As the number of wireless devices in the world increases, so does the demand for flexible radio receiver architectures capable of operating over a wide range of frequencies and communication protocols. The resonance-based channel-select filters used in traditional radio architectures have a fixed frequency response, making them poorly suited for such a receiver. The N-path filter is based on 1960s technology that has received renewed interest in recent years for its application as a linear high Q filter at radio frequencies. N-path filters use passive mixers to apply a frequency transformation to a baseband low-pass filter in order to achieve a high-Q band-pass response at high frequencies. The clock frequency determines the center frequency of the band-pass filter, which makes the filter highly tunable over a broad frequency range. Issues with harmonic transfer and poor attenuation limit the feasibility of using N-path filters in practice. The goal of this thesis is to design an integrated active N-path filter that improves upon the passive N-path filter’s poor harmonic rejection and limited outof- band attenuation. The integrated circuit (IC) is implemented using the CMRF8SF 130nm CMOS process. The design uses a multi-phase clock generation circuit to implement a harmonic rejection mixer in order to suppress the 3rd and 5th harmonic. The completed active N-path filter has a tuning range of 200MHz to 1GHz and the out-ofband attenuation exceeds 60dB throughout this range. The frequency response exhibits a 14.7dB gain at the center frequency and a -3dB bandwidth of 6.8MHz.

No description available.

Ces travaux de recherche portent sur le développement d’un procédé permettant de mélanger, directement en sortie de polycondensation, du polyamide fondu avec d’autres polymères immiscibles en tant qu’additifs. Ce procédé se distingue ainsi des méthodes d’élaboration conventionnelles pour lesquelles une fusion préalable des polymères est nécessaire. L’étude concerne le mélange de polymères de viscosités très différentes (polyamide 66 et polyéthylène glycol) et le mélange de polymères de viscosités similaires (polyamide 66 et copolymère d’éthylène propylène, en présence ou non d’un agent d’interface : polypropylène greffé par de l’anhydride maléique).Une première partie de ce travail a consisté à caractériser la dispersion de ces mélanges élaborés selon des procédés conventionnels. Ce travail a conduit à développer un modèle reliant la taille de la phase dispersée aux principaux paramètres opératoires de chaque procédé, pour le cas rarement recensé dans la littérature, des mélanges de polymères de viscosités très différentes.La seconde partie a été consacrée à la conception et à la réalisation d’une installation constituée d’un pilote de polycondensation équipé, en sortie de réacteurs, d’un dispositif de mélange reposant sur la technologie des mélangeurs statiques. Son fonctionnement a ensuite été éprouvé pour les deux mélanges considérés, grâce des expériences qui ont permis d’analyser l’influence de différentes conditions opératoires sur la morphologie des mélanges générés. La comparaison des résultats obtenus à ceux issus des procédés conventionnels, a alors permis de préciser les performances et les limites du procédé développé dans cette étude / The aim of this work is to develop a process, which enables to blend polyamide in molten state with others polymers, directly at the outlet of a polycondensation reactor. Contrary to currently industrial processes, no remelting stage is needed in this one. The study has been carried out with polyamide 66 / polyethylene glycol blends (products with very different viscosities) and with polyamide 66 / ethylene propylene blends (products with similar viscosities), with or without polypropylene-graft-maleic-anhydride as interfacial agent. The first part of this work deals with the characterization of the dispersions obtained for these blends when their elaborations are carried out using conventional processes. Only few studies are available on blends, which exhibit a large difference between components viscosity. This work led us to develop a model to correlate, in this case, the dispersed phase size to the main operating conditions of each processes.The second part is dedicated to the design and the realization of an experimental installation, which is composed of polycondensation plant equipped, at the outlet of reactors, with a blending device based on static mixers technology. Its operation has been tested and experiments have been carried out in order to study the influence of the different processing parameters on blends morphology. The comparison of the results with those previously obtained using conventional processes allowed then to precise the performances and the limits of the process developed in this study

