El Herbario: significado, valor y uso.

En la historia de la vida sobre la Tierra, el capítulo que trata sobre el almacenamiento y conservación de las plantas se escribe en los dominios del herbario. El herbario posee los ejemplares que documentan la exploración del hombre sobre la superficie terrestre, de manera que no sólo existe el documento escrito que narra la historia del explorador sino que tenemos el privilegio de tocar esos objetos o especímenes. Así, cada herbario en el mundo posee un tesoro escondido de especímenes históricos que son el fiel testigo de las hazañas de un investigador o de una exploración a algún lugar remoto. En las últimas dos décadas el medio en el que se desarrollan los herbarios y sus colecciones han subrido cambios muy significativos, los que a su vez han ejercido presiones sobre quienes manejan las colecciones. Algunos de estos cambios son la disminución de los aportes económicos a los herbarios, el cambio en el uso de la evidencia morfológica hacia la molecular en los estudios sistemáticos y la pérdida acelerada de la biodiversidad que trae aparejada la necesidad urgente de realizar inventarios florísticos. En una era de extinción de biotas, las colecciones valiosas como son hoy día, serán aún más valiosas en los años por venir. Las colecciones representan el testigo imprescindible para la ciencia y el vehículo para llegar a las posibles soluciones. Es por ello que el conocimiento del significado, valor y uso del herbario y sus colecciones reviste una vital importancia para la ciencia y para la sociedad.

Size composition of catches of Yellowfin tuna in the Japanese long-line fishery in the eastern tropical Pacific east of 130°W

ENGLISH (pgs. 267-283): In the spring of 1963, the senior author, who is a member of the staff of the Nankai Regional Fisheries Research. Laboratory, Fisheries Agency, Japanese Government, came to the Institute of Marine Resources of the University of California as a visiting investigator, bringing with him catch statistical data from the fishery in the eastern Pacific, which had been collected at the Nankai Regional Fisheries Research Laboratory (NRFRL) through September 1962, in order to conduct studies of these data in collaboration with the junior author, and with investigators of the InterAmerican Tropical Tuna Commission. A general review of the long-line fishery, based on the catch statistics of the commercial fishing fleet has been published by Suda and Schaefer (1965). In this paper we present an analysis of data respecting the size-composition of yellowfin tuna taken on long-line gear throughout the eastern Pacific between 1958 and 1962, and make some comparisons with data on size-composition of yellowfin tuna taken in the near-surface fishery, by bait boats and purse-seiners, in waters adjacent to the American coast. As has been shown by Suda and Schaefer (1965), the long-line fishery in the eastern Pacific is primarily directed toward the capture of bigeye tuna. However, considerable quantities of yellowfin tuna are also taken on this gear, and, in addition, there are substantial catches of albacore and of several species of spearfishes in some parts of the range of this fishery. Information respecting the catch rates of yellowfin tuna, and information respecting the size-composition of the stock of yellowfin tuna being exploited by the long-line fishery, is of particular interes~" because the yellowfin tuna population of the eastern Pacific is also subject to an intensive fishery by baitboats and purse-seiners which capture this species, together with skipjack, near the surface along the coast of the Americas, and around the outlying islands, in the region of California to northern Chile. SPANISH (pgs. 311-329): En la primavera de 1963, el autor principal, quien es miembro del personal del Nankai Regional Fisheries Research Laboratory, Fisheries Agency del gobierno japonés, vino al Institute of Marine Resources de la Universidad de California en calidad de investigador visitante y trajo consigo datos estadísticos de las capturas de la pesquería en el Pacífico oriental, que habían sido recolectados en el Nankai Regional Fisheries Research Laboratory (NRFRL) hasta septiembre de 1962, con el fin de hacer estudios de esos datos en colaboración con el coautor y con investigadores de la Comisión Interamericana del Atún Tropical. Una revisión general de la pesquería con palangre, basada sobre las estadísticas de captura de la flota pesquera comercial, ha sido publicada por Suda y Schaefer (1965). En este trabajo presentamos un análisis de los datos correspondientes a la composición de tamaños del atún aleta amarilla capturado con equipo palangrero en todo el Pacífico oriental, entre 1958 y 1962, y hacemos algunas comparaciones con los datos sobre la composición de tamaños del atún aleta amarilla cogido en la pesquería superficial cercana, por barcos de carnada y rederos en aguas adyacentes a la costa americana. Como ha sido demostrado por Suda y Schaefer (1965) la pesquería con palangre en el Pacífico oriental tiene como principal objeto la captura del atún ojo grande. Sin embargo, considerables cantidades de atún aleta amarilla son capturadas también por este equipo y, además, hay también considerables capturas de albacora y de diversas especies de peces-espada en algunas partes de la región que abarca esta pesquería. La información respecto a las tasas de captura del atún aleta amarilla, y la relativa a la composición de tamaños del stock de esta especie que explota la pesquería con palangre, es de particular interés, a causa de que la población de atún aleta amarilla del Pacífico oriental es también objeto de una pesca intensiva por barcos de carnada y rederos que capturan esta especie, junto con el barrilete, cerca de la superficie a 10 largo de la costa de las Américas y alrededor de las islas mar afuera, en la región desde California hasta el norte de Chile.

