999 resultados para Nuvem de partículas
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A batch of eighty-four coupons of low carbon steel were investigated at laboratory conditions under a corrosive, cavitative-corrosive (CO2) and corrosive-erosive (SiO2 + CO2) in an aqueous salt solution and two levels of temperature. The following measurements were made on Vickers (HV0,05, HV0,10, HV0,20) Microhardness tests at three levels of subsurface layer. A turbulent flow collided on the cylindrical sample, with and without mechanical stirring and gas bubbling, with and without fluid contamination by solid particles of SiO2, at two temperatures. Surface Roughness and Waviness, under two conditions "as received, after machining" and "after worn out", as well as gravimetric and electrochemical parameter were measured on the two opposite generatrices of each cylindrical sample, on the flow upstream (0°) and downstream (180°) by Profilometry, Mass Variation and Linear Polarization Resistance (LPR). The results of the Microhardness and Surface Texture of all coupons were subjected to statistical comparison, using the software Statgraphics® Centurion XVI, 95% statistical certainty, and significant differences were observed in some arrays of measurements. The corrosive wear rate measured by LPR and mass variation shown to be sensitive to the presence of bubbles and hydrodynamic fluctuations inside the cell, considering the temperature and contamination of corrosive fluid by solid particles. The main results of visual inspection relative to some topologies of the surface damages involving different mechanisms that were seen to give explanation for some fluctuations in wear rates of the steel experimentally investigated
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O gradiente térmico da superfície para o interior do sólido depende da taxa de colisões das partículas e da condutividade térmica do material utilizado. Quando um sólido é imerso em plasma, a transferência de energia ocorre por radiação e colisões das partículas sobre a superfície do material. Dependendo da taxa de colisões das particulas e da condutividade térmica do sólido existirão gradientes térmicos da superfície para o interior das amostras, ocorrendo picos térmicos na superficie, ou seja, o aquecimento pontual nas regiões de colisões. A fim de estudar esse efeito, amostras de aço rápido AISI M35 cujos valores de dureza são fortemente sensíveis à temperatura de revenimento, foram utilizadas como micro sensores térmicos. Amostras foram temperadas em forno resistivo e, em seguida, parte das mesmas foram revenidas em forno resistivo e a outra parte em plasma. A partir do gráfico da dureza (Hv) em função da temperatura (T) das amostras revenidas em forno resistivo foi possível obter uma função Hv(T) para determinação indireta do perfil térmico das amostras tratadas em plasma. As amostras foram revenidas em plasma utilizando temperatura de referência igual a 550 oC. Em seguida foi obtido o perfil de dureza dessas amostras ao longo da seção transversal e, subsequentemente, o perfil de temperatura. Verificou-se que amostras tratadas em plasma, ao contrário daquelas tratadas em forno resistivo, apresentaram gradiente de temperatura da superfície para o núcleo. Além disso, verificou-se que as amostras tratadas em configuração planar apresentaram gradientes térmicos inferiores àquelas tratadas em configuração cátodo oco, variando de 20 a 120 °C, respectivamente
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Thermal insulation is used to protect the heated or cooled surfaces by the low thermal conductivity materials. The rigid ricin polyurethane foams (PURM) are used for thermal insulation and depend on the type and concentration of blowing agent. Obtaining PURM occurs by the use of polyol, silicone, catalyst and blowing agent are pre -mixed, reacting with the isocyanate. The glass is reusable, returnable and recyclable heat insulating material, whose time of heat dissipation determines the degree of relaxation of its structure; and viscosity determines the conditions for fusion, operating temperatures, annealing, etc. The production of PURM composites with waste glass powder (PV) represents economical and renewable actions of manufacturing of thermal insulating materials. Based on these aspects, the study aimed to produce and characterize the PURM composites with PV, whose the mass percentages were 5, 10, 20, 30, 40 and 50 wt%. PURM was obtained commercially, while the PV was recycled from the tailings of the stoning process of a glassmaking; when the refining process was applied to obtain micrometer particles. The PURM + PV composites were studied taking into account the standard sample of pure PURM and the influence of the percentage of PV in this PURM matrix. The results of the chemical, physical and morphological characterization were discussed taking into account the difference in the microstructural morphology of the PURM+PV composites and the pure PURM, as well the results of the physicochemical, mechanical e thermophysical tests