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Navegando por Assunto "Alumina"

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    Adsorção de CU2+ em alumina de transição obtida a partir da mistura de gibbsita e hidróxido de alumínio gel
    (Universidade Federal do Pará, 2015-09-30) PINHEIRO, Darllan do Rosário; MARTELLI, Marlice Cruz; http://lattes.cnpq.br/1213009262936026
    Alumina is one of the most important oxides in the ceramic industry, being used mainly in the form of calcined alumina or fused applied, among other ways, as adsorbent material. In this work is a transition alumina production method from a mixture of gibbsite, from the Bayer process, gel and aluminum hydroxide, from the reaction of aluminum sulfate and ammonium hydroxide targeting the application as an adsorbent material for removing Cu2 + in aqueous solution. Adsorption conditions including contact time and pH were investigated. Assays were carried out at 30 ° C and 50 ° C, in which 1 g of alumina produced was subjected to contact with 100 ml of an aqueous solution containing Cu2 +. The concentrations of the aqueous solutions employed were 100, 200, 400, 800, 1600 and 2000 ppm copper sulphate solution. The characterization of copper sulfate solutions was performed in UV spectrophotometry and characterization of the material produced was carried out by XRD, EDX and BET surface area. Evaluated the contact time to achieve the adsorption equilibrium which is optimized time 15 min. The effect of pH on the adsorption shows that the adsorption temperature increases there is an increased pH compared with the pH of the initial solution of copper sulfate. The isotherms of Langmuir and Freundlich had satisfactory results for adsorption, and the Langmuir isotherm that better fits the adsorption data. Through the equilibrium isotherms it was found that the material produced has adsorption capacity for Cu2 + ion.
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    Análise experimental e numérica da fluidização para aplicações industriais
    (Universidade Federal do Pará, 2012-03) LOURENÇO, Reimar de Oliveira; MESQUITA, André Luiz Amarante; http://lattes.cnpq.br/1331279630816662; MACÊDO, Emanuel Negrão; http://lattes.cnpq.br/8718370108324505
    The gas-particle fluidized beds have great importance in the processing industry, due to have a good effect of mixing between the phases, and high rates of heat and mass transfer, requiring it to lower power consumption. Some typical examples of industrial applications of this equipment can be found in processes involving catalytic reactions, catalyst regeneration, or the combustion and coal of gasification. The understanding of the fluid dynamic behavior of this equipment is of fundamental importance for the fluidized bed can be adapted to new conditions. The literature reports several studies of fluidized bed, reporting varied contributions already incorporated the knowledge of the operation. The CFD (Computational Fluid Dynamics) tool has proved a good alternative for understanding the operation of this equipment. The use of multiphase granular Eulerian model together with the conservation equations of mass, energy and momentum for each of the phases present, has shown success when applied to fluidized beds. Overall, this work is to study the behavior of the fluid dynamic flow of glass beads and alumina in conventional fluidized bed type gas-solid, varying models Gidaspow, Syamlal-O’Brien and Wen-Yu, as well as Turbulence Models K-ε and RSM. More specifically, the work seeks to study the behavior of the fluid-dynamic equipment, by monitoring the most important fluid-dynamic parameters, among which we highlight the minimum fluidization velocity of the same, the pressure drop at minimum fluidization equipment, its porosity and expansion of the bed particles, also at minimum fluidization. Experimental tests were compared with numerical simulations using CFD (Computational Fluid Dynamics) tool, in which good agreement of the simulated results compared to experimental results.
