60 resultados para ACTIVO DE INFORMACIÓN


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[ES] La parte práctica de esta tesis se centra en un proyecto ERASMUS realizado en el Monasterio de San Prudencio de Monte Laturce (Clavijo, La Rioja). Dicho proyecto aparece descrito en varios registros de este mismo repositorio a los que se puede acceder a través del siguiente:

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Desarrollo de aplicación para dispositivos con sistema operativo Android 4.x para consulta de documentación técnica y nueva funcionalidad para la realización de instrucciones. Español.

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Nivel educativo: Grado. Duración (en horas): Más de 50 horas

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Español: Ante el creciente impacto que tiene la actividad de los mercados y entidades cotizadas en el entorno económico y financiero, ha surgido la necesidad de que las empresas comuniquen a sus inversores y otras partes interesadas una amplia gama de información. Para atender a esta necesidad ha sido necesaria una evolución de la legislación, de manera que se han producido numerosos cambios legislativos durante los últimos años. Además, la evolución de la legislación no sólo ha tenido como objetivo atender a la necesidad de información sino que también ha supuesto un mecanismo de transparencia de la actividad empresarial. En este trabajo se analizará la normativa específica existente para este tipo de sociedades, con respecto a las obligaciones de suministro de información públicamente. En este sentido, se ha dejado de lado la información correspondiente a las cuentas anuales, centrando la investigación en la información específica que las sociedades anónimas cotizadas deben publicar. Posteriormente, se analizará la información contenida en los informes de gestión de dos empresas cuyos valores están admitidos a cotización, para poder así comprobar en qué medida las empresas cumplen con las recomendaciones de elaboración vigentes.

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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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Hoy en día las organizaciones sin ánimo de lucro no pasan por un buen momento incluso siendo este mismo instante cuando más se las necesita debido a la crisis tanto a nivel nacional como internacional.En el presente trabajo se estudiará esta negativa situación de las nombradas entidades sin ánimo de lucro explicando primero qué son y para qué son creadas, para más tarde enfatizar el porqué de esta situación. Finalmente, se analizarán las diferentes herramientas que estas entidades utilizan para transmitir confianza a la sociedad.

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Las entidades sin fines de lucro constituyen unas de las figuras más importantes de nuestro entorno. Su existencia es imprescindible ya que atienden a las necesidades de la sociedad. Desempeñan infinidad de actividades que contribuyen al bienestar social, al desarrollo de países, a la protección del medio ambiente, etc. El Sector No Lucrativo presenta peculiaridades que lo diferencian del resto de entidades pertenecientes al Mercado y al Sector Público. Estas características han de ser consideradas por las mismas a la hora de desempeñar sus actividades y de satisfacer a las demandas de información de los usuarios. La rendición de cuentas es fundamental para las ESFL, sin embargo, la normativa legal se ciñe únicamente sobre el área económico-financiera, dejando sin cubrir el resto de áreas de la entidad. Informar sobre el área social supone una labor esencial para este tipo de entidades, dado el impacto que producen sobre la sociedad. En el presente estudio se analizarán las mencionadas particularidades de las ESFL y se estudiarán un conjunto de mecanismos voluntarios que las entidades del Sector pueden emplear con el fin de mostrar transparencia en su gestión y atender a las necesidades de los usuarios.

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[ES] Es obligatorio para las empresas cotizadas que cuenten con una página web para atender el derecho de información de los accionistas, y donde difundir información relevante y obligatoria. Por ello, se creó la normativa necesaria para regular tanto la información mínima que las empresas debían aportar en sus webs, como los requisitos técnicos y jurídicos que dichas páginas debían poseer. No obstante, todas las empresas no presentan la misma información en sus webs, ya que muchas no se limitan a presentar solo la exigida por ley, y ésta puede ser más o menos útil para los usuarios. Por eso, es imprescindible poder conocer de alguna forma la transparencia que las empresas muestran a los usuarios en sus páginas web y en particular a los accionistas, si existe asimetría informativa o no, y saber cuál es el grado de calidad de la información presentada, así como la confianza que se puede tener en la misma.

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Grados recientes como el de Ingeniería Informática de Gestión y Sistemas de Información, y dada la orientación profesional que va a obtener el/la egresado/a para su incorporación en el mundo de la industria, requieren una revisión del enfoque de determinadas materias relativas a, por ejemplo, cómo está estructurado un computador, qué elementos lo conforman, cómo interactúan, etc.; dando al alumnado una visión amplia sin buscar la exhaustividad (propia de otras titulaciones) pero manteniendo un rigor tanto técnico como científico según la materia tratada.

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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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En este trabajo se analizan las decisiones de un agente económico, en un contexto incierto, cuando puede obtener o recibir información que resuelve total o parcialmente la incertidumbre a la que se enfrenta. La recepción de información permite al agente adaptar su decisión al mensaje proporcionado por esa información salvo que haya optado por una alternativa irreversible.

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[ES] Los recursos de naturaleza intangible se han convertido en los bienes más importantes que poseen las empresas para generar riqueza de manera sostenible, en concreto el Capital Humano. Sin embargo, el éxito y supervivencia de la empresa se encuentra sometida a la aprobación de sus grupos de interés (stakeholders). Por ello, las empresas deben adoptar medidas para garantizar que sus actuaciones sean percibidas por sus stakeholders como legítimas; una manera para legitimarse es mediante el suministro de información voluntaria. Por tanto, bajo el marco de la Teoría de la Legitimidad y de los Stakeholders, nuestro objetivo es analizar cómo las empresas españolas están informando de manera voluntaria sobre su Capital Humano en los informes anuales, desde una doble perspectiva informativa: la generación de intangibles (conocimiento) y la responsabilidad social. Así, usando la metodología del análisis de contenido, la evidencia empírica muestra que las empresas españolas suministran escasa información acerca de su Capital Humano, siendo los temas relacionados con la formación y el desarrollo de los empleados los más divulgados. No obstante, y con respecto a la responsabilidad social, hay que destacar la tendencia alcista por parte de las empresas a suministrar información relativa a la política de igualdad y diversidad, la prevención de riesgos laborales y las relaciones entre empleadores y empleados.

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[ES]En 2013 la Comisión Nacional del Mercado de Valores (CNMV) publicó una Guía para el Informe de Gestión de las empresas cotizadas españolas con el ánimo de mejorar la calidad de la información que presentan estas empresas. En este trabajo presentamos una valoración crítica sobre algunos aspectos normalizadores de dicha guía y después proponemos una batería de indicadores que ayuden a realizar el análisis, tanto de los contenidos informativos como del cumplimiento de los principios y reglas que recomienda la guía (CNMV, 2013). Esta no es de aplicación obligatoria, por lo que su implementación no está garantizada por parte de las empresas. En todo caso, los listados de indicadores que proponemos pueden ser de utilidad, tanto con fines de investigación para analizar el nivel de información divulgado, como para las propias entidades, cotizadas y no cotizadas, que quieran cumplir con los requisitos de calidad recomendados a la hora de preparar sus Informes de Gestión.