Even though fluid mechanics is well developed as a science, there are many physical phenomena that we do not yet fully understand. One of these is the deformation rates and fluid stresses generated in a boundary layer for a non-Newtonian fluid. One such non-Newtonian fluid would be a waxy crude oil flowing in a centrifugal pump. This type of flow can be numerically modeled by a rotating disk system, in combination with an appropriate constitutive equation, such as the relation for a Bingham fluid. A Bingham fluid does not begin to flow until the stress magnitude exceeds the yield stress. However, experimental measurements are also required to serve as a database against which the results of the numerical simulation can be interpreted and validated. The purpose of the present research is to gain a better understanding of the behavior of a Bingham fluid in the laminar boundary layer on a rotating disk. For this project, two different techniques were employed: numerical simulation, and laboratory investigations using Particle Image Velocimetry (PIV) and flow visualization. Both methods were applied to the flow of a Bingham fluid over a rotating disk. In the numerical investigations, the flow was characterized by the dimensionless yield stress Bingham number, By, which is the ratio of the yield and viscous stresses. Using von Kármáns similarity transformation, and introducing the rheological behavior of the fluid into the conservation equations, the corresponding nonlinear two-point boundary value problem was formulated. A solution to the problem under investigation was obtained by numerical integration of the set of Ordinary Differential Equations (ODEs) using a multiple shooting method. The influence of the Bingham number on the flow behavior was identified. It decreases the magnitude of the radial and axial velocity components, and increases the magnitude of the tangential velocity component, which has a pronounced effect on the moment coefficient, CM, and the volume flow rate, Q. In the laboratory investigations, since the waxy crude oils are naturally opaque, an ambitious experimental plan to create a transparent oil that was rheologically similar to the Amna waxy crude oil from Libya was developed. The simulant was used for flow visualization experiments, where a transparent fluid was required. To fulfill the demand of the PIV system for a higher degree of visibility, a second Bingham fluid was created and rheologically investigated. The PIV measurements were carried out for both filtered tap water and the Bingham fluid in the same rotating disk apparatus that was used for the flow visualization experiments. Both the axial and radial velocity components in the (r-z) plane were measured for various rotational speeds. Comparison between the numerical and experimental results for the axial and radial velocity profiles for water was found to be satisfactory. Significant discrepancies were found between numerical results and measured values for the Bingham fluid, especially at low rotational speeds, mostly relating to the formation of a yield surface within the tank. Even though the flow in a pump is in some ways different from that of a disk rotating in a tank, some insight about the behavior of the pump flow can be drawn. One conclusion is that the key difference between the flow of a Bingham fluid in rotating equipment from that of a Newtonian fluid such as water relates to the yield surface introduced by the yield stress of the material, which causes an adverse effect on the performance and efficiency of such equipment.

Even though fluid mechanics is well developed as a science, there are many physical phenomena that we do not yet fully understand. One of these is the deformation rates and fluid stresses generated in a boundary layer for a non-Newtonian fluid. One such non-Newtonian fluid would be a waxy crude oil flowing in a centrifugal pump. This type of flow can be numerically modeled by a rotating disk system, in combination with an appropriate constitutive equation, such as the relation for a Bingham fluid. A Bingham fluid does not begin to flow until the stress magnitude exceeds the yield stress. However, experimental measurements are also required to serve as a database against which the results of the numerical simulation can be interpreted and validated. The purpose of the present research is to gain a better understanding of the behavior of a Bingham fluid in the laminar boundary layer on a rotating disk. For this project, two different techniques were employed: numerical simulation, and laboratory investigations using Particle Image Velocimetry (PIV) and flow visualization. Both methods were applied to the flow of a Bingham fluid over a rotating disk. In the numerical investigations, the flow was characterized by the dimensionless yield stress Bingham number, By, which is the ratio of the yield and viscous stresses. Using