Dispositivos de reação miniaturizados tendem a ganhar espaço na indústria de processos químicos por elevarem o transporte de massa e de calor e a segurança dos processos. Para compreender o papel de cada elemento constituinte de um microrreator sobre seu campo de velocidades e fenômenos de mistura, foram simulados um conjunto de dois canais, uma junção em T, 30 canais em formato de serpentina e um microchip completo através da fluidodinâmica computacional. A seção transversal destes microdispositivos têm dimensões entre 100 e 300 µm, enquanto o comprimento dos canais varia de 3000 a 25190 µm. Os modelos computacionais foram discretizados por malhas hexaédricas e os campos de velocidade em estado estacionário foram calculados para vazões de alimentação entre 12,5 e 2000 µL min-1, considerando regime laminar. A mistura foi avaliada pela injeção de traçadores não-reativos e distribuição das respectivas frações mássicas. As simulações foram validadas usando microvelocimetria por imagens de partículas. Os campos de velocidade possuem magnitudes significativas apesar das dimensões reduzidas e baixas vazões de operação dos sistemas. As imagens experimentais do escoamento evidenciaram o formato parabólico do campo de velocidades e o deslocamento de seu ponto máximo nas regiões curvas causado pela força centrífuga, como estimado pelo modelo computacional. Tal força, em conjunto com as forças viscosas na parede, gera fluxos secundários no escoamento. A distribuição de traçadores não-reativos evidenciou a importância dos fluxos secundários para promover mistura na direção ortogonal ao escoamento principal, ocorrendo sob o regime estacionário nas vazões analisadas. O estudo aqui realizado evidencia o emprego da fluidodinâmica computacional como ferramenta para melhor compreensão da fluidodinâmica e como apoio ao projeto de microdispositivos. / Miniaturized reaction vessels are drawing attention of chemical industries because they promote better mass and heat transfer and also enhance process safety. To understand the relevance of each element of a microreactor on the velocity field of the equipment and the corresponding mixing processes, several microdevices were simulated using computational fluid dynamics: an assembly of two channels, a T-junction, 30 channels in a serpentine assembly and a full microreactor. The cross section of the devices is 100 - 300 µm wide and the length of the channels varies between 3000 and 25190 µm. Computational domains were discretized using hexahedral meshes and steady-state velocity fields were computed considering laminar flow for flow rates between 12,5 and 2000 µL min-1. Mixing was evaluated by injecting inert tracers and monitoring their distribution. Simulations were validated against experimental micro particle image velocimetry data. Velocities throughout the devices are relatively high despite the small dimensions of the cross sections and small flow rates. Experimental images of the flow elucidated the parabolic shape of the velocity profile and its distortion on curved segments caused by centrifugal forces, matching predictions of the computational model. Tracer maps indicated secondary flows play an important role in mixing stream perpendicular to the main flow direction. This study emphasizes the use of computational fluid dynamics as a tool for understating flow throughout microdevices and supporting their design.

Este trabalho apresenta o projeto de um bloco LNA-Misturador dentro de um mesmo circuito integrado para aplicações em um receptor Bluetooth 2;45GHz. Uma estratégia de projeto bem clara, concisa e com uma boa base física e matemática foi desenvolvida para auxiliar o processo de projeto de um bloco LNA-Misturador, composto por um LNA cascode em cascata com um misturador de chaveamento de corrente com entradas simples e degeneração indutiva nas fontes dos estágios de transcondutância. Esta estratégia foi adaptada de trabalhos apresentados na literatura. A estratégia de projeto proposta considera o compromisso entre ruído, linearidade, ganho, dissipação de potência, casamento de impedâncias e isolamento de portas, usando as dimensões dos dispositivos e condições de polarização como variáveis de projeto. Com base nesta estratégia se obteve um bloco LNA-Misturador que atinge algumas especificações propostas. Um bloco LNA-Misturador foi projetado e fabricado em uma tecnologia CMOS 0;35µm para validar a estratégia de projeto proposta. Além disso, para atingir os objetivos, durante o desenvolvimento deste trabalho foi dada atenção especial no projeto dos indutores. Foi projetado, fabricado e medido um chip de teste. Para tal fim foram aplicadas técnicas e estruturas de de-embedding nas medidas para conseguir resultados mais confiáveis. Os resultados experimentais obtidos para os indutores e os resultados preliminares do bloco LNA-Misturador s~ao satisfatórios de acordo com as especificações e os esperados das simulações. No entanto, os indutores integrados degradam significativamente o desempenho do bloco LNA-Misturador. Se forem usados processos de fabricação nos quais os indutores apresentem melhor desempenho, os resultados do bloco LNA-Misturador aplicando a estratégia de projeto desenvolvida neste trabalho podem ser melhorados. Finalmente, é importante ressaltar que a estratégia de projeto proposta neste trabalho já está sendo usada e adaptada em outros projetos com o propósito de melhorar os resultados obtidos, e conseguir auxiliar o processo de projeto deste tipo de blocos. / This work presents a fully integrated LNA-Mixer design for a Bluetooth receiver application at 2:45GHz. A concise design strategy with good physics and mathematics basis was developed to assist the design process of a LNA-Mixer block, formed by a cascode LNA in cascade to a single balanced current commutation Mixer with inductive degeneration. This strategy was adapted from literature and considers the trade-offs between noise, linearity, gain, power dissipation, impedance matching and ports isolation, using the device dimensions and bias conditions as design variables. Based on this strategy, the proposed LNA-Mixer design specifications were achieved. To validate the proposed design strategy, the LNA-Mixer were fabricated in a 0:35µm CMOS process. Furthermore, to achieve the specifications, during the development of this work a special attention to the RF CMOS inductors was given. A test chip was designed, fabricated and measured applying de-embedding structures to obtain more reliable results. The experimental results obtained for the inductors and the preliminary results for the LNA-Mixer are satisfactory compared to the specifications and as expected from simulations. However, the integrated inductors degrade the performance of the block significantly and if a manufacturing process in which the inductor has better performance is used, the resulting LNA-Mixer design applying the strategy developed in this work can be improved. Finally, it is important to highlight that the design strategy proposed in this work is already being used and adapted in other designs in order to improve the results, and to assist the design process of such blocks.

