Heat transfer augmentation is of paramount importance in energy transfer and storage systems and the idea of using the inherent vibrations in a system to enhance heat transfer needs to be thoroughly researched upon. The current study numerically investigates an infinitesimally thin plate-fin undergoing forced oscillations over a range of amplitudes and frequencies in the presence of an approach flow. Reduced frequencies of 0.25 ≤ k ≤16 and plunge amplitudes of 0.03125 ≤ h ≤ 8 are investigated at Re=100 and Pr = 0.71. It is shown that the combined effect of frequency and amplitude on heat transfer enhancement can be accounted for as a single parameter “plunge velocity” (0.25 ≤ kh ≤ 4) instead of the individual frequency and amplitude values. For kh > 0.5 a significant increase in Nusselt number ( is observed compared to a stationary plate. With increasing kh or more vigorous oscillations, the increase in becomes more prominent and similar trends and comparable magnitudes were observed for a constant value. Unlike the hydrodynamic counterpart of the study, both Leading Edge Vortices (LEVs) and Trailing Edge Vortices (TEVs) are found to act positively to induce enhanced heat transfer on the plate. Finally, the dependence of heat transfer augmentation on the frequency and amplitude of vibration is quantified with a simple parameterization for a plate-fin in a fluid medium. / M.S. / Heat transfer enhancement is of paramount importance in energy transfer and storage systems. The idea of using the inherent mechanical vibrations in a heat producing system to enhance transfer of unwanted heat from that system needs to be thoroughly researched upon. To investigate this idea, we numerically study an infinitesimally thin plate-fin undergoing forced oscillations over a range of amplitudes and frequencies in the presence of an incoming air flow. It is shown that the combined effect of frequency and amplitude on heat transfer enhancement can be accounted for as a single parameter called “plunge velocity” instead of the individual frequency and amplitude values. For a significant plunge velocity, a significant increase in Nusselt number ( is observed compared to a stationary plate representing an increase in the extent of heat transferred. With more vigorous oscillations, the increase in becomes more prominent and similar trends and comparable magnitudes were observed for a constant value. Finally, the dependence of heat transfer augmentation on the frequency and amplitude of vibration is quantified with a simple parameterization for a plate-fin in a fluid medium.

La maîtrise de la température des composants à forte dissipation, notamment dans les systèmes électroniques nomades, constitue un verrou à leurs développements. Que ce soit pour l'électronique de puissance ou les calculateurs, les densités de puissance requièrent l'utilisation de systèmes de refroidissement de plus en plus performants, en particulier dans le cas des microprocesseurs qui associent miniaturisation et augmentation des fréquences d'horloge. Les conséquences sont multiples, limitation des performances, augmentation de la consommation et du taux de défaillance. C'est dans ce contexte que le projet CANOPEE, réunissant un consortium de partenaire industriel et académique, propose de développer et démontrer les avantages d'une solution technologique active récemment brevetée et appelée OnduloTrans. Elle consiste en un dispositif échangeur-pompe, permettant à la fois d'obtenir un excellent transfert thermique et d'assurer le pompage du fluide caloporteur. OnduloTrans est une solution active de refroidissement basée sur la déformation dynamique d'une paroi d'un canal. Le dispositif est fixé directement à l'aplomb du composant à refroidir. Le canal est déformé suivant une onde progressive pour créer un pompage péristaltique. L'intensification des transferts est obtenue lorsque les variations dynamiques des dimensions du canal viennent perturber la couche limite à l'interface conduction/convection. Le travail de la thèse consiste à concevoir et développer une solution d'actionnement intégrée permettant de mouvoir la paroi souple. Il s'accompagnera d'essais concrets témoignant des performances thermiques de cette solution. L'actionnement mis en oeuvre doit respecter les contraintes hydrauliques et thermiques de l'application embarquée visée, tout particulièrement le faible encombrement et une consommation électrique minimale. La difficulté réside dans les critères antagonistes que sont la production d'une onde progressive de grande amplitude dans un milieu aux dimensions centimétriques. Le manuscrit s'articule en trois parties. Dans un premier temps les solutions d'actionnement envisageables seront explorées. Pour ce faire, la solution OnduloTrans est d'abord décrite. Un état de l'art des solutions de conversion électromécanique, puis des micropompes péristaltiques est entrepris. Les phénomènes hydrauliques propres au micropompage péristaltique sont abordés pour cerner la problématique du développement de l'actionnement. Ensuite les deux chapitres suivants détaillent l'étude de deux solutions piézoélectriques distinctes. Une