Graduation date: 2003 / Best scan available on figures. Original figures are dark.

The fate of antimicrobials entering the aquatic environment is an increasing concern for researchers and regulators, and recent research has focused on antimicrobial contamination from point sources, such as wastewater treatment facility outfalls. The terraccumulation of antimicrobials and mobility in diffuse pollution pathways should not be overlooked as a contributor to the spread of bacterial resistance and the resulting threat to human drug therapy. This review critically examines recent global trends of bacterial resistance, antimicrobial contaminant pathways from agriculture and water treatment processes, and the need to incorporate diffuse pathways into risk assessment and treatment system design. Slow sand filters are used in rural regions where source water may be subjected to antimicrobial contaminant loads from waste discharges and diffuse pollution. A simple model was derived to describe removal efficiencies of antimicrobials in slow sand filtration and calculate antimicrobial concentrations sorbed to the schmutzdecke at the end of a filtration cycle. Input parameters include water quality variables easily quantified by water system personnel and published adsorption, partitioning, and photolysis coefficients. Simulation results for three classes of antimicrobials suggested greater than 4-log removal from 1 ��g/L influent concentrations in the top 30 cm of the sand column, with schmutzdecke concentrations comparable to land-applied biosolids. Sorbed concentrations of the antimicrobial tylosin fed to a pilot filter were within one order of magnitude of the predicted concentration. To investigate the behavior of antimicrobial contaminants during multi-stage filtration, five compounds from four classes of antimicrobials were applied to a mature slow sand filter and roughing filter fed raw water from the Santiam River in Oregon during a 14-day challenge study. Antimicrobial removal efficiency of the filters was calculated from 0.2 mg/L influent concentrations using HPLC MS/MS. and sorption coefficients (K[subscript d], K[subscript oc], K[subscript om]) were calculated for schmutzdecke collected from a mature filter column. Sulfonamides had low sorption coefficients and were largely unaffected by multi-stage filtration. Lincomycin, trimethoprim, and tylosin exhibited higher sorption coefficients and limited mobility within the slow sand filter column. The lack of a significant increase in overall antimicrobial removal efficiency indicated biodegradation is less significant than sorption in multi-stage filtration. / Graduation date: 2004

The validation of UV reactors is currently accomplished by biodosimetry, in which the reactor is treated as a "black-box" and hence cannot account for the dependence of the dose delivery on the complex hydrodynamics and the spatial variation in UV intensity. Alternative methods, such as fluorescent microspheres as non-biological surrogates and computational fluid dynamics (CFD) simulations, have been developed; however, each method has its shortcomings. In this study, a novel technique for the spatial and temporal assessment of the hydrodynamics and the UV dose delivered and the link between these two factors in a lab-scale UV reactor using three dimensional laser induced fluorescence (3DLIF) is developed. This tool can also be utilized for the optimization of UV reactors and to provide data for validation of CFD-based simulation techniques. Regions of optimization include areas around the UV lamp where short-circuiting occurred, a longer inlet approach section that enhances the performance of the reactor by reducing short circuiting paths and a longer outlet region to provide greater mixing. 3DLIF allows real time characterization of mixing and dose delivery in a single lamp UV reactor placed perpendicular to flow by capturing fluorescence images emitted from a laser dye, Rhodamine 6G, using a high speed CCD camera. In addition to three-dimensional mixing, the technique successfully visualized the two-dimensional, transient mixing behaviors such as the recirculation zone and the von Karman vortices and the fluence delivery within the reactor, which has not been possible with traditional tracer test techniques. Finally, a decomposition technique was applied to the flow and fluence delivery based concentration data to reveal similar structures that affect these phenomena. Based on this analysis, changing the flow in the reactor, i.e. the Reynolds number, will directly affect the fluence delivery.

