324 resultados para Filtração


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The advance of drilling in deeper wells has required more thermostable materials. The use of synthetic fluids, which usually have a good chemical stability, faces the environmental constraints, besides it usually generate more discharge and require a costly disposal treatment of drilled cuttings, which are often not efficient and require mechanical components that hinder the operation. The adoption of aqueous fluids generally involves the use of chrome lignosulfonate, used as dispersant, which provides stability on rheological properties and fluid loss under high temperatures and pressures (HTHP). However, due to the environmental impact associated with the use of chrome compounds, the drilling industry needs alternatives that maintain the integrity of the property and ensure success of the operation in view of the strong influence of temperature on the viscosity of aqueous fluids and polymers used in these type fluids, often polysaccharides, passives of hydrolysis and biological degradation. Therefore, vinyl polymers were selected for this study because they have predominantly carbon chain and, in particular, polyvinylpyrrolidone (PVP) for resisting higher temperatures and partially hydrolyzed polyacrylamide (PHPA) and clay by increasing the system's viscosity. Moreover, the absence of acetal bonds reduces the sensitivity to attacks by bacteria. In order to develop an aqueous drilling fluid system for HTHP applications using PVP, HPAM and clay, as main constituents, fluid formulations were prepared and determined its rheological properties using rotary viscometer of the Fann, and volume filtrate obtained by filtration HTHP following the standard API 13B-2. The new fluid system using polyvinylpyrrolidone (PVP) with high molar weight had higher viscosities, gels and yield strength, due to the effect of flocculating clay. On the other hand, the low molecular weight PVP contributed to the formation of disperse systems with lower values in the rheological properties and fluid loss. Both systems are characterized by thermal stability gain up to around 120 ° C, keeping stable rheological parameters. The results were further corroborated through linear clay swelling tests.

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The advance of drilling in deeper wells has required more thermostable materials. The use of synthetic fluids, which usually have a good chemical stability, faces the environmental constraints, besides it usually generate more discharge and require a costly disposal treatment of drilled cuttings, which are often not efficient and require mechanical components that hinder the operation. The adoption of aqueous fluids generally involves the use of chrome lignosulfonate, used as dispersant, which provides stability on rheological properties and fluid loss under high temperatures and pressures (HTHP). However, due to the environmental impact associated with the use of chrome compounds, the drilling industry needs alternatives that maintain the integrity of the property and ensure success of the operation in view of the strong influence of temperature on the viscosity of aqueous fluids and polymers used in these type fluids, often polysaccharides, passives of hydrolysis and biological degradation. Therefore, vinyl polymers were selected for this study because they have predominantly carbon chain and, in particular, polyvinylpyrrolidone (PVP) for resisting higher temperatures and partially hydrolyzed polyacrylamide (PHPA) and clay by increasing the system's viscosity. Moreover, the absence of acetal bonds reduces the sensitivity to attacks by bacteria. In order to develop an aqueous drilling fluid system for HTHP applications using PVP, HPAM and clay, as main constituents, fluid formulations were prepared and determined its rheological properties using rotary viscometer of the Fann, and volume filtrate obtained by filtration HTHP following the standard API 13B-2. The new fluid system using polyvinylpyrrolidone (PVP) with high molar weight had higher viscosities, gels and yield strength, due to the effect of flocculating clay. On the other hand, the low molecular weight PVP contributed to the formation of disperse systems with lower values in the rheological properties and fluid loss. Both systems are characterized by thermal stability gain up to around 120 ° C, keeping stable rheological parameters. The results were further corroborated through linear clay swelling tests.