Traducciones (censuradas) de teatro inglés en la España de Franco. TRACE: Una perspectiva histórica

[ES] La historia del teatro traducido en la España del siglo XX está aún por escribirse. Este segmento de nuestra cultura traducida ha sido tradicionalmente ignorado en las historias del teatro español. Por suerte, lo que hace sólo veinte años se describía como un páramo investigador es hoy un terreno mucho mejor abonado y roturado. Las investigaciones sobre teatro traducido que han visto la luz progresivamente en estos años nos permitirán en breve escribir y documentar la historia del teatro traducido. Se ofrece en este artículo una visión del modo en que podría acometerse esa tarea,partiendo de lo ya investigado en el proyecto TRACE desde la perspectiva de lo archivado por la censura (de teatro) en la época de Franco.

Pruebas diagnósticas e inmunoterapia sublingual en la alergia al látex

316 p. (Bibliogr. 301-316)

Una aproximación psicosocial al conflicto vasco. Construyendo la paz en espacio abierto

450 p.

Análisis de sensibilidad en los procedimientos de calibración de robots de cinemática paralela Aplicación al mecanismo 5R

[ES]Este proyecto investigador tiene como objetivo el ayudar con la calibración del mecanismo de cinco pares de rotación montado en el taller de Ingeniería Mecánica de la ETSI de Bilbao. En primer lugar se estudiarán los algoritmos de optimización prestando especial atención a la comparativa entre Levenberg-Marquart y Gauss-Newton. Se realizarán estudios en Matlab para concluir cuál de los dos es más eficaz tanto en rapidez como en precisión. El que sea más adecuado se implementará en un programa para la calibración del mecanismo 5R. En segundo lugar se estudiarán los índices de observabilidad. Los estudios que se han realizado sobre ellos hasta ahora son poco concluyentes asique se intentará aclarar su utilidad y determinar cuál es el que conviene utilizar en este caso. Para ello se deberá programar la resolución del problema cinemático inverso. Por último se presentarán los resultados y las conclusiones correspondientes. Se propondrá también un plan de desarrollo de una línea de investigación futura que partirá con este trabajo como base.

Estudio del comportamiento aerodinámico de un alerón trasero de un monoplaza tipo Formula Student

[ES]El proyecto investigador tiene el objeto el estudio del comportamiento de un perfil aerodinámico frente a un flujo turbulento, en este caso el aire. Se trata de evaluar las presiones que se ejercen sobre dicho perfil, que será un alerón de monoplaza tipo Formula Student, para comprobar si aporta alguna mejora en el comportamiento del monoplaza la introducción de este paquete aerodinámico. Con la introducción de este perfil en el monoplaza se pretende ganar un mayor agarre en el paso por curva siendo la resistencia al avance en recta la mínima posible, ya que lo que se pretende es hacer el recorrido del circuito en el menor tiempo posible. Por tanto hay dos variables a tener en cuenta a la hora de diseñar el alerón, por un lado esta mejorar el agarre de los neumáticos sobre el asfalto al tomar una curva, lo que nos permitirá tomar la curva a mayor velocidad y por tanto en menos tiempo, y por otro lado, la oposición que el alerón ejerce en el avance en recta disminuyendo su velocidad máxima. En resumen, se trata de comparar la fuerza horizontal y la fuerza vertical que el aire ejerce sobre el perfil aerodinámico a introducir en el monoplaza y evaluar si es beneficioso para este, es decir, si añadiendo dicho perfil se realiza el trazado del circuito en menor tiempo que sin él. Para ello se realizarán simulaciones con un software de modelado físico de flujos y turbulencias sobre un diseño de un alerón dado, con diferentes tipos de flujo, de forma que se asemeje de mejor forma a las condiciones de la pista y se obtendrán los resultados de las presiones que el flujo de aire ejerce sobre las superficies del perfil. Después se obtendrán las fuerzas puntuales vertical y horizontal y se analizaran los datos obtenidos. Deberán tenerse en cuenta, además de los resultados obtenidos, los materiales a emplear a la hora de su fabricación, el proceso de dicha fabricación y el coste que supone tanto el proceso como los materiales empleados.

