688 resultados para Polpa de bauxita


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

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

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

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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

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Pós-graduação em Zootecnia - FCAV

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Pós-graduação em Engenharia Mecânica - FEG

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This completion of course work has as its object of study the Bauxite Province of Paragominas regarded as the richest Amazon bauxite province and whose genesis is related to laterization processes responsible for the formation of mineral deposits of the Rondon Alumina Project, designed to assess areas in the southeast of Pará State, for mineral resources exploration of bauxite, which is the main source of aluminum in the country. Located in the region of Rondon do Pará - PA, the study area is geologically inserted in Lithostratigraphic Unit called Cobertura Laterítica Matura (Mature Lateritic Cover), formed by alteration of paleotropics Cretaceous siliciclastic rocks, and its geomorphology corresponds to a broad plateau with displays of representative profiles of the processes that acted in the region. In this context, the present research aims to characterize the geological evolution of the laterite profile, with detailed studies in the area, geological description of the formations from the bauxite surfaces, and mineralogical composition litochemical of different horizons that were correlated and deployed in an evolutionary model compatible with its traits. The data collected during the analysis subsidized metalogenetic understanding of the processes that acted in the enrichment of aluminum and iron as well as the redistribution of the latter modified profile. The results and information were embodied in the form of geological characterization of the different constituents of mineral associations of bauxite horizons, similarities or differences in both textural and structural aspects, in order to propose a evolutionary model with retaken of gibbsitization processes

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Dentre os reagentes alternativos, têm-se destacado o peróxido de hidrogênio, visando atender às demandas de produção de celulose ECF. Reagentes como cloro e dióxido de cloro reagem com a lignina residual, levando à formação de compostos organoclorados, fator negativo para as questões relacionadas ao meio ambiente. O fator kappa (FK) é determinante para a dosagem de dióxido de cloro em seqüencias de branqueamento que determinarão a alvura requerida e reduzirão a formação de compostos organoclorados no licor residual. O presente estudo avaliará o efeito da lignina residual através do número de permanganato, após o estágio D1, no branqueamento com peróxido de hidrogênio. Foram realizados cinco branqueamentos de polpas iguais por seqüências ECF em ensaios laboratoriais, variando-se o fator kappa entre eles. O branqueamento foi realizado com uma polpa kraft de eucalipto, prédeslignificada com oxigênio, utilizando a quantidade de reagentes requeridas para cada estágio, em sacos de polietileno e mantidas em banho de vapor com controle de temperatura pelo tempo requerido. A seqüência D(E+P)DP proposta foi comparada com a seqüência D(E+P)DD. Os métodos utilizados para realizar este estudo são os de procedimento padrão conforme as normas TAPPI e CPPA para branqueamento em laboratório de polpa celulósica. Foram avaliados os parâmetros de qualidade da polpa branqueada com os valores de alvura, viscosidade, número kappa, número de permanganato, reversão de alvura e custo do processo de branqueamento e a influência do fator kappa sobre cada uma das condições propostas. Os resultados foram interpretados com base para as polpas que atingiram a alvura objetivo de 90 %ISO. Verificou-se que o FK ideal obtido foi de 0,20 para as seqüências avaliadas. A lignina residual afetou negativamente o branqueamento de todas as sequências, sendo a sequência D(E+P)DP com FK de 0,20 e carga ...

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Mesenchymal stem cells (MSCs) are adult multipotent cells with fibroblastoid morphology and adherent to plastic. Furthermore, they can be obtained from different sources. Besides bone marrow, these cells are taken from umbilical cord blood, umbilical vein, saphenous vein, peripheral blood, arteries, liver and fetal pancreas, placenta, dental pulp and adipose tissue. MSCs derived from adipose tissue are important because of the abundant number of cells that can be obtained from this tissue, easy access and little discomfort to the patient. This study compared two techniques for obtaining MSCs from adipose tissue: mechanical dissociation (MD) and enzymatic digestion (ED). We also analyzed the inter-species cross-reactions using commercial monoclonal antibodies directed against surface antigens of stem cells from different species: mouse, horse, rabbit, monkey and human. We found that MD technique is favorable in relation to ED within 15 days of culture, and ED is more efficient in the first days of culture. The data also showed that MD causes less damage to cellular DNA. About inter-species cross-reactions, the monoclonal antibody A69 directed against stem cells from rabbits, which can be used in veterinary medicine, particularly in research involving horses

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The deslignification with oxygen, also denominated pre-O2, consists in a whitening stage, which consists of accomplishing an oxidation of the lignin, and remove it with the alkali, providing a larger earnings in the bleaching of the pulp. The pre-O2 is a process already very established, where a significant part of the cellulose of whitened short fiber produced nowadays suffers deslignification for this method. The conditions of work of this stage contemplate directly in the results of the deslignification level, in the physical, optical and mechanics properties of the pulp, and consequently of the paper, because this is important to know their effects fully. The main variables related to the control of this process are respectively: pressure and oxygen load, alkaline load, consistence, time and temperature, being this last variable was the study focus in this work. The objective of the work was to analyze the effect of the variation of the temperature in the oxygen whitening along every bleaching process of the pulp, refine and in the optical, physics and mechanics properties of the paper. The development of the work was based in four temperature levels (90, 95, 100 and 105°C) combined to two whitening sequences (OD0(E+P)D1P and OAHTD0(E+P)D1P). The results obtained in the oxygen deslignification stage indicated that the elevation of the temperature contemplated in increases of the whiteness, deslignification efficiency and in the viscosity loss allied to the reduction of the selectivity of the process. In the remaining of the whitening, the sequence that included the acid hydrolysis presented values slightly inferior of whiteness, kappa number, viscosity and yield in relation to the other sequence when compared with the samples of same temperatures. Already the physical tests showed that the sequence with acid stage amplifies the values of capillary... (Complete abstract click electronic access below)

