The knowledge of the behavior of non-spherical particles suspended in turbulent flows covers a wide range of applications in engineering and science. Dispersed two-phase flows and turbulence are the most challenging subjects in engineering, and when combined it gives rise to more complexities as the result of the inherent stochastic nature of the turbulence of the carrier-phase together with the random distribution of the dispersed phase. Moreover, for anisotropic particles the coupling between the translation and rotation of particle increases the complication. Because of the practical importance of prolate particleladen turbulent flows, the plenty of numerical and experimental works have been conducted to study such suspensions. Numerical approaches have given valuable insight of turbulent suspension flows, although the computation has been only carried out at the macro scale and models, not including flow distortion around the particle, comprise the detail of the flow in the order of a particle size. In addition, the model of the forces imposed on the particle by the fluid and mass point treatment are strictly valid for infinitely small particle having size less than all scales of the fluid turbulence. Fully resolved solution at the scale of the dispersed phase in turbulent flows for high Reynolds number has been recently performed but is still a challenge. On the other hand, the presence of particle as the dispersed phase makes experimental measurements much more complicated than those with single phase as a result of particles interference. The area of considerable difficulty with this type of experiments is the measurement of the fluid-phase velocity remarkably close to the particle surface. Generally, experimental researches have been concentrated on measuring the mean velocity and Reynolds stresses of the carrier-phase, and the mean velocity, fluctuations, orientation and accumulation of the non-spherical particles. Higher-order quantities, including Lagrangian particle velocity correlations, the carrier-phase turbulence modulation, and two-particle and particlefluid velocity correlations are also of interest. It has been found that the rotational and translational movements of the fibershaped particle depend on the nature of carrier-phase field and fiber characteristics such as aspect ratio, fiber Stokes number, fiber Reynolds number, and the ratio of fiber to flow length scale. With the development of PIV (Particle Image Velocimetry) and PTV (Particle Tracking Velocimetry) techniques, it has been appeared that combined PIV/PTV will be the best available choice for the experimental study of dispersed two-phase flows. The purpose of combined PIV/PTV measurement of two-phase systems is simultaneous measurements of fluid and suspended objects, where the PIV measurement of the fluid phase are combined with PTV measurement of the dispersed phase. The objective of this doctoral thesis is to study the behavior of rod-like particles suspended in wall-bounded turbulent flow through simultaneous PIV/PTV measurements of the velocity of the flow field and particle motion. As a representative of rod-like particles, I have employed cellulose acetate fibers with the length to diameter ratio (aspect ratio) larger than one. Here, It has been considered only dilute suspensions with no flocculation; thus fiber-fiber interaction is negligible. The measurements have been conducted within the parallel planes (2D view) illuminated by laser in the streamwise direction in thin film suspension flowing on the water table setup at Linné FLOW Centre, KTH Mechanics Lab. It is shown that this setup is a well-behaved experimental model of half channel flows often used in Direct Numerical Simulation (DNS) investigations. Therefore, the experimental results are comparable to their DNS counterpart where it is convenient. A single camera PIV technique has been used to measure flowing suspension. Therefore, it has been needed to preprocess images using a spatial median filter to separate images of two phases, tracer particles as representative of fluid and fibers suspended. The well-known PIV processing algorithms have been applied to the phase of fluid. I have also introduced a novel algorithm to recognize and match fibers in consecutive images to track fibers and estimate their velocity. It is not feasible to study all relevant aspects of particle-laden turbulent flows in a single study. In this study, I present the statistics of the rotational and translational motion of fiber-like particles and the surrounding fluid velocity. To the author’s knowledge, remarkably little experimental work has been published to date on simultaneous measurement of fiber motion and turbulence field in a turbulent fiber suspension flow to reveal dynamics of fibers in this regime. Therefore, the results of this work will be profitable in better understanding of such multiphase flows. The statistical analysis of the translational motion of fibers shows that the size of fiber is a significant factor for the dynamical behavior of the fiber near the wall. It has been observed that, in the region near the wall, the probability of presence of the long fibers is high in both the high-speed and low-speed streaks of flow, and the mean velocity of fibers almost conforms to the mean velocity of flow; whereas the short fibers are mostly present in the low-speed areas, and the fiber mean velocity obey the dominant flow velocity in these areas. In the far-wall regions, the translation of fibers is practically unaffected by the aspect ratio, whereas it depends crucially on the wall-normal distance. Moreover, it was found that in the case of long fibers near the wall, the low speed fibers mostly are orientated in streamwise direction. On the other hand, there is no preferential orientation for fast long fibers. Although wall-normal velocities were not measured in this study, it is hypothesized that this behavior is a result of fibers being affected by the sweep and ejection events known to occur in wall-bounded turbulent flow. The fast fibers are in sweep environment and comes from the upper layer. The low speed fibers are into ejection areas in the vicinity of the wall, and the wall has a stabilizing effect on them. The short fibers are still oriented mostly in streamwise direction for a certain range of low velocity. Furthermore, since a considerable change of the fiber behavior is observed in a certain ratio of the fiber length to the fiber distance from the solid wall, it is supposed that this ratio is also a prominent parameter for the behavior of fiber near the wall. The results presented are in terms of viscous wall units wherever are denoted by superscript “+”.

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Ce travail est consacré à l'étude expérimentale des écoulements diphasiques et triphasiques d'inclusions (bulles, gouttes, sphères) en milieux tant newtoniens que non newtoniens à l'échelle microscopique et mésoscopique, en utilisant la visualisation par une caméra rapide, la vélocimétrie par images des particules (PIV) ainsi que la micro-vélocimétrie par images des particules. Des bulles et des gouttes ont été étudiées expérimentalement depuis leur formation, en passant par leur déformation jusqu'à leur coalescence. La formation de bulles dans des micro-mélangeurs a été étudiée et caractérisée par l'obtention de champs de vitesses. Différents paramètres, tels que le cisaillement, la géométrie de la zone de formation, les débits ou encore les propriétés physiques ont été testés afin de développer des lois d'échelles. La traversée d'une interface liquide-liquide par une inclusion a été abordée par des expériences originales, permettant de décrire la dynamique du phénomène, de définir des nombres adimensionnels et de mettre en évidence des instabilités interfaciales. L'effet Weissenberg a également été étudié aux différentes échelles afin de comprendre les phénomènes conduisant à son amplification. Enfin, en milieu viscoélastique et rhéofluidifiant, nous avons caractérisé l'écoulement autour d'une inclusion isolée solide par l'obtention de champs de vitesses. Ces résultats ont permis de confirmer l'origine viscoélastique du sillage négatif et de prédire ses caractéristiques / The present work was devoted to the experimental study of the multiphase flow around inclusions in both Newtonian and non-Newtonian media at respectively microscopic and mesoscopic scales, by means of the Particle Image Velocimetry (both PIV and µ-PIV) and fast camera visualization. Bubbles and drops were experimentally studied starting from their formation, the rising and up to their coalescence and fragmentation. Bubble formation in micro-mixers was also investigated and characterized by measuring the liquid velocity fields. Different parameters, such as the shear rate, the geometry of the micro-mixer, the flow rates or the physical properties were tested to develop correlations of power-law kind. The deformation of a liquid-liquid interface due to the passage of an inclusion was investigated by original experiments in order to observe and describe the dynamics of the phenomenon, to define the reliable dimensionless numbers and also to highlight several interfacial instabilities. The Weissenberg effect was also studied at different scales in various non-Newtonian fluids in comparison with Newtonian fluids to understand the amplification phenomena under the combining effects of instability and normal forces. Finally, the flow around an isolated solid inclusion was characterized by performing the measurements of velocity fields in viscoelastic and shear-thinning fluids. These results were used to confirm the viscoelastic origin of the negative wake behind the solid sphere and to model its characteristics

This thesis reports on investigations carried out to study of the effect of horizontal wall jets on rough, fixed and mobile beds in open channel flow. Experimental tests were carried out, using fixed and mobile sediment beds. Computer simulation models for the flow within the jet and resulting sediment transport were developed and their results analysed in this study. In the experimental phase, tests were carried out with both fixed and mobile sediment beds. The shape of the water surface, numerous point velocity measurements and measurements of the evolving scour hole shape were made. Detailed descriptions of the turbulent flow field over a fixed rough bed and for scour holes at equilibrium were obtained for a range of initial jet conditions. Fully turbulent, multiphase flow was modelled using the Fluent Computational Fluid Dynamics software. This was used to analyze the flow caused by a jet in a rectangle open-channel with a rough bed, and also the flow pattern in a channel with a local scour hole. The volume of fluid (VOF) multiphase method and K- model was used to model the fluid flow in both cases. The model predictions of velocity and shear stress were compared against experimental observations. The experimental data was used to develop new empirical relationships to describe the pattern of boundary shear stress caused by a wall jet over fixed beds and in equilibrium scour holes. These relationships were linked with existing bed-load transport rate models in order to predict the temporal evolution of scour holes. An analytical model describing the relationship between the wall jet flow and the development of a local scour hole shape was reported and its predictions compared with experimental data.

Ce manuscrit s'intéresse au devenir de contaminants organiques dans le sol, et plus précisément celui des composés organo-halogénés volatils (COHV).Il propose des outils d'aide à la décision en utilisant la modélisation numérique appliquée à des problématiques environnementales portant sur le traitement de sites et sols pollués par des COHV. Il présente, à ma connaissance, la première modélisation numérique en 3D, grâce au simulateur TMVOC, d'une technique de dépollution physique, à savoir le pompage réussi au sein d'un aquifère d'un liquide en phase non-aqueuse plus dense que l'eau ou Dense Non-Aqueous Phase Liquid (DNAPL). Les très bons résultats de cette simulation permettent d’envisager l’optimisation d’un système de pompage asservi pour dépolluer un site contaminé aux COHV. Cette thèse s'intéresse aussi à une méthode de d'évaluation, à la fois qualitative et quantitative, de l'efficacité du pompage : un test de traçage utilisant des traceurs bisolubles à coefficients de partage variables (partitioning interwell tracer test – PITT). Ce PITT permet de connaître à la fois la répartition spatiale, au sein d’un aquifère, d’une bulle de DNAPL et aussi d’en évaluer sa saturation et donc son volume. Ce manuscrit met à disposition des outils élaborés et adaptés au traitement d'un DNAPL dans un aquifère. La combinaison des deux techniques présentées, à savoir la modélisation d'un pompage de DNAPL et un PITT, sont parfaitement reproductibles dans des environnements similaires et à l'échelle industrielle. Enfin, ces méthodes permettent de réduire considérablement les coûts de caractérisation (PITT) et d'exploitation par l'optimisation de systèmes de pompage / This manuscript deals with the fate of organic contaminants in soil, more precisely of volatile organo-chlorinated compounds (VOHC) and offers some decision making techniques and tools using numerical modelling applied to environmental issues about the treatment of soils contaminated by VOHC. It presents, to the best knowledge of the auhor, the first 3D numerical modelling, with the simulator TMVOC, of a physical treatment technique, namely the successful pumping within an aquifer, of a Dense Non-Aqueous Phase Liquid (DNAPL). The very good results of this simulation give the opportunity to design a controlled and automated pumping system to remediate a polluted site. This thesis also deols with a tracer test assessment method, both qualitative and quantitative, for the efficiency of this pumping : a partitioning interwell tracer test (PITT). The PITT allows us to determine the spatial repartion of the DNAPL and also to assess its saturation, hence its volume. This manuscript offers elaborated tools adapted to the remediation of a DNAPL in an aquifer. The combination of these two techniques, namely the DNAPL pumping and the PITT, are perfectly reproducible in similar environments up to an industrial scale. Finally, exploitation and characterisation costs for DNAPL remediation can be extremely reduced by numerical modelling and optimisation

In the present work, the flow behavior of an oil-in-water emulsion around and inside the measurement chamber of an in-line optical sensor probe is studied. The emulsion consists of a metalworking fluid, with oil droplets diameter ranging from 100 nanometers to 100 micrometers. The design of the UV-Vis light spectrometer probe is in accordance with the concept proposed in the research project named EPM (Emulsion Process Monitor in Metalworking Processes), carried out within the scope of the BRAGECRIM program between the University of São Paulo and the University of Bremen. This study is based on the numerical simulation of the interactions between the emulsion and the measurement system using computational fluid dynamic techniques, and is aimed at evaluating the effects of the probe geometry, its position relative to the flow field, and fluid properties on the expected spectrometer readings. Such effects are correlated with changes in droplet concentration and or droplet size segregation inside the measurement chamber of the optical probe, which can cause changes in the scattered light intensity readings. Segregation effects due to flow disturbances around the probe can be neglected under normal measurement conditions, with the probe facing the slit area inlet against the flow stream. Based on the simulation results, even if the probe is misplaced, the effect on the measurements is still insignificant. In-situ measurements carried out in a laboratory set up installed in the injection tube of a drilling machine support the simulation results, since no segregation effect related to the measurement system was observed. In addition to the study, the possibility of bacteria attachment on the internal glass walls of the probe was evaluated and it was found that when the flow velocity is large enough to produce a wall shear stress of about 3-5 Pa the bacterial contamination may be avoided. Changes in the probe geometry are proposed in order to attain an isokinetic condition for the flow around and inside the probe, resulting in a higher wall shear stress for lower inlet flow velocities. An additional study was performed using a tracking particle model to understand the relevance of the individual particles behavior under different flow conditions. The results do not indicate any significant effect on the measurements inside the probe, although additional studies should be carried out in this topic by considering a population balance model for the oil droplets. / O presente trabalho tem como objetivo o estudo do comportamento do escoamento de uma emulsão do tipo óleo - em água que flui no interior de câmara/duto de medição e que tem como obstáculo em seu caminho uma sonda de um sensor óptico, sensor óptico este que deve avaliar em tempo real a estabilidade da emulsão onde está inserido. A emulsão é constituída por um fluido de corte para usinagem, com gotículas de óleo de diâmetro variando de 100 nanômetros para 100 micrometros. A sonda utilizada junto ao espectrômetro de luz UV- Vis está de acordo com o conceito proposto no projeto de pesquisa chamado EPM (Emulsion Process Monitor in Metalworking Fluid), realizado no âmbito do programa BRAGECRIM entre a Universidade de São Paulo e a Universidade de Bremen. Este estudo baseia-se na simulação numérica das interações entre a emulsão e o sistema de medição proposto, utilizando técnicas de Fluido Dinâmica Computacional (CFD), e tem por objetivo avaliar os efeitos da geometria da sonda, a sua posição em relação ao campo do escoamento, e propriedades do fluido, em especial as propriedades a serem medidas pelo espectrômetro. Tais efeitos estão correlacionadas com alterações na concentração de gotas e a segregação ou o tamanho das gotas dentro da câmara de medição da sonda óptica, o que pode causar mudanças nas leituras de intensidade de luz difusa. Efeitos de segregação devido a perturbações do escoamento em torno da sonda podem ser negligenciados, em condições normais de medição, com a sonda voltada para frente e sua área de entrada contra a corrente do escoamento. Com base nos resultados de simulação, mesmo que a sonda seja deslocada, o efeito sobre as medições ainda é insignificante. Medições foram efetuadas em laboratório e também foram realizadas medições in-situ utilizando um adaptador de medição acoplado diretamente no tubo de injeção de fluido de corte da máquina de perfuração, estes testes foram feitos para de validar os resultados obtidos por simulação, uma vez que não se observou qualquer efeito de segregação relacionada com o sistema de medição. Além disso, foi acrescentada ao estudo, a possibilidade de fixação de bactérias nas paredes de vidro internas da sonda e verificou-se que quando a velocidade de escoamento é suficientemente grande para produzir uma tensão de cisalhamento de cerca de 3-5 Pa a fixação de bacteriana pode ser evitado. Aproveitando os resultados do estudo para prevenção de contaminação por bactéria, mudanças na geometria da sonda foram propostas a fim de atingir uma condição isocinética para o escoamento ao redor e dentro da sonda, resultando em uma maior tensão de cisalhamento para baixas velocidades de fluxo de entrada. Por fim um estudo adicional foi realizado utilizando um modelo de rastreamento de partículas para compreender a relevância do comportamento individual de cada partícula no escoamento da emulsão. Os resultados não indicam qualquer efeito significativo sobre as medições no interior da sonda, embora estudos adicionais devem ser realizados neste tópico, considerando um modelo de balanço populacional para as gotículas de óleo.

Uma das dificuldades relacionadas com a exploração de petróleo é o transporte de óleo pesado, que devido a sua alta viscosidade, acarreta em uma elevada perda de carga no sistema. Para proporcionar economia de energia aplica-se o método do Core Annular Flow (CAF) onde é utilizado um escoamento anular bifásico em que a água escoa na periferia da tubulação para redução do gasto energético. O presente trabalho visou compreender e reproduzir este fenômeno, desenvolvendo simulações em CFD através do pacote comercial ANSYS FLUENT considerando o escoamento 3D, turbulento, isotérmico e incompressível para casos estacionários e transientes. A interface entre a água e o óleo foi adequadamente reproduzida em diferentes geometrias como tubo reto e com curva. O método LES para simulação de grandes escalas provou ser o melhor método de turbulência dentre os testados, como k-epsilon e modelo de tensores de Reynolds, de forma com que a interface fosse representada corretamente. O modelo para sistema multifásico adotado foi o Volume de Fluido (VOF), comparado com o comportamento experimental e com dados da literatura. Os fenômenos de swirl observados experimentalmente também foram reproduzidos de forma satisfatória. / One of the difficulties related to oil exploration is the transportation of heavy oil, which due to its high viscosity, causes a high pressure drop in the system. In order to provide energy savings, the Core Annular Flow (CAF) method applies where a two-phase annular flow occurs in which water flows at the periphery adjacent to the pipe to reduce energy expenditure. The present work aimed to understand and reproduce this phenomenon, developing CFD simulations through the commercial package ANSYS FLUENT considering flow as 3D, turbulent, isothermal and incompressible for stationary and transient cases. The interface between water and oil has been properly reproduced in different geometries such as straight pipe and pipe with a curve. The LES method for large scale simulation proved to be the best turbulence method among the tested, such as k-epsilon and Reynolds stress model, so that the interface was correctly represented. The model for the multiphase system adopted was the Volume of Fluid (VOF), compared to the experimental behavior and with data from the literature. The experimentally observed swirl phenomena were also reproduced satisfactorily.

Simulating the exact chaotic turbulent flow field about any geometry is a dilemma between accuracy and computational resources, which has been continuously studied for just over a hundred years. This thesis is a complete walk-through of the entire process utilized to approximate the flow ingested by a Sevik-type rotor based on solutions to the Reynolds Averaged Navier-Stokes equations (RANS). The Multiple Reference Frame fluid model is utilized by the code of ANSYS-FLUENT and results are validated by experimental wake data. Three open rotor configurations are studied including a uniform inflow and the rotor near a plate with and without a thick boundary layer. Furthermore, observations are made to determine the variation in velocity profiles of the ingested turbulent flow due to varying flow conditions. / by Felipe Ferreira Lachowski. / Thesis (M.S.C.S.)--Florida Atlantic University, 2013. / Includes bibliography. / Mode of access: World Wide Web. / System requirements: Adobe Reader.

This thesis presents an investigation on multiphase reactor hydrodynamics using magnetic resonance imaging (MRI). The study demonstrates experimental techniques by which computational and quasi-analytical fluid models may be validated. Three types of industrially-important multiphase reaction vessels are considered: a co-current upflow gas-liquid-solid bed, a co-current downward trickle bed (gas, liquid, solid), and a gas-solid fluidised bed. These reactors were selected as they commonly demonstrate local hydrodynamic anisotropy which affects the global performance of industrial units. MRI was used to obtain 2D velocity images of the gas and liquid phases in the packed beds, and of the gas and the solid phases in the fluidised bed. This study reports the first spatially resolved velocity measurements of both the gas and liquid phases in a co-current upflow bed, and the gas and solid phases of an isolated bubble in a fluidised bed. The experimental vessels were: 52 mm in diameter using 5 mm glass spheres in the upflow bed at 8 bara, 27 mm with 5 mm glass spheres in the trickle bed at 6.75 bara, and 52 mm using 1.2 mm poppy seeds as the fluidised particles at 8.5 bara. The experiments were conducted at a laboratory temperature of 25.0 ± 3.0 °C. In the upflow bed, time-averaged velocity images were acquired over a 2.5 h experimental time. This was done to capture the steady state behaviour of the vessel operating in the pulsing flow regime. The temporally-stable trickle flow state in the trickle bed was imaged over 15-100 minutes. In both packed beds, severe spatial anisotropy in the distribution of flow between pores was revealed. Furthermore, the data were used to determine classical design features such as catalyst wetting and liquid holdup which compared well with literature models. The trickle bed data were further analysed using a morphological algorithm which unambiguously identified the gas-liquid and liquid-solid interfaces. The interfacial flow fields were found to be similar to the bulk flow, with most voxels exhibiting static behaviour. The amount of interaction between the phases was found to be minimal, which is typical of the low interaction regime. A single bubble injection system was employed in the fluidised bed which allowed the injection of isolated bubbles into the incipiently fluidised bed. It also enabled the triggered acquisition of NMR data at precise time intervals. The bubble was found to be an indented ellipsoidal shape, which rose with atypical behaviour which caused it to collapse. Rise velocity was found to be consistent with theory, and the injected bubbles were sufficiently spatially reproducible to acquire 2D velocity images using single-point imaging. These velocity images showed flow behaviour characteristic of a 'fast' rising bubble, with a gas recirculation cloud 37 mm in diameter. The particle field was shown to have very high flow in the bubble wake, revealing the mechanism of bubble collapse. The flow data were compared to classical two-phase fluidisation theory, which revealed noteworthy differences in the division of flow between the particulate and bubbling regions.

Uma das dificuldades relacionadas com a exploração de petróleo é o transporte de óleo pesado, que devido a sua alta viscosidade, acarreta em uma elevada perda de carga no sistema. Para proporcionar economia de energia aplica-se o método do Core Annular Flow (CAF) onde é utilizado um escoamento anular bifásico em que a água escoa na periferia da tubulação para redução do gasto energético. O presente trabalho visou compreender e reproduzir este fenômeno, desenvolvendo simulações em CFD através do pacote comercial ANSYS FLUENT considerando o escoamento 3D, turbulento, isotérmico e incompressível para casos estacionários e transientes. A interface entre a água e o óleo foi adequadamente reproduzida em diferentes geometrias como tubo reto e com curva. O método LES para simulação de grandes escalas provou ser o melhor método de turbulência dentre os testados, como k-epsilon e modelo de tensores de Reynolds, de forma com que a interface fosse representada corretamente. O modelo para sistema multifásico adotado foi o Volume de Fluido (VOF), comparado com o comportamento experimental e com dados da literatura. Os fenômenos de swirl observados experimentalmente também foram reproduzidos de forma satisfatória. / One of the difficulties related to oil exploration is the transportation of heavy oil, which due to its high viscosity, causes a high pressure drop in the system. In order to provide energy savings, the Core Annular Flow (CAF) method applies where a two-phase annular flow occurs in which water flows at the periphery adjacent to the pipe to reduce energy expenditure. The present work aimed to understand and reproduce this phenomenon, developing CFD simulations through the commercial package ANSYS FLUENT considering flow as 3D, turbulent, isothermal and incompressible for stationary and transient cases. The interface between water and oil has been properly reproduced in different geometries such as straight pipe and pipe with a curve. The LES method for large scale simulation proved to be the best turbulence method among the tested, such as k-epsilon and Reynolds stress model, so that the interface was correctly represented. The model for the multiphase system adopted was the Volume of Fluid (VOF), compared to the experimental behavior and with data from the literature. The experimentally observed swirl phenomena were also reproduced satisfactorily.