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    Aproveitamento do rejeito de caulim na produção de alumina para cerâmica e sílica de baixa granulometria
    (Universidade Federal do Pará, 2000-11-29) FLORES, Silvia Maria Pereira; NEVES, Roberto de Freitas; http://lattes.cnpq.br/9559386620588673
    The Amazon region detains 10% of the world reserves of kaolim. Since the seventy's, two great amazonic beds of kaolim are explored, producing kaolim for paper cover. In the beneficiation process, it's generated an elevated volume of polluted industrial residue which is deposited in extensivas and onerous lagoons of sedimentation. Because of the residue is very voluminous, these lagoons become an environmental problem of great proportions, due the extensivas deforested areas used for their constructions ( Barata, 1998). In this work, are suggested altematives of economic utilization of this residue, which is constituted, mainly, by a suspension of the claymineral kaolinite, for the production of pozolane, aluminium sulphate, the synthesis of the ammonium alum and alumina for ceramics utilization. The methodology constitutes in the drying and the calcination of the residue, followed by the extraction of the AI retained by the acid lixiviation H2SO4 ) followed by the ammonium alum crystallisation, for the reaction with the concentrated NH4OH, by means of pH control, and later calcination at 1200°C, getting a-Al2O3, with no sodium and Iow granulometry. From the aluminas obtained, are made bodies of proof smashed and sintered at 1600°C, to the determination of the ceramics properties, which are compared to one of the commercial alumina. After the acid lixiviation for the AI extraction, results as an insoluble material, an amorphous silica, for which it is suggested, as an additional contribution, an economic application, using it as artificial pozolane in building portland cement, making mechanics tests for the evaluation of its performance. The material that were used and synthesized were characterized throught the use of the X ray diffraction, eletronic scanning microscopy, the infra-red spectroscopy, thermogravimetry, differential thermic analisys, particle size analysis, specific area BET, porosity, chemical analisys throught umid means and throught X ray fluorescence.
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    Confecção de discos de desbaste a partir de AI2O3 e pó de vidro
    (Universidade Federal do Pará, 2009) OLIVEIRA, Rosane Felice de; DIAS, Carmen Gilda Barroso Tavares; http://lattes.cnpq.br/2113791118142177
    This article describes the development of abrasive and cutting disks made of alumina and waste glass powder to apply in cutting tools. These disk mills are used to micromize rigid post-consumed thermoplastics and let its use in a lot of recycling process, as rotomolding. This cutting disk uses glass powder as a fluxing agent and poly(ethylene terephthalate) post-consumed to give a plastic behavior to the powder, making it easier to fill in the mold. The amounts of glass powder were analyzed from previous studies with different minerals, as diopside and feldspar, since the studies with waste glass powder substituting natural minerals are recent. The development of the disks occurs in two steps. The first one is the homogeneization of the compounds with the calculated amounts. Afterwards it's pressed and taken to the mufla to get the percolation of the resin and its complete degradation up to a temperature of 900oC, pre-sintering and soften the silicates. After getting these green composites, it happens the second and final step, when the disks are sintered to decrease the porosity and improve its strength, followed by a superficial finish and cutting tests.
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    Desacidificação de frações destiladas de produto líquido orgânico do craqueamento termo-catalítico de óleos vegetais via adsorção em y-alumina e lama vermelha ativada
    (Universidade Federal do Pará, 2015-04-16) COSTA, Karen Marcela Barros da; BORGES, Luiz Eduardo Pizarro; http://lattes.cnpq.br/8756886156388456; MACHADO, Nelio Teixeira; http://lattes.cnpq.br/5698208558551065
    This paper studied the adsorption of residual free fatty acids (carboxylic acids) present in distilled fractions from the Liquid Organic Product (PLO) obtained by thermal catalytic cracking of vegetable oil. The objective was to deacidification of distilled fractions obtained from the distillation of the PLO. The experiments were performed using different distilled fractions using three different adsorbents, y-Alumina, Red Mud Thermally activated (400 °C) and Red mud chemically activated with solutions of HCl in different concentrations (0.25, 1 and 2M). The adsorbent capacity relative to adsorption of free fatty acids was evaluated by means of kinetic studies, measuring the change in concentration of free fatty acids present before and after adsorption by determining the Acid Number. The results indicated that increasing the initial concentration of acids decreases the adsorption capacity of the adsorbent, showing that the process is less effective at higher concentrations. For experiments with different percentages of adsorbents seen that when using 0.5% adsorbent to obtain greater efficiency in the removal of fatty acids, which decreases with increasing percentage of adsorbent. The most efficient adsorbent was red mud activated with 1M HCl, which was obtained a reduction of 98% of the fatty acids to a sample with an initial acid number of 4 mg KOH/g. Mathematical modeling indicated that the kinetic model that best represents the process was the Pseudo Second- Order. Therefore, the results show that the adsorbents used are mostly effective in the removal of free fatty acids and the initial concentration of acids in the sample has a direct effect on the performance of adsorption thereof.
