Los linajes de Bizkaia en la Baja Edad Media: poder, parentesco y conflicto

Este libro se ocupa del principal protagonista de la historia medieval de Bizkaia: el hidalgo. Como en el resto de Europa Occidental, la nobleza del Señorío, organizada social y políticamente en linajes, acapara las fuentes de renta y traza sus estrategias sobre la alianza y la violencia. Sin embargo, en Bizkaia, la violencia feudal alcanzará cotas extremas en lo que se conoce como "luchas de bandos". La competencia entre los hidalgos se fundamenta en un argumento tan sólido como simple: el "más valer". "Más valer" en rentas y atreguados, "más valer" en descendencia bastarda o legítima, "más valer" que mueve a matar al vecino como forma extrema de sometimiento. En este contexto el linaje destaca como una referencia existencial paralela a tan extrema ideología de la competencia. En él se desarrolla la vida, se revelan los signos del poder y se conforma la imagen propia sobre la de los antepasados. Al filo del 1500, esta manifestación local de la honra tendrá tal éxito que contagiará al resto de los vizcaínos de la época forzando la implantación de la "hidalguía universal"

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.

Compensación del factor de potencia en instalaciones eléctricas industriales de baja tensión.

[ES]En las últimas décadas, la optimización de las instalaciones eléctricas se ha convertido en una de las prioridades más importantes de las empresas. En este sentido, la corrección del factor de potencia supone un importante tema a analizar y resolver. Hoy en día, se dispone de muchos métodos de compensación, pero en la mayoría de los casos, la implementación de baterías de condensadores resulta la mejor opción. Por otra parte, dependiendo de la distribución elegida en la instalación de los condensadores, se consiguen ciertas ventajas y desventajas en cuanto a componentes reactivas en el sistema eléctrico y costes finales de la compensación se refiere. Además del desarrollo teórico, se dispondrá de simulaciones realizadas en herramientas de cálculo que ayudarán a la comprobación de estas ideas.

[A_Llodio_Goikoetxea] Documentación geométrica de los restos de una prensa de sidra en el Caserío Goikoetxea, barrio de Isusi (Laudio/Llodio, Álava)

[ES] Los restos corresponden a un agujero que se han encontrado en la excavación del pórtico y que se relaciona con un posible poste y un pilar de madera en el interior del caserío que parece una reutilización de los elementos de la antigua prensa.

Comparativa entre diferencial de baja impedancia de generador y de baja impedancia de transformador.

[ES]El objetivo principal de TFG es analizar y comparar el funcionamiento de las protecciones diferenciales de baja impedancia de generador y de transformador de potencia. Para ello, se describirán sus características principales de forma teórica y se realizarán simulaciones mediante el módulo SimPowersSystems contenido en Matlab.

Análisis de la influencia de los sistemas de puesta a tierra en la eficiencia de instalaciones eléctricas de baja tensión residenciales e industriales.

[EN]Nowadays, global society is more aware of electrical energy’s risks than never before, and electrical safety has turned a priority when a new installation is designed. So, a great protection to an unwanted electric hazard is required, being specially careful with indirect contacts. If a circuit has an insulation failure and an indirect contact is produced, there is risk of an accidental electrocution, risk that must be avoided by making a good choice of the grounding methodology and properly coordinating the electrical protections in the installation. In order to minimize that risk, a study of low voltage industrial and residential installation’s grounding methodologies is introduced, analyzing the tree grounding methodologies internationally accepted (TT, TN, IT). In addition, two real examples are solved (using a computer-aided engineering software), confirming the results of the theoretical study.

Propuesta de intervención de actividad física contra el sedentarismo en lonjas juveniles del barrio bilbaino de Zorrotza

[ES] Con el presente estudio descriptivo se pretende obtener los siguientes objetivos: reunir la mayor bibliografía posible sobre las lonjas juveniles. Conocer estos tipos de espacios y qué actividades son las que se realizan en ellos. Tomando como punto de partida la observación de una lonja ubicada en el barrio Bilbaíno de Zorroza, se analizarán los comportamientos que se dan en estos espacios. Además se pretende ofrecer terminología sobre la juventud de hoy en día y las actividades de ocio en las que participan. Los estudios previos destacan un elevado consumo de drogas seguido de hábitos sedentarios. Al mismo tiempo, se presenta una propuesta de intervención en estos espacios y poder así ofrecer alternativas de ocio contra el sedentarismo a medio y largo plazo. Se espera de este trabajo que nos ofrezca más información sobre las actividades que se realizan en las lonjas juveniles y el tipo de drogas que más se consumen ellas, así como la frecuencia con la que se consumen.

