996 resultados para Diesel. Remoção de enxofre. Adsorção. Vermiculita. Tensoativos. Microemulsão
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Pós-graduação em Odontologia Restauradora - ICT
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
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Pós-graduação em Aquicultura - FCAV
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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)
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A remoção da smear layer é um procedimento importante para a regeneração periodontal e para o tratamento da sensibilidade dentinária. Diversos tratamentos tem sido realizados para sua remoção, porém, mostrando resultados conflitantes ou insatisfatórios. No presente estudo nos propomos a analisar através do microscópio eletrônico de varredura a eficiência dos detergentes: lauril sulfato de sódio, Plax e de mamona assim como o EDTA 24% na remoção da smear layer. Todos os produtos testados foram aplicados com bolinha de algodão, renovada a cada 30 segundos, a qual era esfregada na superfície radicular por diferentes períodos. As fotomicrografias foram analisadas através da aplicação de um índice de remoção da smear layer por três examinadores calibrados e os resultados analisados estatisticamente. De acordo com nossos resultados pudemos chegar as seguintes conclusões: 1- a instrumentação com curetas de Gracey provocou a formação da smear layer; 2- o detergente lauril sulfato de sódio não removeu a smear layer, tendo sido o pior resultado entre os detergentes testados; 3- Os detergentes Plax e de mamona mostraram resultados semelhantes entre si e superiores ao controle negativo e ao lauril sulfato de sódio, porém, não removeram a smear layer satisfatoriamente; 4- O EDTA 24% neutro mostrou ser eficiente para a remoção da smear layer.
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In materials science, the search for technological improvements have become one of the main subject of study of researchers. This is especially true in the case of materials with reduced sizes, in the nanometer scale. Important phenomena to be studied in these cases are the desorption and adsorption on two-dimensional materials, such as graphene. These phenomena are of great importance in the study of interactions between organic films, synthesis or catalysis of reactions on surfaces and even in the creation of nanoscale devices [1, 2, 3, 4]. Between the most important topics related to these phenomena are the storage of gases in low-dimensional systems and the study of nanostructured fuel cells or batteries. In this context we used two different parametrizations for the reactive force field ReaxFF to study the potential barriers and reaction barriers of our system. First we made a study about the Reaction Barriers and Energy Barriers for bonds between graphene and the following atoms: sulfur, fluorine, hydrogen, nitrogen and oxygen. It is important to have this information in order to make it possible to understand how these atoms react with the graphene sheet. Subsequently, we calculate reaction barriers for mixed structures where fluorine is a fixed element bonded to graphene and other element is simultaneously bonded to graphene. This other element (N, O, H or S) is varied in its possible relative positions (ortho, meta and para in relation to fluorine in either: the same side and in the opposite side of the graphene membrane)
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The lubricant oil used in engines of internal combustion must be, periodically, changed. Its mainly function in the engines is to reduce the friction between the pieces, but its presence also promotes the cleanness and the refrigeration of the equipment. These attributions, at the end of some cycles of operation, make the oil to be dirty, that is, full of contaminating substances such as water, gasoline, diesel, additives, oxidized hydro-carbons and rests of metals, not being recommended, therefore, its discarding in the environment. Thus, all the used lubricant oil that leaves the automobiles engine has been thrust, waiting for a solution. The pollution generated by the discarding of a ton of used oil per day in the soil or in the rivers is equivalent to a domestic sewer of 40 thousand of people. The indiscriminate burning of the used lubricant oil generates significant emissions of metallic oxides, besides other toxic gases, like the dioxin and sulphur oxides. In this context, the mean objective of this essay was to effectuate the rerrefine of the used lubricant oil, aiming the increase of its life cycle and consequently contributing for the reduction of the environmental pollution. According to the used process, it was possible to get a rerrefine oil, of good quality, which physicistchemistries properties are in compliance with the norms of NBR and ASTM