The removal of microbial populations from potable water has been a practice with great importance towards public health, as it has resulted in the reduction of literally millions of cases of infectious disease. In the United States, pathogenic organisms are most commonly removed from drinking water through the application of chlorine. Ninety-nine per cent of all U.S. potable water treatment facilities that disinfect, rely on chlorine as their sole or primary disinfectant, and over 175,000,000 Americans regularly consume chlorinated water. In 1974, Rook and Bellar et al. published studies which indicated that chlorine reacted with organic matter in water during treatment to produce a wide-range of halogenated by-products. Since that time, numerous analyses have been performed to isolate and identify the by-products of chlorination. Toxicologic and epidemiologic studies have been performed, some of which suggest that the use of chlorine as a disinfectant may be contributing to the incidence of chronic disease in the United States. Because of the concern that the use of chlorine for potable water disinfection may be contributing to chronic disease, Amendments to the Safe Drinking Water Act (SDWA) have been promulgated which strictly regulate disinfectants and disinfection by-products. Future disinfectant and disinfectant by-product regulations (1992) will have a major impact on the purveyors of potable water in the U.S.. Probably the largest challenge U.S. water treatment utilities now face is in the attempt to control for disinfectants and disinfectant by-products while maintaining the microbiological integrity of the water supply. The SDWA Amendments and their supporting regulations will result in major changes in the way water quality parameters are measured, and the way disinfection and treatment strategies are practiced. This thesis looks closely at the role of chlorine as a disinfectant, the by-products arising from chlorine reacting with organic matter, as well as the rationale behind the disinfectant and disinfectant by-product regulations. After examining the chemical, toxicologic and epidemiologic evidence which fueled the new SDWA regulations, available treatment strategies for meeting the new regulations will be detailed and examined. A water treatment strategy which best appears to maximize the reduction of waterborne disease and minimize the risk of chronic disease will then be offered. / Graduation date: 1992

CAPES / A utilização de coagulantes naturais no tratamento de água vem sendo uma alternativa cada vez mais empregada a fim de evitar possíveis danos à saúde e ao meio ambiente causados por determinados coagulantes químicos. A Moringa oleifera é uma árvore de múltiplos usos, cujas sementes possuem uma eficiente atividade como coagulante natural. Entretanto, estudos apontam para uma possível toxicidade deste extrato. Baseando-se nisto, o objetivo do presente trabalho foi o de avaliar a toxicidade de três diferentes extratos de M. oleifera (extrato aquoso, extrato salino da semente integral e extrato salino da semente sem óleo) e da água tratada com os mesmos extratos, frente a duas espécies de microcrustáceos utilizadas como bioindicadoras de toxicidade (Daphnia magna e Artemia salina). Nos ensaios de toxicidade aguda dos extratos utilizando D. magna, verificou-se uma CE50 de 314,05 mg.L-1 para o extrato salino da semente integral e 346,76 mg.L-1 para o extrato salino da semente sem óleo. O extrato aquoso não apresentou toxicidade nem mesmo nas maiores concentrações (400 a 600 mg.L-1). Para o organismo A. salina, nenhum dos extratos mostrou-se tóxico. Nos ensaios realizados com a água tratada com os extratos de M. oleifera, foi encontrada toxicidade para D. magna nas frações sobrenadante (CE50=296,02 mg.L-1) e sedimentada (CE50=291,04 mg.L-1) da água tratada com o extrato salino da semente integral. Para a água tratada com o extrato salino da semente sem óleo, da mesma forma encontrou-se toxicidade nas frações sobrenadante (CE50=351,17 mg.L-1) e sedimentada (CE50=342,32 mg.L-1), o que indica que a toxicidade do extrato não é reduzida após a coagulação/floculação/sedimentação. No teste crônico realizado utilizando organismos de D. magna expostos durante 21 dias ao extrato salino da semente integral de M. oleifera, foram observadas alterações nos parâmetros avaliados (mortalidade, fecundidade e crescimento), sendo que quanto maior a concentração testada, maiores os efeitos tóxicos. Ao término dos 21 dias experimentais, havia ocorrido a mortalidade de 100% dos indivíduos expostos às maiores concentrações (10 e 15 mg.L-1). Além disso, houve grande variação na fecundidade entre os grupos. Com base nestes resultados, é possível afirmar que a utilização de elevadas concentrações do extrato de M. oleifera (acima de 300 mg.L-1) pode causar danos agudos ao organismo D. magna. Entretanto, na prática, as concentrações utilizadas deste coagulante são consideravelmente menores, variando principalmente entre 50 e 150 mg.L-1, de acordo com dados da literatura. Da mesma forma, a diluição que ocorreria no meio hídrico dificilmente proporcionaria que a concentração permanecesse elevada, mesmo que grande quantidade do extrato chegasse ao meio ambiente. Com base nisso, é possível afirmar que o uso do extrato da M. oleifera