De pilotos lemanes a prácticos del Puerto de Bilbao

El objetivo de este trabajo es conocer un poco más en profundidad el servicio de practicaje, la importancia de éste y, más concretamente, la actividad desarrollada por la actual Corporación de Prácticos del Puerto y Ría de Bilbao. Para esto, se hará un viaje por el tiempo y se analizará el practicaje desde sus comienzos, hacia el siglo XV [Saavedra, 1957, p.56] hasta la actualidad. Asimismo, se tratará de explicar cuál es el papel del práctico y los demás trabajadores de la Corporación por medio del relato del transcurso del día a día de un práctico en su guardia.

Comercio y burguesía mercantil de Bilbao en la segunda mitad del siglo XVIII

El presente estudio toma como marco cronológico de investigación la segunda mitad del siglo XVIII, época de la Ilustración, de la fundación de la Real Sociedad Bascongada de los Amigos del País y del florecimiento de las compañías comerciales y navieras de San Sebastián y Bilbao. Época de desarrollo y esplendor durante el reinado de Carlos III, pero también de inicio de una profunda crisis y decadencia de las industrias naval y siderúrgica en las postrimerías del siglo, como en repetidas ocasiones lo ha hecho ver D. Julio Caro Baroja. Moviéndonos dentro de este ámbito temporal, nuestro propósito ha sido el de intentar reconstruir el desenvolvimiento de las actividades comerciales de Bilbao y de sus hombres de negocios, tomando como objeto principal de nuestra investigación las fluctuaciones de su comercio activo de exportación, sometido a las variaciones de la demanda externa.

Cartas enviadas por Jon Bilbao a Justo Garate entre 1948 y 1990

11 cartas + 1 fragmento (mecanografiadas) ; entre 215x135mm y 210x295mm.

Carta enviada por Tomás Bilbao Hospitalet a Justo Garate

1 carta (mecanografiada) ; 215x155mm

Propuesta de un modelo de competitividad portuaria: aplicación para Bilbao y las líneas marítimas de contenedores

[ES] Este trabajo de investigación pretende proponer un modelo de cuantificación de la competitividad portuaria que puede alcanzar un puerto comercial para un tráfico de contenedores. Derivado de este objetivo, podría conseguirse una Estrategia a la medida para un puerto concreto orientada a la búsqueda de mercados, fundamentalmente. Para este último aspecto, esta investigación se centra en el Puerto de Bilbao y los servicios directos de línea regular en contenedor en las rutas intercontinentales que conectan Europa con América y el Caribe. La finalidad principal es la elaboración de un modelo teórico tratado dentro del área de la ciencia de la Economía de la Empresa como antecedente inmediato y básico de la Dirección Estratégica. Se consideran varios factores en el proceso de selección de un puerto que pueden contribuir a las preferencias de elección, tanto los relativos a las características del mismo, como a su hinterland para los grupos de usuarios. También se analizarán los estudios sobre modelos y métodos de competitividad portuaria considerados por la literatura especializada en los últimos años. La metodología a utilizar será una combinación de distintos métodos, para la consecución de cada uno de los objetivos. La investigación se apoya en el análisis de Importance–Performance (IPa) que consiste en evaluar tanto la satisfacción del cliente y la calidad del servicio. El análisis IPa tiene preponderancia para la obtención de un índice de competitividad de un puerto de contenedores. Dicho índice podría ser calculado mediante el uso de postulados y reglas de la matemática, en concreto de la Teoría de la Decisión/ Investigación de Operaciones.

Proyecto no concluido para la Alhóndiga de Bilbao. Una propuesta sobre la Estética objetiva de Jorge Oteiza como método de investigación.

785p. -- De forma paralela al proceso de investigación para esta Tesis el investigador llevó a cabo un documental de 80 minutos de duración, titulado "Oteiza y el Centro Cultural Alhóndiga. Proyecto estético para Bilbao". Este documental está elaborado a partir de las entrevistas arriba señaladas, así como de material audiovisual inédito sobre este proyecto. El documental está expuesto de forma permanente en el Museo Jorge Oteiza (Alzuza, Navarra)

Krisia eta politikak. Irrati-telebista publikoa ikusmiran : Ikus-entzunezko Komunikazio eta Publizitate Saileko II Nazioarteko Kongresua : aktak : (UPV/EHU) Bilbao 2012ko urriaren 4 eta 5