von Kármáns similarity transformation, and introducing the rheological behavior of the fluid into the conservation equations, the corresponding nonlinear two-point boundary value problem was formulated. A solution to the problem under investigation was obtained by numerical integration of the set of Ordinary Differential Equations (ODEs) using a multiple shooting method. The influence of the Bingham number on the flow behavior was identified. It decreases the magnitude of the radial and axial velocity components, and increases the magnitude of the tangential velocity component, which has a pronounced effect on the moment coefficient, CM, and the volume flow rate, Q. In the laboratory investigations, since the waxy crude oils are naturally opaque, an ambitious experimental plan to create a transparent oil that was rheologically similar to the Amna waxy crude oil from Libya was developed. The simulant was used for flow visualization experiments, where a transparent fluid was required. To fulfill the demand of the PIV system for a higher degree of visibility, a second Bingham fluid was created and rheologically investigated. The PIV measurements were carried out for both filtered tap water and the Bingham fluid in the same rotating disk apparatus that was used for the flow visualization experiments. Both the axial and radial velocity components in the (r-z) plane were measured for various rotational speeds. Comparison between the numerical and experimental results for the axial and radial velocity profiles for water was found to be satisfactory. Significant discrepancies were found between numerical results and measured values for the Bingham fluid, especially at low rotational speeds, mostly relating to the formation of a yield surface within the tank. Even though the flow in a pump is in some ways different from that of a disk rotating in a tank, some insight about the behavior of the pump flow can be drawn. One conclusion is that the key difference between the flow of a Bingham fluid in rotating equipment from that of a Newtonian fluid such as water relates to the yield surface introduced by the yield stress of the material, which causes an adverse effect on the performance and efficiency of such equipment.

Orientador: José Manoel Balthazar / Banca: Bento Rodrigues de Pontes Junior / Banca: Vicente Lopes Junior / Resumo: Nesta dissertação faz-se a análise da dinâmica não-linear de um sistema que possui preso a ele um motor de corrente contínua com potência limitada, onde são acoplados uma mola não linear e um amortecedor do tipo magneto-reológico (dispositivo que tem como fluído interno o fluído magneto-reológico). Com o objetivo de estudar e analisar a influência deste dispositivo na dinâmica do oscilador. Inicialmente apresenta-se uma breve descrição do tipo de problema estudado (sistemas não ideais) e uma revisão dos principais trabalhos que têm sido feitos tendo este dispositivo como foco de estudos. Apresentam-se os modelos utilizados para prever o comportamento destes dispositivos e também uma síntese de alguns modelos (mecânicos e matemáticos) mais elaborados e completos utilizados também para prever este comportamento. A partir daí é feita a apresentação do modelo que prevê o comportamento do amortecedor MR utilizado (modelo Bingham) e de uma suavização do mesmo, utilizada com o objetivo de melhorar o comportamento computacional do modelo inicial, junto a isso, apresenta-se a modelagem matemática do problema visando à obtenção das equações governantes do sistema. Faz-se então a análise do sistema durante a passagem pela ressonância (onde a freqüência de rotação do motor CC se aproxima numericamente e passa pela freqüência natural do sistema), analisando o efeito deste amortecedor durante esta passagem, analisa-se também a influência do dispositivo na evolução do Efeito Sommerfeld, um dos fenômenos intrínsecos desta classe de sistemas e também é feita uma analise do sistema em condições de movimento caótico também com o objetivo de prever o comportamento deste dispositivo, tudo isso é executado através da integração numérica das equações governantes do sistema. Para efeito de ilustração apresenta-se, também, uma pequena amostra do comportamento do sistema ideal paralelo ao estudado ... / Abstract: In this dissertation it made the analysis of the nonlinear dynamics of a system that possess to fixed it a direct-current motor with limited power, where is connected a damper of the type Magnetorheological (device that has as fluid intern the fluid Magnetorheological), with the objective to study and to analyze the influence of this device in the dynamics of the oscillator. Initially one brief description of the type of studied problem is presented (nonideal systems) and a revision of the main works that have been made having this device as focus of studies. The used models are presented to predict the behavior of these