981 resultados para ACTIVATED SLUDGE PROCESS
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Membrane bioreactors (MBRs) are a combination of activated sludge bioreactors and membrane filtration, enabling high quality effluent with a small footprint. However, they can be beset by fouling, which causes an increase in transmembrane pressure (TMP). Modelling and simulation of changes in TMP could be useful to describe fouling through the identification of the most relevant operating conditions. Using experimental data from a MBR pilot plant operated for 462days, two different models were developed: a deterministic model using activated sludge model n°2d (ASM2d) for the biological component and a resistance in-series model for the filtration component as well as a data-driven model based on multivariable regressions. Once validated, these models were used to describe membrane fouling (as changes in TMP over time) under different operating conditions. The deterministic model performed better at higher temperatures (>20°C), constant operating conditions (DO set-point, membrane air-flow, pH and ORP), and high mixed liquor suspended solids (>6.9gL-1) and flux changes. At low pH (<7) or periods with higher pH changes, the data-driven model was more accurate. Changes in the DO set-point of the aerobic reactor that affected the TMP were also better described by the data-driven model. By combining the use of both models, a better description of fouling can be achieved under different operating conditions
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This work presents a study about the elimination of anticancer drugs, a group of pollutants considered recalcitrant during conventional activated sludge wastewater treatment, using a biological treatment based on the fungus Trametes versicolor. A 10-L fluidized bed bioreactor inoculated with this fungus was set up in order to evaluate the removal of 10 selected anticancer drugs in real hospital wastewater. Almost all the tested anticancer drugs were completely removed from the wastewater at the end of the batch experiment (8 d) with the exception of Ifosfamide and Tamoxifen. These two recalcitrant compounds, together with Cyclophosphamide, were selected for further studies to test their degradability by T. versicolor under optimal growth conditions. Cyclophosphamide and Ifosfamide were inalterable during batch experiments both at high and low concentration, whereas Tamoxifen exhibited a decrease in its concentration along the treatment. Two positional isomers of a hydroxylated form of Tamoxifen were identified during this experiment using a high resolution mass spectrometry based on ultra-high performance chromatography coupled to an Orbitrap detector (LTQ-Velos Orbitrap). Finally the identified transformation products of Tamoxifen were monitored in the bioreactor run with real hospital wastewater
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Nitrous oxide emissions from an activated sludge plant which serves a research institute in Rio de Janeiro city were estimated from six unit processes (grit tank, sand trap, aeration tank, secondary settling tank, sludge recirculation line and aerobic digester sludge tank) and also from the plant effluent. Total estimated annual flux was 3.2 x 10(4) g N2O yr-1 of which about 90% was from the aeration tank. Emission factors estimated from population served, wastewater flow and nitrogen load (conversion ratio) were 13 g N2O person-1 yr-1, 9.0 x 10-5 g N2O Lwastewater-1 and 0.14%.
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Nitrous oxide (N2O) emissions were measured monthly from January to June 2010 in the aeration tank of a wastewater treatment plant (WWTP) in Southeast Brazil. Emissions were lower in summer than winter and were positively related with influent ammonium (NH4+) concentration. The average N2O emission was 1.11 kg N day-1 corresponding to 0.02% of the influent total nitrogen load. The average emission factor calculated for the population served was 2.5 lower than that proposed by the Intergovernmental Panel on Climate Change (IPCC) for inventories of N2O emissions from WWTPs with controlled nitrification and denitrification processes.
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Three bacterial strains were isolated from the activated sludge system of petroleum refinery wastewater, identified by partial sequencing of 16S rDNA, and classified as Acinetobacter genomospecies 3, Bacillus pumilus, and Bacillus flexus. The degradation efficiency of aromatic hydrocarbons was evaluated by gas chromatography with a flame ionization detector. In a mineral medium containing anthracene and phenanthrene and the consortium of microorganisms, the removal efficiency was 96% and 99%, respectively, after 30 days. The good rate of hydrocarbon degradation proves the operational efficiency of the microbial consortium in treating effluents containing these compounds.
