Direct lift control for aircraft has been around in the aeronautical industry for decades but is mainly used in commercial aircraft with dedicated direct lift control surfaces. The focus of this thesis is to investigate if direct lift control is feasible for a fighter aircraft, similar to Saab JAS 39 Gripen, without dedicated control surfaces. The modelled system is an aircraft that is inherently unstable and contains nonlinearities both in its aerodynamics and in the form of limited control surface deflection and deflection rates. The dynamics of the aircraft are linearised around a flight case representative of a landing scenario. Direct lift control is then applied to give a more immediate relation from pilot stick input to change in flight path angle while also preserving the pitch attitude. Two different control strategies, linear quadratic control and model predictive control, were chosen for the implementation. Since fighter aircraft are systems with fast dynamics it was important to limit the computational time. This constraint motivated the use of specialised methods to speed up the optimisation of the model predictive controller. Results from simulations in a nonlinear simulation environment supplied by Saab, as well as tests in high-fidelity flight simulation rigs with a pilot, proved that direct lift control is feasible for the investigated fighter aircraft. Sufficient control authority and performance when controlling the flight path angle were observed. Both developed controllers have their own advantages and which strategy is the most suitable depends on what the user prioritises. Pilot workload during landing as well as precision at touch down were deemed similar to conventional control.

Cette thèse traite du problème de la chute de robots humanoïdes. L’étude consiste à découpler la stratégie de chute en une phase de pré-impact et une phase de post-impact. Dans la première, une solution géométrique permet au robot de choisir des points d’impact dans un environnement encombré. Pour ce faire, le robot réadapte sa posture tout en évident les singularités de chute et en préparant le seconde phase. La phase de post-impact utilise une commande par Programmation Quadratique (QP) qui permet d’adapter les gains Proportionnels-Dérivés (PD)des moteurs en ligne, ceci afin d’obtenir de la compliance dans les articulations. L’approche consiste à incorporer les gains de raideur et d’amortissement dans le vecteur d’optimisation du QP avec les variables habituelles que sont l’accélération articulaire et les forces de contact. Les contraintes ont été adaptées à ce nouveau QP. Enfin,comme la solution est locale, une commande de modèle prédictif sur un modèle simplifié du robot. A chaque pas du développement, plusieurs expériences et simulations ont été effectuées. / This thesis deals with the problem of humanoid falling with a decoupled strategy consisting of a pre-impactand a post-impact stages. In the pre-impact stage, geometrical reasoning allows the robot to choose appropriateimpact points in the surrounding environment –that can be unstructured and may contain cluttered obstacles,and to adopt a posture to reach them while avoiding impact singularities and preparing for the post-impact. Thepost-impact stage uses a quadratic program controller that adapts on-line the joint proportional-derivative (PD)gains to make the robot compliant, i.e. to absorb post-impact dynamics, which lowers possible damage risks.We propose a new approach incorporating the stiffness and damping gains directly as decision variables in theQP along with the usually-considered variables that are the joint accelerations and contact forces. By doing so,various constraints can be added to the QP. Finally, since the gain adaptation is local, we added a preview ona time-horizon for more optimal gain adaptation based on model reduction. At each step of the development,several experiments on the humanoid robot HRP-4 in a full-dynamics simulator are presented and discussed.

