The influence of light intensities and micropollutants on the removal of total coliforms and E. coli from wastewater in a flat-panel photobioreactor.

The presence of micropollutants and pathogens in sanitary wastewater and surface water is a growing concern that impacts public health, environmental balance and the maintenance of water supply services. To improve sanitary wastewater treatment, it is necessary to develop and improve sustainable technologies. Among the available options, microalgae-based systems stand out for their efficiency and generation of value-added byproducts. To study the impact of luminosity and the presence of micropollutants (13 selected) on the removal of E. coli and total coliforms from real anaerobically treated wastewater, a pilot flat-panel photobioreactor (50 L) was operated in batch mode in a tropical climate region. This is the first study to evaluate whether micropollutants interfere with coliform groups, considering a microalgae-based system and an experiment in a tropical climate region. E. coli had better removal (from 104 to 101 CFU 100 mL-1) than did total coliforms (from 104 to 103 CFU 100 mL-1). The removal of E. coli was more strongly linked to luminosity and temperature, while the removal of total coliforms was influenced by the presence of the selected micropollutants.

Nutrient and pathogen removal from anaerobically treated black water by microalgae.

The demand for systems that efficiently and sustainably recover value-added compounds and materials from waste streams is a major challenge. The use of wastewater as a source for recovery of carbon and nutrients is an attractive and sustainable alternative. In this study, anaerobically treated black water was treated in photobioreactors (PBRs) inoculated with Chlorella sorokiniana, and the process was investigated in terms of phosphorus and nitrogen removal, biomass growth, and the removal of pathogens. The consumption of bicarbonate (alkalinity) and acetate (volatile fatty acids) as carbon sources by microalgae was investigated. The average nutrient removal achieved was 66% for N and 74% for P. A high consumption of alkalinity (83%) and volatile organic acids (76%) was observed, which suggests that these compounds were used as a source of carbon. The biomass production was 73 mg L-1 day-1, with a mean biomass of 0.7 g L-1 at the end of the batch treatment. At the end of the experiments, a log removal/inactivation of 0.51 log for total coliforms and 2.73 log for Escherichia coli (E. coli) was observed. The configuration used, a flat-panel PBR operated in batch mode without CO2 supplementation, is a cost-effective and environmentally sustainable method for recovering of nutrients and production of algal biomass.

Acompanhamento operacional e avaliação de uma estação compacta de tratamento de esgoto sanitário: reator UASB seguido de filtro aerado submerso / Operational monitoring and evaluation of a compact sanitary wastewater treatment plant: UASB reactor followed by submerged aerated filter

RESUMO Estações Compactas de Tratamento de Efluentes (ECTEs) são uma ótima alternativa para a implantação de sistemas descentralizados de esgoto doméstico que possam atender pequenas comunidades. No entanto, tais sistemas ainda são pouco utilizados e há pouca experiência em relação à sua operação. Diante de tal demanda, esta pesquisa visou avaliar a eficiência e realizar o acompanhamento operacional de uma ECTE composta por reator Upflow Anaerobic Sludge Blanket (UASB), seguido de filtro aerado submerso (FAS), que está localizada no município de Uru, em São Paulo, Brasil. Durante a pesquisa, o sistema mostrou-se uma alternativa viável de tratamento para pequenas comunidades, pois apresentou boa eficiência, com valores médios de remoção de demanda bioquímica de oxigênio (DBO5) e demanda química de oxigênio (DQO) de 91 e 85%, respectivamente. O monitoramento realizado durante a pesquisa também contribuiu para melhorias gerais no sistema.

ABSTRACT Compact Wastewater Treatment Plants (CWTPs) are a great alternative to implementing decentralized sewage systems that can serve small communities. However, such systems are still poorly used and there is little experience regarding their operation. Based on such demand, this research aimed to evaluate the efficiency and to conduct an operational monitoring of a CWTP composed by an Upflow Anaerobic Sludge Blanket (UASB) reactor, followed by Submerged Aerated Filter (SAF), in the city of Uru, São Paulo, Brazil. During the research, the system proved to be a viable alternative for small communities, because it showed good efficiency, with average removal values of biochemical oxygen demand (BOD5) and chemical oxygen demand (COD) of 91 and 85%, respectively. The monitoring carried out during the research also contributed to general improvements in the system.

