Diseño de un aerogenerador de muy baja potencia para la alimentación de sistemas eléctricos aislados

[ES]En este Proyecto se desarrolla el diseño y la optimización de un aerogenerador de muy pequeña potencia enfocado a alimentar sistemas eléctricos aislados; concretamente, un sistema de iluminación. Se analizan todos los componentes del sistema aerogenerador, comparando las diversas alternativas posibles y eligiendo soluciones sencillas, baratas y eficientes para cada uno de ellos. Asimismo, se lleva a cabo un primer dimensionamiento de los mismos. El esfuerzo de diseño se ha centrado en las palas, por considerarse el componente más crítico y menos normalizado. Se han estudiado herramientas para su análisis detallado y su optimización desde el punto de vista aerodinámico, y éstas han sido implementadas en Matlab. Esto ha permitido generar un diseño óptimo ajustado a las necesidades del sistema. Asimismo, se han realizado las correspondientes tareas de planificación, analizado los múltiples beneficios de tipo técnico, económico, social y ambiental que la ejecución del presente Proyecto reportará, haciendo una programación completa del mismo y un análisis de los costes que supondrá.

Caracterización térmica de sistemas de cobertura vegetal para edificios

[ES]La caracterización térmica de una fachada vegetal es una tarea difícil que requiere un nivel de certeza y predicción realista de modelos en situaciones exteriores dinámicas. El estudio teórico de elementos constructivos complejos no asemeja la realidad, por lo que para obtener la correcta caracterización es necesario ensayar dichos elementos y analizar los datos obtenidos. Para ello se utilizan las células de ensayo PASLINK y el entorno informático LORD. A través de ellos, se obtiene la transmitancia térmica dinámica de la fachada vegetal ensayada en condiciones exteriores reales.

Análisis comparativo de alternativas o soluciones de sistemas estructurales en acero y madera para marquesinas de aparcamiento

[ES]En este trabajo se hace un análisis y una comparación de las diferentes formas estructurales que puede adoptar una marquesina de aparcamiento, principalmente estructuras hechas en madera y acero. Para la realización del citado análisis se han valorado las ventajas y desventajas de los materiales, funcionalidad, mantenimiento, estética, dificultad de ejecución y economicidad, realizándose asimismo un diseño de marquesina utilizando uno u otro de los materiales citados. Para la ejecución de la marquesina, se formula un diseño que cumplimente los condicionantes de funcionalidad del elemento. A su vez, se analiza, parte por parte, todo el sistema estructural, empezando por determinar las acciones que van a aparecer y deberán ser transmitidas al terreno. Una vez obtenidos los esfuerzos que se han de transmitir, se formula una hipótesis de calidad del terreno de cimentación, con el fin de determinar las características de la cimentación. Previamente se realiza un predimensionado del sistema estructural, para cuyo cálculo se ha utilizado el programa informático Tricalc. Obtenidas las dimensiones exactas y los detalles constructivos para cada una de las opciones de materiales a analizar (madera y acero), se evalúa económicamente cada diseño obtenido, para determinar la solución más económica y rentable desde el punto de vista, por ejemplo del montaje y desmontaje, así como por el mantenimiento. Además de las funciones estructurales, también se analiza la adaptación al entorno de la madera y el acero.

Modelización de la propagación radioeléctrica en entornos indoor y outdoor aplicada a los sistemas de comunicaciones móviles

[ES]En este documento se tratará de recopilar toda la información y documentación que se ha buscado y desarrollado para la elaboración del proyecto que se está llevando a cabo. El objetivo final del mismo consiste en el análisis y estudio de los canales de propagación en entornos indoor y outdoor y su posterior comercialización en el mercado de las telecomunicaciones. Este documento recoge los aspectos necesarios para finalizar el proyecto con éxito, tales como planificación, alcance, beneficios del proyecto,presupuesto...

Estudio de la metodología para la medida de la exposición EM debida a sistemas LTE

[ES]En este documento se presenta el Trabajo Fin de Grado llevado a cabo con el objetivo de realizar el estudio de la metodología adecuada para medir la exposición electromagnética (EM) de sistemas LTE (Long Term Evolution). La exposición EM es un aspecto importante para la población, la cual es consciente de los potenciales efectos que pueden causar dichas radiaciones. Para alcanzar los objetivos de este trabajo, se ha analizado el estado del arte asociado a dicho sistema, con el fin de distinguir el comportamiento de la señal LTE y así, realizar el estudio de los parámetros relevantes en la configuración de los equipos. Se ha logrado definir una metodología que permite diferenciar adecuadamente los momentos de actividad y no actividad, observándose las franjas horarias asociadas. Además, empleando la metodología definida, se han realizado medidas de la exposición en la Escuela Técnica Superior de Ingeniería de Bilbao comparando los datos obtenidos con el nivel de referencia permitido para validar el cumplimiento de la normativa vigente.

Estructura y arquitectura de computadores : guía práctica para alumnos de primero y segundo curso de Grado en Ingeniería Informática de Gestión y Sistemas de Información

Grados recientes como el de Ingeniería Informática de Gestión y Sistemas de Información, y dada la orientación profesional que va a obtener el/la egresado/a para su incorporación en el mundo de la industria, requieren una revisión del enfoque de determinadas materias relativas a, por ejemplo, cómo está estructurado un computador, qué elementos lo conforman, cómo interactúan, etc.; dando al alumnado una visión amplia sin buscar la exhaustividad (propia de otras titulaciones) pero manteniendo un rigor tanto técnico como científico según la materia tratada.