The use of robotic manipulators in industrial applications is continuously growing. Therefore, the proposal of novel kinematic architectures for robotic manipulators can be a strategy for coping with the required performance of specific tasks. On this matter, the parallel manipulators represent an alternative to fulfill this gap. The objective of this manuscript is to prove that the energy efficiency of parallel manipulators can be increased by the use of kinematic redundancy. Due to the presence of kinematic redundancy, the number of solutions to the inverse kinematics problem become infinite. Hence, a redundancy resolution scheme is required to select a suitable one among the infinite solutions. In this work, a model predictive control (MPC) based method is proposed as redundancy resolution scheme. This proposal is evaluated numerically and experimentally by comparing the energy consumption of non-redundant and kinematically redundant manipulators during the execution of pre-defined tasks. The non-redundant manipulator under study is the planar parallel 3RRR manipulator. This manipulator consists of three identical kinematic chains containing one active revolute joint and two passive revolute joints. Kinematic redundancies were added to the manipulator by including one active prismatic joint in each kinematic chain. In this way, the kinematically redundant manipulator under study is the planar parallel 3PRRR manipulator. By activating or locking the prismatic joints, up to three levels of kinematic redundancy can be evaluated. Numerical kinematic and dynamic models of the manipulators under study were derived not only for their numerical evaluation but also for the derivation of the model-based redundancy resolution scheme. Experimental data was acquired using the prototype built at the Laboratory of Dynamics at São Carlos School of Engineering at University of São Paulo. This experimental data was exploited for assessing the usability of the MPC for deriving a redundancy resolution scheme and for evaluating the impact of several levels of kinematic redundancy on the manipulator\'s energy consumption. Based on this data, one can conclude that MPC can be a suitable alternative for solve redundancy resolution problems and that the redundant parallel manipulators presented a lower energy consumption than the non-redundant one to execute the pre-defined tasks. The rate of reduction on the energy consumption achieved by the redundant manipulators varied between 6% and 60% depending on the task. Nevertheless, the numerical and experimental data presented differences in some particular cases. / O número de aplicações realizadas pelos manipuladores robóticos cresce continuamente. Assim, o desenvolvimento de novas arquiteturas para os manipuladores robóticos mais adaptadas a aplicações concretas é necessário. Destarte, os manipuladores paralelos constituem uma alternativa a ser considerada. O objetivo deste texto é provar que a eficiência energética dos manipuladores paralelos pode ser incrementada por meio da redundância cinemática. A presença de redundância cinemática implica um número infinito de soluções no problema da cinemática inversa. Logo, é precisso um esquema de resolução de redundância para escolher uma das soluções. No presente texto, um método baseado no modelo de controle preditivo (MPC), é proposto como esquema de resolução de redundância. Esta proposta é avaliada tanto numérica como experimentalmente comparando o consumo energético dos manipuladores não redundante e redundantes durante a execução de umas trajetórias predefinidas. O manipulador paralelo não redundante estudado é o 3RRR. Este manipulador é composto por três cadeias cinemáticas idênticas que incluem uma junta rotativa ativa e duas juntas rotativas passivas. Redundâncias cinemáticas foram adicionadas ao manipulador incluindo uma junta prismática ativa em cada uma das três cadeias cinemáticas, obtendo assim, o manipulador redundante 3PRRR. Ativando ou bloqueando as juntas prismáticas podem ser avaliados até três níveis de redundância cinemática. Modelos matemáticos dos manipuladores foram propostos tanto para a estabelecer uma avaliação numérica como para a dedução do esquema de resolução de redundância. Um protótipo do manipulador 3PRRR construído na Escola da Engenharia de São Carlos foi usado para realizar os experimentos. Os dados experimentais foram utilizados para comprovar a utilidade do MPC como esquema de resolução de redundância, e para avaliar os efeitos da redundância cinemática no consumo energético. Com fundamento nos resultados é possível concluir que o MPC pode ser uma alternativa adequada para resolver problemas de resolução de redundância e que os manipuladores paralelos redundantes apresentaram um menor consumo energético para realizar a mesma tarefa quando comparados aos não redundante. A taxa de redução da energia em favor dos manipuladores redundantes varia entre 6% e 60% dependendo da tarefa. Por outro lado, a análise numérica mostrou discrepâncias com a análise experimental em certas circunstâncias.

