Arctic Ocean monitoring with near-real-time data transfer is urgently needed. The harsh and remote conditions constraining year-round observation sites present significant logistical challenges and energy needs for sustained Arctic observations. The Arctic project group is attempting to design a mechanical structure to harvest energy from low-speed current in the Arctic Ocean. An Arctic energy harvesting system that consists of a transverse flux generator, boosted by a nozzle-diffuser-duct, and an American multiblade turbine that drives the generator, are designed in this study. The transverse flux generator is then optimized based on its design parameters and the optimization successfully improves the torque performance of the generator while maintaining the largest power output. The American turbine fits the extreme low-speed current condition (<0.2m/s) well and could support the rotation of the generator. Finally, the article compares the energy harvesting system is compared with the existing ones in the market and demonstrates its superior performance. / Master of Science / Arctic area has great potential and it is beneficial to monitor and do research in the Arctic area. The continuous energy could be a problem. The challenging and isolated conditions that limit the establishment of year-round observation stations pose significant logistical hurdles and energy requirements for continuous Arctic data collection. To address this, the Arctic project team is endeavoring to create a mechanical structure capable of harnessing energy from low-speed currents in the Arctic Ocean.

Wind tunnels are important tools used in physics and engineering, with a wide range of usability and applications in industrial, research, and educational settings. A wind tunnel holds an object steady while generating airflow over it, often to study the interaction between the object and the airflow. The design of wind tunnels can be very costly, extensive, and difficult to implement. This paper analyzes literature on wind tunnels to compile a method for designing a portable wind tunnel suitable for educational and demonstrative purposes. The method includes design guidelines for each component, including the test section, contraction, settling chamber, honeycomb, diffuser, and fan section. A blueprint for a wind tunnel with specified dimensions is presented. The blueprint is designed to fit a Boeing 747-200 model, scaled at 1:390, and therefore have a 40 cm long test section with a 20x20 cm square cross-section. The designed wind tunnel achieves a velocity of 5 m/s in the test section. Emphasizing portability, simplicity, and functionality, this wind tunnel design enhances educational experiences, making complex fluid dynamics concepts accessible and engaging for students.

Achieving energy neutrality has shifted focus towards aeration systems optimization, due to the high energy consumption of aeration processes in modern advanced wastewater treatment plants. The activated sludge wastewater treatment process is dependent on aeration efficiency which supplies the oxygen needed in the treatment process. The process is a complex heterogeneous mixture of microorganisms, bacteria, particles, colloids, natural organic matter, polymers and cations with varying densities, shapes and sizes. These activated sludge parameters have different impacts on aeration efficiency defined by the OTE, % and alpha. Oxygen transfer efficiency (OTE) is the mass of oxygen transferred into the liquid from the mass of air or oxygen supplied, and is expressed as a percentage (%). OTE is the actual operating efficiency of an aeration system. The alpha Factor (α) is the ratio of standard oxygen transfer efficiency at process conditions (αSOTE) to standard oxygen transfer efficiency of clean water (SOTE). It is also referred to as the ratio of process water volumetric mass transfer coefficient to clean water volumetric mass transfer coefficient. The alpha factor accounts for wastewater contaminants (i.e. soap and detergent) which have an adverse effect on oxygen transfer efficiency. Understanding their different impacts and how different treatment technologies affect aeration efficiency will help to optimize and improve aeration efficiency so as to reduce plant operating costs. A pilot scale study of fine pore diffuser fouling and mitigation, quantified by dynamic wet pressure (DWP), oxygen transfer efficiency and alpha measurement were performed at Blue Plains, Washington DC. In the study a mechanical cleaning method, reverse flexing (RF), was used to treat two diffusers (RF1, RF2) to mitigate fouling, while two diffusers were kept as a control with no reverse flexing. A 45 % increase in DWP of the control diffuser after 17 month of operation was observed, an indication of fouling. RF treated diffusers (RF1 and RF2) did not show any significant increase in DWP, and in comparison to the control diffuser prevented a 35 % increase in DWP. Hence, the RF fouling mitigation technique potentially saved blower energy consumption by reducing the pressure burden on the air blower and the blower energy requirement. However, no significant impact of the RF fouling mitigation treatment technique in preventing a decrease in alpha-fouling (𝝰F) of the fine pore diffusers over time of operation was observed. This was because either the RF treatment method maintained wide pore openings after cleaning over time, or a dominant effect of other wastewater characteristics such as the surfactant concentration or particulate COD could have interfered with OTE. Further studies on the impact of wastewater characteristics (i.e., surfactants and particulate COD) and operating conditions on OTE and alpha were carried out in another series of pilot and batch scale tests. In this study, the influence of different wastewater matrices (treatment phases) on oxygen transfer efficiency (OTE) and alpha using full-scale studies at the Blue Plains Treatment Plant was investigated. A strong relationship between the wastewater matrices with oxygen transfer characteristics was established, and as expected increased alphas were observed for the cleanest wastewater matrices (i.e., with highest effluent quality). There was a 46 % increase in alpha as the total COD and surfactant concentrations decreased from 303 to 24 mgCOD/L and 12 to 0.3 mg/L measured as sodium dodecyl sulphate (SDS) in the nitrification/denitrification effluent with respect to the raw influent. The alpha improvement with respect to the decrease in COD and surfactant concentration suggested the impact of one or more of the wastewater characteristics on OTE and alpha. Batch testing conducted to characterize the mechanistic impact of the wastewater contaminants present in the different wastewater matrices found that the major contaminants influencing OTE and alpha were surfactants and particulate/colloidal material. The volumetric mass transfer coefficient (kLa) measurements from the test also identified surfactant and colloidal COD as the major wastewater contaminants present in the influent and chemically enhanced primary treatment (CEPT) effluent wastewaters impacting OTE and alpha. Soluble COD was observed to potentially improve OTE and alpha due to its contribution in enhancing the oxygen uptake rate (OUR). Although the indirect positive impact of OUR on alpha observed in this study contradicts some other studies, it shows the need for further investigation of OUR impacts on oxygen transfer. Importantly, the mechanistic characterization and quantitative correlation between wastewater contaminants and aeration efficiency found in this study will help to minimize overdesign with respect to aeration system specification, energy wastage, and hence the cost of operation. This study therefore shows new tools as well as the identification of critical factors impacting OTE and alpha in addition to diffuser fouling. Gas transfer depression caused by surfactants when they accumulate at the gas-liquid interface during the activated sludge wastewater treatment process reduces oxygen mass transfer rates, OTE and alpha which increases energy cost. In order to address the adverse effect of surfactants on OTE and alpha, another study was designed to evaluate 4 different wastewater secondary treatment strategies/technologies that enhances surfactant removal through enhanced biosorption and biodegradation, and to also determine their effect on oxygen transfer and alpha. A series of pilot and batch scale tests were conducted to compare and correlate surfactant removal efficiency and alpha for a) conventional high-rate activated sludge (HRAS), b) optimized HRAS with contactor-stabilization technology (HRAS-CS), c) optimized HRAS bioaugmented (Bioaug) with nitrification sludge (Nit S) and d) optimized bioaugmented HRAS with an anaerobic selector phase technology (An-S) reactor system configuration. The treatment technologies showed surfactant percentage removals of 37, 45, 61 and 87 %, and alphas of 0.37 ±0.01, 0.42 ±0.02, 0.44 ±0.01 and 0.60 ±0.02 for conventional HRAS, HRAS-CS, Bioaug and the An-S reactor system configuration, respectively. The optimized bioaugmented anaerobic selector phase technology showed the highest increased surfactant removal (135 %) through enhanced surfactant biosorption and biodegradation under anaerobic conditions, which also complemented the highest