947 resultados para Érase una vez
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El presente trabajo analiza el proceso de internacionalización y la estrategia de marketing llevados a cabo por la cooperativa industrial vizcaína Batz. Mediante ello se ha tratado de evaluar la forma en que ha actuado la empresa en relación a ambos aspectos a lo largo de su trayectoria. El trabajo comienza con unos breves apuntes dedicados a presentar algunos aspectos teóricos sobre la internacionalización de empresas y las estrategias de marketing. Una vez analizados los rasgos principales de la cooperativa objeto de estudio en el segundo capítulo, los capítulos tercero y cuarto abordan el análisis del proceso de internacionalización y la estrategia de marketing seguidos por la empresa, respectivamente. Del estudio realizado se concluye que la empresa ha seguido un proceso de internacionalización en el que destaca la coherencia entre los retos planteados en cada momento y las respuestas dadas, las cuales han sido acompañadas y respaldadas por decisiones de marketing acertadas.
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El objetivo principal de este trabajo consiste en conocer el valor de la empresa mediante diferentes métodos de valoración. La valoración de las empresas es una herramienta muy importante para conocer el valor real de las empresas y no el valor que obtenemos mediante sus datos más próximos (balance etc.). En este periodo de crisis, la compra/venta de todo tipo de empresas está a la orden del día y el conocer su precio exacto por el cual vender/comprar la empresa puede marcar el éxito o fracaso de la transacción. En este trabajo calcularemos el valor de la cooperativa Eroski. Dicha empresa no se encuentra en sus mejores momentos y resulta interesante ver si realmente es conveniente liquidar la empresa etc. Para llegar a esa valoración final, primero se realizara un análisis del entorno de Eroski mirando por un lado la economía española y por otro lado el sector de la distribución. Donde se estudiara la situación de Eroski frente a su competencia así como el análisis del consumo de las familias, salarios etc. También se tendrá en cuenta la situación interna mediante un análisis económico-financiero. Posteriormente, calcularemos las tasas de actualización para calcular los valores corregidos de los balances y de esta forma se utilizará distintos métodos del cálculo del valor de la empresa Eroski, entre ellos utilizaremos el método patrimonial, el método de flujos de caja y el método bursátil. Por último, una vez obtenidos todos lo resultados, se presenta las concusiones y el valor estimado de la empresa en cada método.
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[ES]Este proyecto pretende plantear una solución viable y que, por tanto, resulte económicamente rentable, para la gestión de los lodos de depuradora generados en una estación de tratamiento de aguas residuales. Así, este documento se centrará, por una parte, en realizar un acercamiento al mundo de la depuración de aguas residuales y en estudiar los distintos procesos y tratamientos que se llevan a cabo en una depuradora, y por otra, planteará la valorización energética de los lodos mediante su combustión en una planta de generación de energía eléctrica como la solución al problema de gestión que suponen, no sin antes haber valorado las distintas alternativas posibles en cuanto a la salida que se les podría dar a estos fangos. De esta forma, la base del proyecto, una vez se haya optado por la alternativa de la valorización energética como la opción a desarrollar, consistirá en plantear los principios y fundamentos necesarios para el diseño de la planta de generación de energía eléctrica mediante lodos de depuradora que se pretenderá instalar. Se realizará, por tanto, una descripción de la planta generadora de electricidad detallándose el proceso que se llevará a cabo en la misma. Asimismo, se realizará el dimensionamiento de los diferentes equipos que tomarán parte en dicho proceso. Para finalizar, se planteará el estudio económico y de rentabilidad del proyecto que constituirá la creación de una planta de generación eléctrica mediante lodos, con el fin de comprobar el grado de viabilidad del mismo, y se analizarán los posibles riesgos a los que puede exponerse un proyecto de este tipo.
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El siguiente trabajo consiste en el desarrollo de un plan de marketing para la apertura de un centro franquiciado de la empresa Fitness19 en la localidad de Algorta, Getxo. Se trata de una franquicia española que basa su actividad en la instalación de centros deportivos de Fitness “Low Cost”, es decir, de bajo coste para el usuario. Con esto lo que pretenden es diferenciarse del resto de empresas de su sector ofreciendo unos servicios especializados a bajo coste. La filosofía que siguen es la de ofrecer solo fitness, que es lo que realmente busca el cliente, al mejor precio. De esta manera, presentaremos el proyecto, analizaremos el entorno de la empresa (tanto genérico como específico) y su situación interna con el objetivo de definir las amenazas, oportunidades, debilidades y fortalezas que presenta. Para ello examinaremos el ámbito geográfico en el que se planea su implantación y su mercado y detallaremos los servicios que pone a nuestra disposición la franquicia. Una vez realizado este análisis y diagnóstico se procederá a la elaboración de las estrategias de marketing y se detallará un plan de acción y control para su consiguiente aplicación. El objetivo del análisis y la planificación es llevar a cabo la tarea de crear y poner en funcionamiento de forma exitosa el centro franquiciado siguiendo un plan estructurado y preciso. Este plan está diseñado para abarcar todas las estrategias y acciones necesarias desde el momento de creación de la empresa, que será en Mayo de 2015, pasando por la ubicación, obra del local y su apertura hasta la época navideña de ese mismo año. De esta manera se definen en el trabajo dos etapas muy diferentes: etapa preapertura y etapa de actividad.
