CH and C2 radicals characterization in natural gas turbulent diffusion flames

This paper reports the construction of an axisymmetric nonpremixed piloted jet burner, with well-defined initial and boundary conditions, known as the Delft burner, to assess turbulence-chemistry interaction in non-premixed turbulent flames. Detailed experimental information is described, involving hot-wire anemometry, thin-wire thermocouples and chemiluminescence visualization measurements. Radial profile of the axial mean velocity indicates excellent agreement between flow patterns developed within Delft installation and the one described herein. Chemiluminescence emissions from CH and C2 free-radicals were acquired with a CCD camera. Tomography reconstruction analysis was utilised to compare radical emissions and temperature spatial distributions. There was a strong dependence between temperature and CH/C 2 emissions. This is an indication that these radicals can be used in flame front studies.

A preliminary physicochemical, exergetic and economic study of hydrogen production utilizing glycerol

This work has as objective to demonstrate technical and economic viability of hydrogen production utilizing glycerol. The volume of this substance, which was initially produced by synthetic ways (from oil-derived products), has increased dramatically due mainly to biodiesel production through transesterification process which has glycerol as main residue. The surplus amount of glycerol has been generally utilized to feed poultry or as fuel in boilers, beyond other applications such as production of soaps, chemical products for food industry, explosives, and others. The difficulty to allocate this additional amount of glycerol has become it in an enormous environment problem, in contrary to the objective of biodiesel chain, which is to diminish environmental impact substituting oil and its derivatives, which release more emissions than biofuels, do not contribute to CO2-cycle and are not renewable sources. Beyond to utilize glycerol in combustion processes, this material could be utilized for hydrogen production. However, a small quantity of works (theoretical and experimental) and reports concerning this theme could be encountered. Firstly, the produced glycerol must be purified since non-reacted amounts of materials, inclusively catalysts, contribute to deactivate catalysts utilized in hydrogen production processes. The volume of non-reacted reactants and non-utilized catalysts during transesterification process could be reutilized. Various technologies of thermochemical generation of hydrogen that utilizes glycerol (and other fuels) were evaluated and the greatest performances and their conditions are encountered as soon as the most efficient technology of hydrogen production. Firstly, a physicochemical analysis must be performed. This step has as objective to evaluate the necessary amount of reactants to produce a determined volume of hydrogen and determine thermodynamic conditions (such as temperature and pressure) where the major performances of hydrogen production could be encountered. The calculations are based on the process where advance degrees are found and hence, fractions of products (especially hydrogen, however, CO2, CO, CH4 and solid carbon could be also encountered) are calculated. To produce 1 Nm3/h of gaseous hydrogen (necessary for a PEMFC - Proton Exchange Membrane Fuel Cell - containing an electric efficiency of about 40%, to generate 1 kWh), 0,558 kg/h of glycerol is necessary in global steam reforming, 0,978 kg/h of glycerol in partial oxidation and cracking processes, and 0,782 kg/h of glycerol in autothermal reforming process. The dry reforming process could not be performed to produce hydrogen utilizing glycerol, in contrary to the utilization of methane, ethanol, and other hydrocarbons. In this study, steam reforming process was preferred due mainly to higher efficiencies of production and the need of minor amount of glycerol as cited above. In the global steam reforming of glycerine, for one mole of glycerol, three moles of water are necessary to produce three moles of CO2 and seven moles of H2. The response reactions process was utilized to predict steam reforming process more accurately. In this mean, the production of solid carbon, CO, and CH4, beyond CO2 and hydrogen was predicted. However, traces of acetaldehyde (C2H2), ethylene (C2H4), ethylene glycol, acetone, and others were encountered in some experimental studies. The rates of determined products obviously depend on the adopted catalysts (and its physical and chemical properties) and thermodynamic conditions of hydrogen production. Eight reactions of steam reforming and cracking were predicted considering only the determined products. In the case of steam reforming at 600°C, the advance degree of this reactor could attain its maximum value, i.e., overall volume of reactants could be obtained whether this reaction is maintained at 1 atm. As soon as temperature of this reaction increases the advance degree also increase, in contrary to the pressure, where advance degree decrease as soon as pressure increase. The fact of temperature of reforming is relatively small, lower costs of installation could be attained, especially cheaper thermocouples and smaller amount of thermo insulators and materials for its assembling. Utilizing the response reactions process in steam reforming, the predicted volumes of products, for the production of 1 Nm3/h of H2 and thermodynamic conditions as cited previously, were 0,264 kg/h of CO (13% of molar fraction of reaction products), 0,038 kg/h of CH4 (3% of molar fraction), 0,028 kg/h of C (3% of molar fraction), and 0,623 kg/h of CO2 (20% of molar fraction). Through process of water-gas shift reactions (WGSR) an additional amount of hydrogen could be produced utilizing mainly the volumes of produced CO and CH4. The overall results (steam reforming plus WGSR) could be similar to global steam reforming. An attention must to be taking into account due to the possibility to produce an additional amount of CH4 (through methanation process) and solid carbon (through Boudouard process). The production of solid carbon must to be avoided because this reactant diminishes (filling the pores) and even deactivate active area of catalysts. To avoid solid carbon production, an additional amount of water is suggested. This method could be also utilized to diminish the volume of CO (through WGSR process) since this product is prejudicial for the activity of low temperature fuel cells (such as PEMFC). In some works, more three or even six moles of water are suggested. A net energy balance of studied hydrogen production processes (at 1 atm only) was developed. In this balance, low heat value of reactant and products and utilized energy for the process (heat supply) were cited. In the case of steam reforming utilizing response reactions, global steam reforming, and cracking processes, the maximum net energy was detected at 700°C. Partial oxidation and autothermal reforming obtained negative net energy in all cited temperatures despite to be exothermic reactions. For global steam reforming, the major value was 114 kJ/h. In the case of steam reforming, the highest value of net energy was detected in this temperature (-170 kJ/h). The major values were detected in the cracking process (up to 2586 kJ/h). The exergetic analysis has as objective, associated with physicochemical analysis, to determine conditions where reactions could be performed at higher efficiencies with lower losses. This study was performed through calculations of exergetic and rational efficiencies, and irreversibilities. In this analysis, as in the previously performed physicochemical analysis, conditions such as temperature of 600°C and pressure of 1 atm for global steam reforming process were suggested due to lower irreversibility and higher efficiencies. Subsequently, higher irreversibilities and lower efficiencies were detected in autothermal reforming, partial oxidation and cracking process. Comparing global reaction of steam reforming with more-accurate steam reforming, it was verified that efficiencies were diminished and irreversibilities were increased. These results could be altered with introduction of WGSR process. An economic analysis could be performed to evaluate the cost of generated hydrogen and determine means to diminish the costs. This analysis suggests an annual period of operation between 5000-7000 hours, interest rates of up to 20% per annum (considering Brazilian conditions), and pay-back of up to 20 years. Another considerations must to be take into account such as tariffs of utilized glycerol and electricity (to be utilized as heat source and (or) for own process as pumps, lamps, valves, and other devices), installation (estimated as US$ 15.000 for a plant of 1 Nm3/h) and maintenance cost. The adoption of emission trading schemes such as carbon credits could be performed since this is a process with potential of mitigates environment impact. Not considering credit carbons, the minor cost of calculated H2 was 0,16288 US$/kWh if glycerol is also utilized as heat sources and 0,17677 US$/kWh if electricity is utilized as heat sources. The range of considered tariff of glycerol was 0-0,1 US$/kWh (taking as basis LHV of H2) and the tariff of electricity is US$ 0,0867 US$/kWh, with demand cost of 12,49 US$/kW. The costs of electricity were obtained by Companhia Bandeirante, localized in São Paulo State. The differences among costs of hydrogen production utilizing glycerol and electricity as heat source was in a range between 0,3-5,8%. This technology in this moment is not mature. However, it allows the employment generation with the additional utilization of glycerol, especially with plants associated with biodiesel plants. The produced hydrogen and electricity could be utilized in own process, increasing its final performance.

Influence of the coloring agent concentration on bleaching gel and pulp chamber temperatures during dental bleaching

This study evaluated the Influence of the coloring agent concentration on the temperature of the gel layer and pulp chamber during dental bleaching with an LED/laser light source. Ten human incisors and a digital thermometer with K-type thermocouples were used. Using a high-speed spherical diamond bur, endodontic access was gained through openings on the lingual faces until pulp chamber was exposed. One end of the thermocouple was placed on the labial surface (immersed in bleaching gel) and the other end in the pulp chamber. The same 10 specimens were used in the 12 groups, according to the type and concentration of bleaching gel. Each bleaching gel was used in four different concentrations: manipulated without coloring, with normal quantity recommended by the manufacturer, with double the recommended amount of coloring, and with triple the recommended amount of coloring. The temperature rise was measured every 30 seconds for three minutes with a K-type thermocouple. The data were analyzed by ANOVA to examine the concentration and type of bleaching gel. This test was followed by Tukey's test, which was performed Independently for the gel at the labial surface and the pulp chamber (a = 5%). For both surfaces, values of p = 0.00 were obtained for all factors and for the Interaction between them. The varying concentrations of coloring agent produced statistically significant differences in terms of temperature increase for both the gel layer and the pulp chamber during activation.

Influência da técnica cirúrgica guiada para implantes sobre o aquecimento ósseo, a viabilidade celular imediata e a deformação de fresas após osteotomia para implantes

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Clareamento com peróxido de hidrogênio a 35% ativado por diversas fontes de energia: análise térmica e microdureza do esmalte

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Estimativa do tempo de vaporização das toras e sua implicação no desdobro e na secagem da madeira de Eucalyptus grandis

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

Avaliação da eficiência de isolantes térmicos por reflexão, utilizados como subcoberturas

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

Transferência de calor em leitos fixos com aplicação em reatores de fermentação em estado sólido

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Estudo numérico e experimental do resfriamento convectivo de vegetais cilíndricos

Pós-graduação em Física - IGCE

Avaliação in vitro da fotopolimerização de bráquetes vestibulares e linguais com arco de plasma, led e luz halógena

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Estudo dos níveis de tensões de crescimento e influência da vaporização de toras na qualidade do desdobro da madeira de Hevea brasiliensis

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Análise termoelástica experimental e computacional por elementos finitos da parede externa em concreto armado de um forno de cozimento de anodo

Nesta dissertação foi desenvolvido um estudo sobre o comportamento de uma estrutura em concreto armado submetida a elevadas variações térmicas. A estrutura analisada consiste na parede externa de um forno de cozimento de anodo utilizado na produção de Alumínio, e está submetida a variações térmicas de cerca de 125C devido à própria operação do forno. As motivações principais para o estudo foram a ocorrência de grandes deformações e o surgimento de fissuras na estrutura, o que poderia provocar a inutilização do forno. O objetivo do trabalho foi a investigação das causas destas patologias, assim como o estabelecimento de propostas para reforço da estrutura. Para isso, foram realizados estudos experimentais e computacionais do comportamento da estrutura. Inicialmente, a estrutura foi monitorada utilizando-se transdutores de deslocamento e sensores de temperatura (termopares), conectados a um sistema de aquisição de dados para obtenção e armazenamento automática das amostras ao longo do tempo. Em seguida, foram desenvolvidos modelos computacionais em Elementos Finitos com auxilio do programa computacional Algor, para determinação da distribuição de temperatura e as correspondentes tensões e deformações de origem térmica na estrutura. Nestes estudos, foram realizadas análises estacionárias e transientes de condução de calor, seguidas de análises de tensões de origem térmica. Como conclusão do estudo, tem-se que a metodologia proposta para a solução do problema foi bastante satisfatória, solucionando o problema de forma precisa, porém econômica.

Estudo experimental de um reator de gaseificação em um leito fixo de açaí

Um leito de gaseificação de pequena escala foi projetado, construído e operado com o objetivo de investigar os parâmetros que influenciam o processo de gaseificação de um leito fixo de caroço de açaí. O reator é do tipo topo aberto downdraft estratificado, de dimensões de 15 cm de diâmetro interno por 1,5 m de altura, com isolamento térmico. O gás produzido foi coletado a jusante do leito de gaseificação e condensado para remoção de alcatrão, o qual foi posteriormente quantificado em titulador Karl Fisher. Após remoção do alcatrão o gás foi introduzido em um Micro GC para quantificação dos percentuais molares de H², CO, N² e CH⁴. O perfil de temperatura do leito foi medido com termopares tipo K posicionados ao longo do eixo longitudinal do leito em distâncias de 10 cm. A vazão de ar foi medida com auxilio de um tubo de Pitot e um micromanômetro. As aquisições dos dados de temperatura foram feitas por um data logger e vazão mássica do ar sendo feita usando comunicação RS232 do micromanômetro. Os procedimentos experimentais foram feitos ao longo de 4 horas de operação do leito de gaseificação, com consumo médio de biomassa de 1,6 kg/h, com 6 dados do perfil de temperatura, vazão mássica de ar, perda de carga do leito e concentração dos gases obtidos no processo de gaseificação e quantificação do teor de alcatrão condensável presente no gás. Verificou-se que o gaseificador de leito de açaí pode ser operado através de uma gama bastante ampla de taxas de fluxo de ar de 2 a 5 kg/h, com a quantidade de energia do gás produzido variando de 5 a 15 MJ/h. As concentrações típicas dos gases obtidos no leito foram de 13% de H², 11% de CO, 1,3% de CH⁴. A eficiência máxima de gás frio de 57% e teor médio de alcatrão de 155 g/m³.

Influência da convecção termossolutal na transição colunar/equiaxial em ligas Al-Si sob condições unidirecionais e transitórias de extração de calor

A relação entre macroestrutura e propriedades mecânicas de um material tem sido objeto de intensa investigação pois o tamanho dos grãos, a orientação cristalina e a distribuição dos mesmos exercem influência direta no comportamento mecânico dos produtos acabados. Assim, o entendimento dos fatores que influenciam a formação das zonas estruturais coquilhada, colunar e equiaxial nos materiais fundidos como, por exemplo, o sistema de liga, composição da liga, temperatura de vazamento, temperatura do molde, material do molde, coeficientes de transferência de calor na interface metal/molde, taxa de resfriamento, gradientes térmicos, dimensão da peça, presença de convecção no líquido, transporte de soluto, etc é de fundamental importância para a melhoria da eficiência do processo de fundição envolvido. Com base no conhecimento dos princípios termofísicos em que essas zonas são formadas, é possível manipular de forma bastante razoável a estrutura dos produtos fundidos e, conseqüentemente, as propriedades mecânicas dos mesmos. Tendo como principal foco a análise da mudança da zona colunar para a equiaxial, este trabalho apresenta um estudo teórico-experimental sobre a transição colunar/equiaxial (TCE) das ligas hipoeutéticas Al- 3%Si, Al-7%Si Al-9%Si solidificadas unidirecionalmente em um dispositivo horizontal refrigerado a água sob condições transientes de fluxo de calor. A condição de contato térmico na superfície de extração de calor foi padronizada como sendo polida. Os perfis térmicos foram medidos em diferentes posições do lingote e os dados foram armazenados automaticamente. Um método numérico é utilizado na determinação de variáveis térmicas de solidificação como coeficientes de transferência de calor na interface metal/molde (h_i), velocidades das isotermas liquidus (V_L), gradientes térmicos (G_L) e taxas de resfriamento (T_R) que influenciam diretamente a referida transição estrutural. Os resultados teóricos e experimentais apresentaram boa concordância. Um estudo comparativo entre os resultados obtidos neste trabalho e valores propostos na literatura para analisar a TCE durante a solidificação unidirecional vertical ascendente sob condições transientes de extração de calor das ligas investigadas, também é apresentado.

Fratura precoce da porcelana em restaurações com infra-estrutura de zircônia: influência de gradientes térmicos no desenvolvimento e magnitude de tensões residuais e transitórias

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)