Un grand effort a été réalisé ces dernières années dans la compréhension du champ d'écoulement et du transfert de chaleur dans les canaux de refroidissement internes présents dans les pales de turbine. En effet, des systèmes de refroidissement avancés ont non seulement conduit à l'augmentation de l'efficacité de la turbine à gaz en augmentant la température d'entrée de la turbine au-dessus de la température de fusion du matériau, mais également en augmentant la durée de vie de la turbine. Pour permettre de tels progrès, des techniques expérimentales et numériques modernes ont été largement appliquées afin d'interpréter et d'optimiser l'aérodynamique et le transfert de chaleur dans les canaux de refroidissement internes. Cependant, les données disponibles sont limitées dans le cas des canaux de refroidissement internes dans les aubes de rotor de turbine. Les gradients de rotation et de température introduisent des forces de flottabilité de type Coriolis et centripète dans le référentiel rotatif, modifiant de manière significative l'aérothermodynamique par rapport aux passages stationnaires. Dans le cas des pales de rotor de turbine, la plupart des investigations sont soit basées sur des mesures ponctuelles, soit sont contraintes à des régimes de rotation faibles. L'objectif principal de ce travail est d'étudier le débit détaillé et le transfert de chaleur d'un canal de refroidissement interne à des conditions de fonctionnement dimensionnelles sans moteur représentatives. Ce travail introduit une section d'essai en laboratoire qui exploite des canaux à nervures sur un large éventail de nombres de Reynolds, de rotation et de flottabilité. Dans le présent travail, le nombre de Reynolds va de 15,000 à 55,000, le nombre de rotation maximum est égal à 0.77 et le nombre maximal de flottabilité est égal à 0.77. La nouvelle installation expérimentale consiste en une conception polyvalente qui permet l'interchangeabilité de la géométrie testée, de sorte que les canaux de différents rapports d'aspect et les géométries de nervure peut être facilement installé. La particle image velocimetry et la thermographie à cristaux liquides sont effectuées pour fournir des mesures précises de vitesse et de transfert de chaleur dans les mêmes conditions opératoires, ce qui conduit à un ensemble de données expérimentales unique. De plus, des simulations à grands virages sont réalisées pour donner une image de l'ensemble du champ d'écoulement et compléter les observations expérimentales. En outre, l'approche numérique vise à fournir une méthodologie robuste qui est capable de fournir des prédictions haute-fidélité de la performance des canaux de refroidissement internes. / A great effort has been carried out over the recent years in the understanding of the flow field and heat transfer in the internal cooling channels present in turbine blades. Indeed, advanced cooling schemes have not only lead to the increase of the gas turbine efficiency by increasing the Turbine Inlet Temperature above the material melting temperature, but also the increase of the turbine lifespan. To allow such progresses, modern experimental and numerical techniques have been widely applied in order to interpret and optimize the aerodynamics and heat transfer in internal cooling channels. However, the available data is limited in the case of internal cooling channels in turbine rotor blades. Rotation and temperature gradients introduce Coriolis and centripetal buoyancy forces in the rotating frame of reference, modifying significantly the aerothermodynamics from that of the stationary passages. In the case of turbine rotor blades, most of the investigations are either based on point-wise measurements or are constraint to low rotational regimes. The main objective of this work is to study the detailed flow and heat transfer of an internal cooling channel at representative engine dimensionless operating conditions. This work introduces a laboratory test section that operates ribbed channels over a wide range of Reynolds, Rotation and Buoyancy numbers. In the present work, the Reynolds number ranges from 15,000 to 55,000, the maximum Rotation number is equal to 0.77, and the maximum Buoyancy number is equal to 0.77. The new experimental facility consists in a versatile design that allows the interchangeability of the tested geometry, so that channels of different aspect ratios and rib geometries can be easily fitted. Particle Image Velocimetry and Liquid Crystal Thermography are performed to provide accurate velocity and heat transfer measurements under the same operating conditions, which lead to a unique experimental data set. Moreover, Large Eddy Simulations are carried out to give a picture of the entire flow field and complement the experimental observations. Additionally, the numerical approach intends to provide a robust methodology that is able to provide high fidelity predictions of the performance of internal cooling channels.

