829 resultados para Spray pyrolysis


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Experiments to evaluate the effect of in-season calcium (Ca) sprays on late-season peach (Prunus persica L. Batsch cv. Calrico) were carried out for a 2-year period. Calcium formulations (0.5% and 1.0% in 2008 and only 0.5% tested in 2009) supplied either as CaCl2 or Ca propionate in combination with two or three adjuvants (0.05% of the nonionic surfactants Tween 20 and Break Thru, and 0.5% carboxymethylcellulose, CMC) were sprayed four to five times over the growing season. Peach mesocarp and endocarp Ca concentrations were determined on a 15-day basis from the beginning of May until the end of June. Further tissue analyses were performed at harvest. A decreasing trend in fruit Ca concentrations over the growing season was always observed regardless of the Ca treatments. Both in 2008 and 2009, significant tissue Ca increments associated with the application of Ca-containing sprays in combination with adjuvants were only observed in June, which may be coincident with the period of pit hardening. In 2008, both at harvest and after cold storage, the total soluble-solids concentration (° Brix) of fruits supplied with Ca propionate (0.5% and 1.0% Ca) was always lower as compared to the rest of treatments. The application of multiple Ca-containing sprays increased firmness at harvest and after cold storage, especially when CaCl2 was the active ingredient used. Supplying the adjuvants Tween 20 and CMC increased fruit acidity both at harvest and after cold storage. Evaluation of the development of physiological disorders after cold storage (2 weeks at 0°C) indicated a lower susceptibility of Ca-treated fruits to internal browning. Fruits treated with multiple CaCl2-, CMC-, and Break Thru®-containing sprays during the growing season were significantly less prone to the development of chilling injuries as compared to untreated peaches.

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The EFDA-ITER programme for materials wants to develop new structural materials for future nuclear magnetic fusion reactors. In this context, special attention must be paid in the development of new composite materials that could support the hard working conditions of the nuclear fusion reactors: high temperature, high stresses, and high radiation.

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The group vaporization of a monodisperse fuel-spray jet discharging into a hot coflowing gaseous stream is investigated for steady flow by numerical and asymptotic methods with a two-continua formulation used for the description of the gas and liquid phases. The jet is assumed to be slender and laminar, as occurs when the Reynolds number is moderately large, so that the boundary-layer form of the conservation equations can be employed in the analysis. Two dimensionless parameters are found to control the flow structure, namely the spray dilution parameter 1, defined as the mass of liquid fuel per unit mass of gas in the spray stream, and the group vaporization parameter e, defined as the ratio of the characteristic time of spray evolution due to droplet vaporization to the characteristic diffusion time across the jet. It is observed that, for the small values of e often encountered in applications, vaporization occurs only in a thin layer separating the spray from the outer droplet-free stream. This regime of sheath vaporization, which is controlled by heat conduction, is amenable to a simplified asymptotic description, independent of ε,in which the location of the vaporization layer is determined numerically as a free boundary in a parabolic problem involving matching of the separate solutions in the external streams, with appropriate jump conditions obtained from analysis of the quasi-steady vaporization front. Separate consideration of dilute and dense sprays, corresponding, respectively, to the asymptotic limits λ<<1 and λ>>1, enables simplified descriptions to be obtained for the different flow variables, including explicit analytic expressions for the spray penetration distance.

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Conditions are identified under which analyses of laminar mixing layers can shed light on aspects of turbulent spray combustion. With this in mind, laminar spray-combustion models are formulated for both non-premixed and partially premixed systems. The laminar mixing layer separating a hot-air stream from a monodisperse spray carried by either an inert gas or air is investigated numerically and analytically in an effort to increase understanding of the ignition process leading to stabilization of high-speed spray combustion. The problem is formulated in an Eulerian framework, with the conservation equations written in the boundary-layer approximation and with a one-step Arrhenius model adopted for the chemistry description. The numerical integrations unveil two different types of ignition behaviour depending on the fuel availability in the reaction kernel, which in turn depends on the rates of droplet vaporization and fuel-vapour diffusion. When sufficient fuel is available near the hot boundary, as occurs when the thermochemical properties of heptane are employed for the fuel in the integrations, combustion is established through a precipitous temperature increase at a well-defined thermal-runaway location, a phenomenon that is amenable to a theoretical analysis based on activation-energy asymptotics, presented here, following earlier ideas developed in describing unsteady gaseous ignition in mixing layers. By way of contrast, when the amount of fuel vapour reaching the hot boundary is small, as is observed in the computations employing the thermochemical properties of methanol, the incipient chemical reaction gives rise to a slowly developing lean deflagration that consumes the available fuel as it propagates across the mixing layer towards the spray. The flame structure that develops downstream from the ignition point depends on the fuel considered and also on the spray carrier gas, with fuel sprays carried by air displaying either a lean deflagration bounding a region of distributed reaction or a distinct double-flame structure with a rich premixed flame on the spray side and a diffusion flame on the air side. Results are calculated for the distributions of mixture fraction and scalar dissipation rate across the mixing layer that reveal complexities that serve to identify differences between spray-flamelet and gaseous-flamelet problems.