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This paper presents a study of the applicability of adsorption isotherms, known as Langmuir and Freundlich isotherm, between the biosorptive interaction of yeast lyophilized Saccharomyces cerevisiae and textile dyes. To that end, we prepared stock solutions of the textile dyes Direct Red 23 and Direct Red 75 in the concentration of 1.000μg/mL and a yeast suspension at 2,5%. We did experiments for two cases, firstly for the case that we have a fix concentration of yeast at 0,500mg/mL and an variable concentration of dye range from40, 50, 60, 80 and 100μg/mL, then for the case that we fixed the concentration of dye at 100μg/mL and the yeast concentration was variable range from 0,250, 0,500, 0,750, 1,000, 1,250mg/mL. For the dye Direct Red 23 we did analysis in the pH 2,5, 4,5 and 6,5; for the Direct Red 75, we just did for the pH 2,5. We leave the dye solution in contact with the yeast for 2 hours at a constant temperature of 30°C and then centrifuged and analyzed the sample in a spectrophotometer and finally made and analysis of parameters for the removal and study of the isotherms. After the biosorption, was observed that for the Direct Red 23 in the pH 2,5 was needed 1,407mg/mL of yeast for total removal, while for the pH 4,5 was needed 8,806mg/mL and in pH 6,5 was 9,286mg/mL; for the Direct Red 75 in pH 2,5 was needed 1,337mg/mL. This difference can be explain by the adsorption isotherms, was observed that in the case when the yeast was fix when we had in a acid pH the behavior of the system was compatible with the Langmuir isotherm, and thus, an monolayer pattern. And that when we decrease the acidity of the medium the system became more compatible with a Freundlich isotherm, and thus, a multilayer pattern; for the case that the yeast was variable this is not much evident, however for the pH 2,5 she became compatible with a Langmuir isotherm... (Complete abstract click electronic access below)
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The globalization is each day more aggressive and demanding even more that new products be manufactured and therefore be delivered to many places in the globe. Thus, an efficient and vigorous transport system is demanded. There are many ways to transport a product, but one of the most used in the world is shipping. A marine vessel presents diversified structures of size and functions. In order to this system has more efficiency, alternatives should be used to obtain important energy savings. Usually, a vessel present a propulsion system purely mechanical, therefore the use of alternatives propulsions, like diesel-electric, is increasing. This graduation work has as main focus demonstrate the functioning of a diesel-electric propulsion system, since the main characteristics of each component of the system, likewise the analysis and electrical calculation, showing the advantages in relation to the conventional diesel propulsion system
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A zidovudina (AZT) é um antirretroviral que apresenta baixa biodisponibilidade devido seu intenso metabolismo pré2sistêmico. A via nasal tem sido estudada como alternativa para evitar este efeito, mas possui limitações, como os mecanismos de depuração mucociliar, que podem ser minimizadas através do desenvolvimento de sistemas de liberação mucoadesivos. O presente estudo tem por objetivo caracterizar sistemas tensoativos visando o desenvolvimento de uma formulação mucoadesiva para potencial administração nasal de AZT. Para isso, foi utilizada uma microemulsão (ME) composta por álcool cetílico etoxilado 20 OE e propoxilado 5 OP (PRO), ácido oleico (AO) e água. Foi testada a incorporação de polímeros mucoadesivos – policarbofil (PF), carbopol 971 (C971), 974 (C974) e quitosana (QS) na ME. Os sistemas foram caracterizados por microscopia de luz polarizada (MLP), quantificação do AZT, reologia de fluxo e oscilatória, análise do perfil de textura (TPA) e obtenção da força de mucoadesão. Os resultados mostraram que foi possível incorporar 0,1 % (p/v) dos polímeros e os sistemas incorporaram mais AZT do que a solução aquosa. Os sistemas apresentam fluxo newtoniano. Quando misturados ao muco artificial (MA), os sistemas tiveram G’ aumentado e houve mudança da ME para fase hexagonal. No teste TPA, a dureza da ME contendo PF foi a maior. Pode2se concluir que é possível obter uma formulação precursora de matriz com características de textura e reologia favoráveis à aplicação nasal. O sistema foi capaz de incorporar o AZT e apresentou grande potencial mucoadesivo. Esta estratégia se mostra promissora na melhora da terapia... (Resumo completo, clicar acesso eletrônico abaixo)