O objetivo principal desta tese foi a implantação de uma nova estratégia para a integração da otimização em tempo real (RTO), com o controle preditivo multivariável em uma unidade de processo industrial. A solução proposta pode ser considerada como uma estratégia de uma camada, na qual os problemas de controle e otimização econômica são resolvidos simultaneamente, na mesma camada da estrutura de controle. Supondo que o objetivo econômico a ser maximizado (minimizado) seja uma função côncava (convexa) das entradas e saídas de processo, o controlador MPC com otimização econômica (OMPC) foi obtido através da inclusão do gradiente reduzido do objetivo econômico, na função objetivo do controlador preditivo. Esta abordagem foi testada inicialmente através da simulação do conjunto reator regenerador de uma Unidade de Craqueamento Catalítico Fluido (UFCC). O controlador otimizador foi implementado com sucesso em uma coluna de destilação de tolueno, na Unidade de Recuperação de Aromáticos da refinaria de Cubatão da Petrobras. Este controlador está em funcionamento contínuo por cerca de um ano, sem qualquer problema relatado. Para a determinação das condições ótimas, um modelo rigoroso de coluna de destilação multicomponentes no estado estacionário é incluído no controlador preditivo para permitir o cálculo online do objetivo econômico. A trajetória prevista para o sistema de destilação até o ponto ótimo é calculada utilizando-se um modelo linear dinâmico, o qual foi obtido através de testes em degrau na planta real. O ponto ótimo obtido através da estratégia proposta leva em consideração as restrições nas entradas manipuladas e a faixa de controle para as saídas. O problema de otimização resultante para cálculo das ações de controle é uma QP, que pode ser facilmente resolvida com os solvers disponíveis. O MPC com otimização econômica foi implementado como um módulo do pacote SICON (Sistema de Controle da Petrobras). / This thesis was mainly aimed at the implementation of a new strategy for the integration of real time optimization (RTO) with multivariable predictive control in an industrial process system. The proposed strategy can be considered as a one-layer strategy where the control and economic optimization problems are solved simultaneously in the same layer of the control structure. Assuming that the economic objective to be maximized (minimized) is a concave (convex) function of the process inputs and outputs, the optimizing model predictive control (OMPC) was obtained through the inclusion of the reduced gradient of the economic objective in the control objective of the predictive controller. The approach was initially tested through the simulation of the reactorregenerator of a Fluid Catalytic Cracking Unit (FCCU). The optimizing controller has been successfully implemented in a toluene distillation column at the Aromatic Recovery Unit of the Cubatão refinery of Petrobras. This controller has been in continuous operation for about one year without any reported problem. For determining the optimum operating conditions, a steady-state rigorous multicomponent distillation model is included in the predictive controller to allow the on-line computation of the economic objective. The predicted trajectory of the distillation system towards the optimum point is computed with a linear dynamic model that was obtained through step tests in the real plant. The optimum point that is achieved with the proposed strategy takes into account the constraints in the manipulated inputs and the zone control of the outputs. The resulting optimization problem that produces the control actions is a QP that can be easily solved with available solvers. The optimizing MPC was implemented as a module of the SICON (Petrobras Control System) package.

The present research study is comprised of two main parts. The first part aims at the development of a systematic system-theoretic framework that allows the derivation of optimal chemotherapy protocols for HIV patients. The proposed framework is conceptually aligned with a notion of continuous-time model predictive control of nonlinear dynamical systems, and results in an optimal way to control viral replication, while maintaining low antiretroviral drug toxicity levels. This study is particularly important because it naturally integrates powerful system-theoretic techniques into a clinically challenging problem with worldwide implications, namely the one of developing chemotherapy patterns for HIV patients that are effective and do not induce adverse side-effects. The second part introduces a new digital controller design methodology for nonlinear (bio)chemical processes, that reflects contemporary necessities in the practical implementation of advanced process control strategies via digital computer-based algorithms. The proposed methodology relies on the derivation of an accurate sampled-data representation of the process, and the subsequent formulation and solution to a nonlinear digital controller synthesis problem. In particular, for the latter two distinct approaches are followed that are both based on the methodological principles of Lyapunov design and rely on a short-horizon model-based prediction and optimization of the rate of“energy dissipation" of the system, as it is realized through the time derivative of an appropriately selected Lyapunov function. First, the Lyapunov function is computed by solving the discrete Lyapunov matrix equation. In the second approach however, it is computed by solving a Zubov-like functional equation based on the system's drift vector field. Finally, two examples of a chemical and a biological reactor that both exhibit nonlinear behavior illustrate the main features of the proposed digital controller design method.

