46 resultados para GASES DEL EFECTO INVERNADERO


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El estudio de los impactos económicos de las políticas de control del cambio climático requiere del uso de modelos adecuados. Este artículo presenta un Modelo Dinámico de Equilibrio General Aplicado tipo Ramsey. El modelo implementa un mercado de permisos de emisión perfecto que garantiza una reducción de emisiones eficiente y efectiva, permitiéndonos calcular los costes económicos mínimos asociados al control de las emisiones de efecto invernadero. Además aprovecha al máximo la disponibilidad de datos existentes en España 1) utilizando una matriz de contabilidad social (o SAM) energética mediante la integración de la información económica de la Tablas Input-Output y la información energética de los Balances Energéticos y 2) considerando todas la emisiones sujetas a control además del CO2. Los MEGAs dinámicos son inéditos en cuanto a su elaboración y aplicación en España y permiten investigar ex-ante los efectos de políticas públicas en el medio y en largo plazo.

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INGLÉS:Juvenile mussels (Mytilus galloprovincialis) were collected and maintained under restrictive and optimal feeding conditions. After 7 months maintenance fast and slow growth individuals were selected for study of the effect of diet quality on selection efficiencies and absorption of food in fast and slow growth mussels. The objective of this experiment was to confirm that the physiological components responsible for the differentiation were able to vary according to the environmental conditions. The analysis of physiological traits indicates that under conditions of abundant food efficiency and absorption efficiences are the main factors that explain the differences in growth. Under conditions of restricted food are physiological differences that give rise to differences in growth.

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[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.

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228 p. : il. Nota: Otro título en Teseo: "la modulación selectiva de los niveles de glutatión con l-2-oxo-4-tiazolidina carboxilato aumenta la eficacia de la interleucina-2 e incrementa el beneficio terapéutico de la bioquimioterapia del melanoma metastático"

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170 p.

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128 p. Retirada a solicitud de la autora 03/03/2016

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El propósito de este trabajo de fin de grado es realizar un análisis acerca del efecto de la crisis actual sobre las entidades sin fines lucrativos. Las entidades del Tercer Sector, al igual que las entidades tanto del sector público como privado, se han visto fuertemente afectadas por la crisis que se atraviesa desde 2008. Los efectos de la crisis se han podido ver reflejados en distintos aspectos de las entidades sin ánimo de lucro, pero entre los más importantes se encuentran la dificultad de obtener financiación, y el fuerte aumento de la demanda de este sector, debido a que las personas o colectivos que se han visto afectados han acudido a estas entidades para buscar ayuda. Con lo que respecta a la financiación previa a la crisis, la gran mayoría de las entidades no lucrativas venían siendo financiadas por el sector público, lo cuál ha supuesto un gran problema ya que toda esa financiación pública se ha visto reducida a causa de la crisis, y por tanto estas entidades tienen que esforzarse en captar financiación privada. Para que la obtención de esta financiación sea más fácil se recomienda que la información que suministran estas entidades sea transparente y así se genere confianza. El aumento de la demanda de este sector está provocando en las entidades sin ánimo de lucro la prioridad de la cobertura de las necesidades básicas de los individuos.

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[EN] The main goal of this study is to analyze how organizational commitment has a mediating effect on the relation between transformational leadership and organizational trust. Therefore we developed an organization analysis based on a survey that was used to collect primary data from a sample of 58 employees. We obtained a 71% response rate and these data were analyzed using quantitative methodological techniques and linear regression. The research was conducted at the Serralves Foundation (Porto, Portugal) to empirically test the proposed research model and its hypotheses. The empirical results confirm that transformational leadership positively enhances organizational trust. However, transformational leadership and organizational trust are not significantly influenced by organizational commitment, thus not having a mediating effect on this relationship. Such results assume particular relevance because they become a basis for comparative studies in similar organizations. This study brings some theoretical contributions to the literature by analyzing the mediating effect of organizational commitment on the relation between transformational leadership and organizational trust in cultural organizations and has also some practical management implications, as it draws attention to the importance of a set of practices, job satisfaction oriented, which can effectively lead to organizational commitment intervention in the relationship between transformational leadership and organizational trust.

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[ES] La enfermedad celíaca (EC) es una enteropatía autoinmune de predisposición genética, producida por la ingestión en la dieta de péptidos derivados de cereales como el trigo o la cebada. Aunque se creía que afectaba casi de forma exclusiva a los individuos europeos (1%), actualmente se conocen casos en todo el mundo. El modelo patogénico se centra en los mecanismos de la inmunidad adaptativa dependientes de la estimulación de linfocitos T CD4+ reactivos, pero existe además un efecto tóxico directo del gluten sobre el epitelio intestinal, dependiente de la inmunidad innata. La participación de la Genética en la susceptibilidad a la enfermedad es conocida desde hace tiempo, siendo el locus HLA el que explica aproximadamente el 40% del componente genético de la enfermedad. Para tratar de identificar otros genes con susceptibilidad, se han venido realizando múltiples esfuerzos durante los últimos años. Uno de los últimos, llevado a cabo en 2011, fue el Proyecto Immunochip. En él, se analizaron más de 200.000 variantes y se descubrieron 13 nuevos loci de riesgo para la EC, que junto con los descubiertos en anteriores trabajos y el locus HLA, daban un total de 40 loci de riesgo. Entre ellos, se encontraba la región que ocupa el gen LPP . Localizado en el cromosoma 3, un estudio reciente lo vincula con los procesos de adhesión celular en el intestino. En el presente trabajo, se ha estudiado el efecto de la gliadina sobre la expresión del gen de interés (LPP ) y el posible efecto de un silenciamiento del mismo sobre dos genes relacionados con las uniones celulares (ACTB y TJP1). En el caso de la gliadina, no se halló un cambio significativo en la expresión del gen. Mientras, los resultados del efecto del silenciamiento fueron dispares, no siendo concluyentes para el gen ACTB, pero encontrando una posible asociación entre los genes LPP y TJP1.

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[ES] Este trabajo profundiza en el estudio de los factores que influyen en la competitividad internacional de las nuevas empresas internacionales y, en consecuencia, en su resultado internacional. Aunando las disciplinas del emprendedurismo y del marketing internacional, se trata de remarcar la importancia del conocimiento relacional a través de la influencia de la orientación al mercado de la red en los resultados internacionales logrados por estas empresas en base al efector mediador de las ventajas competitivas. Los resultados obtenidos del contraste de hipótesis, mediante modelos de ecuaciones estructurales y análisis multi-muestra, confirman que la orientación al mercado de la red resulta determinante en la obtención de resultados internacionales superiores por parte de las nuevas empresas. Esta influencia se produce de forma indirecta a partir del efecto mediador de las ventajas competitivas en diferenciación y costes desarrolladas por las mismas. Este estudio extiende la investigación pasada en torno al emprendedurismo internacional, incluyendo nuevas aportaciones propias de la disciplina del marketing respecto a los antecedentes de la competitividad y los resultados de las nuevas empresas internacionales en los mercados exteriores. Además, los resultados obtenidos animan a emprendedores en el contexto internacional a considerar el valor explícito de otros factores distintos al conocimiento experiencial, que la empresa adquiere de forma gradual conforme se incrementa su experiencia en el mercado exterior, para darse cuenta del valor potencial que el conocimiento relacional asociado a la orientación al mercado de la red tiene como antecedente para la consecución de ventajas competitivas en el mercado internacional.

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133 p.