936 resultados para Carbeto de nióbio. Aço ferrítico 15Kh2MFA. Metalurgia do pó.Moagem de alta energia e materiais compósitos


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El objetivo de este trabajo, es el de implementar un módulo autoformativo para facilitar el proceso de aprendizaje de la asignatura Metalurgia y soldadura del Instituto Técnico Central. Antes de entrar en detalle sobre el tema, se exponen teorías

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Exposición de los métodos más comunes utilizados en la metalurgia extractiva para obtener de un mineral compuesto el material que nos interesa. Entre los procesos de extracción, uno de los más comunes es el de reducción, que puede ser de varios tipos, como la reducción por carbón, por hidrógeno o la aluminotermia, entre otros.

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A busca de uma maior competitividade tem levado a indústria a utilizar temperaturas de cementação cada vez mais elevadas. Este aumento na temperatura permite uma significativa diminuição dos tempos de tratamentos, porém pode levar a um aumento generalizado ou anormal do tamanho de grão austenítico bastante deletério as propriedades mecânicas do material. A utilização de elementos formadores de precipitados é uma alternativa para minimizar este problema. Neste trabalho foi estudado um aço SAE 5115 com adição de 0,038% em peso nióbio para ancoramento de grão. Para este estudo foi simulado um tratamento térmico de cementação em temperaturas mais elevadas, como 1000 e 1050°C, por duas horas, partindo-se de duas condições, bruto de laminação e esferoidizado. A técnica de microscopia eletrônica de transmissão (MET) foi empregada para caracterizar os precipitados, bem como avaliar sua contribuição no ancoramento do grão. A caracterização dos precipitados quanto sua composição, morfologia, tamanho e distribuição, foi realizada analisando-se amostras preparadas por extração de réplicas em filme de carbono e por lâminas finas pelo método de polimento plano no “Tripod Polisher”. Sendo que este último, convencionalmente não utilizado em aço, possibilita a obtenção de amostras com extensa área fina para observação no MET, além de facilitar a análise por minimizar o efeito de desvio de feixe em amostras magnéticas. Os resultados das análises comprovam a precipitação de partículas complexas de Nb e que a forma de distribuição, bem como o percentual de tamanho dos precipitados é de suma importância para o ancoramento do grão. Verificou-se uma tendência maior para o aparecimento de grão anormal nas amostras que sofreram o processo de esferoidização.

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Este trabalho busca desenvolver um aço para cementação a alta temperatura através da adição de nióbio como microligante, a fim de que os compostos formados forneçam partículas de segunda fase que atuem como ancoradoras do grão austenítico, já que o processo de crescimento de grão, especialmente anormal, é conseqüência natural das temperaturas envolvidas. A elevação da temperatura tem como objetivo proporcionar um ganho em produtividade pela redução dos tempos de cementação. Procura-se também estabelecer uma comparação do aço proposto a aços de cementação convencionais (DIN 17Cr3 e SAE 5115). Utilizou-se um aço SAE 5115 com 0,034% de nióbio, que foi submetido a diferentes condições de ensaio em laboratório: deformação a frio por compressão livre em três graus de deformação (isento, 25 e 50%); com posterior aquecimento em patamares de temperatura que simulam diferentes níveis de cementação (930 , 950 , 1000 e 1050 C), bem como diferentes tempos de manutenção em temperatura, de tal forma a atingir camadas cementadas hipotéticas em torno de 1,0 mm de profundidade. Encerram-se os testes submetendo o aço estudado a um processo de produção industrial de pinos de pistão, que sofrem deformação a temperatura ambiente e cementação a 950 C por 2,5 h O aço SAE 5115 ao “Nb” mostrou um melhor desempenho no controle dos grãos austeníticos, tanto para os ensaios de simulação realizados em laboratório e comparados ao aço DIN 17Cr3, como frente ao processo de produção de pinos de pistão tendo como comparativo o aço SAE 5115. O modelo teórico de Hudd e outros (que trata os carbonitretos de nióbio como de extensiva solubilidade mútua) e o de Gladman (que define os nitretos de alumínio e de nióbio como mutuamente exclusivos), associados às equações de Wagner (para coalescimento das partículas de segunda fase), bem como à equação de Gladman e Pickering (que determina o raio crítico de partícula para uma distribuição aleatória de partículas), mostraram-se bastante adequados em prever a resposta das partículas precipitadas, partindo-se da composição química do aço, principalmente para as partículas de carbonitreto de nióbio em condições que não envolvessem níveis elevados de deformação.