Comparativa de metodologías de cálculo de faltas en redes eléctricas de baja tensión residenciales e industriales.

[ES]Este trabajo se basa en la aplicación de distintas metodologías (norma europea, método fácil y norma americana) para la obtención de las corrientes de cortocircuito en un sistema eléctrico de baja tensión, de forma que se sepa de antemano el valor de dichas corrientes en cualquier punto del circuito para el correcto dimensionamiento de los dispositivos de protección a emplear.

O destino das coisas contadas: cadernos, escritas e lixo: a arte em Barrio

O presente trabalho faz uma análise da obra de Artur Barrio a partir de uma aproximação da materialidade de sua obra. Após um estudo preliminar de aspectos históricos e da fortuna crítica do artista, os Cadernos livros surgiram como um aprofundamento dessa questão, pois são um misto de rascunho, lugar de memória e obra de arte, configurando o cerne da obra de Barrio. Nesse contato, surge a escrita em simbiose com a própria materialidade da obra, a ponto de não ser possível discernir onde começa a obra e onde termina a escrita. Surgem traços de abjeção, de lembrança, de silêncio, de risco. Uma escrita fragmentária que se alastra por todos os lados, fugindo aos Cadernos e tomando todos os espaços da ocupação implementada por Barrio: salas, museus, ruas, cidades. Ao deixar seus rastros, seus vestígios, essa escrita caminha para um grau zero, agregando contaminações e se transformando num ato quase primitivo. Torna-se, assim, a fundação da materialidade e do trabalho de Artur Barrio

Taller Integrado 3A (Proyectos V, Construcción I y Urbanismo III)

Nivel educativo: Grado. Duración (en horas): Más de 50 horas

Commercial Whaling, Especially for Gray Whales, Eschrichtius robustus, and Humpback Whales, Megaptera novaeangliae, at California and Baja California Shore Stations in the 19th Century (1854–1899)

Shore whaling along North America’s California and Baja California coasts during 1854–99 was ancillary to the offshore and alongshore American whale fishery, which had begun in the North Pacific in the early 1800’s and was flourishing by the 1840’s. From its inception at Monterey, Calif., in the mid 1850’s, the shore fishery, involving open boats deployed from land to catch and tow whales for processing, eventually spread from Monterey south to San Diego and Baja California and north to Crescent City near the California–Oregon border. It had declined to a relict industry by the 1880’s, although sporadic efforts continued into the early 20th century. The main target species were gray whales, Eschrichtius robustus, and humpback whales, Megaptera novaeangliae, with the valuable North Pacific right whale, Eubalaena japonica, also pursued opportunistically. Catch data are grossly incomplete for most stations; no logbooks were kept for these operations as they were for high-seas whaling voyages. Even when good information is available on catch levels, usually as number of whales landed or quantity of oil produced, it is rarely broken down by species. Therefore, we devised methods for extrapolation, interpolation, pro rationing, correction, and informed judgment to produce time series of catches. The resulting estimates of landings from 1854 to 1899 are 3,150 (SE = 112) gray whales and 1,637 (SE = 62) humpback whales. The numbers landed should be multiplied by 1.2 to account for hunting loss (i.e. whales harpooned or shot but not recovered and processed).

Regularização fundiária urbana de interesse social: a coordenação entre as políticas de urbanismo e de habitação social no Brasil à luz de experiências do direito francês

A regularização fundiária urbana de interesse social só pode ser compreendida juridicamente se considerar-se que, além da legalização da posse ou da propriedade do bem imóvel, ela abrange obrigatoriamente uma série de intervenções urbanísticas fundamentais. Outra premissa necessária ao estudo jurídico é que esta espécie de operação urbana não pode ser compreendida isoladamente, enquanto uma instituição particular, pois ela pressupõe a definição das condições por meio das quais o planejamento urbano e o planejamento habitacional se determinam reciprocamente, favorecendo a concretização de direitos fundamentais. Três valores-base devem inspirar o desenvolvimento desta correlação entre as políticas urbanísticas e as habitacionais, são eles: a moradia como direito fundamental complexo ligado à ideia mais ampla de direito à cidade, a propriedade como direito protegido juridicamente apenas quando observado o princípio da função social da propriedade e a justa distribuição das mais-valias urbanas como princípio reitor da intervenção dos poderes públicos nos espaços urbanos para efetivar uma distribuição mais isonômica do espaço. Com base no contexto normativo brasileiro e a realidade institucional concreta dos Municípios e tendo em vista a experiência francesa a respeito das políticas urbanas e habitacionais, é possível pensar um quadro legal e regimes jurídicos adequados à realização mais eficaz das operações urbanas de regularização fundiária.