Made available in DSpace on 2014-12-17T15:42:13Z (GMT). No. of bitstreams: 1 ValdeliceRS_TESE.pdf: 2586359 bytes, checksum: e3d9d5d8e2c97ad0990f43fd755545a2 (MD5) Previous issue date: 2010-11-26 / One of the main applications of methane is in the production of syngas, a mixture of hydrogen and carbon monoxide. Procedures used in this process are steam reforming, CO2 reforming, partial oxidation and autothermal reforming. The present study evaluated and compared the behavior of nickel catalysts supported on mixed oxides of cerium and manganese in the partial oxidation of methane with that of nickel catalysts supported on mixed oxides of cerium and zirconium. Mixed oxides of cerium and zirconium or cerium and manganese were synthesized using two different preparation methods, the polymeric precursor based on Pechini method and combustion reaction using a microwave. This was followed by impregnation with nickel content of 15 %. Samples were calcined at 300, 800 and 900 ?C and characterized by specific surface area (SSA), X-ray fluorescence (XRF), X-ray diffraction (XRD), scanning electron microscopy (SEM), temperature programmed reduction (TPR) and the reaction of partial oxidation of methane. The specific areas of samples decrease with the rise in calcination temperature and after nickel impregnation. Metal-cerium solid solution was formed and the presence of other manganese species outside the solid solution structure was confirmed in the compound with the highest amounts of manganese oxides showed. With regard to scanning electron microscopy, supports based on cerium and zirconium prepared by Pechini method exhibited agglomerated particles without uniform geometry or visible pores on the surface. However, compounds containing manganese presented empty spaces in its structure. Through synthesis by combustion reaction, morphology acquired independently of the proposed composition demonstrated greater porosity in relation to Pechini synthesis. Although catalysts were prepared using different synthesis methods, the insertion of nickel showed very similar reduction profiles (TPR). In relation to nickel catalysts supported on mixed oxide of cerium and zirconium, there is an initial reduction of NiO species that present certain interaction with the support. This is followed by the reduction of Ce4+ in Ce3+ surface, with subsequent bulk reduction. For catalysts containing manganese, a reduction of nickel oxide species occurs, followed by two stages of reduction for species Mn2O3 in Mn3O4 and Mn3O4 in MnO, with subsequent reduction of bulk. With respect to partial oxidation reactions, the nickel catalyst supported on mixed oxide of cerium and zirconium, prepared using the Pechini method, exhibited CH4 conversion of approximately 80 %, with conversion of 81 % when prepared by combustion. This behavior continued for 10 hours of reaction. Manganese content was also found to directly influence catalytic activity of materials; the greater the manganese oxide content, the faster deactivation and destabilization occurred in the catalyst. In both synthesis methods, the nickel catalyst supported on mixed oxide of cerium and zirconium maintained an H2/CO ratio very close to 2 during the 10 hours of partial oxidation reaction. Samples containing manganese displayed smaller H2/CO ratios and lower performance in partial oxidation. / Uma das principais aplica??es do metano ? a produ??o de g?s de s?ntese, mistura de hidrog?nio e mon?xido de carbono. Os processos utilizados na produ??o de g?s de s?ntese a partir do metano s?o: reforma a vapor, reforma com CO2, oxida??o parcial e reforma autot?rmica. Neste trabalho, o comportamento de catalisadores de n?quel suportados em ?xidos mistos de c?rio e mangan?s na rea??o de oxida??o parcial do metano foi avaliado e comparado com o catalisador de n?quel suportados no ?xido misto de c?rio e zirc?nio. Os ?xidos mistos de c?rio e zirc?nio ou c?rio e mangan?s foram sintetizadas usando dois diferentes m?todos de prepara??o; o de precursores polim?ricos baseado no processo Pechini e por rea??o de combust?o usando um micro-ondas, seguido da impregna??o de n?quel com teor de 15 %. As amostras foram calcinadas a 300, 800 e 900 ?C e caracterizados por ?rea espec?fica (ASE), fluoresc?ncia de raios X (FRX), difra??o de raios X (DRX), microscopia eletr?nica de varredura (MEV), redu??o ? temperatura programada (RTP) e a rea??o de oxida??o parcial do metano. As ?reas espec?ficas das amostras diminuem com o aumento da temperatura de calcina??o e ap?s a impregna??o com n?quel. A solu??o s?lida c?rio-metal foi formada e nos composto com as maiores quantidades de ?xidos de mangan?s verificou-se a presen?a de outras esp?cies de mangan?s fora da estrutura da solu??o s?lida. Quanto ? microscopia eletr?nica de varredura os suportes a base de c?rio e zirc?nio preparados via Pechini exibem part?culas aglomeradas, sem geometria uniforme e sem a visualiza??o de poros na superf?cie, enquanto os compostos contendo mangan?s apresentaram alguns vazios na sua estrutura. Atrav?s da s?ntese por rea??o de combust?o a morfologia adquirida independente da composi??o proposta apresentou uma maior porosidade em rela??o ? s?ntese Pechini. Mesmo sendo os catalisadores preparados por diferentes m?todos de s?ntese, a inser??o de n?quel deixou seus perfis de redu??o (RTP) muito semelhantes. Para os catalisadores de n?quel suportados no ?xido misto de c?rio e zirc?nio, h? em primeiro lugar redu??o de esp?cies NiO que apresentam certa intera??o com o suporte, seguido da redu??o de Ce4+ em Ce3+ superficiais, com posterior redu??o do bulk. Para os catalisadores contendo mangan?s h? a redu??o das esp?cies de ?xido de n?quel, seguido de duas etapas de redu??o para as esp?cies Mn2O3 em Mn3O4 e Mn3O4 em MnO, com posterior redu??o do bulk. Quanto ?s rea??es de oxida??o parcial, o catalisador de n?quel suportados no ?xido misto de c?rio e zirc?nio preparado via m?todo Pechini, apresentou uma convers?o de CH4 de cerca de 80 %, sendo 81 % a convers?o quando preparado via combust?o. Esse comportamento manteve-se durante 10 horas de rea??o. Observou-se tamb?m que o teor de mangan?s influencia diretamente na atividade catal?tica dos materiais, quanto maior o teor de ?xido de mangan?s mais r?pido o catalisador apresentava desativa??o e desestabiliza??o. Para ambos os m?todos de s?ntese o catalisador de n?quel suportados no ?xido misto de c?rio e zirc?nio manteve a raz?o H2/CO bem pr?xima de 2 durante as 10 horas em que ocorre a rea??o de oxida??o parcial. As amostras contendo mangan?s apresentaram menores raz?es de H2/CO e menor desempenho na oxida??o parcial.

Made available in DSpace on 2014-12-17T14:06:48Z (GMT). No. of bitstreams: 1 WersonMC.pdf: 1184207 bytes, checksum: f2f0598e463a68730749344c713c5bff (MD5) Previous issue date: 2008-02-22 / The Tungsten/copper composites are commonly used for electrical and thermal objectives like heat sinks and lectrical conductors, propitiating an excellent thermal and electrical conductivity. These properties are dependents of the composition, crystallite size and production process. The high energy milling of the powder of W-Cu produces an dispersion high and homogenization levels with crystallite size of W very small in the ductile Cu phase. This work discusses the effect of the HEM in preparation of the W-25Cu composite powders. Three techniques of powder preparation were utilized: milling the dry with powder of thick Cu, milling the dry with powder of fine Cu and milling the wet with powder of thick Cu. The form, size and composition of the particles of the powders milled were observed by scanning electron microscopy (SEM). The X-ray diffraction (XRD) was used to analyse the phases, lattice parameters, size and microstrain of the crystallite. The analyse of the crystalline structure of the W-25Cu powders milled made by Rietveld Method suggests the partial solid solubility of the constituent elements of the Cu in lattice of the W. This analyse shows too that the HEM produces the reduction high on the crystallite size and the increase in the lattice strain of both phases, this is more intense in the phase W / Os comp?sitos de Tungst?nio/Cobre (W-Cu) s?o geralmente usadas para fins el?tricos e t?rmicos como dissipadores de calor e condutores el?tricos, devido as suas excelentes propriedades de condutividades t?rmica e el?trica. Essas propriedades s?o dependentes da composi??o, do tamanho de cristalito e principalmente do processo de fabrica??o. A moagem de alta energia de p?s W-Cu produz alto n?vel de homogeneiza??o e dispers?o com cristalitos de W muito fino na fase d?ctil Cu. Este trabalho discute o efeito da MAE na prepara??o dos p?s comp?sitos W-25Cu. Tr?s t?cnicas de prepara??o dos p?s foram utilizadas: moagem a seco com p? de Cu grosso, moagem a seco com p? de Cu fino e moagem a ?mido com p? de Cu grosso. A forma, tamanho e a composi??o das part?culas dos p?s mo?dos foram observadas por microsc?pio eletr?nico de varredura (MEV). A difra??o de raios-X(DRX) foi usada para observar as fases, par?metros de rede, tamanho e microtens?o dos cristalitos. A an?lise da estrutura cristalina dos p?s mo?dos de W-25Cu feita pelo m?todo de Rietveld sugere uma solubilidade s?lida parcial dos elementos constituintes do cobre (Cu) na rede do tungst?nio (W). Essa an?lise tamb?m mostra que a MAE produz uma alta redu??o no tamanho dos cristalitos e um aumento de tens?o na rede de ambas as fases, isto ocorre com maior intensidade na fase do W