devices and also a synthesis of some models (mechanics and mathematicians) more elaborated and complete also used to predict this behavior. To continue this work, we present the model that predict the behavior of used MR damper (the Bingham Model) and a smoothing of the same, used with the objective to improve the computational behavior of the initial model and the mathematical modeling of the problem, together this, we show mathematical modeling of this problem aiming at to the attainment of the governing equations of the system. The analysis of the system it is made then during the passage for the resonance (where the frequency of DC motor it approaches numerically and crosses the natural frequency of the system), analyzing the effect of this damper during this passage, the influence of the device in the evolution of Sommerfeld Effect is also analyzed, one of the intrinsic phenomena of this classroom of systems and also is made a analyzes of the system in conditions of chaotic motions also with the objective to predict the behavior of this device, everything this is executed through the numerical integration of the governing equations of the system. For illustration effect it is presented, also, a small sample of the behavior of the parallel ideal system to the studied one, also with the presence of shock absorber MR, in the.. / Mestre

[pt] Como parte da linha de pesquisa na área de estimulação de poços de petróleo, foi montado um viscosímetro tubular para análise das características de comportamento reológico de um fluido de fraturamento hidráulico (HPGUAR), dotado de dispositivo para preparação do fluido . Os dados experimentais obtidos foram tratados analiticamente segundo dois tipos de equações constitutivas: as do Modelo de Ostwald, amplamente utilizadas pelos pesquisadores da área de Engenharia de Petróleo, e as do Modelo de Bingham. Pela avaliação dos resultados obtidos, pode-se concluir que parecem ocorrer evidências de que o Modelo de Bingham possa ser mais adequado, por retratar de forma mais independente as contribuições isoladas do atrito viscoso e da componente gerada pela viscosidade plástica, na análise teológica do HPGUAR. Sugere-se que investigações mais detalhadas devam ser conduzidas, posto que eventualmente poderiam ser bastante úteis no esclarecimento da pendência existente nos resultados experimentais obtidos por diversos autores consultados. / [en] In order to contribute in the investigation of the stimulation operation of an oil reservoir was built a tubular viscometer to determine the rheological properties of a hydraulic fracturing fluid (HPGUAR). This test rig included a system to prepare the hydraulic fracturing fluid. The experimental results were modelled according to two types of constitutive equations: the Ostwald Model one, widely used in the Petroleum Engineers field, and the Bingham Model one. An evaluation of the experimental results suggests that the Bingham Model should be more adequate than the other one, specifically when it shows the contribuition from the viscous friction and from the plastic viscosity independently, in the determination of the rheological properties of the HPGUAR. More detailed investigations must be carried out, although they should be very usefull in better explaning the differeces obtained among several investigators.

Made available in DSpace on 2016-04-01T17:54:41Z (GMT). No. of bitstreams: 0 Previous issue date: 2008-06-18. Added 1 bitstream(s) on 2016-04-01T18:00:22Z : No. of bitstreams: 1 000563860.pdf: 2622089 bytes, checksum: e07ff1d0d497a33adaec5ce6119b0e03 (MD5) / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES) / Nesta dissertação faz-se a análise da dinâmica não-linear de um sistema que possui preso a ele um motor de corrente contínua com potência limitada, onde são acoplados uma mola não linear e um amortecedor do tipo magneto-reológico (dispositivo que tem como fluído interno o fluído magneto-reológico). Com o objetivo de estudar e analisar a influência deste dispositivo na dinâmica do oscilador. Inicialmente apresenta-se uma breve descrição do tipo de problema estudado (sistemas não ideais) e uma revisão dos principais trabalhos que têm sido feitos tendo este dispositivo como foco de estudos. Apresentam-se os modelos utilizados para prever o comportamento destes dispositivos e também uma síntese de alguns modelos (mecânicos e matemáticos) mais elaborados e completos utilizados também para prever este comportamento. A partir daí é feita a apresentação do modelo que prevê o comportamento do amortecedor MR utilizado (modelo Bingham) e de uma suavização do mesmo, utilizada com o objetivo de melhorar o comportamento computacional do modelo inicial, junto a isso, apresenta-se a modelagem matemática do problema visando à obtenção das equações governantes do sistema. Faz-se então a análise do sistema durante a passagem pela ressonância (onde a freqüência de rotação do motor CC se aproxima numericamente e passa pela freqüência natural do sistema), analisando o efeito deste amortecedor durante esta passagem, analisa-se também a influência do dispositivo na evolução do Efeito Sommerfeld, um dos fenômenos intrínsecos desta classe de sistemas e também é feita uma analise do sistema em condições de movimento caótico também com o objetivo de prever o comportamento deste dispositivo, tudo isso é executado através da integração numérica das equações governantes do sistema. Para efeito de ilustração apresenta-se, também, uma pequena amostra do comportamento do sistema ideal paralelo ao estudado ... / In this dissertation it made the analysis of the nonlinear dynamics of a system that possess to fixed it a direct-current motor with limited power, where is connected a damper of the type Magnetorheological (device that has as fluid intern the fluid Magnetorheological), with the objective to study and to analyze the influence of this device in the dynamics of the oscillator. Initially one brief description of the type of studied problem is presented (nonideal systems) and a revision of the main works that have been made having this device as focus of studies. The used models are presented to predict the behavior of these devices and also a synthesis of some models (mechanics and mathematicians) more elaborated and complete also used to predict this behavior. To continue this work, we present the model that predict the behavior of used MR damper (the Bingham Model) and a smoothing of the same, used with the objective to improve the computational behavior of the initial model and the mathematical modeling of the problem, together this, we show mathematical modeling of this problem aiming at to the attainment of the governing equations of the system. The analysis of the system it is made then during the passage for the resonance (where the frequency of DC motor it approaches numerically and crosses the natural frequency of the system), analyzing the effect of this damper during this passage, the influence of the device in the evolution of Sommerfeld Effect is also analyzed, one of the intrinsic phenomena of this classroom of systems and also is made a analyzes of the system in conditions of chaotic motions also with the objective to predict the behavior of this device, everything this is executed through the numerical integration of the governing equations of the system. For illustration effect it is presented, also, a small sample of the behavior of the parallel ideal system to the studied one, also with the presence of shock absorber MR, in the..

<p>Soils, in general, undergo both elastic and plastic deformations upon loading. Strain dependant anisotropic elasto-plastic models are required for realistic modeling for soil-tool mechanics that will address issues like stress history and soil anisotropy. Although several such models have been proposed, the science of coupled poro-mechanical analysis of an unsaturated soil has not been fully addressed.</p><p>Tillage tool modeling is primarily concerned with the analysis of soil deformation patterns and development of force prediction models for design optimization. Most of the models are based on quasi-static soil failure patterns that cause difficulty in accurately predicting soil-tool behaviour and soil forces for high speed operation. In recent years efforts have been made to improve the conventional analytical and experimental models by numerical approaches. Numerical simulations of soil-tool interactions using finite element modeling (FEM) and discrete element method (DEM) were mostly based on a solid mechanics approach. Due to limitations of constitutive relations, predictions of these numerical models have not been able to address tillage dynamics with high shear rates. The contribution of this research was to study the dynamics of soil-tool interaction using computational fluid dynamics (CFD) from the perspective of soil visco-plastic behavior.</p><p>A motorised soil rheometer was developed for evaluating soil visco-plastic parameters for CFD simulations. The apparatus was used to determine soil yield stress and viscosity at different soil moisture and compaction levels.</p><p>Three-dimensional CFD analyses were carried out using a commercial software CFX 4.4 to observe soil failure patterns around a tool and the pressure distribution on and around the tool. Duct flow as well as free-surface flow simulations of visco-plastic soil as a non-Newtonian Bingham material indicated soil deformation comprising of plastic flow and plug flow patterns. The soil failure front advancement demonstrated a critical speed range of 4 to 6.5 m s-1 where advancement of the failure front did not increase with speed. Soil pressure on the tool surface increased with the tool operating speed. Pressure distribution on the tool surface and draft requirement agreed well with the published literature based on experimental results and FEM analysis. The CFD approach, in its first attempt to tillage process, demonstrated its greater potential for dynamic modeling of soil-tool interaction.</p>

