Abstention, null and blank votes in the Basque Autonomous Community

The objectives of this essay are twofold. First it reviews the reason for abstaining (or casting a null or blank vote) in elections. It also provides the data of abstention in the elections to the European Parliament. Fewer data are available on blank and null votes. These are provided for some countries. The second objective is to analyze the data of the elections in the Basque Autonomous Community since 1977. The evolution through time is commented. The main features are the low participation in the European elections on the one hand and the importance of the null vote in the 2003-2009 period.

Abstention, null and blank votes in the Basque Autonomous Community

The objectives of this essay are twofold. First it reviews the reason for abstaining (or casting a null or blank vote) in elections. It also provides the data of abstention in the elections to the European Parliament. Fewer data are available on blank and null votes. These are provided for some countries. The second objective is to analyze the data of the elections in the Basque Autonomous Community since 1977. The evolution through time is commented. The main features are the low participation in the European elections on the one hand and the importance of the null vote in the 2003-2009 period.

Análisis del mercado eléctrico en Escandinavia: NORD POOL

La electricidad es un elemento muy importante para la sociedad y cada vez se depende más para la vida moderna y el trabajo. Como consecuencia, el consumo de electricidad ha crecido año a año y por lo tanto, la producción también ha aumentado. Esto ha provocado que los países estén interconectados entre sí para poder satisfacer la demanda de electricidad. Esta situación ha llevado a la formación del mayor mercado a nivel global de intercambio de electricidad. Este trabajo tiene como objetivo analizar el mercado eléctrico de los países de Noruega, Suecia, Finlandia y Dinamarca y el análisis de los precios de la electricidad. Los resultados sugieren que los precios de la electricidad son muy volátiles, es por ello que en invierno la media de los precios es más alta y en verano es más baja.

Análisis del mercado eléctrico en Escandinavia: NORD POOL

La electricidad es un elemento muy importante para la sociedad y cada vez se depende más para la vida moderna y el trabajo. Como consecuencia, el consumo de electricidad ha crecido año a año y por lo tanto, la producción también ha aumentado. Esto ha provocado que los países estén interconectados entre sí para poder satisfacer la demanda de electricidad. Esta situación ha llevado a la formación del mayor mercado a nivel global de intercambio de electricidad. Este trabajo tiene como objetivo analizar el mercado eléctrico de los países de Noruega, Suecia, Finlandia y Dinamarca y el análisis de los precios de la electricidad. Los resultados sugieren que los precios de la electricidad son muy volátiles, es por ello que en invierno la media de los precios es más alta y en verano es más baja.

Vivienda energeticamente sostenible ubicada en Xàtiva.

[ES]Se van a diseñar las instalaciones necesarias para que una vivienda unifamiliar sea energeticamente sostenible. La unica fuente disponible es la solar y los paneles se van a encargar de convertir la energia disponible para los usuarios.La documentación del presente Proyecto de Ejecución de la instalación fotovoltaica en vivienda aislada, tanto gráfica como escrita, se redacta para establecer todos los datos descriptivos, urbanísticos y técnicos, para conseguir llevar a buen término, la instalación fotovoltaica de una vivienda unifamiliar aislada, según el reglamento eléctrico de baja tensión.

Modelización acústica del interior de un Tren de Alta Velocidad

[ES]El presente Trabajo de Fin de Grado, titulado ‘Modelización Acústica del Interior de un Tren de Alta Velocidad’, tiene como objetivo el análisis acústico a bajas frecuencias del habitáculo de un coche de un tren de alta velocidad. La temática ha sido elegida debido a la creciente presencia de trenes de alta velocidad en nuestro entorno, en los cuales el Control Acústico o de Ruidos es un aspecto muy importante para el confort del medio de transporte. Dentro de los ruidos por los que se ve afectado el tren, los de baja frecuencia son los más difíciles de tratar y controlar, y es por ello que van a constituir la línea de trabajo de este proyecto. La estructura de lo que se va a tratar en este proyecto es la siguiente: En primer lugar, se analizará el contexto en que se encuadra este proyecto y las razones que han llevado a su realización. Posteriormente, se explicarán los fundamentos teóricos que hay detrás de los análisis que se van a realizar. Más adelante se pasará al análisis del caso práctico que se ha elegido para ilustrar el proyecto: el habitáculo de un coche del tren Serie 120 de Renfe, construido por CAF [1, 2, 3]. Se realizarán tanto análisis modales como de respuesta forzada. Dicho ejemplo servirá de base para asentar las conclusiones y proponer la aplicación que se les puede dar a éstas, así como las líneas de investigación para las cuales este proyecto puede ser un punto de partida.

Design and evaluation of an optical switching node

[EN]For a good development of elastic optical networks, the design of flexible optical switching nodes is required. This work analyses the previously proposed flexible architectures and, based on the most appropriate, which is the Architecture on Demand (AoD), proposes a specific configuration of the node that includes spatial and spectral switching and the wavelength conversion functionality with a low blocking probability and the minimum amount of modules; the characteristics of the traffic that the designed node is able to cope with are specified in the last chapter. An evaluation of the designed node is also done, and, compared to the other architectures, it is shown that the Architecture on Demand gives better results than others and that it has a higher potential for future developments.

