Deposición de carbono en las superficies de películas delgadas de Fe sumergidas en tolueno en condiciones ambientales

Las nanoestructuras han sido muy estudiadas debido a su importancia en aplicaciones tecnológicas y biomédicas, como por ejemplo el recubrimiento de los sensores y biosensores. Estas necesitan ser recubiertas para su protección y/o funcionalización. Un estudio sobre las superficies de nanopartículas magnéticas y esféricas (MNPs) de Fe y Ni reveló que el tolueno actúa como catalizador de reacciones de condensación de los componentes aromáticos formando estructuras gigantes, policíclicas e irregulares, creando así una especie de recubrimiento de carbono. También se ha estudiado la posibilidad de formar recubrimientos con carbono en películas de hierro y permalloy (FeNi) en tiempos largos de tratamiento de 1 año. En el presente trabajo, debido a los resultados anteriores para las películas delgadas de hierro, se ha estudiado el desarrollo del proceso de deposición del grafeno defectuoso a temperatura ambiente, sobre las superficies de las películas delgadas de hierro en periodos de entre unos días hasta medio año aproximadamente. Se ha hecho un estudio en función del tiempo de inmersión en tolueno de las propiedades estructurales y magnéticas de las películas de hierro depositadas sobre vidrio. Las películas de hierro han sido preparadas por el método de pulverización catódica y después sumergidas en tolueno. Las técnicas utilizadas para la caracterización estructural han sido, la difracción de Rayos-X, los estudios de microscopia electrónica de barrido (SEM) y la perfilómetría. La caracterización magnética se ha hecho con un magnetómetro de Kerr (MOKE) y un magnetómetro vibrante (VSM). Las muestras cristalizaban en el sistema cúbico FCC del grupo espacial Fm-3m, con parámetro de celda de 3.5922Ǻ. El tamaño de dominio coherente para los índices de Miller (110) ha ido aumentando a lo largo del tratamiento. Para el índice de Miller (211) el tamaño de dominio coherente ha disminuido. Este comportamiento se explica tendiendo en cuenta el modelo propuesto en la literatura científica del proceso de formación de las estructuras de grafeno defectuoso. El análisis de las imágenes de SEM y los correspondientes datos de la emisión de Rayos-X han confirmado la presencia del carbono en la superficie. La cantidad del carbono en la superficie de las películas de hierro aumenta con el incremento del tiempo de inmersión en tolueno. Ha sido posible detectar la presencia del carbono en la superficie después de 9 días de inmersión (por lo tanto, el proceso de las estructuras policíclicas e irregulares es relativamente rápido). La deposición del carbono no resulta en una formación de estructura uniforme, así que cuanto más largo es el tratamiento, más complicadas son las estructuras. Como resultado del tratamiento superficial durante aproximadamente medio año, se observa un aumento de rugosidad de un micrómetro aproximadamente. La diferencia entre las medidas de MOKE y VSM para el campo coercitivo y la remanencia, se explica teniendo en cuenta el proceso de oxidación de la superficie y la interacción de algunas partes de la película de hierro con el tolueno, que pueden causar la relajación de las tensiones. La imanación de saturación obtenida para las películas después del tiempo de tratamiento de 135 días es de 192 emu por gramo. La disminución de la imanación de saturación es debida a la oxidación de las películas por el contacto con la atmósfera y el tolueno. En un cálculo aproximado se ha llegado a la conclusión que dicha capa tiene un espesor de 50 nm, repartida en dos capas de 25 nm. De todo lo anterior y de la base de análisis de las propiedades estructurales y magnéticas de las películas delgadas de hierro sumergidas en tolueno para hacer el tratamiento superficial a temperatura ambiente, se concluye, que las estructuras policíclicas e irregulares de grafeno defectuoso se forman relativamente rápido. El tratamiento con el tolueno no causa muchos cambios en la estructura y en las propiedades magnéticas, se trata de procesos superficiales. La modificación in situ de películas de hierro en tolueno, puede ser candidato a método de protección y funcionalización de los sensores magnéticos.

