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Wastewater treatment plants (WWTPs) are recognized as important sources of Antibiotic Resistant Bacteria (ARBs) and Antibiotic Resistant Genes (ARGs), and might play a role in the removal and dissemination of antimicrobial resistance (AMR) in the environment. Detailed information about AMR removal by the different treatment technologies commonly applied in urban WWTPs is needed. This study investigated the occurrence, removal and characterization of ARBs in WWTPs employing different technologies: WWTP-A (conventional activated sludge-CAS), WWTP-B (UASB reactor followed by biological trickling filter) and WWTP-C (modified activated sludge followed by UV disinfection-MAS/UV). Samples of raw sewage (RI) and treated effluent (TE) were collected and, through the cultivation-based method using 11 antibiotics, the antibiotic resistance profiles were characterized in a one-year period. MAS was effective in reducing ARB counts (2 to 3 log units), compared to CAS (1 log unit) and UASB/BTF (0.5 log unit). The composition of cultivable ARB differed between RI and TE samples. Escherichia was predominant in RI (56/118); whilst in TE Escherichia (31/118) was followed by Bacillus (22/118), Shigella (14/118) and Enterococcus (14/118). Most of the isolates identified (370/394) harboured at least two ARGs and in over 80 % of the isolates, 4 or more ARG (int1, blaTEM, TetA, sul1 and qnrB) were detected. A reduction in the resistance prevalence was observed in effluents after CAS and MAS processes; whilst a slight increase was observed in treated effluents from UASB/BTF and after UV disinfection stage. The multi-drug resistance (MDR) phenotype was attributed to 84.3 % of the isolates from RI (27/32) and 63.6 % from TE (21/33) samples and 52.3 % of the isolates (34/65) were resistant to carbapenems (imipenem, meropenem, ertapenem). The results indicate that treated effluents are still a source for MDR bacteria and ARGs dissemination to aquatic environments. The importance of biological sewage treatment was reinforced by the significant reductions in ARB counts observed. However, implementation of additional treatments is needed to mitigate MDR bacteria release into the environment.

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Dissolved gases in the effluent of anaerobic reactors, specifically dissolved methane (D-CH4) and sulphide (S2-), are a drawback for anaerobic-based sewage treatment plants (STPs). This article studied the simultaneous desorption/removal of both gases from anaerobic effluents with hollow fibre membrane contactors (HFMCs), evaluating two types of membrane materials (e.g. microporous and dense) at different operating conditions (atmospheric air as sweeping gas or vacuum, and different gas/liquid flows and vacuum pressures). The transfer of other gases, such as O2 and CO2, was studied as well. Desorption/removal efficiencies up to 99% for D-CH4 and 100% for S2- were obtained, with the higher efficiencies reported for the dense HFMC and with air as sweeping gas. It was found that the removal mechanism for S2- was oxidation with O2 from the air. In addition, the use of air as sweeping gas allowed the obtention of a nearly O2 saturated effluent, with more elevated dissolved oxygen concentrations in the microporous HFMC. Finally, it was found that the higher mass-transfer resistance in the dense membrane was compensated by a better performance in the liquid phase (lower mass-transfer resistance) in this unit, which allowed better D-CH4 desorption efficiencies.

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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.

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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.

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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.

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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.

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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.

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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.

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Anaerobic digestion of food wastes coupled with digestate post-treatment using microalgae-based systems could recover large amounts of energy and nutrients worldwide. However, the development of full-scale implementations requires overcoming microalgae inhibition by high ammonia concentrations and low light transmittances affecting photosynthesis. This study evaluated the potential of microalgae-based reactors supplied with red light-emitting diodes (LEDs) at low intensity (660 nm and 15 µmol·m-2·s-1) to treat food waste digestate. LED reactors were compared with control reactors exposed to solar radiation. From a range of species in the inoculum, Chlorella vulgaris showed high adaptation to both lighting regimes and digestate environmental conditions, characterized by a C:N:P ratio of 74:74:1. Removal efficiencies for control and LED reactors were 84.0% and 95.8% for soluble chemical oxygen demand (COD) and 89.4% and 53.0% for ammonia, respectively. Approximately 50% of ammonia in control reactor and 15% in LED reactor was lost from the systems, whereas 17% and 36% of ammonia was transformed to organic nitrogen in control and LED reactors, respectively. Low-intensity LEDs maintained microalgae growth in levels similar to solar radiation and supported efficient digestate treatment, showing a potential for further application in optimization of full scale reactors at a relatively low energy cost.

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The effects of temperature reduction (from 35 °C to 20 °C) on nitrogen removal performance and microbial diversity of an anammox sequencing batch reactor were evaluated. The reactor was fed for 148 days with anaerobically pretreated municipal wastewater amended with nitrite. On average, removal efficiencies of ammonium and nitrite were high (96%) during the enrichment period and phases 1 (at 35 °C) and 2 (at 25 °C), and slightly decreased (to 90%) when the reactor was operated at 20 °C. Deep sequencing analysis revealed that microbial community structure changed with temperature decrease. Anammox bacteria (Ca. Brocadia and Ca. Anammoximicrobium) and denitrifiers (Burkholderiales, Myxococcales, Rhodocyclales, Xanthomonadales, and Pseudomonadales) were favoured when the temperature was lowered from 35 °C to 25 °C, while Anaerolineales and Clostridiales were negatively affected. The results support the feasibility of using the anammox process for mainstream nitrogen removal from anaerobically pretreated municipal wastewater at typical tropical temperatures.

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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.

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RESUMO Este artigo busca consolidar as principais características, vantagens e desvantagens de métodos disponíveis no meio técnico e científico para o controle de odores e corrosão em redes coletoras e estações de tratamento de esgoto, trazendo uma abordagem atualizada sobre soluções preventivas relacionadas à concepção e à operação de sistemas de esgotamento, com adição de compostos químicos ou aeração em fase líquida. São apresentados os princípios de cada técnica e consolidadas as principais diretrizes para o projeto de alternativas. Além disso, são apresentadas diretrizes para a concepção de soluções corretivas com contenção e exaustão de unidades/fontes potencialmente odorantes, incluindo uma discussão sobre os processos atualmente disponíveis no meio técnico-científico para tratamento de gases odorantes e corrosivos.

ABSTRACT This paper aims to consolidating the main characteristics, advantages and disadvantages of available methods in technical-scientific community to odor and corrosion control in sanitary sewerage systems and treatment plants, taking along an innovative approach on preventive solutions related to sewage systems design and operation with addition of chemicals or liquid phase aeration. The main beliefs of each technique are presented as well as the main guidelines for alternatives design. In addition, guidelines are given for corrective solutions design of covers and exhaust of potentially odorous sources, as well as a brief discussion of processes currently available in the technical-scientific community to the treatment of odorant odorous and corrosive gases.

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Methane is produced in anaerobic environments, such as reactors used to treat wastewaters, and can be consumed by methanotrophs. The composition and structure of a microbial community enriched from anaerobic sewage sludge under methane-oxidation condition coupled to denitrification were investigated. Denaturing gradient gel electrophoresis (DGGE) analysis retrieved sequences of Methylocaldum and Chloroflexi. Deep sequencing analysis revealed a complex community that changed over time and was affected by methane concentration. Methylocaldum (8.2%), Methylosinus (2.3%), Methylomonas (0.02%), Methylacidiphilales (0.45%), Nitrospirales (0.18%), and Methanosarcinales (0.3%) were detected. Despite denitrifying conditions provided, Nitrospirales and Methanosarcinales, known to perform anaerobic methane oxidation coupled to denitrification (DAMO) process, were in very low abundance. Results demonstrated that aerobic and anaerobic methanotrophs coexisted in the reactor together with heterotrophic microorganisms, suggesting that a diverse microbial community was important to sustain methanotrophic activity. The methanogenic sludge was a good inoculum to enrich methanotrophs, and cultivation conditions play a selective role in determining community composition.