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In typical liquid-fueled burners the fuel is injected as a high-velocity liquid jet that breaks up to form the spray. The initial heating and vaporization of the liquid fuel rely on the relatively large temperatures of the sourrounding gas, which may include hot combustion products and preheated air. The heat exchange between the liquid and the gas phases is enhanced by droplet dispersion arising from the turbulent motion. Chemical reaction takes place once molecular mixing between the fuel vapor and the oxidizer has occurred in mixing layers separating the spray flow from the hot air stream. Since in most applications the injection velocities are much larger than the premixed-flame propagation velocity, combustion stabilization relies on autoignition of the fuel-oxygen mixture, with the combustion stand-off distance being controlled by the interaction of turbulent transport, droplet heating and vaporization, and gas-phase chemical reactions. In this study, conditions are identified under which analyses of laminar flamelets canshed light on aspects of turbulent spray ignition. This study extends earlier fundamental work by Liñan & Crespo (1976) on ignition in gaseous mixing layers to ignition of sprays. Studies of laminar mixing layers have been found to be instrumental in developing un-derstanding of turbulent combustion (Peters 2000), including the ignition of turbulent gaseous diffusion flames (Mastorakos 2009). For the spray problem at hand, the configuration selected, shown in Figure 1, involves a coflow mixing layer formed between a stream of hot air moving at velocity UA and a monodisperse spray moving at velocity USUA. The boundary-layer approximation will be used below to describe the resulting sl ender flow, which exhibits different igniting behaviors depending on the characteristics of t he fuel. In this approximation, consideration of the case U A = U S enables laminar ignition distances to be related to ignition times of unstrained spray flamelets, thereby pro viding quantitative information of direct applicability in regions of low scala r dissipation-rate in turbulent reactive flows (see the discussion in pp. 181–186 of Peters (2000)) . This report is organized as follows. Effects of droplet dispersion dynamics on ignition of sprays in turbulent mixing layers are discussed in Section 2. The formulation f or ignition in laminar mixing layers is outlined in Sections 3 and 4. The results are presented in Section 5. In Section 6, the mixture-fraction field and associated scalar dissipat ion rates for spray ignition are discussed. Finally, some brief conclusions are drawn in Section 7.

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Sulphur compounds remaining in petroleum fractions from topping, hydroskimming or deep conversion processes are a growing concern for oil refiners since in the lapse of a few years the sulphur specification for motor fuels has dropped from 500 mg/kg to 10 mg/kg in most European countries. This increasingly stringent regulation has forced refineries to greatly improve their hydrodesulfurization units, increasing the desulfurization rates and thus consuming huge amounts of hydrogen.

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A indústria de alimentos está constantemente desenvolvendo produtos que fornecem, além de nutrientes, benefícios adicionais à saúde, tais como os enriquecidos com vitaminas. A vitamina D3 (colecalciferol) é sintetizada na pele durante a exposição da luz solar, controla a homeostase de cálcio e fósforo, metabolismo ósseo, pressão arterial e reabsorção renal de cálcio. O processo de microencapsulação vem sendo bastante aplicado em alimentos e um dos objetivos principais é o controle da liberação do agente ativo no momento e local desejado. A tecnologia de spray chilling é interessante para a microencapsulação de vitaminas lipossolúveis. O objetivo deste trabalho foi microencapsular vitamina D3, utilizando o método de spray chilling para a produção das micropartículas lipídicas sólidas (MLS). Para produção das MLS utilizou-se gordura vegetal com ponto de fusão em torno de 48 °C como carreador. Três tratamentos foram estabelecidos: sem aditivos (T1), com adição de 1% de cera de abelha (T2) e com 1% de lecitina de soja (T3). As micropartículas foram caracterizadas quanto à morfologia por microscopia eletrônica de varredura, tamanho médio por difração a laser, espectroscopia no infravermelho por transformada de Fourier (FTIR) e foi analisada a estabilidade da vitamina D3 durante o armazenamento a 10 e 25 °C, por meio de quantificações periódicas em cromatografia líquida de alta eficiência (CLAE). As micropartículas obtidas foram esféricas, semelhantes morfologicamente e com distribuição monocaudal de partículas. O tamanho médio das partículas variou em função dos seus ingredientes, sendo que as micropartículas produzidas apenas com vitamina e gordura foram menores em relação às demais (83,0% < 100 µm). A espectroscopia na região do infravermelho (FTIR) demonstrou que não ocorreu interação entre os ingredientes. A estabilidade da vitamina D3 encapsulada foi satisfatória ao longo de 65 dias com valores superiores a 87% para os três tratamentos e a temperatura apresentou influência na estabilidade. As MLS produzidas com cera apresentaram melhores resultados de estabilidade de vitamina D3 com valores de 90,18 ± 2,23 % após 65 dias de estocagem. Esses resultados são promissores e demostram a viabilidade da técnica de spray chilling na produção de MLS carregadas de vitamina D3, possibilitando uma futura aplicação em alimentos.