increased alpha (62 %) achieved when compared to the conventional HRAS. This study showed that the optimized bioaugmented anaerobic selector phase reactor system configuration is a promising technology or strategy to minimize the surfactant effects on alpha during the secondary aeration treatment stage / Ph. D. / In the activated sludge process, the energy requirement for aeration which also includes nitrogen removal is a major operating expense for utilities, and it has limited the ability of most water and wastewater reclamation facilities to achieve energy neutrality. Aeration has therefore become one of the most energy and capital intensive aspects of wastewater treatment. There are still knowledge gaps and mechanistic understanding of the impact of wastewater characteristics and treatment processes on aeration efficiency, which past and current studies are yet to provide. Aeration efficiency is defined by oxygen transfer efficiency and alpha (an indicator of wastewater contaminant effect on aeration efficiency). This study provided an insight into important wastewater characteristics, treatment processes and operational parameters contributing to aeration cost. An understanding of the impacts of wastewater characteristics and how different treatment technologies affect aeration efficiency as discussed in this study will help design engineers and operators to optimize and improve aeration efficiency, so as to reduce plant operating costs. The first study objective on fine bubble diffuser fouling dynamics and physical treatment method quantified by dynamic wet pressure (DWP), oxygen transfer efficiency and alpha measurement was carried out in a pilot reactor. DWP quantified the fouling dynamics of fine pore diffusers. A diffuser fouling physical treatment (reverse flexing, RF) method was able to mitigate fouling of the fine pore diffusers by preventing an increase in DWP normally observed in fouled fine pore diffusers. The RF treatment method reduced fouling by 35 % as compared to the control diffuser (without reverse flexing). This will reduce the pressure burden and air blower energy requirement. The second study objective evaluated the impact of different wastewater characteristics and removal in different stages on aeration efficiency. Test results in this study showed that surfactant and particulate COD fractions were the major characteristics constituents contained in wastewater that depressed aeration efficiency defined by OTE and alpha. Soluble COD did not show any inhibiting effect on OTE and alpha. The third study objective evaluated three different optimized wastewater treatment technologies of surfactant removal during aeration treatment process; 1) High rate activated sludge (HRAS) with contactor-stabilization technology (The contactor stabilization process) (HRAS-CS); 2) HRAS bioaugmented (BioAug) with nitrification sludge (Nit S); and 3) Bioaugmented HRAS with an anaerobic selector phase (An-S) configuration. All three technologies increased surfactant removal through enhanced biosorption and biodegradation to various degrees when compared the conventional high rate activated sludge treatment, but the An-S treatment technology achieved the highest surfactant removal and alpha improvement. The study also established the optimum performance process conditions for each optimized treatment technology.

Wind tunnels are important tools used in physics and engineering, with a wide range of usability and applications in industrial, research, and educational settings. A wind tunnel holds an object steady while generating airflow over it, often to study the interaction between the object and the airflow. The design of wind tunnels can be very costly, extensive, and difficult to implement. This paper analyzes literature on wind tunnels to compile a method for designing a portable wind tunnel suitable for educational and demonstrative purposes. The method includes design guidelines for each component, including the test section, contraction, settling chamber, honeycomb, diffuser, and fan section. A blueprint for a wind tunnel with specified dimensions is presented. The blueprint is designed to fit a Boeing 747-200 model, scaled at 1:390, and therefore have a 40 cm long test section with a 20x20 cm square cross-section. The designed wind tunnel achieves a velocity of 5 m/s in the test section. Emphasizing portability, simplicity, and functionality, this wind tunnel design enhances educational experiences, making complex fluid dynamics concepts accessible and engaging for students.

Thesis (MScEng (Mechanical and Mechatronic Engineering))--University of Stellenbosch, 2011. / Please refer to full text to view abstract.