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The new market, focused on sustainability and other environmental concerns, refers to innovations that seek alternative forms of production. In pulp and paper bleaching alternative reagents are studied, for example, hydrogen peroxide, in partial substitution of chlorine dioxide in order to reduce the formation of organochlorines. In this context, this study examined the burden of hydrogen peroxide (H2O2) on alkaline extraction stage (stage Ep) required for the bleaching of pulp with eucalyptus kraft pulp, pre-oxygen delignified to obtain equivalent brightness at 90 ± 0.5% ISO, as well as its effect on quality of pulp produced. The pulp was bleached by the sequence D(Ep)DP, with the application of factor kappa of 0.14 and varying the concentration of hydrogen peroxide in Ep stage three, five, seven and nine kilograms of reagent per ton of pulp absolutely drought. The final P stage was optimized with the use of six, nine and twelve pounds of hydrogen peroxide per ton of absolutely dry pulp to achieve the required brightness. The quality of the pulp produced was analyzed based on the kappa number, the brightness and the viscosity. The methods were performed according to standards set by the standard TAPPI (Technical Association of the Pulp and Paper Industry). The best result was obtained using the following D0Ep(7)D1P(6), which showed a viscosity of 19.9 cP, 89.6% ISO brightness, consumption of 94.9 kg / t of reagents and reagent costs of US$ 28.15, because it showed better pulp quality for a lower cost compared to the others. It was found that the greater the amount of hydrogen peroxide in alkaline extraction, the lower the kappa number and increased the amount of residual hydrogen peroxide. The higher the charge of hydrogen peroxide in Ep stage, the lower the need for hydrogen peroxide in the final P stage, reducing the cost of bleaching

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Phenolic compounds represent one of the main groups of secondary metabolites. Due to their chemical diversity, they have a variety of functions in plants, such as protection against ultraviolet radiation, herbivores and pathogens, and attraction of pollinators or dispersers of fruits and seeds. For human, the phenolic compounds are used like food colorings and flavors and, due to their pharmacological properties, mainly to antioxidant activity, they are associated with several health benefits, such as delay senility, prevention and therapy of cardiovascular diseases and of some cancers. The grapes are considered one of the main source of phenolic compounds and the fruit and its products are consumed in Brazil and worldwide. Considering the phenolic compounds diversity and their different distribution in the grape parts, this work had like aims the extraction, identification and quantification of the main classes of phenolic compounds of 10 grape varieties. The content of total phenols, flavanols and anthocyanins were determined, respectively, according to the Folin-Ciocalteu, DMACA and comparison of pH spectrophotometric methods. The content of total phenols varied from 142.75 + 1.86 to 483.39 + 5.90 mg.L-1 in the peel and from 86.50 + 0.54 to 146.32 + 9.97 mg.L-1 in the pulp. The amount of total flavanols varied from 3.68 + 0.03 to 6.92 + 0.26 mg.L-1 in the peel and from 0.90 + 0.00 to 1.36 + 0.00 mg.L-1 in the pulp. The content of total anthocyanins varied from 7.00 + 0.99 to 406.56 + 39.50 mg.L-1 in the peel and from 2.88 + 0.28 to 46.36 + 1.89 mg.L-1 in the pulp. The phenolic compounds concentration was higher in the peel than in the pulp. The total phenols and anthocyanins varied a lot while the total flavanols were more constant. The flavanols represent the smaller portion of phenolic compounds

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A xilana, o segundo principal componente da parede celular vegetal, pertence ao grupo das hemiceluloses, sendo composta por diferentes carboidratos, principalmente xilose e arabinose. Na natureza, devido a sua heterogeneidade estrutural, este complexo polissacarídeo é completamente hidrolisado pela ação sinergística de diferentes enzimas, incluindo xilanases e β-xilosidases, responsáveis pela degradação da sua cadeia principal e outras enzimas chamadas auxiliares ou desramificantes, importantes para remoção dos grupos laterais. Dentre estas últimas, destacam-se as α-L-arabinofuranosidases, enzimas responsáveis pela remoção de resíduos L-arabinofuranosil do polímero. As arabinofuranosidases podem ser produzidas por micro-organismos, como bactérias e fungos, sendo essencialmente enzimas extracelulares. Fungos, especialmente os de solo e madeira, têm sido utilizados para produção de enzimas xilanolíticas, sendo particularmente interessantes do ponto de vista industrial, pelo fato de secretarem suas enzimas diretamente no meio em que se encontram não necessitando de ruptura celular para a liberação das mesmas. Além disso, apresentam níveis de produção mais elevados que os obtidos em culturas bacterianas ou de leveduras. A crescente preocupação com a escassez dos recursos naturais e com a degradação ambiental tem levado à busca por tecnologias mais eficientes, mais competitivas e menos poluentes. Atualmente, muitos processos industriais empregam enzimas microbianas, apresentando inúmeras vantagens em relação às técnicas convencionais. As α-L-arabinofuranosidases podem ser utilizadas individualmente ou em combinação com outras enzimas, representando uma ferramenta promissora para aplicação em diversos processos biotecnológicos como no branqueamento da polpa celulósica, na síntese de oligossacarídeos, na produção de etanol de segunda geração, ou ainda...(Resumo completo, clicar acesso eletrônico abaixo)