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In this work a chitosan (CS) ionically crosslinked were manufactured by treatment with sulfuric acid solution for application in the treatment of wastewater from oil industry. Two crosslinking process were developed: homogeneous and heterogeneous. In the homogeneous process the ratio molar of SO42-/ NH3+ (1:6 and 1:4) were the variable analyzed, denominated CS16 and CS14 respectively. In the heterogeneous process the soaking time of the membranes in sulfuric acid solution were the variable studied, being used times of 5 (CS5) and 30 (CS30) minutes. FTIR-ATR results indicated no changes in the characteristics of chitosan after homogeneous crosslinking process, while heterogeneous crosslinking showed formation of ionic bonds between protonated groups from chitosan and the crosslinking agent sulfate ions. TG/DTG and XRD analysis confirmed the formation of these interactions, as also shown the new structure on the surface region of CS5 and CS30 membranes compared to CS, CS16 e CS14. Swelling test in aqueous medium have shown that crosslinking process reduced the membrane sorption capacity. Swelling test in acid medium demonstrated that CS16 and CS14 membranes increasing the adsorption capacity up to a maximum percentage of 140% approximately, whereas the CS5 e CS30 reached a maximum of 60%. The mechanical properties indicated the stiff and ductile behavior of crosslinked membrane. Adsorption experiments of CuCl2 results that CS16 membranes reached the efficiency maximum with 73% of copper removal at pH 5.0 and 87% at pH 4.0. The experiments with CuSO4 also obtained efficiency maximum to the CS16 membrane and 80% to the removal of Cu2+ ions. Also was verified that the increase of concentration and temperature cause a decrease in the adsorption capacity for all membranes. Kinetics study indicated that pseudo-second-order obtained characterized better the membranes. Equilibrium studies demonstrated that the CS, CS16 and CS14 follow the Langmuir model, whereas CS5 and CS30 follows Freundlich model. Filtration experiments results with rejection maximum to the CS16 and CS5 membranes, reaching 92 and 98% respectively.

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In this work a chitosan (CS) ionically crosslinked were manufactured by treatment with sulfuric acid solution for application in the treatment of wastewater from oil industry. Two crosslinking process were developed: homogeneous and heterogeneous. In the homogeneous process the ratio molar of SO42-/ NH3+ (1:6 and 1:4) were the variable analyzed, denominated CS16 and CS14 respectively. In the heterogeneous process the soaking time of the membranes in sulfuric acid solution were the variable studied, being used times of 5 (CS5) and 30 (CS30) minutes. FTIR-ATR results indicated no changes in the characteristics of chitosan after homogeneous crosslinking process, while heterogeneous crosslinking showed formation of ionic bonds between protonated groups from chitosan and the crosslinking agent sulfate ions. TG/DTG and XRD analysis confirmed the formation of these interactions, as also shown the new structure on the surface region of CS5 and CS30 membranes compared to CS, CS16 e CS14. Swelling test in aqueous medium have shown that crosslinking process reduced the membrane sorption capacity. Swelling test in acid medium demonstrated that CS16 and CS14 membranes increasing the adsorption capacity up to a maximum percentage of 140% approximately, whereas the CS5 e CS30 reached a maximum of 60%. The mechanical properties indicated the stiff and ductile behavior of crosslinked membrane. Adsorption experiments of CuCl2 results that CS16 membranes reached the efficiency maximum with 73% of copper removal at pH 5.0 and 87% at pH 4.0. The experiments with CuSO4 also obtained efficiency maximum to the CS16 membrane and 80% to the removal of Cu2+ ions. Also was verified that the increase of concentration and temperature cause a decrease in the adsorption capacity for all membranes. Kinetics study indicated that pseudo-second-order obtained characterized better the membranes. Equilibrium studies demonstrated that the CS, CS16 and CS14 follow the Langmuir model, whereas CS5 and CS30 follows Freundlich model. Filtration experiments results with rejection maximum to the CS16 and CS5 membranes, reaching 92 and 98% respectively.

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Metabolic syndrome (MS) is defined as a set of cardiovascular risk factors including obesity, systemic high blood pressure (SHBP), changes in glucose metabolism and dyslipidemia. The prevalence of MS in renal transplant recipients (RTR) ranges from 15% to 65%, increasing the risk of cardiovascular disease (CVD) and reducing renal allograft survival in the long term. The objectives of this study were to determine the prevalence and frequency of MS in renal transplant patients according to gender and time of transplantation and to evaluate renal function in patients with and without MS. Patients and Methods: Crosssectional study conducted from August 2012 to September 2013 involving 153 renal transplant recipients. MS was defined according to the National Cholesterol Education Program (NCEP) Adult Treatment Panel III (ATP III). The sample was divided into two groups: patients with metabolic syndrome (WMS patients) and patients without metabolic syndrome (WoMS patients) and according to gender. The WMS patients were stratified into quartiles according to the renal transplantation period (RTP), and variables related to MS were analyzed for both sexes. Results: MS was diagnosed in 58.1% of the studied population, specifically in MS was found 58.4% of men and 41.6% of women (P ˂ 0.05). The male and female with MS were 48.8 ± 11.6 years old vs. 47.1 ± 12.7 years old and the time of post transplantation was 76.1 ± 76.5 months vs. 84.7 ± 65.4 months, respectively (P >0,05). When we compared the sexes in the WMS group, systolic blood pressure (SBP) was higher in men (137.0 ± 18.1 vs. 128.9 ± 13.6 mmHg, P= 0.029), while the other components of MS did not exhibit significant differences. With respect to renal function, when we compared the sexes in the WMS group, the serum creatinine (sCr) was higher in men (1.73 ± 0.69 vs. 1.31 ± 0.47 mg/dL, P= 0.0012), while the urinary protein/creatinine ratio was higher in women (0.48 ± 0.69 vs. 0.37 ± 0.48 mg/dL, P=0.0150). We found no significant difference in the estimated glomerular filtration rate (eGFR) between WMS and WoMS patients for women and men (50.6 ± 19.1 vs. 50.1 ± 18.3 mL/min/1.73 m², P=0.909). We found a significant positive association between eGFR and HDL-c levels (r=0.3371; P=0.0145) for WMS men. The MS components showed no significant differences in RTP for different interquartile ranges, except for diastolic blood pressure (DBP) in women, where there was a significant variation among the quartiles evaluated (P=0.0009). Conclusion: the prevalence of MS was similar in the different quartiles in both sexes, in relation to time post TX. There was no significant difference in eGFR in patients WMS and WoMS, in both sexes. Concluding that the MS did not vary in relation to time post transplant.