Análisis y comparación de movimientos parásitos en manipulador paralelo 1-PRS 2-PRU

[ES]En primer lugar, se analiza el contexto investigador tratando de aportar una visión global de la situación de la I+D en el entorno geográfico, institucional y departamental. En segundo lugar, describo de forma somera la temática general en la que enmarcar las dos propuestas de investigación mencionadas así como los objetivos generales que me planteo. En tercer lugar, se realiza aquí una recopilación de los resultados previos de investigación que sirven de punto de partida para las líneas de investigación que aquí se plantean. En último lugar, planteo las dos líneas de investigación con detalle, incluyendo los fundamentos necesarios y resultados preliminares

Recorrido y reflexiones en torno al pensamiento analítico de Georges Laplace: movimiento, interdependencia y arquetipos en la construcción de una arqueología científica

Homenaje a Georges Laplace, realizado en Vitoria-Gasteiz el 13,14 y 15 de noviembre de 2012. Edición a cargo de Aitor Calvo, Aitor Sánchez, Maite García-Rojas y Mónica Alonso-Eguíluz.

Formación y trayectorias profesionales de los artistas vascos. Resultados de la encuesta INNOCREA 2013

El presente informe es uno de los resultados obtenidos en el proyecto de investigación INNOCRE2, Mapa de la Innovación en el Sector Cultural y Creativo de Euskadi, que fue financiado por el Departamento de Industria, Innovación, Comercio y Turismo del Gobierno Vasco (Programa Saiotek, Proyecto S-OA12UN002, 2012-junio 2014). El investigador principal de dicho proyecto fue Javier Echeverría Ezponda (investigador Ikerbasque adscrito al Departamento de Sociología 2 de la Universidad del País Vasco/Euskal Herriko Unibertsitatea). Auxkin Galarraga es profesor del Departamento de Sociología y Trabajo Social de dicha universidad y Liliana Rocca es investigadora y consultora en el área de Psicología Social. El proyecto desarrolló una de las líneas de investigación del grupo de Alto Rendimiento (Nivel A) del sistema universitario vasco “INNOLAB: Innovación, Cambio, Complejidad”, dirigido por Ander Gurrutxaga. A pesar de que la elaboración de este informe ha sido realizado por los firmantes de este artículo, tanto en el diseño metodológico de la encuesta, como en la posterior explotación de los datos también ha participado un amplio grupo de investigadores coordinado por Javier Echeverría y compuesto por orden alfabético por Antón Arana, Marcos Engelken, Andrea Estankona, Ander Gurrutxaga, Zuhar Iruretagoiena, Arantza Lauzirika, Álvaro Luna, Iñaki Martínez de Albeniz, Lucía Merino y Natxo Rodríguez.

Leitura em meios virtuais: uma análise qualitativa do trabalho e desafios docentes

A presente pesquisa caracteriza-se como um estudo de caso com abordagem qualitativa de análise, tem caráter etnográfico e propôs dar continuidade à pesquisa de Guimarães (2008). Analisamos, na prática de sala de aula de um sujeito selecionado entre os participantes do estudo anterior, como ocorre o trabalho com leitura em E/LE em materiais retirados da Internet. Para isso, partimos dos seguintes questionamentos: (1) o que, para o professor, em sua prática, representa desenvolver atividades de leitura; (2) que tratamento recebem os textos oriundos do meio virtual e (3) como a prática, objetivos e base teórica deste professor se relacionam com a sua auto-imagem que aparece no questionário (Guimarães, 2008).Selecionamos o sujeito em função de sua alta adesão ao uso de recursos informáticos e sua proposta de ensino-aprendizagem de espanhol como língua estrangeira com base no desenvolvimento da compreensão leitora. Utilizamos como instrumentos de coleta de dados: o questionário da pesquisa de Guimarães (2008), os materiais utilizados pelo professor nas aulas observadas, as fontes originais virtuais dos textos presentes nesses materiais, o diário de campo do pesquisador, as gravações em áudio das aulas analisadas e a entrevista realizada com o informante. Nossa base teórica está fundamentada nos modelos de leitura, em especial o sócio-interacional, na caracterização da leitura em meio digital e no processo de transposição didática. Verificamos que o sujeito, baseado na teoria sócio-interacional, tem como foco de seu trabalho o desenvolvimento da habilidade leitora de seus alunos. Analisamos, também, as mudanças promovidas nos textos usados em sala de aula, em comparação às suas versões originais digitais. Discutimos que essas alterações podem trazer as consequências para o desenvolvimento da competência leitora e compreensão do texto por parte dos leitores-alunos, tanto no que se refere, especificamente, ao seu letramento digital como no processo leitor como um todo. Sobre a auto-imagem que o professor constrói através do questionário de Guimarães (2008), concluímos que, como apontado, o informante desenvolve um trabalho direcionado ao ensino de leitura em E/LE, assim como tem a internet como uma das principais fontes de materiais para suas aulas. Porém, a estrutura da instituição na qual atua o limita e altera as formas de trabalhar com textos e ferramentas virtuais, proporcionando uma mudança no perfil definido pelo questionário

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)

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).

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.

Measurement of polycyclic aromatic hydrocarbons in ambient air by fluorescence spectroscopic techniques

250 p. + anexos