pode ser incentivado, mas desde que utilizado com cautela, evitando-se concentrações elevadas. / The use of natural coagulants for water treatment has been an alternative increasingly employed in order to avoid possible damage to health and the environment caused by certain chemical coagulants. Moringa oleifera is a multipurpose tree whose seeds have an efficient activity as natural coagulant. However, studies point to a possible toxicity of this extract. Based on this, the objective of this study was to evaluate the toxicity of three different extracts of M. oleifera (aqueous extract, saline extract of the whole seed and saline extract of the seed without oil) and water treated with the same extracts, against two species of microcrustaceans used as bioindicators of toxicity (Artemia salina and Daphnia magna). In acute toxicity tests of the extracts using D. magna, there was an EC50 of 314.05 mg.L-1 for the saline extract of the whole seed and 346.76 mg.L-1 for the saline extract of the seed without oil. The aqueous extract showed no toxicity even at the highest concentrations (400 to 600 mg.L-1). For the organism A. saline, none of the extracts proved toxic. In the tests performed with water treated with the extracts of M. oleifera, toxicity was found for D. magna in the supernatant fractions (EC50=296.02 mg.L-1) and sedimented (EC50=291.04 mg.L-1) of treated water with the saline extract of the whole seed. For the treated water with the saline extract of the seed without oil, was found toxicity in the supernatant fraction (EC50=351.17 mg.L-1) and the sedimented fraction (EC50=342.32 mg.L-1), which indicates that the toxicity of the extract is not reduced after coagulation/flocculation. In the chronic test performed using D. magna exposed during 21 days to the saline extract of the whole seed of M. oleifera, changes in the evaluated parameters (mortality, fertility and growth) were observed, and as higher the concentration tested, bigger was the toxicity. At the end of the 21 experimental days, there had been a 100% mortality of individuals exposed to higher concentrations (10 and 15 mg.L-1). Furthermore, there was wide variation in fertility between the groups. Based on these results, we can say that the use of high concentrations of the extract of M. oleifera (above 300 mg.L-1) can cause acute damage for D. magna. However in practice, the concentrations used of this coagulant are considerably smaller, ranging mainly between 50 and 150 mg.L-1, according to literature data. Likewise, the dilution that occur in the aquatic environment, hardly provide high concentration of the extract in the water bodies. Based on this, we can say that the use of the extract of M. oleifera can be encouraged, but if used with caution, avoiding high concentrations.

PUMPS mimics natural geothermal vents as a conceptual model designed for the remediation of acid mine water (AMW) in voids of abandoned gold mines of the Witwatersrand Basin in South Africa. In this system, a reaction chamber containing Desulfotomaculum kuznetsovii sulfate reducing bacteria will be set at the bottom of a 3-4 km deep mine that will be flooded. A geothermal system with at least one (1) doublet will be drilled from the bottom of the mine to the depth of 8km, where the temperatures are sufficient for geothermal energy harvesting. AMW, used as a geothermal fluid, will be pumped down the injection well and circulate through hot rock. The hot water is then used to generate electricity and then channelled into the reaction chamber to undergo bio-remediation. Following treatment, the water flows back into the mine voids where it will improve the quality of untreated AMW through dilution. Eventually, the mine will be flooded with clean water that can be stored underground and/or pumped up to surface for social and ecosystem services. Following an introduction and proof of concept for the PUMPS, the research builds further on the technical and economic evaluation of the PUMPS in order to assert its viability and sustainability. The technical viability includes testing the ability for Desulfotomaculum kuznetsovii to survive in high pressure condition; quantifying the amount of energy that can be drawn from the geothermal reservoir; determining the placement and scheme of the geothermal wells; and, finally, developing a robust economic model of the system. Experiments show that Desulfotomaculum Kuznetsovii can tolerate high pressure conditions in of at least 100bar at their ideal sulfate reducing temperature of 63°C. Geochemical modelling shows that AMW can be used effectively as a geothermal fluid for PUMPS. To achieve highest efficiency and minimal fluid loss, the geothermal wells should be placed along the SSE-NNW direction, based on the known stress field across the Witwatersrand Basin. With a flow rate of 30l/s the energy drawn from the geothermal reservoir is sufficient to drive PUMPS and the surplus energy is determined by the volume of AMW treated per day. All results indicate that the PUMPS is technically and economically viable. The economic model shows that the value and viability of the PUMPS is best reflected with a comprehensive inclusion of potential revenue (for example from chemical solution mining of deep seated gold) and financial/environmental incentives.