Mezclas y nanocompuestos de policaprolactona y resina fenoxi: caracterización, morfología y propiedades de transporte

La Tesis recoge un estudio experimental sobre mezclas y nanocompuestos de dos polímeros comerciales, ambos con peculiares capacidades a la hora de disgregar arcillas a nivel nanoscópico y de mezclarse con otros polímeros, lo que les hace particularmente atractivos a la hora de preparar masterbatches con altos contenidos en arcillas. Se han estudiado, entre otros efectos, el papel que las arcillas juegan en los fenómenos de cristalización de la policaprolactona y, sobre todo, en las propiedades de transporte de gases y vapores a través de los nanocompuestos obtenidos con las arcillas y los polímeros objeto de la Tesis. Con idénticos puntos de vista se han analizado mezclas binarias de ambos polímeros, incluyendo un estudio tentativo de uno de sus posibles nanocompuestos. Finalmente, se ha realizado un estudio de mezclas de policaprolactona con un polímero conductor, el polipirrol. En este caso, la cristalización del primero induce, con pequeñas cantidades del segundo, una red en éste que asegura una conductividad estimable y una mejora en las propiedades de transporte al dióxido de carbono.

Procesado, estructura y propiedades de materiales compuestos de matriz termoplástica y nanorefuerzos de carbono

208 p.

Plan de mejora ante los resultados del análisis de los hábitos deportivos y el sedentarismo en estudiantes de 12-13 años de los centros escolares Lauro Ikastola, Colegio Miribilla y Txorierri Ikastetxea

El presente estudio es una investigación llevada a cabo con chicos y chicas de entre 12 y 13 años sobre los hábitos deportivos y el sedentarismo. El estudio se ha llevado a cabo en 3 centros escolares vizcaínos diferentes: Lauro Ikastola (Loiu), Txorierri ikastetxea (Derio) y Colegio Miribilla (Bilbao) con el fin de abarcar y analizar una mayor heterogeneidad de alumnos. Hoy en día el sedentarismo infantil es un factor de ri esgo muy importante entre los más jóvenes y por ello es de vital importancia trabajar y proponer una serie de acciones y estrategias para incentivar a los adolescentes a llevar una vida activa y saludable.

Competitividad y fuga de carbono: el caso de la economía vasca

4 p.

Ingredientes de una transición sostenible hacia una ciudad baja en carbono

4 p.

Irakaskuntza Esperientzien Elkartrukerako Jardunaldiak IEEJ-13

[ES]En la Facultad de Informática de Donostia-San Sebastián siempre se ha podido encontrar interés por la renovación pedagógica. Los desarrollos conceptuales y tecnológicos que hemos experimentado en las últimas décadas en nuestra materia de estudio han llevado a continuos cambios en el diseño de contenidos y formas docentes. En el año 2010, en la Facultad de Informática, comenzábamos a dar forma a una iniciativa que perseguía, principalmente, promover la reflexión individual y grupal sobre nuestra docencia. La iniciativa fue liderada desde el equipo directivo del centro pero en todo momento se ha considerado que debe estar alimentada por la voluntad individual y colectiva de compromiso con un modelo docente compartido, generado desde la integración de propuestas y experiencias del propio profesorado de la facultad. A nuestro entender, la idea clave de este modelo es definir un marco de actuación capaz de integrar las individualidades pero que promueva la concepción de equipo en busca de la mejor formación de nuestros estudiantes. Durante este tiempo hemos organizado seminarios y jornadas en los que ha primado la formación colectiva en nuestro contexto, para promover la coordinación y colaboración. En esta ocasión, entendimos que podía ser el momento de abrir nuestras experiencias a otros centros de la UPV/EHU y, además, animarlos a que nos expusieran las suyas. Así han surgido las Jornadas de Intercambio de Experiencias Docentes, de las que este volumen recoge las ponencias presentadas. Las 21 ponencias presentadas, que provienen de 11 centros distintos de la UPV/EHU, son un reflejo del interés suscitado por la propuesta de estas jornadas. Los temas abordados en las ponencias van desde experiencias y reflexiones docentes en el uso metodologías activas, pasando por análisis de asuntos de organización y gestión, y tocando los trabajos de fin de grado, a experiencias novedosas de formación en alternancia con la empresa o experiencias promovidas por los propios estudiantes.

