Les silencieux à baffles parallèles sont largement utilisés dans les systèmes de chauffage, ventilation et climatisation (CVC) pour réduire le bruit généré par les sources aérauliques. Ces silencieux sont composés d'un certain nombre de baffles insérés dans un conduit de section rectangulaire. Chaque baffle est constitué d'un cadre métallique garni d'un matériau absorbant. Ce travail de thèse vise à analyser l'efficacité acoustique de ces silencieux afin d'en améliorer les performances en basses fréquences. Dans un premier temps, un modèle de propagation bidimensionnel à ``couches'' est développé afin de prédire les pertes par transmission pour une large variété de ce type de silencieux. Ce modèle multimodal repose principalement sur le calcul des modes acoustiques pour la pression moyenne dans chaque couche et a pour avantage de simplifier grandement la procédure de raccordement modal à l'interface entre deux domaines successifs. C'est un modèle facilement implémentable et approprié à des procédures d'optimisation de par sa rapidité et sa facilité de mise en données. Il a été validé expérimentalement lors de deux campagnes de mesure à des échelles réduite et réelle. Dans un second temps, le modèle développé est utilisé pour appréhender différentes pistes d'amélioration en basses fréquences et concevoir des solutions optimisées. Des premières pistes sont examinées dans le cas de silencieux standards concernant l'influence du nombre de baffles, de la symétrie et de la périodicité du silencieux sur le couplage modal et les performances acoustiques. Les autres pistes d'amélioration ainsi que les solutions optimisées ne figurent pas dans cette version pour des raisons de confidentialité. / Baffle-type silencers are widely used in the heating, ventilation and air conditioning (HVAC) systems of buildings to reduce noise being emitted from air-moving devices such as fans and air conditioners. These silencers generally consist of several baffles inserted in a duct with a rectangular cross section. Each baffle is made of sound absorbing material such as rockwool or glasswool. Usually, a metallic fairing is also placed at each end of the baffle. This thesis aims to analyze the effectiveness of these acoustic silencers to improve performance at low frequencies. First, a two-dimensional multimodal model is developed to predict the transmission loss for a wide variety of this type of silencer. The numerical model relies mainly on the computation of approximate acoustic modes for the mean pressure in each layer corresponding either to the airway or the baffle. The method offers the advantage that it greatly simplifies the mode matching procedure at the junction between successive domains and it can be used to tackle relatively complex geometrical configurations with the possibility of taking into account the presence of resistive screens between the porous baffle and the air domain. It is also an easy-to-implement and relatively inexpensive model suitable for optimization purposes. It has been experimentally validated in two measurement campaigns at reduced and actual scales. In a second step, the developed model is used to investigate different ways of improving performance at low frequencies. Suggested improvements are discussed in the case of standard silencers regarding the influence of the number of baffles, symmetry and periodicity of the silencer on the modal coupling and acoustic performance. For confidentiality reasons, other suggested improvements and optimized solutions are not included in this version.