by Pun See-mun and Lam Poon-yuen. / Thesis (M.B.A.)--Chinese University of Hong Kong, 1988. / Bibliography: leaves 111-112.

The objective of this research is to develop, characterize, and demonstrate novel parametric architectures capable of wideband operation while maintaining high gain and stability. To begin the study, phase-incoherent upconverting parametric amplifiers will be explored by first developing a set of analytical models describing their achievable gain and efficiency. These models will provide a set of design tools to optimize and evaluate prototype circuit boards. The prototype boards will then be used to demonstrate their achievable gain, bandwidth, efficiency, and stability. Further investigation of the analytical models and data collected from the prototype boards will conclude bandwidth and gain limitations and end the investigation into phase-incoherent upconverting parametric amplifiers in lieu of negative-resistance parametric amplifiers. Traditionally, there were two versions of negative-resistance parametric amplifiers available: degenerate and non-degenerate. Both modes of operation are considered single-frequency amplifiers because both the input and output frequencies occur at the source frequency. Degenerate parametric amplifiers offer more power gain than their non-degenerate counterpart and do not require additional circuitry for idler currents. As a result, a phase-coherent degenerate parametric amplifier printed circuit board prototype will be built to investigate achievable gain, bandwidth, and stability. Analytical models will be developed to describe the gain and efficiency of phase-coherent degenerate parametric amplifiers. The presence of a negative resistance suggests the possibility of instability under certain operating conditions, therefore, an in-depth stability study of phase-coherent degenerate parametric amplifiers will be performed. The observation of upconversion gain in phase-coherent degenerate parametric amplifiers will spark investigation into a previously unknown parametric architecture: phase-coherent upconverting parametric amplifiers. Using the phase-coherent degenerate parametric amplifier prototype board, stable phase-coherent upconversion with gain will be demonstrated from the source input frequency to its third harmonic. An analytical model describing the large-signal transducer gain of phase-coherent upconverting parametric amplifiers from the first to the third harmonic of the source input will be derived and validated using the prototype board and simulations.

Dispositivos de reação miniaturizados tendem a ganhar espaço na indústria de processos químicos por elevarem o transporte de massa e de calor e a segurança dos processos. Para compreender o papel de cada elemento constituinte de um microrreator sobre seu campo de velocidades e fenômenos de mistura, foram simulados um conjunto de dois canais, uma junção em T, 30 canais em formato de serpentina e um microchip completo através da fluidodinâmica computacional. A seção transversal destes microdispositivos têm dimensões entre 100 e 300 µm, enquanto o comprimento dos canais varia de 3000 a 25190 µm. Os modelos computacionais foram discretizados por malhas hexaédricas e os campos de velocidade em estado estacionário foram calculados para vazões de alimentação entre 12,5 e 2000 µL min-1, considerando regime laminar. A mistura foi avaliada pela injeção de traçadores não-reativos e distribuição das respectivas frações mássicas. As simulações foram validadas usando microvelocimetria por imagens de partículas. Os campos de velocidade possuem magnitudes significativas apesar das dimensões reduzidas e baixas vazões de operação dos sistemas. As imagens experimentais do escoamento evidenciaram o formato parabólico do campo de velocidades e o deslocamento de seu ponto máximo nas regiões curvas causado pela força centrífuga, como estimado pelo modelo computacional. Tal força, em conjunto com as forças viscosas na parede, gera fluxos secundários no escoamento. A distribuição de traçadores não-reativos evidenciou a importância dos fluxos secundários para promover mistura na direção ortogonal ao escoamento principal, ocorrendo sob o regime estacionário nas vazões analisadas. O estudo aqui realizado evidencia o emprego da fluidodinâmica computacional como ferramenta para melhor compreensão da fluidodinâmica e como apoio ao projeto de microdispositivos. / Miniaturized reaction vessels are drawing attention of chemical industries because they promote better mass and heat transfer and also enhance process safety. To understand the relevance of each element of a microreactor on the velocity field of the equipment and the corresponding mixing processes, several microdevices were simulated using computational fluid dynamics: an assembly of two channels, a T-junction, 30 channels in a serpentine assembly and a full microreactor. The cross section of the devices is 100 - 300 µm wide and the length of the channels varies between 3000 and 25190 µm. Computational domains were discretized using hexahedral meshes and steady-state velocity fields were computed considering laminar flow for flow rates between 12,5 and 2000 µL min-1. Mixing was evaluated by injecting inert tracers and monitoring their distribution. Simulations were validated against experimental micro particle image velocimetry data. Velocities throughout the devices are relatively high despite the small dimensions of the cross sections and small flow rates. Experimental images of the flow elucidated the parabolic shape of the velocity profile and its distortion on curved segments caused by centrifugal forces, matching predictions of the computational model. Tracer maps indicated secondary flows play an important role in mixing stream perpendicular to the main flow direction. This study emphasizes the use of computational fluid dynamics as a tool for understating flow throughout microdevices and supporting their design.

Este trabalho apresenta o projeto de um bloco LNA-Misturador dentro de um mesmo circuito integrado para aplicações em um receptor Bluetooth 2;45GHz. Uma estratégia de projeto bem clara, concisa e com uma boa base física e matemática foi desenvolvida para auxiliar o processo de projeto de um bloco LNA-Misturador, composto por um LNA cascode em cascata com um misturador de chaveamento de corrente com entradas simples e degeneração indutiva nas fontes dos estágios de transcondutância. Esta estratégia foi adaptada de trabalhos apresentados na literatura. A estratégia de projeto proposta considera o compromisso entre ruído, linearidade, ganho, dissipação de potência, casamento de impedâncias e isolamento de portas, usando as dimensões dos dispositivos e condições de polarização como variáveis de projeto. Com base nesta estratégia se obteve um bloco LNA-Misturador que atinge algumas especificações propostas. Um bloco LNA-Misturador foi projetado e fabricado em uma tecnologia CMOS 0;35µm para validar a estratégia de projeto proposta. Além disso, para atingir os objetivos, durante o desenvolvimento deste trabalho foi dada atenção especial no projeto dos indutores. Foi projetado, fabricado e medido um chip de teste. Para tal fim foram aplicadas técnicas e estruturas de de-embedding nas medidas para conseguir resultados mais confiáveis. Os resultados experimentais obtidos para os indutores e os resultados preliminares do bloco LNA-Misturador s~ao satisfatórios de acordo com as especificações e os esperados das simulações. No entanto, os indutores integrados degradam significativamente o desempenho do bloco LNA-Misturador. Se forem usados processos de fabricação nos quais os indutores apresentem melhor desempenho, os resultados do bloco LNA-Misturador aplicando a estratégia de projeto desenvolvida neste trabalho podem ser melhorados. Finalmente, é importante ressaltar que a estratégia de projeto proposta neste trabalho já está sendo usada e adaptada em outros projetos com o propósito de melhorar os resultados obtidos, e conseguir auxiliar o processo de projeto deste tipo de blocos. / This work presents a fully integrated LNA-Mixer design for a Bluetooth receiver application at 2:45GHz. A concise design strategy with good physics and mathematics basis was developed to assist the design process of a LNA-Mixer block, formed by a cascode LNA in cascade to a single balanced current commutation Mixer with inductive degeneration. This strategy was adapted from literature and considers the trade-offs between noise, linearity, gain, power dissipation, impedance matching and ports isolation, using the device dimensions and bias conditions as design variables. Based on this strategy, the proposed LNA-Mixer design specifications were achieved. To validate the proposed design strategy, the LNA-Mixer were fabricated in a 0:35µm CMOS process. Furthermore, to achieve the specifications, during the development of this work a special attention to the RF CMOS inductors was given. A test chip was designed, fabricated and measured applying de-embedding structures to obtain more reliable results. The experimental results obtained for the inductors and the preliminary results for the LNA-Mixer are satisfactory compared to the specifications and as expected from simulations. However, the integrated inductors degrade the performance of the block significantly and if a manufacturing process in which the inductor has better performance is used, the resulting LNA-Mixer design applying the strategy developed in this work can be improved. Finally, it is important to highlight that the design strategy proposed in this work is already being used and adapted in other designs in order to improve the results, and to assist the design process of such blocks.