1. Ponentziak: - Public Service Broadcasting in Europe: a comparative analysis. - Lengua, poder y espacio de comunicación. Cataluña y el papel de la CCMA en la normalización del catalán. - Medios públicos, democracia y el rol de la Universidad Pública. - Servicio público radiotelevisivo, independencia de gestión e informativa. - Retos para un espacio vasco de comunicación. El papel de EITB en el sistema comunicativo Vasco. 2. Komunikazioak : I. Irrati-telebista zerbitzu publikoaren finantzaketa - I. La financiación del servicio público de radiotelevisión: - El efecto dominó. Nuevas estrategias de financiación del documental creativo ante la crisis de la televisión pública en Europa. - El Comercio ubicuo como medio de financiación de las televisiones públicas. - Euskal zinemaren ekoizpena eta finantzazioa: EiTBren funtzioa. - The Financing of Public Television in Spain, the chronicles of an announced death. Country case analysis and proposals for funding the wreck. - Europako hizkuntza gutxituetako irrati-telebista publikoak: eragin ekonomikoa eta finantzaketa arazoak. II. Hedabide publikoak teknologia berrien erronkaren aurrean : - Los servicios públicos europeos de radio y televisión ante la convergencia mediática. - Análisis de contenido longitudinal de rtve.es y canalsur.es. La selección y jerarquización de la noticias principales de portada. - RTVE a la carta en tiempos de crisis. Digitalización en el contexto de la crisis económica. De los canales temáticos a la televisión a la carta. - La social TV revoluciona el panorama de la televisión convencional. Análisis del fenómeno de los twittersodios en RTVE. - Televisiones autonómicas y redes sociales. - Análisis de los contenidos audiovisuales en los agregadores de notas de prensa. - Impacto de Internet en la TV generalista: Innovación en los contenidos y nuevas fórmulas de negocio. III. Informazio-saioak hedabide publikoetan : - La calidad y el rigor en los informativos de TVE. - Percepción de la independencia informativa en la radiotelevisión pública a través de los debates de la comisión de control parlamentario del congreso de los diputados, tras la aprobación de la ley 17/2006. -¿Propaganda o información? El tratamiento discursivo de la actualidad valenciana en los informativos de Canal 9. - Medios públicos y comunicadores de confianza. La sintonía con el público como rutina profesional. - La percepción de los jóvenes andaluces del modelo de servicio público de la RTVA. - La construcción mediática de los candidatos. Los informativos de las televisiones públicas en campaña electoral. - Análisis de la gestión y regulación de RTVE (periodo 2004-2011) y su influencia en la información periodística. IV. Irrati publikoaren erronkak - La radio local: una especie en peligro de extinción. El caso de Girona. - Hego Euskal Herriko Udal Irratiak, eredu baten porrota. - La extinción de la proximidad en la radio pública estatal. - Desafíos de la radiodifusión pública y local en Andalucía. V. Hedabide publikoetako profesionalak: - El Estatuto de Redacción en EITB: Un sueño a punto de convertirse en realidad. - La reivindicación de los profesionales ante el nuevo escenario de la televisión pública en España. - La educación en Competencia Mediática de los espectadores y de los profesionales de la televisión pública. - Libros de estilo y directrices editoriales: referente de calidad en el Periodismo audiovisual y multimedia de los medios públicos. VI. Telebista publikoen gobernantza: telebista autonomikoen kasua: - Hacia un nuevo modelo en tiempos de crisis económica: el caso de la televisión autonómica valenciana. - Retos y perspectivas para la televisión pública andaluza. - El reflejo de Caín. Política y televisión pública en el Principado de Asturias (2005-2012). - Empresa de comunicación y entorno político. El porqué, en su momento, del servicio público audiovisual en Asturias. - Canal Sur Televisión en tiempos de crisis. ¿El fin de un modelo público de televisión en Andalucía? VII. Irrati-telebista publikoaren erregulazioa: - La corregulación como aplicación y complemento del marco legal. La necesidad de repensar el gobierno del sector audiovisual. - Los consejos audiovisuales españoles en el marco de las autoridades de regulación europeas del audiovisual. - Valores de servicio

Tipografía Popular Urbana: Los rótulos del pequeño negocio en el paisaje de Bilbao

419 páginas. 561 fotografías originales.

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.

Generación dinámica de parrillas de productos en Magento en base al análisis de datos de fuentes abiertas

En este Trabajo de Fin de Grado desarrollado en la empresa On4U, se ha implementado un módulo para Magento, cuya función principal es la generación dinámica de parrillas de productos en base al análisis del tiempo meteorológico, teniendo en cuenta la localización del cliente. Además, el módulo guarda automáticamente las compras efectuadas, junto con la información externa, para un posible análisis posterior que relacione los hábitos de compra con el tiempo meteorológico. Aunque se haya centrado en este caso de uso, se ha desarrollado con un enfoque modular, de tal manera que fuese fácil de integrar en el módulo el uso de otra fuente abierta de información. Para poder realizar el proyecto, se ha tenido que profundizar en varios conceptos relacionados con la plataforma de eCommerce Magento, entre ellos, el patrón Modelo-Vista-Controlador y el ciclo de vida de una petición.