This thesis presents results of an experimental investigation that characterizes the wall vibration of a pipe with turbulent flow passing through it. Specifically, experiments were conducted using a water flow loop to address three general phenomena. The topics of investigation were: 1) How does the pipe wall vibration depend on the average flow speed, pipe diameter, and pipe thickness for an unsupported pipe? 2) How does the behavior change if the pipe is clamp supported at various clamping lengths? 3) What influence does turbulence generation caused by holed baffle plates exert on the pipe response? A single pipe material (PVC) was used with a range of internal diameters from 5.08 cm to 10.16 cm and diameter to thickness ratios ranging from 8.90 to 16.94. The average flow speed that the experiments were conducted at ranged from 0 to 11.5 m/s. Pipe vibrations were characterized by accelerometers mounted on the pipe wall at several locations along the pipe length. Rms values of the pipe wall acceleration and velocity time series were measured at various flow speeds. Power spectral densities of the accelerometer data were computed and analyzed. Concurrent wall pressure fluctuation measurements were also obtained. The results show that for a fully developed turbulent flow, the rms of the wall pressure fluctuations is proportional to the rms of the wall acceleration and each scale nominally as the square of the average fluid velocity. Also, the rms of the pipe wall acceleration increases with decreasing pipe wall thickness. When changes were made in the pipe support length, it was observed that, in general, pipe support length exercises little influence on the pipe wall acceleration. The influence of pipe support length on the pipe wall velocity is much more pronounced. A non-dimensional parameter describing the pipe wall acceleration is defined and its dependence on relevant independent non-dimensional parameters is presented. Turbulence was induced using baffle plates with various sizes (2.54 cm to 0.159 cm) and numbers of holes drilled through them to provide a constant through area of 35.48 cm2 for each plate. Cavitation exists at high speeds for the largest holed baffle plates and this significantly increases the rms of the pipe wall acceleration. As the baffle plate hole size decreases, vibration levels were observed to return to levels that were observed when no baffle plate was employed. Power spectral densities of the accelerometer data from each baffle plate scenario were also computed and analyzed.

No description available.

Submitted by Fabricia Fialho Reginato (fabriciar) on 2015-08-03T22:53:16Z No. of bitstreams: 1 MarceloCaetano.pdf: 5404511 bytes, checksum: f5ccf4e834b73eeb355f4e39a14ef0cf (MD5) / Made available in DSpace on 2015-08-03T22:53:16Z (GMT). No. of bitstreams: 1 MarceloCaetano.pdf: 5404511 bytes, checksum: f5ccf4e834b73eeb355f4e39a14ef0cf (MD5) Previous issue date: 2009-03 / Caixa Econômica Federal / CNPQ – Conselho Nacional de Desenvolvimento Científico e Tecnológico / FINEP - Financiadora de Estudos e Projetos / MMA - Ministério do meio Ambiente / PROSAB - Programa de Pesquisa em Saneamento Básico / UNISINOS - Universidade do Vale do Rio dos Sinos / Em lixiviados de Aterros Sanitários (LAS), o nitrogênio amoniacal (NA) pode alcançar concentrações superiores a 2000 mg/L e, se disposto no meio ambiente sob estas concentrações, pode causar severos impactos ambientais e à saúde pública. Entre as alternativas para remoção de NA de lixiviados, o processo de “stripping” é um dos métodos utilizados mundialmente e que se destaca tecnicamente. O objetivo deste trabalho foi o estudo da remoção de amônia por “stripping” do lixiviado proveniente do Aterro Sanitário de São Leopoldo/RS, utilizando um processo físico de tratamento. O estudo foi desenvolvido através de ensaios de batelada em Reator de Chicanas (RC) precedidos por ensaios de bancada que empregaram Teste de Jarros. As variáveis testadas para o monitoramento do experimento foram: concentração inicial de NA e vazão de recirculação de lixiviado; sendo realizadas amostragens e análises físicoquímicas dos seguintes parâmetros: pH, DQO, temperatura, série de nitrogênio, série de sólidos, alcalinidade, nitrito e nitrato para verificação da eficiência do sistema. Em nenhum dos ensaios foi promovido a alteração do pH e/ou temperatura do lixiviado. Os resultados mostraram, para um tempo de detenção