Master´s thesis Hydrodynamic mixing of water-ash mixture in vessel is interested in describing fluid and solid particles flow in a vessel. The mixing was conducted in cylindrical vessel by a radial nozzle. The goal of the thesis is to describe flow field and places where the most of the particles are descending according to position, depth, flow rate and nozzle orientation in the vessel. An experiment was conducted in order to investigate and document 8 different positions and orientation of the nozzle. Significant changes in flow fields and mixing time were observed. A mathematical model of the vessel with the nozzle was created in Fluent program. Places with the lowest velocities according to the model were in good agreement with places where the most of the solid particles were descending.

The main goal of doctoral thesis is optimization cooling of the synchronous machine. Problem is solved based on the finite element method with use of ANSYS software. Work is built up from theoretical part where is comparison of base equations for heat transfer and simulations for several models. Next part shows us two methods how simulate free and force convection. Depends on the better method from the previous two methods is used for next calculations with several algorithm which are used for find of best parameters for synchronous machine. Our control parameter is mass flow rate.

Turbulent and cavitation induced pipe vibration is a large problem in industry often resulting in pipe failures. This thesis provides an experimental investigation on turbulent flow and cavitation induced pipe vibration caused by sharp edged baffle plates. Due to large pressure losses across a baffle plate, cavitation can result. Cavitation can be destructive to pipe flow in the form of induced pipe wall vibration and cavitation inception. Incipient and critical cavitation numbers are design points that are often used in designing baffle plate type geometries. This investigation presents how these design limits vary with the influencing parameters by exploring a range of different baffle plate geometries. The baffle plates explored contained varying hole sizes that ranged from 0.159 cm to 2.54 cm, with the total through area, or openness, of each baffle plate ranging between 11% and 60%. Plate thickness varied from 0.32–0.635 cm. Reynolds numbers ranged from 5 x 10^4 -85 x 104. The results show that the cavitation design limits are function of size scale effects and the loss coefficient only. The results also show that the loss coefficient for a baffle plate varies not only with total through area ratio, but also due with the plate thickness to baffle hole diameter ratio. Pipe wall vibrations were shown to decrease with increased through area ratio and increased thickness to diameter ratios. An investigation was also performed to characterize the attenuation of vibration in the streamwise direction of a baffle plate. It was show that the attenuation was largely effected by the presence of cavitation. Attenuation was shown to be a function of the geometry of the baffle plate. This work resulted in empirical models that can be used for predicting pipe vibration levels, the point of cavitation inception, and the streamwise distance where the attenuation of vibration levels caused by a baffle plate occurs.

This thesis focuses on identifying acoustic noise generating components in piezoelectric blowers through transverse velocity measurements and the development of a numerical fluid model. Piezoelectric ceramics have proven useful for many industries and areas of research involving: high precision actuators, noise control, ultrasonic devices, and many other areas. As of late, a unique adaptation of piezoelectric ceramics is surfacing in the area of pumping and cooling. Air pumps that use these ceramics replace the traditional electric motor, resulting in lower power consumption, less moving parts, constant pressure gradients, lower overall weight, and a low profile. The current drawback of this application is the acoustic radiation produced by the blowers. Since these blowers are new to market, little research or development has been done to characterize the noise emissions. This thesis studies the acoustic emissions from the front face of a Murata piezoelectric blower. Jet noise and structural vibrations are two acoustic sources of interest that are studied in this research. A Direct Numerical Simulation (DNS) of the fluid flow through a Murata blower is developed to better identify noise generating mechanisms. The model solutions predict trends in sound pressure levels (SPL) of the jet noise and volumetric flow rates. Both the SPL and flow rate are shown to be functions of critical geometrical dimensions within the flow path of a Murata blower. Important dimensional components are identified as well as non-influential ones. Design guidelines are given to reduce noise emission from the front side of a blower and increase the volumetric flow rate. The results of this research have a direct impact on the piezoelectric blower industry and future blower designs.

No description available.

No description available.

