Aplicación de la teoría de carteras con activos numismáticos y metales preciosos

[ES] El objetivo del trabajo es la construcción de diferentes carteras compuestas por activos numismáticos de oro y metales nobles (oro, plata, platino, paladio y rodio); con el fin de construir aquella cartera que mejor se adapte al inversor, acorde a su perfil y conocer cuál es la Cartera del Mercado. Para ello, mediante la Teoría de Carteras (Markowitz, 1952; 1959), construiremos la Frontera Eficiente y trazaremos la Línea del Mercado de Capitales o CML.

Reformado de hidrocarburos logísticos sobre catalizadores de NiAl2O4 de prestaciones mejoradas

La obtención de corrientes ricas en hidrógeno se presenta como un reto de alto interés industrial ya que constituyen la alimentación de los sistemas de producción energética más prometedores a medio-largo plazo, las pilas de combustible. El avance en la implementación industrial de estos dispositivos está condicionado por la disponibilidad de fuentes de hidrógeno fácilmente disponibles y almacenables. Los combustibles logísticos (gas natural, gasolina y diesel) son recursos todavía abundantes cuya transformación química puede satisfacer esta demanda de hidrógeno. En este Trabajo Fin de Grado se plantea un estudio sobre diferentes estrategias de reformado (oxidación parcial, reformado con vapor de agua o reformado autotérmico) empleando espinelas de aluminato de níquel como catalizadores alternativos a los metales nobles (Rh)

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.

Síntesis y caracterización de perovskitas LaCoO3 y LaMnO3 para la oxidación de NO a NO2

Las perovskitas con fórmula general ABO(3) son una alternativa prometedora a los catalizadores convencionales basados en metales nobles para la reducción de contaminantes procedentes de motores diésel, debido a su bajo coste, excelentes propiedades redox y alta durabilidad. En este trabajo se sintetizarán las perovskitas LaCoO3 y LaMnO3, por el método del ácido cítrico. Las muestras preparadas serán caracterizadas por técnicas como XRD, BET, H2-TPR y SEM. Se analizará su actividad en la reacción de oxidación de NO a NO(2).

Contribución al estudio de sistemas de hipertermia óptica y su aplicación en muestras biológicas

Las nanopartículas de metales nobles (especialmente las de oro) tienen un gran potencial asociado al desarrollo de sistemas de terapia contra el cáncer debido principalmente a sus propiedades ópticas, ya que cuando son irradiadas con un haz de luz sintonizado en longitud de onda con su máximo de Resonancia de Plasmón Superficial, absorben de manera muy eficiente dicha luz y la disipan rápidamente al medio en forma de calor localizado. Esta característica por tanto, puede ser aprovechada para conseguir elevar la temperatura de células tumorales hasta sobrepasar umbrales a partir de los cuales se produciría la muerte celular. Partiendo de estos principios, esta tesis se centra en el desarrollo y la caracterización de una serie de prototipos de hipertermia óptica basados en la irradiación de nanopartículas de oro con un haz de luz adecuado, así como en la aplicación in vitro de la terapia sobre células cancerígenas. Además, el trabajo se orienta a identificar y comprender los procesos mecánicos y térmicos asociados a este tipo de hipertermia, y a desarrollar modelos que los describan, estudiando y planteando nuevas formas de irradiación, para, en última instancia, poder optimizar los procesos descritos y hacerlos más efectivos. Los resultados obtenidos indican que, el uso de nanopartículas de oro, y más concretamente de nanorods de oro, para llevar a cabo terapias de hipertermia óptica, permite desarrollar terapias muy efectivas para inducir muerte en células cancerígenas, especialmente en tumores superficiales, o como complemento quirúrgico en tumores internos. Sin embargo, los efectos de la toxicidad de las nanopartículas de oro, aún deben ser detalladamente estudiados, ya que este tipo de terapias sólo será viable si se consigue una completa biocompatibilidad. Por otro lado, el estudio exhaustivo de los procesos térmicos que tienen lugar durante la irradiación de las nanopartículas ha dado lugar a una serie de modelos que permiten determinar la efectividad fototérmica de las nanopartículas y además, visualizar la evolución de la temperatura tanto a escala nanométrica como a escala macrométrica, en función de los parámetros ópticos y térmicos del sistema. El planteamiento de nuevas formas de irradiación y el desarrollo de dispositivos orientados a estudiar los fenómenos mecánicos que tienen lugar durante la irradiación pulsada de baja frecuencia y baja potencia de nanopartículas de oro, ha dado lugar a la detección de ondas de presión asociadas a procesos de expansión termoelástica, abriendo la puerta al desarrollo de terapias de hipertermia que combinen la muerte celular producida por calentamiento con la muerte derivada de los fenómenos mecánicos descritos.VII Noble metal nanoparticles (especially gold ones), have a huge potential in the development of therapy systems against cancer mainly due to their optical properties, so that, when these particles are irradiated with a light that is syntonized in wavelength with their maximum of Surface Plasmon Resonance, they effectively absorb and dissipate the light to the surrounding medium as localized heat. We can take advantage of this characteristic for rising the temperature of cancer cells above the threshold at which cellular death would occur. From these principles, this thesis is oriented to the development and characterization of a series of optical hyperthermia prototypes based on the irradiation of gold nanoparticles using the suitable light, and on the in vitro application of this therapy over cancer cells, to understand the mechanical and thermal processes associated with this kind of hyperthermia, developing descriptive models, and to study and to approach new ways of irradiation in order to, ultimately, optimize the described processes and make them more effective. The obtained results show that, the use of gold nanoparticles, and more specifically, of gold nanorods, to carry out optical hyperthermia therapies, allows the development of very effective therapies in order to induce death in VIII cancer cells, especially in superficial tumors, or like surgical complement in more internal tumors. However, the toxicity effects of the gold nanoparticles still need to be studied more detail, because this kind of therapies will be feasible only if a complete biocompatibility is achieved. On the other hand, the exhaustive study of the thermal processes that take place during the irradiation of the nanoparticles resulted in a series of models that allow the determination of the photothermal efficiency of the nanoparticles and also the visualization of the temperature evolution, both at nanoscale and at macroscale, as a function of the optical and thermal parameters of the system. The proposal of new ways of irradiation and the development of devices oriented to study the mechanical effects that take place during the low frequency and low power pulsing irradiation of gold nanoparticles has led to the detection of pressure waves associated to thermoelastic expansion processes, opening the door to the development of hyperthermia therapies that combine the cellular death due to the heating with the death derived from the described mechanical phenomena.

