957 resultados para Second-generation biodiesel


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Biodiesel production has increased over the last decade because of the benefits associated with this fuel, including renewability, domestic feedstock, lower toxicity, and biodegradability. From 2008, the use of beef tallow as a feedstock for biodiesel production in Brazil has increased in significance, representing the second largest source of biodiesel, after soybeans. However, the performance of biodiesel in cold weather conditions is worse than diesel because of deposition of insoluble at low temperatures, accelerating the plugging of fuel filters and injectors of the vehicle engine. Studies have been conducted on beef tallow biodiesel, mostly related to the properties of thermal and oxidative stability. However, few studies have described the nature of the precipitate formed and its influence on product quality. Research suggests that the cause of deposition is related to the nature of saturated esters and monoacylglycerols as inducing agents. This study monitored the levels of mono-, diand triacylglycerols, the oxidation stability and the cold filter plugging point (CFPP) in beef tallow biodiesel samples from two commercial producers in Brazil for a period of twelve months. Filtered precipitates were analyzed by comparative techniques of GCFID, HPLC-UV/VIS, HPLC-MS-IT-TOF and TG to verify the nature, using monopalmitin and monostearin as reference standards. The formation of precipitate reduced the levels of monoacylglycerols in the beef tallow biodiesel. GC-FID and LCMS- IT-TOF results confirmed the nature of the deposit as saturated monoacylglycerols, predominantly monostearin and monopalmitin as the second major component. Moreover the TG analysis of the residue indicated similar thermal decomposition of the reference standards. The precipitate did not affect the oxidation stability of beef tallow biodiesel and the CFPP characteristic of blends up B60. However, the presence of iron reduced significantly the oxidation stability of biodiesel

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Biodiesel production has increased over the last decade because of the benefits associated with this fuel, including renewability, domestic feedstock, lower toxicity, and biodegradability. From 2008, the use of beef tallow as a feedstock for biodiesel production in Brazil has increased in significance, representing the second largest source of biodiesel, after soybeans. However, the performance of biodiesel in cold weather conditions is worse than diesel because of deposition of insoluble at low temperatures, accelerating the plugging of fuel filters and injectors of the vehicle engine. Studies have been conducted on beef tallow biodiesel, mostly related to the properties of thermal and oxidative stability. However, few studies have described the nature of the precipitate formed and its influence on product quality. Research suggests that the cause of deposition is related to the nature of saturated esters and monoacylglycerols as inducing agents. This study monitored the levels of mono-, diand triacylglycerols, the oxidation stability and the cold filter plugging point (CFPP) in beef tallow biodiesel samples from two commercial producers in Brazil for a period of twelve months. Filtered precipitates were analyzed by comparative techniques of GCFID, HPLC-UV/VIS, HPLC-MS-IT-TOF and TG to verify the nature, using monopalmitin and monostearin as reference standards. The formation of precipitate reduced the levels of monoacylglycerols in the beef tallow biodiesel. GC-FID and LCMS- IT-TOF results confirmed the nature of the deposit as saturated monoacylglycerols, predominantly monostearin and monopalmitin as the second major component. Moreover the TG analysis of the residue indicated similar thermal decomposition of the reference standards. The precipitate did not affect the oxidation stability of beef tallow biodiesel and the CFPP characteristic of blends up B60. However, the presence of iron reduced significantly the oxidation stability of biodiesel

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Biodiesel is a fuel made up by mono-alkyl-esters of long chain fatty acids, derived from vegetable oils or animal fat. This fuel can be used in compression ignition engines for automotive propulsion or energy generation, as a partial or total substitute of fossil diesel fuel. Biodiesel can be processed from different mechanisms. Transesterification is the most common process for obtaining biodiesel, in which an ester compound reacts with an alcohol to form a new ester and a new alcohol. These reactions are normally catalyzed by the addition of an acid or a base. Initially sunflower, castor and soybean oil physicochemical properties are determined according to standard test methods, to evaluate if they had favorable conditions for use as raw material in the transesterification reaction. Sunflower, castor and soybean biodiesel were obtained by the methylic transesterification route in the presence of KOH and presented a yield above 93% m/m. The sunflower/castor and soybean/castor blends were studied with the aim of evaluating the thermal and oxidative stability of the biofuels. The biodiesel and blends were characterized by acid value, iodine value, density, flash point, sulfur content, and content of methanol and esters by gas chromatography (GC). Also studies of thermal and oxidative stability by Thermogravimetry (TG), Differential Scanning Calorimetry High Pressure (P-DSC) and dynamic method exothermic and Rancimat were carried out. Biodiesel sunflower and soybean are presented according to the specifications established by the Resolution ANP no 7/2008. Biodiesel from castor oil, as expected, showed a high density and kinematic viscosity. For the blends studied, the concentration of castor biodiesel to increased the density, kinematic viscosity and flash point. The addition of castor biodiesel as antioxidant in sunflower and soybean biodiesels is promising, for a significant improvement in resistance to autoxidation and therefore on its oxidative stability. The blends showed that compliance with the requirements of the ANP have been included in the range of 20-40%. This form may be used as a partial substitute of fossil diesel

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We obtain a solution for the gluon propagador in Landau gauge within two distinct approximations for the Schwinger-Dyson equations (SIDE). The first, named Mandelstam's approximation, consist in neglecting all contributions that come from fermions and ghosts fields while in the second, the ghosts fields are taken into account leading to a coupled system of integral equations. In both cases we show that a dynamical mass for the gluon propagator can arise as a solution.

