Hibridación de un remolcador portuario

Este TFG consiste en la comparación de dos sistemas de propulsión y generación eléctrica. El primero de ellos una propulsión diesel mecánica, el remolcador real; y el segundo una propulsión híbrida, el remolcador de estudio. Se hace la comparativa desde dos puntos de vista las emisiones de gases de escape y los consumos de combustible.

Leitura em meios virtuais: uma análise qualitativa do trabalho e desafios docentes

A presente pesquisa caracteriza-se como um estudo de caso com abordagem qualitativa de análise, tem caráter etnográfico e propôs dar continuidade à pesquisa de Guimarães (2008). Analisamos, na prática de sala de aula de um sujeito selecionado entre os participantes do estudo anterior, como ocorre o trabalho com leitura em E/LE em materiais retirados da Internet. Para isso, partimos dos seguintes questionamentos: (1) o que, para o professor, em sua prática, representa desenvolver atividades de leitura; (2) que tratamento recebem os textos oriundos do meio virtual e (3) como a prática, objetivos e base teórica deste professor se relacionam com a sua auto-imagem que aparece no questionário (Guimarães, 2008).Selecionamos o sujeito em função de sua alta adesão ao uso de recursos informáticos e sua proposta de ensino-aprendizagem de espanhol como língua estrangeira com base no desenvolvimento da compreensão leitora. Utilizamos como instrumentos de coleta de dados: o questionário da pesquisa de Guimarães (2008), os materiais utilizados pelo professor nas aulas observadas, as fontes originais virtuais dos textos presentes nesses materiais, o diário de campo do pesquisador, as gravações em áudio das aulas analisadas e a entrevista realizada com o informante. Nossa base teórica está fundamentada nos modelos de leitura, em especial o sócio-interacional, na caracterização da leitura em meio digital e no processo de transposição didática. Verificamos que o sujeito, baseado na teoria sócio-interacional, tem como foco de seu trabalho o desenvolvimento da habilidade leitora de seus alunos. Analisamos, também, as mudanças promovidas nos textos usados em sala de aula, em comparação às suas versões originais digitais. Discutimos que essas alterações podem trazer as consequências para o desenvolvimento da competência leitora e compreensão do texto por parte dos leitores-alunos, tanto no que se refere, especificamente, ao seu letramento digital como no processo leitor como um todo. Sobre a auto-imagem que o professor constrói através do questionário de Guimarães (2008), concluímos que, como apontado, o informante desenvolve um trabalho direcionado ao ensino de leitura em E/LE, assim como tem a internet como uma das principais fontes de materiais para suas aulas. Porém, a estrutura da instituição na qual atua o limita e altera as formas de trabalhar com textos e ferramentas virtuais, proporcionando uma mudança no perfil definido pelo questionário

Teatro y traducción (inglés-español). Análisis comparativo de traducciones comerciales. Who's Afraid of Virginia Woolf?

El presente trabajo se centra en un análisis comparativo en varios niveles de las traducciones producidas a partir de la obra teatral Who’s Afraid of Virginia Woolf? (Albee 1962): las de Marcelo De Ridder, José Méndez y Alberto Mira, realizadas con distintos fines y en momentos histórico culturales diferenciados. Asimismo hemos integrado en la comparación la adaptación cinematográfica y los correspondientes textos audiovisuales en inglés y en español, con el fin de ofrecer una visión más inclusiva del modo en que se ha generado esta cadena textual. Para manejar el mencionado corpus, nos hemos valido de herramientas informáticas. Por un lado, el programa TRACEAligner ha resultado de gran utilidad para alinear los textos teatrales. Por otro lado, SubRip ha posibilitado la extracción del subtitulado en inglés y en español del DVD, que después hemos organizado en una tabla bitextual. A través de una metodología fundamentada en estudios de investigación relevantes, hemos examinado el corpus desde una perspectiva extratextual, macroestructural, microestructural e intersistémica. Esto nos ha permitido interrelacionar las traducciones en aspectos tan importantes como los factores contextuales que afectan a su producción, las características de las publicaciones (o del libreto inédito), la transferencia de las unidades estructurales y argumentales, la correspondencia con rasgos de distintos tipos de traducciones, los fenómenos de traducción con mayor incidencia o las adaptaciones derivadas de los procesos de censura. Gracias a la comparación de estos temas, se pueden apreciar las características distintivas de cada texto. Otro asunto que se trata a lo largo del análisis es la identificación del texto fuente de cada traducción, especialmente de la de Méndez. Hemos tratado de demostrar que Méndez parte del texto norteamericano, no de la traducción de Ridder, como se ha sugerido (Espejo 1998: 111 112). Por último, recogemos una serie de conclusiones que pretenden verter luz sobre las cuestiones planteadas en la introducción.