Susceptibilidad de especies nobles a diferentes herbicidas, en diferentes dosis en café (Coffea arabica L.)

Con el propósito de evaluar la susceptibilidad de especies nobles a diferentes dosis de herbicidas en cafetales, se condujo el presente trabajo que se llevó a cabo en el Centro Experimental de Café del Pacifico "Mauricio López Munguía", ubicado en Municipio de Masatepe, departamento de Masaya y en la Finca "El doble" Municipio del Crucero, departamento de Managua, a partir de Mayo de1991a Enero de 1992. Las especies nobles estudiadas fueron Commelina díffusa, Panicun trichoides y Desmodium ovalifolium sembradas en las calles del cafeto. Commelina diffusa y Oplismenus burmannii, establecidas de forma natural en las calles del cafeto. Se probaron tres herbicidas: Paraquat (Gramoxone), Glifosato (Round up) y 2.4-D evaluándose en cada uno tres dosis que se escogieron partiendo de las dosis comerciales utilizadas por los caficultores. Se usó diseño de bloques completos al azar con arreglo en parcelas subdivididas con 4 repeticiones, 108 tratamientos para el experimento de coberturas sembradas y arreglo en parcelas divididas con 3 repeticiones, 27 tratamientos para Oplismenus burmannii y 3 repeticiones, 18 tratamientos para Commelina diffusa.Se evaluó porcentaje de susceptibilidad a los 8,15,30,45 y 60 días después de aplicación y porcentaje de recuperación a los 45 y 60 días después de aplicación para el experimento de coberturas sembradas. En los otros dos experimentos se tomó porcentaje de susceptibilidad a los 15,30 y 45 días después de aplicación y porcentaje de recuperación a los 45 días después de aplicación. Las diferentes dosis ensayadas no mostraron diferencias significativas. Oplismenus burmannii presentó el menor grado de susceptibilidad y el mayor porcentaje de recuperación a los herbicidas. Commelina diffusa presentó el mayor grado de susceptibilidad a los herbicidas ensayados. 2,4-D no ejerció ningún efecto sobre Oplismenus burmatmii y Panicum trichoides. De forma general en donde se aplicó Paraquat se observó el mayor porcentaje de recuperación de las especies nobles.

¿Por qué son tan útiles los metales?

