Aprendizaje Basado en Proyectos para la asignatura Ingeniería del Software

Duración (en horas): Más de 50 horas. Destinatario: Estudiante y Docente

Recursos de combustible en central nuclear de fusión en el País Vasco

[ES]Este trabajo surge de la inquietud del alumno sobre la energía nuclear y mas concretamente sobre la energía de fusión. Esta inquietud se plasma en una recopilación de información sobre los combustibles necesarios , su abundancia y su forma de obtención actual. Analizaremos la posibilidad de implantar alguna de estas plantas de combustible en el País Vasco, junto con un estudio de una posible central nuclear de fusión con la suma de la potencia de cada uno de los reactores de fisión que se encuentran actualmente en funcionamiento en el estado Español. Compararemos las cantidades de combustible necesarias en un año de uranio y el combustible de fusión, así como el coste de construcción de cada una.

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.

Manual práctico para la elaboración de proyectos en ingeniería civil

Este libro pretende ser un resumen de los apuntes utilizados en clase durante los últimos once años en la impartición de la asignatura de Proyectos, dentro de la antigua Ingeniería Técnica de Obras Públicas, que tras la implantación de Bolonia ha sido reemplazada por la de Ingeniería Civil. Tiene un enfoque eminentemente práctico; muchos de los apartados de este libro no son de obligado cumplimiento o imprescindibles de cara a ser incorporados a un proyecto de ingeniería civil. Pueden ser adaptados o presentados de un modo diferente, en algunos casos, e incluso son meras sugerencias, además de algunos ejemplos que se han incorporado. Estas páginas están enfocadas sobre todo a entender la documentación que forma un proyecto, de cara a que el alumno tenga claro cómo debe de plasmar todos los planos, cálculos e información que se genera a medida que avanzamos en el proyecto.

Optimization of the pyrolysis process for the production of a biomass derived reducing agent and hydrogen-rich gases

221 p.

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.

Hidrocraqueo de aromáticos ligeros a n-alcanos C2+. Variables de proceso y modelado cinético

323 p.

Proceso de pirólisis y reformado en línea para la producción de H2 a partir de residuos plásticos

266 p.

Máquinas de aprendizaje extremo para aplicaciones en ingeniería: implementaciones de alta velocidad sobre FPGAs

Los principales objetivos del presente trabajo son el estudio de las redes neuronales artificiales, los dispositivos reconfigurables de alta velocidad, como son las FPGAs, y su aplicación a un ejemplo concreto: el reconocimiento en tiempo real de diferentes tipos de suelo en imágenes de satélite. Con este fin se propone el diseño de una red neuronal y su implementación en un dispositivo de lógica programable usando el lenguaje de descripción del hardware VHDL (Very High Description Language). Otro de los objetivos del trabajo es conocer los entornos de desarrollo que los fabricantes de dispositivos de lógica programable ponen a disposición de los diseñadores y manejar herramientas de software matemático como Matlab.

Cursos semipresenciales y telepresenciales, con soporte on-line, de adaptación al grado de ingeniería de edificación para arquitectos técnicos

Sin índice de impacto (2010)

Asistencia técnica de ingeniería y diseño industrial. Adecuación de equipos y herramientas.

27 hojas : ilustraciones, planos.

Manipulación de la senescencia de alfalfa (Medicago sativa L.) por ingeniería genética

En plantas forrajeras como la alfalfa, la senescencia foliar produce tanto una pérdida de la biomasa de forraje como una reducción de la calidad del mismo. Una estrategia molecular para retrasar la senescencia mediante la ingeniería genética se basa en la expresión de la secuencia codificante de la isopentenil transferasa (ipt), enzima clave en la biosíntesis de citoquininas. Para lograrlo resulta crítico la utilización de promotores con expresión no constitutiva que permitan la producción sitio-específica y autorregulada de citoquininas. La manipulación de la senescencia constituye un objetivo particularmente atractivo en especies forrajeras. Se transformaron clones de alfalfa con las construcción AtMYB32-ipt, se logró la regeneración de 3 plantas transgénicas, las cuales fueron confirmadas por PCR al amplificar el transgen ipt. La expresión del transgen se confirmó por RT-PCR y a través de la técnica de Southern blot se observó un patrón de inserción múltiple. También se estableció el patrón de expresión de la construcción AtMYB32-gus, la cual se limitó a los tejidos vasculares, con cierta variabilidad de expresión en la parte aérea las plantas. Los fenotipos observados en las plantas AtMYB32-ipt fueron desde plantas normales a plantas que perdieron la dominancia apical con raíces necrosadas en su mayoría. Se evaluó la senescencia foliar a través de bioensayos de hojas de plantas que incorporaron el transgen ipt y plantas que no lo incorporaron, se observó una senescencia foliar retrasada en plantas transgénicas, se cuantificó dicho retraso a través de los contenidos de clorofila a y b, proteínas foliares totales y cambios en el perfil de las proteínas foliares en geles SDS-PAGE (subunidad mayor de Rubisco). Se observó a los 35 días un mayor contenido de clorofila a y b, proteínas foliares y una mayor intensidad de las bandas de la subunidad mayor de Rubisco en las plantas que incorporaron el transgen ipt