première solution piézoélectrique à onde discrète est développée dans le second chapitre. Elle consiste en une répartition d'actionneurs flextensionnels le long de la paroi souple. Une méthodologie de prédimensionnement basée sur des modèles mécaniques simples est présentée. L'onde progressive créée étant très particulière, une méthode analytique de calcul du débit, validée par simulations numériques, permet d'étudier l'influence de la commande des actionneurs. Un prototype est finalement réalisé avec l'aide des partenaires. De nombreux essais sont ensuite réalisés afin de valider les différentes hypothèses et déterminer les premières performances hydrauliques et thermiques du dispositif. Le troisième chapitre aborde une solution à onde progressive continue et actionnement intégré à la membrane. Le but est ici de prouver le concept de pompage péristaltique par flexion contrôlée d'une plaque intégrant une couche piézoélectrique. Un modèle de dimensionnement 1D constitué de tronçons piézoélectriques répartis à la surface est tout d'abord présenté. La répartition des segments piézoélectriques fait ensuite l'objet d'une étude paramétrique afin de définir judicieusement leur disposition, ceci en vue de maximiser le débit théorique. Cette étude paramétrique est finalement couplée à une optimisation des commandes électriques, évaluée par les résultats d'un prototype. / Controlling the temperature of components with high thermal dissipation is a constraining factor in their developments, especially in embedded electronic systems. Power density, whether in computing or power electronics, requires the use of ever more efficient cooling systems. This is especially true for microprocessors in which increasingly miniaturization and clock frequency are combined. Consequently, without the adequate cooling, the performance is severely limited and its power consumption increased as well as the failure rate. In this challenging context a consortium of industrial and academic partners created the CANOPEE project. CANOPEE focus is to develop and prove the advantages of a recently patented solution called OnduloTrans. The solution is an exchanger-pump device, ensuring at the same time an excellent heat transfer and the pumping of the coolant. OnduloTrans is an active cooling solution based on the dynamic deformation of a thin wall. This deformation is in the manner of a pseudo travelling wave to satisfy a peristaltic pumping. The device is fixed directly above the component to be cooled, thus the liquid flows on its surface. The enhancement in heat transfer is obtained when the dynamic variations of the channel thickness disturb the boundary layer near the conduction / convection interface. The purpose of this thesis was to study the capability of such active pumping system and to design an integrated actuation solution to move the flexible wall. It will result to experimental tests showing the thermal performance of this solution. The implemented actuation system must respect the constraints for on-board applications, especially compactness and minimal power consumption. The challenge stands in the trade-off between the production of a large amplitude travelling wave and the limited volume available. The manuscript is divided into three parts. Initially, the different actuation solutions will be explored. To do this, the OnduloTrans solution is first described. Then, a state of the art of electromechanical conversion solutions and peristaltic micropumps is undertaken. After that, the specific hydraulic phenomena involved in peristaltic micropumps are discussed to determine the difficulties in the development of such actuation system. Then the two next chapters detail the study of two distinct piezoelectric solutions. A discrete wave piezoelectric solution is presented in the second chapter. It consists of a distribution of flextensional actuators along the flexible wall. A pre-dimensioning methodology based on simple mechanical models is presented. The created wave is very particular, so an analytical method is developed to evaluate the flow rate and making possible to study the impact of the actuator control strategy. This algorithmic method is validated by comparison with finite element numerical simulations. A prototype is finally made with the support of partners. Several tests are then carried out in order to validate the hypotheses and evaluate the preliminary hydraulic and thermal performances of the prototype. The third chapter addresses a continuous travelling wave solution and an actuation system integrated into the membrane. The purpose here is to prove the concept of peristaltic pumping by controlled bending of a plate incorporating a piezoelectric layer. A 1D dimensioning model consisting of piezoelectric segments distributed on the surface is first presented. The distribution of the piezoelectric segments is then the subject of a parametric study to judiciously define their arrangement, in order to maximize the theoretical flow. This parametric study is finally coupled with an optimization of electrical controls, and compared to the experimental results of a prototype.