Le contrôle précis des boucles de régulation existantes sur une machine frigorifique est essentiel à son bon fonctionnement. Il existe plusieurs méthodes de régulation parmi lesquelles on retrouve la plus ancienne et la plus connue : la commande PID (Proportionnelle, Intégrale et Dérivée). Malgré la simplicité apparente des relations mises en jeu, le régulateur PID est assez délicat à ajuster sur des processus présentant de fortes perturbations comme les installations frigorifiques. L’objectif du travail présenté est de mettre en œuvre une commande prédictive fonctionnelle (PFC) afin de réguler la surchauffe en sortie d’évaporateur, la pression de condensation et la puissance frigorifique sur une installation munie d’un compresseur à vitesse variable. L’utilisation d’une commande PFC nécessite de réaliser une prédiction de l’évolution à venir de la sortie du procédé. C’est un modèle interne qui fait office de modèle de connaissance. En assimilant le procédé à un système du premier ordre, la mise en œuvre de cette commande ne nécessite que trois paramètres : un gain statique, une constante de temps et un retard pur. L’originalité de la démarche développée a consisté à réaliser une modélisation physique de la machine afin de déterminer les paramètres précédents par une approche macroscopique. Une bibliothèque de modèles physiques a été élaborée permettant de simuler le comportement de différents évaporateurs, condenseurs, compresseurs ou vannes de détente. La commande développée a ensuite été implantée sur un automate industriel programmable et des expériences ont été réalisées sur deux machines différentes. La première est constituée de deux échangeurs à tubes et calandre et d’un compresseur à pistons, alors que la seconde comprend un évaporateur à plaques, une batterie à ailettes et un compresseur à vis. / An accurate control of fluids flow is essential in any refrigeration system. As the conventional Proportional-Integral-Derivative (PID) control with invariable parameters can lead to unsatisfactory performance because of the variation of refrigeration unit parameters under disturbances, the aim of the work presented here is to develop a method for using Predictive Functional Control (PFC) to regulate the evaporator superheat, the condensing pressure and the cooling capacity on a variable-speed refrigeration system. Using a predictive controller requires to predic future change at the output of the process. This prediction is based on an internal model used as known model. By assuming that the behaviour of refrigerating machine heat exchangers can be represented using a first-order model, the implementation of PFC requires only three parameters: gain, time constant and time delay. In order to determine these parameters an original method has been developed which is based on the physical modelling of the machine. Physical models for different types of evaporator, condenser, compressor or expansion valve have been established to quantify heat transfer and refrigerant flow rate in these components. The control system created has been incorporated into an industrial programmable logic controller and used for experiments on two different refrigerating machines: the first one is composed of two shell and tube heat exchangers and a reciprocating compressor, whereas the second one is composed of a plate evaporator, a finned-tube condenser and a screw compressor. The tests performed show that PFC controller succeed in maintaining a precise chilled liquid temperature.

La problématique traitée dans cette thèse concerne la commande de robots manipulateurs à articulations flexibles. Les méthodes développées visent à satisfaire les spécifications de performance et de robustesse en suivi de trajectoire, ainsi qu’à assurer un niveau de sécurité compatible avec un scénario de fonctionnement interactif dans lequel l’homme et le robot partagent un même espace de travail. Seules les mesures moteur sont utilisées dans un contexte d’instrumentation réduite. Le premier objectif de performance de la commande de mouvement est atteint grâce à l’identification expérimentale d’un modèle flexible représentatif du système, et l’usage de ce modèle pour la synthèse de lois de commande avancées intégrées au sein d’une structure cascade. Deux approches complémentaires fondées d’une part sur la commande prédictive de type GPC (Generalized Predictive Control), et d’autre part sur la commande Hinfini, sont considérées pour la synthèse de lois de commande à deux degrés de liberté, prédictives et robustes. Les performances de ces deux approches sont analysées et évaluées expérimentalement. Le deuxième objectif de sécurité est abordé à travers un algorithme de détection de collisions du robot avec son environnement, sans capteur d’effort et en présence d’incertitudes de modélisation. Afin de séparer efficacement les effets dynamiques des collisions de ceux des erreurs de modélisation, une stratégie adaptative de filtrage et de décision tenant compte de l’état du système est proposée. La validation expérimentale montre une très bonne sensibilité de détection, compatible avec les normes et les recommandations de sécurité relatives à la robotique collaborative. / The present thesis addresses the problem of motion control of flexible-joint robot manipulators using motor sensors only. The global objective is to guarantee tracking performance and robustness with respect to modeling uncertainties, together with safe human-robot interaction in a collaborative scenario where the robot and the human operator share the same workspace. The first objective of performance is achieved through the experimental identification of a flexible model of the system and the use of this model for the design of advanced control laws implemented in a cascade structure. Two complementary approaches, based either on predictive (Generalized Predictive Control, GPC) or Hinfinity control frameworks, are considered to design predictive and robust two degrees-of-freedom controllers. Experimental evaluation and analysis of the proposed strategies is provided. The second objective of safety is addressed by a novel algorithm for human-robot collision detection, without force sensors and in the presence of modeling uncertainties. In order to efficiently separate the dynamic effects of the collisions from the effects due to modeling errors, the proposed approach includes adaptive filtering and uses dynamic thresholds depending on the robot state. Experimental evaluation demonstrates a good detection sensitivity which is consistent with safety standards and recommendations for collaborative robotics.

