Generoaren Trataera Ikonografikoa eta Idatzikoa “Urtxintxa 4 Urte” Testuliburuan

Gradu amaierako lan honetan, “Utxintxa 4 urte” testuliburuaren azterketa egin da. Ikerketaren helburua: generoaren trataera ikertzea testuliburuko ikonografian eta idatzizkoan. Alde batetik, Haur Hezkuntzako testuliburuetan, emakumeen eta gizonezkoen arteko berdintasunari erreparatu zaio. Eta, horretarako, marrazkiak, argazkiak eta bertan agerturiko testu idatziak izan dira kontuan hartuak, besteak beste, emakumezkoen eta gizonezkoen presentzia eta maiztasuna, pertsona eta pertsonaien garrantzia eta orrialde mistoen agerpena. Bestetik, testuliburuan agertzen diren lanbideei dagokienez, emakumeen eta gizonen arteko berdintasuna, lanbide motak eta lan eremua aztertu dira. Azkenik, generoari loturiko testua ikertu da. Horiek horrela, haurren ikasketa prozesuan testuliburuek daukaten garrantzia kontuan hartuta, nabarmendu da, eta nahitaezkoa ikusten da, batetik, edukien eta balioen eguneratzea eta, bestetik, aldaketarako urratsak ematea, testuliburuen bidez sexu bazterketarik eman ez dadin.

Tertulias literarias dialógicas: apostando por las estrategias educativas de éxito

[spa] Este trabajo se centra en las tertulias literarias dialógicas calificadas como prácticas educativas de éxito para fomentar la inclusión y la transformación social desde el sistema escolar. Contextualizando estas actividades dentro de la educación inclusiva y abordando los principios del aprendizaje dialógico, se analiza la metodología de las mismas para presentar una propuesta de intervención en el CEP Juan Bautista Zabala. Todo ello con el objetivo de implementar esta estrategia exitosa y evaluar la actividad desde la perspectiva de la metodología comunicativa crítica, es decir, otorgando especial relevancia a las opiniones de los protagonistas sobre la experiencia vivida.

Análisis de una metodología para el estudio de los textos del periodismo de investigación.

493 p.

Ingredientes de una transición sostenible hacia una ciudad baja en carbono

4 p.

La cerámica de la Segunda Edad del Hierro en el País Vasco: Estudio tecnológico, funcional y social

670 p. Capítulos de introducción, metodología, discusión y conclusiones en castellano e inglés.

Informazio-iturrien garrantzia berrikuntza teknologikoko jardueretarako

[EU]Gaur egunean bizi dugun krisi ekonomiko, produkzio ereduen transformazio eta globalizazioko testuinguruan, ikerketa, garapena eta berrikuntza (I+G+b) ezinbesteko faktoreak bilakatu dira herrialdeen hazkunde eta enpresen lidergo zein biziraupenerako. Berritasunaren bilatze horretan, egungo merkatuan enpresek etengabe egin beharreko egokitzapen teknologikoak direla eta, berrikuntza teknologikoak, hau da, produktuan edo prozesuan berritzeak, berebiziko garrantzia du. Gainera, oro har, lehiakortasunik ez galtzeko informazio estrategikoaren jabe izatea enpresentzat funtsezkoa bada ere, berrikuntza jarduerak aurrera eramateko oraindik ere gailentasun handiagoa dauka. Informazio estrategikoa iturri ezberdinetatik jaso daiteke eta horietako bakoitzari ematen zaion garrantzia ezberdina da. Lan honen helburua erlazio hori aztertzearena izanik, ondoriozta dezakegu, alde batetik, produktuan zein prozesuan berritzen duten enpresek, berrikuntza teknologikoak aurrera eramateko garaian, enpresa barnetik jasotako informazioari ematen diotela garrantzi gehien. Eta bestaldetik, instituzio publikoetatik, hau da, unibertsitate edo goi-ikasketetako zentroetatik, ikerketako erakunde publikoetatik edota zentro teknologikoetatik jasotako informazioari garrantzi gutxi ematen zaiola.

Diseño y desarrollo de un sistema de comunicaciones integrales para ambulancias en redes de nueva generación

[ES]En este proyecto se diseña y se desarrolla todo lo necesario para la realización y el establecimiento de un sistema de comunicaciones integrales para ambulancias haciendo uso de redes de nueva generación, siguiendo la estructura de NGN (Next Generation Networking). Con este fin, se analiza en profundidad el funcionamiento habitual de las ambulancias y su metodología en el uso de los medios de comunicación actuales. De esta manera, el sistema se desarrollará cumpliendo todas las características de los medios de comunicación de emergencias actuales y supliendo las deficiencias de estos, siendo de relevancia todas las comunicaciones multimedia

La transparencia en la emisión de información de las entidades sin fines de lucro: hacia un modelo de indicadores

527 p.

Una aproximación al sector eléctrico

Español:Este TFG pretende exponer de un modo sencillo el mercado eléctrico español. Se trata de un tema de elevada complejidad y gran extensión. Con el fin de alcanzar una idea clara, hemos decidido centrarnos en los puntos de mayor relevancia. En las secciones siguientes abordamos cuestiones relativas al mercado mayorista (pool) y minorista español así como la incipiente reforma eléctrica llevada a cabo por el Gobierno. Después de una breve Introducción, la sección 2 enumera una serie de términos que se utilizan con frecuencia en esta área. La sección 3 proporciona algunos antecedentes sobre el sector eléctrico. La sección 4 se refiere al mercado mayorista, en el cual se realiza la compra-venta diaria de electricidad. En él participan los productores, los distribuidores y los comercializadores de electricidad, así como los consumidores cualificados de energía eléctrica. Dentro de éste nos encontramos el mercado a plazo (o forward), el mercado diario (o spot) y el mercado a corto plazo (o de ajuste). La sección 5 trata del mercado minorista, su diseño y composición. Aquí, las empresas encargadas de comercializar energía (que compran en el mercado mayorista a las empresas generadoras) se la venden a los consumidores finales. En la sección 6 se aborda la Reforma Eléctrica, aclarando los cambios sufridos desde su implantación. Los hechos más llamativos a este respecto son: la eliminación de las subastas CESUR y el cambio de la Tarifa de Último Recurso (TUR) a un Precio Voluntario para el Pequeño Consumidor (PVPC). Por último, hay una sección final con las principales conclusiones.