<p>Many flow cases in fluid dynamics face undesirable flow separation due torising static pressure on wall boundaries. This occurs e.g. due to geometry as ina highly curved turbine inlet duct or e.g. on flow control surfaces such as wingtrailing edge flaps within a certain angle of attack range. Here, flow controldevices are often used in order to enhance the flow and delay or even totallyeliminate flow separation. Flow control can e.g. be achieved by using passiveor active vortex generators (VG) that enable momentum mixing in such flows.This thesis focusses on passive VGs, represented by VG vanes that are mountedupright on the surface in wall-bounded flows. They typically have an angle ofincidence to the mean flow and, by that, generate vortex structures that in turnallow for the desired momentum mixing in order to prevent flow separation.A statistical VG model approach, developed by KTH Stockholm and FOI,the Swedish Defence Research Agency, has been evaluated computationally.Such a statistical VG model approach removes the need to build fully resolvedthree-dimensional geometries of VGs in a computational fluid dynamics mesh.Usually, the generation of these fully resolved geometries is rather costly interms of preprocessing and computations. By applying this VG model, thecosts reduce to computations without VG effects included. Nevertheless, theVG model needs to be set up in order to define the modelled VG geometry inan easy and fast preprocessing step. The presented model has shown sensitivityfor parameter variations such as the modelled VG geometry and the VG modellocation in wall-bounded zero pressure gradient and adverse pressure gradientflows on a flat plate, in a diffuser, and on an airfoil with its high-lift systemextracted. It could be proven that the VG model qualitatively describes correcttrends and tendencies for these different applications.</p>

Difusores podem ser empregados para extração de sacarose da cana de açúcar e da beterraba, para a extração de tanino da casca de acácia negra e para extração de óleos vegetais de plantas oleaginosas. Apesar de operarem de forma simples do ponto de vista mecânico e químico, problemas que ocorrem na sua operação comprometem a eficiência de extração. A modelagem, simulação e otimização de difusores de biomassa mostra-se essencial para melhor compreender tais problemas e propor estratégias otimizadas de projeto e operação. Nesse contexto, a tese aqui proposta tem como objetivo principal modelar e simular a operação de um difusor de biomassa de 10 estágios (Biomassa entra pelo estágio 1 e sai do difusor pelo estágio 10. A água de embebição faz o trajeto em contracorrente, i.e. entra pelo estágio 10 e sai pelo estágio 1) para, posteriormente, otimizá-lo mono e multi-objetivamente considerando a possibilidade de conexão entre todos os estágios de extração. No caso da otimização mono-objetivo, no qual uma vazão de embebição de líquido fixa é considerada, o principal objetivo da otimização consiste em maximizar a concentração de soluto no líquido que deixa o difusor a partir de mudanças aleatórias nos coeficientes de conectividade do difusor. Já para a otimização multi-objetivo, a vazão de embebição de líquido que entra no difusor é considerada variável. Sendo assim, a otimização do sistema requer a maximização de dois objetivos simultaneamente (a maximização da concentração de soluto no líquido e minimização da concentração final de soluto na biomassa) a partir de mudanças aleatórias nos coeficientes de conectividade do difusor. Além disso, visto que a minimização de problemas operacionais está relacionada com a monitoração da altura de nível de líquido no leito de fibra, diferentes sinais para detecção de presença de líquido no leito de fibras em um estágio de extração experimental foram testados. Dos resultados de simulação e otimização obtidos, podemos concluir que novas conexões entre os estágios do difusor podem otimizar o processo de extração o que contraria o senso comum segundo o qual as conexões devem ser sequenciais. No caso da otimização mono-objetivo, 82 a 89% do fluido é direcionado para o estágio seguinte ao longo dos estágios de extração (exceto para o estágio 6, no qual esse valor é de 100%). A recirculação do fluido para o mesmo estágio é mais acentuada nos estágios finais (estágios 1 a 4), apresentando o difusor otimizado 14 a 18% de recirculação do fluido para o mesmo estágio nesses estágios enquanto para os demais estágios a recirculação varia entre 0 e 11%. Já para os estágios iniciais (estágios 5, 7, 8 e 9), a recirculação do fluido para o estágio anterior apresenta maior destaque, variando de 6 a 16% enquanto para os demais estágios é de apenas 0 a 2%. O estágio 6, por sua vez, é o único que se conecta exclusivamente com o estágio seguinte. Para a otimização multi-objetivo, resultados similares foram encontrados, sendo que a probabilidade de que 85 a 100% do fluido seja circulada para o estágio seguinte está entre 93 e 99%. Em relação a recirculação para o mesmo estágio, a probabilidade de que de 0 a 15% do fluido seja recirculado varia de 58 a 79% para os estágios 1 a 4, de 49 a 55% para os estágios medianos 5, 6 e 7 e de 60 a 90% para os três últimos estágios (estágios 8, 9 e 10). Para a conexão com o estágio