La Tomographie à Emission de Positrons (TEP) permet d'obtenir une mesure dynamique et résolue en espace de la concentration d'un traceur radioactif injecté au patient. La quantification du débit sanguin cérébral par TEP repose sur l'utilisation d'un modèle cinétique le reliant à la variation spatio-temporelle de la concentration du traceur dans le cerveau. Différents modèles cinétiques sont proposés dans la littérature. Cependant, la majorité d'entre eux repose sur une modélisation compartimentale de l'organe observé. Dans ce cas, l'organe est subdivisé en un compartiment capillaire échangeant avec un compartiment tissulaire par une cinétique le plus souvent du premier ordre. Les résultats obtenus avec ce type de modèle sous-estiment le débit et ne permettent pas de prédire les premiers instants de la dynamique de répartition du traceur. Ces faiblesses ont été confirmées suite à l'amélioration de la résolution temporelle des tomographes, conduisant à l'élaboration de modèles incorporant plus de réalité physiologique. Cependant, tous ces modèles sont développés pour modéliser les échanges entre la micro-circulation et le tissu environnant à l'échelle d'un capillaire (échelle microscopique). Or la résolution spatiale des tomographes utilisés en clinique ne permet pas de distinguer la micro-circulation et le tissu. L'utilisation de ces modèles cinétiques avec des mesures de concentrations macroscopiques dépasse donc leur cadre théorique de validité et peut introduire des résultats faussés. Dans ce contexte, nous proposons un modèle cinétique basé sur le changement d'échelle (utilisant la méthode de prise de moyenne volumique). Ce changement d'échelle permet de remplacer l'ensemble micro-circulation/tissu par un volume fictif, homogène, dont les propriétés macroscopiques sont calculées à partir des propriétés microscopiques d'un Volume Elémentaire Représentatif (VER) du milieu. Dans un premier temps, afin de pouvoir comparer les résultats de ce modèle avec ceux du modèle compartimental standard, le VER considéré est constitué d'un capillaire unique et de son enveloppe de tissu, puis une complexité géométrique supplémentaire est introduite en considérant un réseau de capillaire isotrope à l'échelle de Darcy. Ces modèles sont utilisés pour identifier le débit à l'aide d'une méthode inverse. Pour cela, l'évolution temporelle du champ de concentration dans notre géométrie de référence, qui ne peut être mesurée par TEP en raison de sa faible résolution spatiale, est déterminée par des simulations numériques ainsi que par des mesures in vitro à l'aide d'un modèle expérimental, également développé au cours de ce travail, permettant de reproduire l'écoulement dans un canal traversant une matrice diffusante (gel d'alginate). / Positron Emission Tomography (PET) provides a dynamic and space-resolved measurement of the concentration field of a radioactive tracer previously injected to the patient. Quantification of cerebral blood flow by PET is based on the use of a kinetic model linking cerebral blood flow to the spatial and temporal variations of tracer concentration in the brain. Various kinetic models have been proposed in the literature. However, most of the mare based on a compartmental approach of the observed organ In this case, the organ is divided in two compartments, the capillary and the tissue, and the exchanges between these two compartments are often described by a first order kinetic model. Results obtained with this kind of model under estimate the flow rate and are notable to predict the first instants of the tracer dynamics distribution. With the continuous improvement of the temporal resolution of PET, these weaknesses have been confirmed, which led to the development of models incorporating more physiological reality. However, all these models have been developed to describe exchanges between micro-circulation and surrounding tissue at the scale of capillary vessels (microscopic scale). Because the spatial resolution of PET inclinical practice is insufficient to allow the distinction between micro-circulation and tissue, using of these models with kinetic measurement of macroscopic concentrations exceeds their theoretical validity and can introduce false results. In this context, we propose a kinetic model based on up-scaling (using the method of volume averaging). This up-scaling technique allows to replace the two previous compartments (tissue and micro-circulation) by an homogeneous fictive volume, whose macroscopic properties are calculated from the microscopic properties of are presentative elementary volume (REV) of the medium. First, in order to compare the results of this model with those of the standard compartmental model, the considered REV consists of a single capillary and its surrounding tissue. Second, additional geometric complexity is introduced by considering an isotropic capillary network at the Darcy scale. These models are used to identify the flow rate using an inverse method. For that purpose, the temporal evolution of concentration field in a geometry of reference, which can't be measured by PET due to its low spatial resolution, is determined by numerical simulations and by in vitro measurements. These measurements are performed using an experimental model developed during this work to reproduce the flow in a channel passing through a diffusive matrix (alginate gel).