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Tämä diplomityö tehtiin Vihdin Vesihuoltolaitoksen Nummelan jäteveden puhdistamolle. Työssä tutkittiin typenpoistoa kunnallisista jätevesistä membraanibioreaktorin (MBR) avulla. MBR:ssä yhdistyvät perinteinen aktiivilieteprosessi ja kalvosuodatus. Työn tavoite oli päästä yli 95 % typenpoistoon. Aluksi typenpoisto oli yli 80 %, kun pilot-mittakaavan MBR-laitosta operoitiin perinteisen prosessin parametrein. Typenpoistoa onnistuttiin tehostamaan nostamalla nitraattipitoisen palautuslietteen kierrätystä prosessin alkupäähän (1600 L/h) ja lisäämällä aktiivista biomassaa reaktorissa. Yli 90 % typenpoisto edellytti myös pidempää viipymäaikaa (noin kaksinkertainen perinteiseen prosessiin verrattuna). Tutkimuksessa päästiin parhaimmillaan jopa 95 % typenpoistumaan operoimalla laitteistoa pienellä typpikuormalla (0,1 kg/vrk) ja alhaisemmalla lietepitoisuudella (10 g/L). Typpikuorman noustessa (0,3 kg/vrk) typenpoistoteho laski. Tätä onnistuttiin parantamaan (yli 90 %) nostamalla biomassan määrää reaktorissa (15 g/L). Hyvän typenpoiston saavuttaminen edellytti myös suurempaa metanolin ja hapen syöttöä.
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Phosphate (Pi) is one among the most important essential residues in maintenance and inheritance of life, with far diverse physiological role as structural, functional and energy transduction. Phosphate accumulation in wastewaters containing run off of fertilizers and industrial discharges is a global problem that results in algal blooms in bays, lakes and waterways. Currently available methods for removing phosphates from wastewater are based primarily on polyP accumulation by the activated sludge bacteria. PolyP plays a critical role in several environmental and biotechnological problems. Possible relation of interaction between polyP accumulation phenomenon, the low biomass, low Pi uptake, and varying results obtained in response to the impact of sodium chloride, pH, temperature, various inorganic salts and additional carbon sources studied, are all intriguing observations in the present investigation. The results of the present study have evidenced very clearly the scope for potential strains of bacteria from both sea water and marine sediments which could be exploited both for Pi removal in wastewater released by industries and intensive aquaculture practices in to the aquatic environment as well as to harness the potential strains for industrial production of polyP which was wide range of applications.
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The activated sludge and anaerobic digestion processes have been modelled in widely accepted models. Nevertheless, these models still have limitations when describing operational problems of microbiological origin. The aim of this thesis is to develop a knowledge-based model to simulate risk of plant-wide operational problems of microbiological origin.For the risk model heuristic knowledge from experts and literature was implemented in a rule-based system. Using fuzzy logic, the system can infer a risk index for the main operational problems of microbiological origin (i.e. filamentous bulking, biological foaming, rising sludge and deflocculation). To show the results of the risk model, it was implemented in the Benchmark Simulation Models. This allowed to study the risk model's response in different scenarios and control strategies. The risk model has shown to be really useful providing a third criterion to evaluate control strategies apart from the economical and environmental criteria.
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En aquesta tesis s'ha desenvolupat un sistema de control capaç d'optimitzar el funcionament dels Reactors Discontinus Seqüencials dins el camp de l'eliminació de matèria orgànica i nitrogen de les aigües residuals. El sistema de control permet ajustar en línia la durada de les etapes de reacció a partir de mesures directes o indirectes de sondes. En una primera etapa de la tesis s'ha estudiat la calibració de models matemàtics que permeten realitzar fàcilment provatures de diferents estratègies de control. A partir de l'anàlisis de dades històriques s'han plantejat diferents opcions per controlar l'SBR i les més convenients s'han provat mitjançant simulació. Després d'assegurar l'èxit de l'estratègia de control mitjançant simulacions s'ha implementat en una planta semi-industrial. Finalment es planteja l'estructura d'uns sistema supervisor encarregat de controlar el funcionament de l'SBR no només a nivell de fases sinó també a nivell cicle.