imediatamente anterior, a probabilidade de que de 0 a 15% do fluido seja direcionado para o estágio anterior é maior nos estágios 1, 2, 8 e 9, variando entre 31 e 38%. Para a detecção da presença de líquido no leito de fibras em um estágio de extração, dois tipos de sinais diferentes, condutividade elétrica e radiação infravermelha, foram testados. Os testes foram realizados, em um estágio de extração experimental, primeiramente apenas com água e, em seguida, com bagaço de cana. Os medidores de condutividade mostraram-se estáveis e com repetitividade quando testados com água. Já nos testes realizados com bagaço de cana, o sinal de condutividade mostrou-se insuficiente para a detecção de líquido. Para os medidores de infravermelho testados com água, os mesmos apresentaram alguns sintomas de instabilidade e variabilidade. Quando testados com cana, os medidores de infravermelho também apresentam instabilidade e variâncias distintas que dependem da posição do medidor no difusor e, consequentemente, da compactação do leito de fibra. Infere-se então que um aumento da variância do sinal pode ser um indicativo de um aumento da compactação do leito e, consequentemente, de diminuição da sua permeabilidade. / Diffusers can be used to extract sucrose from sugarcane and sugarbeet, to extract tannin from black acacia bark and to extract oil from oleaginous plants. Although they operate simply from a mechanical and chemical point of view, problems that occur in their operation can compromise the extraction efficiency. The modeling, simulation and optimization of biomass diffusers is essential to better understand such problems and propose optimized strategies for their project and operation. In this context, the main objective of the proposed thesis is to model and simulate the operation of a ten- stage biomass diffuser to later optimize it mono and multi-objectively considering the possibility of connection among all extraction stages. In the case of the mono-objective optimization, in which a fixed liquid imbibition flow rate is considered, the main objective of the optimization is to maximize the concentration of solute in the liquid that leaves the diffuser from random changes in the connectivity coefficients of the diffuser. For the multi-objective optimization, the liquid imbibition flow rate entering the diffuser is considered variable. Therefore, the optimization of the system requires the maximization of two objectives simultaneously (the maximization of the solute concentration in the liquid and minimization of the final solute concentration in the biomass) from random changes in the diffuser connectivity coefficients. In addition, since the minimization of operational problems is related to the monitoring of liquid level height in the fiber bed, different types of signals for level measurement were tested on an experimental extraction stage. From the simulation and optimization results, we can conclude that new connections among the stages of the diffuser can optimize the extraction process which runs counter to common sense that connections must be sequential. In the case of the mono-objective optimization, 82 to 89% of the fluid is directed to the next stage along the extraction stages (except for stage 6, in which this value is 100%). The recirculation of the fluid to the same stage is more pronounced in the final stages (stages 1 to 4), with the optimized diffuser having 14 to 18% of fluid recirculation for the same stage in these stages while for the remaining stages the recirculation varies between 0 and 11%. For the initial stages (stages 5, 7, 8 and 9), fluid recirculation to the previous stage is more prominent, varying from 6 to 16% while for the remaining stages it is only 0 to 2%. Stage 6, in turn, is the only one that connects only to the next stage. For the multi-objective optimization, similar results were found, with the probability of 85 to 100% of the fluid being circulated to the next stage being between 93 and 99%. Regarding recirculation to the same stage, the probability of 0 to 15% of the fluid being recirculated varies from 58 to 79% for stages 1 to 4, from 49 to 55% for the medium stages 5, 6 and 7 and from 60 to 90% for the last three stages (stages 8, 9 and 10). For the connection to the immediately preceding stage, the probability that 0 to 15% of the fluid being directed to the previous stage is greater in stages 1, 2, 8 and 9, ranging from 31 to 38%. For liquid level measurement, two different types of signals, electrical conductivity and infrared radiation were tested. The tests were first carried out only with water and then with sugarcane bagasse. Conductivity meters were stable and repeatable when tested with water. In the tests performed with sugarcane bagasse, the conductivity signal was insufficient for level measurement. For water-tested infrared meters, they have shown some instability symptoms and variability. When tested with cane, the infrared meters exhibit instability and distinct variances that depend on the position of the meter in the diffuser and, consequently, bed compactation. It can be then inferred that an increase in the signal variance can be also an indicative of increased bed compactation and, consequently, decreased bed permeability.