hidráulica (TDH) de 12 dias, uma remoção de NA variando de 27% a 52%, porém não sendo suficiente para o atendimento dos padrões nacionais legislativos de emissão de efluentes em recursos hídricos. O parâmetro “temperatura”, estatisticamente, mostrou influenciar na remoção de NA, sendo obtidos maiores remoções para temperaturas ambiente superiores a 20ºC. Para as condições avaliadas por esta dissertação, conclui-se que, em temperaturas ambiente superiores a 20ºC a melhor opção técnica-ambiental de tratamento de LAS é a utilização, no RC, de vazão de recirculação de lixiviado de 1,7 m³/h. Já para temperaturas inferiores a 20ºC, o melhor desempenho do RC ocorreu com vazão de recirculação 0,0m³/h (sem bomba); o que representa uma redução do consumo de energia, entretanto sugere-se um aumento do TDH. Pelos resultados conseguidos, o RC se torna uma opção viável tecnicamente para tratamento de LAS, como um processo físico para remoção de amônia por “stripping”, podendo ser indicado como um pré- tratamento aos sistemas biológicos. / The ammoniacal nitrogen (AN) from landfill leachates (LL) may cause severe impacts on the environment and public health if disposal at concentrations above 2000 mg/L. The stripping process is one of the methods worldwide used and technically outstanding among the alternatives for AN removal from leachates. The study of physical treatment process for removal of ammonia from the leachate in a landfill in São Leopoldo/RS was the objective of this work. The study was developed through batch tests in a baffle reactor (BR) that was previous by bench tests using the jar test. The variables tested to monitor the experiment were: initial concentration of AN and leachate recirculation flow. Samplings and physicochemical analyses of the following parameters were performed: pH, COD, temperature, nitrogen series, solids series, alkalinity, nitrite and nitrate to verify system efficiency. None of the assays was realized changes in pH and/or temperature in leachate. The hydraulic detention time (HDT) of 12 days resulted in AN removal ranging from 27% to 52%. However, this is not sufficient to comply with the national legislative standards of effluent emission into water resources. Statistically the “temperature” parameter showed influence on AN removal and greater removals were obtained for ambient temperatures above 20ºC. For the evaluated conditions was conclude that the best technical-enviromental option for treatment of LL is the leachate recirculation flow of 1.7 m³/h at temperatures higher than 20ºC. On the other hand, for temperatures below 20ºC the best BR performance occurred with leachate recirculation flow of 0.0 m³/h (without pump). This represents a reduction of energy consumes but is necessary an increase of HDT. According to the results obtained, the BR is a technically feasible option to treat LL as a physical process to remove ammonia by stripping and it may be indicated as a pre-treatment before biological systems.

The petroleum fuels are nonrenewable, are finites resources and its combustion produces many pollutants into the atmosphere. So, researches aiming alternative sources of energy have been increased. Vegetable oils seem to be a great alternative to produce biodiesel - a renewable fuel, non-toxic and releases fewer pollutants. The sunflower is a great oilseed for biodiesel production, because it can be planted in northeastern of Brazil during the rainy season. Biodiesel can be obtained by transesterification: reaction between vegetable and/or animal fat with shot chain alcohol in presence of catalyst. The aim of this work is to study the effect of the process variable in the production of biodiesel – agitation speed - and even equipment configuration, as characteristic impeller and presence or absence of chicanery in the reactor. For this, full factorial design 2 ³ was performed a resulting in eight experiments. The biodiesel was produced by the transesterification reaction from refined sunflower oil and anhydrous ethanol, and sodium hydroxide P.A. as catalyst. The following operating conditions were used: temperature of the thermostatic bath maintained at 70 °C; weight of catalyst of 1.5% by weight of oil; ratio between number of moles of oil ans ethanol of 1:10; and reaction time of 30 min. Prior to reaction, was performed to characterize the oil, as well as the characterization of biodiesel obtained after the reaction. It