The main purpose of this thesis was to propose and test a new approach that captures the features of single and multiple bubbles dynamics using the Shan and Chen-type lattice Boltzmann method (LBM). Two dimensional bubbles motions were simulated considering the buoyancy effect for which the topology of the bubble is characterized by the Eötvös (Eo), and Morton (M) numbers. A qualitative and quantitative validation were performed using the Level set method. Bubble shape deformation was captured and analysis based on terminal Reynolds number and degree of circularity show very good agreement with the experimental results and with available simulation results. In sum, this study presents crucial preliminary information to further analyze multiphase fluid flows in various contexts.

Thesis name: Scuba diving equipment, systems of equipment organization and their comparison Thesis aim: To draw out historical information, to describe diving equipment and its function. To process individual systems of diving equipment's orders and to describe pro-and- cons of each of those systems. Method: Studying of accessible sources. Content analysis of technical literature and other sources. Retrieval of equipment's technical parametres. Analysis and processing of information. Results: The outcome is evaluation of different systems of diving equipment's orders. Comparison and recommendation of suitability for different kinds of scuba diving with equipment. Keywords: Diving equipment, systems of diving equipment's orders, buoyancy compensator, configuration, scuba diving with equipment

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[pt] No âmbito das cervejarias artesanais, foi recentemente inventado um medidor de densidade de líquidos que opera por um princípio incomum: o do deslocamento do centro de carena. Esse medidor obtém suas medições a partir da sua própria inclinação enquanto está flutuando, mas sua implementação original converte as medidas do acelerômetro em medidas de massa específica por uma regressão polinomial. Contudo, ele não faz correções de temperatura, de forma que a influência dessa grandeza é desconsiderada na regressão. Adicionalmente, o medidor não indica qual a sua incerteza de medição. Esta dissertação teve como objetivos criar um modelo matemático do fenômeno, que não foi localizado na bibliografia existente; utilizar o modelo para a obtenção de uma estimativa da incerteza de medição, comparando as metodologias de incerteza do GUM e a que utiliza o método de Monte Carlo do Suplemento 1 e utilizando a segunda abordagem para validar a primeira; executar experimentos com um protótipo de um medidor desse tipo, comparando os resultados com um densímetro de laboratório; e realizar a caracterização metrológica do medidor. Todos esses objetivos foram cumpridos, sendo que a caracterização incluiu: sugestões de procedimentos de calibração e de medição; os resultados do experimento, incluindo a distribuição esperada na saída, com média Peso de um objeto – para um sólido rígido = 1,0500 g/cm(3) e incerteza expandida máxima de U95 por cento(p) = U95 por cento(1,0000) = 0,0028 g/cm(3) (fator de abrangência k = 1,96) no intervalo de medição entre 1,0000 g/cm(3) e 1,1000 g/cm(3); equações para a estimativa da incerteza de medidores desse tipo; a estimação de uma curva de incerteza para a faixa de calibração, segundo as medições de calibração; as contribuições de cada grandeza de entrada sobre a incerteza estimada de saída e algumas sugestões de como o medidor poderia ser modificado para melhorar o resultado. / [en] In the context of craft breweries, a recently invented liquid density meter works by leveraging an unusual principle: the displacement of the center of buoyancy. This meter obtains its measurements from its own tilt while it is floating, but its original implementation converts the accelerometer measurements into density measurements with a polynomial regression. However, it doesn t make temperature corrections, so that the influence of this quantity is disregarded in the regression. Additionally, the meter does not indicate its measurement uncertainty. The objective of this dissertation was to create a mathematical model of the phenomenon, which was not found in the existing bibliography; use the model to obtain an estimate of the measurement uncertainty, comparing the uncertainty methodologies of the GUM and the one that uses the Monte Carlo method of its Supplement 1 and using the second approach to validate the first; perform experiments with a prototype of such a meter, comparing the results with a laboratory densimeter; and perform the metrological characterization of the meter. All these objectives were met, and the characterization included: a suggestion of calibration and measurement procedures; the results of the experiment, including the expected output distribution, with mean of Weight of an object – for a rigid solid= 1.0500 g/cm(3) and maximum expanded uncertainty U95 percent(p) = U95 percent(1.0000) = 0.0028 g/cm(3) (k = 1.96 coverage factor) in the measurement range between 1.0000 g/cm(3) and 1.1000 g/cm(3); equations for estimating the uncertainty of this type of meter; the estimation of an uncertainty curve for the calibration range, according to the calibration measurements; the contributions of each input quantity to the estimated output uncertainty and some suggestions on how the meter could be modified to improve the result.