by values obtained of density, hardness, compressive strength, specific heat, thermal conductivity and diffusivity. In general, the structure of pure PURM showed large, elongated and regular pores, while PURM+PV composites showed irregular, small and rounded pores with shapeless cells. This may have contributed to reducing their mechanical strength, especially for PURM - PV50. The hardness and density were found to have a proportional relationship with the PV content on PURM matrix. The specific heat, thermal diffusivity and thermal conductivity showed proportional relationship to each other. So, this has been realized that the increasing the PV content on PURM matrix resulted in the rise of diffusivity and thermal conductivity and the decrease of the specific heat. However, the values obtained by the PURM composites were similar the values of pure PURM, mainly the PURM-PV5 and PURM-PV10. Therefore, these composites can be applied like thermal insulator; furthermore, their use could reduce the production costs and to preserve the environment
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Acerola (Malpighia emarginata D.C.) is a red fruit widely cultivated in Brazil, especially in the Northeastern region. Its increasing demand is attributed to its high ascorbic acid contents. Besides ascorbic acid, widely known by its health-benefit effects, acerola is rich in anthocyanins, which contribute for the antioxidant power of the fruit. Acerola processing produces a bright-red pomace, usually discarded. The further processing of this pomace, in order to explore its antioxidant compounds, could enhance acerola market value and rentability of its processing. Both ascorbic acid and anthocyanins are highly susceptible to degradation, that can be delayed by microencapsulation, which consists on packing particles (core) in an edible matrix (wall material). This work has been made with the purpose of producing a microencapsulated acerola pomace extract, which could be used by the food industry as a functional ingredient with antioxidant and coloring properties. Antioxidant compounds were recovered by pressing the pomace diluted in a solvent (a citric acid aqueous solution), by using a central composite design, with two variables: citric acid concentration in the solvent (0-2%), and solvent: pomace mass ratio (2:1-6:1). The acerola pomace extract was then microencapsulated by spray drying. A central composite design was adopted, with three variables: inlet temperature of the spray dryer (170o-200oC), wall material: acerola solids mass ratio (2:1-5:1), and degree of maltodextrin replacement by cashew tree gum as wall material (0-100%). The cashew tree gum was used because of its similarity to arabic gum, which is regarded as the wall material by excellence. The following conditions were considered as optimal for extraction of anthocyanins and ascorbic acid: solvent/pomace ratio, 5:1, and no citric acid in the solvent. 82.47% of the anthocyanins were recovered, as well as 83.22% of the ascorbic acid. Anthocyanin and ascorbic acid retentions were favored by lower inlet temperatures, higher wall material: acerola solids mass ratio and higher maltodextrin replacement by cashew tree gum, which was presented as a promising wall material. The more adequate microencapsulation conditions, based not only on retention of antioxidant compounds but also on physical properties of the final powder, were the following: inlet temperature, 185oC; wall material: acerola solids mass ratio, 5:1, and minimum degree of maltodextrin replacement by cashew tree gum, 50%
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O período de permanência do herbicida na água pode ser influenciado pelo fluxo da água nos reservatórios e pela adsorção a partículas de argilas em suspensão, bem como pela degradação luminosa e por microrganismos. Objetivou-se com este trabalho avaliar diferentes períodos de exposição a concentrações do herbicida diquat no controle de Egeria densa, Egeria najas e Ceratophyllum demersum. O delineamento experimental utilizado foi o inteiramente casualizado, com quatro repetições, em esquema fatorial 6 x 5, mais uma testemunha. Foram testados seis períodos de exposição das plantas (30, 60, 120, 240, 480 e 960 minutos) a cinco concentrações do herbicida diquat (0,075; 0,15; 0,3; 0,6; e 1,2 ppm produto comercial Reward 240 g L ¹). As avaliações de controle das plantas daninhas imersas foram visuais e, no final do experimento, foi avaliada a massa seca das plantas, para determinar a porcentagem de redução da biomassa. Observou-se que apenas 30 minutos de exposição das espécies imersas E. densa e C. demersum à concentração de 0,075 ppm foi suficiente para proporcionar redução da massa seca em ambas as espécies. Para controle de E. najas aos 7 DAA houve necessidade de um período maior que 120 minutos de exposição, considerando a mesma concentração do herbicida. Esses resultados evidenciam o potencial de uso do diquat no controle de plantas daninhas aquáticas imersas em locais que apresentam rápida renovação de água.