All modern High Temperature Reactors (HTR) thermal cycles have one thing in common: the use of some form of heat exchanger. This heat exchanger is used to pre-heat or cool the primary loop gas, from where the secondary power generation cycle is driven. The Compact Heat Exchanger (CHE) type offers high heat loads in smaller volumes. Various studies have been done to improve the heat transfer in the flow channels of these CHEs but little focus has been placed on the thermal design of surrounding material in such a heat exchanger. The focus of this study is on the effective material usage in a CHE. Three test cases were investigated (trapezoidal, serpentine and zigzag layouts with semi-circular cross-sections) all under the same boundary conditions. Computational Fluid Dynamics (CFD) was used to simulate these test cases and the results were evaluated according to four factors, the volume ratio, heat spots, temperature difference and the combined enhancement factor. From the results it was concluded that the zigzag layout performs best when evaluated according to the volume ratio and the temperature difference and gave the best overall enhancement factor. The serpentine layout performed the worst when evaluated according to the enhancement factor. / Thesis (MIng (Nuclear Engineering))--North-West University, Potchefstroom Campus, 2013

All modern High Temperature Reactors (HTR) thermal cycles have one thing in common: the use of some form of heat exchanger. This heat exchanger is used to pre-heat or cool the primary loop gas, from where the secondary power generation cycle is driven. The Compact Heat Exchanger (CHE) type offers high heat loads in smaller volumes. Various studies have been done to improve the heat transfer in the flow channels of these CHEs but little focus has been placed on the thermal design of surrounding material in such a heat exchanger. The focus of this study is on the effective material usage in a CHE. Three test cases were investigated (trapezoidal, serpentine and zigzag layouts with semi-circular cross-sections) all under the same boundary conditions. Computational Fluid Dynamics (CFD) was used to simulate these test cases and the results were evaluated according to four factors, the volume ratio, heat spots, temperature difference and the combined enhancement factor. From the results it was concluded that the zigzag layout performs best when evaluated according to the volume ratio and the temperature difference and gave the best overall enhancement factor. The serpentine layout performed the worst when evaluated according to the enhancement factor. / Thesis (MIng (Nuclear Engineering))--North-West University, Potchefstroom Campus, 2013

No description available.

Tesla valve applications for passive flow enhancement in micro fluidic applications are promising, because of its design of no-moving-parts. The effectiveness of the valve (measured via its pressure and thermal diodicity) can be increased by creating a multi-staged Tesla valve. Present study investigates the effect of varying Reynolds number (25-200) on flow rectification and thermal enhancement capability of a Tesla valve. Gamboa Morris Forster (GMF) design with a cross-section of 1mm2 and constant valve-to-valve distance (1mm) was utilized for this research. An arbitrary fluid with constant properties at a reference temperature was used as the working fluid. Periodicity in flow and thermal distribution are noticed in the latter part of MSTV. Average friction factor and pressure diodicity decreased with increasing Reynolds number whereas average Nusselt number and thermal diodicity increased. Correlations for friction factor, pressure diodicity, Nusselt number, and thermal diodicity were derived by fitting a non-linear curve fit model.