Producción de hidrogeno a partir de plasticos mediante pirólisis y reformado catalítico en línea

Los plásticos proporcionan claros beneficios a la sociedad, es un material de innegable utilidad presente en infinidad de productos de uso cotidiano . No obstante, p ese a no ser considerados resi duos peligrosos, los res i duos plásticos representan un problema ambiental global de creciente preocupación ya que la cultura del uso y desecho que prevalece hoy en día hac e que la generación de res i duos ocurra de manera masiva y conti nua . Además, e l plástico es un material inorgánico que tiene alta durabilidad. Se calcula que puede tardar entre 100 y 1000 años en degradarse d ependiendo del tipo de plástico, lo que supone que no se reincorpore fácilmente a los ciclos naturales, permaneciendo por largos periodos y afectando de diferentes maneras los lugares donde queda dispuesto. Por lo tanto, los impactos ambientales son acumulativos, de largo plazo y lejanos. El interés de reciclar los plá sticos surge por la necesidad de eliminar su dep ó sito en vertederos, donde dada su baja degradabilidad solo originan problemas medioambientales y de deterioro del paisaje. A nivel mundial , el principal impacto ambiental de los res i duos p lásticos es la contaminación de los océanos y mares. Es un impacto acumulativo que se presenta a largo plazo y cubre gran cantidad de espacios de todo el planeta. Se han encontrado cantidades substanciales de residuos contaminando los hábitats marinos desde los polos hasta el ecuador, desde costas remotas inhabitadas hasta costas altamente pobladas y áreas profundas del océano (Barnes y cols., 2009 ) . El bajo peso del plástico, que es una ventaja en las etapas de distri bución y consumo del producto plástico, se convierte en una problemática ambiental cuando los residuos plásticos navegan por corrientes subterráneas, ríos, mares y océanos.

Producción de hidrógeno por reformado catalítico en fase acuosa de disoluciones de metanol. Catalizador de Platino.

El objetivo que persigue la línea de investigación en la que se engloba este trabajo es la obtención de hidrógeno desde disoluciones acuosas de metanol (aproximadamente del 10% de metanol), considerando estos compuestos como una forma de almacenar hidrógeno y obtenerlo a baja temperatura “on-board” en un vehículo mediante el reformado en fase acuosa. El reto es conseguir un sistema catalítico de pequeño volumen y rápida respuesta a las demandas de hidrógeno con elevado rendimiento y calidad apropiada (<10 ppm de CO) para las pilas de combustible PEM. Los objetivos planteados en el siguiente trabajo se centran en la preparación y caracterización de un catalizador de platino soportado en alúmina, y la puesta en marcha de un reactor discontinuo de mezcla perfecta a presión para la evaluación de catalizadores en el proceso de reformado en fase líquida.

La diversidad de los modelos de participación laboral de las mujeres en la UE-27

[ESP] El objetivo de este artículo es relacionar las características de la inserción laboral femenina con su grado de participación en el mercado laboral en los países de la Unión Europea a través de los datos proporcionados por Eurostat. Nos interesa conocer si una mayor participación laboral entre las mujeres va aparejada con un modelo laboral “femenino”, esto es, con empleos a tiempo parcial, temporales, de baja remuneración y en determinados sectores y ocupaciones. O si por el contrario, en los países en los cuales la tasa de empleo femenina es elevada y hay menor brecha con respecto a la de los hombres, el modelo de inserción laboral de mujeres y hombres es similar. La diversidad de los mercados de trabajo y también de las políticas públicas y de las estructuras productivas en un área tan amplia como al UE27, nos impide establecer modelos de inserción laboral femenina claros, aunque sí hemos podido apuntar rasgos comunes con respecto a las desigualdades de género entre países.

Posibles conflictos éticos entre los paradigmas científico-tecnológicos dominantes y la mejora del bienestar de la población en algunas economías emergentes

En los últimos años, algunos países emergentes como China, India y Brasil, han experimentado importantes avances en el área de la innovación científicotecnológica. En este artículo se realiza una primera aproximación a los dilemas éticos que se plantean entre los diversos paradigmas-científico tecnológicos y la mejora del bienestar de la población en estos países. Se evalúan los diversos tipos de conocimiento (patentes y derechos de propiedad intelectual, conocimiento tradicional, innovaciones de base social e innovaciones inclusivas) en función de criterios que tienen que ver con su base local, los objetivos que persiguen y los valores relacionados con esos objetivos. Para los países de renta media y baja, las innovaciones de base social y las innovaciones inclusivas podrían favorecer en mayor medida la mejora del bienestar de sus poblaciones.

Estudio sobre las relaciones entre la percepción de competencia, el estado de ánimo y la tolerancia al estrés en jóvenes deportistas en formación

247 p.

Avances en el modelado de la combustión de biomasa en spouted bed cónico

290 p.

Modelization and analysis of the electric arc in low voltage circuit breakers

246 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.