Um dos grandes desafios para a Ciência é buscar processos metodológicos que reflitam direta ou indiretamente no ambiente, diminuindo o impacto ao meio e ao mesmo tempo, proporcionando o desenvolvimento desses processos. A água é, atualmente, um desses desafios, principalmente quanto à disponibilidade e ao padrão de qualidade microbiológico e físico-químico para consumo. Por causa desta problemática, é que o trabalho teve como objetivo utilizar sementes de moringa para redução da turbidez, por apresentar um biocoagulante que apresenta vantagens, quando se compara com os coagulantes químicos. A água foi coletada no rio Capibaribe, no município de Recife, Pernambuco, Brasil. Os parâmetros físico-químicos como pH, condutividade elétrica e turbidez foram determinados antes (pH=8,11; CE=8,35 mS/cm; turbidez=16,62 NTU) e após o tratamento. As concentrações do pó da Moringa oleífera foram 0, 50, 100, 200, 250 e 300 mg/200mL de água, relacionados com tempo de contato correspondente a 0,1, 2, 4 e 6 horas, sendo estes ajustados pelo planejamento experimental DCCR. Após os ensaios, o resultado obtido na remoção de até 100 % da turbidez foi com a concentração de 200 mg, com o tempo de sedimentação de 2 horas, comprovando a eficiência do biocoagulante presente na semente da Moringa oleífera para a clarificação da água. Antes e após os tratamentos foram determinadas turbidez, pH e condutividade elétrica. Os resultados foram analisados pela tabela ANOVA e o gráfico de Pearson que representavam respectivamente um nível de significância de 5 % e correlação entre as variáveis. Verificou-se que o tempo de sedimentação e o pH apresentou correlação de 0,63; e de turbidez com pH foi de 0,49. Os resultados observados nas fotomicrografias eletrônicas de varredura indicam melhoria da biossorvência de partículas dissolvidas. / One of the greatest challenges for science is searching for methodological processes which reflect directly or indirectly in the environment, decreasing the environmental impact and at the same time, providing the development of these processes. Water is currently one of those challenges, especially with regard to the availability and the pattern of physical-chemical and microbiological quality for consumption. Because of this problem, is that the work aims using moringa seeds to reduce turbidity, by presenting a biological coagulant that has advantages, when compared with the chemical coagulants. The water was collected in the Capibaribe River, in the municipality of Recife, Pernambuco, Brazil. The physical and chemical parameters such as pH, electrical conductivity and turbidity were determined before (pH=8 .11; CE=8.35 mS/cm; turbidez= 16.62 NTU) and after treatment. The Moringa powder oleifera were 0, 50, 100, 200, 250 and 300 mg/200mL of water, related to contact time corresponding to 0.1, 2, 4, and 6:0, which are adjusted for planning experimental CCRD. After the tests, the result obtained in the removal of up to 100 of the turbidity was with the concentration of 200 mg, with the time of sedimentation 2:0, proving the efficiency of biological coagulant present in Moringa seed oleifera for clarifying the water. Before and after the treatments were determined turbidity, pH and electrical conductivity. The results were analyzed by ANOVA table and the chart of Pearson representing respectively a significance level of 5 and correlation between variables. It was found that the time of sedimentation and pH showed correlation of 0.63; turbidity and pH was 0.49. The results observed in the electronic scanning photomicrographs indicate improvement in the particle biological sorvente dissolved.