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    Desenvolvimento de unidade piloto de transferência de massa gás/líquido: redução da reatividade do resíduo da indústria de alumina através da reação com gases de combustão
    (Universidade Federal do Pará, 2013-02) VENANCIO, Luis Carlos Alves; SOUZA, José Antônio da Silva; http://lattes.cnpq.br/6157348947425968; MACÊDO, Emanuel Negrão; http://lattes.cnpq.br/8718370108324505
    The bauxite refining using the Bayer process produces 0.7 to 2.0 tons of the residue known as red mud and about 1.0 ton of CO2 for each ton of alumina produced. The bauxite residue, although not particularly toxic, poses risks to the environment due to its large volume and reactivity. According to the latest technology, part of the moisture is removed and it is stacked on sealed areas specially constructed. More than 95% of the bauxite residue that has been produced (2.6 Bt until 2007) was discarded, especially in ponds on land. This thesis shows the design, construction and operation of a pilot scale gas liquid mass transfer unity with the objective of testing the reduction of the reactivity of the bauxite residue through a reaction with flue gas. As an additional gain, there is a reduction of carbon dioxide and sulfur dioxide emissions. This unity, with three reactors, was designed in order to consume minimal power, process the effluent as efficiently as possible and minimize the investment cost. Twenty-five experiments were realized with duration from 80 to 520 minutes each. The gases were analyzed at the entry and exit with electrochemical cells and non-dispersive infrared sensors. The pH was monitored during and after the reaction in order to evaluate the short and long-term results as well as the stability of the reactions. It was demonstrated the viability of reacting the bauxite residue with the flue gas from the refinery without previous processing with the stabilization pH reaching 10.5.
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    Estudo cinético e das isotermas de adsorção dos óleos de palma (Elaes guineensis, Jacq.) e andiroba (Carapa guianensis, Aubl.) em y-alumina e modelagem da dessorção com dióxido de carbono supercrítico
    (Universidade Federal do Pará, 2013-11-08) AMARAL, Anderson Rocha; MACHADO, Nelio Teixeira; http://lattes.cnpq.br/5698208558551065
    In this work, the variables of the batch adsorption process of palm (Elaeis guineensis, Jacq.) and andiroba (Carapa guianensis, Aubl.) vegetables oils on thermally activated alumina at 723,15 K and 923,15 K (y-alumina) has been investigated by analyzing the influence of temperature, time, mass of vegetable oil, mass of adsorbent on the adsorbent capacity. A kinetic model of second-order was proposed to modeling the adsorption capacity of free fatty acids (FFA). Capacity results of FFA of the crude palm oil on y-alumina AG.450 at 328.15 K and of the crude andiroba oil on y-alumina AG.650 at 323.15 K were obtained from the consecutive adsorption experiments and adjusted by isotherms of Langmuir e BET. The transfer mass model of TAN & LIOU (1989) was used to modeling the kinetic desorption of the palm oil from y-alumina AG.650 and of the andiroba oil on y-alumina AG.450 with supercritical carbon dioxide, evaluating the yields, errors, correlation coefficients and the residues of the desorbed oil mass versus predicted by the model.The study of the variables influence, over the adsorption capacity, presented negative correlation (with exponential behavior) to the variable mass of oil. The adsorbent mass influence, presented a positive correlation (with a linear behavior) and