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Realizou-se um experimento em uma área de implantação da cultura do eucalipto no município de São Miguel Arcanjo-SP, com o objetivo de avaliar a eficácia da aplicação aérea de grânulos de argila como veículo dos herbicidas sulfentrazone e isoxaflutole, no controle de plantas daninhas. Foi realizada aplicação aérea dos herbicidas sulfentrazone, nas doses de 500 e 750 g i.a. ha-1, e isoxaflutole, nas doses de 150 e 225 g i.a. ha-1, utilizando-se como veículo grânulos de argila com densidade de 1,05 g cm ³, alta capacidade de absorção (24 mL 100 g-1), alta resistência ao desgaste e tamanho das partículas entre 500 mícrons e 1 mm. Também foram feitas aplicações via líquida dos mesmos herbicidas e doses com um pulverizador convencional, acoplado a um trator. Além desses tratamentos, foi mantida uma parcela testemunha, sem aplicação dos herbicidas. Nas parcelas experimentais foram semeadas as espécies de plantas daninhas Brachiaria decumbens, Ipomoea grandifolia, Merremia cissoides e Panicum maximum, sendo realizadas avaliações visuais de controle aos 75 e 110 dias após a aplicação. em geral, foram observados, nas plantas daninhas avaliadas, resultados de controle semelhantes ou superiores para a aplicação aérea (via grânulos) até 75 DAA e superiores para essa modalidade de aplicação aos 110 DAA, indicando uma extensão no período do efeito do residual dos herbicidas estudados.
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As fontes de P mais utilizadas são os fosfatos solúveis em água, pela maior facilidade de liberação de P no solo. Entretanto, devido às características dos solos tropicais, grande parte desse P acaba adsorvida às partículas do solo, tornando-se indisponível. Os fosfatos reativos podem, inicialmente, liberar o P de maneira mais lenta; entretanto, a partir dos cultivos, este elemento poderá ser liberado de forma contínua, podendo haver menor fixação. O objetivo deste trabalho foi estudar a resposta à aplicação de duas fontes de P na cultura do triticale e o efeito residual dessa adubação no milheto, cultivados em semeadura direta, avaliando-se: fertilidade do solo; produção de matéria seca; teor e quantidade de P nas plantas e palha de cobertura; densidade de plantas; teor e quantidade de P nos grãos; e produtividade do triticale. O experimento foi conduzido em Latossolo Vermelho distroférrico. No mês de abril foram aplicados, a lanço, em superfície, três tratamentos: sem aplicação de P2O5; aplicação de 80 kg ha-1 de P2O5 de superfosfato triplo; e aplicação de 80 kg ha-1 de P2O5 de fosfato natural Arad. em seguida, semeou-se o triticale (X Triticosecale Wittmack), que foi conduzido até a colheita. em setembro, após a colheita do triticale, semeou-se o milheto (Pennisetum glaucum (L.) R. Brown), com o objetivo de elevar a cobertura de palha do solo, sendo ele dessecado no florescimento no mês de novembro. A aplicação de fosfato solúvel em superfície proporcionou lixiviação do P até a camada de 5-10 cm de profundidade do solo e melhor nutrição fosfatada do triticale cultivado em seguida, assim como maior produção de grãos. Apesar do aumento no teor de P disponível no solo, proporcionado pelo fosfato solúvel, a aplicação de P no triticale não redundou em elevação da produção de matéria seca, do teor e da quantidade de P na parte aérea do milheto cultivado em sequência.