Cette thèse s’attache à la maximisation de la consommation du dioxyde de carbone par les microalgues. En effet, suite aux différentes problématiques environnementales actuelles liées principalement aux émissions importantes de gaz à effet de serre et notamment le CO2, il a été démontré que les microalgues jouent un rôle très prometteur pour la bio-fixation du CO2. Dans cette optique, nous nous intéressons à la mise en place d’une loi de commande robuste permettant de garantir des conditions opératoires optimales pour une culture de la microalgue Chlorella vulgaris dans un photobioréacteur instrumenté. Cette thèse repose sur trois axes principaux. Le premier porte sur la modélisation de la croissance de l’espèce algale choisie à partir d’un modèle mathématique traduisant l’influence de la lumière et de la concentration en carbone inorganique total. En vue de la commande, le deuxième axe est consacré à l’estimation de la concentration cellulaire à partir des mesures disponibles en temps réel du dioxyde de carbone dissous. Trois types d’observateurs ont été étudiés et comparés : filtre de Kalman étendu, observateur asymptotique et observateur par intervalles. Le dernier axe concerne l’implantation d’une loi de commande prédictive non-linéaire couplée à une stratégie d’estimation pour la régulation de la concentration cellulaire autour d’une valeur maximisant la consommation du CO2. Les performances et la robustesse de cette commande ont été validées en simulation et expérimentalement sur un photobioréacteur instrumenté à l’échelle de laboratoire. Cette thèse est une étude préliminaire pour la mise en œuvre de la maximisation de la fixation du dioxyde de carbone par les microalgues. / This thesis deals with the optimization of carbon dioxide consumption by microalgae. Indeed, following several current environmental issues primarily related to large emissions of CO2, it is shown that microalgae represent a very promising solution for CO2 mitigation. From this perspective, we are interested in the optimization strategy of CO2 consumption through the development of a robust control law. The main aim is to ensure optimal operating conditions for a Chlorella vulgaris culture in an instrumented photobioreactor. The thesis is based on three major axes. The first one concerns growth modeling of the selected species based on a mathematical model reflecting the influence of light and total inorganic carbon concentration. For the control context, the second axis is related to biomass estimation from the real-time measurement of dissolved carbon dioxide. This step is necessary for the control part due to the lack of affordable real-time sensors for this kind of measurement. Three observers structures have been studied and compared: an extended Kalman filter, an asymptotic observer and an interval observer. The last axis deals with the implementation of a non-linear predictive control law coupled to the estimation strategy for the regulation of the cellular concentration around a value which maximizes the CO2 consumption. Performance and robustness of this control law have been validated in simulation and experimentally on a laboratory-scale instrumented photobioreactor. This thesis represents a preliminary study for the optimization of CO2 mitigation strategy by microalgae.