Tratamento de esgoto sanitário de baixa carga utilizando reator compartimentado anaeróbio/aeróbio em escala piloto / Treatment of low-strength sanitary sewage using an anaerobic/aerobic baffled reactor in pilot scale

RESUMO O objetivo principal da pesquisa foi avaliar o potencial de tratamento de esgoto sanitário de baixa carga orgânica em reator compartimentado anaeróbio/aeróbio (RCAA) em escala piloto. O reator, mantido em temperatura ambiente (27ºC a 30ºC), foi implantado no campus da Universidade Estadual Paulista "Júlio de Mesquita Filho" (UNESP) (Bauru, SP, Brasil) e tratou esgoto sanitário com carga orgânica entre 0,06 e 0,61 kg DQO.d-1. O RCAA é composto de quatro câmaras fisicamente separadas, sendo as três primeiras anaeróbias e a quarta aeróbia, seguidas por decantador laminar. O monitoramento foi realizado durante o período de 203 dias para tempos de detenção hidráulica total (TDH) de 33, 22, 16,5 e 8,25 horas. Durante o período experimental, verificou-se remoção média de matéria orgânica, em termos de demanda química de oxigênio total (DQOTotal), de 71 a 82% no sistema completo, com valores elevados de remoção na fase anaeróbia entre 62 e 71%. Em termos de sólidos em suspensão totais (SST), o reator apresentou remoções médias em torno de 90%. Os resultados obtidos nesta pesquisa permitiram um avanço no conhecimento operacional de uma alternativa biotecnológica de baixo custo, com o propósito de diminuir o impacto causado pela geração de esgotos de pequenas comunidades urbanas e rurais que ainda não contam com sistema de tratamento, e ainda possibilitar o reúso do efluente tratado.

ABSTRACT The research's main goal was to evaluate the treatment potential of low-strength sanitary sewage in an anaerobic/aerobic baffled reactor (AABR) at pilot-scale. The reactor, maintained at room temperature (27ºC to 30ºC), was deployed at Universidade Estadual Paulista "Júlio de Mesquita Filho" (UNESP), campus Bauru (SP, Brazil), and treated sanitary sewage with organic charge between 0.06 and 0.61 kgCOD.d-1. The AABR was composed by four chambers, physically separated, being the first three chambers anaerobic and the forth chamber aerobic, followed by a settling tank. The monitoration was done during 203 days for the hydraulic retention times (HRT) of 33, 22, 16.5 and 8.25 hours. During the experimental period, it was verified in the whole system a chemical oxygen demand (COD) removal between 71 and 82%, with high removal rates in the anaerobic phase between 62 and 71%. In terms of total suspended solids (TSS), the reactor reached average removal around 90%. The progress reached with this research allowed to present a low cost biotechnological alternative, with the propose of solving the sewage demand derived from small urban and rural communities, and also making possible the reuse of the treated effluent.

Desinfecção de efluente anaeróbio com o uso de ozônio/cloro / Anaerobic effluent disinfection using ozone/chlorine

O principal objetivo desta pesquisa foi estudar o processo de oxidação, a eficiência da inativação de coliformes e a formação de subprodutos da ozonização, associado com a desinfecção de efluente sanitário anaeróbio proveniente de um reator UASB. Tal evento foi realizado por meio da aplicação das dosagens de ozônio de 5,0 mg.O3.L-1+ 10 mg.Cl2.L-1 (ensaio 1); 8,0 mg.O3.L-1+ 20 mg.Cl2.L-1 (ensaio 2) e 10,0 mg.O3.L-1+ 30 mg.Cl2.L-1 (ensaio 3). Neste trabalho, utilizou-se efluente da Estação de Tratamento de Esgoto da Universidade de São Paulo, no Brasil. As reduções médias totais da demanda química de oxigênio para os efluentes ozonizados/clorados foram de 9, 32 e 37% para os ensaios 1, 2 e 3, respectivamente. A inativação dos coliformes totais variou de >5,7 até 6,4 log10 e >5,8 até >6,0 log10para Escherichia coli. A formação de aldeídos não sofreu mudanças significativas (p=0,05) para as dosagens e os tempos de contato aplicados após os ensaios de ozonização/cloração.

The main purpose of this research was to study the oxidation process, the coliform inactivation effectiveness, and the formation of ozone disinfection byproducts, which were associated with disinfection of the anaerobic sanitary wastewater effluent from a UASB reactor. Such event was performed with ozone applied at doses of 5.0 mg.O3.L-1+ 10 mg.Cl2.L-1 (essay 1); 8.0 mg.O3.L-1+ 20 mg.Cl2.L-1 (essay 2), and 10.0 mg.O3.L-1+ 30 mg.Cl2.L-1 (essay 3). The wastewater used in this research was generated at the Wastewater Treatment Plant of Universidade de São Paulo, in Brazil. The total mean decreases of the chemical oxygen demand for ozonized/chlorinated effluents were 9, 32 and 37% for assays 1, 2 and 3 respectively. The total coliform inactivation varied from >5,7 to 6,4 log10 and >5.8 to >6.0 log10 for Escherichia coli. The formation of aldehydes did not suffer any significant changes (p=0.05) for dosages and contact times applied after ozonation/chlorination assays.