Análisis del concurso de acreedores y sus diferentes salidas

En este trabajo se ha tratado de explicar la importancia del concurso de acreedores, así como sus ventajas e inconvenientes. Se ha decido analizar dos empresas españolas que han pasado por esta situación pero que han tenido dos finales distintos. Para ello se han utilizado herramientas de predicción del fracaso empresarial: la solvencia, liquidez, endeudamiento, el modelo Z-Score de Altman y el estado de flujos reclasificado y los recursos generados, para evaluar la situación económico-financiera de ambas entidades. A pesar de la existencia de grandes igualdades entre ella, se ha detectado una diferencia importante basada en la apuesta de los administradores concursales por un plan de viabilidad que ha permitido alcanzar el convenio que se ha logrado firmar con los acreedores y mantener el principio de empresa en funcionamiento.

Balance de la política fiscal desarrollada en España en época de crisis. ¿Por qué elegir el camino contractivo?

The use of a contractive fiscal policy in times of crisis and austerity can lead to so many different opinion streams which can be, at the same time, very opposite with each other. The high budget deficit in some economies has forced the eurozone to implement austerity policies, meaning that the debate is now more alive than ever. Therefore, the aim of this paper is to analyze the effects of the implementation of a contractive policy during a crisis considering the case of Spain. The positive effects in financial markets were noticed due to the decrease of the risk premium and the payment of interests, and also thanks to the increase of trust towards Spain. This way, the reduction of the Spanish deficit was remarkable but in any case there is still a long path until reaching the limit of 3% of the GDP. Also, in the short run it is possible to see that the consolidation had contractive effects in the economic activity but, in the long run, the debate is among the defenders of the fact that austerity is followed by a growing period and the ones opposing to it due to the drowning effect produced by it.

Los diversos modelos de predicción de fracaso empresarial

Este estudio es una revisión de la literatura sobre la predicción del fracaso empresarial, definiendo en primer lugar el concepto de fracaso junto con sus limitaciones, y realizando un estudio sobre los modelos de predicción de fracaso empresarial más relevantes que hayan sido desarrollados en estos casi 100 años. Partiendo de unos modelos simples basados en el estudio y análisis de los ratios, hasta efectuar unas metodologías innovadoras, como el análisis multivariante, la aplicación de variables ficticias en los estudios, el modelo de regresión logit, y actualmente empleando programas informáticos basados en la inteligencia artificial utilizando las redes neuronales y los árboles de decisión.

Factores determinantes de las crisis financieras: un análisis cualitativo

A lo largo del siglo XX han sucedido un gran número de crisis financieras, y muchas de las que surgieron en épocas pasadas siguen teniendo repercusión en el contexto económico-financiero actual. En muchos aspectos, la crisis actual no ha sido muy diferente de acontecimientos que hemos visto en los mercados emergentes durante la última década, ya que vemos que se dan circunstancias similares en los comportamientos económicos y financieros que desembocan en las crisis. En este contexto, el objetivo principal de este estudio es identificar las causas comunes a los episodios de crisis más relevantes que han precedido a la crisis financiera actual y compararlos con los factores desencadenantes de ésta. Para ello, la metodología empleada es la analítico-sintética, que consiste en analizar el fenómeno objeto de estudio y sintetizarlo para obtener, finalmente, una serie de conclusiones. Las conclusiones de este trabajo señalan la existencia de dos clasificaciones de crisis en base a la literatura teórica: la primera, que las divide en bancarias, monetarias y financieras; y la segunda, que distingue entre modelos teóricos de Primera, Segunda y Tercera Generación. Todas ellas presentan además unas causas comunes que también han sido explicativas del episodio de crisis que estamos padeciendo actualmente.

Instituciones Microfinancieras y banca tradicional: diferencias en funcionamiento y resultados durante la crisis

Español: A finales del 2007 muchas entidades financieras comenzaron a mostrar cifras negativas en sus balances y tras la quiebra de entidades de gran peso económico como el banco Lehman Brothers en Estados Unidos en septiembre del 2008, el mundo se ha visto envuelto en una crisis económica de la que parece no verse el final. Las entidades financieras tradicionales han centrado sus esfuerzos en obtener las mayores rentabilidades posibles, invirtiendo sus recursos en activos muy arriesgados, que si bien en un principio generaban beneficios muy elevados, a día de hoy han hecho quebrar muchas entidades a nivel mundial y han provocado la pérdida de los ahorros de muchos ciudadanos. Ajenas a esto se encuentran las entidades microfinancieras, que con un enfoque muy diferente al de la banca tradicional, se han centrado en proporcionar financiación a aquellos que dada su situación económica y falta de garantías no podían acudir al sector financiero tradicional. Tras realizar un análisis de los resultados de ambos modelos financieros desde 2006 hasta 2012, se ha podido comprobar como el sector microfinanciero presenta resultados más favorables y muestra una mayor prosperidad de cara al futuro. Por lo general, estas entidades mantienen niveles de solvencia más elevados y emplean todos sus recursos en proporcionar financiación a sus clientes. Finalmente, la solución a los problemas del sistema financiero tradicional se basa en un aumento de los niveles de capital de sus entidades, volviendo a un modelo de banca tradicional centrado en ofrecer financiación al público, con provisiones más liquidas y mayores garantías ante necesidades de liquidez como las retiradas masivas de depósitos recientemente sufridas.

