionado ao correto gerenciamento do lodo anaeróbio do reator UASB, a fim de que sejam evitadas sobrecargas nos FBP.

The research aimed at evaluating the operation of trickling filters (TF) post-UASB reactors without the secondary sedimentation stage, in terms of biochemical and chemical oxygen demand (BOD and COD) and total suspended solids (TSS) removal. The experimental apparatus consisted of one UASB reactor followed by four TF in parallel, each one filled with a different packing media. The UASB reactor was operated at a permanent hydraulic regime, while three operational conditions were imposed to the TF during the experimental period. In general, the UASB/TF systems were able to comply with the discharge standards. At low organic loading rates (OLR), no improvements in terms of organic matter removal, with the use of higher surface area packing media were observed. However, the use of a sponge-based packing media provided significant improvements on final effluent quality. The use of UASB/TF systems without secondary sedimentation can constitute an attractive alternative in terms of operational simplification of this technology, and an important strategy for domestic wastewater treatment in developing countries. However, the success of this technology is strictly connected to the correct anaerobic sludge management of the UASB reactor, in order to avoid overloads on the TF.

Characterization and removal of specific organic constituents in an UASB-trickling-filter system treating domestic wastewater.

This paper presents the characterization of specific organic constituents (carbohydrates, proteins and lipids) in raw sewage and in the anaerobic and aerobic effluents of a demo-scale (500 inhabitants) UASB- trickling-filter system. The evaluation of such parameters was carried out for two operating conditions, either without sludge recirculation (experiment I) from the trickling filter to the UASB reactor or with sludge recirculation (experiment II), for sludge thickening and stabilization, in the anaerobic reactor. The results showed that the contribution of acetic acid, carbohydrates, proteins and lipids amounted for approximately 70% of the total COD fed to the UASB during experiment I, whereas during experiment II these constituents amounted for only around 40% of the total COD. Although very high BOD and COD overall removal efficiencies were observed for the treatment system (around 90% and 80%, respectively), it was possible to infer that these efficiencies were mainly related to the removal of carbohydrates and lipids (around 80% removal), and of other non-identified constituents. The removal of proteins was much lower (around 50% removal), and the relative contribution of proteins to the total COD increased along the treatment course, being responsible for most of the residual COD of the treatment units. In the present system configuration, the UASB reactor played a major role in the removal of carbohydrates, whereas the trickling filter was very effective in the removal of lipids. The return of aerobic sludge for thickening and stabilization in the UASB reactor did not affect its performance.

Alternativas para o controle de emissões odorantes em reatores anaeróbios tratando esgoto doméstico / Alternatives for the control of odorous emissions in anaerobic reactors treating domestic wastewater

Esta nota técnica busca consolidar as principais características, vantagens e desvantagens dos métodos usualmente empregados para o controle de emissões odorantes, discorrendo criticamente acerca da aplicabilidade de cada um dos métodos para o tratamento de odores em estações de tratamento de esgoto doméstico. Verificou-se que vários métodos são sofisticados, de elevado custo e, muitas vezes, não aplicáveis ao tratamento de odores emitidos em reatores anaeróbios tratando esgoto doméstico. Uma análise qualitativa dos vários métodos indica que a combustão direta e os processos bioquímicos são os que reúnem o maior conjunto de vantagens para o tratamento de gases residuais emitidos em reatores anaeróbios.

This technical note aims at consolidating the main characteristics, advantages and disadvantages of the methods usually applied to the control of odorous emissions, with a critical analysis upon the applicability of each method to the treatment of odours in treatment plants of domestic wastewater. It was verified that several methods are sophisticated, present high cost, and are often non-applicable to the treatment of odour emissions from anaerobic reactors treating domestic wastewater. The qualitative analysis of the various methods points out that direct combustion and biochemical processes gather more advantages for the treatment of waste gases produced in anaerobic reactors.

Enriquecimento de bactérias anaeróbias oxidadoras de amônia - anammox / Enrichment of anaerobic ammonium oxidizing bacteria - anammox

Bactérias anaeróbias oxidadoras de amônia (bactérias Anammox, do inglês anaerobic ammonium oxidizing bacteria) foram enriquecidas em reator em batelada sequencial (RBS), a partir de lodo proveniente de um sistema convencional de lodos ativados tratando esgoto doméstico de Belo Horizonte (MG). Após três meses de cultivo, atividade Anammox foi detectada no sistema pelo consumo de quantidades estequiométricas de NO2- e NH4+. Análises de hibridação in situ fluorescente (FISH, do inglês fluorescent in situ hybridization) confirmaram a presença de bactérias Anammox, provavelmente Candidatus Brocadia anammoxidans, e revelaram que estas representavam 53 por cento do total de células (após 6 meses de cultivo). O desempenho do reator ao longo dos sete meses de operação demonstrou remoção quase que total de nitrito, baseada em concentração afluente de 61 a 95 mg N-NO2-/L. A eficiência máxima de remoção de amônia alcançada foi de 95 por cento, a partir de concentração afluente de 55 a 82 mg N-NH4+/L.