was observed that the presence of baffle contributed to obtain lower yields throughout the reaction. When used impeller 2 (turbine impeller with dimensions greater than those reported in the literature), higher yields were obtained at the beginning of the reaction. The stirring speed of 35o rpm contributed to higher yields were obtained at the beginning of the reaction. / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / Os combustíveis derivados do petróleo são não-renováveis, são fontes finitas e sua combustão emite muitos poluentes para a atmosfera. Com isso, têm aumentado as pesquisas por fontes alternativas de energia. Os óleos vegetais parecem ser uma ótima alternativa para obtenção de biodiesel - um combustível renovável, não-tóxico e que libera menos poluentes. O girassol é uma oleaginosa com potencial utilização para produção de biodiesel, podendo ser plantada no Nordeste brasileiro no período chuvoso. O biodiesel pode ser obtido através da transesterificação: reação entre gordura vegetal e/ou animal com álcool de cadeia curta, na presença de catalisador. O objetivo do presente trabalho é estudar o efeito da variável de processo na produção do biodiesel – velocidade de agitação - e ainda configuração do equipamento, como: característica do impelidor e presença ou não de chicana no reator. Para isso, foi realizado um planejamento fatorial completo 2³, resultando em 8 experimentos. O biodiesel foi produzido por reação de transesterificação a partir de óleo de girassol refinado e etanol anidro, tendo-se hidróxido de sódio P.A. como catalisador. Foram utilizadas as seguintes condições operacionais: temperatura de reação de 70 ºC; relação entre a massa de catalisador e a massa do óleo de 1,5%; relação entre número de mols óleo/álcool etílico de 1:10; e, tempo total de reação de 30 min. Previamente à reação, foi realizada a caracterização do óleo, bem como, a caracterização do biodiesel obtido após a reação. Foi observado que a presença de chicana contribuiu para a obtenção de menores rendimentos durante toda a reação. Ao ser utilizado o impelidor 2 (impelidor tipo turbina com dimensões maiores que aquelas citadas na literatura) foram obtidos rendimentos mais elevados no início da reação. A velocidade de agitação de 350 rpm contribuiu para que fossem obtidos maiores rendimentos no início da reação.

A literatura corrente possui informações limitadas sobre o projeto da área de troca térmica de tanques com jaqueta, serpentina helicoidal, serpentina espiral e chicana tubular vertical, em operação com fluidos não-Newtonianos. A presente tese teve por objetivo principal analisar a transferência de calor, potência consumida e ampliação de escala em tanques com impulsores mecânicos na agitação de fluidos não-Newtonianos com duas superfícies de transmissão de calor, chicana tubular vertical e serpentina em espiral. O trabalho também visou fornecer métodos de ampliação de escala de tanques com agitação para fluidos não-Newtonianos que sigam o modelo reológico da lei das potências. A unidade experimental contemplou dois tanques de acrílico, com volume de 10 litros e 50 litros, respectivamente, chicanas tubulares verticais e serpentina em espiral. Os impulsores mecânicos utilizados foram o axial com 4 pás inclinadas a 45° e o radial turbina com 6 pás planas. Como fluidos utilizaram-se soluções aquosas de carboximetilcelulose (0,5%, 1,0% e 1,5%), solução aquosa de carbopol 940 (1,5%), solução aquosa de sacarose (50%) e água. Todos os experimentos foram conduzidos em batelada. Com os dados obtidos, empregou-se o uso de regressões para a obtenção da Equação de Nusselt, as quais forneceram valores de coeficiente de determinação ajustados entre 0,83 e 0,89 com Reynolds no intervalo de 20 a 405000, Prandtl na faixa de 4 a 6400 e índice reológico do modelo da lei das potências entre 0,45 e 1,00. Observou-se que no aquecimento realizado com a chicana tubular vertical, o impulsor radial forneceu coeficientes de convecção 20% acima quando comparado com o impulsor axial, entretanto o consumo de potência foi cerca de 66% maior em relação ao impulsor axial. No caso da serpentina espiral, o impulsor axial promoveu coeficientes de convecção por volta de 15% superiores em relação ao impulsor radial com um consumo de potência 65% menor. Desse modo, em processos em que não é necessária uma elevada turbulência, recomenda-se o uso do impulsor axial com a serpentina espiral, porém, se