Estudo da viabilidade técnica do uso das argilas da região do agreste potiguar para produção de peças cerâmicas: caracterização e formulação

In recent decades, ceramic products have become indispensable to the technological development of humanity, occupying important positions in scientific production and consequently in industrial production. One area of the economy that continues to absorb large amounts of the products of this sector is Construction. Among the branches of the ceramic industry, there are the red ceramic industry which is traditionally the basis of that economic sector. Among the reasons for which the red ceramic industry became popular in the country, and specifically in Rio Grande do Norte, is the abundance of this raw material, easily found throughout the national territory. However, it appears that the red ceramic industry has deficiencies in technology and skilled labor, resulting in the production of ceramic goods with low added value. Among the factors that determine the quality of the ceramic products red has the proper formulation of the ceramic mass, the conformation and the firing temperature. Thus, the overall goal of this work is to study the mineralogical and technological properties, two clays from the region of the Wasteland Potiguar industrial ceramist. Therefore, the raw materials were characterized by analysis of Xray diffraction (XRD) analysis, X-ray fluorescence (XRF), particle size analysis (FA), scanning electron microscopy (SEM), optical microscopy (OM ), plasticity index (PI), thermal gravimetric analysis (TGA) and differential thermal analysis (DTA). The technological properties of the material were analyzed by water absorption tests (AA%) porosity (% PA), the linear shrinkage (RT%), apparent density (MEA), loss on ignition (PF%) and flexural strength three points (TRF)

Desenvolvimento de catalisadores bifuncionais de óxido de zircônio modificado por óxidos de tungstênio e molibdênio contendo platina para a reação de isomerização de n-parafinas

Bifunctional catalysts based on zircon oxide modified by tungsten (W = 10, 15 and 20 %) and by molybdenum oxide (Mo= 10, 15 e 20 %) containg platinum (Pt = 1%) were prepared by the polymeric precursor method. For comparison, catalysts the tungsten base was also prepared by the impregnation method. After calcinations at 600, 700 and 800 ºC, the catalysts were characterized by X-ray diffraction, fourier-transform infrared spectroscopy, thermogravimetric and differential thermal analysis, nitrogen adsorption and scanning electron microscopy. The profile of metals reduction was determined by temperature programmed reduction. The synthesized catalysts were tested in n-heptane isomerization. X-ray diffractogram of the Pt/WOx-ZrO2 and Pt/MoOx-ZrO2 catalysts revealed the presence of tetragonal ZrO2 and platinum metallic phases in all calcined samples. Diffraction peaks due WO3 and ZrO2 monoclinic also were observed in some samples of the Pt/WOx-ZrO2 catalysts. In the Pt/MoOx-ZrO2 catalysts also were observed diffraction peaks due ZrO2 monoclinic and Zr(MoO4)2 oxide. These phases contained on Pt/WOx-ZrO2 and Pt/MoOx-ZrO2 catalysts varied in accordance with the W or Mo loading and in accordance with the calcination temperature. The infrared spectra showed absorption bands due O-W-O and W=O bonds in the Pt/WOx-ZrO2 catalysts and due O-Mo-O, Mo=O and Mo-O bonds in the Pt/MoOx-ZrO2 catalysts. Specific surface area for Pt/WOx-ZrO2 catalysts varied from 30-160 m2 g-1 and for the Pt/MoOx-ZrO2 catalysts varied from 10-120 m2 g-1. The metals loading (W or Mo) and the calcination temperature influence directly in the specific surface area of the samples. The reduction profile of Pt/WOx-ZrO2 catalysts showed two peaks at lower temperatures, which are attributed to platinum reduction. The reduction of WOx species was evidenced by two reduction peak at high temperatures. In the case of Pt/MoOx-ZrO2 catalysts, the reduction profile showed three reduction events, which are attributed to reduction of MoOx species deposited on the support and in some samples one of the peak is related to the reduction of Zr(MoO4)2 oxide. Pt/WOx-ZrO2 catalysts were active in the n-heptane isomerization with high selectivity to 3-methyl-hexane, 2,3- dimethyl-pentane, 2-methyl-hexane among other branched hydrocarbons. The Pt/MoOx-ZrO2 catalysts practically didn't present activity for the n-heptane isomerization, generating mainly products originating from the catalytic cracking

Síntese e caracterização de pós Ba(x)Sr(1-x)Co0,8Fe0,2O3- através do método de coprecipitação via oxalato