La thèse résume la recherche sur le fonctionnement et l’écoulement autour d’une éolienne caréné à deux rotors. Le placement d’une turbine à l’entrée d’un canal divergent permet d’augmenter le débit massique à travers le rotor. Afin de mieux tirer parti de l’augmentation de la vitesse du vent à l’entrée du diffuseur, il a été décidé d’examiner la possibilité de placer un deuxième rotor, tournant dans le sens opposé, dans cette zone.L'étude menée combinait plusieurs voies de recherche différentes, y compris les méthodes de la mécanique des fluides numérique (CFD) et des études expérimentales. Cela a permis de mieux comprendre la nature de l'écoulement et du fonctionnement d'une éolienne à deux rotors. Des recherches expérimentales ont été menées dans la soufflerie de l’Institut de Turbomachinerie de l’Ecole Polytechnique de Lodz (Pologne). Une série de mesures de systèmes d'éoliennes divers, avec et sans carénage, à un et deux rotors, a été réalisée. Les résultats recueillis ont permis de confirmer que le carénage pouvait augmenter considérablement (même deux fois) l'efficacité du rotor. Cependant, les forces aérodynamiques et la vitesse de rotation augmentent également. Cet inconvénient peut être partiellement résolu en utilisant un deuxième rotor et en répartissant les charges aérodynamiques sur deux étages de turbine.Une partie importante de l'étude était les simulations numériques. Ils ont permis de préciser la nature et les paramètres de l'écoulement et d'estimer leur impact sur les performances de l'éolienne. Deux modèles numériques différents ont été développés:• Modèle rotor complet (anglais : Fully-resolved Rotor Model, FRM): modèle URANS dans ANSYS CFX, basé sur la discrétisation de la géométrie complète du rotor; ce modèle a été utilisé pour l'analyse de l’écoulement,• Modèle hybride CFD-BET (théorie de l’élément de pâle): modèle RANS dans ANSYS Fluent, dans lequel le rotor est représenté par les termes source dans les équations de Navier-Stokes, déterminés par un code interne; ce modèle a été utilisé pour évaluer les performances de différentes configurations d'éoliennes.Au cours de la recherche, une correction empirique interne de la perte d’extrémité de la pâle (anglais : tip loss correction) a été proposée, en tenant compte de l’influence du diffuseur. L’étude réalisée a permis d’observer, entre autres, que le déplacement du rotor en aval vers la sortie du diffuseur pouvait entraîner une réduction de la vitesse du vent à travers le rotor en amont, placé à l’entrée du diffuseur, et une diminution de la puissance globale du système. / Doctoral dissertation summarizes the research on the functioning and flow around a two-stage, shrouded wind turbine. Placing the turbine at the inlet of a diverging channel allows to increase the mass flow rate of the flow through the rotor. To better take advantage of the increase in wind speed at the diffuser inlet, it was decided to examine the possibility of placing a second rotor in this area, with the opposite direction of rotation.The conducted study combined several different research paths, including Computational Fluid Dynamics (CFD) methods and experimental studies. This allowed for a more refined understanding of the nature of the flow and operation of a wind turbine with two rotors. Experimental research was carried out in the IMP TUL wind tunnel. A series of measurements of various turbine systems with and without shroud, with single- and double-rotor wind turbine were made. The collected results allowed to confirm that the shrouding can significantly (even twice) increase the efficiency of the rotor. However, aerodynamic forces and rotational speed also increase. This disadvantage can be partially addressed by using a second rotor and distributing aerodynamic loads to two turbine stages.An important part of the study were numerical simulations. They allowed to specify in more detail the nature and parameters of the flow and to estimate their impact on the performance of the wind turbine. Two different numerical models were developed:• Fully-resolved Rotor Model: URANS model in ANSYS CFX, based on discretising the entire geometry of the rotor, used for the flow analysis,• Hybrid model CFD-BET (Blade-Element Theory): RANS model in ANSYS Fluent, in which the rotor is represented by source terms in the Navier-Stokes equations, determined by an in-house code; the model was used to evaluate the performance of different wind turbine configurations.In the course of the research an in-house, empirical tip loss correction was proposed, taking into account the influence of the diffuser. The performed study permitted to observe, among others, that moving the rear rotor towards the outlet of the diffuser may result in a reduction of the wind speed through the front rotor, placed at the inlet to the diffuser, and a decrease in the overall system power.