the temperature increase is favorable to the adsorption process. The total reduction of the FFA after three consecutive adsorptions of the crude palm oil on y-alumina AG.450 and after four consecutive adsorptions on -alumina AG.650 with andiroba oil, were 21.07 % and 40.29 %, respectively. The modeling of the FFA capacity to the palm oil with Langmuir model, presented a high experimental data prediction ability (R² = 0.9610), as well as to the andiroba oil with the BET model, which presented a high adjustment (R² = 0.9140). Tan & Liou model evidenced high prediction capacity of the desorption oil mass from γ-alumina for all experiments, minimum correlation coefficient of 0.9230 and magnitude residues of 10-1 grams. The yields, based on adsorbate initial mass, of the palm oil desorbed from y-alumina AG.650 at 20 MPa up to 30 MPa and 323.15 K up to 328.15 K were 28.880 % up to 34.563 %, while to the andiroba oil on y-alumina AG.450 at 15 MPa up to 25 MPa at 323.15 K were 14.108 % up to 27.972 %. The yields results shows that the increase of pressure and temperature are favorable to the supercritical desorption.
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    Estudo do processo de craqueamento termocatalítico do óleo de palma (Elaeis guineensis) com lama vermelha calcinada e alumina ativada em reatores de bancada e batelada
    (Universidade Federal do Pará, 2015-05-29) LOURENÇO, Rafael Martins; BORGES, Luiz Eduardo Pizarro; http://lattes.cnpq.br/8756886156388456; MACHADO, Nelio Teixeira; http://lattes.cnpq.br/5698208558551065
    In the present work was to study the thermal catalytic cracking process palm oil for biofuel production. In the development of this study were performed in crackings Bench and Semipilot. Initially, basic catalysts in cracking tests were performed (Red Mud; Red Mud Calcined at 550 ° C; Red Mud Calcined at 800C; Red Mud Calcined at 1000 ° C; Activated Alumina (AA) with NaOH 20% solution and Activated Alumina (AA) NaOH solution 30%) and acid (not activated alumina) in bench scale using as raw palm oil. Before the mentioned catalysts are used in thermal catalytics crackings, they were subjected to the following tests: Fourier Transform Infrared (FT-IR); Scanning Electron Microscopy (SEM); X-ray Diffraction (XRD) and BET in order to characterize them. The results of the bench scale showed that the cracked products Gross (PCB's) achieved in thermal catalytics oil crackings using as a catalyst 15% Red Mud Calcined at 800 ° C and 15% AA by NaOH 20% solution, had a significant reduction in their Acidity Index (IA's) compared to the IA's of heat and thermal catalytics crackings used with other catalysts. In Semipilot Scale the thermal catalytics crackings were developed with the best results obtained, Bench Scale, between the Red Mud’s Calcined or not in different concentrations (15% of Red Mud Calcined 800 ° C) and between the Activated Aluminas or not at various concentrations (AA with 15% NaOH solution at 20%) compared to IA's, in addition to the thermal cracking which was also reproduced on the scale. Some of the products obtained in Semipilot Scale was submitted to distillation in Bench Scale to obtain fractions corresponding to the tracks: gasoline, kerosene, light diesel and heavy diesel. The RMN analysis of 13C, held on the heat crackings and diesel thermal catalytic with 15% Red Mud Calcined at 800 °C proves that they are basically formed from long chain fatty acids. Moreover, the GC-MS performed in the cut of gasoline range (40 °C- 175 °C) showed that the three gasolines analyzed showed the formation of paraffinic hydrocarbons, olefinic and naphthenic.