o processo demandar uma turbulência significativa, deve-se usar o impulsor radial com a chicana tubular vertical. Em uma última análise, os modelos não-lineares obtidos para ampliação de escala forneceram erros entre 11% e 20% na predição da rotação no tanque industrial, os quais são válidos para Reynolds modificados de Metzner e Otto (1957) na faixa de 20 a 4000 e para fluidos não-Newtonianos pseudoplásticos com índices reológicos entre 0,45 e 1,00. / Current literature has limited information on the design of the thermal exchange area of tanks with jacket, helical coil, spiral coil and vertical tuber baffle, in operation with non-Newtonian fluids. The main purpose of this thesis was to analyze heat transfer, power consumption and scale-up in tanks with mechanical impellers in the agitation of non-Newtonian fluids with two heat transfer surfaces, vertical tube baffle and spiral coil. The work also aimed to provide methods of scale-up tank scale with agitation for non-Newtonian fluids that follow the rheology model of the law of powers. The experimental unit included two acrylic tanks, with a volume of 10 liters and 50 liters, respectively, vertical tube baffles and spiral coil. The mechanical impellers used were the 45° pitched blade turbine (PBT) and the Rushton turbine (RT). Aqueous solutions of carboxymethylcellulose (0.5%, 1.0% and 1.5%), aqueous solution of carbopol 940 (1.5%), aqueous solution of sucrose (50%) and water were used as fluids. All the experiments were conducted in batch. With the obtained data, we used the regressions to obtain the Nusselt Equation, which provided coefficient of determination values adjusted between 0.83 and 0.89 with Reynolds in the range of 20 to 405000, Prandtl in the range of 4 to 6400 and rheological index of the power law model between 0.45 and 1.00. It was observed that in the heating performed with the vertical tube baffle, the RT provided convection coefficients 20% higher when compared to the axial impeller, however the power consumption was about 66% higher in relation to the PBT. In the case of the spiral coil, the PBT promoted convection coefficients around 15% higher than the RT with 65% lower power consumption. Thus, in processes where high turbulence is not required, it is recommended to use the PBT with the spiral coil, but if the process requires significant turbulence, the RT must be used with the vertical tubular chassis. In a final analysis, the nonlinear models obtained for scaling provided errors between 11% and 20% in the prediction of rotation in the industrial tank, which are valid for Metzner and Otto (1957) modified Reynolds in the range of 20 to 4000 and for non-Newtonian pseudoplastic fluids with rheological indexes between 0.45 and 1.00.

A literatura corrente possui informações limitadas sobre o projeto da área de troca térmica de tanques com jaqueta, serpentina helicoidal, serpentina espiral e chicana tubular vertical, em operação com fluidos não-Newtonianos. A presente tese teve por objetivo principal analisar a transferência de calor, potência consumida e ampliação de escala em tanques com impulsores mecânicos na agitação de fluidos não-Newtonianos com duas superfícies de transmissão de calor, chicana tubular vertical e serpentina em espiral. O trabalho também visou fornecer métodos de ampliação de escala de tanques com agitação para fluidos não-Newtonianos que sigam o modelo reológico da lei das potências. A unidade experimental contemplou dois tanques de acrílico, com volume de 10 litros e 50 litros, respectivamente, chicanas tubulares verticais e serpentina em espiral. Os impulsores mecânicos utilizados foram o axial com 4 pás inclinadas a 45° e o radial turbina com 6 pás planas. Como fluidos utilizaram-se soluções aquosas de carboximetilcelulose (0,5%, 1,0% e 1,5%), solução aquosa de carbopol 940 (1,5%), solução aquosa de sacarose (50%) e água. Todos os experimentos foram conduzidos em batelada. Com os dados obtidos, empregou-se o uso de regressões para a obtenção da Equação de Nusselt, as quais forneceram valores de coeficiente de determinação ajustados entre 0,83 e 0,89 com Reynolds no intervalo de 20 a 405000, Prandtl na faixa de 4 a 6400 e índice reológico do modelo da lei das potências entre 0,45 e 1,00. Observou-se que no aquecimento realizado com a chicana tubular vertical, o impulsor radial forneceu coeficientes de convecção 20% acima quando comparado com o impulsor axial, entretanto