160 resultados para Peneira rotativa


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Curso de Tecnologia Sucroalcooleira. Disciplina de Tecnologia de Produção de Açúcar. Ilustração. Dimensão: 1672x980. Tamanho: 215Kb.

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[ES] En el presente trabajo, se ha tratado de recoger la información relevante sobre el proceso de soldadura por fricción rotativa aplicado a la automoción, desde la experiencia adquirida por el autor en GKN Driveline Zumaia. En los primeros capítulos, se explica el proceso de soldadura desde diferentes enfoques y se describe brevemente la planta de fabricación GKN Driveline Zumaia y su producto fabricado mediante este proceso de soldadura. En los siguientes capítulos las tres principales fases del ciclo de soldadura con los parámetros que lo gestionan. Finalmente en los últimos y siguiendo el flujo del proceso de fabricación, se exponen otros tres capítulos que tienen que ver con este proceso de soldadura por fricción rotativa: Materia prima, máquina y ensayos no destructivos.

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Curso de Tecnologia Sucroalcooleira. Disciplina de Tecnologia de Produção de Açúcar. Ilustração. Dimensão: 4052x2289. Tamanho: 481Kb.

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Avaliou-se o comportamento de ovinos em pastagem de capim-tanzânia irrigado sob suplementação (0,0; 0,6; 1,2 e 1,8% PV) com concentrado. O delineamento utilizado foi o inteiramente casualizado com seis repetições (ovinos). A porcentagem do tempo total sob o sombrite, pastejando, ruminando, em outras atividades, em ócio, o número de ingestões de suplemento/sal, de defecações, de micções e de ingestão de água e a taxa de bocado foram estimados dividindo-se o dia em oito períodos de 3 horas (das 5 às 8 h; 8 às 11 h; 11 às 14 h; 14 às 17 h; 17 às 20 h; 20 às 23 h; 23 às 2 h; 2 às 5 h). O tempo de pastejo foi maior entre os animais que não receberam suplementação e decresceu progressivamente, voltando a elevar somente com 1,8% de suplementação. O tempo de ruminação foi maior nos animais com suplementação de 0,6% PV, principalmente das 14 às 17 h e das 17 às 20 h, enquanto o tempo de ócio foi maior no nível de 1,2% PV. A ingestão de água elevou-se com o aumento da suplementação até 1,2% PV e concentrou-se entre 11 e 14 h. O número de micções e de defecações foi maior com suplementação no nível de 1,8% PV. A elevação progressiva na taxa de bocado até o nível de suplementação de 1,2% PV no período das 11 às 20 h com posterior redução sugere efeito aditivo do suplemento sobre o pasto até esse nível, no qual se inicia efeito substitutivo. O tempo sob o sombrite concentrou-se no período das 8 às 14 h e reduziu com a suplementação até 1,2% PV. A suplementação afeta o comportamento ingestivo de ovinos em pastejo, uma vez que, no nível de 1,2% PV, houve otimização da capacidade ingestiva dos animais. Níveis superiores de suplementação comprometem o comportamento ingestivo, por isso, são necessárias alterações na formulação do suplemento quando utilizados níveis mais elevados.

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The catalytic cracking of triglycerides presents itself as a possible alternative to the production of biofuels with low emission of pollutants. In this work were synthesized the SAPO-5, the catalysts for the cracking reaction of soybean oil is presented. The solids were powder X-ray diffraction (XRD), thermogravimetric analysis (TG/DTG) and infrared spectroscopy (FTIR). The analyses indicated that the synthesis method has employed to obtain materials with high surface area and high acid. The soybean oil thermal and thermal catalytic cracking, realized from the room temperature to 450 ºC in a simple distillation system, has allowed obtaining two liquid fractions, each consisting of two phases, one aqueous and another organic, organic liquid (OL). The OL obtained from first fractions has shown high acid index, even in the thermal catalytic process. The products obtained in the cracking of soybean oil were analyzed by distillation, acid number, infra-red spectroscopy, density, viscosity, carbon residue, cetane number determination and characterization. The analysis of the products obtained in the presence and in the absence of the SAPO-5 permitted to conclude that all the solids tested presented catalytic activity in the deoxygenation of final products only at the second step of the cracking process

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Mesoporous molecular sieves of MCM-41 type are considered as promising support for metal in the refining processes of petroleum-based materials as catalysts and adsorbents for environmental protection. In this work, mesoporous molecular sieves MCM-41 were modified with different rare earth ions (La, Eu e Yb) for the obtaining nanostrutured materials with catalytic properties. The catalysts were synthesized by the hydrothermal method at 100oC for 120 h, presenting, all the samples, in the gel of synthesis molar ratio Si/Ln = 50. The obtained materials after calcination at 500oC for 2 h were characterized by XRD, surface area BET, TG/DTG, FTIR, and hydrothermal stability at 700ºC. The XRD analysis of the catalysts indicated that the materials containing rare earth presented characteristic hexagonal structure of the mesoporous materials of the type MCM-41. The TG curves showed that the decomposition of the structural template occurs in the materials at temperatures lower than 500oC. The samples presented variations as the specific superficial area, average diameter of pores and thickness of the silica wall, as a function of the nature of the rare earth impregnated in the mesoporous material. Hydrotermal stability was evaluated through the exposition of the materials to water vapour at 700°C. The thiophene adsorptions reach a maximum at 80% of conversion and incorporation of the rare earths showed influence in the process. Adsorption capacity followed the sequence: Yb-MCM-41 < La-MCM-41 < Eu-MCM-41 < MCM-41

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The nanostructured molecular sieve SBA-15 was synthesized by the hydrothermal method, and modified with lanthanum with Si/La molar ratios of 25, 50, 75 and 100. The materials were evaluated as catalysts for the cracking of n-hexane model reaction. Type SBA- 15 and LaSBA-15 mesoporous materials were synthesized using tetraetilortosilicato as a source of silica, hydrochloric acid, heptahydrate lanthanum chloride and distilled water. Pluronic P123 triblock. polymer was used as structure template. The syntheses were carried out by 72 hours. The obtained SBA-15 samples were previously analyzed by thermogravimetry, in order to check the conditions of calcination for removal of organic template. Then, the calcined materials were characterized by X-ray diffraction, infrared spectroscopy, adsorption and desorption of nitrogen, scanning electron microscopy and X-ray microanalysis by dispersive energy. The acidity of the samples was determined using adsorption of n-bulinamina and desorption followed by thermogravimetry. It was found that the hydrothermal synthesis method was suitable for the synthesis of the SBA-15 mesoporous materials, with an excellent degree of hexagonal ordering. The reactions of catalytic cracking of n-hexane were carried out using a fixed bed continuous flow microreactor, coupled on-line to a gas chromatograph. From the catalytic evaluation, it was observed that the mesoporous materials containing lanthanum showed different results for the reaction of cracking of nhexane compared to the unmodified mesoporous material SBA-15. As a result of cracking was obtained as main products hydrocarbons in the range of C1 to C5. The catalyst that showed better properties in relation to the acidity and catalytic activity was LaSBA-15 with the ratio Si/La = 50

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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

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