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The hydrocycloning operation has a goal to separate solid-liquid suspensions and liquid-liquid emulsions through the centrifugal force action. Hydrocyclones are equipment with reduced size and used in both clarification and thickening. This device is used in many areas, like petrochemical and minerals process, and accumulate advantages like versatility and low cost of maintenance. However, the demand to improve the process and to reduce the costs has motivated several studies of equipment optimization. The filtering hydrocyclone is a non-conventional equipment developed at FEQUI/UFU with objective to improve the hydrocycloning separation efficiency. The purpose of this study is to evaluate the operating conditions of feed concentration and underflow diameter on the performance of a filtering geometry optimized to minimization of energy costs. The filtration effect was investigated through the comparison between the performance of the Optimized Filtering Hydrocyclone (HCOF) and the Optimized Concentrator Hydrocyclone (HCO). Because of the resemblance of hydrocyclones performance, the filtration did not represent significant effect on the performance of the HCOF. It was found that in this geometry the decrease of the variable underflow diameter was very favorable to thickening operation. The suspension concentration of quartzite at 1.0% of solids in volume was increased about 42 times when the 3 mm underflow diameter was used. The increase on the feed solid percentage was good for decreasing the energy spent, so that a minimum number of Euler of 730 was achieved at CVA = 10.0%v. However, a greater amount of solids in suspension leads to a lower efficiency of the equipment. Therefore, to minimize the underflow-to-throughput ratio and keep a high efficiency level, it is indicated to work with dilute suspension (CVA = 1.0%) and 3 mm underflow diameter (η = 67%). But if it is necessary to work with high feed concentration, the use of 5 mm underflow diameter provides a rise in the efficiency. The HCO hydrocyclone was compared to the traditional family of hydrocyclones Rietema and presented advantages like higher efficiency (34% higher in average) and lower energy costs (20% lower in average). Finally, the efficiency curves and project equation have been raised for the HCO hydrocyclone each with satisfactory adjust.

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O chá é a bebida mais consumida no mundo depois da água, no entanto, é no continente Asiático que é mais consumido. Existem vários tipos diferentes de chá “descendentes” da planta Camellia sinensis. É uma bebida multifacetada e benéfica para o próprio consumidor, devido às suas propriedades organoléticas e propriedades benéficas para a saúde (presença de antioxidantes). Hoje em dia existe uma crescente procura por produtos inovadores, de elevada qualidade nutricional, nomeadamente produtos alimentares com propriedades diuréticas ou dietéticas. Por outro lado, os organismos marinhos têm-se revelado como fonte de compostos bioativos com elevado potencial. Nomeadamente as algas que têm demonstrado produzir moléculas, pelo seu metabolismo secundário, com aplicação alimentar, farmacológica, entre outras. Desta forma, o principal objetivo do trabalho foi avaliar a capacidade da alga Fucus Spiralis, uma alga edível com elevado poder antioxidante, na transferência de antioxidantes durante a preparação de uma tisana, para o desenvolvimento de uma bebida inovadora “chá de alga”. Por outro lado, este trabalho teve também como objetivo fazer uma nova tisana “variante” do chá verde alga Fucus Spiralis. De modo a estudar o melhor processo para a secagem da alga, esta foi seca através de três métodos: liofilização, em estufa e no secador Tray-drier. Para os três métodos foram avaliados vários parâmetros químicos, como a quantificação de polifenóis totais, cor, aW e teor de humidade. As análises foram realizadas logo após a secagem. Ao longo do tempo (60 dias), foi também medido a quantificação de polifenóis com a alga embalada a vácuo e sem estar embalada a vácuo. Finalmente, adicionando a alga, o chá verde e aditivos alimentares, procederam-se a três diferentes processos de conservação: esterilização, pasteurização e filtração (filtro 0,22μm). Após estes tratamentos foi realizado um estudo microbiológico, a variação de cor e a quantificação de polifenóis totais ao longo de 30 dias. O menor valor obtido de aW foi observado para a alga liofilizada. Por outro lado os menores valores de humidade foram obtidos pela secagem por liofilização e pela utilização da estufa ventilada. A realização da tisana de Fucus spiralis revelou a libertação de antioxidantes em todos os processos de secagem e para todas as concentrações testadas (0,1g; 0,5g e 1g/300mL). No entanto, a libertação de polifenóis revelou-se apenas dependente do processo de secagem para a concentração de 0,5 g/300 mL, onde a quantificação total de polifenóis foi superior para o processo de liofilização (0,246 ± 0,049 mg equivalentes de ácido gálico/mL). Este valor não apresentou diferenças estatisticamente significativas com os polifenóis quantificados para a concentração de 1g/300mL. O armazenamento da alga Fucus spiralis ao longo de 60 dias em vácuo ou na ausência de vácuo não provocaram alterações na quantificação total de polifenóis e foi independente do processo de secagem. Durante os 60 dias ocorreu uma diminuição dependente do tempo dos polifenóis libertados para a tisana de alga. Esta diminuição foi particularmente acentuada até aos 15 dias. A formulação de uma tisana com 0,5g da alga Fucus spiralis e 0,5g de chá verde revelou-se, tendencialmente, com maior concentração de polifenóis de que uma tisana com 1 g de chá verde ou 1 g. Para a tisana com 0,5g da alga Fucus spiralis e 0,5g de chá verde o processo de esterilização e pasteurização não impediram o crescimento de microrganismo ao final de 30 dias de armazenamento da tisana. Contrariamente, o processo de filtração garantiu ausência de carga bacteriana durante os 30 dias de armazenamento. Por outro lado os níveis de polifenóis diminuíram ligeiramente ao longo do tempo de armazenamento, mas de um modo independente do processo de conservação. Desta forma, as tisanas de alga (Fucus spiralis) e chá verde desenvolvidas no presente trabalho, quando liofilizadas e filtradas, apresentaram um elevado potencial antioxidante, apresentando-se como um produto inovador para a indústria alimentar.

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AIMS: Renal dysfunction is a powerful predictor of adverse outcomes in patients hospitalized for acute coronary syndrome. Three new glomerular filtration rate (GFR) estimating equations recently emerged, based on serum creatinine (CKD-EPIcreat), serum cystatin C (CKD-EPIcyst) or a combination of both (CKD-EPIcreat/cyst), and they are currently recommended to confirm the presence of renal dysfunction. Our aim was to analyse the predictive value of these new estimated GFR (eGFR) equations regarding mid-term mortality in patients with acute coronary syndrome, and compare them with the traditional Modification of Diet in Renal Disease (MDRD-4) formula. METHODS AND RESULTS: 801 patients admitted for acute coronary syndrome (age 67.3±13.3 years, 68.5% male) and followed for 23.6±9.8 months were included. For each equation, patient risk stratification was performed based on eGFR values: high-risk group (eGFR<60ml/min per 1.73m2) and low-risk group (eGFR⩾60ml/min per 1.73m2). The predictive performances of these equations were compared using area under each receiver operating characteristic curves (AUCs). Overall risk stratification improvement was assessed by the net reclassification improvement index. The incidence of the primary endpoint was 18.1%. The CKD-EPIcyst equation had the highest overall discriminate performance regarding mid-term mortality (AUC 0.782±0.20) and outperformed all other equations (ρ<0.001 in all comparisons). When compared with the MDRD-4 formula, the CKD-EPIcyst equation accurately reclassified a significant percentage of patients into more appropriate risk categories (net reclassification improvement index of 11.9% (p=0.003)). The CKD-EPIcyst equation added prognostic power to the Global Registry of Acute Coronary Events (GRACE) score in the prediction of mid-term mortality. CONCLUSION: The CKD-EPIcyst equation provides a novel and improved method for assessing the mid-term mortality risk in patients admitted for acute coronary syndrome, outperforming the most widely used formula (MDRD-4), and improving the predictive value of the GRACE score. These results reinforce the added value of cystatin C as a risk marker in these patients.

