903 resultados para Anaerobic sequential batch reactor


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Female albino rats were used for the sequential histopathological study of experimental paracoccidioidomycosis. The animals were inoculated intraperitoneally with a strain of Paracoccidioides brasiliensis in the yeast-like phase, and sacrificed at given intervals from 1 to 168 days after inoculation; each animal received an inoculum of 4 x 10(6) cells in 0.8 ml of saline. The control group received saline containing scrapings of the culture medium. Tissue from the inoculation site was examined. The cellular population, the extracellular matrix, and the presence and characteristics of fungi were analysed in the inflammatory granulomatous process by light microscopy. The results allowed to separate the kinetic of the inflammatory response into three stages: 1) neutrophilic or macrophagic-neutrophilic; 2) pre-granulomatous; 3) granulomatous. Synthesis of the extracellular matrix began with the depositing of fibrin-like material, and increased gradually with deposits of collagen, proteoglycans, and glycoproteins. Parasites were present in all of the examined periods. Recurrences of the disease were clearly shown through the concurrence of recently-formed granulomas with older granulomas, implying that this type of granulomatous process does not eliminate the disease, nor is it able to limit fungal dissemination over a prolonged period of time.

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Desulfovibrio desulfuricans was the first species of a sulphatereducing bacterium to be isolated, in 1895. Since that time, many questions were raised in the scientific community regarding the metabolic and ecological aspects of these bacteria. At present, there is still a myriad of open questions remaining to be answered to enlarge our knowledge of the metabolic pathways operative in these bacteria that have implications in the sulfur cycle, in biocorrosion, namely in sewers and in oil and gas systems, and in bioremediation of several toxic metals. The work presented in this dissertation aimed at contributing with new insights of enzymes involved in two different metabolic systems on Desulfovibrio species, namely enzymes that play a role in the response to oxidative stress and that are involved in the haem biosynthetic pathway.(...)

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Human mesenchymal stem/stromal cells (MSCs) have received considerable attention in the field of cell-based therapies due to their high differentiation potential and ability to modulate immune responses. However, since these cells can only be isolated in very low quantities, successful realization of these therapies requires MSCs ex-vivo expansion to achieve relevant cell doses. The metabolic activity is one of the parameters often monitored during MSCs cultivation by using expensive multi-analytical methods, some of them time-consuming. The present work evaluates the use of mid-infrared (MIR) spectroscopy, through rapid and economic high-throughput analyses associated to multivariate data analysis, to monitor three different MSCs cultivation runs conducted in spinner flasks, under xeno-free culture conditions, which differ in the type of microcarriers used and the culture feeding strategy applied. After evaluating diverse spectral preprocessing techniques, the optimized partial least square (PLS) regression models based on the MIR spectra to estimate the glucose, lactate and ammonia concentrations yielded high coefficients of determination (R2 ≥ 0.98, ≥0.98, and ≥0.94, respectively) and low prediction errors (RMSECV ≤ 4.7%, ≤4.4% and ≤5.7%, respectively). Besides PLS models valid for specific expansion protocols, a robust model simultaneously valid for the three processes was also built for predicting glucose, lactate and ammonia, yielding a R2 of 0.95, 0.97 and 0.86, and a RMSECV of 0.33, 0.57, and 0.09 mM, respectively. Therefore, MIR spectroscopy combined with multivariate data analysis represents a promising tool for both optimization and control of MSCs expansion processes.

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Dissertação para obtenção do Grau de Mestre em Engenharia Informática

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We consider two Cournot firms, one located in the home country and the other in the foreign country, producing substitute goods for consumption in a third country. We suppose that neither the home government nor the foreign firm know the costs of the home firm, while the foreign firm cost is common knowledge. We determine the separating sequential equilibrium outputs.

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Schistosomiasis constitutes a major public health problem, with an estimated 200 million individuals infected worldwide and 700 million people living in risk areas. In Brazil there are areas of high, medium and low endemicity. Studies have shown that in endemic areas with a low prevalence of Schistosoma infection the sensitivity of parasitological methods is clearly reduced. Consequently diagnosis is often impeded due to the presence of false-negative results. The aim of this study is to present the PCR reamplification (Re-PCR) protocol for the detection of Schistosoma mansoni in samples with low parasite load (with less than 100 eggs per gram (epg) of feces). Three methods were used for the lysis of the envelopes of the S. mansoni eggs and two techniques of DNA extraction were carried out. Extracted DNA was quantified, and the results suggested that the extraction technique, which mixed glass beads with a guanidine isothiocyanate/phenol/chloroform (GT) solution, produced good results. PCR reamplification was conducted and detection sensitivity was found to be five eggs per 500 mg of artificially marked feces. The results achieved using these methods suggest that they are potentially viable for the detection of Schistosoma infection with low parasite load.