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    Estudo geofísico para a caracterização geológica e hidrogeológica da subsuperfície rasa em área de deposição de rejeitos sólidos no município de Barcarena-PA
    (Universidade Federal do Pará, 2002) NEVES, Ana Paula Vilas Boas; LUIZ, José Gouvêa; http://lattes.cnpq.br/8676530374310847
    This geophysical study was carried out in the ALBRAS Solid Refuse Deposition Area located in Barcarena, State of Pará. The results allowed to characterize the subsurface, giving information on the geological layers and hidrogeological parameters like direction and velocity of underground flow. Three geophysical methods were used in the study: Spontaneous potential, dc-resistivity, and electromagnetic (slingram). During the study, an experiment of infiltration of salty water in the ground was performed and monitored through electrical imaging. Spontaneous potential gave information on the direction of local underground flow of water. Electrical imaging allowed to estimate the velocity and the direction of underground flow along the imaging profile. The models obtained from the inversion of vertical electrical sounding apparent resistivity data showed a good correlation with gamma ray logging run in wells in the studied area. The interpreted resitivity and thickness of the models provided detailing for the shallow lithological units. Analysis of electromagnetic data on profiles, soundings, and contouring maps lead to the identification of conductive zones (clayed material) and resistive zones (sandy material). Besides, a good correlation among 14080 Hz electromagnetic contouring map and spontaneous potential map was observed.
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    Interação CFD-DEM em fluidização: aplicação para o setor mineral
    (Universidade Federal do Pará, 2013) CASTELO BRANCO JÚNIOR, Alan Mota; VAZ, Jerson Rogério Pinheiro; http://lattes.cnpq.br/1623983294183975; MESQUITA, André Luiz Amarante; http://lattes.cnpq.br/1331279630816662
    The particle fluidization process is widely used in the industry, mainly due to the high heat and mass transfer rates between the phases. The coupling between the Computational Fluid Dynamics (CFD) and the Discrete Element Method (DEM) has become attractive for the simulation of fluidization, because in this case the particles movement is analyzed in a more direct way than in other types of approaches. The main problem with the CFD-DEM coupling is the high demand for computational capacity in order to track the movement of all the particles in the system, what it leads to the use of some strategies to reduce the simulation time which in case of incorrect usage can prejudice the results. The present work deals with the application of the CFD-DEM coupling in the analysis of alumina fluidization, which is an important problem for the mineral sector. It were analyzed several parameters capable of influencing the results and the simulation time like the time steps, the drag models, the particle size distribution, the spring constant, the usage of representative particles bigger than the actual particles, etc. The DEM model used was the Linear Spring Dashpot model (LSD). All the simulations were carried out with the software ANSYS FLUENT 14.5 and the results obtained were compared with experimental data and the data available in the literature. These results allowed to verify the capability of the Linear Spring Dashpot Model for predicting the global behavior of alumina beds and reducing the simulation time, since the model parameters are defined adequately.
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    Preparation of refractory calcium aluminate cement using the sonochemical process
    (2013-08) LOURENÇO, Rafaela Roberta; ANGÉLICA, Rômulo Simões; RODRIGUES, José de Anchieta
    Calcium aluminate cements (CAC) were prepared using the sonochemical process, followed by heat treatment. A study was made of the action of ultrasonic waves and the influence of thermal treatment conditions on two initial molar compositions of 1:1 and 1:2 of calcia:alumina. The aqueous suspension containing the raw materials (A-50 alumina and CaO) was subjected to an ultrasonic bath, followed by drying and burning at 1000, 1200 and 1300 ºC. These cements were characterized by SEM, XRD and the mechanical strength was evaluated by splitting tensile tests, using commercial cement as a reference. Furthermore, the phases were semi-quantified using the Rietveld method. The results show that hydration and sonochemical action increased the reactivity of the raw materials during firing and that phase formation is dependent on the thermal treatment conditions. The CAC cements were obtained at temperatures at least 200 ºC lower than those used in conventional methods, indicating the potential of this route of synthesis.
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