Advanced Reaction Systems for Hydrogen Production

[EN] This PhD work started in March 2010 with the support of the University of the Basque Country (UPV/EHU) under the program named “Formación de Personal Investigador” at the Chemical and Environmental Engineering Department in the Faculty of Engineering of Bilbao. The major part of the Thesis work was carried out in the mentioned department, as a member of the Sustainable Process Engineering (SuPrEn) research group. In addition, this PhD Thesis includes the research work developed during a period of 6 months at the Institut für Mikrotechnik Mainz GmbH, IMM, in Germany. During the four years of the Thesis, conventional and microreactor systems were tested for several feedstocks renewable and non-renewable, gases and liquids through several reforming processes in order to produce hydrogen. For this purpose, new catalytic formulations which showed high activity, selectivity and stability were design. As a consequence, the PhD work performed allowed the publication of seven scientific articles in peer-reviewed journals. This PhD Thesis is divided into the following six chapters described below. The opportunity of this work is established on the basis of the transition period needed for moving from a petroleum based energy system to a renewable based new one. Consequently, the present global energy scenario was detailed in Chapter 1, and the role of hydrogen as a real alternative in the future energy system was justified based on several outlooks. Therefore, renewable and non-renewable hydrogen production routes were presented, explaining the corresponding benefits and drawbacks. Then, the raw materials used in this Thesis work were described and the most important issues regarding the processes and the characteristics of the catalytic formulations were explained. The introduction chapter finishes by introducing the concepts of decentralized production and process intensification with the use of microreactors. In addition, a small description of these innovative reaction systems and the benefits that entailed their use were also mentioned. In Chapter 2 the main objectives of this Thesis work are summarized. The development of advanced reaction systems for hydrogen rich mixtures production is the main objective. In addition, the use and comparison between two different reaction systems, (fixed bed reactor (FBR) and microreactor), the processing of renewable raw materials, the development of new, active, selective and stable catalytic formulations, and the optimization of the operating conditions were also established as additional partial objectives. Methane and natural gas (NG) steam reforming experimental results obtained when operated with microreactor and FBR systems are presented in Chapter 3. For these experiments nickel-based (Ni/Al2O3 and Ni/MgO) and noble metal-based (Pd/Al2O3 and Pt/Al2O3) catalysts were prepared by wet impregnation and their catalytic activity was measured at several temperatures, from 973 to 1073 K, different S/C ratios, from 1.0 to 2.0, and atmospheric pressure. The Weight Hourly Space Velocity (WHSV) was maintained constant in order to compare the catalytic activity in both reaction systems. The results obtained showed a better performance of the catalysts operating in microreactors. The Ni/MgO catalyst reached the highest hydrogen production yield at 1073 K and steam-to-carbon ratio (S/C) of 1.5 under Steam methane Reforming (SMR) conditions. In addition, this catalyst also showed good activity and stability under NG reforming at S/C=1.0 and 2.0. The Ni/Al2O3 catalyst also showed high activity and good stability and it was the catalyst reaching the highest methane conversion (72.9 %) and H2out/CH4in ratio (2.4) under SMR conditions at 1073 K and S/C=1.0. However, this catalyst suffered from deactivation when it was tested under NG reforming conditions. Regarding the activity measurements carried out with the noble metal-based catalysts in the microreactor systems, they suffered a very quick deactivation, probably because of the effects attributed to carbon deposition, which was detected by Scanning Electron Microscope (SEM). When the FBR was used no catalytic activity was measured with the catalysts under investigation, probably because they were operated at the same WHSV than the microreactors and these WHSVs were too high for FBR system. In Chapter 4 biogas reforming processes were studied. This chapter starts with an introduction explaining the properties of the biogas and the main production routes. Then, the experimental procedure carried out is detailed giving concrete information about the experimental set-up, defining the parameters measured, specifying the characteristics of the reactors used and describing the characterization techniques utilized. Each following section describes the results obtained from activity testing with the different catalysts prepared, which is subsequently summarized: Section 4.3: Biogas reforming processes using γ-Al2O3 based catalysts The activity results obtained by several Ni-based catalysts and a bimetallic Rh-Ni catalyst supported on magnesia or alumina modified with oxides like CeO2 and ZrO2 are presented in this section. In addition, an alumina-based commercial catalyst was tested in order to compare the activity results measured. Four different biogas reforming processes were studied using a FBR: dry reforming (DR), biogas steam reforming (BSR), biogas oxidative reforming (BOR) and tri-reforming (TR). For the BSR process different steam to carbon ratios (S/C) from 1.0 to 3.0, were tested. In the case of BOR process the oxygen-to-methane (O2/CH4) ratio was varied from 0.125 to 0.50. Finally, for TR processes different S/C ratios from 1.0 to 3.0, and O2/CH4 ratios of 0.25 and 0.50 were studied. Then, the catalysts which achieved high activity and stability were impregnated in a microreactor to explore the viability of process intensification. The operation with microreactors was carried out under the best experimental conditions measured in the FBR. In addition, the physicochemical characterization of the fresh and spent catalysts was carried out by Inductively Coupled Plasma Atomic Emission Spectroscopy (ICP-AES), N2 physisorption, H2 chemisorption, Temperature Programmed Reduction (TPR), SEM, X-ray Photoelectron Spectroscopy (XPS) and X-ray powder Diffraction (XRD). Operating with the FBR, conversions close to the ones predicted by thermodynamic calculations were obtained by most of the