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O objetivo desse trabalho foi obter polpa de guavira desidratada por atomização, utilizando maltodextrina ou goma arábica como agentes carreadores. Inicialmente, avaliou-se a influência das condições de processo, temperatura do ar de secagem (130, 155 e 180) °C e vazão volumétrica da mistura (20 e 40) mL/min, o tipo e concentração de agente carreador (10 e 20) % nas características físicas, físico-químicas e atividade antioxidante do produto obtido. As propriedades analisadas foram umidade, atividade de água, higroscopicidade, solubilidade, cor, distribuição e tamanho médio de partículas, morfologia, compostos fenólicos totais e atividade antioxidante. A temperatura do ar de secagem e a vazão volumétrica de alimentação influenciaram significativamente todas as propriedades da guavira em pó. A umidade e atividade de água apresentaram os menores valores na temperatura intermediária, independentemente do tipo e concentração do carreador usado. A solubilidade das amostras adicionadas de maltodextrina foram superiores às amostras com goma arábica. O aumento da concentração de agente carreador, em geral, proporcionou um aumento no parâmetro L* e diminuição dos parâmetros a* e b*, tornando as amostras mais claras e reduzindo as tonalidades vermelha e amarela. A guavira em pó apresentou coloração próxima do amarelo e marrom, com grande variação nos parâmetros de cor C* e H* em função das diferentes condições de secagem. A distribuição do tamanho de partículas não teve um padrão definido e o tamanho médio das amostras com maltodextrina foram maiores do que as com goma arábica para a temperatura do ar a 130 °C. No entanto, para as outras temperaturas (155 e 180) °C não houve um comportamento específico do tamanho das partículas em função da vazão de alimentação, tipo e ou concentração de agente carreador. A análise de microscopia eletrônica de varredura permitiu observar que as partículas obtidas tanto com maltodextrina como goma arábica apresentaram formato esférico, superfície rugosa e com adesão de partículas menores nas de maior tamanho, sendo que a superfície das partículas com goma arábica também apresentaram concavidades. A atividade antioxidante foi superior quando utilizada a temperatura de secagem intermediária. A partir das condições selecionadas na primeira etapa (temperatura do ar de 155 °C, vazão volumétrica da mistura de 40 mL/min e 10% de maltodextrina ou goma arábica) a polpa de guavira em pó foi caracterizada quanto a temperatura de transição vítrea, as isotermas de adsorção e a estabilidade à estocagem do ácido ascórbico, compostos fenólicos totais e da atividade antioxidante da polpa de guavira em pó produzida por spray drying ao longo de 120 dias. As temperaturas de transição vítrea foram de (25,2 ± 2,7 °C e 31,4 ± 0,4) °C para os pós produzidos com goma arábica e maltodextrina, respectivamente. O modelo de BET apresentou ajuste muito bom (R2>0,99) para descrever o comportamento de sorção de água das amostras nas temperaturas de (20, 30 e 40) °C. A polpa de guavira em pó produzida com goma arábica apresentou maior adsorção de água do que as amostras obtidas com maltodextrina. No estudo da estabilidade, as amostras foram acondicionadas em embalagem de polietileno laminado e armazenadas a 25 °C e umidade relativa de 75%. A embalagem de polietileno laminado foi eficiente na manutenção do teor de ácido ascórbico e atividade antioxidante da guavira em pó por um período de 120 dias, independente do carreador adicionado. O teor de compostos fenólicos para a guavira em pó com goma arábica apresentou uma redução nos primeiros 22 dias, contudo a amostra com maltodextrina manteve-se estável durante 120 dias de armazenamento.

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Comunicación presentada en forma de póster en el "12th Mediterranean Congress of Chemical Engineering", Barcelona (Spain), November 15-18, 2011