o consumo de potência foi cerca de 66% maior em relação ao impulsor axial. No caso da serpentina espiral, o impulsor axial promoveu coeficientes de convecção por volta de 15% superiores em relação ao impulsor radial com um consumo de potência 65% menor. Desse modo, em processos em que não é necessária uma elevada turbulência, recomenda-se o uso do impulsor axial com a serpentina espiral, porém, se o processo demandar uma turbulência significativa, deve-se usar o impulsor radial com a chicana tubular vertical. Em uma última análise, os modelos não-lineares obtidos para ampliação de escala forneceram erros entre 11% e 20% na predição da rotação no tanque industrial, os quais são válidos para Reynolds modificados de Metzner e Otto (1957) na faixa de 20 a 4000 e para fluidos não-Newtonianos pseudoplásticos com índices reológicos entre 0,45 e 1,00. / Current literature has limited information on the design of the thermal exchange area of tanks with jacket, helical coil, spiral coil and vertical tuber baffle, in operation with non-Newtonian fluids. The main purpose of this thesis was to analyze heat transfer, power consumption and scale-up in tanks with mechanical impellers in the agitation of non-Newtonian fluids with two heat transfer surfaces, vertical tube baffle and spiral coil. The work also aimed to provide methods of scale-up tank scale with agitation for non-Newtonian fluids that follow the rheology model of the law of powers. The experimental unit included two acrylic tanks, with a volume of 10 liters and 50 liters, respectively, vertical tube baffles and spiral coil. The mechanical impellers used were the 45° pitched blade turbine (PBT) and the Rushton turbine (RT). Aqueous solutions of carboxymethylcellulose (0.5%, 1.0% and 1.5%), aqueous solution of carbopol 940 (1.5%), aqueous solution of sucrose (50%) and water were used as fluids. All the experiments were conducted in batch. With the obtained data, we used the regressions to obtain the Nusselt Equation, which provided coefficient of determination values adjusted between 0.83 and 0.89 with Reynolds in the range of 20 to 405000, Prandtl in the range of 4 to 6400 and rheological index of the power law model between 0.45 and 1.00. It was observed that in the heating performed with the vertical tube baffle, the RT provided convection coefficients 20% higher when compared to the axial impeller, however the power consumption was about 66% higher in relation to the PBT. In the case of the spiral coil, the PBT promoted convection coefficients around 15% higher than the RT with 65% lower power consumption. Thus, in processes where high turbulence is not required, it is recommended to use the PBT with the spiral coil, but if the process requires significant turbulence, the RT must be used with the vertical tubular chassis. In a final analysis, the nonlinear models obtained for scaling provided errors between 11% and 20% in the prediction of rotation in the industrial tank, which are valid for Metzner and Otto (1957) modified Reynolds in the range of 20 to 4000 and for non-Newtonian pseudoplastic fluids with rheological indexes between 0.45 and 1.00.

Lined silencers of various configurations are used to attenuate the noise from building HVAC equipment, gas turbines, and other machinery. First-mode analytical solutions are presented for sound attenuation along rectangular lined ducts, parallel-baffle silencers, and circular lined ducts. The sound absorptive lining is treated using a bulk property model. The analytical solutions entail solving a nonlinear characteristic equation in the transverse direction after the rigid-wall boundary condition is applied. The solution is compared to the boundary element solution and a local impedance analytical solution for several test cases.

The thesis is dealing with comparing dissipation of the kinetic energy water flow using various bottom elements based on model research. There is missing information about efficiency of different kinds of bottom elements. This absence does not allow to compare different modification of the bottom of stilling basins. Within experimental research were measured depths in different variants. Based on the results of model tests are evaluated and tabulated sorted variants of the combat efficiency of the kinetic energy water flow. The results will be used for the efficient and economic design of additional alterations of stilling basins.