Dropwise condensation (DWC) has the potential to enhance heat transfer compared to filmwise condensation (FWC). The heat transfer rates achieved by DWC depend on the drop size distribution, which is influenced by nucleation processes of newly formed drops. In DWC modeling, the nucleation site density Ns is used as an input parameter to obtain the drop size distribution of small drops. However, due to the small scale of the condensate nuclei, direct observation is difficult, and experimental data on the nucleation site density are scarce. In the literature, values in the range of 109 m−2 to 1015 m−2 can be found for Ns. In this paper, we report DWC experiments on SiO2 and 1H,1H,2H,2H-perfluorodecyltriethoxysilane (PFDTES) thin hydrophobic coatings that show significantly different nucleation site densities. Nucleation site densities are estimated from high-speed imaging of small drops during initial condensation and from model calibration using established DWC theory. We have found the values for Ns to be in the range from 1.1×1010 m−2 to 5.1×1011 m−2 for the SiO2 coating and 1011 m−2 to 1013 m−2 for the PFDTES coating. Our results show that there can be large differences in the nucleation site density under similar conditions depending on the surface properties. This underlines the importance of investigating nucleation site density specifically for each surface and under consideration of the specific process conditions used for DWC.

No description available.

This research comprises an experimental and theoretical study on convective boiling inside tubes containing twisted-tape inserts. The demand for more compact and efficient thermal systems, in which the heat exchangers plays an important role, has led to the development and use of various heat transfer enhancement techniques. Among them twisted-tape insert as a swirl flow device is one of the most used. Twisted-tape inserts have been used for over more than one century ago as a technique of heat transfer enhancement applied to heat exchangers. However, the heat transfer augmentation comes together with pressure drop increment, impacting the pumping power and, consequently, the system efficiency. Moreover, until now it is not clear, the operational conditions under which the heat transfer coefficient augmentation by the use of twisted-tape inserts overcomes pressure drop penalty. In the present study, initially, extensive investigations of the literature concerning convective boiling inside plain tubes with and without twisted-tape inserts were performed. This literature review covers pressure drop, heat transfer coefficient and the leading frictional pressure drop gradient and heat transfer coefficient predictive methods during convective boiling inside tubes with and without twisted-tape inserts. Then, pressure drop and heat transfer coefficient results acquired in the present study were obtained in an experimental apparatus of 12.7 and 15.9 mm ID tubes during flow boiling of R134a for twisted-tape ratios of 3, 4, 9, 14 and tubes without inserts, mass velocities ranging from 75 to 200 kg/m2 s, saturation temperatures of 5 and 15°C and heat fluxes of 5 and 10 kW/m2. The experimental results were parametrically analyzed and compared against the predictive methods from literature. An analysis of the enhancement of the heat transfer coefficient and the pressure drop penalty is presented. Heat transfer coefficient increments up to 45% keeping the same pumping power and pressure drop penalty of about 35% were obtained by using twisted-tape relative to tubes without inserts. Additionally, through comparison of the present study experimental results with the predictive methods from the literature for heat transfer coefficient during two-phase flow inside tube containing twisted-tape inserts, it was verified that non of these methods predict satisfactory well the experimental results. However, a new method was develop for predicting the heat transfer coefficient during flow boiling inside tubes containing twisted-tape inserts based on the experimental results obtained in the present study. The predictive method takes into account the physical picture of the swirl flow phenomenon by including swirl flow effects promoted by the twisted-tape inserts. The proposed method predicts satisfactorily well the data obtained in the present study, predicting 89.1% of the experimental data within an error band of ± 30% and absolute mean deviation of 15.7%. / A presente pesquisa trata-se de um estudo teórico e experimental sobre a ebulição convectiva no interior de tubos com fitas retorcidas. A crescente demanda por sistemas térmicos mais compactos e eficientes, nos quais os trocadores de calor apresentam elevada relevância, tem motivado o desenvolvimento de inúmeras técnicas de intensificação de troca de calor, sendo que a utilização de fitas retorcidas é uma das técnicas mais adotadas. Fitas retorcidas são utilizadas como técnicas de intensificação de troca de calor há mais de um século. Entretanto o incremento da transferência de calor é acompanhado do aumento da perda de pressão, que por sua vez implica em aumento da potência de bombeamento, e consequentemente afeta a eficiência global do sistema. Adicionalmente, até os dias de hoje não há consenso sobre as condições operacionais em que o ganho com o incremento do coeficiente de transferência de calor é superior à perda devido ao aumento da perda de pressão. Neste estudo, inicialmente foi realizada uma extensa revisão da literatura sobre a ebulição convectiva no interior de tubos com e sem fitas retorcidas. Esta revisão aborda aspectos relacionados à perda de pressão e ao coeficiente de transferência de calor, juntamente com os métodos de previsão destes parâmetros. Foram realizados experimentos para determinação experimental de perda de pressão e coeficiente de transferência de calor, em aparato experimental contando com tubos horizontais com diâmetros internos iguais a 12,7 e 15,9 mm, para escoamento bifásico de R134a, razões de retorcimento iguais a 3, 4, 9, 14 e tubo sem fita, velocidades mássicas entre 75 e 200 kg/m²s, temperaturas de saturação iguais a 5 e 15°C, e fluxo de calor iguais a 5 e 10 kW/m². Os resultados experimentais foram analisados e comparados com estimativas segundo métodos disponíveis na literatura. Uma análise do aumento do coeficiente de transferência de calor e da perda de pressão friccional é apresentada. Foram verificados incrementos do coeficiente de transferência de calor de até 45% para a mesma potência de bombeamento, e aumento de perda de pressão de aproximadamente 35% para tubos com fitas retorcidas em relação aos tubos sem fita. Adicionalmente, através da comparação dos resultados experimentais com os métodos de previsão para coeficiente de transferência de calor, foi verificado que nenhuma metodologia apresentava previsões satisfatórias dos resultados. Portanto um novo método para previsão do coeficiente de transferência de calor durante ebulição convectiva no interior de tubos com fitas retorcidas foi desenvolvido com base nos resultados experimentais obtidos durante o presente estudo. O método proposto é função de parâmetros geométricos e do escoamento, e também de parâmetros físicos do escoamento rotacional induzido pela fita. A metodologia desenvolvida apresenta previsões satisfatórias dos resultados experimentais, prevendo 89,1% dos resultados experimentais com erro inferior a ± 30% e erro médio absoluto igual a 15,7%.

In the last few decades, augmentation of heat transfer has emerged as an important research topic. Although many promising heat transfer enhancement techniques have been proposed, such as the use of longitudinal vortex generators, few researches deal with thermal optimization. In the present work, it was conducted an optimization of delta winglet vortex generators position and angles in a fin-tube compact heat exchanger with two rows of tubes in staggered tube arrangement. Two approaches were evaluated: Response Surface Methodology (Neural Networking) and Direct Optimization. Finite-Volume based commercial software (Fluent) was used to analyze heat transfer, flow structure and pressure loss in the presence of longitudinal vortex generators (LVG). The delta winglet aspect ratio was 2 and the Reynolds numbers, based on fin pitch, were 250 and 1400. Four vortex generator parameters which impact heat exchanger performance were analyzed: LVG position in direction x-y, attack angle (θ) and roll angle (ᵩ). The present work is the first to study the influence of LVG roll angle on heat transfer enhancement. In total, eight independent LVG