catalysts tested. The Rh-Ni/Ce-Al2O3 catalyst obtained the highest hydrogen production yield in DR. In BSR process, the Ni/Ce-Al2O3 catalyst achieved the best activity results operating at S/C=1.0. In the case of BOR process, the Ni/Ce-Zr-Al2O3 catalyst showed the highest reactants conversion values operating at O2/CH4=0.25. Finally, in the TR process the Rh-Ni/Ce-Al2O3 catalyst obtained the best results operating at S/C=1.0 and O2/CH4=0.25. Therefore, these three catalysts were selected to be coated onto microchannels in order to test its performance under BOR and TR processes conditions. Although the operation using microreactors was carried out under considerably higher WHSV, similar conversions and yields as the ones measured in FBR were measured. Furthermore, attending to other measurements like Turnover Frequency (TOF) and Hydrogen Productivity (PROD), the values calculated for the catalysts tested in microreactors were one order of magnitude higher. Thus, due to the low dispersion degree measured by H2-chemisorption, the Ni/Ce-Al2O3 catalyst reached the highest TOF and PROD values. Section 4.4: Biogas reforming processes using Zeolites L based catalysts In this section three type of L zeolites, with different morphology and size, were synthesized and used as catalyst support. Then, for each type of L zeolite three nickel monometallic and their homologous Rh-Ni bimetallic catalysts were prepared by the wetness impregnation method. These catalysts were tested using the FBR under DR process and different conditions of BSR (S/C ratio of 1.0 and 2.0), BOR (O2/CH4 ratio of 0.25 and 0.50) and TR processes (at S/C=1.0 and O2/CH4=0.25). The characterization of these catalysts was also carried out by using the same techniques mentioned in the previous section. Very high methane and carbon dioxide conversion values were measured for almost all the catalysts under investigation. The experimental results evidenced the better catalytic behavior of the bimetallic catalysts as compared to the monometallic ones. Comparing the catalysts behavior with regards to their morphology, for the BSR process the Disc catalysts were the most active ones at the lowest S/C ratio tested. On the contrary, the Cylindrical (30–60 nm) catalysts were more active under BOR conditions at O2/CH4=0.25 and TR processes. By the contrary, the Cylindrical (1–3 µm) catalysts showed the worst activity results for both processes. Section 4.5: Biogas reforming processes using Na+ and Cs+ doped Zeolites LTL based catalysts A method for the synthesis of Linde Type L (LTL) zeolite under microwave-assisted hydrothermal conditions and its behavior as a support for heterogeneously catalyzed hydrogen production is described in this section. Then, rhodium and nickel-based bimetallic catalysts were prepared in order to be tested by DR process and BOR process at O2/CH4=0.25. Moreover, the characterization of the catalysts under investigation was also carried out. Higher activities were achieved by the catalysts prepared from the non-doped zeolites, Rh-Ni/D and Rh-Ni/N, as compared to the ones supported on Na+ and Cs+ exchanged supports. However, the differences between them were not very significant. In addition, the Na+ and Cs+ incorporation affected mainly to the Disc catalysts. Comparing the results obtained by these catalysts with the ones studied in the section 4.4, in general worst results were achieved under DR conditions and almost the same results when operated under BOR conditions. In Chapter 5 the ethylene glycol (EG) as feed for syngas production by steam reforming (SR) and oxidative steam reforming (OSR) was studied by using microchannel reactors. The product composition was determined at a S/C of 4.0, reaction temperatures between 625°C and 725°C, atmospheric pressure and Volume Hourly Space Velocities (VHSV) between 100 and 300 NL/(gcath). This work was divided in two sections. The first one corresponds to the introduction of the main and most promising EG production routes. Then, the new experimental procedure is detailed and the information about the experimental set-up and the measured parameters is described. The characterization was carried out using the same techniques as for the previous chapter. Then, the next sections correspond to the catalytic activity and catalysts characterization results. Section 5.3: xRh-cm and xRh-np catalysts for ethylene glycol reforming Initially, catalysts with different rhodium loading, from 1.0 to 5.0 wt. %, and supported on α-Al2O3 were prepared by two different preparation methods (conventional impregnation and separate nanoparticle synthesis). Then, the catalysts were compared regarding their measured activity and selectivity, as well as the characterization results obtained before and after the activity tests carried out. The samples prepared by a conventional impregnation method showed generally higher activity compared to catalysts prepared from Rh nanoparticles. By-product formation of species such as acetaldehyde, ethane and ethylene was detected, regardless if oxygen was added to the feed or not. Among the catalysts tested, the 2.5Rh-cm catalyst was considered the best one. Section 5.4: 2.5Rh-cm catalyst support modification with CeO2 and La2O3 In this part of the Chapter 5, the catalyst showing the best performance in the previous section, the 2.5Rh-Al2O3 catalyst, was selected in order to be improved. Therefore, new Rh based catalysts were designed using α-Al2O3 and being modified this support with different contents of CeO2 or La2O3 oxides. All the catalysts containing additives showed complete conversion and selectivities close to the equilibrium in both SR and OSR processes. In addition, for these catalysts the concentrations measured for the C2H4, CH4, CH3CHO and C2H6 by-products were very low. Finally, the 2.5Rh-20Ce catalyst was selected according to its catalytic activity and characterization results in order to run a stability test, which lasted more than 115 hours under stable operation. The last chapter, Chapter 6, summarizes the main conclusions achieved throughout this Thesis work. Although very high reactant conversions and rich hydrogen mixtures were obtained using a fixed bed reaction system, the use of microreactors improves the key issues, heat and mass transfer limitations, through which the reforming reactions are intensified. Therefore, they seem to be a very interesting and promising alternative for process intensification and decentralized production for remote application.