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O Brasil, terceiro maior produtor de biodiesel do mundo e terceiro maior produtor mundial de frango, pode incrementar, na sua matriz energética, o uso de óleo oriundo de aves como alternativa aos combustíveis fósseis e à redução da dependência do óleo de soja para esse fim. O país dispõe de mais de 350 milhões de litros de óleo de frango por ano. Considerando a aplicação dos combustíveis alternativos para os motores a diesel, em máquinas agrícolas, o trabalho teve por objetivo avaliar o desempenho do motor de um trator agrícola de 53kW acoplado pela TDP em bancada dinamométrica, operando com biodiesel metílico de óleo de frango e misturas com óleo diesel, sendo: B5 (testemunha), B20, B40, B60, B80 e B100. Avaliaram-se a potência, o torque, a reserva de torque, o consumo de combustível, o consumo de energia e a eficiência térmica do motor. O ensaio foi instalado com delineamento inteiramente casualizado (DIC) em esquema fatorial com seis tratamentos. Os resultados foram submetidos à análise de variância e as médias ajustadas por equações de regressão. Foram observadas perdas na geração de potência e torque, aumento no consumo de combustível, redução do consumo energético e melhoria na eficiência térmica do motor, de acordo com o aumento da proporção de biodiesel na mistura.

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Lead toxicity was studied in rats exposed from conception until weaning and assessed by monitoring offspring behavior in both the open field and elevated plus maze and by determining tissue lead in an assessment schedule extended to first (F1) and second (F2) generations. Dams utilized for the F1 generation were submitted to 750 ppm of lead (acetate) in drinking water during pregnancy and lactation. For F1 pups, behavioral alterations were not detected in the elevated plus maze, while in the open field, spontaneous locomotor activity as well as time of both grooming and rearing increased, while freezing time decreased in 30- and 90-day-old rats. Lead content was higher in tissues of 1- and 30-day-old pups. However, in 90-day-old rats, lead was detected only in the femur. F2 generation was lead-free but still presented alterations in both locomotor activity and grooming in 30- and 90-day-old pups. It appears that developmental lead exposure may cause behavioral effects during the developmental stage of the F1 generation, which remains throughout the animal's adult life as a sequel, regardless of lead accumulation, and is extended to the F2 generation of rats. (C) 2001 Elsevier B.V. All rights reserved.

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This paper presents a methodology for the study of a molten carbonate fuel cell co-generation system. This system is applied to a dairy industry of medium size that typically demands 2100 kW of electricity, 8500 kg/h of saturated steam (P = 1.08 MPa) and 2725 kW of cold water production. Depending on the associated recuperation equipment, the co-generation system permits the recovery of waste heat, which can be used for the production of steam, hot and cold water, hot and cold air. In this study, a comparison is made between two configurations of fuel cell co-generation systems (FCCS). The plant performance has been evaluated on the basis of fuel utilisation efficiency and each system component evaluated on the basis of second law efficiency. The energy analysis presented shows a fuel utilisation efficiency of about 87% and exergy analysis shows that the irreversibilities in the combustion chamber of the plant are significant. Further, the payback period estimated for the fuel cell investment between US$ 1000 and US$ 1500/k-W is about 3 and 6 years, respectively. (C) 2002 Elsevier B.V. B.V. All rights reserved.

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We discuss the solutions obtained for the gluon propagador in Landau gauge within two distinct approximations for the Schwinger-Dyson equations (SDE). The first, named Mandelstam's approximation, consist in neglecting all contributions that come from fermions and ghosts fields while in the second, the ghosts fields are taken into account leading to a coupled system of integral equations. In both cases we show that a dynamical mass for the gluon propagator can arise as a solution. © 2005 American Institute of Physics.

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This paper presents two discrete sliding mode control (SMC) design. The first one is a discrete-time SMC design that doesn't take into account the time-delay. The second one is a discrete-time SMC design, which takes in consideration the time-delay. The proposed techniques aim at the accomplishment simplicity and robustness for an uncertainty class. Simulations results are shown and the effectiveness of the used techniques is analyzed. © 2006 IEEE.