Duración (en horas): De 11 a 20 horas. Nivel educativo: Grado

Depuración de aguas residuales urbanas y concentración de metales en fangos digeridos

[ES] La progresiva implantación de plantas de tratamiento de aguas residuales urbanas ha ido estableciendo una experiencia en el conocimiento de la eficacia de tratamiento de los diversos parámetros en plazos largos de funcionamiento. El análisis y comparación de resultados y tecnologías debe pennitir conocer las características de fiabilidad en la operación y el comportamiento frente a los diversos aspectos de la nonnativa legal. Además, el análisis en diferentes épocas del año puede producir distintos resultados o conclusiones. En este trabajo se ha tomado para el análisis una planta de tratamiento convencional, estudiando inicialmente los porcentajes medios de eliminación de diferentes parámetros, en relación asimismo con las necesidades que debe satisfacer. En condiciones de alta carga orgánica, la concentración de nitrógeno y algún tóxico especial parecen plantear las mayores dificultades. Se ha deseado focalizar la atención en el proceso de concentración de metales que se. produce en las plantas con tratamiento anaerobío de fangos. Por este motivo se Uevó a cabo un estudio de la evolución de metales en la depuración y la concentración de fangos digeridos. El fenómeno resulta de interés para analizar la calidad de las aguas que se obtienen, aunque debe considerarse también la concentración de metales en el destino final que se dé a los fangos tratados.

Materiales Condensados y con Estructura Abierta basados en Fosfitos de Metales 3d

438 p.

Caracterización del medio supergénico en el yacimiento Ni-Cu (PGE) de Aguablanca, SW Iberia. Redistribución de metales base y PGE

1 v. (pág. var.)

Estudio hidrogeoquímico del lago ácido de Cueva de la Mora (IPB, Huelva): controles sobre la concentración de metales y modelo de estratificación

298 p.

Dendrorremediación: El uso de Betula alba para monitorizar y reducir el contenido de metales en suelos mineros.

[EN] The intense industrial activity that took place over the past century resulted in large contaminated áreas. This is an important risk to human health and environmental safety. Recent biotechnological techniques for bioremediation include phytoremediation, which uses plants to remove or stabilize contaminants in soils. In our study we choose birch (Betula alba) as the preferred species to remedy mining soils, due to it produces a large biomass and can accumulate high levels of toxic elements in its tissues. The aim of this study was (i) to determine the possibility of using this species in reforestation and/or remediation of mining soils (ii) to elucidate the potential of tocopherol levels as indicators of heavy metal pollution. Trees growing in mining soils with high concentrations of Zn, Cd and Pb were sampled and the metal content in various organs and in tree rings was analyzed. α-tocoferol levels were also analyzed as an indicator of stress. The results showed a different distribution of metals in plant tissues. Zn and Cd had a higher accumulation in leaves, whereas Pb was stored in the timber. In addition, the metal content in tree rings was higher in older rings, leading to a conclusion that older tissues present a detoxification strategy. Furthermore, we saw how the presence of α- tocoferol on branches can be an indicator of metal stress in plants and it can be also used as a monitoring factor.

Desarrollo de recubrimientos inteligentes de base de metales de transición

Este trabajo tiene como objetivo estudiar las propiedades estructurales y magnéticas de diferentes películas delgadas anisótropas de permalloy. Algunas de las muestras a estudiar han sido depositadas con diferentes velocidades de deposición, y otras de ellas se han depositado sobre diferentes capas de base sobre el sustrato. Todas ellas han sido producidas mediante pulverización catódica.

Estandarización de un bioensayo con Cucumis sativus para la determinación de la fitotoxicidad de metales en suelos y aguas

Los bioensayos con plantas son una herramienta indispensable para la evaluación de la toxicidad de los suelos. Gran parte de la variabilidad que dificulta su generalización y la interpretación de resultados radica en la falta de un protocolo estandarizado y común que elimine las variables asociadas a las condiciones experimentales, al germoplasma vegetal y a los bioindicadores relevantes de toxicidad que existen entre los bioensayos tradicionales con plantas. En nuestro estudio proponemos un bioensayo que permite de una forma sencilla, barata y efectiva cuantificar el efecto fitotóxico de los contaminantes en suelo y agua. La estandarización del material vegetal, las condiciones del ensayo y el análisis de imagen permiten mayor fiabilidad y una economía de tiempo y esfuerzo en estos bioensayos. En este estudio se presentan los resultados de toxicidad de Zn, Cd y Pb en disolución y suelos mineros mediante marcadores de biométricos, fisiológicos y génicos de Cucumis sativus.

Nuevos vanadatos híbridos de metales de transición. Síntesis hidrotermal, estudio estructural y de sus propiedades espectroscópicas y magnéticas

267 p.