El pintor navarro Juan Ochoa de Arín (1600-1652) y su producción en Gipuzkoa

Investigación realizada dentro del Programa de Formación y Perfeccionamiento de Personal Investigador del Gobierno Vasco (2010-2013).

Escultura romanista en Gipuzkoa. El taller de Tolosa

El romanismo, estilo al que pertenecen las obras escultóricas estudiadas en este libro, es una adaptación del manierismo italiano de Miguel Ángel y sus seguidores que se caracteriza por la concepción de figuras de gran idealización, de anatomía exaltada y pletóricas de fuerza. En esta publicación se analizan con detenimiento los retablos de finales del siglo XVI y comienzos del XVII en sus vertientes arquitectónica, escultural y pictórica de esta zona geográfica comprendida en el norte de la Península. Se trata de un tema poco estudiado y con su abordaje se han intentado proporcionar las herramientas para que estas obras, algunas de ellas recientemente restauradas, sean valoradas y apreciadas como se merecen. Para ello, las obras se encuadran en el marco político, administrativo, religioso y artístico del entorno de Tolosa, en Gipuzkoa, donde en el cambio de centuria artistas como Jerónimo de Larrea o Pedro de Goicoechea realizaron los retablos mayores de Itsasondo o Irura, en los que se consolida este nuevo estilo contrarreformista. El romanismo se ve analizado en su vertiente estilística, iconográfica o en sus fuentes gráficas, mientras que en cuanto a los artistas estudiados se centra la atención en los aspectos biográficos y profesionales, ofreciendo un amplio catálogo de obras que se distribuyen en el curso del río Oria, desde el actual Goierri hasta la costa cantábrica.

Transformaciones en el retablo mayor de San Miguel Arcángel de Lazkao (Gipuzkoa): del Barroco al Neoclasicismo

[ES] El retablo mayor de la localidad guipuzcoana de Lazkao fue realizado por Juan de Ursularre en 1683, siguiendo los parámetros de la retablística barroca. Queriendo engrandecer su aspecto, fue paulatinamente transformado durante el siglo XVIII. Por ello se concibió un nuevo cascarón con pinturas enviadas desde Madrid y más tarde se adecuó a los nuevos gustos neoclásicos mediante una radical reforma realizada en 1791 que consistió en eliminar todo atisbo de decoración barroca.

Arte en Quintana del Pidio (Burgos): estudio histórico-artístico de la iglesia de Santiago Apóstol

La parroquia de Santiago Apóstol de Quintana del Pidio, situada en la ribera burgalesa, se levanta en la plaza mayor de la citada localidad, junto al ayuntamiento. Esta construcción tardogótica de finales de la Edad Media se fue completando con una torre de comienzos del siglo XVI, una portada y una sacristía barrocas y una única capilla dedicada al Santo Cristo, edificada ya en el siglo XVIII. En su interior se conservan cinco retablos barrocos que ejemplifican las fases clasicista, churrigueresca y rococó. También cuenta con pinturas, un interesante ajuar de platería y otros objetos de mobiliario, ornamentos o indumentaria que han sido estudiados en el libro. La metodología histórico-artística empleada en este trabajo permite entender la obra en su contexto, completando su significado con una lectura iconográfica cuando procede. Con la catalogación y la aportación de datos sobre las artes de esta parroquia ribereña se pretenden poner el valor las obras que desde la segunda mitad del siglo XV han ido completando el patrimonio artístico de esta villa para que se adquiera conciencia de su importancia y se dediquen los recursos necesarios para su conservación en el futuro.

Polímeros de Coordinación con Centros Metálicos en Entornos de Coordinación Variables: Posibles Aplicaciones.

Presentación de power point. Comunicación oral presentada en el 1er Simposium sobre Propiedades y Aplicaciones de MOFs y COFs, celebrado en Granada en abril de 2015

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.

