919 resultados para Reactor fuel reprocessing.


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This work describes the synthesis and characterization of a new octakis[3-(2,2'-dipyridylamine)propyl]octasilsesquioxane (T8-Pr-DPA), and a study of the metal ion preconcentration in fuel ethanol. Batch and column experiments were conducted to investigate for the removal of heavy metal ions from fuel ethanol. The results showed that the Langmuir allowed to describe the sorption equilibrium data of the metal ions on T8-Pr-DPA in a satisfactory way. The following maximum adsorption capacities (in mmolg-1) were determined: 3.62 for Fe (III), 3.32 for Cr (III), 2.15 for Cu (II), 1.80 for Co (II), 1.62 for Pb (II), 1.32 for Ni (II) and 0.88 for Zn (II). The thermodynamic parameters for the adsorption process such as free energy of adsorption (δG), enthalpy of adsorption (δH) and entropy of adsorption (δS) were calculated. Thermodynamic parameters showed that the system has favorable enthalpic, Gibbs free energy, and entropic values. The sorption-desorption of the metal ions has made possible the development of a preconcentration and determination method of metal ions at trace level in fuel ethanol. The method of quantitative analysis for Fe, Cu, Ni and Zn in fuel ethanol by Flame AAS was validated. Several parameters have been taken into account and evaluated for the validation of method, namely: linearity, limit of detection, limit of quantification, and the relative standard deviation and accuracy. The accuracy of the method was assessed by testing analyte recovery in the fuel ethanol samples. © 2013 Elsevier B.V.

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The production of xylooligosaccharides (XOS) using a packed-bed enzymatic reactor was studied at lab-scale. For this, a xylanase from Aspergillus versicolor was immobilized on different supports. The optimal derivative was xylanase immobilized on glyoxyl-agarose supports. This derivative preserved 85% of its catalytic activity; it was around 700-fold more stable than the soluble enzyme after incubation at 60. °C and was able to be reused for at least 10 1. h-cycles retaining full catalytic activity. About 18% of oligosaccharides with prebiotic interest (X2-X6) were produced by the glyoxyl derivative in batch hydrolysis. The production of xylobiose was 2.5-fold higher using the immobilized preparation than with soluble enzyme and small concentrations of xylose (<0.1%) were observed only at the end of the reaction. The derivative was employed on a packed bed reactor, and the continuous operation with no recirculation reached 56% and 70% of the end of reaction with flow rates of 60. mL/h and 12. mL/h, respectively. In continuous operation with recirculation at a flow rate of 60. mL/h, the reaction was completed after four hours. © 2013 Elsevier B.V.

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Pós-graduação em Agronomia (Energia na Agricultura) - FCA

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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

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Pós-graduação em Agronomia (Energia na Agricultura) - FCA

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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.

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A gaseificação é uma conversão termoquímica da biomassa em gás combustível, que pode ser usado como combustível em motores de combustão interna ou como gás de síntese para a indústria química. Para checar o desempenho de um gaseificador temos de quantificar a energia contida no gás produzido e a quantidade de carbono convertido por meio dos cálculos de eficiência energética e de conversão de carbono através dos dados obtidos experimentalmente. A eficiência energética é uma relação entre os fluxos de gás e biomassa e de suas respectivas quantidades de energia, no mesmo sentido, a conversão de carbono é a quantidade de compostos carbonáceos presentes no gás convertido a partir da quantidade de carbono presente na composição da biomassa. O presente documento avalia a eficiência energética e de carbono na conversão de um protótipo de um gaseificador indiano do tipo downdraft produzido por uma empresa local (Floragás). Os parâmetros nominais do gaseificador são: capacidade de produção de gás de 45 kWt, consumo de biomassa (caroço de açaí) de 15 kg/h. As dimensões do gaseificador são: DI 150 mm e altura de 2000 mm). A eficiência energética e a taxa de conversão de carbono foram quantificados, a queda de pressão devido ao leito do reator e a temperatura dos gases também foram medidos na saída do reator e também, a concentração de alcatrão, partículas e gases não condensáveis (CO, CO2, CH4, SO2, N2 e NOx) nos gases de combustão após a sistema de limpeza.

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The purpose of this study was to determine the Minimum Inhibitory Concentration (MIC) of pure or mixed chemicals for Saccharomyces cerevisiae and Lactobacillus fermentum in the samples isolated from distilleries with serious bacterial contamination problems. The biocides, which showed the best results were: 3,4,4' trichlorocarbanilide (TCC), tested at pH 4.0 (MIC = 3.12 mg/l), TCC with benzethonium chloride (CBe) at pH 6.0 (MIC = 3.12 mg/l) and TCC mixed with benzalkonium chloride (CBa) at pH 6.0 (MIC = 1.53 mg /l). If CBa was used in sugar cane milling in 1:1 ratio with TCC, a 8 times reduction of CBa was possible. This formulation also should be tested in fermentation steps since it was more difficult for the bacterium to develop resistance to biocide. There was no inhibition of S. cerevisiae and there were only antibiotics as an option to bacterial control of fuel ethanol fermentation by S. cerevisiae.

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

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Perovskite, single multiferroic bismuth ferrite was prepared by two chemical methods: auto-combustion and soft chemical route. Influence of different fuels and complexing agents and thermal treatment on purity of bismuth ferrite powders and density of bismuth ferrite ceramics were investigated. X-ray diffraction technique (XRD) indicated that optimal temperatures and times for calcination and sintering are 600 degrees C for 2 h and 800 degrees C for 1 h with quenching, respectively. Scanning electron microscopy (SEM) analysis showed that soft route synthesized samples formed softer agglomerates and smaller grains with less secondary phases. Powders and pellets were characterized by Brunauer Emmett Teller (BET) specific surface area analysis, particle size distribution, Fourier transform infrared spectroscopy (FT-IR), dilatometry, Raman spectroscopy, X-ray photoelectron spectroscopy (XPS), dielectric and magnetic measurements. Resistivity and origin of electrical resistance were studied by means of impedance measurements. (C) 2014 Elsevier Ltd and Techna Group S.r.l. All rights reserved.

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Applications of ultrasound were starting from 1912 with the primary objective the detection of icebergs on prevention of maritime accidents. Algae, fish deaths and destruction were observed in the vicinity of sonar that equipped ships and submarines during the First World War.The evolutions of research and studies with ultrasound have big advances following the discovery of piezoelectric transducers in science and technology. As an example we can mention its application in microsurgery, fatigue detection in aerospace mechanics, catalysis sonochemical, biotechnology and others.The work presented here aims to demonstrate the application of ultrasonic in pulsed mode beams in biotechnology with the aim of improving the fermentation of a culture broth containing biological agents. In these experiments we used as ultrasound equipment and oscilator Sonics VCX-600 (20KHz), probe type wave guide. The experiments were conducted in a glass reactor of 200 mL of biomaterial containing cane juice and Saccharomyces cerevisiae in suspension. The parameters analyzed were related to the content Alcohlic (FID gas chromatography), and cell viability (Neubauer chamber), TRS (refractometry). Analysis of results showed that the total production exceeded in irradiated samples compared to normal fermentation (without ultrasound), suggesting additional advantage of ultrasound activation. Lastin Trials 1400 min, showed ethanol production systems 12% more than non-enabled systems. In this context alternatives for ethanol production, bio fuel and many other byproducts of the alcohol industries and chemicals could benefit from the use of ultrasound beams in this range of frequencies.