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This work developed a methodology that uses the thermoeconomic functional diagram applied for allocating the cost of products produced by a biodiesel plant. The first part of this work discusses some definitions of exergy and thermoeconomy, with a detailed description of the biodiesel plant studied, identification of the system functions through Physical Diagram, calculation of the irreversibilities of the plant, construction of the Thermoeconomic Functional Diagram and determination of the expressions for the plant's exergetic functions. In order to calculate the exergetic increments and the physical exergy of certain flows in each step, the Chemical Engineering Simulation Software HYSYS 3.2 was used. The equipments that have the highest irreversibilities in the plant were identified after the exergy calculation. It was also found that the lowest irreversibility in the system refers to the process with a molar ratio of 6:1 and a reaction temperature of 60 °C in the transesterification process. In the second part of this work (Part II), it was calculated the thermoeconomic cost of producing biodiesel and related products, including the costs of carbon credits for the CO2 that is not released into the atmosphere, when a percentage of biodiesel is added to the petroleum diesel used by Brazil's internal diesel fleet (case study). © 2013 Elsevier Ltd. All rights reserved.

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The effects of soybean and castorbean meals were evaluated separately, and in combinations at different ratios, as substrates for lipase production by Botryosphaeria ribis EC-01 in submerged fermentation using only distilled water. The addition of glycerol analytical grade (AG) and glycerol crude (CG) to soybean and castorbean meals separately and in combination, were also examined for lipase production. Glycerol-AG increased enzyme production, whereas glycerol-CG decreased it. A 24 factorial design was developed to determine the best concentrations of soybean meal, castorbean meal, glycerol-AG, and KH2PO4 to optimize lipase production by B. ribis EC-01. Soybean meal and glycerol-AG had a significant effect on lipase production, whereas castorbean meal did not. A second treatment (22 factorial design central composite) was developed, and optimal lipase production (4,820 U/g of dry solids content (ds)) was obtained when B. ribis EC-01 was grown on 0.5 % (w/v) soybean meal and 5.2 % (v/v) glycerol in distilled water, which was in agreement with the predicted value (4,892 U/g ds) calculated by the model. The unitary cost of lipase production determined under the optimized conditions developed ranged from US$0.42 to 0.44 based on nutrient costs. The fungal lipase was immobilized onto Celite and showed high thermal stability and was used for transesterification of soybean oil in methanol (1:3) resulting in 36 % of fatty acyl alkyl ester content. The apparent K m and V max were determined and were 1.86 mM and 14.29 μmol min -1 mg-1, respectively. © 2013 Springer Science+Business Media New York.

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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

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The potential of natural and heat-treated Macauba palm cake as adsorbent for the removal of Methylene Blue (MB) and Congo Red (CR) from solution has been investigated. Equilibrium adsorption was attained in <7 h and the process was favored at pH 5.0 for MB and pH 6.5 for CR with an adsorbent (g):adsorbate (mL) ratio of 1:200 and an initial concentration of adsorbate of 25 mg L−1. The maximum adsorption capacities of the natural and heat-treated materials were, respectively, 25.80 and 32.30 mg g−1 for MB, and 32.00 and 20.30 mg g−1 for CR. The isotherm model proposed by Sips represented most adequately the adsorption of MB and CR. The adsorptions of the dyes were best described in terms of a pseudo second-order reaction. Thermodynamic parameters such as ΔHo, ΔSo and ΔGo were calculated. The adsorption process was found to be endothermic and spontaneous. Macauba palm cake is adequate for the removal of waste dye from industrial effluents by virtue of its abundance, low cost and efficiency of adsorption.