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

325 p.

La innovación de la metrópoli: de Bilbao a Oresund y San Diego

445 p.

Las relaciones de género en los centros sociales okupados de Bilbao

Gaztetxeetan nesken eta mutilen arteko harremanak nolakoak diren eta zelako ekintzak ematen diren ikus-lehioa izango da ikerketa. Askotan teoria eta praktika ez datoz bat. Beraz gaztetxeek antolamendu horizontala dute, antitaurinoak, antisexistak… dira baina gero eguneroko funtzionamenduan heziketak inposatutako hainbat rol sexistak errepikatzen dira. Eta nahiz eta errealitatea aldatzen ari den gaztetxeetan edo asanbladetan gai hauek ateratzea oso zaila da. Gehienetan arazoa ez delako identifikatzen. Horregatik, hausnarketa bultzatzea eta aldaketak eragitea du helburu ikerlanak.

Reutilización de escoria negra de acería como soporte en biofiltros para la eliminación de H2S del biogás.

[EN]Due to the limitations associated with fossil fuels it is necessary to promote energy sources that are renewable as well as eco-friendly, such as biogas generated in anaerobic digesters. The biogas, composed principally of methane and CO2, is the result of the biodegradation of organic matter under anaerobic conditions. Its use as fuel is limited by the presence of minority compounds such as hydrogen sulphide (H2S); therefore, its pre-treatment is necessary. Currently there are various technologies for the removal of H2S from a gas stream, but most of them are based on physic-chemical treatments which have a number of drawbacks as reactive consumption, generation of secondary flows, etc. Biofiltration has been used as an efficient and low cost alternative to conventional purification processes, and excellent results for the degradation of H2S have been obtained. However process can be limited due to the progressive ageing of the support material, along with the loss of nutrients and other specific characteristics necessary for the good development of biomass. The purpose of this project is to develop a mixed support consisting of a mixture of an organic material and an inorganic support for its application in the removal of the H2S from biogas. This support material helps to optimize the characteristics of the bed and extend its lifespan. The development of such material will contribute to the implementation of biofiltration for treating biogas from anaerobic digesters for its use as biofuel. The inorganic material used is electric arc furnace (EAF) black slag, a by-product generated in large quantities in the production of steel in the Basque Country. Although traditionally the slag has been used in civil engineering, its physicochemical characteristics make it suitable for reuse as a filter medium in biofiltration. The main conclusion drawn from the experimental results is that EAF black slag is a suitable co-packing material in organic biofilters treating H2S-polluted gaseous streams. High pollutant removal rates have been achieved during the whole experimental period. The removal capacity recorded in biofilters with less inorganic material was higher than in those with higher slag portion. Nevertheless, all the biofilters have shown a satisfactory response even at high inlet loads (48 g·m-3·h-1), where the RE has not decreased over 82%.

Revisión bibliográfica del tratamiento de biogás por biofiltración.

[ES]En el siguiente trabajo se ha realizado una revisión bibliográfica en la que se muestran los resultados obtenidos al llevar a cabo la purificación del biogás y/o la eliminación del metano, en los casos en los que su valorización no sea posible, mediante métodos biológicos (biofiltración). Se recogen asimismo las diversas fuentes desde las que se genera el biogás (generación incontrolada o producción controlada) junto con las concentraciones típicas de todos los compuestos que pueden formar su composición. En la purificación del biogás se ha estudiado la eliminación de compuestos perjudiciales para el aprovechamiento energético del biogás, como son el sulfuro de hidrógeno (H2S), los mercaptanos y los siloxanos. Para el estudio de los compuestos a eliminar se ha diferenciado entre distintas configuraciones de biorreactores (biofiltros, biofiltros percoladores y biolavadores) y para cada una de ellas se han recogido datos representativos como la temperatura óptima de operación, las diferencias entre operar a pH ácido o básico (teniendo en cuenta que el pH natural de operación es ácido pero que en estas condiciones la solubilidad del H2S es menor y el relleno se deteriora con mayor rapidez). También se ha analizado la influencia de la cantidad de oxígeno necesario para garantizar la degradación total de los contaminantes y evitar la acumulación de depósitos de azufre, llegando incluso a necesitarse proporciones de O2/H2S de 49.2 para la oxidación completa del H2S. Se ha estudiado también la cantidad necesaria de nitrógeno (nutriente) en los procesos llevados a cabo en condiciones anaerobias (cercana a 200 mgN-NO3 -/L), así como el efecto que tienen los compuestos producidos en la oxidación parcial (azufre elemental (S0), metanol, formaldehido, etc.) en el funcionamiento del sistema.