554 resultados para Controladores robustos
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Tesis (Doctor en Ingeniería Eléctrica) U.A.N.L. Facultad de Ingeniería Mecánica y Eléctrica, 2008
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Tesis (Doctor en Ingeniería de Materiales) UANL, 2013.
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Os controladores programáveis tornaram-se fator decisivo para o controle de processos em ambientes industriais. Permitir o gerenciamento desses, eleva-os ao mesmo grupo de outros equipamentos da rede. Gerenciar esses dispositivos e o processo controlado tende a facilitar a identificação de falhas, as intervenções no processo e demais vantagens trazidas por um bom esquema de gerência. Uma maneira de realizar esse gerenciamento é por meio de programas conhecidos como supervisórios. Além das aplicações de supervisão, uma nova classe de ferramentas, que também possibilita o gerenciamento tanto do controlador quanto do processo a esse submetido, vem sendo disponibilizada. A presença de protocolos de gerenciamento, tal qual o SNMP, já é uma realidade em alguns dos modelos de equipamentos oferecidos por vários fabricantes, promovendo uma integração com plataformas de gerência já existentes no mercado. A proposta deste trabalho inclui a elaboração de um modelo de gerenciamento usando XML, atualmente em ampla ascensão e aceitação. Está, também, previsto a construção de um protótipo capaz de realizar as funções de um agente. A criação de um modelo de gerenciamento baseado em tecnologias e especificações abertas, tais como XML e Web, possibilita desde a utilização de um navegador, até o desenvolvimento de novas ferramentas para a requisição/aquisição de dados em controladores.
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A presente dissertação tem como objetivo estudar e aprimorar métodos de projetos de controladores para sistemas de potência, sendo que esse trabalho trata da estabilidade dinâmica de sistemas de potência e, portanto, do projeto de controladores amortecedores de oscilações eletromecânicas para esses sistemas. A escolha dos métodos aqui estudados foi orientada pelos requisitos que um estabilizador de sistemas de potência (ESP) deve ter, que são robustez, descentralização e coordenação. Sendo que alguns deles tiveram suas características aprimoradas para atender a esses requisitos. A abordagem dos métodos estudados foi restringida à análise no domínio tempo, pois a abordagem temporal facilita a modelagem das incertezas paramétricas, para atender ao requisito da robustez, e também permite a formulação do controle descentralizado de maneira simples. Além disso, a abordagem temporal permite a formulação do problema de projeto utilizando desigualdades matriciais lineares (LMI’s), as quais possuem como vantagem o fato do conjunto solução ser sempre convexo e a existência de algoritmos eficientes para o cálculo de sua solução. De fato, existem diversos pacotes computacionais desenvolvidos no mercado para o cálculo da solução de um problema de inequações matriciais lineares. Por esse motivo, os métodos de projeto para controladores de saída buscam sempre colocar o problema na forma de LMI’s, tendo em vista que ela garante a obtenção de solução, caso essa solução exista.