Ceramic powders based on oxides of perovskite-type structure is of fundamental interest nowadays, since they have important ionic-electronic conductivity in the use of materials with technological applications such as gas sensors, oxygen permeation membranes, catalysts and electrolytes for solid oxide fuel cells (SOFC). The main objective of the project is to develop nanostructured ceramic compounds quaternary-based oxide Barium (Br), Strontium (Sr), Cobalt (Co) and Iron (Fe). In this project were synthesized compounds BaxSr(1-x)Co0, 8Fe0,2O3- (x = 0.2, 0.5 and 0.8) through the oxalate co-precipitation method. The synthesized powders were characterized by thermogravimetric analysis and differential thermal analysis (TGADTA), X-ray diffraction (XRD) with the Rietveld refinement using the software MAUD and scanning electron microscopy (SEM). The results showed that the synthesis technique used was suitable for production of nanostructured ceramic solid solutions. The powders obtained had a crystalline phase with perovskite-type structure. The TGA-DTA results showed that the homogeneous phase of interest was obtained temperature above 1034°C. It was also observed that the heating rate of the calcination process did not affect the elimination of impurities present in the ceramic powder. The variation in the addition of barium dopant promoted changes in the average crystallite size in the nanometer range, the composition being BSCF(5582) obtained the lowest value (179.0nm). The results obtained by oxalate co-precipitation method were compared with those synthesis methods in solid state and EDTA-citrate method

Effect of precursor solution on the formation of perovskite phase of Pb(Mg-1/Nb-3(2/3))O-3 thin films

Precursor solutions for Pb(Mg1/3Nb2/3)O-3 (PMN) synthesis were obtained by Pechini's method. The influence of the concentration of organic materials on the phase formation has been studied. For this purpose, PMN solutions were prepared with different precursors and were characterized by thermogravimetric and differential thermal analysis. The obtained solutions were deposited onto a Si (100) substrate by dip coating and pre-treated in a hot plate at 300 degreesC for 1 h. The films were annealed at 600, 700, 800 and 900 degreesC for 1 h and characterized by X-ray diffraction. The perovskite phase was formed after annealing at 600 and 700 degreesC when the solution of PMN was prepared with a lower amount of organic material and starting with mobium oxide. By increasing the temperature to 800 or 900 degreesC, only the formation of pyrochlore phase was observed. With the solution prepared from mobium ethoxide, only the presence of pyrochlore phase was observed independently of the annealing temperature. (C) 2002 Elsevier B.V. B.V. All rights reserved.

Evaluation of organic molecules originated during composting process

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Síntese e caracterização do sistema ZrO2-SiO2 com adição de cobalto para uso como pigmentos cerâmicos

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

Protected magnetic particles: Silica on yttrium iron garnet

The formation of silica on core yttrium iron garnet presents a variety of different applications as corrosion resistance and stabilization of magnetic properties. Well-defined magnetic particles were prepared by heterocoagulating silica on yttrium iron garnet to protect the core. Yttrium iron garnet was obtained using a homogeneous nucleation process by controlling the chemical routes from cation hydrolysis in acid medium. The heterocoagulation was induced by tetraethyl orthosilicate hydrolysis in appropriate yttrium iron garnet dispersion medium. The presence of silica on yttrium iron garnet was characterized by vibrating sample magnetometry, X-ray photoemission spectroscopy, transmission electron microscopy, small area electron diffraction and differential thermal analysis. © 2001 Elsevier Science B.V. All rights reserved.

Estudos de absorção e emissão de UV/Vis em xerogéis de sílica dopados com cromo obtidos por processo Sol-Gel

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Estudos das propriedades ópticas e térmicas dos xerogéis de sílica dopados com Rodamina B

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Estudo da forma e da distribuição de tamanho de partículas de alumina em dispersões coloidais relacionado a sedimentação gravitacional

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

Recuperação e aplicação do dicromato de potássio proveniente do resíduo de sulfocrômica

A simple procedure for recovering potassium dichromate (K2Cr2O7 ) from treatment of residual sulphochromic solution was proposed in the present work by means of cooling crystallization. The decrease of temperature favored the crystallization of K2Cr2O7 due to the decrease of solubility. 5.0 L of sulphochromic wastes containing 48.08 g L-1 of Cr(VI) were treated and the process of crystallization was performed in three steps until crystals were not formed anymore. On each step the content of Crtotal was determined by flame atomic absorption spectrometry and Cr(VI) by colorimetric method with 1,5- diphenylcarbazide, resulting in the removal of 91% and 92% of Crtotal and Cr(VI), respectively. After the last step, the remaining Cr(VI) in the solution was reduced to Cr(III) from the addition of NaHSO3 , recovering via precipitation in pH 8 approximately 36.13 g of Cr(OH)3 . The final supernatant was discarded since chromium content was below the maximum limit established by the Brazilian legislation for effluents discharge, which corresponds to 0.10 and 1.0 mg L-1 of Cr(VI) and Cr(III), respectively. 628.4 g of K2Cr2O7 were recovered and the salt was characterized by X-ray diffraction and differential thermal analysis. Its applicability was compared to the standard K2Cr2O7 when determining the soil organic matter, in which there was no significant difference, thus inferring that the recovered compound may be incorporated on routine analyses. This recovering process allowed the reuse of K2Cr2O7 , thus reducing costs with the acquisition of new reagents and environmental impacts caused by the inadequate discard of sulphochromic solutions.

Estudo energético do bagaço de diferentes variedades de cana-de-açucar

Pós-graduação em Química - IBILCE

Qualidade física e sensorial de biscoitos doces com fécula de mandioca

Neste trabalho, foi avaliada a substituição de 5,10 e 15% de farinha de trigo por fécula de mandioca na elaboração de biscoito doce. Ambas, farinha e fécula, foram submetidas à caracterização físico-química, reológica e análise térmica diferencial (DTA). Os biscoitos produzidos foram comparados por meio de análises sensoriais e microbiológicas. O resultado da análise térmica diferencial não mostrou qualquer alteração no comportamento de gelatinização do amido. O teste de aceitação sensorial mostrou que a crocância foi o único atributo que apresentou diferença significativa, indicando a viabilidade técnica de substituição da farinha de trigo por 15% de fécula de mandioca.

Estudo da influência do tempo de reação e do teor de “Na” na síntese de zeólitas

Este trabalho objetiva sintetizar zeólita tipo “A” utilizando como matéria-prima caulim de enchimento. A síntese das Zeolitas foi realizada em curto tempo e sem agitação. Os materiais de partida e o produto obtido foram identificados e caracterizados por Difração de Raios X (DRX), Espectrometria de Fluorescência de Raios X, Microscopia Eletrônica de Varredura (MEV), Análise Granulométrica e Análise Térmica Diferencial e Gravimétrica (DTA e TG). No processo de síntese foi utilizado como fonte de sílica e alumina o metacaulim, que foi calcinado na temperatura de 600 °C, por 2 horas de patamar de queima em um forno tipo mufla. Como fonte de sódio se utilizou uma solução de hidróxido de sódio 5 M, no sistema também foi adicionado água destilada. Foram realizadas diversas sínteses no interior de uma estufa a 110 °C. A variação no tempo de reação e no teor de sódio foram as variáveis estudadas no processo. Os resultados da síntese da zeólita A se mostraram satisfatório, principalmente no tempo de 10 h e com a relação Al/Na = 0,57. O tempo de reação e a quantidade de sódio são diretamente proporcionais à formação de outra fase zeolítica denominada hidroxisodalita. A partir da zeólita A, por troca iônica com uma solução de cloreto de cálcio foi possível obter a zeólita 5A sem agitação.

Craqueamento termocatalítico da borra de neutralização do óleo de palma (Elaeis guineensis) em escala piloto

Os subprodutos das indústrias de refino de óleo e de biodiesel, como a borra de neutralização, são bastante extensivos e devido a sua baixa pureza e valor econômico constituem uma problemática para essas indústrias no descarte e destinação, sendo de fundamental interesse pesquisas para a utilização desse rejeito. Portanto, este trabalho visa investigar uma alternativa viável, econômica e ambiental para o destino deste subproduto usando o Processo de Craqueamento Termocatalítico da Borra de Neutralização do Óleo de Palma (Elaeis guineensis, Jaqc) em escala piloto utilizando-se 5, 10 e 15% de Carbonato de Sódio (Na²CO³) como catalisador e temperaturas finais de 440ºC e 420ºC. A borra foi obtida pelo processo de neutralização e submetida a uma desidratação e caracterizada assim como o catalisador foi desidratado em estufa e caracterizado em relação à Difração de Raio-X, Análise Térmica Gravimétrica (ATG) e à Análise Térmica Diferencial (TDA). Foram realizados cinco testes de craqueamento termocatalítico na Usina Piloto de Craqueamento (THERMTEK/FEQ/UFPA) o qual é constituído em um reator com agitação mecânica e capacidade de 125 litros, além da dinâmica do processo e destilação dos produtos do craqueamento. O produto líquido orgânico (PLO), amostras da dinâmica do processo e frações da destilação foram caracterizados de acordo com cada norma exigida pela ANP N°65 e analisadas por IV e RMN. Após as análises dos resultados verificou-se que a eficiência do processo aumenta com catalisador e temperatura e que a matéria-prima fornece produtos de baixa acidez e com boas características para uso como combustível. Pela análise da termodinâmica do processo percebeu que alguns parâmetros como viscosidade, densidade e ponto de fulgor diminuem com o tempo e aumento da temperatura, formando hidrocarbonetos mais leves. Com relação à destilação, as frações nas faixas mais pesadas se assemelham ao óleo diesel do petróleo na maioria dos parâmetros exigidos pela ANP N°65.