<p>Soils, in general, undergo both elastic and plastic deformations upon loading. Strain dependant anisotropic elasto-plastic models are required for realistic modeling for soil-tool mechanics that will address issues like stress history and soil anisotropy. Although several such models have been proposed, the science of coupled poro-mechanical analysis of an unsaturated soil has not been fully addressed.</p><p>Tillage tool modeling is primarily concerned with the analysis of soil deformation patterns and development of force prediction models for design optimization. Most of the models are based on quasi-static soil failure patterns that cause difficulty in accurately predicting soil-tool behaviour and soil forces for high speed operation. In recent years efforts have been made to improve the conventional analytical and experimental models by numerical approaches. Numerical simulations of soil-tool interactions using finite element modeling (FEM) and discrete element method (DEM) were mostly based on a solid mechanics approach. Due to limitations of constitutive relations, predictions of these numerical models have not been able to address tillage dynamics with high shear rates. The contribution of this research was to study the dynamics of soil-tool interaction using computational fluid dynamics (CFD) from the perspective of soil visco-plastic behavior.</p><p>A motorised soil rheometer was developed for evaluating soil visco-plastic parameters for CFD simulations. The apparatus was used to determine soil yield stress and viscosity at different soil moisture and compaction levels.</p><p>Three-dimensional CFD analyses were carried out using a commercial software CFX 4.4 to observe soil failure patterns around a tool and the pressure distribution on and around the tool. Duct flow as well as free-surface flow simulations of visco-plastic soil as a non-Newtonian Bingham material indicated soil deformation comprising of plastic flow and plug flow patterns. The soil failure front advancement demonstrated a critical speed range of 4 to 6.5 m s-1 where advancement of the failure front did not increase with speed. Soil pressure on the tool surface increased with the tool operating speed. Pressure distribution on the tool surface and draft requirement agreed well with the published literature based on experimental results and FEM analysis. The CFD approach, in its first attempt to tillage process, demonstrated its greater potential for dynamic modeling of soil-tool interaction.</p>

This work deals with the research of degradation of magnetorheological (MR) fluid during long-term loading under conditions that correspond to the real load in the linear MR devices such as dampers. The behaviour of MR fluid is described by a Bingham model of viscoplastic fluid. The parameters of this model are the yield stress and viscosity. Their values are determined by the shear rate from 1 to 2,8104 s-1. Results of durability tests show a significant decrease in viscosity of MR fluid, a gradual increase in yield stress in the off-state and a significant decrease in MR effect. The paper also described the effect of temperature on these parameters and there is also designed a method of non-assembly diagnostic of the MR fluid state in the damper using the "rate of pulsation."

The rheological properties of cement-based grouts play a key role in determining the final spread in grouted rock formations. Rheologically, cement grouts are known to be complex thixotropic fluids, but their steady flow behavior is often described by fitting the simple Bingham constitutive law to flow curve data. The resultant Bingham parameters are then used in grouting design of e.g. tunnels, to estimate the penetration length. Since cement grouts are thixotropic suspensions, the interpretation of their flow curves as obtained from flow sweeps in concentric cylinder rotational rheometers is often complicated by: the presence of wall slip, sedimentation and unstable flow at low shear rates. A systematic approach to study these effects within the constraints of the concentric cylinder geometry (Couette) and for different cement grout concentrations was carried out as part of the Licentiate research work. Of particular interest was the influence of geometry and flow sweep measurement interval on flow curves, including the characteristic unstable flow branch that appears at applied shear rates that are below the critical shear rate. The unstable flow branch observed below the critical shear rate has been described as a characteristic feature in the flow curves of thixotropic suspensions, e.g. cement grouts, laponite. From a practical standpoint, this information can then