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A estrutura de propriedade anglo-saxônica, e o seu clássico problema de agência, com conflitos entre gestores e acionistas, caracterizados por propriedades pulverizadas, apesar de ser predominante na literatura, não constituí a regra, mas sim a exceção. O Brasil, diferentemente dos Estados Unidos e da Inglaterra, possuí uma estrutura de propriedade concentrada, onde é forte a presença de acionistas majoritários. Nesse caso, o conflito verificado não é entre gestores e acionistas (conflito agente X principal), mas sim entre acionistas majoritários e acionistas minoritários (conflito principal X principal). No mercado de capitais brasileiro, há duas classes de ações, as ordinárias (com direito a voto), e as preferências (sem direito a voto), o que viola a regra existente em muitos países, como nos Estados Unidos, de uma ação, um voto. Sendo assim, em muitos casos, ocorre uma combinação de muito poder com pouca alocação de recursos próprios na empresa. Diante disso, o presente estudo teve como objetivo estimar a magnitude dos direitos de votos, de fluxo de caixa, e do excesso de votos dos acionistas majoritários (das ações ordinárias) das empresas listadas no índice Bovespa – Ibovespa para os anos de 2009 e 2010 (carteira teórica do terceiro quadrimestre dos respectivos anos), separando-as por setor de atuação e por tipo de acionista majoritário. Para este estudo foi analisada uma amostra de 121 empresas, utilizando a metodologia quanto aos fins (descritiva e explicativa), e quanto aos meios (bibliográfica e documental). A coleta de dados foi feita no sistema Economática e nos IAN’s da CVM. Como resultados a pesquisa corroborou as hipóteses da literatura existente de que a estrutura de capital das empresas brasileiras de capital aberto é concentrada, principalmente no capital acionário (média de 51,95% e mediana de 51,20% em 2009, e 47,16% e 51,70% em 2010), e ocorrendo em vários casos uma distância considerável entre o poder de voto e o poder do fluxo de caixa dos acionistas majoritários (média de 1,10 em 2009 e mediana de 1,24, e 1,07 e 0,98 em 2010). Com isso, também se verifica que o conflito principal X principal é o predominante no Brasil.
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This work proposes an environment for programming programmable logic controllers applied to oil wells with BCP type method of artificially lifting. The environment will have an editor based in the diagram of sequential functions for programming of PLCs. This language was chosen due to the fact of being high-level and accepted by the international standard IEC 61131-3. The use of these control programs in real PLC will be possible with the use of an intermediate level of language based on XML specification PLCopen T6 XML. For the testing and validation of the control programs, an area should be available for viewing variables obtained through communication with a real PLC. Thus, the main contribution of this work is to develop a computational environment that allows: modeling, testing and validating the controls represented in SFC and applied in oil wells with BCP type method of artificially lifting
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This work presents a proposal to detect interface in atmospheric oil tanks by installing a differential pressure level transmitter to infer the oil-water interface. The main goal of this project is to maximize the quantity of free water that is delivered to the drainage line by controlling the interface. A Fuzzy Controller has been implemented by using the interface transmitter as the Process Variable. Two ladder routine was generated to perform the control. One routine was developed to calculate the error and error variation. The other was generate to develop the fuzzy controller itself. By using rules, the fuzzy controller uses these variables to set the output. The output is the position variation of the drainage valve. Although the ladder routine was implemented into an Allen Bradley PLC, Control Logix family it can be implemented into any brand of PLCs
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From their early days, Electrical Submergible Pumping (ESP) units have excelled in lifting much greater liquid rates than most of the other types of artificial lift and developed by good performance in wells with high BSW, in onshore and offshore environments. For all artificial lift system, the lifetime and frequency of interventions are of paramount importance, given the high costs of rigs and equipment, plus the losses coming from a halt in production. In search of a better life of the system comes the need to work with the same efficiency and security within the limits of their equipment, this implies the need for periodic adjustments, monitoring and control. How is increasing the prospect of minimizing direct human actions, these adjustments should be made increasingly via automation. The automated system not only provides a longer life, but also greater control over the production of the well. The controller is the brain of most automation systems, it is inserted the logic and strategies in the work process in order to get you to work efficiently. So great is the importance of controlling for any automation system is expected that, with better understanding of ESP system and the development of research, many controllers will be proposed for this method of artificial lift. Once a controller is proposed, it must be tested and validated before they take it as efficient and functional. The use of a producing well or a test well could favor the completion of testing, but with the serious risk that flaws in the design of the controller were to cause damage to oil well equipment, many of them expensive. Given this reality, the main objective of the present work is to present an environment for evaluation of fuzzy controllers for wells equipped with ESP system, using a computer simulator representing a virtual oil well, a software design fuzzy controllers and a PLC. The use of the proposed environment will enable a reduction in time required for testing and adjustments to the controller and evaluated a rapid diagnosis of their efficiency and effectiveness. The control algorithms are implemented in both high-level language, through the controller design software, such as specific language for programming PLCs, Ladder Diagram language.