Modelado de sistemas concurrentes con OMNeT++

El objetivo del siguiente proyecto es proporcionar una herramienta para estudiar el rendimiento de sistemas multiprocesador. Para ello estos sistemas serán previamente modelados como redes de Petri y simulados mediante el entorno de simulación de sistemas de eventos discretos OMNeT++.

Sistemas SCR y NSR-SCR para DeNOx en corrientes de escape diésel: Formulaciones, cinética y modelización

314 p.

La integración de los sistemas de gestión normalizados: un análisis de los principales estudios empíricos.

[ES]En la actualidad, muchas empresas organizan sus sistemas de gestión basándose en las normas y estándares internacionales (ISO 9000, ISO 14000, OHSAS 18000…). Considerando que todos ellos están soportados en unos principios comunes, las organizaciones tratan de aprovechar las sinergias existentes entre dichos sistemas buscando la mayor integración posible y la obtención de beneficios, tales como el ahorro de costes, la disminución de la burocracia o la mejora de la eficiencia. Por ello, el objetivo del presente trabajo es aportar una serie de recomendaciones que permitan a las empresas orientar la integración de sus sistemas de gestión de una manera sencilla y ágil.

Desarrollo de sistemas constructivos de aplicación al edificio industrial del futuro: su adaptabilidad a los sistemas de producción.

[EN]In this project are going to be defined some needs of the industry, now and in the future, and, then, an analysis of the solutions is going to be done, creating a small guide of design. Firstly, is going to be defined what the modern industry is and then, and using that definition, the needs of the new industry are going to be defined. Secondly, different examples of modern industrial buildings will be analyzed taking into account the needs of the industry previously defined. This project could help anyone to understand better the importance of the buildings in the new industry and how are them changing because the evolution of the containers is, at least, the evolution of the industry.

Arquitectura de Comunicaciones para Sistemas Ciber-Físicos Basada en OPC UA

[ES]Los sistemas Ciber-Físicos (Cyber-Physical Systems – CPS) son dispositivos que integran computación, control y comunicaciones. Actualmente se puede encontrar este tipo de sistemas en áreas tan diversas como la industria aeroespacial, automotriz, procesos químicos, infraestructura civil, etc. Entre las arquitecturas de comunicación empleadas en estos dispositivos, OPC UA se consolida como la más adecuada. OPC Unified Architecture es la nueva generación de tecnología propuesta por OPC Foundation para transmitir datos en bruto e información pre procesada entre los niveles de producción y los sistemas de planificación de producto de la empresa. Mediante OPC UA se puede disponer de toda la información deseada para cualquier aplicación y usuario autorizados, en cualquier instante y en cualquier lugar. En este proyecto se pretende desarrollar una arquitectura basada en OPC UA sobre CPSs para el acceso a datos de producción. Para ello se partirá de arquitecturas basadas en PC empotrados y redes de comunicación industriales.

Análisis de la influencia de los sistemas de puesta a tierra en la eficiencia de instalaciones eléctricas de baja tensión residenciales e industriales.

[EN]Nowadays, global society is more aware of electrical energy’s risks than never before, and electrical safety has turned a priority when a new installation is designed. So, a great protection to an unwanted electric hazard is required, being specially careful with indirect contacts. If a circuit has an insulation failure and an indirect contact is produced, there is risk of an accidental electrocution, risk that must be avoided by making a good choice of the grounding methodology and properly coordinating the electrical protections in the installation. In order to minimize that risk, a study of low voltage industrial and residential installation’s grounding methodologies is introduced, analyzing the tree grounding methodologies internationally accepted (TT, TN, IT). In addition, two real examples are solved (using a computer-aided engineering software), confirming the results of the theoretical study.

Efectos macroeconómicos de la progresividad en los sistemas de seguridad social: una aplicación al caso de los Estados Unidos

[ES] Este trabajo estudia los potenciales efectos macroeconómicos de una reforma que aumente la progresividad del sistema de Seguridad Social de los Estados Unidos de América. Condicionados por los supuestos del modelo, los resultados abogan por un aumento en el bienestar social con un determinado aumento de la progresividad. Esto es debido a que la redistribución total de la renta de los más pudientes a los que cuentan con menos recursos origina un contexto de menor bienestar social. Además, los resultados respaldan la validez del tipo de cotización como herramienta para ajustar el nivel de progresividad del sistema y rechazan la tasa de reemplazo de la pensión como mecanismo para conseguir dicho fin.