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The present work shows a contribution to the studies of development and solid sinterization of a metallic matrix composite MMC that has as starter materials 316L stainless steel atomized with water, and two different Tantalum Carbide TaC powders, with averages crystallite sizes of 13.78 nm and 40.66 nm. Aiming the metallic matrix s density and hardness increase was added different nanometric sizes of TaC by dispersion. The 316L stainless steel is an alloy largely used because it s high resistance to corrosion property. Although, its application is limited by the low wear resistance, consequence of its low hardness. Besides this, it shows low sinterability and it cannot be hardened by thermal treatments traditional methods because of the austenitic structure, face centered cubic, stabilized mainly in nickel presence. Steel samples added with TaC 3% wt (each sample with different type of carbide), following a mechanical milling route using conventional mill for 24 hours. Each one of the resulted samples, as well as the pure steel sample, were compacted at 700 MPa, room temperature, without any addictive, uniaxial tension, using a 5 mm diameter cylindrical mold, and quantity calculated to obtain compacted final average height of 5 mm. Subsequently, were sintered in vacuum atmosphere, temperature of 1290ºC, heating rate of 20ºC/min, using different soaking times of 30 and 60 min and cooled at room temperature. The sintered samples were submitted to density and micro-hardness analysis. The TaC reforced samples showed higher density values and an expressive hardness increase. The complementary analysis in optical microscope, scanning electronic microscope and X ray diffractometer, showed that the TaC, processed form, contributed with the hardness increase, by densification, itself hardness and grains growth control at the metallic matrix, segregating itself to the grain boarders

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The nanostructures materials are characterized to have particle size smaller than 100 nm and could reach 1 nm. Due to the extremely reduced dimensions of the grains, the properties of these materials are significantly modified relatively when compared with the conventional materials. In the present work was accomplished a study and characterization of the molybdenum carbide, seeking obtain it with particles size in the nanometers order and evaluate its potential as catalyst in the reaction of partial methane oxidation. The method used for obtaining the molybdenum carbide was starting from the precursor ammonium heptamolybdate of that was developed in split into two oven, in reactor of fixed bed, with at a heating rate of 5ºC/min, in a flow of methane and hydrogen whose flow was of 15L/h with 5% of methane for all of the samples. The studied temperatures were 350, 500, 600, 650, 660, 675 and 700ºC and were conducted for 0, 60, 120 and 180 minutes, and the percent amount and the crystallite size of the intermediate phases were determined by the Rietveld refinement method. The carbide obtained at 660ºC for 3 hours of reaction showed the best results, 24 nm. Certain the best synthesis condition, a passivating study was accomplished, in these conditions, to verify the stability of the carbide when exposed to the air. The molybdenum carbide was characterized by SEM, TEM, elemental analysis, ICP-AES, TG in atmosphere of hydrogen and TPR. Through the elemental analysis and ICP-AES the presence carbon load was verified. TG in atmosphere of hydrogen proved that is necessary the passivating of the molybdenum carbide, because occur oxidation in room temperature. The catalytic test was accomplished in the plant of Fischer-Tropsch of CTGAS, that is composed of a reactor of fixed bed. Already the catalytic test showed that the carbide presents activity for partial oxidation, but the operational conditions should be adjusted to improve the conversion

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Among the heterogeneous catalysts materials made from niobium show up as an alternative to meet the demand of catalysts for biodiesel production. This study aims to evaluate the potential of a heterogeneous catalyst derived from a complex of niobium in the reaction of methyl esterification of oleic acid. The catalyst was synthesized after calcination at different temperatures of a niobium complex ((NH4)3[NbO(C2O4)3].H2O) generating a niobium oxide nanostructure with a different commercial niobium oxide used to synthesize the complex. The commercial niobium oxide, the complex niobium and niobium catalyst were characterized by thermogravimetry (TG and DTA), surface area analysis (BET), scanning electron microscopy (SEM) and X-ray diffraction (XRD), showing the catalyst has researched morphological and crystallographic indicating a catalytic potential higher than that of commercial niobium oxide characteristics. Factorial with central composite design point, with three factors (calcination temperature, molar ratio of alcohol/oleic acid and mass percentage of catalyst) was performed. Noting that the optimal experimental point was given by the complex calcination temperature of 600°C, a molar ratio alcohol/oleic acid of 3.007/1 and the catalyst mass percentage of 7.998%, with a conversion of 22.44% oleic acid in methyl oleate to 60 min of reaction. We performed a composite linear and quadratic regression to determine an optimal statistical point of the reaction, the temperature of calcination of the complex at 450°C, the molar ratio of alcohol/oleic acid 3.3408/1 and mass percentage of catalyst of 7.6833% . Kinetic modeling to estimate parameters for heterogeneous catalysis it set well the experimental results with a final conversion of 85.01% with 42.38% of catalyst and without catalyst at 240 min reaction was performed. Allowing to evaluate the catalyst catalytic studied has the potential to be used in biodiesel production

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This work presents a spray-dryer designed to oxalate-niobate precursors and suitable for the production of Niobium Carbide. The dryer was intended to produce powders of controlled particle size. First, the precursor is dissolved in water to produce a solution of known concentration and then it is atomized on the spray-dryer to produce the powder. This equipment consists of a 304 stainless steel chamber, 0.48 m x 1.9 m (diameter x length), with a conical shape at the lower portion, which is assembled on a vertical platform. The chamber is heated by three 4 kW electrical resistances. In this process, drying air is heated as it flows inside a serpentine surrounding the chamber, in contrary to more traditional processes in which the hot drying air is used to heat the component. The air enters the chamber at the same temperature of the chamber, thus avoiding adherence of particles on the internal surface. The low speed flow is concurrent, directed from the top to the bottom portion of the chamber. Powders are deposited on a 0.4 m diameter tray, which separates the cylindrical portion from the conical portion of the chamber. The humid air is discharged though a plug placed underneath the collecting tray. A factorial experimental planning was prepared to study the influence of five parameters (concentration, input flow, operation temperature, drying air flow and spray air flow) on the characteristics of the powders produced. Particle size distribution and shape were measured by laser granulometry and scanning electronic microscopy. Then, the powders are submitted to reaction in a CH4 / H2 atmosphere to compare the characteristics of spray-dried powders with powders synthetizided by conventional methods

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Seeking a greater appreciation of cheese whey was developed to process the hydrogenation of lactose for the production of lactitol, a polyol with high added value, using the catalyst Ni / activated carbon (15% and 20% nickel), the nitride Mo2N, the bimetallic carbide Ni-Mo/ activated carbon and carbide Mo2C. After synthesis, the prepared catalysts were analyzed by MEV, XRD, laser granulometry and B.E.T. The reactor used in catalytic hydrogenation of lactose was the type of bed mud with a pressure (68 atm), temperature (120 oC) and stirring speed (500 rpm) remained constant during the experiments. The system operated in batch mode for the solid and liquid and semi-continuous to gas. Besides the nature of the catalyst, we studied the influence of pH of reaction medium for Mo2C carbide as well as evaluating the character of the protein inhibitor and chloride ions on the activity of catalysts Ni (20%)/Activated Carbon and bimetallic carbide Ni-Mo/Activated Carbon. The decrease in protein levels was performed by coagulation with chitosan and adsorption of chloride ions was performed by ion exchange resins. In the process of protein adsorption and chloride ions, the maximum percentage extracted was about 74% and 79% respectively. The micrographs of the powders of Mo2C and Mo2N presented in the form of homogeneous clusters, whereas for the catalysts supported on activated carbon, microporous structure proved impregnated with small particles indicating the presence of metal. The results showed high conversion of lactose to lactitol 90% for the catalyst Ni (20%)/Activated Carbon at pH 6 and 46% for the carbide Mo2C pH 8 (after addition of NH4OH) using the commercial lactose. Monitoring the evolution of the constituents present in the reaction medium was made by liquid chromatography. A kinetic model of heterogeneous Langmuir Hinshelwood type was developed which showed that the estimated constants based catalysts promoted carbide and nitride with a certain speed the adsorption, desorption and production of lactitol

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HZSM5 zeolite was modified by exchanging proton by niobium (V). Several samples were obtained with various degrees of exchange. Pore volumes and acidity were measured to characterize these exchanged zeolites. Catalytic properties were evaluated with two reaction tests: m-xylene transformation and n-heptane cracking. The introduction of niobium on HZSM5 zeolite decreases the diffusion coefficient of 2-methyl-pentane and increases the zeolite acidity. The sample containing niobium are initially more active in cracking of n-heptane and m-xylene isomerization than HZSM5 alone.

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

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Pós-graduação em Química - IQ