Anaerobic ammonium-oxidizing (Anammox) bacteria were enriched from sludge collected at a conventional activated sludge system treating domestic wastewater of Belo Horizonte(MG), Brazil, employing a sequencing batch reactor (SBR). After three months of cultivation, Anammox activity was detected in the system by the consumption of stoichiometric amounts of NO2- and NH4+. Fluorescent in situ hybridization (FISH) results revealed the presence of Anammox bacteria (probably Candidatus Brocadia anammoxidans) and showed that they accounted for 53 percent of the total bacterial population (after 6 months of cultivation). The reactor performance during the seven months of operation showed a near perfect removal of nitrite, based on the influent NO2--N concentration of 61-95 mg/L. The maximum ammonia removal efficiency was 95 percent from the influent N-NH4+ concentration of 55-82 mg/L.

Efeito do tratamento térmico de lodo anaeróbio sobre as características de biodegradabilidade da fração orgânica / Effect of thermal treatment of anaerobic sludge on the biodegradability characteristics of the organic fraction

O presente trabalho avalia o efeito do tratamento térmico do lodo excedente de reatores UASB sobre as características de biodegradabilidade da fração orgânica remanescente, empregando-se o biogás como fonte de energia. O tratamento térmico proporcionou a elevação da temperatura do lodo até valores próximos a 75° C, para tempos de aquecimento de sete horas. Amostras coletadas em diferentes momentos mostraram melhoras significativas na biodegradabilidade do lodo tratado termicamente, com incrementos em 60 vezes para a DBO filtrada, de 30 por cento para a DBO total e 50 por cento para a produção de biogás. Adicionalmente, o retorno do lodo tratado termicamente para o reator UASB não prejudicou as características do efluente.

This paper aimed at evaluating the effect of thermal treatment of excess anaerobic sludge upon the biodegradability characteristics of the remaining organic fraction, using biogas generated in the wastewater treatment process as energy source. Direct burning of the biogas allowed an increase in the sludge temperature up to values close to 75º C, for a seven-hour heating period. Samples taken at different heating times showed significant increase of the biodegradability characteristics of the thermally treated sludge, with augments of around 60 times for filtered BOD, 30 percent for total BOD and 50 percent for biogas production. In addition, no adverse effect on effluent quality was noticed when the thermally treated sludge was returned to the UASB reactor.

Concepção e avaliação de uma unidade de peneiramento forçado para a redução do tamanho de partículas presentes no esgoto bruto doméstico / Design and evaluation of a forced sieving unit (FSU) for the reduction of the particle size present in raw domestic sewage

Este trabalho teve como objetivo a concepção e o teste de uma unidade de peneiramento forçado, utilizada para o pré-tratamento do esgoto bruto com vistas à redução do tamanho de partículas de matéria orgânica. A unidade de peneiramento forçado (UPF) era constituída de uma peneira metálica (abertura de malha de 1 mm) inserida na tubulação de recalque através da qual o esgoto efluente era bombeado. O peneiramento forçado resultou em maior concentração de partículas com diâmetro entre 1,8 e 30 µm, sem que houvesse retenção de material particulado. Todavia, a UPF não influenciou na redução/retenção de DQO TOTAL do esgoto bruto.

The work focused on the conception and test of a forced sieving unit, used for the pre-treatment of raw sewage aiming at the reduction of organic matter particle size. The pre-treatment unit involved the use of a metallic sieve (1 mm cut-off) assembled inside the pipeline through which the influent sewage was pumped. The results indicated that the forced sieving resulted in a higher concentration of particles with range diameter between 1.8 and 30 µm, without the retention of particulate material. However, the forced sieving unit did not influence the reduction/retention of COD TOTAL of the raw sewage.

Tratamento térmico de lodo anaeróbio com utilização do biogás gerado em reatores UASB: avaliação da autossustentabilidade do sistema e do efeito sobre a higienização e a desidratação do lodo / Thermal treatment of anaerobic sludge utilizing biogas produced in UASB reactors: evaluation of system self-sustainability and the effect on sludge hygienization and dehydration

O presente trabalho objetiva avaliar a eficiência do biogás gerado em reatores UASB como fonte de energia para higienização térmica do lodo excedente, atentando-se ainda para a autossustentabilidade do sistema e para a avaliação do desaguamento do lodo tratado termicamente. Foi desenvolvido em um aparato experimental em escala de demonstração constituído de reator UASB, reservatório de biogás, reator térmico e leitos de secagem. A autossustentabilidade foi verificada por meio de balanço térmico teórico e de testes experimentais de higienização térmica. Estes testes indicaram que o aproveitamento da energia térmica do biogás foi suficiente para aquecer o lodo em temperaturas de 55 a 65ºC, durante três a cinco horas, possibilitando a completa eliminação de ovos viáveis de helmintos. No entanto, o processo de desidratação se mostrou muito mais difícil para o lodo tratado termicamente.

The objective of this research was to determine how effectively biogas produced in UASB reactors could be used as a source of heat for the thermal hygienization of excess anaerobic sludge, whether the system can operate on a self-sustained basis and how the dehydration of the thermally treated sludge behave. The experiments were conducted in a demonstration-scale setup comprising UASB reactor, biogas holder, thermal reactor and sludge drying beds. The self-sustainability of the system was evaluated by the systemâ€TMs theoretical thermal balance and by experimental hygienization tests. These tests indicated that the recovery of thermal energy from the biogas was sufficient to heat the sludge at temperatures in the range of 55 to 65ºC, for three to five hours, allowing the complete elimination of viable helminth eggs. However, the dehydration process showed to be much more difficult for the thermally treated sludge.