Estrategias de Internacionalización en el sector hotelero: Estudio de casos

Este Trabajo de Fin de Grado se centra en el análisis de las principales estrategias de internacionalización de las dos cadenas hoteleras de mayor relevancia a nivel nacional: Meliá Hotels International y NH Hotel Group. Tras comenzar con un pequeño marco conceptual basado en la revisión bibliográfica de autores expertos en dirección estratégica e internacionalización, se ha procedido a realizar una investigación cualitativa: En primer lugar se describe el desarrollo de ambas compañías en el ámbito internacional hasta llegar a la actualidad, para proseguir con el análisis de sus actuales estrategias de internacionalización y formas de crecimiento. Por último se evalúan los resultados obtenidos y se dan a conocer sus futuras líneas de actuación a nivel internacional

Optimización de la metodología para la producción de hongos comestibles

El cultivo de hongos comestibles saprófitos constituye un sistema de producción-consumo, que ha adquirido gran relevancia social, económica y ecológica. Con el fin de abaratar costes a la vez que aprovechar y reciclar residuos forestales, el objetivo de este trabajo se ha centrado en evaluar la viabilidad del aserrín de Eucalyptus globulus como soporte del cultivo en bolsa de Lentinula edodes (hongo comercializado conocido como Shiitake) y Agrocybe aegerita (hongo no comercializado comúnmente llamado Seta de Chopo). Se han evaluado 6 formulaciones, todas ellas con el aserrín como componente principal y con adición de diferentes suplementos: cereales (salvado y mijo), un controlador del pH (CaCO3) y un estimulador de crecimiento (CaSO4). Se ha determinado el crecimiento miceliar sobre cada uno de los sustratos, así como la producción de carpoforos (tanto en cantidad como en calidad) y la duración del periodo de fructificación. La mezcla más efectiva para la producción de L. edodes fue aquella que contenía yeso y azúcar mientras que para A. aegerita el salvado resultó ser el mejor suplemento.

PLASTICIDAD DE LOS RECEPTORES DE LA SEROTONINA EN LAS ASTAS POSTERIORES DE LA MÉDULA ESPINAL DE LA RATA: INTERACCIÓN CON LA NEUROTRANSMISIÓN OPIOIDÉRGICA Y GLUTAMATÉRGICA EN UN MODELO DE DOLOR PERSIST

Una de las principales características de las vías descendentes provenientes de la RVMMes su capacidad para modular la transmisión nociceptiva en la médula espinal de manerabidireccional, es decir su capacidad tanto de facilitarla como de inhibirla. En este trabajomostramos que la activación de los receptores de la serotonina presentes en neuronas dela médula espinal puede tanto aumentar como disminuir los potenciales evocados porfibras C, o bien no producir cambio alguno en los mismos, dependiendo del subtipo dereceptor que se reclute. Demostramos también que la modulación de la nocicepción pormedio de los subtipos 5-HT1A, -2A, -2B, y -4 se modifica profundamente por efecto dela LNR.Datos previos que documentan mecanismos de interacción entre receptores del glutamatoy de la serotonina en otras regiones del SNC nos han conducido a plantear la hipótesis desu posible existencia en neuronas de las astas posteriores y su función en el dolorpersistente. Hemos hallado que la activación del receptor 5-HT2A induce cambiosplásticos de mGluR1 en las astas posteriores a través de un mecanismo intracelulardependiente de PKC. Esta modulación adquiere un papel clave en los signos desensibilización inducidos por la LNR a partir del quinto día posterior a la lesión. Por suparte, la activación del receptor 5-HT2B induce la fosforilación del receptor NMDA en ladensidad sináptica de las neuronas de las astas posteriores tras la LNR. Este mecanismoes mediado por la translocación de la isoforma ¿ de la PKC al espacio sináptico. El papelde 5-HT2B en la sensibilización central predomina en los primeros 2 días post-ligadura, ypierde relevancia en los días sucesivos.Además, la neurotransmisión serotoninérgica mediada por los receptores 5-HT2A y5-HT2B en animales sometidos a ligadura de L5 tiene un impacto negativo sobre laactividad antinociceptiva de los receptores opioides ¿ y ¿ en la médula espinal. Estosresultados sugieren que la intervención sobre los receptores 2A y 2B podría servir de basepara mejorar la eficacia de la analgesia por opioides en personas con dolor crónico.

Jabetza industriala. Markei buruzko legeria

[ES]Este volumen completa un repaso a una legislación que en el ámbito mercantil es esencial, como es la propiedad industrial y el Derecho de marcas, que tiene una especial dificultad por tratarse de un ámbito de gran relevancia económica y afectar, en igual medida, al mercado industrial

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.

Justicia penal restaurativa y justicia penal negociada, retórica y práctica. Estudio empírico del programa de mediación intrajudicial penal en Bizkaia

633 p.