Evolución geológica cuaternaria del valle del río Deba (Gipuzkoa)

196 p.

Análisis comparativo de traducciones comerciales en medios audiovisuales. Subtitulado I. “Hubble: 15 años de descubrimientos”

En este trabajo se realiza un estudio descriptivo-comparativo de la traducción de los subtítulos correspondientes al documental de divulgación científica titulado Hubble: 15 Years of Discovery (2005). Antes de realizar el análisis comparativo del corpus se sitúa la traducción comercial de este documento en el campo de estudio que abarca la traducción audiovisual, y en particular en el relativo a la subtitulación. El corpus textual seleccionado pertenece al género textual de la divulgación científica cuyas características se analizan. Tras abordar la cuestión de la selección del texto objeto de estudio, se detalla el proceso de recopilación del corpus, prestando especial atención a la elección del programa que se ha utilizado para la extracción de subtítulos a partir de la copia comercial del texto seleccionado (Hubble, 2005) en formato DVD. Se da cuenta de la compilación del corpus en forma de tabla que contiene el total de unidades bitextuales (subtítulos en inglés y español, identificados por los respectivos códigos de tiempo). El análisis del corpus bi-textual correspondiente a los subtítulos del documental (20 000 palabras, 715 SubtO y 724 SubtM), se efectúa mediante la clasificación de todos aquellos procedimientos de traducción observados. La taxonomía empleada para la clasificación de dichos procedimientos permite establecer cuatro grandes categorías: modulación, supresión, inequivalencia y adición. Dicha división cuatripartita da pie para establecer aquellas subcategorías que reflejan y ayudan a describir los procedimientos de traducción identificados en el proceso de análisis comparativo del corpus bitextual. Por razones de espacio, en la redacción final del presente trabajo se ofrece únicamente una muestra del conjunto total de ejemplos analizados para la realización de este estudio. Se pretende que dicha muestra represente por orden de incidencia, todos los fenómenos de traducción identificados y descritos, utilizando la taxonomía seleccionada, en el proceso de comparación del doblaje original inglés de Hubble y la traducción al español (subtítulos). Por último, se han recogido los datos relativos a la frecuencia de aparición de cada uno de los procedimientos de traducción para poder realizar una valoración global de los resultados obtenidos y relacionarlos con el género textual al que pertenece el documental objeto de estudio.

Spin-related phenomena in magnetic and spin-orbit couppled bose-einstein condensates

129 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.

Insatisfacción corporal y práctica de actividad física y deportiva en adolescentes de Gipuzkoa

238 p.

Charge and spin transport in graphene devices

170 p.

Proceso catalítico de transformación de dimetil éter en olefinas (DTO)

325 p.

La iluminación y la ventilación naturales en el edificio industrial: la solución al diseño del sistema estructural

[ES]El principal objetivo de este proyecto es analizar una serie de soluciones para la iluminación y la ventilación natural en el edificio industrial para realizar una comparación entre ellas. En lo que respecta a la elección de la mejor alternativa, se considerarán las ventajas y desventajas de cada una así como diversos factores externos, como su mantenimiento.

Cálculos de fatiga con tensiones aleatorias en trenes de aterrizaje de aeronaves.