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O objetivo deste trabalho foi avaliar a concentração e a absorção de macronutrientes em soja cultivada em subseqüência a sete espécies vegetais em solo com diferentes níveis de compactação. O experimento foi conduzido em vasos contendo amostras de um Latossolo Vermelho, textura franco-arenosa, com camada de 3,5 cm compactada até as densidades de 1,12, 1,36 e 1,60 Mg m³, em que se cultivou anteriormente aveia-preta, guandu, milheto, mucuna-preta, soja, sorgo granífero, tremoço azul, mantendo-se um tratamento sem planta (pousio). Essas espécies se desenvolveram por 37 a 39 dias, foram cortadas ao nível do solo, picadas em partículas de, aproximadamente, 3 cm, e deixadas sobre a superfície do vaso por 40 dias. As plantas foram colhidas 28 dias após a emergência. Avaliou-se a produção de matéria seca, concentração e acúmulo de macronutrientes na parte aérea das plantas. A compactação do solo em subsuperfície diminui a nutrição da soja. A nutrição da soja é beneficiada quando cultivada em sucessão a plantas de cobertura no solo. O pousio antecedendo a cultura da soja não é recomendado como meio de reduzir os efeitos da compactação do solo.
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Currently, studies in the area of polymeric microcapsules and nanocapsules and controlled release are considerably advanced. This work aims the study and development of microcapsules and nanocapsules from Chitosan/MDI, using a new technique of interfacial polycondensation combined to spontaneous emulsification, for encapsulation of BZ-3. It was firstly elaborated an experimental design of 23 of the particle in white without the presence of BZ-3 and Miglyol, where the variables were the concentrations of MDI, chitosan and solvent. Starting from the data supplied by the experimental design was chosen the experiment with smaller particle diameter and only added like this BZ-3 and Miglyol. The suspension containing concentrations of 6.25 mg/mL, 12.5 mg/mL, 18.75 mg/mL, 25 mg/mL of BZ-3 were prepared, nevertheless, during the storage time, these formulations presented drug precipitates in the suspensions of 18.75 mg/mL and 25 mg/mL of BZ-3. This apparition of precipitate was attributed to the diffusion of BZ-3 for the aqueous phase without any encapsulation, suggesting so the use of the smaller concentrations of the BZ-3. The suspension containing 6.25mg/mL of BZ3 presented average size of 1.47μm, zeta potential of 61 mV, pH 5.64 and this sample showed an amount of BZ-3 and drug entrapment of 100 %. The suspension containing 12.5mg/mL of BZ-3 presented average size of 1.76μm, zeta potential of 47.4 mV, pH 5.71 and this sample showed an amount of BZ-3 and drug entrapment of 100 %. Then, showing such important characteristics, these two formulations were chosen for futher continuity to the study. These formulations were also characterized by the morphology, FTIR, stability for Turbiscan, DSC and a study of controlled release of the BZ-3 was elaborated in different receiving means
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The nanostructures materials are characterized to have particle size smaller than 100 nm and could reach 1 nm. Due to the extremely reduced dimensions of the grains, the properties of these materials are significantly modified relatively when compared with the conventional materials. In the present work was accomplished a study and characterization of the molybdenum carbide, seeking obtain it with particles size in the nanometers order and evaluate its potential as catalyst in the reaction of partial methane oxidation. The method used for obtaining the molybdenum carbide was starting from the precursor ammonium heptamolybdate of that was developed in split into two oven, in reactor of fixed bed, with at a heating rate of 5ºC/min, in a flow of methane and hydrogen whose flow was of 15L/h with 5% of methane for all of the samples. The studied temperatures were 350, 500, 600, 650, 660, 675 and 700ºC and were conducted for 0, 60, 120 and 180 minutes, and the percent amount and the crystallite size of the intermediate phases were determined by the Rietveld refinement method. The carbide obtained at 660ºC for 3 hours of reaction showed the best results, 24 nm. Certain the best synthesis condition, a passivating study was accomplished, in these conditions, to verify the stability of the carbide when exposed to the air. The molybdenum carbide was characterized by SEM, TEM, elemental analysis, ICP-AES, TG in atmosphere of hydrogen and TPR. Through the elemental analysis and ICP-AES the presence carbon load was verified. TG in atmosphere of hydrogen proved that is necessary the passivating of the molybdenum carbide, because occur oxidation in room temperature. The catalytic test was accomplished in the plant of Fischer-Tropsch of CTGAS, that is composed of a reactor of fixed bed. Already the catalytic test showed that the carbide presents activity for partial oxidation, but the operational conditions should be adjusted to improve the conversion