be readily used to improve rheological measurements of cement grouts. The existence of the critical shear rate below which no stable flow occurs, plus the complex wall slip phenomenon are then discussed by considering how they affect actual spread in rough and smooth rock fractures. Another major part of the research presented in this thesis relates to the measurement of model yield stress fluid (YSF), i.e. Carbopol, velocity profiles within the radial flow geometry. Radial flow between parallel plates, is an idealized fundamental flow configuration that is often used as a basis for grout spread estimation in planar rock fractures. Compared to other flow configurations with YSFs, e.g. channels, only a limited amount of work has presented analytical solutions, numerical models and especially experimental work for radial flow. Thus, as a first step towards more systematic studies of the plug flow region of YSFs in radial flow the current work presents the design, manufacture and for the first time velocity profile measurements that were conducted by using the pulsed Ultrasound Velocity Profiling (UVP) technique. The current observations for tests carried out with different disk spacings and flow rates show a distinct plug region, coupled with wall slip effects for the Carbopol model YSF fluid that was used. The theoretically predicted velocity profiles and the measured ones agree reasonably well, and the main discrepancies are discussed. Future studies, would then be targeted at improving the current experimental setup, for detailed measurements of the plug flow region along the radial length, which remains a challenging issue for studies on YSFs and engineering applications such as rock grouting design. / Cementbaserade injekteringsmedels reologiska egenskaper har en stor påverkan på strömning och inträngningslängd i sprickigt berg. Medlens reologi är komplex, inklusive tixotropi, men strömningen beskrivs ändå oftast med den enkla linjära Bingham modellen i injekteringssammanhang. De två parametrarna från denna modell, flytgräns och viskositet, används sedan inom injekteringsdesign, för t.ex. tunnlar och dammar, för att bedöma inträngningen. Eftersom cementbaserade medel är tixoptropa suspensioner försvåras utvärderingen vid mätning med konventionella rotationsviskometrar på grund av glidning vid fasta begränsningsytor, sedimentation/separation av partiklarna och instabila flöden vid låga deformationshastigheter. En systematisk mätprocedur för att studera ovanstående problem med rotationsviskometer och koncentriska cylindrar samt olika vanliga vattencementtal, har utförts inom ramen för detta licentiatarbete. Av särskilt intresse har varit att studera effekten av olika geometrier och tidsintervallet mellan mätningarna, inklusive den instabila delen av flödeskurvan då deformationshastigheten är lägre än ett kritiskt värde. Denna del av kurvan har i litteraturen beskrivits som karakteristisk för tixotropa suspensioner, som t.ex. cementbaserade injekteringsmedel. Praktiskt kan ovanstående kunskap användas för att förbättra mätningen av de reologiska egenskaperna. Existensen av en kritisk deformationshastighet under vilken det inte finns något stabilt flöde, i kombination med glidning vid fasta begränsningsytor, diskuteras särskilt med hänsyn till dess påverkan på faktisk inträngning i släta och råa bergsprickor. Ett annat fokus i licentiatarbetet har varit att studera icke-Newtonska modellvätskors (Carbopol) radiella strömning mellan parallella plattor. Denna typ av strömningsgeometri används ofta som en idealiserad konfiguration för strömning i bergsprickor. I jämförelse med andra enklare geometrier, finns endast en begränsad forskning utförd för denna geometri både då det gäller analytiska och numeriska beräkningar men framförallt då det gäller experiment. Som ett första steg inför en mer systematisk undersökning av icke-Newtonsk radiella strömning presenteras i detta arbete framtagandet av en fysisk laboratoriemodell där hastighetsprofilerna mellan plattorna för första gången visualiserats med hjälp av ultraljud. De utförda mätningarna med tre olika öppningar mellan plattorna sam tre olika värden på det konstanta flödet, visar på en distinkt plugg som är ett resultat av vätskans flytgräns samt glidning i gränsskiktet mellan vätskan och plattornas fasta begränsningsytor. En jämförelse mellan uppmätta hastighetsprofiler och analytiskt beräknade diskuteras där resultaten överensstämmer relativt väl, med beaktande av de långtgående förenklade antaganden som krävs för beräkningarna. Fortsatta studier kommer att fokuseras på att förbättra laboratoriemodellen för en mer detaljerad studie av icke-Newtonska vätskors strömning och hur pluggen utvecklas under den radiella inträngningen, vilket fortsättningsvis är av betydelse för design av injektering i bergsprickor. / <p>QC 20190521</p>