O objetivo deste estudo foi mensurar o fluxo salivar, pH, capacidade tampão, concentrações de proteína total e ácido siálico, atividades das enzimas amilase e peroxidase e concentração dos íons sódio, potássio, cálcio, fósforo, zinco e magnésio em saliva total de indivíduos síndrome de Down com idade entre 1 e 25 anos. Nos indivíduos com idade entre 1 e 5 anos a saliva total foi coletada através de uma leve sucção, enquanto que nos outros indivíduos com idade entre 6 e 10, 11 e 15, 15 e 20, 21 e 25 a saliva total foi coletada com estimulação mecânica através da mastigação de parafilm, durante 10 minutos. O pH e a capacidade tampão foramdeterminadas usando um pHmetro digital. A capacidade tampão foi mensurada através de titulação com HCl a 0,01N. A concentração de eletrólitos foi determinada através de um espectrofotômetro de emissão atômica com fonte de excitação de argônio induzido. A proteína total foi mensurada através do reagente de Folin. A atividade da amilase foi mensurada através da produção de maltose e a atividade da peroxidase foi mensurada através da utilização de orto-dianisidina. Para a analise estatística os dados foram apresentados em media ± desvio padrão. Foi utilizado o teste “t" de Student para determinar as diferenças entre as medias dos indivíduos síndrome de Down e o grupo controle. Nenhuma diferença significante foi observada na concentração de ácido siálico, fósforo, zinco, magnésio e cálcio entre os indivíduos síndrome de Down e o grupo controle. A concentração de sódio, proteína total e a capacidade tampão demonstraram ser maior nos indivíduos com síndrome de Down em comparação ao grupo controle. Por outro lado, o fluxo salivar, a concentração de potássio, e a atividade das enzimas amilase e peroxidase foram menores no grupo síndrome de Down quando comparado ao grupo controle. Estes resultados sugerem que as pessoas com síndrome de Down apresentam alterações no metabolismo do ducto e/ou das células acinares das glândulas salivares. / The aim of this study was to measure the flow rate, pH, buffer capacity, sialic acid, total protein concentrations, amylase and peroxidase activities and sodium, potassium, calcium, phosphorus, zinc and magnesium concentration whole saliva of individuals with Down syndrome aged 1 - 25 years. In individuals aged 1-5 years the whole saliva was collected under slight suction, while in the others individuals aged 6-10, 11-15, 15-20, 21-25 the whole saliva was collected with stimulation by chewing a piece of parafilm, for 10 minutes. The pH and the buffer capacity were determined using a digital pHmeter. The buffer capacity was measured by titration with 0.01 N HCl. Electrolyte concentrations were determined by inductively coupled argon plasma with atomic emission spectrometry. Sialic acid was determined by thiobarbituric acid assay. Protein was determined by the folin’s phenol reagent. Amylase was assayed measuring the maltose produced by the breakdown of starch and peroxidase with ortho dianisidine. For statistical analysis the date are presented as mean ± SD. Student’s “t" test was used to determine differences between the mean of the Down syndrome and control groups. No statistically significant differences were observed in sialic acid, phosphorus, zinc, magnesium and calcium concentration between the individuals with Down syndrome and control group. The sodium and total protein concentration and buffer capacity showed higher in the Down syndrome than in the control group. On the other hand the flow rate and potassium concentration, amylase and peroxidase activities were lower in the Down syndrome than in the control group. These results suggest that the Down syndrome persons present alteration in the metabolism of the duct and/or acinar cells of salivary glands.