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Dissertação para obtenção do Grau de Mestre em Engenharia Química e Bioquímica

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Dissertação para obtenção do Grau de Mestre em Engenharia Química e Bioquímica

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Dissertação para obtenção do Grau de Mestre em Engenharia do Ambiente, perfil de Engenharia Sanitária

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Dissertação para obtenção do Grau de Mestre em Engenharia Química e Bioquímica

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Dissertation for the Master degree in Biotechnology

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Dissertação para obtenção do Grau de Mestre em Engenharia Química e Bioquímica

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Phycoremediation of swine wastewaters has been widely reported as an attractive tertiary treatment system, that effectively removes the excessive nutrient loadswhilst offering a valuable source of feedstock biomass. Digestate from an upflow anaerobic sludge blanket (UASB, 6%v/v) and a nitrification reactor (NR; 50% v/v) were used as culturing media to microalgae. Experiments were carried out in lab scale photobioreactors (PBRs) using a consortia of Chlorella and Scenedesmus. Ammonia (44 to 90%) and phosphorus (77%) were efficiently removed from both effluents tested after 4 days. Microalgae biomass harvested from the UASB effluent showed 57, 34 and 1% of proteins, carbohydrates and lipids, respectively. Comparatively, the cellular composition of microalgae grown on NR effluent had lower protein (43%) but higher carbohydrate (42%) contents. Negligible difference in lipid fraction was observed independently of the effluents tested. The results suggest that the biomass harvested from phycoremediation of swine wastewaters can offer a valuable protein and carbohydrate feedstock for nutritional and biotechnological applications.

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Energy conservation in chemotrophic anaerobic bacteria is achieved by two possible processes, substrate level phosphorylation (SLP) and electron transfer phosphorylation (ETP). This second mechanism, also known as respiration, involves chemiosmotic coupling. However, a third mechanism for energy coupling was recently proposed: the flavin-based electron bifurcation (FBEB). (...)

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O presente trabalho tem como objectivo contribuir para o estudo do desenvolvimento de um modelo matemático aplicado à digestão anaeróbia de resíduos sólidos, que incorpore os condicionamentos da geometria dos reactores e a sua influência na cinética do processo biológico. Nesse sentido, o trabalho propõe-se avaliar o comportamento cinético de três reactores, com o mesmo volume mas com diferentes relações tridimensionais, utilizando o mesmo substrato, e idênticos parâmetros ambientais e operacionais de funcionamento. Pretendeu-se estudar em que medida a relação do comprimento, largura e altura de um reactor pode interferir nas taxas de remoção de substrato, condicionando a respectiva difusão na biomassa e crescimento dos microrganismos. Considera-se que este aspecto é do maior interesse para o desenvolvimento de um modelo cinético, podendo minimizar desvios inerentes à própria modelação de processos biológicos complexos. A geometria do reactor, que se correlaciona com uma determinada relação tridimensional, pode constituir um parâmetro importante, que se designou por Kcig (Constante de Inibição Geométrica), dada a influência que poderá exercer na cinética do processo biológico. A sua avaliação, parametrização e consequente modelação, deverá facilitar a escolha da relação comprimento/largura/altura mais adequada, de forma a optimizar o funcionamento operacional do reactor. O plano experimental desenvolveu-se em duas fases, utilizando-se dois substratos com graus distintos de dificuldade de utilização pelos microrganismos, nomeadamente: Fase 1 (glucose), Fase 2 (FORSU e relva). Concluiu-se que a cinética do processo é influenciada pela relação entre as áreas de separação de biogás/biomassa (As) e de contacto biomassa/reactor (Ac), que interferem na geometria do reactor. Assim, através dos resultados das fases 1 e 2 pode observar-se que a variação da taxa de remoção de substrato se aproxima de uma função de saturação, pelo que se propõe uma adaptação do modelo de Monod, através de um formalismo que incorpora uma grandeza adimensional, Kcig, para reflectir o efeito da geometria do reactor. Verificou-se que a equação adoptada para Kcig se mostrou adequada, o que permitiu, através do modelo de Monod ajustado, estimar os valores de rx máx e Ks que se admite estarem mais próximos dos verdadeiros, embora se considere que apenas se pretende corrigi-los em função do efeito da geometria do reactor. Por outro lado, o estudo permitiu identificar um valor de Kcig para o reactor de 2,5 L, a partir do qual poderá não ser interessante a relação entre a taxa de remoção de substrato e a área de construção do reactor.