Les transducteurs ultrasonores capacitifs micro-usinés (cMUT : capacitive Micromachined Ultrasound Transducers) apparaissent, au vu de leur maturité croissante, comme une alternative de plus en plus viable à la technologie piézoélectrique. Caractérisés par une large bande passante et une large directivité, ces transducteurs sont des solutions intéressantes pour le développement de sondes ultrasonores « exotiques » dont les spécifications sont difficilement atteignables en technologie piézoélectrique. C'est dans ce contexte et fort de l'expérience acquise par notre laboratoire sur cette technologie pendant plus d'une dizaine d'années, que s'est inscrit ce travail de thèse. L'originalité du travail rapporté ici est d'aller de l'analyse du comportement général des barrettes cMUT jusqu'à un exemple précis de conception de sonde cMUT pour l'évaluation du tissu osseux. Des outils de modélisation précis et rapides, basés sur l'introduction de conditions de périodicité, ont été développés. Plusieurs modèles ont ainsi été mis en place afin d'adapter la stratégie de modélisation à la topologie du dispositif cMUT à modéliser : cellule isolée, colonne de cellules, matrice de cellules et élément de barrette. Ces modèles ont permis d'étudier le comportement des éléments de barrette cMUT et d'améliorer notre connaissance sur les mécanismes physiques mis en jeu. De cette façon, l'origine des effets de baffle, problème récurrent du comportement des barrettes cMUT, a clairement été interprété par l'intermédiaire d'une analyse modale. Des solutions ont ainsi été identifiées et proposées afin d'optimiser le comportement des barrettes cMUT, de façon à réduire la présence des effets de baffle et à augmenter leur bande passante. Le développement d'une barrette cMUT dédiée à l'évaluation du tissu osseux est présenté dans sa totalité, afin d'illustrer les différents aspects liés à la conception d'une sonde de cette technologie. Un travail original de caractérisation a été réalisé sur cette barrette, afin d'estimer l'homogénéité inter-cellules à l'échelle de l'élément et l'homogénéité inter-éléments à l'échelle de la barrette. Enfin, une confrontation a été réalisée avec une sonde PZT de même topologie sur plusieurs fantômes osseux. Il a ainsi été démontré que la sonde cMUT permettait la détection d'un plus grand nombre de modes guidés, et par conséquent, une meilleure évaluation du tissu osseux. / Following recent advances, the capacitive Micromachined Ultrasound Transducers (cMUT) technology seems to be a good alternative to the piezoelectric technology. For specific applications, the requirements and specifications of the probe are sometimes difficult to obtain with the traditional PZT technology. The cMUT technology, with both large bandwidth and angular directivity, can be an interesting way to overcome these limitations. This PhD has been carried out in this context, in a laboratory which has nearly 10 years of experience in the field of cMUT technology. The originality of the work sustained in this PhD is that it covers the cMUT technology, from general aspects dealing of modeling and characterization up to a complete example of cMUT-based probe applied to the assessment of cortical bone. Fast and accurate modeling tools, based on periodicity conditions, have been developed. Several models have been proposed to match the modeling strategy to the topology of the cMUT array : isolated cell, columns of cells, 2-D matrix of cells and array element. These models have been used to analyze the cMUT array behavior and to understand how mutual couplings between cMUTs impact the response of one element. Origins of the baffle effect, well-known as a recurrent problem in cMUT probe, have been explained using an original method based on the normal mode decomposition of the radiated pressure field. Thus, solutions have been identified and tested to optimize the cMUT frequency response, i.e. to increase the bandwidth, and to suppress parasitic disturbances linked to baffle effect in the electroacoustic response. The development of a dedicated cMUT array for the assessment of bone tissue is accurately detailed in the manuscript, including description of the design rules, fabrication steps and packaging procedure. An original characterization work has been carried out in order to check the device homogeneity, first from cell to cell and then from element to element. Finally, a comparison with a PZT probe with the same topology has been performed on bone mimicking phantom. Nice results has been obtained, showing that cMUT probe allows detecting higher number of guided modes in the cortical shell, and consequently, improving the cortical bone assessment.