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES) / O consumo de águas com alto teor de flúor pode resultar em fluorose dental ou esquelética, além de outros malefícios para a saúde pública. Neste sentido, o presente trabalho avaliou o processo de redução de flúor contido em excesso em água sintética e subterrânea fluorada a partir do processo de coagulação/floculação/sedimentação (C/F/S) com extrato aquoso de Moringa oleifera Lam e, do processo combinado com filtração por membranas. Os ensaios de C/F/S foram realizados em equipamento “jar test”, sendo a Moringa, utilizada na forma de extrato aquoso em diferentes concentrações. As amostras de água sintética e subterrânea foram fluoradas com fluoreto de sódio (NaF) nas concentrações de 3,0; 5,0; 7,5 e 10,0 mg F-/L e, variando-se o pH entre 3, 7 e 9. Os ensaios combinados com membranas de microfiltração e ultrafiltração, utilizando-se pressões de 1 e 2 bar, consistiram em submeter amostras de água sintética fluorada na concentração inicial de 5,0 mg F-/L, concentração de Moringa de 5 g/L e, pH7 ao processo de C/F/S, seguido da passagem pelo módulo de micro-ultrafiltração. O monitoramento do sistema de tratamento proposto, foi verificado por meio das análises de cor aparente, turbidez, pH, condutividade e flúor, antes e após os ensaios. Os resultados demonstraram bons valores de eficiência para o tratamento proposto de C/F/S, sendo que, para a concentração inicial de flúor de 3,0 mg F-/L todos os residuais de flúor tanto para a água sintética como para a água subterrânea fluorada, ficaram abaixo do valor máximo estabelecido pela Portaria nº 2.914/2011 do Ministério da Saúde que estabelece o limite de 1,5 mg F-/L. Os demais residuais provenientes das concentrações de 5,0; 7,5 e 10,0 mg F-/L, ficaram ligeiramente acima da legislação. Os valores de pH final ficaram dentro da faixa de neutralidade. Em relação aos parâmetros cor, turbidez e condutividade final, houve um ligeiro aumento dos valores, sendo indicado uma posterior etapa de pós-tratamento, como a adoção de filtração. Para o processo combinado, obteve-se bons resultados de redução de flúor, cor e turbidez da ordem de 83,0 %, 96,0 % e 98,0 %, respectivamente, para a membrana de 5 kDa utilizando pressão de 2 bar. De modo geral, os processos de tratamento propostos utilizando extrato de sementes de Moringa oleifera Lam, demonstraram-se como uma boa alternativa para a redução do excesso de flúor em águas, tendo-se em vista a utilização de um agente coagulante natural, biodegradável e responsável pela geração de um menor volume de lodo, diferentemente do que é observado com a utilização de coagulantes químicos. / The consumption of water with high fluoride levels may result in dental or skeletal fluorosis, and other hazards to public health. In this sense, the present study evaluated the process of reducing excess fluoride contained in fluoridated synthetic water and groundwater from the coagulation/ flocculation/sedimentation (C/F/S) with aqueous extract of Moringa oleifera Lam, and the process combined with membrane filtration. Assays C/F/S were performed in "jar test", and Moringa, used in the aqueous extract at different concentrations. Water samples were fluorinated and ground synthetic sodium fluoride (NaF) at concentrations of 3.0, 5.0, 7.5 and 10.0 mg F-/L, varying the pH between 3, 7 and 9. Tests combined with microfiltration and ultrafiltration membranes, using pressures of 1 bar and 2, consisting in subjecting samples of fluorinated synthetic water initial concentration of 5.0 mg F-/L, Moringa concentration of 5 g/L and , pH7 to process C/F/S, followed by passage through micro-ultrafiltration module. The monitoring system proposed treatment was assessed through analyzes of apparent color, turbidity, pH, conductivity and fluoride before and after the tests. The results showed good efficiency values proposed for the treatment of C/F/S, and so the initial concentration of 3.0 mg/L of fluoride all residual to both the synthetic water as the water Fluorinated underground, were below the maximum established by Ordinance nº 2.914/2011 the Ministry of Health establishing the limit of 1.5 mg F-/L. The remaining residual concentration of from 5.0: 7.5 and 10.0 mg F-/L, were slightly above the law. The final pH values were within the range of neutrality. The parameters color, turbidity and conductivity end there was a slight increase in values, and a subsequent step indicated post-treatment such as the adoption of filtration. To the combined process, good results were obtained reduction fluorine, color and turbidity of the order of 83.0%, 96.0% and 98.0% respectively for the 5 kDa membrane using pressure of 2 bar. Generally, treatment processes proposed using seed extract Moringa oleifera Lam, proved to be a good alternative to the reduction of excess of fluorine in water, with a view to the use of a coagulating agent natural, biodegradable and the generation of smaller volumes of sludge, unlike what is observed with the use of chemical coagulants.