parameters were considered: (x₁y₁θ₁ᵩ₁) for the first tube and (x₂y₂θ₂ᵩ₂) for the second tube. Factor Analysis method (software ModeFrontier) was used to study of the influence of these LVG parameters in heat exchanger performance. The effect of each LVG parameter on heat transfer and pressure loss, expressed in terms of Colburn factor (j) and Friction factor (f), respectively, were evaluated. The optimized LVG configurations led to heat transfer enhancement rates that are much higher than reported in the literature. Direct Optimization reported better results than Response Surface Methodology for all objective functions. Important interactions were found between VG1 and VG2, which influenced the results of Colburn (j) and Friction (f) factors for each Reynolds number. Particularly, it was found that the asymmetry of the LVG, in which the VG2 parameters strongly depend on the VG1 parameters, plays a key role to enhance heat transfer. Moreover, for each Reynolds number and each objective function, there is an optimal LVG arrangement. If the objective is to mitigate pressure drop, VG1 may be suppressed because its main goal is increasing the heat transfer downstream. On the other hand, VG2 was relevant for both increase the heat transfer and decrease the pressure drop. Roll angle had a strong influence on Friction factor (f), especially for VG1 and low Reynolds number. / Por muitos anos, a intensificação da transferência de calor tem despontado como um importante tópico de pesquisa. Embora existam muitas técnicas eficazes de intensificação da transferência de calor, como o uso de geradores de vórtices, poucos trabalhos de pesquisa lidam com a otimização. Neste trabalho, foi realizada a otimização das posições e ângulos dos geradores de vórtice longitudinal (LVG) tipo meia asa delta, considerando um trocador de calor tubo-aleta compacto com duas linhas de tubos desalinhados. Duas abordagens foram empregadas: Método da Superfície de Resposta (Neural Networking) e Otimização Direta. Um software comercial (Fluent), baseado na metodologia de volumes finitos, foi empregado na análise numérica da transferência de calor, estruturas vorticais e perda de pressão no escoamento, na presença de LVG. A razão de aspecto dos geradores de vórtice foi 2 e o número de Reynolds, baseado na distância entre as aletas, foram de 250 e 1400. Foram analisados quatro parâmetros dos LVG, os quais impactam na performance do trocador de calor: a posição do LVG na direção x-y, o ângulo de ataque (θ) e o ângulo de rolamento (ᵩ). O ângulo de rolamento foi primeiramente estudado neste trabalho. No total, oito parâmetros independentes do LVG foram considerados: (x₁y₁θ₁ᵩ₁) para o primeiro tubo e (x₂y₂θ₂ᵩ₂) para o segundo tubo. O método da Análise Fatorial (software ModeFrontier) foi aplicado no estudo da influência destes parâmetros dos LVG na performance do trocador de calor. Também foi avaliado o efeito de cada um destes parâmetros na transferência de calor e perda de pressão do escoamento, expressos em termos do fator de Colburn (j) e do fator de Atrito (f), respectivamente. As configurações otimizadas dos LVG, conduziram à taxas de transferência de calor maiores do que aquelas reportadas pela literatura. A Otimização Direta mostrou resultados melhores do que através da metodologia de Superfície de Resposta para todas as funções objetivas avaliadas neste trabalho. Importantes interações foram identificadas entre VG1 e VG2, os quais influenciaram nos resultados dos fatores de Colburn (j) e Atrito (f) para cada número de Reynolds. Particularmente, foi identificado que a assimetria dos LVG desempenha um papel fundamental na intensificação da transferência de calor, onde os parâmetros de VG2 dependem fortemente dos parâmetros de VG1. Além disso, para cada número de Reynolds e para cada função objetivo, existe uma configuração ótima dos parâmetros do LVG. Se o objetivo é a redução da perda de pressão global, VG1 poderia ser suprimido da modelagem, pois a sua principal função é aumentar a transferência de calor ao longo da aleta. Por outro lado, VG2 foi relevante tanto para aumentar a transferência de calor quanto para diminuir a perda de pressão. O ângulo de rolamento teve grande influência sobre o resultado do fator de Atrito (f), especialmente para VG1 e para baixo número de Reynolds.