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This work addresses issues related to analysis and development of multivariable predictive controllers based on bilinear multi-models. Linear Generalized Predictive Control (GPC) monovariable and multivariable is shown, and highlighted its properties, key features and applications in industry. Bilinear GPC, the basis for the development of this thesis, is presented by the time-step quasilinearization approach. Some results are presented using this controller in order to show its best performance when compared to linear GPC, since the bilinear models represent better the dynamics of certain processes. Time-step quasilinearization, due to the fact that it is an approximation, causes a prediction error, which limits the performance of this controller when prediction horizon increases. Due to its prediction error, Bilinear GPC with iterative compensation is shown in order to minimize this error, seeking a better performance than the classic Bilinear GPC. Results of iterative compensation algorithm are shown. The use of multi-model is discussed in this thesis, in order to correct the deficiency of controllers based on single model, when they are applied in cases with large operation ranges. Methods of measuring the distance between models, also called metrics, are the main contribution of this thesis. Several application results in simulated distillation columns, which are close enough to actual behaviour of them, are made, and the results have shown satisfactory
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Due of industrial informatics several attempts have been done to develop notations and semantics, which are used for classifying and describing different kind of system behavior, particularly in the modeling phase. Such attempts provide the infrastructure to resolve some real problems of engineering and construct practical systems that aim at, mainly, to increase the productivity, quality, and security of the process. Despite the many studies that have attempted to develop friendly methods for industrial controller programming, they are still programmed by conventional trial-and-error methods and, in practice, there is little written documentation on these systems. The ideal solution would be to use a computational environment that allows industrial engineers to implement the system using high-level language and that follows international standards. Accordingly, this work proposes a methodology for plant and control modelling of the discrete event systems that include sequential, parallel and timed operations, using a formalism based on Statecharts, denominated Basic Statechart (BSC). The methodology also permits automatic procedures to validate and implement these systems. To validate our methodology, we presented two case studies with typical examples of the manufacturing sector. The first example shows a sequential control for a tagged machine, which is used to illustrated dependences between the devices of the plant. In the second example, we discuss more than one strategy for controlling a manufacturing cell. The model with no control has 72 states (distinct configurations) and, the model with sequential control generated 20 different states, but they only act in 8 distinct configurations. The model with parallel control generated 210 different states, but these 210 configurations act only in 26 distinct configurations, therefore, one strategy control less restrictive than previous. Lastly, we presented one example for highlight the modular characteristic of our methodology, which it is very important to maintenance of applications. In this example, the sensors for identifying pieces in the plant were removed. So, changes in the control model are needed to transmit the information of the input buffer sensor to the others positions of the cell
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On this paper, it is made a comparative analysis among a controller fuzzy coupled to a PID neural adjusted by an AGwith several traditional control techniques, all of them applied in a system of tanks (I model of 2nd order non lineal). With the objective of making possible the techniques involved in the comparative analysis and to validate the control to be compared, simulations were accomplished of some control techniques (conventional PID adjusted by GA, Neural PID (PIDN) adjusted by GA, Fuzzy PI, two Fuzzy attached to a PID Neural adjusted by GA and Fuzzy MISO (3 inputs) attached to a PIDN adjusted by GA) to have some comparative effects with the considered controller. After doing, all the tests, some control structures were elected from all the tested techniques on the simulating stage (conventional PID adjusted by GA, Fuzzy PI, two Fuzzy attached to a PIDN adjusted by GA and Fuzzy MISO (3 inputs) attached to a PIDN adjusted by GA), to be implemented at the real system of tanks. These two kinds of operation, both the simulated and the real, were very important to achieve a solid basement in order to establish the comparisons and the possible validations show by the results
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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior