130 resultados para Chlorination.
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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)
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Pós-graduação em Engenharia Civil - FEIS
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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)
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Com o objetivo de avaliar a efetiva ação sanitizante do tratamento de carcaças bovinas e bubalinas pelo cloro e de outros procedimentos higiênicos empregados no abate, foram selecionados aleatoriamente 35 bovídeos abatidos em um estabelecimento de abate localizado na região metropolitana de Belém, assim como a superfície de equipamentos e utensílios, a água empregada na lavagem das meias carcaças e o interior de câmaras frigoríficas. Para a coleta das amostras foram aplicados swabs na superfície muscular dos cortes de carne (coxão, flanco, lombo, paleta e pescoço) usando molde estéril de 100 cm2, e na superfície de facas e serras que, rotineiramente, entraram em contato direto com as carcaças. As amostras foram enviadas em solução salina peptonada para análise laboratorial. Para avaliação da qualidade sanitária da água empregada na higienização no decorrer das operações de abate e no tratamento de sanitização, foram feitas coletas de água antes da cloração e no chuveiro de lavagem por aspersão das meias carcaças em recipientes estéreis com adição de 1% de tiossulfato de sódio 0,25% para a água clorada, após o que enviadas para análise microbiológica. Avaliando a condição sanitária de câmaras frigoríficas, foram empregadas placas entre-abertas sobre o piso com meios de cultura específicos. As amostras coletadas através da técnica do swab (superfície de carcaças e superfície de facas e serras) e as amostras de água foram submetidas a análises microbiológicas de contagem de bactérias aeróbias estritas e facultativas viáveis, contagem de coliformes e ao isolamento presuntivo de enterobactérias. Os resultados foram analisados através de análise de variância, e teste de Tukey a 5% de probabilidade, e à estatística descritiva. Os resultados médios das análises microbiológicas para as carcaças antes e depois do emprego do tratamento foi, respectivamente, de 2,1x102 UFC/cm2 e 5,9x102 UFC/cm2 para aeróbios estritos e facultativos viáveis; 8,2x101 UFC/cm2 e 6,1x101 UFC/cm2 para contagem de coliformes, e 100% e 86% de presença de enterobactérias. A superfície de facas e serras obtiveram resultados médios variando de 8,6x104 a >1,3x106 UFC/utensílio para aeróbios mesófilos e de 1,7x103 a 4,3x105 UFC/utensílio para coliformes, e 100% de presença para enterobactérias. Para as amostras de água houve redução no número de microorganismos aeróbios após a cloração para 60%, 20% de presença de coliformes e 20% de presença de enterobactérias. As câmaras frigoríficas apresentaram-se contaminadas com microorganismos aeróbios mesófilos e coliformes. Os resultados do presente estudo permitiram concluir que não houve eficiência no tratamento da água pelo cloro, com condições sanitárias inadequadas para as câmaras frigoríficas e superfície de equipamentos e utensílios empregados nas operações do abate.
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Com vista a contribuir e aprimorar o processo de gestão das águas rondonienses em andamento, os resultados de análises físico-químicas e bacteriológicas das águas de rios, a partir de amostras coletadas em 64 pontos, constantes nos arquivos do 2º Zoneamento Sócioeconômico-Ecológico do Estado de Rondônia – 2º ZSEE/RO, apresentados por rio ou igarapé e município, foram tratados e reorganizados por bacia hidrográfica, através do uso de planilha eletrônica “Excel” e do software Statistica. Buscou-se a caracterização da qualidade de águas superficiais nas principais bacias hidrográficas do Estado de Rondônia, considerando propriedades físicas e organolépticas, químicas e bacteriológicas. Também foram feitas avaliação da potabilidade e do índice de qualidade de água - IQA. Com as análises foram obtidas informações descritivas e, para testar o ajuste dos dados à distribuição normal, foi utilizado o método de Shapiro-Wilk. O estudo permitiu concluir que as águas superficiais analisadas em geral excederam os padrões bacteriológicos de potabilidade, necessitando de tratamento por cloração ou fervura e prévia filtração para consumo humano.
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Com vistas a contribuir e aprimorar o processo de gestão em andamento das águas subterrâneas do Estado de Rondônia, os dados de 384 resultados de análises físico-químicas e/ou bacteriológicas de poços constantes nos arquivos do 2º Zoneamento Sócio-Econômico-Ecológico do Estado de Rondônia – ZSEE/RO, apresentados por localidades, foram tratados e reorganizados por bacia hidrográfica. Buscou-se a caracterização da qualidade de águas subterrâneas nas principais bacias hidrográficas do Estado de Rondônia, considerando propriedades físicas (cor, pH e turbidez), químicas (cloreto, ferro total, sulfato, oxigênio consumido, dureza total, dureza em cálcio, dureza em magnésio, sólidos totais, nitrogênio nitrito, nitrogênio nitrato, gás carbônico livre e alcalinidade HCO3) e bacteriológicas (contagem padrão de bactérias, número mais provável de coliformes totais, número mais provável de coliformes fecais e número mais provável de colônias - método membrana filtrante). Para testar o ajuste dos dados à distribuição normal foi utilizado o método de Kolmogorov-Smirnov, modificado por Lilliefors. O estudo demonstrou que as águas subterrâneas analisadas possuem boa qualidade físico-organoléptica. As bacias dos rios Madeira e Machado apresentam maiores alterações nos valores de pH, cloreto e nitrato, caracterizando perda de qualidade dos recursos hídricos subterrâneos, em função do adensamento populacional. A bacia hidrográfica do rio Abunã caracteriza-se como a de maior risco de contaminação fecal. Em geral, as águas analisadas apresentam resultados que excedem os padrões bacteriológicos de potabilidade, necessitando de tratamento por cloração ou fervura e prévia filtração para consumo humano.
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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)
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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)
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Pós-graduação em Engenharia Civil - FEIS
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Water disinfection usually requires expensive chemicals or equipment. Chlorination is a common disinfection method, although it is not able to inactivate all pathogens. High concentrations of residual chlorine also cause an unpleasant taste and smell in drinking water. As an alternative, photocatalysis and photoelectrochemical treatment has a high disinfection potential in drinking water by using solid catalysts, such as titanium dioxide. Highly reactive hydroxyl radical generated during the process serves as the main oxidant, capable of inactivating a wide range of microorganisms. In this study, we proposed a novel comparison between Gram-positive and gram-negative microorganisms. An immobilized TiO2 film promoted higher efficiency in water disinfection processes. The treatment effectively inactivated Escherichia coli and Staphylococcus aureus bacterial microorganisms in a shorter period than other alternative methods.
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Water quality is very important for the health and the population welfare, and the public supply system must provide water quality and suffi cient quantity for the entire population. Water treatment stations, are the main way to obtain water quality. When this doesn’t occur, several problems can affect the population, in this case, using water with poor quality is a constant risk of emergence causing various diseases. The elimination of microorganisms in treated water reduces competition, encouraging the multiplication of chlorine resistant bacteria as Mycobacterium genus frequently isolated from treated and chlorinated water. Considering the lack of indication from examinations of mycobacteria routine laboratory for quality control of drinking water and other human uses, the objective was to verify the presence isolate and identify the environmental mycobacteria in the system water source surface of Araraquara - SP. We analyzed 40 water samples, distributed as follows: ten water gross collected at Station Water Treatment Plant (WTP), harvested after ten fi ltration; ten collected in the reservoir after chlorination and ten in the network distribution. Were recovered 43 isolates of mycobacteria. All isolates were subjected to PCR-PRA. The mycobacteria were identifi ed as M. lentifl avum, M. parafortuitum, M. genavense, M. gordonae, M. fortuitum, M. confl uent, M. duvalii, M. avium subspecies paratuberculosis and M. szulgai. With these results, was concluded that water is an important source of environmental mycobacteria probably related to several human diseases, suggesting the carrying out continuous monitoring of the microorganisms in the system drinking water.
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Selective oxidation is one of the simplest functionalization methods and essentially all monomers used in manufacturing artificial fibers and plastics are obtained by catalytic oxidation processes. Formally, oxidation is considered as an increase in the oxidation number of the carbon atoms, then reactions such as dehydrogenation, ammoxidation, cyclization or chlorination are all oxidation reactions. In this field, most of processes for the synthesis of important chemicals used vanadium oxide-based catalysts. These catalytic systems are used either in the form of multicomponent mixed oxides and oxysalts, e.g., in the oxidation of n-butane (V/P/O) and of benzene (supported V/Mo/O) to maleic anhydride, or in the form of supported metal oxide, e.g., in the manufacture of phthalic anhydride by o-xylene oxidation, of sulphuric acid by oxidation of SO2, in the reduction of NOx with ammonia and in the ammoxidation of alkyl aromatics. In addition, supported vanadia catalysts have also been investigated for the oxidative dehydrogenation of alkanes to olefins , oxidation of pentane to maleic anhydride and the selective oxidation of methanol to formaldehyde or methyl formate [1]. During my PhD I focused my work on two gas phase selective oxidation reactions. The work was done at the Department of Industrial Chemistry and Materials (University of Bologna) in collaboration with Polynt SpA. Polynt is a leader company in the development, production and marketing of catalysts for gas-phase oxidation. In particular, I studied the catalytic system for n-butane oxidation to maleic anhydride (fluid bed technology) and for o-xylene oxidation to phthalic anhydride. Both reactions are catalyzed by systems based on vanadium, but catalysts are completely different. Part A is dedicated to the study of V/P/O catalyst for n-butane selective oxidation, while in the Part B the results of an investigation on TiO2-supported V2O5, catalyst for o-xylene oxidation are showed. In Part A, a general introduction about the importance of maleic anhydride, its uses, the industrial processes and the catalytic system are reported. The reaction is the only industrial direct oxidation of paraffins to a chemical intermediate. It is produced by n-butane oxidation either using fixed bed and fluid bed technology; in both cases the catalyst is the vanadyl pyrophosphate (VPP). Notwithstanding the good performances, the yield value didn’t exceed 60% and the system is continuously studied to improve activity and selectivity. The main open problem is the understanding of the real active phase working under reaction conditions. Several articles deal with the role of different crystalline and/or amorphous vanadium/phosphorous (VPO) compounds. In all cases, bulk VPP is assumed to constitute the core of the active phase, while two different hypotheses have been formulated concerning the catalytic surface. In one case the development of surface amorphous layers that play a direct role in the reaction is described, in the second case specific planes of crystalline VPP are assumed to contribute to the reaction pattern, and the redox process occurs reversibly between VPP and VOPO4. Both hypotheses are supported also by in-situ characterization techniques, but the experiments were performed with different catalysts and probably under slightly different working conditions. Due to complexity of the system, these differences could be the cause of the contradictions present in literature. Supposing that a key role could be played by P/V ratio, I prepared, characterized and tested two samples with different P/V ratio. Transformation occurring on catalytic surfaces under different conditions of temperature and gas-phase composition were studied by means of in-situ Raman spectroscopy, trying to investigate the changes that VPP undergoes during reaction. The goal is to understand which kind of compound constituting the catalyst surface is the most active and selective for butane oxidation reaction, and also which features the catalyst should possess to ensure the development of this surface (e.g. catalyst composition). On the basis of results from this study, it could be possible to project a new catalyst more active and selective with respect to the present ones. In fact, the second topic investigated is the possibility to reproduce the surface active layer of VPP onto a support. In general, supportation is a way to improve mechanical features of the catalysts and to overcome problems such as possible development of local hot spot temperatures, which could cause a decrease of selectivity at high conversion, and high costs of catalyst. In literature it is possible to find different works dealing with the development of supported catalysts, but in general intrinsic characteristics of VPP are worsened due to the chemical interaction between active phase and support. Moreover all these works deal with the supportation of VPP; on the contrary, my work is an attempt to build-up a V/P/O active layer on the surface of a zirconia support by thermal treatment of a precursor obtained by impregnation of a V5+ salt and of H3PO4. In-situ Raman analysis during the thermal treatment, as well as reactivity tests are used to investigate the parameters that may influence the generation of the active phase. Part B is devoted to the study of o-xylene oxidation of phthalic anhydride; industrially, the reaction is carried out in gas-phase using as catalysts a supported system formed by V2O5 on TiO2. The V/Ti/O system is quite complex; different vanadium species could be present on the titania surface, as a function of the vanadium content and of the titania surface area: (i) V species which is chemically bound to the support via oxo bridges (isolated V in octahedral or tetrahedral coordination, depending on the hydration degree), (ii) a polymeric species spread over titania, and (iii) bulk vanadium oxide, either amorphous or crystalline. The different species could have different catalytic properties therefore changing the relative amount of V species can be a way to optimize the catalytic performances of the system. For this reason, samples containing increasing amount of vanadium were prepared and tested in the oxidation of o-xylene, with the aim of find a correlations between V/Ti/O catalytic activity and the amount of the different vanadium species. The second part deals with the role of a gas-phase promoter. Catalytic surface can change under working conditions; the high temperatures and a different gas-phase composition could have an effect also on the formation of different V species. Furthermore, in the industrial practice, the vanadium oxide-based catalysts need the addition of gas-phase promoters in the feed stream, that although do not have a direct role in the reaction stoichiometry, when present leads to considerable improvement of catalytic performance. Starting point of my investigation is the possibility that steam, a component always present in oxidation reactions environment, could cause changes in the nature of catalytic surface under reaction conditions. For this reason, the dynamic phenomena occurring at the surface of a 7wt% V2O5 on TiO2 catalyst in the presence of steam is investigated by means of Raman spectroscopy. Moreover a correlation between the amount of the different vanadium species and catalytic performances have been searched. Finally, the role of dopants has been studied. The industrial V/Ti/O system contains several dopants; the nature and the relative amount of promoters may vary depending on catalyst supplier and on the technology employed for the process, either a single-bed or a multi-layer catalytic fixed-bed. Promoters have a quite remarkable effect on both activity and selectivity to phthalic anhydride. Their role is crucial, and the proper control of the relative amount of each component is fundamental for the process performance. Furthermore, it can not be excluded that the same promoter may play different role depending on reaction conditions (T, composition of gas phase..). The reaction network of phthalic anhydride formation is very complex and includes several parallel and consecutive reactions; for this reason a proper understanding of the role of each dopant cannot be separated from the analysis of the reaction scheme. One of the most important promoters at industrial level, which is always present in the catalytic formulations is Cs. It is known that Cs plays an important role on selectivity to phthalic anhydride, but the reasons of this phenomenon are not really clear. Therefore the effect of Cs on the reaction scheme has been investigated at two different temperature with the aim of evidencing in which step of the reaction network this promoter plays its role.
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As water quality interventions are scaled up to meet the Millennium Development Goal of halving the proportion of the population without access to safe drinking water by 2015 there has been much discussion on the merits of household- and source-level interventions. This study furthers the discussion by examining specific interventions through the use of embodied human and material energy. Embodied energy quantifies the total energy required to produce and use an intervention, including all upstream energy transactions. This model uses material quantities and prices to calculate embodied energy using national economic input/output-based models from China, the United States and Mali. Embodied energy is a measure of aggregate environmental impacts of the interventions. Human energy quantifies the caloric expenditure associated with the installation and operation of an intervention is calculated using the physical activity ratios (PARs) and basal metabolic rates (BMRs). Human energy is a measure of aggregate social impacts of an intervention. A total of four household treatment interventions – biosand filtration, chlorination, ceramic filtration and boiling – and four water source-level interventions – an improved well, a rope pump, a hand pump and a solar pump – are evaluated in the context of Mali, West Africa. Source-level interventions slightly out-perform household-level interventions in terms of having less total embodied energy. Human energy, typically assumed to be a negligible portion of total embodied energy, is shown to be significant to all eight interventions, and contributing over half of total embodied energy in four of the interventions. Traditional gender roles in Mali dictate the types of work performed by men and women. When the human energy is disaggregated by gender, it is seen that women perform over 99% of the work associated with seven of the eight interventions. This has profound implications for gender equality in the context of water quality interventions, and may justify investment in interventions that reduce human energy burdens.