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Os ensaios de largura de trabalho e uniformidade de distribuição são de difícil execução para o agricultor por exigirem equipamentos, recursos e métodos complexos. Portanto, este trabalho teve como objetivo avaliar coletores alternativos para tornar mais acessível a regulagem e a avaliação de distribuidores de fertilizantes sólidos a lanço. Foram utilizados quatro diferentes conjuntos de coletores: i) coletores construídos segundo a norma ISO 5690/1; ii) coletores de polietileno (bandejas plásticas) com tela de sombreamento para evitar o ricochete de material; iii) coletores formados por caixas de leite longa vida, e iv) coletores formados por vasos de polietileno (número 3,5). Também foram utilizados três diferentes distribuidores para as avaliações. Os coletores alternativos apresentaram maior retenção de partículas que os coletores normatizados. A largura efetiva de trabalho obtida para os coeficientes de variação de 12,5; 15; 17,5 e 20% variou entre os coletores nos diferentes percursos. O coletor que mais se assemelhou à norma foram os vasos de polietileno. Constatou-se que a altura dos coletores foi mais importante para sua eficiência do que a sua área de coleta.
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
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The generation of effluent from the finishing process in textile industry is a serious environmental problem and turned into an object of study in several scientific papers. Contamination with dyes and the presences of substances that are toxic to the environment characterize this difficult treatment effluent. Several processes have already been evaluated to remove and even degrade such pollutants are examples: coagulation-flocculation, biological treatment and advanced oxidative processes, but not yet sufficient to enable the recovery of dye or at least of the recovery agent. An alternative to this problem is the cloud point extraction that involves the application of nonionic surfactants at temperatures above the cloud point, making the water a weak solvent to the surfactant, providing the agglomeration of those molecules around the dyes molecules by affinity with the organic phase. After that, the formation of two phases occurred: the diluted one, poor in dye and surfactant, and the other one, coacervate, with higher concentrations of dye and surfactants than the other one. The later use of the coacervate as a dye and surfactant recycle shows the technical and economic viability of this process. In this paper, the cloud point extraction is used to remove the dye Reactive Blue from the water, using nonionic surfactant nonyl phenol with 9,5 etoxilations. The aim is to solubilize the dye molecules in surfactant, varying the concentration and temperature to study its effects. Evaluating the dye concentration in dilute phase after extraction, it is possible to analyze thermodynamic variables, build Langmuir isotherms, determine the behavior of the coacervate volume for a surfactant concentration and temperature, the distribution coefficient and the dye removal efficiency. The concentration of surfactant proved itself to be crucial to the success of the treatment. The results of removal efficiency reached values of 91,38%, 90,69%, 89,58%, 87,22% and 84,18% to temperatures of 65,0, 67,5, 70,0, 72,5 and 75,0°C, respectively, showing that the cloud point extraction is an efficient alternative for the treatment of wastewater containing Reactive Blue