The focus of this work is to investigate the dissolution of MW25, a non-radioactive simulant of UK high-level nuclear waste borosilicate glass, and to predict its performance in the near field of a geological repository. A single-pass flow-through (SPFT) experimental system was used to measure the forward dissolution rates of MW25. Experiments were conducted in two parts. Experiment Part 1 considers the dissolution of the waste glass in deionised water at 40 and 90 oC and circum-neutral pH. Experiment Part 2 considers the dissolution of the waste glass in simulant groundwaters, with similar compositions to groundwaters of Callovo-Oxfordian clay (lower-strength sedimentary rock (LSSR)) and Borrowdale Volcanic Group rocks (higher-strength rock (HSR)), at 40 oC and pH 7. The forward dissolution rate measured in deionised water was found to be approximately one order of magnitude higher at 90 oC than at 40 oC. A similar release was observed for Si, Mg and Al at 40 oC and 90 oC, whereas the B, Cs, Na, Li and Mo showed an order of magnitude increase when the temperature was increased from 40 to 90 oC for low q/S values. The activation energy (Ea) of the reactions shows that the dissolution process is a surface phenomenon. At 90 oC the net effect of the processes governing MW25 dissolution led to the preferential release of boron and alkali metals relative to the release of Si during the transient dissolution stage, accompanied by an increase in the concentration of silicic acid. This suggests that the solution activity of silicic acid at a higher temperature has a weak influence on the release of the mobile elements. The forward dissolution rate measured in LSSR simulant groundwater was found to be slightly higher than that measured in HSR simulant groundwater. The dissolution behaviour of MW25 in both groundwaters is consistent with its behaviour in deionised water at 40 oC, with the dissolution rates of elements increasing as flow rates were increased. However, forward dissolution rates measured in the simulant groundwaters were lower than the forward dissolution rates measured in deionised water under these experimental conditions. This is attributable to the interaction of the components of the simulant groundwaters with the glass, as revealed by post-reaction surface analyses, and a consequential lower alkalinity of the leachates collected in the experiments with simulant groundwater than in deionised water. Reactive chemical transport simulations of waste glass dissolution and radionuclide release in a hypothetical near field were conducted over a time span of a million years with GoldSim. The results showed that enclosing the waste glass in a steel canister covered by a copper canister and emplacing the waste package in a granite host rock is optimal for the long-term isolation of the radionuclides. The waste glass was found to play a significant role in the overall performance of the near field. This study features a new method for estimating the surface area of reacted glass powder more accurately than the geometric surface area estimate, which is the preferred standard method among researchers.

A study was conducted to evaluate the properties and processes influencing the rate and magnitude of volume decrease and strength gain for oil sand fine tailings resulting from a change in bitumen extraction process (caustic versus non-caustic) and the effect of adding a coagulant to caustic fine tailings. Laboratory flume deposition tests were carried out with the objective to hydraulically deposit oil sand tailings and compare the effects of extraction processes on the nature of beach deposits in terms of geometry, particle size distribution, and density. A good correlation exists between flume deposition tests results using oil sand tailings and the various other tailings materials. These comparisons show the reliability and effectiveness of flume deposition tests in terms of establishing general relationships and can serve as a guide to predict beach slopes. Fine tailings were collected from the various flume tests and a comprehensive description of physical and chemical characteristics of the different fine tailings was carried out. The characteristics of the fine tailings is presented in terms of index properties, mineralogy, specific surface area, water chemistry, liquid limits, particle size distribution and structure. The influence of these fundamental properties on the compressibility, hydraulic conductivity and shear strength properties of the fine tailings was assessed. Fourteen two meter and one meter high standpipe tests were instrumented to monitor the rate and magnitude of self-weight consolidation of the different fine tailings materials. Consolidation tests using slurry consolidometers were carried out to determine consolidation properties, namely compressibility and hydraulic conductivity, as well as the effect of adding a coagulant (calcium sulphate [CaSO4]) to caustic fine tailings. The thixotropic strength of the fine tailings was examined by measuring shear strength over time using a vane shear apparatus. A difference in water chemistry during bitumen extraction was concluded to be the cause of substantial differences in particle size distributions and degree of dispersion of the comparable caustic and non-caustic fine tailings. The degree of dispersion was consistent with predictions for dispersed clays established by the sodium adsorption ratio (SAR) values for these materials. The biggest advantage of non-caustic fine tailings and treating caustic fine tailings with coagulant is an increased initial settlement rate and slightly increased hydraulic conductivity at higher void ratios. Thereafter, compressibility and hydraulic conductivity are governed by effective stress. The chemical characteristics of fine tailings (water chemistry, degree of dispersion) do not have a significant impact on their compressibility behaviour and have only a small influence at high void ratio (low effective stress). Fine tailings from a caustic based extraction process had relatively higher shear strengths than comparable non-caustic fine tailings at equivalent void ratios. However, shear strength differences were small and the overall impact on consolidation behaviour, which also depends on compressibility and hydraulic conductivity, is not expected to be significant.