[ES]Muchas de las piezas de vehículos trabajan bajo tensiones aleatorias, y por ello, es necesario tener en cuenta la fatiga por daño acumulativo de los materiales en el diseño. Sin embargo, no hay ningún método de cálculo específico en este ámbito, sino que se disponen de diferentes posibles elecciones, situación que incurre en la necesidad de una comparación entre ellos para tener cierto criterio de selección. Aportar ese criterio es la razón de ser de este informe, que se intentará corroborar con un análisis de una pieza de un tren de aterrizaje de una aeronave, bien por el tipo de cargas al que está sujeto cómo por la creciente importancia del sector aeronáutico en la industria en el cual el diseño tiene especial interés.

Surf oholeko gilen elementu finitu bidezko analisia.

[EU]Lan honetan, surf oholetan erabiltzen diren gila mota desberdinen analisia egin da. Horretarako, merkatuan garrantzi handiena duten bi enpresek euren katalogoetan eskaintzen dituzten modelo batzuk aztertu dira. Ingeniaritza simulazioak ahalbidetzen dituen ansys softwarea erabiliz egin da aukeratutako modeloen diseinu geometrikoa. Hauen analisiari ekin baino lehenago, gila hauetako bat aztertu da, hau osatzen duen materiala ezagutu eta ezaugarriak zehaztu asmoz. Aztertutakoa modelo guztiek erabiltzen duten ohiko materiala izanik, lortutako emaitzak baliogarriak dira gila guztiak aztertzeko. Materialaren propietateak ezagututa eta aipatutako softwareaz baliatuz, analisi estatikoa egin da. Horretarako, surfean aurkitzen diren ohiko egoera batzuk irudikatu dira, hauetan agertzen diren esfortzuak kalkulatuz. Gila bakoitzaren portaera, jasandako tentsio eta deformazioak aztertuz ondorioztatu da. Horrela, kasu bakoitzean komenigarrienak diren ezaugarriak oinarri hartuz, modelo desberdinen arteko konparaketa egin da.

Análisis comparativo de traducciones comerciales en medios audiovisuales. Subtitulado II. "El club de los poetas muertos".

El presente trabajo de fin de grado se centra en el estudio descriptivo-comparativo de los subtítulos en español y los de la versión original inglesa del largometraje cinematográfico El club de los poetas muertos (1989), además de sus correspondientes versiones dobladas. Una vez abordada la cuestión de la selección del material objeto de estudio, se trata el proceso de recopilación del corpus textual (23 000 palabras; 1800 subtítulos originales y 1633 en español), haciendo especial hincapié en las herramientas informáticas utilizadas para la extracción de los subtítulos, tanto originales como traducidos al castellano, desde una copia DVD. Posteriormente se ha organizado dicho corpus en una tabla, generando así unidades bitextuales comparables. Los resultados que se presentan en este TFG nacen del análisis y clasificación de los procedimientos de traducción observados tras la comparación de dichas unidades. Gracias a parte de la literatura utilizada para este trabajo (Merino 1986, Molina y Hurtado 2002 y Pajares 2010), se ha podido emplear una taxonomía que permitiera clasificar los fenómenos observados en cuatro grandes categorías: adición, inequivalencia, modificación y supresión. Dentro de cada categoría se han identificado diferentes subcategorías que se ajustan con mayor precisión a los fenómenos específicos identificados. Debido a las limitaciones de extensión del presente trabajo, el resultado final solo ofrece una muestra de todos los ejemplos recogidos, presentados por orden alfabético y atendiendo a la clasificación taxonómica fijada. En último lugar, las conclusiones pretenden verter luz a aquellas cuestiones planteadas en la introducción de este trabajo, así como presentar una valoración general de los resultados obtenidos.

Estudio de optimización de la línea de evacuación del parque eólico de la Sía.

[ES]Estudio de la capacidad de transporte de energía del Parque eólico de la Sía mediante la implementación de un método de cálculo variable(CIGRE)en contraposición a los métodos estáticos y constantes. Mediante la comparación y estudio de éstos se evaluará la posibilidad de ampliar la capacidad del parque.