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O reator seqüencial em batelada (RSB) é uma variante de lodos ativados capaz de promover a remoção da matéria orgânica, a remoção dos nutrientes e a separação da fase sólida da líquida em uma unidade. A valorização das áreas urbanas, a carência de tratamento terciário e a crescente necessidade de redução nas dimensões de estações de tratamento de esgoto devem impulsionar o desenvolvimento de pesquisas sobre RSB em curto espaço de tempo. A partir deste cenário, o presente trabalho teve como objetivo modelar o comportamento do reator seqüencial em batelada a partir da teoria desenvolvida por Marais e colaboradores. Dentro deste contexto, a cinética de oxidação dos compostos orgânicos e do nitrogênio na forma amoniacal foi descrita e modelada. O trabalho experimental foi realizado em duas escalas: bancada e piloto. O experimento em escala de bancada foi dividido em duas fases. Foram utilizados dois RSBs e um sistema de fluxo contínuo. Um reator seqüencial em batelada (RSB1) foi operado com idade de lodo. O outro reator em batelada (RSB2) foi operado em função da relação F/M e o sistema de fluxo contínuo (FC1) por idade de lodo. Estes reatores foram utilizados como controle no monitoramento do RSB1 Na primeira fase, os três sistemas removeram apenas matéria orgânica. Na fase seguinte, removeram matéria orgânica e nitrogênio. A partir dos resultados obtidos em escala de bancada, foi possível concluir que o modelo desenvolvido pode ser aplicado ao reator seqüencial em batelada operando com idade de lodo, permitindo determinar a qualidade do efluente, a produção de lodo e o consumo de oxidante. Além disso, foi possível descrever o comportamento da taxa de consumo de oxigênio em função da oxidação da matéria orgânica biodegradável e da oxidação do nitrogênio na forma amoniacal. O reator seqüencial em batelada operado com idade de lodo (RSB1) alcançou remoção média de matéria orgânica de 90 % nas idades de lodo de 30, 20, 10 e 5 dias. A remoção média de nitrogênio mais elevada foi obtida na idade de lodo de 20 dias e atingiu 87 %. Nas demais idades de lodo a remoção média de nitrogênio variou entre 79 e 42 %. A modelagem do comportamento do reator seqüencial em batelada resultou numa proposta de metodologia para o dimensionamento que tem como finalidade abolir critérios obsoletos e inadequados para o dimensionamento de lodos ativados em batelada No experimento em escala piloto, foram utilizados um reator seqüencial em batelada, denominado RSB, e um sistema de fluxo contínuo com a configuração Bardenpho, denominado FC. Os sistemas de lodos ativados sob investigação foram monitorados em duas idades de lodo: 30 e 10 dias. Os dados do experimento em escala piloto mostraram que os processos físico-químicos e biológicos envolvidos na remoção de matéria orgânica e nitrogênio no RSB foram mais eficientes do que no Bardenpho quando trataram o mesmo esgoto doméstico e foram submetidos às mesmas condições operacionais. No RSB, obteve-se 88 e 89 % de remoção de matéria orgânica nas idades de lodo de 10 e 30 dias, respectivamente. Nesta seqüência das idades de lodo, a eficiência do Bardenpho caiu de 87 para 76 %. O sistema de fluxo contínuo removeu 66 e 52 % do nitrogênio total afluente nas idades de lodo de 10 e 30 dias, respectivamente. A eficiência do RSB na remoção de nitrogênio foi determinada apenas na idade de lodo de 10 dias e alcançou 69 %. A partir dos resultados obtidos em escala de bancada e piloto, constata-se que o reator seqüencial em batelada operando com idade de lodo pode ser utilizado no tratamento de esgoto doméstico e obter eficiência na remoção de matéria orgânica e nitrogênio igual ou superior ao sistema de fluxo contínuo.
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)
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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)