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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.

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The performance of a demonstration-scale anaerobic reactor treating food waste was evaluated with an emphasis on microbial response to increasing organic loading rates (OLRs). The reactor exhibited a stable performance in terms of methane yield at OLR ranging from 1.0 to 2.4 kg VS L-1 day-1 (phases I and II), compared to that at phase III (OLR: 1.0-1.5 kg VS L-1 day-1) when the food waste exhibited greater acidity. Deep sequencing analysis revealed shifts in the microbial composition at each operational phase. The phyla Firmicutes and Bacteroidetes were favoured, whereas the abundance of Proteobacteria and Chloroflexi decreased at higher OLRs, indicating that fermenting-, hydrolytic- (and acidogenic) bacteria were selected under this condition. Changes were observed in the composition of methanogens, and not the abundance, in response to a shift in OLR. Methanosaeta and Methanospirillum dominated at low OLRs, indicating the importance of both acetoclastic and hydrogenotrophic methanogens for methane production during this condition. Methanosaeta almost disappeared at high OLRs, whereas Methanoculleus was favoured. Syntrophic prokaryotes were in high abundance (>9%), indicating that syntrophic methane production was important in this reactor. Syntrophic interactions between hydrogen-producer (Syntrophomonas and Desulfosporosinus) and hydrogenotrophic methanogens were more evident at high OLR. These results indicate that hydrogenotrophic methanogenesis contributed significantly to methane production at higher OLRs than when the reactor was operated at low OLR.

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The use of biofilters (working bed volume of 7.85 L) for the oxidation of CH4 at low concentrations (from 0.17%v/v to 3.63%v/v, typically in waste gas from anaerobic sewage treatment) was investigated and four empty bed residence times were tested (in min): 42.8, 29.5, 19.6, and 7.4. Mixtures of organic (composted leaves) and three non-organic materials (sponge-based material - SBM, blast furnace slag - BFS, and expanded vermiculite - ExpV) were used as packing media. Along 188 operational days after the steady state was reached (95 days for start-up), the CH4 mineralization decreased while the inlet loads gradually increased from 3.0 ± 0.8 gCH4 m(-3) h(-1) to 148.8 ± 4.4 gCH4 m(-3) h(-1). The biofilter packed with ExpV showed the best results, since the CH4 conversions decreased from 95.0 ± 5.0% to 12.7 ± 3.7% as a function of inlet concentration, compared to the other two biofilters (SBM and BFS) which showed CH4 conversions decreasing from 56.0 ± 5.4% to 3.5 ± 1.2% as a function of inlet concentration. The methanotrophic activity of biomass taken from ExpV biofilter was three times higher than the activity of biomass from the other two biofilters. Taken together, these results suggested that ExpV provides an attractive environment for microbial growth, besides the mechanical resistance provided to the whole packing media, showing the potential to its use in biofiltration of diffuse CH4 emissions.

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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).

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Long-term effects of COD/N ratios on the nitrogen removal performance and bacterial community of an anammox reactor were evaluated by adding a synthetic medium (with glucose) and real anaerobic effluent to a SBR. At a COD/N ratio of 2.8 (COD, 390mg·L(-1)) ammonium removal efficiency was 66%, while nitrite removal remained high (99%). However, at a COD/N ratio of 5.0 (COD, 300mg·L(-1)), ammonium and nitrite removal efficiencies were high (84% and 99%, respectively). High COD, nitrite, and ammonium removal efficiencies (80%, 90% and 95%, respectively) were obtained on adding anaerobically pre-treated municipal wastewater (with nitrite) to the reactor. DGGE revealed that the addition of anaerobic effluent changed the bacterial community structure and selected for DNA sequences related to Brocadia sinica and Chloroflexi. Adding glucose and anaerobic effluent increased denitrifiers concentration threefold. Thus, the possibility of using the anammox process to remove nitrogen from anaerobically pre-treated municipal wastewater was demonstrated.

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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.

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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.