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Environmental sustainability has become one of the topics of greatest interest in industry, mainly due to effluent generation. Phenols are found in many industries effluents, these industries might be refineries, coal processing, pharmaceutical, plastics, paints and paper and pulp industries. Because phenolic compounds are toxic to humans and aquatic organisms, Federal Resolution CONAMA No. 430 of 13.05.2011 limits the maximum content of phenols, in 0.5 mg.L-1, for release in freshwater bodies. In the effluents treatment, the liquid-liquid extraction process is the most economical for the phenol recovery, because consumes little energy, but in most cases implements an organic solvent, and the use of it can cause some environmental problems due to the high toxicity of this compound. Because of this, exists a need for new methodologies, which aims to replace these solvents for biodegradable ones. Some literature studies demonstrate the feasibility of phenolic compounds removing from aqueous effluents, by biodegradable solvents. In this extraction kind called "Cloud Point Extraction" is used a nonionic surfactant as extracting agent of phenolic compounds. In order to optimize the phenol extraction process, this paper studies the mathematical modeling and optimization of extraction parameters and investigates the effect of the independent variables in the process. A 32 full factorial design has been done with operating temperature and surfactant concentration as independent variables and, parameters extraction: Volumetric fraction of coacervate phase, surfactant and residual concentration of phenol in dilute phase after separation phase and phenol extraction efficiency, as dependent variables. To achieve the objectives presented before, the work was carried out in five steps: (i) selection of some literature data, (ii) use of Box-Behnken model to find out mathematical models that describes the process of phenol extraction, (iii) Data analysis were performed using STATISTICA 7.0 and the analysis of variance was used to assess the model significance and prediction (iv) models optimization using the response surface method (v) Mathematical models validation using additional measures, from samples different from the ones used to construct the model. The results showed that the mathematical models found are able to calculate the effect of the surfactant concentration and the operating temperature in each extraction parameter studied, respecting the boundaries used. The models optimization allowed the achievement of consistent and applicable results in a simple and quick way leading to high efficiency in process operation.
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In this research, the drying process of acerola waste was investigated by using a spouted bed drier. The process was conducted using high density polyethylene inert particles with the objective of producing an ascorbic acid-rich final product. The fruit waste was ground and used to prepare different water-maltodextrin suspensions. Initially, fluidynamical experiments were conducted in order to evaluate the feeding effect on the spouted bed drier fluidynamics behavior. The experimental planning 23 + 3 was used to investigate the effect of the following variables: solids concentration, drying air temperature, intermittence time, production efficiency, solids retention and product losses by elutriation of fine particles on drier walls. The effect of selected independent variables on the drier stability was also evaluated based on a parameter defined as the ratio between the feed suspension volume and the total inert particles volume. Finally, the powder quality was verified in experiments with fixed feed flow and varying air drying temperature, drying air velocity and intermittence time. It was observed that the suspension interferes in the spouted bed drier fluidynamics behavior, and higher air flow is necessary to stabilize the drier. The suspension also promotes the expansion of the spouted bed diameter, decreases the solid circulation and favors the air distribution at the flush area. All variables interfere in the spouted bed performance, and the solids concentration has a major effect on the material retention and losses. The intermittence time also has great effect on the stability and material retention. When it comes to production efficiency, the main effect observed was the drying air temperature. First order models were well adjusted to retention and losses data. The acerola powder presented ascorbic acid levels around 600 to 700 mg/100g. Similar moisture and ascorbic acid levels were obtained for powders obtained by spouted bed and spray drier. However, the powder production efficiency of the spray drier was lower when compared to spouted bed drier. When it comes to energetic analysis, the spray drier process was superior. The results obtained for spouted bed drier are promising and highly dependent on the operational parameters chosen, but in general, it is inferred that this drying process is adequate for paste and suspension drying