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Os extremos climáticos impactam negativamente o agronegócio brasileiro e ameaçam o desenvolvimento das comunidades rurais que são altamente dos recursos naturais. Por isso é fundamental estudar-se a cadeia produtiva de dendê (Elais guineensis Jacq.) de óleo diante de futuros riscos climáticos, devido o Estado do Pará ser o maior produtor nacional de dendê e a cadeia ser estruturada com a integração da agricultura familiar á cadeia agrícola. O objetivo desta pesquisa foi de analisar as vulnerabilidades dos agricultores familiares da Comunidade Águas Pretas do município de Moju, Estado do Pará, inseridos na cadeia de produção de biodiesel de dendê, diante dos extremos de precipitação. A pesquisa foi desenvolvida em dois momentos: o primeiro analisou os extremos climáticos da série temporal de precipitação de 1981 a 2009 empregando o método descritivo e dos quantis, e o segundo momento analisou a vulnerabilidade dos agricultores através de variáveis/indicadores de desvantagem socioeconômica, tecnológica e de percepção, que representavam situação de vulnerabilidade. Para a identificação de vulnerabilidade dos agricultores foi utilizado a análise fatorial por componentes principais, a elaboração de índices de vulnerabilidade climática e a análise agrupamento, onde foram alocados 22 agricultores em cinco categorias de classificação rédefinidas. Os resultados obtidos mostraram que a ocorrência de extremos muito secos e muito chuvosos na série de dados entre os anos de 1981 a 2009 do município de Moju (PA). O risco climático identificado no município representa grande ameaça à produção de dendê, uma vez que os impactos dos extremos de precipitação sobre a planta vão desde distúrbios nas fases de desenvolvimento até, a redução parcial e total da produção dos cachos de dendê. Estes impactos em longo prazo, afeta diretamente os agricultores familiares que são dependentes da venda exclusiva dos cachos de dendê á agroindústria, assim como compromete aos objetivos de inclusão social e produção de energia renovável do Programa de biodiesel. Os agricultores familiares da comunidade Águas Pretas integrados a cadeia de produção de biodiesel de dendê reagiram de formas distintas, considerando fatores socioeconômico, tecnológico e de percepção, sendo distribuídos em cinco categorias de vulnerabilidade (alta, média alta, média, média baixa e baixa). Os grupos de vulnerabilidade de maior interesse na pesquisa foram de alta e baixa vulnerabilidade, correspondentes a 14% (3 agricultores) e 18% (agricultores), respectivamente, do total de agricultores entrevistados. O grupo de alta vulnerabilidade foi caracterizado por agricultores que utilizaram com baixa eficiência a maior parte das variáveis de desvantagens, indicando dificuldades de competir e adaptar-se, em caso de extremos climáticos. No grupo de baixa vulnerabilidade foi caracterizado por agricultores que usam com eficiência todas as macrovariáveis estudadas, mostrando vantagens socioeconômicas, tecnológicas e de percepção. Este grupo se mostrou mais adaptado em caso de extremos de clima, dentro da cadeia de biodiesel, podendo ser parâmetros para elaborações de estratégias de adaptação local. A percepção do risco e os fatores levantados mostraram-se ser um forte recurso para analisar a situação de vulnerabilidade dos agricultores locais. A percepção do agricultor é orientada segundo suas convicções e experiências diárias, sendo determinantes para elaboração de estratégias adaptativas para enfrentar extremos climáticos.

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Neste trabalho investigaram-se de forma sistemática as variáveis operacionais de processo envolvidas nas operações de separação aplicadas no pré-tratamento do óleo de palma bruto (Elaeis guineensis, jacq) e na purificação do biodiesel produzido via transesterificação etanólica utilizando NaOH como catalisador, em escala de laboratório. Na etapa de pré-tratamento foram investigados os processos de Filtração e Decantação, sendo a filtração do produto da neutralização realizada a 40ºC, 50ºC e 60ºC, enquanto que na Decantação, avaliaram-se as temperaturas de 40ºC e 60ºC em 120 minutos. Em seguida, investigou-se a influência do tempo de decantação de 60, 90 e 120 minutos no processo de lavagem do óleo neutralizado a 40ºC e 60ºC, seguida de Desidratação sob vácuo a 80ºC, tendo sido investigado nesta etapa a influência da pressão. Após a reação de transesterificação, avaliou-se o processo de Evaporação do etanol em excesso, onde em um primeiro momento investigou-se as temperaturas de 70 e 80ºC, mantendo-se o tempo de evaporação constante em 20 minutos, no intervalo de 613,30 a 80,00 mbar, e em um segundo momento analisou-se as pressões de operação de 480,00 e 346,66 mbar. Em seguida, investigou-se a influência do tempo no processo de decantação da fase rica em glicerol a 70ºC, para tempos de 60, 120 e 180 minutos. Sendo realizada a lavagem da fase rica em ésteres a 70ºC, para os tempos de 60, 90 e 120 minutos de decantação da água residual. Avaliou-se ainda a eficiência do processo de centrifugação da mistura biodiesel e glicerol a 60 e 70ºC a 2000 rpm, para um tempo de 15 minutos. Em seguida, procedeu-se a lavagem da fase rica em ésteres com água a 60 e 70ºC, sendo a separação realizada via centrifugação a 60 e 70ºC. As fases ricas em ésteres, obtidas via decantação e centrifugação, foram submetidas à Desidratação sob vácuo, e caracterizadas em conformidade com as especificações da ANP. De acordo com os resultados experimentais, com base na qualidade do óleo neutro e rendimento do processo, observou-se que a Filtração a 50ºC gerou os melhores resultados para o pré-tratamento do óleo. Em relação à Evaporação do etanol, o melhor percentual de recuperação foi obtido a 80ºC e 346,6 mbar. Com relação à separação da fase ricas em ésteres e glicerol, o processo de Centrifugação a 60ºC gerou um biodiesel de melhor qualidade e maior rendimento. Observou-se ainda, a necessidade de uma segunda etapa de centrifugação de forma a minimizar a perdas de biodiesel na fase rica em glicerol.