Le contrôle de la porosité des supports de catalyseurs est un enjeu important dans l'industrie du raffinage. L'objectif de cette thèse est de développer un nouveau procédé de précipitation afin d'obtenir des alumines γ présentant des propriétés texturales originales vis-à-vis de celles préparées de façon conventionnelle par précipitation de boehmite en réacteur agité. Pour cela, les influences combinées du précurseur, de la technologie de mélange et du temps de micromélange sur les propriétés physiques du produit final ont été étudiées. Ce travail de thèse propose donc une comparaison de trois technologies de mélange : un réacteur agité conventionnel, un réacteur à disque tournant et un disperseur rotor-stator. Les gammes de temps de micromélange accessibles avec chacun de ces réacteurs sont déterminées par la méthode iodure-iodate. L'étude porte sur la précipitation de deux précurseurs de l'alumine : la boehmite, classiquement utilisée, ainsi que la NH4-dawsonite, dont l'intérêt pour la préparation de supports de catalyseurs est plus récent. Leur solubilité est estimée dans la mesure du possible à l'aide des données thermodynamiques de la littérature. Dans le cadre de cette étude préliminaire, un modèle de suivi de la sursaturation en fonction du temps de micromélange est mis en place à l'aide des équations cinétiques de la précipitation de la boehmite. La caractérisation de la NH4-dawsonite précipitée en réacteur agité met en évidence l'intérêt de ce précurseur pour obtenir des alumines à forte porosité présentant des diamètres poreux moyens entre 10 et 30 nm. Une nuance est toutefois apportée aux fortes surfaces spécifiques généralement revendiquées sur ce matériau dans la littérature. Malgré tout, les propriétés texturales de l'alumine ex-dawsonite présentent une évolution thermique atypique lui permettant de se démarquer de l'alumine ex-boehmite. L'étude de la précipitation en mélangeur rapide met en évidence une grande différence de comportement entre les deux précurseurs. Contrairement à la boehmite, la forte sensibilité de la NH4-dawsonite au temps de micromélange permet d'obtenir une large gamme de propriétés texturales. Ce travail de thèse confirme donc l'intérêt de la NH4-dawsonite comme précurseur alternatif de l'alumine pour obtenir des propriétés texturales originales. L'utilisation de plusieurs systèmes précurseur / technologie de mélange s'avère également prometteuse pour couvrir une large gamme de propriétés texturales / Control of catalyst supports porosity is an important challenge for the refining industry. The aim of this thesis is to develop a new precipitation process in order to obtain γ-alumina supports exhibiting new textural properties compared with those prepared by the conventional boehmite precipitation route in stirred tank reactor. For that purpose, combined influences of precursor, mixing technology and micromixing time on the final product physical properties were studied.Three mixing technologies were compared: a classic stirred tank reactor, a sliding surface mixing device and a rotor-stator mixer. Micromixing time ranges achievable with each of these reactors were determined using the iodide-iodate method. The study focused on the precipitation of two alumina precursors: boehmite, usually used, and NH4-dawsonite, which interest for catalyst supports preparation is quite recent. A model was developed to simulate the supersaturation evolution as a function of the micromixing time, based on boehmite precipitation kinetic equations.Characterization of NH4-dawsonite precipitated in a stirred tank reactor confirmed this precursor interest in order to prepare high porosity aluminas with mean pore diameters ranging between 10 and 30 nm. Study of the precipitation conducted in fast contacting mixers highlighted a significant difference in the behaviour of both precursors. Contrary to boehmite, NH4-dawsonite high sensitivity to micromixing time led to a wide range of textural properties.This thesis work therefore confirms the NH4-dawsonite potential as an alternative alumina precursor in order to reach new textural properties. The use of several precursor / mixing technology systems has also proven promising to cover a wide range of textural properties