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[ES]El objetivo principal de este proyecto se centra en modelizar correctamente la capa límite sobre el perfil alar donde se produce la transición del régimen laminar al régimen transitorio. Como objetivo secundario se encuentra el afianzamiento de las bases teóricas de mecánica de fluidos obtenidas en la escuela y la adquisición de más conocimientos relacionados con la aerodinámica, concretamente con la capa límite. En una primera parte se tratarán los conceptos generales de los perfiles alares y se hará una breve introducción a los distintos tipos de mallado existentes. También se explicará el concepto de capa límite y todo lo relacionado con ella. A continuación, se establecerán los criterios de selección del modelo de turbulencia más adecuado y se mostrarán los resultados obtenidos de los distintos tipos de modelos de turbulencia anteriormente mencionados. Una vez seleccionado un modelo de turbulencia se profundizará en su estudio, aplicándolo a varios perfiles NACA. Se analizarán los resultados obtenidos y los errores y se buscarán posibles soluciones. Finalmente, se procederá a sacar las conclusiones del modelo escogido y se comparará con una serie de ensayos experimentales con objeto de poder validarlo.
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[ES]El análisis y la resolución de casos prácticos engloban la resolución de casos prácticos, el análisis de las alternativas posibles o la resolución de casos concretos. En este trabajo se pretende analizar y resolver un caso concreto, de un proceso de producción de hidrógeno. Una vez expuesto el contexto y el análisis de las alternativas, se procederá a explicar el proceso de obtención y aprovechamiento del hidrógeno. El hidrógeno, se obtendrá a partir de la gasificación d la biomasa. Una vez se haya obtenido la corriente de hidrógeno, esta alimentará a una pila de alta temperatura tipo SOFC, para obtener generación combinada de calor y electricidad.
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El proyecto propuesto consiste en el desarrollo de una aplicación para el sistema operativo móvil Android OS que permita al usuario crear y editar composiciones musicales mediante pentagramas que una vez finalizados serán exportados al formato abierto MusicXML, de manera que puedan ser reproducidos, editados y visualizados en herramientas de terceros que soporten dicho formato. Este proyecto consta de diversas fases, a saber, la planificación integral del proyecto, tanto temporal como económica, el diseño de la aplicación con el correspondiente estudio de las tecnologías requeridas para el mismo, la implementación del código que compondrá la aplicación, las pruebas que garanticen en la medida de lo posible la calidad y robustez del código y la defensa de este proyecto ante un tribunal. Este proyecto no tiene como única finalidad la creación de la aplicación mencionada, sino que también tiene por objeto la puesta en práctica de los conocimientos adquiridos durante el período formativo y conocer de primera mano las distintas facetas que compone un proyecto, como son los problemas inesperados que surgen y la capacidad para resolverlos de manera eficaz en el menor tiempo posible, la gestión del tiempo invertido en las tareas y el cuidado de los detalles, que son de gran importancia y que necesitan una gran cantidad de tiempo para su limado.
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Desde o Século passado, a figura feminina tem o seu papel e o seu comportamento social impostos pelo meio do qual ela faz parte. Atualmente, embora muitas mudanças tenham ocorrido, ainda há expectativa quanto às atitudes e aos padrões femininos, sejam eles de forma física, de vestuário ou de comportamento. Na busca de tais modelos de sucesso, a mulher vê como aliada a revista femininaNão podemos nos esquecer, a respeito das revistas femininas, que historicamente as mulheres tiveram acesso à leitura e à escrita bastante tempo depois dos homens. Por esse motivo, talvez, elas possam ser vistas como uma presa fácil aos olhos dos editores, uma vez que seu contato com a leitura é recente e consequentemente sua análise crítica menos desenvolvida. Um dos recursos utilizados pela mídia, entre elas as revistas femininas, é explorar ao máximo o caráter argumentativo dos termos. Uma vez que seu objetivo maior é exercer influência sobre a população, ela utiliza o poder de persuasão das palavras para alcançar tal objetivo.A dissertação que ora apresento teve por objetivo não só a busca dos artifícios argumentativos utilizados nessas revistas, a fim de convencer a mulher do Século XXI de que seu papel permanece inalterado, mas também mostrar que esse tipo de manifestação escrita deve ser lido com maior cuidado e maior atenção diferentemente do que da atitude habitual de leitura de textos cujo único objetivo é apenas entreter
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Duración (en horas): Más de 50 horas Destinatario: Profesor
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Duración (en horas): Más de 50 horas Destinatario: Estudiante y Docente
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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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Proyecto de Fin de Grado, especialidad en Computación. Se ha desarrollado un software en ROS para detectar posturas y movimientos de personas. Para ello, se utiliza la información del esqueleto proporcionada por el sensor Kinect y la biblioteca OpenNI. Se ha realizado un enfoque basado en técnicas de aprendizaje supervisado para generar modelos que clasifiquen posturas estáticas. En el caso de los movimientos, el enfoque se ha basado en clustering. Estos modelos, una vez generados, se incluyen como parte del software, que reacciona ante las posturas y gestos que realice un usuario.
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170 p.
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250 p. + anexos
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162 p.