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The volume of liquid effluent generated in cattle slaughterhouses is quite high and cannot be released untreated in water bodies due to its high pollution load of predominantly organic origin. To minimize the environmental impacts of its industrial wastewater and meet the local environmental legislation, abattoirs shall make the treatment of these effluents. The present work aims to develop the study of a reactor by sequential batch pilot scale, in order to optimize their performance in treating wastewater from a cattle slaughterhouse. The treatment system used was developed and installed in the Laboratory of Wastewater Treatment, in Faculty of Science and Technology UNESP, Presidente Prudente campus. The procedure used followed the operation of sequential batch reactors, in which all processes and treatment operations occurring sequentially in a single unit, by establishing specific operating cycles, which comprise the following separated phases: aerobic reaction, anoxic reaction, sedimentation and emptying. Aiming to improve the quality of treatment was planned the addition of coagulant Poly Aluminum Chloride (PAC) in the reactor, by determining their optimal dosage by Jar-test trials. Were prepared four steps with specific operating cycles: step one or acclimatization (10 hour of aeration, one hour and 30 minutes of sedimentation and 30 minutes for exchanging the effluent); step 2 (6 hours of aeration or aerobic phase, 4 hours and 45 minutes of stirring or anoxic phase and 1 hour and 15 minutes for sedimentation and exchange effluent); step 3 (2 hours and 30 minutes of aeration, 8 hours and 15 minutes of stirring and 1 hour and 15 minutes for sedimentation and exchange) and step 4 (2 hours of aeration, 8 hours and 45 minutes of stirring and 1 hour and 15 minutes for sedimentation and exchange)... (Complete abstract click electronic access below)
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O objetivo do presente estudo foi verificar o efeito da adição de um prebiótico nas características de crescimento, resistência às condições do trato gastrintestinal e remoção de colesterol in vitro, das cepas de Enterococcus faecium CRL183 e Lactobacillus helveticus 416. A fonte de prebiótico foi composta por Inulina GR – Orafti, sendo testadas as seguintes concentrações: 1,0%, 2,0%, 3,0%; 4,0%; 5,0% e 6,0% p/v). Para a avaliação da resistência às condições do trato gastrintestinal, os microrganismos foram colocados em contato com um fluido gástrico simulado por 2 horas (9g/L de NaCl, 3g/L de pepsina, pH 1,8) e com um fluido intestinal simulado por 3 horas (0,9g/L de pancreatina, 12,5g/L de bicarbonato de sódio e 6,0 g/L de Oxgall). Após o período de contato com os fluidos, foram realizadas diluições seriais e plaqueamento em meios específicos. No estudo de redução de colesterol, meios de cultura contendo inulina e colesterol (1%) foram inoculados com as cepas probióticas e incubados em anaerobiose a 37°C/24h. A capacidade de redução do colesterol foi determinada pela diferença entre a concentração de colesterol adicionada ao meio de cultura e a de colesterol residual. Os resultados foram submetidos à análise de variância e teste de médias de Tukey (p≤0,05). A adição de inulina não resultou em alteração no ciclo logarítmico de crescimento dos microrganismos. Porém, quando os dados foram submetidos à análise estatística, constatou-se que a adição de 1% a 4% de inulina inibiu o crescimento de Lactobacillus helveticus 416, sendo que para as concentrações de 5% a 6% estas alterações não foram perceptíveis. A cepa de Enterococcus faecium CRL 183 apresentou crescimento superior na presença de 2% e 4% de inulina. Após o contato com o fluido gástrico simulado, observou-se redução de 1 ciclo logarítmico no crescimento da cepa... (Resumo completo, clicar acesso eletrônico abaixo)