Estudio de una estrategia alternativa de ingeniería genética para incrementar la fijación biológica de nitrógeno atmosférico

Para satisfacer los altos rendimientos que impulsan la agricultura moderna la aplicación de fertilizantes nitrogenados ha sido fundamental. Dado que la base de la producción industrial de los fertilizantes químicos esta basado en el uso de combustibles fósiles, estos, actualmente, incrementan el costo económico debido a la disminución constante de las reservas de petróleo. Además, dada la baja eficiencia en el uso del fertilizante aplicado por parte de las plantas y el alto impacto ambiental debido a la emisión de óxido nitroso, resulta necesario emprender la búsqueda de nuevas estrategias para aumentar la concentración del nitrógeno fijado. Una de las propuestas para disminuir la aplicación de fertilizantes es el uso de microorganismos fijadores de nitrógeno; que ya son ampliamente utilizados en leguminosas por su capacidad de establecer asociaciones simbióticas; las cuales, lamentablemente, aún no han sido encontradas entre los principales cultivos de cereales. El objetivo del presente trabajo es la producción de una técnica de ingeniería genética que permita obtener bacterias fijadoras de nitrógeno recombinantes capaces de asociarse a distintos cultivos vegetales incrementando la productividad de los mismos. Para ello, los genes que sintetizan la nitrogenasa (nif), que están co-localizados en una isla genómica, en Pseudomonas stutzeri A1501 se transfirieron, vía el cósmido recombinante X940, a un promotor del crecimiento vegetal, Pseudomonas protegens Pf-5. La bacteria recombinante obtenida, P. protegens Pf-5 X940, fue capaz de crecer en medios de cultivo deficientes en nitrógeno o con el agregado de amonio; mostró una alta actividad nitrogenasa, liberando al medio de cultivo cantidades significativas de amonio y presentó expresión de los genes nif, sugiriendo que el proceso de fijación, en esta bacteria, es constitutivo. Las inoculaciones de especies vegetales (arabidopsis, alfalfa, festuca alta y maíz) con Pf-5 X940 aumentaron la concentración de amonio en el suelo y la productividad de las plantas en condiciones deficientes de nitrógeno. Estos resultados inician un nuevo camino hacia la producción efectiva de inoculantes recombinantes para la fijación de nitrógeno en un amplio rango de cultivos

Estudio de una estrategia alternativa de ingeniería genética para incrementar la fijación biológica de nitrógeno atmosférico

Para satisfacer los altos rendimientos que impulsan la agricultura moderna la aplicación de fertilizantes nitrogenados ha sido fundamental. Dado que la base de la producción industrial de los fertilizantes químicos esta basado en el uso de combustibles fósiles, estos, actualmente, incrementan el costo económico debido a la disminución constante de las reservas de petróleo. Además, dada la baja eficiencia en el uso del fertilizante aplicado por parte de las plantas y el alto impacto ambiental debido a la emisión de óxido nitroso, resulta necesario emprender la búsqueda de nuevas estrategias para aumentar la concentración del nitrógeno fijado. Una de las propuestas para disminuir la aplicación de fertilizantes es el uso de microorganismos fijadores de nitrógeno; que ya son ampliamente utilizados en leguminosas por su capacidad de establecer asociaciones simbióticas; las cuales, lamentablemente, aún no han sido encontradas entre los principales cultivos de cereales. El objetivo del presente trabajo es la producción de una técnica de ingeniería genética que permita obtener bacterias fijadoras de nitrógeno recombinantes capaces de asociarse a distintos cultivos vegetales incrementando la productividad de los mismos. Para ello, los genes que sintetizan la nitrogenasa (nif), que están co-localizados en una isla genómica, en Pseudomonas stutzeri A1501 se transfirieron, vía el cósmido recombinante X940, a un promotor del crecimiento vegetal, Pseudomonas protegens Pf-5. La bacteria recombinante obtenida, P. protegens Pf-5 X940, fue capaz de crecer en medios de cultivo deficientes en nitrógeno o con el agregado de amonio; mostró una alta actividad nitrogenasa, liberando al medio de cultivo cantidades significativas de amonio y presentó expresión de los genes nif, sugiriendo que el proceso de fijación, en esta bacteria, es constitutivo. Las inoculaciones de especies vegetales (arabidopsis, alfalfa, festuca alta y maíz)con Pf-5 X940 aumentaron la concentración de amonio en el suelo y la productividad de las plantas en condiciones deficientes de nitrógeno. Estos resultados inician un nuevo camino hacia la producción efectiva de inoculantes recombinantes para la fijación de nitrógeno en un amplio rango de cultivos