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES) / O consumo de águas com alto teor de flúor pode resultar em fluorose dental ou esquelética, além de outros malefícios para a saúde pública. Neste sentido, o presente trabalho avaliou o processo de redução de flúor contido em excesso em água sintética e subterrânea fluorada a partir do processo de coagulação/floculação/sedimentação (C/F/S) com extrato aquoso de Moringa oleifera Lam e, do processo combinado com filtração por membranas. Os ensaios de C/F/S foram realizados em equipamento “jar test”, sendo a Moringa, utilizada na forma de extrato aquoso em diferentes concentrações. As amostras de água sintética e subterrânea foram fluoradas com fluoreto de sódio (NaF) nas concentrações de 3,0; 5,0; 7,5 e 10,0 mg F-/L e, variando-se o pH entre 3, 7 e 9. Os ensaios combinados com membranas de microfiltração e ultrafiltração, utilizando-se pressões de 1 e 2 bar, consistiram em submeter amostras de água sintética fluorada na concentração inicial de 5,0 mg F-/L, concentração de Moringa de 5 g/L e, pH7 ao processo de C/F/S, seguido da passagem pelo módulo de micro-ultrafiltração. O monitoramento do sistema de tratamento proposto, foi verificado por meio das análises de cor aparente, turbidez, pH, condutividade e flúor, antes e após os ensaios. Os resultados demonstraram bons valores de eficiência para o tratamento proposto de C/F/S, sendo que, para a concentração inicial de flúor de 3,0 mg F-/L todos os residuais de flúor tanto para a água sintética como para a água subterrânea fluorada, ficaram abaixo do valor máximo estabelecido pela Portaria nº 2.914/2011 do Ministério da Saúde que estabelece o limite de 1,5 mg F-/L. Os demais residuais provenientes das concentrações de 5,0; 7,5 e 10,0 mg F-/L, ficaram ligeiramente acima da legislação. Os valores de pH final ficaram dentro da faixa de neutralidade. Em relação aos parâmetros cor, turbidez e condutividade final, houve um ligeiro aumento dos valores, sendo indicado uma posterior etapa de pós-tratamento, como a adoção de filtração. Para o processo combinado, obteve-se bons resultados de redução de flúor, cor e turbidez da ordem de 83,0 %, 96,0 % e 98,0 %, respectivamente, para a membrana de 5 kDa utilizando pressão de 2 bar. De modo geral, os processos de tratamento propostos utilizando extrato de sementes de Moringa oleifera Lam, demonstraram-se como uma boa alternativa para a redução do excesso de flúor em águas, tendo-se em vista a utilização de um agente coagulante natural, biodegradável e responsável pela geração de um menor volume de lodo, diferentemente do que é observado com a utilização de coagulantes químicos. / The consumption of water with high fluoride levels may result in dental or skeletal fluorosis, and other hazards to public health. In this sense, the present study evaluated the process of reducing excess fluoride contained in fluoridated synthetic water and groundwater from the coagulation/ flocculation/sedimentation (C/F/S) with aqueous extract of Moringa oleifera Lam, and the process combined with membrane filtration. Assays C/F/S were performed in "jar test", and Moringa, used in the aqueous extract at different concentrations. Water samples were fluorinated and ground synthetic sodium fluoride (NaF) at concentrations of 3.0, 5.0, 7.5 and 10.0 mg F-/L, varying the pH between 3, 7 and 9. Tests combined with microfiltration and ultrafiltration membranes, using pressures of 1 bar and 2, consisting in subjecting samples of fluorinated synthetic water initial concentration of 5.0 mg F-/L, Moringa concentration of 5 g/L and , pH7 to process C/F/S, followed by passage through micro-ultrafiltration module. The monitoring system proposed treatment was assessed through analyzes of apparent color, turbidity, pH, conductivity and fluoride before and after the tests. The results showed good efficiency values proposed for the treatment of C/F/S, and so the initial concentration of 3.0 mg/L of fluoride all residual to both the synthetic water as the water Fluorinated underground, were below the maximum established by Ordinance nº 2.914/2011 the Ministry of Health establishing the limit of 1.5 mg F-/L. The remaining residual concentration of from 5.0: 7.5 and 10.0 mg F-/L, were slightly above the law. The final pH values were within the range of neutrality. The parameters color, turbidity and conductivity end there was a slight increase in values, and a subsequent step indicated post-treatment such as the adoption of filtration. To the combined process, good results were obtained reduction fluorine, color and turbidity of the order of 83.0%, 96.0% and 98.0% respectively for the 5 kDa membrane using pressure of 2 bar. Generally, treatment processes proposed using seed extract Moringa oleifera Lam, proved to be a good alternative to the reduction of excess of fluorine in water, with a view to the use of a coagulating agent natural, biodegradable and the generation of smaller volumes of sludge, unlike what is observed with the use of chemical coagulants.

Orientador: Ruben Bresaola Júnior / Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Civil, Arquitetura e Urbanismo / Made available in DSpace on 2018-08-17T01:59:19Z (GMT). No. of bitstreams: 1 Franquini_PauloEduardo_M.pdf: 2223374 bytes, checksum: daba13dae2b6107bdc84e30e66001bf8 (MD5) Previous issue date: 2010 / Resumo: A presente pesquisa teve por objetivo avaliar, em escala de laboratório, a formação de subprodutos da desinfecção (SPD), aldeídos (ALD) e trialometanos (THM), originados a partir da oxidação em soluções contendo ácidos húmicos na presença ou não de íons brometo, sob a ação do cloro livre, sob diferentes concentrações e tempos de contato. A técnica analítica utilizada foi a extração líquido-líquido e cromatografia gasosa com detector de captura de elétrons, a qual proporcionou a separação dos SPD originados em espécies: formaldeído, acetaldeído, glioxal, metilglioxal, clorofórmio, bromodiclorometano, dibromoclorometano e bromofórmio. A presença de íons brometo proporcionou maiores concentrações de ALD totais (TALD) e THM totais (TTHM), sob o tempo de contato de 12 h e 24 h, respectivamente. A variação de concentração de íons brometo de 0,50 para 2,00 mg L?1, promoveu uma depreciação na concentração de TALD em 12 h e uma inversão nas concentrações das espécies predominantes que existiam na ausência dos íons. A inversão nas concentrações das espécies predominantes de THM que existiam na ausência dos íons também foi presenciada, sendo que prevaleceram as espécies bromadas em detrimento das cloradas. Os resultados com íons brometo indicaram a possibilidade da existência de reações de oxidação competitivas para cada grupo de SPD e discutidas no trabalho. A remoção dos SPD foi realizada por adsorção mediante a utilização de carvão ativado em pó (CAP) em diferentes dosagens e com tempos de detenção do CAP de 60 e 120 min, seguido de simulação, em laboratório, do tratamento convencional de água, utilizando-se o sulfato de alumínio como coagulante. Os resultados destes ensaios realizados demonstraram remoções da ordem de 77% para os aldeídos totais, empregando-se dosagem de 30 mg L?1 de CAP e de 86% para os THM totais, empregando-se dosagem de 100 mg L?1 do mesmo, ambas as remoções sob tempo de detenção de 60 min. Os resultados de remoções de THM totais proporcionaram a adequação da água nos limites estabelecidos pela legislação brasileira e permitiram realizar simulações de custo do CAP a ser utilizado nas estações de tratamento de água / Abstract: The present research was to evaluate, in laboratory scale, the formation of disinfection byproducts (DPB), aldehydes (ALD) and trihalomethanes (THM), originated from the oxidation in solutions containing humic acids in the presence or not of ions bromide, under the action of free chlorine, under different concentrations and timing contact. The analytical technique used was the extraction liquid-liquid and gás chromatography with electrons detector capture, which provided the separation of DPB originated in species: formaldehyde, acetaldehyde, glyoxal, methyl-glyoxal, chloroform, bromodichloromethane, dibromochloromethane and bromoform. The presence of íons bromide gave higher concentrations of total ALD (TALD) and total THM (TTHM), under the time contact of 12 h and 24 h, respectively. The variation in the concentration of íons bromide from 0,50 to 2,00 mg L?1, caused depreciation in the concentration of TALD and a reversal in concentrations of predominant species that existed in the absence of ions. The reversal in concentrations of the THM predominant species that existed in the íons absence was also seen, and the brominated species prevailed at the detriment of chlorinated ones. The results with ions bromide indicated the possibility of the existence of competitive oxidation reactions for each group of DPB and it was discussed on the work. The removal of DPB was performed by adsorption using powdered activated carbon (PAC) in different dosages and with times of detention of PAC of 60 and 120 min, followed by simulation of the conventional water treatment, in the laboratory, using aluminum sulphate as coagulant. The adsorption test results, followed by coagulation, flocculation, sedimentation and filtration, showed removals of the order of 77% for TALD, using dosage of 30 mg L?1 PAC, and 86% for TTHM, using dosage of 100 mg L?1 of the same, both removals under detention time of 60 min. The total THM removal results gave the adequacy of water within the limits established by Brazilian legislation and allowed the realizations of simulations of cost of PAC to be used in water treatment / Mestrado / Saneamento e Ambiente / Mestre em Engenharia Civil