La voiture autonome pourrait réduire le nombre de morts et de blessés sur les routes tout en améliorant l'efficacité du trafic. Cependant, afin d'assurer leur déploiement en masse sur les routes ouvertes au public, leur sécurité doit être garantie en toutes circonstances. Cette thèse traite de l'architecture de planification et de contrôle pour la conduite automatisée et défend l'idée que l'intention du véhicule doit correspondre aux actions réalisées afin de garantir la sécurité à tout moment. Pour cela, la faisabilité cinématique et dynamique de la trajectoire de référence doit être assurée. Sinon, le contrôleur, aveugle aux obstacles, n'est pas capable de la suivre, entraînant un danger pour la voiture elle-même et les autres usagers de la route. L'architecture proposée repose sur la commande à modèle prédictif fondée sur un modèle bicyclette cinématique afin de planifier des trajectoires de référence sûres. La faisabilité de la trajectoire de référence est assurée en ajoutant une contrainte dynamique sur l'angle au volant, contrainte issue de ces travaux, afin d'assurer que le modèle bicyclette cinématique reste valide. Plusieurs contrôleurs à haute-fréquence sont ensuite comparés afin de souligner leurs avantages et inconvénients. Enfin, quelques résultats préliminaires sur les contrôleurs à base de commande sans modèle et leur application au contrôle automobile sont présentés. En particulier, une méthode efficace pour ajuster les paramètres est proposée et implémentée avec succès sur la voiture expérimentale de l'ENSIAME en partenariat avec le laboratoire LAMIH de Valenciennes. / Autonomous vehicles are believed to reduce the number of deaths and casualties on the roads while improving the traffic efficiency. However, before their mass deployment on open public roads, their safety must be guaranteed at all time.Therefore, this thesis deals with the motion planning and control architecture for autonomous vehicles and claims that the intention of the vehicle must match with its actual actions. For that purpose, the kinematic and dynamic feasibility of the reference trajectory should be ensured. Otherwise, the controller which is blind to obstacles is unable to track it, setting the ego-vehicle and other traffic participants in jeopardy. The proposed architecture uses Model Predictive Control based on a kinematic bicycle model for planning safe reference trajectories. Its feasibility is ensured by adding a dynamic constraint on the steering angle which has been derived in this work in order to ensure the validity of the kinematic bicycle model. Several high-frequency controllers are then compared and their assets and drawbacks are highlighted. Finally, some preliminary work on model-free controllers and their application to automotive control are presented. In particular, an efficient tuning method is proposed and implemented successfully on the experimental vehicle of ENSIAME in collaboration with the laboratory LAMIH of Valenciennes.

A validação de modelos lineares é uma etapa importante em um projeto de Identificação de Sistemas, pois a escolha correta do modelo para representar a maior parte da dinâmica do processo, dentro de um número finito de técnicas de identificação e em torno de um ponto de operação, permite o sucesso no desenvolvimento de controladores preditivos e de controladores robustos. Por tal razão, o objetivo principal desta Tese é o desenvolvimento de um método de validação de modelos lineares, tendo como ferramentas de avaliação os métodos estatísticos, avaliações dinâmicas e análise da robustez do modelo. O componente principal do sistema de validação de modelos lineares proposto é o desenvolvimento de um sistema fuzzy para análise dos resultados obtidos pelas ferramentas utilizadas na etapa de validação. O projeto de Identificação de Sistemas é baseado em dados reais de operação de uma Planta-Piloto de Neutralização de pH, localizada no Laboratório de Controle de Processos Industriais da Escola Politécnica da USP. Para verificar o resultado da validação, todos os modelos são testados em um controlador preditivo do tipo QDMC (Quadratic Dynamic Matrix Control) para seguir uma trajetória de referência. Os critérios utilizados para avaliar o desempenho do controlador QDMC, para cada modelo utilizado, foram a velocidade de resposta do controlador e o índice da mínima variabilidade da variável de processo. Os resultados mostram que a confiabilidade do sistema de validação projetado para malhas com baixa e alta não-linearidade em um processo real, foram de 85,71% e 50%, respectivamente, com relação aos índices de desempenho obtidos pelo controlador QDMC. / Linear model validation is the most important stage in System Identification Project because, the model correct selection to represent the most of process dynamic allows the success in the development of predictive and robust controllers, within identification technique finite number and around the operation point. For this reason, the development of linear model validation methods is the main objective in this Thesis, taking as a tools of assessing the statistical, dynamic and robustness methods. Fuzzy system is the main component of model linear validation system proposed to analyze the results obtained by the tools used in validation stage. System Identification project is performed through operation real data of a pH neutralization pilot plant, located at the Industrial Process Control Laboratory, IPCL, of the Escola Politécnica of the University of São Paulo, Brazil. In order to verify the validation results, all modes are used in QDMC type predictive controller, to follow a set point tracking. The criterions used to assess the QDMC controller performance were the speed response and the process variable minimum variance index, for each model used. The results show that the validation system reliability were 85.71% and 50% projected for low and high non-linearity in a real process, respectively, linking to the performance indexes obtained by the QDMC controller.