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.

Nanocomposites de Poliuretanos Elastoméricos y Nanotubos de Carbono Multipared

218p. -- Tesis con mención "Doctor europeus" realizada en el periodo de Octubre 2005-Mayo 2010, en el Grupo "Materiales+Tecnologías" (GMT).

Exploring new labelling strategies for boronated compounds: towards fast development and efficient assessment of BNCT drug candidates

208 p.

Órdenes generales del Cuerpo de Ejército nº XIV del Ejército del Norte, dadas entre los días 13 y 15 de agosto de 1937 y firmadas por el Jefe del estado Mayor Ernesto de la Fuente y los Comisarios generales Máximo Astiz y Cecilio Egaña

Orden nº 52 (13 de agosto). Unidad de instalación, Carpeta Rectorado G-12. 1 hoja. Orden nº 53 (15 de agosto). Unidad de instalación, Carpeta Rectorado G-13. 1 hoja. Mecanografiadas

Validación de métodos analíticos para la determinación de Amonio, Nitrato y Carbono Orgánico en aguas de estuario.

[es]El principal objetivo de este trabajo es la validación de métodos analíticos nuevos como son la determinación de amonio, nitrato y carbono orgánico total en muestras de aguas de estuario ya que no se han encontrado estudios para este tipo de muestras. A partir de este objetivo principal, se pretende, por un lado, comprobar la influencia de la diferente salinidad de las muestras en el desarrollo de métodos potenciométricos mediante ISE para la medida de nitrato y amonio y del equipo de TOC-VCSN para la determinación de carbono orgánico. Además, con la ayuda de cálculos estadísticos, determinar la incertidumbre asociada a la determinación de la concentración de amonio, nitrato y carbono orgánico en las muestras. Y, por último, analizar la posible variación de las muestras a lo largo del tiempo para comprobar su estabilidad.

Number of Players and Relative Pitch Area per Player: Comparing Their Influence on Heart Rate and Physical Demands in Under-12 and Under-13 Football Players

The aim of the present study is to analyse the influence of different large-sided games (LSGs) on the physical and physiological variables in under-12s (U12) and -13s (U13) soccer players. The effects of the combination of different number of players per team, 7, 9, and 11 (P7, P9, and P11, respectively) with three relative pitch areas, 100, 200, and 300 m(2) (A100, A200, and A300, respectively), were analysed in this study. The variables analysed were: 1) global indicator such as total distance (TD); work:rest ratio (W:R); player-load (PL) and maximal speed (V-max); 2) heart rate (HR) mean and time spent in different intensity zones of HR (<75%, 75-84%, 84-90% and >90%), and; 3) five absolute (<8, 8-13, 13-16 and >16 Km h(-1)) and three relative speed categories (<40%, 40-60% and >60% V-max). The results support the theory that a change in format (player number and pitch dimensions) affects no similarly in the two players categories. Although it can seem that U13 players are more demanded in this kind of LSG, when the work load is assessed from a relative point of view, great pitch dimensions and/or high number of player per team are involved in the training task to the U12 players. The results of this study could alert to the coaches to avoid some types of LSGs for the U12 players such as:P11 played in A100, A200 or A300, P9 played in A200 or A300 and P7 played in A300 due to that U13>U12 in several physical and physiological variables (W:R, time spent in 84-90% HRmax, distance in 8-13 and 13-16 Km h(-1) and time spent in 40-60% V-max). These results may help youth soccer coaches to plan the progressive introduction of LSGs so that task demands are adapted to the physiological and physical development of participants.