The separating turbulent flow in a plane asymmetric diffuser with 8.5 degrees opening angle is investigated experimentally and computationally. The considered flow case is suitable for fundamental studies of separation, separation control and turbulence modelling. The flow case has been studied in a specially designed wind-tunnel under well controlled conditions. The average velocity and fluctuation fields have been mapped out with stereoscopic particle image velocimetry (PIV). Knowledge of all velocity components allows the study of several quantities of interest in turbulence modelling such as the turbulence kinetic energy, the turbulence anisotropy tensor and the turbulence production rate tensor. Pressures are measured through the diffuser. The measured data will form a reference database which can be used for evaluation of turbulence models and other computational investigations. Time-resolved stereoscopic PIV is used in an investigation of turbulence structures in the flow and their temporal evolution. A comparative study is made where the measured turbulence data are used to evaluate an explicit algebraic Reynolds stress turbulence model (EARSM). A discussion regarding the underlying reasons for the discrepancies found between the experimental and the model results is made. A model for investigations of separation suppression by means of vortex generating devices is presented together with results from the model in the plane asymmetric diffuser geometry. A short article on the importance of negative production-rates of turbulent kinetic energy for the reverse flow region in separated flows is presented. A detailed description of the experimental setup and PIV measurement procedures is given in a technical report. / QC 20100923

This thesis examines methods for designing and analyzing kinetic turbines based on blade element momentum (BEM) theory and computational fluid dynamics (CFD). The underlying goal of the work was to assess the potential augmentation of power production associated with enclosing the turbine in an expanding duct. Thus, a comparison of the potential performance of ducted and non-ducted turbines was carried out. This required de ning optimal turbine performance for both concepts. BEM is the typical tool used for turbine optimization and is very well established in the context of wind turbine design. BEM was suitable for conventional turbines, but could not account for the influence of ducts, and no established methodology for designing ducted turbines could be found in the literature. Thus, methods were established to design and analyze ducted turbines based on an extended version of BEM (with CFD-derived coe cients), and based on CFD simulation. Additional complications arise in designing tidal turbines because traditional techniques for kinetic turbine design have been established for wind turbines, which are similar in their principle of operation but are driven by flows with inherently different boundary conditions than tidal currents. The major difference is that tidal flows are bounded by the ocean floor, the water surface and channel walls. Thus, analytical and CFD-based methods were established to account for the effects of these boundaries (called blockage effects) on the optimal design and performance of turbines. Additionally, tidal flows are driven by changes in the water surface height in the ocean and their velocity is limited by viscous effects. Turbines introduced into a tidal flow increase the total drag in the system and reduce the total flow in a region (e.g. a tidal channel). An analytical method to account for this was taken from the eld of tidal resource assessment, and along with the methods to account for ducts and blockage effects, was incorporated into a rotor optimization framework. It was found that the non-ducted turbine can produce more power per installed device frontal area and can be operated to induce a lesser reduction to the flow through a given tidal channel for a given level of power production. It was also found that by optimizing turbines for array con gurations that occupy a large portion of the cross sectional area of a given tidal channel (i.e. tidal fences), the per-device power can be improved signi cantly compared to a sparse-array scenario. For turbines occupying 50% of a channel cross section, the predicted power improves is by a factor of three. Thus, it has been recommended that future work focus on analyzing such a strategy in more detail. / Graduate