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Os Planos de Segurança da Água surgem com a necessidade de aumentar a segurança da água de abastecimento, superando a monitorização de conformidade de “fim de linha”, permitindo aumentar a confiança do consumidor na qualidade da água que lhe é fornecida. Esta nova abordagem recorre a uma metodologia de gestão baseada na identificação e no controlo de riscos em pontos críticos de um sistema de abastecimento, em complemento do controlo realizado através da monitorização da conformidade da água entregue aos consumidores. O Plano de Segurança da Água (PSA) encontra-se implementado no Sistema Regional do Carvoeiro (SRC) desde o ano de 2009. O SRC é um sistema de abastecimento de água em alta, sendo constituído por conjunto de infraestruturas de captação, tratamento, transporte e armazenamento de água desde a sua origem, localizada no rio Vouga, em Carvoeiro, até aos municípios integrados na Associação de Municípios do Carvoeiro-Vouga. Atendendo à obra de expansão do SRC, tornou-se imperativo efetuar uma revisão ao PSA, sendo este o objetivo primordial do trabalho de estágio desenvolvido na empresa Águas do Vouga S.A, concessionária responsável pela gestão do SRC. Para a prossecução deste objetivo, o trabalho desenvolvido envolveu os seguintes passos metodológicos: identificação das operações aplicadas no SRC; identificação de perigos e eventos perigosos em todos os órgãos constituintes do sistema; avaliação de riscos; identificação de pontos críticos de controlo; identificação de pontos de monitorização e medidas preventivas; elaboração do plano de monitorização, incluindo, procedimentos de controlo operacional em condições normais de funcionamento e em caso de desvio; validação deste plano. Deste trabalho resultou a identificação de 166 eventos perigosos, 17 tipologias de perigos, 3 pontos de controlo crítico e 17 pontos de monitorização. Os pontos de controlo crítico foram identificados nos processos de tratamento da ETA do Carvoeiro. O primeiro foi localizado na etapa de filtração com areia, antracite e zeólitos correspondendo aos perigos com metais (Fe e Mn), outros compostos químicos perigosos, partículas, turvação, matéria orgânica e alumínio. O segundo ponto foi identificado na etapa de filtração com filtros de carvão ativado granular relativo ao aparecimento de sabor e cianotoxinas. O terceiro ponto de controlo crítico foi encontrado na etapa de desinfeção referente aos microrganismos patogénicos. Os pontos de monitorização foram localizados ao longo do sistema em situações onde não se dispõem de nenhuma medida de controlo para eliminar o perigo e antes e após os pontos de controlo crítico. O plano de monitorização foi desenvolvido para estes pontos, embora os limites e procedimentos definidos devam ser alvo de revisão após a conclusão da obra de expansão do sistema. A validação da revisão do plano foi iniciada, mas cingiu-se apenas na avaliação preliminar de riscos, prévia ao início de operação da ETA do Carvoeiro. Para além da revisão deste plano, foram realizadas outras tarefas, nomeadamente uma análise à qualidade da água fornecida e distribuída pelo sistema, a elaboração do plano PCQA para o ano de 2016, a configuração da plataforma de gestão operacional NAVIATM e a revisão do Manual de Gestão da Águas do Vouga relativo ao processo de qualidade na captação, tratamento e distribuição e ao processo de qualidade na gestão do PSA.

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A produção de peptídeos bioativos de distintas fontes de proteínas vem ganhando espaço na produção científica e tecnológica, despertando interesse do setor empresarial. Paralelamente a isso, devido à elevada concentração de proteínas na biomassa das microalgas Spirulina e Chlorella, estas apresentam grande potencial para a extração de biocompostos com alto valor agregado, como biopeptídeos de microalgas. As proteínas são uma importante fonte de peptídeos bioativos, mas estes não estão ativos na proteína precursora e devem ser liberados para que apresentem efeitos fisiológicos desejados. Essa liberação pode ser feita através de hidrólise enzimática a partir de proteases, sendo um dos métodos mais utilizados para a produção destes biocompostos. Dentro deste contexto, vários estudos vêm mostrando o uso da tecnologia por secagem em spray dryer para a obtenção de nanopartículas que contenham compostos bioativos, sendo, essa técnica, amplamente utilizada para transformar líquidos em pós, podendo ser aplicada em materiais sensíveis à temperatura. Este estudo teve como objetivo obter peptídeos bioativos através da reação enzimática, tendo como substrato a biomassa de Spirulina sp. LEB 18 e Chlorella pyrenoidosa e, na sequência, obter nanopartículas contendo os biopeptídeos. Primeiramente, foram testadas as 3 proteases comerciais (Protemax 580 L, Protemax N 200 e pepsina) para a produção de hidrolisados proteicos de microalgas, para isso foram realizados 3 delineamentos compostos centrais para cada microalga em estudo (Chlorella e Spirulina). Os delineamentos utilizados foram do tipo 23 com três repetições no ponto central, variando-se a concentração de enzima (5 a 10 U.mL-1), a concentração de substrato (5 a 10 %) e o tempo de reação (60 a 240 min). Após, realizou-se 2 delineamentos compostos rotacionais do tipo 22 com pontos centrais, um para cada microalga, utilizando-se para a hidrólise a enzima Protemax 580L (5 U.mL-1) variando-se a concentração de substrato e tempo de reação, para todos ensaios estudou-se a solubilidade, capacidade de retenção de água, atividade antioxidante e digestibilidade. Foi selecionado um ensaio para cada microalga, levando em conta os melhores resultados. Então nova hidrólise enzimática foi realizada sendo o sistema reacional composto pela enzima Protemax 580 L (5 U.mL-1) e pela biomassa de Spirulina sp. LEB 18 ou Chlorella pyrenoidosa (4% de proteína) durante tempo de 200 min. Os hidrolisados foram purificados por filtração a vácuo com membranas millipores de diferentes tamanhos (0,45; 0,2 e 0,1 µm) e por colunas com membrana vertical Amicon® Ultra 0.5 (3K e 10K), sendo que após cada etapa, foi realizado teste de atividade antioxidante pelos métodos de poder redutor, DPPH e ABTS, a fim de verificar a permanência da atividade antioxidante. Utilizou-se nano spray dryer Büchi modelo B 90 para a secagem das amostras, sendo o tamanho das partículas obtidas analisados por microscopia eletrônica de varredura (MEV). Por fim, conclui-se que a biomassa de microalgas pode ser utilizada como fonte de produção de peptídeos bioativos com elevada atividade antioxidante e que dentre as microalgas estudadas, Spirulina sp. LEB 18 apresentou melhores resultados, em todas as análises realizadas, quando comparada com Chlorella pyrenoidosa. Esse estudo, também visou utilizar a nanobiotecnologia para obtenção de nanoparículas contendo os biopeptídeos, para tal, utilizou-se o nano Buchi Spray Dryer B-90, o qual gerou partículas nanométricas de 14 a 18 nm para o hidrolisado de Spirulina e de 72 a 108 nm para o hidrolisado de Chlorella.

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In the last decades, the effects of the air pollution have been increasing, especially in the case of the human health diseases. In order to overcome this problem, scientists have been studying the components of the air. As a part of water-soluble organic compounds, amino acids are present in the atmospheric environment as components of diverse living organisms which can be responsible for spreading diseases through the air. Liquid chromatography is one technique capable of distinguish the different amino acids from each other. In this work, aiming at separating the amino acids found in the aerosols samples collected in Aveiro, the ability of four columns (Mixed-Mode WAX-1, Mixed-Mode HILIC-1, Luna HILIC and Luna C18) to separate four amino acids (aspartic acid, lysine, glycine and tryptophan) and the way the interaction of the stationary phases of the columns with the analytes is influenced by organic solvent concentration and presence/concentration of the buffer, are being assessed. In the Mixed-Mode WAX-1 column, the chromatograms of the distinct amino acids revealed the separation was not efficient, since the retention times were very similar. In the case of lysine, in the elution with 80% (V/V) MeOH, the peaks appeared during the volume void. In the Mixed-Mode HILIC-1 column, the variation of the organic solvent concentration did not affect the elution of the four studied amino acids. Considering the Luna HILIC column, the retention times of the amino acids were too close to each other to ensure a separation among each other. Lastly, the Luna C18 column revealed to be useful to separate amino acids in a gradient mode, being the variation of the mobile phase composition in the organic solvent concentration (ACN). Luna C18 was the column used to separate the amino acids in the real samples and the mobile phase had acidified water and ACN. The gradient consisted in the following program: 0 – 2 min: 5% (V/V) ACN, 2 – 8 min: 5 – 2 % (V/V) ACN, 8 – 16 min: 2% (V/V) ACN, 16 – 20 min: 2 – 20 % (V/V) ACN, 20 – 35 min: 20 – 35 % (V/V) ACN. The aerosols samples were collected by using three passive samplers placed in two different locations in Aveiro and each sampler had two filters - one faced up and the other faced down. After the sampling, the water-soluble organic compounds was extracted by dissolution in ultra-pure water, sonication bath and filtration. The resulting filtered solutions were diluted in acidified water for the chromatographic separation. The results from liquid chromatography revealed the presence of the amino acids, although it was not possible to identify each one of them individually. The chromatograms and the fluorescence spectra showed the existence of some patterns: the samples that correspond to the up filters had more intense peaks and signals, revealing that the up filters collected more organic matter.

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-D-glucosidase (EC 3.2.1.21) is one of the most interesting glycosidases, especially for hydrolysis cellobiose releasing glucose, is last step degradation of cellulose. This function makes the -D-glucosidase is of great interest as a versatile industrial biocatalyst, being critical to various bio-treatment / biorefinery processes, such as bioethanol production. Hen in the report, a -D-glucosidase was extracts from protein extracted of the invertebrate marine Artemia franciscana was purified and characterized with a combination of precipitation with ammonium sulfate (0 - 30%, 30 to 50%, 50 to 80%), the fraction saturated in the range of 30 to 50% (called F-II) was applied in a molecular exclusion chromatography, in Sephacryl S-200, the fractions corresponding to the first peak of activity of -D-glucosidase were gathered and applied in a chromatography of ion exchange in Mono Q; the third peak this protein obtained chromatography, which coincides with the peak of activity of -D-glucosidase was held and applied in a gel filtration chromatography Superose 12 where the first peak protein, which has activity of -D-glucosidase was rechromatography on Superose 12. This enzyme is probably multimerica, consisting of three subunit molecular mass of 52.7 kDa (determined by SDS-PAGE) with native molecular mass of 157 kDa (determined by gel filtration chromatography on Superose 12 under the system FPLC). The enzyme was purified 44.09 times with a recovery of 1.01%. Using up p-nitrophenyl-β-D-glucopiranoside as substrate obtained a Km apparent of 0.229 mM and a Vmax of 1.109 mM.60min-1.mL-1mM. The optimum pH and optimum temperature of catalysis of the synthetic substrate were 5.0 and 45 °C, respectively. The activity of the -D-glucosidase was strongly, inhibited by silver nitrate and N- etylmaleimide, this inhibition indicates the involvement of radical sulfidrila the hydrolysis of synthetic substrate. The -D-glucosidase of Artemia franciscana presented degradativa action on celobiose, lactose and on the synthetic substrate -nitrophenyl-β-D-glucopiranoside indicating potential use of this enzyme in the industry mainly for the production of bioethanol (production of alcohol from the participating cellulose), and production hydrolysate milk (devoid of milk lactose)

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Four different sponge species were screened using Ouchterlony agarose gel and immunodiffusion tests to identify cross-reactivity with the polyclonal antibody IgG anti-deglicosilated CvL, a lectin from Cliona varians. Crude extract from the sponge Cinachyrella apion showed cross-reactivity and also a strong haemmaglutinating activity towards human erythrocytes of all ABO groups. Thus, it was submitted to acetone fractionation, IgG anti-deglicosilated CvL Sepharose affinity chromatography, and Fast Protein Liquid Chromatography (FPLC-AKTA) gel filtration on a Superose 6 10 300 column to purify a novel lectin. C. apion lectin (CaL) agglutinated all types of human erythrocytes with preference for papainized type A and O erythrocytes. The haemagglutinating activity is independent of Ca2+, Mg2+ and Mn2+ ions, and it was strongly inhibited by the disaccharide D-lactose, up to a minimum concentration of 6.25 mM. CaL molecular mass determined by FPLC-AKTA gel filtration on a Superose 12 10 300 column and SDS gel electrophoresis was approximately 124 kDa, consisting of eight subunits of 15.5 kDa, assembled by hydrophobic interactions. The lectin was relatively heat- and pH-stable. Leishmania chagasi romastigotes were agglutinated by CaL, indicating that lactose receptors could be presented in this parasite stage. These findings are indicative of the physiological defense roles of CaL and its possible use in the antibiosis of pathogenic protozoa

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This work studies the involved enzymatic way in the metabolism of glycosaminoglycans sulfateds in the mollusc Pomacea sp. Had been identified endoglycosidases and exoglycosidases in the enzymatic extract of the mollusc Pomacea sp by means of hydrolysis activity in condroitim sulphate of whale cartilage and of the p-Nitrofenil-β-glucuronide, respectively. The enzymatic extracts qere obtained of Pomacea sp. being used of 0.1 sodium acetate buffer, pH 5.0 and later centrifugated the 8,000 x g and the presents proteins in the sobrenadante were submitted to the fractionament with two crescents ammonium sulphate concentrations, the visualized activity biggest in the F2 fraction (50-80%). The β-glucuronidase (F3) was isolated in gel chromatography filtration Biogel 1.5m, the purification degree was ratified in Chromatography Liquid of high efficiency (HPLC). The enzyme was purificated 6.362,5 times with 35,6% yield. The β -glucuronidase isolated in this work showed a molecular mass of 100 kDa, determined for eletroforese in poliacrilamida gel . The determination of the ideal kinetic parameters for the catalysis of the p-nitrofenil- β -glucuronide for β-glucuronidase, showed excellent activity in pH 5,0 and temperature 65ºC for 6 hours and apparent Km of 72 x 10-2 mM. It is necessary for the total degradation of 3mM of p-N-β-glucoronide, the amount of 1,2μg of ss-glucuronidase. The BaCl2 increased the activity of ss-glucuronidase, and the activity was inhibited completely by the composites SDS and NaH2PO4

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Atualmente há uma crescente preocupação quanto à qualidade dos recursos hídricos, e essa notória inquietação se deve em parte ao aumento na demanda e consumo de água a nível global, uma vez que o crescimento econômico, juntamente com o desenvolvimento tecnológico, agrícola e industrial conduz a poluição ambiental. Neste contexto, os agrotóxicos, apresentam um alto fator de risco para a qualidade dos recursos hídricos, pois essas substâncias geralmente são tóxicas e não biodegradáveis. Diante deste cenário, um dos maiores desafios nos dias atuais é a eliminação de uma parte significativa, dessa poluição, a qual é causada por esses contaminantes orgânicos tóxicos. O processo clássico de oxidação biológica falha na eliminação de compostos tóxicos, bem como de contaminantes orgânicos recalcitrantes. Além disso, os processos físico-químicos, como a adsorção em carvão ativado, floculação, e a filtração por membranas, apenas transferem esses contaminantes de fase, sem que ocorra a sua destruição. Sendo assim, surge a necessidade da adoção de técnicas que possam ser destrutivas a essas espécies. Os Processos Oxidativos Avançados, surgem como um caminho alternativo para diminuir e eliminar os resíduos desses contaminantes orgânicos. Por tanto, tiveram-se como objetivos neste trabalho: (i) desenvolver e otimizar um processo Fenton empregando ferro zero e peróxido de hidrogênio (Fe0 /H2O2) (ii) utilizar como fonte de ferro zero para o processo Fenton limalha de ferro, a qual é um resíduo da atividade metalúrgica na cidade de Rio Grande (iii) otimizar o tempo de reação (TR) e tempo de homogeneização (TH) para a Fotocatálise Heterogênea empregando um catalisador de sílica dopada com dióxido de titânio e dicloreto de tris (2,2-bipiridina) rutênio II (iv) desenvolver um método cromatográfico empregando LC-DAD para realizar o monitoramento da degradação dos agrotóxicos (v) empregar a LC-MS/MS para confirmar a degradação dos agrotóxicos e monitorar a formação de produtos (vi) empregar IC para monitorar a formação de espécies iônicas (vii) realizar a determinação de COT para estimar a mineralização do carbono orgânico dissolvido. Para tanto, um total de seis agrotóxicos foram selecionados para a o estudo de degradação: bentazona, carbofurano, clomazona, diurom, tebuconazole e piraclostrobina. O sistema Fe0 /H2O2 desenvolvido para a degradação dos agrotóxicos mostrou ser eficiente. A eficiência de degradação foi fortemente afetada pelo pH, massa de limalha de ferro e concentração de peróxido de hidrogênio. As melhores condições para a degradação foram: pH 2,0, 5 mmol L-1 H2O2 e 2,0 g de limalha de ferro. No tempo total de 20 min o carbono orgânico total foi reduzido levando a mineralização de 55%, com taxas de degradação que variaram de 51 a 100%. A utilização de recirculação no sistema Fe0 /H2O2 elevou a taxa de degradação dos agrotóxicos bentazona e carbofurano. As taxas variaram de 93 a 100% de degradação, com um tempo total de reação de 120 min, chegando a 63% de mineralização. O sistema TiO2/UV também mostrou-se adequado a degradação dos agrotóxicos. As condições ótimas foram 20 mg de catalisador, pH 7, TH de 15 min e TR de 110 min. O sistema apresentou taxas de degradação que variaram de 71 a 99,98%. Levando a mineralização de 97,60% da demanda de carbono orgânico.