Welding is used extensively in aerospace, automotive, chemical, manufacturing, electronic and power-generation industries. Thermally-induced residual stresses due to welding can significantly impair the performance and reliability of welded structures. Numerical simulation of weld pool dynamics is important as experimental measurements of velocities and temperature profiles are difficult due to the small size of the weld pool and the presence of the arc. From a structural integrity perspective of welded structures, it is necessary to have an accurate spatial and temporal thermal distribution in the welded structure before stress analysis is performed. Existing research on weld pool dynamics simulation has ignored the effect of fluid flow in the weld pool on the temperature field of the welded joint. Previous research has established that the weld pool depth/width (D/W) ratio and Heat Affected Zone (HAZ) are significantly altered by the weld pool dynamics. Hence, for a more accurate estimation of the thermally-induced stresses it is desired to incorporate the weld pool dynamics into the analysis. Moreover, the effects of microstructure evolution in the HAZ on the mechanical behavior of the structure need to be included in the analysis for better mechanical response prediction. In this study, a three-dimensional model for the thermo-mechanical analysis of Gas Tungsten Arc (GTA) welding of thin stainless steel butt-joint plates has been developed. The model incorporates the effects of thermal energy redistribution through weld pool dynamics into the structural behavior calculations. Through material modeling the effects of microstructure change/phase transformation are indirectly included in the model. The developed weld pool dynamics model includes the effects of current, arc length, and electrode angle on the heat flux and current density distributions. All the major weld pool driving forces are included, namely surface tension gradient, plasma drag force, electromagnetic force, and buoyancy. The weld D/W predictions are validated with experimental results. They agree well. The effects of welding parameters (like welding speed, current, arc length, etc.) on the weld D/W ratio are documented. The workpiece deformation and stress distributions are also highlighted. The transverse and longitudinal residual stress distribution plots across the weld bead and their variations with welding speed and current are also provided. The mathematical framework developed here serves as a robust tool for better prediction of weld D/W ratio and thermally-induced stress evolution and distribution in a welded structure by coupling the different fields in a welding process. / Ph. D.

In this thesis, the ribbed ducts of the internal cooling passage in turbine blading are investigated to demonstrate the effects of high speed rotation. Rotation coupled with high temperature operating conditions alters the mean flow, turbulence, and heat transfer augmentation due to Coriolis and centrifugal buoyancy forces that arises from density stratification in the domain. Gas turbine engines operate in particle laden environments (sand, volcanic ash), and particulate matter ingested by the engine can make their way into the blade internal cooling passages over thousands of operating hours. These particulates can deposit on the walls of these cooling passages and degrade performance of the turbine blade. Large-Eddy Simulations (LES) with temperature dependent properties is used for turbulent flow and heat transfer in the ribbed cooling passages and Lagrangian tracking is used to calculate the particle trajectories together with a wall deposition model. The conditions used are Re=100,000, Rotation number, Ro = 0.0 and 0.2, and centrifugal Buoyancy parameters of Bo=0, 0.5, and 1.0. First, the independent effects of Coriolis and centrifugal buoyancy forces are investigated, with a focus on the additional augmentation obtained in heat transfer with the addition of centrifugal buoyancy. Coriolis forces are known to augment heat transfer at the trailing wall and attenuate the same at the leading wall. Phenomenological arguments stated that centrifugal buoyancy augments the effects of Coriolis forces in outward flow in the first pass while opposing the effect of Coriolis forces during inward flow in the second pass. In this study, it was found that in the first pass, centrifugal buoyancy had a greater effect in augmenting heat transfer at the trailing wall than in attenuating heat transfer at the leading wall. On the contrary, it aided heat transfer in the second half of the first pass at the leading wall by energizing the flow near the wall. Also, contrary to phenomenological arguments, inclusion of centrifugal buoyancy augmented heat transfer over Coriolis forces alone on both the leading and trailing walls of the second pass. Sand ingestion is then investigated, by injecting 200,000 particles in the size range of 0.5-175μm with 65% of the particles below 10 μm. Three duct wall temperatures are investigated, 950, 1000 and 1050 °C with an inlet temperature of flow and particles at 527 °C . The impingement, deposition levels, and impact characteristics are recorded as the particles move through the domain. It was found that the Coriolis force greatly increases deposition. This was made prevalent in the first pass, as 84% of the deposits in the domain occurred in the first pass for the rotating case, whereas only 27% of deposits occurred in the first pass for the stationary case with the majority of deposits occurring in the bend region. This was due to an increased interaction with the trailing wall in the rotating case whereas particles in the stationary case were allowed to remain in the mean flow and gain momentum, making rebounding from a wall during collision more likely than deposition. In contrast, the variation of wall temperatures caused little to no change in deposition levels. This was concluded to be a result of the high Reynolds number used in the flow. At high Reynolds numbers, the particles have a short residence times in the internal cooling circuit not allowing the flow and particles to heat up to the wall temperature. Overall, 87% of the injected particles deposited in the rotating duct whereas 58% deposited in the stationary duct. / Master of Science

Over the last two centuries, there has been a continual evolution of how occupied rooms are heated, with inventors competing to design new heating devices. In particular, there is a wide range of convector types, which vary in shape, size, design, material, operating medium and application. With approximately 190 million convectors installed in the UK alone, the question arises regarding the dependencies on the efficiency of heat distribution through convector-induced filling flows. A standard approach to evaluate convector performance is based on the convector strength only, the implication being the stronger the convector the better the performance. This work has gone beyond the limits of a stereotypical assessment in pursuit of answers regarding the physics of convector-induced filling and a new objective method to evaluate the efficiency of this transient process. The ultimate goal has been to provide a deep understanding of filling and stratification induced by a convector, in order to heat rooms rapidly and effectively. An experimental facility has been designed that approximates dynamic similarity between the experimental set-up and a real-life room with a convector. In the experiments, a rectangular sectioned water tank represents a room and a saline source rectangular sectioned panel with sintered side walls provides a convector representation. Experiments have been performed in water with a saline solution to ensure high Rayleigh numbers. Diagnostic techniques involve a combination of a shadowgraph method, a dye-attenuation method, direct salinity measurements and a new application of Particle Image Velocimetry (PIV). Interesting insight into convector-induced buoyancy-driven flows has been gained. As a result, new guidelines aimed at heating rooms more rapidly and effectively have been proposed. The key outcome that can be immediately applied is that, for a given convector strength, heat distribution with height can be improved by adjusting the convector position. For instance, faster filling leading to more uniform heat distribution occurs in rooms with convectors detached from side walls, due to large-scale mixing flows in the early period of filling. Also shorter convectors relative to the room height, positioned close to the floor level, promote faster and more uniform filling. An attempt to describe the transient filling has been made and to do so statistical methods, application specific, have been developed. As a result, the empirical equations describing both the filling rates in different stages of filling and the development of stratification have been derived, which rank the governing parameters, based on their importance, as either dominant or subordinate. Two dominant parameters governing filling flows are the non-dimensional accumulation parameter B and the Rayleigh number ΔRa, which are related to the convector strength. The impact of these two parameters is constant throughout the process. The parameters accounting for the system geometry and filling time (T) are subordinate parameters. Their impact, visible in the early period, decreases as filling continues.

Motivated by the existence of complex behaviors arising from interactions between chemistry and fluid dynamics in numerous research problems and every-day life situations, we theoretically investigate the dynamics resulting from the interplay between chemistry, diffusion, and fluid motions in a reactive aqueous solution. As a chemical reaction induces changes in the temperature and in the composition of the reactive medium, such a reaction can modify the properties of the solution (density, viscosity, surface tension,…) and thereby trigger convective motions, which in turn affect the reaction. Two classes of convective flows are commonly occurring in solutions open to air, namely Marangoni flows arising from surface tension gradients and buoyancy flows driven by density gradients. As both flows can be induced by compositional changes as well as thermal changes and in turn modify them, the resulting experimental dynamics are often complex. The purpose of our thesis is to gain insight into these intricate dynamics thanks to the theoretical analysis of model systems where only one type of convective flow is present. In particular, we numerically study the spatio-temporal evolution of model chemical fronts resulting from the coupling between reactions, diffusion, and convection. Such fronts correspond to self-organized interfaces between the products and the reactants, which typically have different density and surface tension. Fluid motions are therefore spontaneously induced due to these differences across the front. In this context, we first address the propagation of a model autocatalytic front in a horizontal solution layer, in the presence of pure Marangoni convection on the one hand and of pure buoyancy convection on the other hand. We evidence that, in both cases, the system attains an asymptotic dynamics characterized by a steady fluid vortex traveling with the front at a constant speed. The presence of convection results in a deformation and acceleration of the chemical front compared to the reaction-diffusion situation. However we note important differences between the Marangoni and buoyancy cases that could help differentiate experimentally between the influence of each hydrodynamic effect arising in solutions open to the air. We also consider how the kinetics and the exothermicity of the reaction influence the dynamics of the system. The propagation of an isothermal front occurring when two diffusive reactants are initially separated and react according to a simple bimolecular reaction is next studied in the presence of chemically-induced buoyancy convection. We show that the reaction-diffusion predictions established for convection-free systems are modified in the presence of fluid motions and propose a new way to classify the various possible reaction-diffusion-convection dynamics./En induisant des changements de composition et de température, une réaction chimique peut modifier les propriétés physiques (densité, viscosité, tension superficielle,…) de la solution dans laquelle elle se déroule et ainsi générer des mouvements de convection qui, à leur tour, peuvent affecter la réaction. Les deux sources de convection les plus courantes en solution ouverte à l’air sont les gradients de tension superficielle, ou effets Marangoni, et les gradients de densité. Comme ces deux sources sont en compétition et peuvent toutes deux résulter de différences de concentration ou de température, les dynamiques observées expérimentalement sont souvent complexes. Le but de notre thèse est de contribuer à la compréhension de telles dynamiques par une étude théorique analysant des modèles réaction-diffusion-convection simples. En particulier, nous étudions numériquement l’évolution spatio-temporelle de fronts chimiques résultant du couplage entre chimie non-linéaire, diffusion et hydrodynamique. Ces fronts constituent l’interface auto-organisée entre les produits et les réactifs qui typiquement ont des densités et tensions superficielles différentes. Des mouvements du fluide peuvent dès lors être spontanément initiés dus à ces différences au travers du front. Dans ce contexte, nous étudions la propagation d’un front chimique autocatalytique se propageant dans une solution aqueuse horizontale, d’une part en la seule présence d’effets Marangoni, et d’autre part en présence uniquement d’effets de densité. Nous avons montré que dans les deux cas, le système atteint une dynamique asymptotique caractérisée par la présence d’un rouleau de convection stationnaire se propageant à vitesse constante avec le front. Ce front est à la fois déformé et accéléré par les mouvements convectifs par rapport à la situation réaction-diffusion. Nous avons mis en évidence d’importantes différences entre les deux régimes hydrodynamiques qui pourraient aider les expérimentateurs à différencier les effets de tension superficielle de ceux de densité générés par la propagation de fronts chimiques en solution. Nous avons également considéré l’influence de la cinétique de réaction ainsi que de l’exothermicité sur la dynamique de ces fronts. Enfin, nous avons étudié la propagation en présence de convection d’un front de réaction impliquant deux espèces de densités différentes, initialement séparées et réagissant selon une cinétique bimoléculaire. Nous avons montré que la convection modifie les propriétés réaction-diffusion du système et nous proposons de nouveaux critères pour classifier les dynamiques réaction-diffusion-convection.