Apaf-1 Inhibitors Protect from Unwanted Cell Death in In Vivo Models of Kidney Ischemia and Chemotherapy Induced Ototoxicity

Background: Excessive apoptosis induces unwanted cell death and promotes pathological conditions. Drug discovery efforts aimed at decreasing apoptotic damage initially targeted the inhibition of effector caspases. Although such inhibitors were effective, safety problems led to slow pharmacological development. Therefore, apoptosis inhibition is still considered an unmet medical need. Methodology and Principal Findings: The interaction between Apaf-1 and the inhibitors was confirmed by NMR. Target specificity was evaluated in cellular models by siRNa based approaches. Cell recovery was confirmed by MTT, clonogenicity and flow cytometry assays. The efficiency of the compounds as antiapoptotic agents was tested in cellular and in vivo models of protection upon cisplatin induced ototoxicity in a zebrafish model and from hypoxia and reperfusion kidney damage in a rat model of hot ischemia. Conclusions: Apaf-1 inhibitors decreased Cytc release and apoptosome-mediated activation of procaspase-9 preventing cell and tissue damage in ex vivo experiments and in vivo animal models of apoptotic damage. Our results provide evidence that Apaf-1 pharmacological inhibition has therapeutic potential for the treatment of apoptosis-related diseases.

LC-MS based methods for phytosterols determination in oenological matrices. Targeted metabolomic study of Rioja grape varieties

221 p.+ anexos

Modular integration and on-chip sensing approaches for tunable fluid control polymer microdevices

228 p.

Criminología ambiental orientada a la delincuencia juvenil

Este trabajo ofrece una revisión bibliográfica buscando transmitir una mayor comprensión de la delincuencia juvenil desde el punto de vista de la criminología ambiental. Y con el objeto de profundizar en el conocimiento de las características espaciales de la delincuencia juvenil, se analizan de forma descriptiva los dtos obtenidos de 84 atestados de la Guardia Municipal de Donostia, correspondientes a detenciones de menores de entre 14 y 18 años en los años 2013 y 2014.

Régimen económico matrimonial en defecto de pacto y derecho internacional privado: determinación de la ley aplicable

El objetivo del Trabajo de Fin de Grado ha sido combinar tres bloques de análisis: el derecho normativo interno español en materia de derecho internacional privado, el derecho comparado en el marco de la Unión Europea y el derecho europeo (los reglamentos en vigor) y los dos proyectos de reglamento en esta materia actualmente en tramitación. Mediante el trabajo se persigue demostrar la necesidad y oportunidad de que el derecho europeo, sin armonizar sustantivamente las regulaciones de cada estado miembro, utilice las técnicas del derecho internacional para seleccionar el Tribunal competente, designar la ley aplicable reconocimiento y ejecución de decisiones judiciales en materia del derecho de familia internacional y centrándonos en el sector de régimen económico matrimonial en defecto de pacto.

La integración de los sistemas de gestión normalizados: un análisis de los principales estudios empíricos.

[ES]En la actualidad, muchas empresas organizan sus sistemas de gestión basándose en las normas y estándares internacionales (ISO 9000, ISO 14000, OHSAS 18000…). Considerando que todos ellos están soportados en unos principios comunes, las organizaciones tratan de aprovechar las sinergias existentes entre dichos sistemas buscando la mayor integración posible y la obtención de beneficios, tales como el ahorro de costes, la disminución de la burocracia o la mejora de la eficiencia. Por ello, el objetivo del presente trabajo es aportar una serie de recomendaciones que permitan a las empresas orientar la integración de sus sistemas de gestión de una manera sencilla y ágil.

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

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

Análisis de las diferentes tecnologías de centrales termosolares.

[ES]En este proyecto se recoge un análisis de las diferentes tecnologías de centrales termosolares. Las energías renovables tienen un papel fundamental en el abastecimiento energético futuro, ya que son una fuente inagotable con un impacto medioambiental mínimo. Dentro de las renovables, la energía termosolar es una de las más destacables en España, que se ha situado como el país líder en termosolar. Existen cuatro tecnologías diferentes para este tipo de centrales, por lo que el objetivo de este trabajo es profundizar en su conocimiento y proporcionar un criterio objetivo que permita seleccionar la más adecuada en futuras instalaciones. Para ello, se considerarán tanto aspectos técnicos como económicos, con el fin de estudiar las principales ventajas y desventajas de cada tipo.