Ce travail porte sur l’étude expérimentale et numérique de l’écoulement des mousses humides dans un canal horizontal droit de section carrée avec ou sans singularités. Il est consacré tout particulièrement à déterminer les paramètres pertinents de l’écoulement dont la chute de pression longitudinale, les champs de vitesse de l’écoulement de mousse en proche parois, les épaisseurs de films liquides minces et épais en paroi et l’évolution de la contrainte pariétale pour une mousse humide dont la fraction gazeuse varie de 55 à 85% et la vitesse débitante de la mousse est 2, 4 puis 6 cm/s. Une fois ces paramètres déterminés en conduite horizontale droite, nous avons ensuite effectué des mesures sur différentes géométries représentant un élargissement brusque, une chicane verticale et écoulement de mousse autour d’un cylindre, dont le but est d’étudier la réorganisation de l’écoulement en vue de déterminer le comportement rhéologique des mousses en écoulement à l’aval et à l’amont des singularités. Finalement, une étude de simulation numérique (CFD) en utilisant les lois de comportement de type Bingham, pour fluides non newtoniens, a été effectuée afin de tester sa capacité de représenter des écoulements type mousse humide dans une conduite horizontale avec ou sans singularités. Nous avons vérifié tout d’abord l’évolution longitudinale de la pression statique qui est linéaire à l’amont comme à l’aval loin des zones influencées par les singularités. La chute de pression singulière reste à peu près constante pour une vitesse débitante donnée de la mousse. À partir de la technique de Vélocimétrie par Image de Particule (PIV), nous avons déterminé les composantes de vitesse au voisinage immédiat des singularités. Ces mesures nous ont permis de mettre en évidence l’existence de différents régimes d’écoulement, et de déterminer la réorganisation et le comportement rhéologique de l’écoulement de mousse autour des géométries étudiées. L’analyse des mesures d’épaisseur de films liquides, obtenues par la méthode conductimétrique, indique que la paroi reste mouillée par un film liquide suffisamment épais pour qu’on puisse appliquer la méthode électrochimique. Les signaux polarographiques obtenus avec la mousse présentent alors de fortes fluctuations. La comparaison de celles-ci avec les contraintes pariétales déduites à partir des mesures de la chute de pression montre bien une bonne concordance. L’étude numérique (CFD), effectuée pour une fraction volumique de gaz égale à 70% et qui s’écoule avec une vitesse débitante de 2 cm/s, montre que le modèle rhéologique de Bingham pourrait être bien adapté à ce genre de mousse humide évoluant en écoulement en bloc. / This work is an experimental and numerical study of aqueous foam flow inside a horizontal square duct, with and without flow disruption devices (fdd). It is especially devoted to determine the pertinent parameters of the flow: longitudinal pressure losses, velocity fields of foam flow near the walls, liquid film thickness (thick and thin), and the wall shear stress evolution, for an aqueous foam with a void fraction range between 55 and 85%, for a mean foam flow velocity of 2, 4 and 6 cm/s. Once they were determined, inside the horizontal channel, we carried out measurements over different geometries: half-sudden expansion, vertical fence and foam flow around a cylinder. The goal was to study the foam flow reorganization to well understand the rheological behavior of aqueous foam flow in the vicinities of different fdd. Finally, a numerical simulation (CFD), using the Bingham behavior model of non-Newtonian fluid, was undertaken to test its capacity to represent the aqueous foam flow inside the horizontal duct with flow disruption devices. First of all, we verified the static longitudinal pressure evolution, which varies linearly upstream and downstream far from the fdd. The singular pressure loss remains constant for a given mean foam velocity and a foam quality (void fraction). From the Particle Imaging Velocimetry (PIV) technique (2D), we determined the two velocity components in the immediate vicinities of the disruption devices. They allowed us to put into evidence the different foam flow regimes and to observe the foam flow reorganization and rheological behavior through the studied fdd. The slip-layer thickness analysis, obtained using the conductimetry method, shows that the wall presents a liquid film thick enough to apply an electrochemical technique (polarography). Thus, the polarographic signals, obtained for the foam flow, present important fluctuations. They were compared to the wall shear stress deducted from the measurement of pressure losses, showing a good similarity between them. The numerical study (CFD), carried out for aqueous foam flow with a void fraction of 70% and a mean foam flow velocity of 2 cm/s, shows that the Bingham rheological model can be adapted to this kind of aqueous foam flow which is flowing like a block.