Paraísos fiscales: una aproximación a los agujeros negros de la economía

Este estudio intenta dar a conocer esos territorios calificados como paraísos fiscales, así como su funcionamiento, tamaño, los efectos económicos que ejercen sobre la economía globalizada y los estados; basado en investigaciones previas de diferentes expertos e instituciones. Ha quedado demostrado como las operaciones opacas realizadas en estos territorios han tenido un gran impacto en la actual situación de crisis financiera y económica, de manera que deben tomarse medidas más decisivas y efectivas para su control y regulación con el fin de evitar una próxima crisis global; por lo que en este estudio se presentan dos capítulos que recogen estas preocupaciones. Además he querido averiguar la relación que guardan estos paraísos fiscales con nuestro país, de manera que se hará una especial mención al caso de España teniendo en cuenta el efecto de las operaciones financieras opacas ejercen sobre el país así como la cuantía de los flujos financieros con destino a paraísos fiscales tienen como origen nuestro país. Finalmente, se procede a realizar un resumen de los escándalos financieros más relevantes a nivel mundial relacionados con paraísos fiscales. En español.

Valoración de Empresas: Arflu, S.A.

A través de la realización de esta valoración, se espera conocer el verdadero valor o rango de valores de la empresa Arflu S.A., además de descubrir qué es lo que la hace tan atractiva de cara a terceros.

Valoración de bio-oil completo por craqueo catalítico en condiciones de la unidad FCC de refinería

351 p.

Diseño, creación y explotación de una base de datos en el ámbito de la gestión empresarial

Duración (en horas): Más de 50 horas Destinatario: Estudiante y Docente

Optimization of the pyrolysis process for the production of a biomass derived reducing agent and hydrogen-rich gases

221 p.

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.

Development of the heterogeneous catalysts for the production of levulinic acid from furfuryl alcohol

207 p.

Descripción de empresas en crisis financiera: el caso de Argentina en las décadas del 1990 y 2000

[ES]Las investigaciones sobre la predicción de quiebras empresariales que se han venido dando en los últimos cincuenta años han indicado que la crisis financiera de las empresas ha sido y es un tema de preocupación en el mundo, también en Argentina. El horizonte de análisis de este trabajo comprende dos períodos de estabilidad económica en la década de 1990 y la del 2000, con la intención de comparar los indicadores financieros que explican la crisis empresarial en cada uno de ellos. De esta manera, se procura continuar con el aporte de evidencia empírica en esta línea de investigación, mediante el análisis de los indicadores, que según la literatura, influyen en el pronóstico de riesgo de crisis financiera. Estos estudios descriptivos previos a los inferenciales pueden ser replicados en otras economías emergentes, como herramienta de diagnostico de la vulnerabilidad financiera de las empresas.

Caso práctico de auditoría de cuentas de la empresa SOGE Absorber, SA

[ES] Este documento recoge los procedimientos llevados a cabo y las conclusiones a las que ha dado lugar el trabajo de auditoría realizado a la sociedad SOGE Absorber SA, dedicada a la producción y distribución de amortiguadores, resortes y otros componentes de la industria del automóvil tanto para vehículos turísticos como industriales. En el presente documento se procederá a realizar un estudio del entorno y características de la entidad con la finalidad de evaluar el nivel de riesgo de auditoría y conocer mejor la situación económico-financiera. El objetivo final de la auditoría realizada será aumentar la confianza de los usuarios en los EEFF, para lo que se emitirá, por parte del auditor, una opinión sobre si los estados financieros han sido preparados, en todos los aspectos significativos, de conformidad con el marco de información financiera que le es aplicable. Como base para dicha opinión, el marco normativo de auditoría requiere que el auditor obtenga una seguridad razonable de que dichos estados financieros en su conjunto están libres de incorrección material,debida a fraude o error. En todo caso, la auditoría de cuentas de la empresa SOGE Absorber SA que se presenta en este proyecto toma como base las Normas Técnicas de Auditoría (NTA) vigentes a fecha 1 de enero de 2014, constituidas por las Normas Internacionales de Auditoría adoptadas en España (NIA-ES). El Trabajo Fin de Grado (TFG) recoge algunos de los aspectos más significativos detectados en la auditoría de Cuentas del ejercicio cerrado a 31 de diciembre de 2014.

Los centros offshore al descubierto

[ES] Los paraísos fiscales forman parte de la economía global desde hace aproximadamente un siglo. Estos centros financieros han contado con la pasividad de los gobiernos y de los organismos internacionales, la cual ha favorecido su desarrollo. Este aspecto unido a su naturaleza genera que la información existente en torno a los paraísos fiscales carezca de una precisión total.