Cosméticos María D'uol: Gulliver en el país de los gigantes

Duración (en horas): De 21 a 30 horas Destinatario: Estudiante y Docente

Antecedentes de la institucionalización de las organizaciones

[ES] Esta investigación es un intento de avanzar en la comprensión de por qué las organizaciones son sensibles a la institucionalización. Para ello, describimos los elementos clave que ayudan a explicar el origen del proceso corporativo de institucionalización. Además, se ha seguido una metodología de investigación cualitativa, utilizando la técnica del concept mapping , para agrupar en constructos los diferentes ítems que actúan como factores motivadores de la transformación de las organizaciones en instituciones. Metodológicamente hemos tratado de obviar la separación entre viejo y nuevo institucionalismo siguiendo a los autores que cuestionan la conveniencia de trazar una línea divisoria entre la vieja y la nueva teoría. Consideramos que el papel del CEO es esencial en el impulso del proceso de institucionalización, aunque en muchas ocasiones sus decisiones estén apoyadas o hayan pasado por el filtro de los equipos de gobierno de la organización o de los consejos de administración. Cualquier impulso que realice la organización dependerá fundamentalmente de las capacidades, las sensaciones, la formación y el modo de pensar del CEO. Los resultados refuerzan varios de los temas claves sugeridos en la literatura sobre Teoría Institucional. En particular, se establece una clasificación con los motivos que dan origen a las iniciativas institucionales, a saber: autoridad institucional; ventaja en gestión; e, implicación social. Esta clasificación es coincidente, en una gran medida, con los pilares de la institucionalización que han sido definidos en la literatura de la teoría institucional, ayudando a comprender, con mayor detalle, el origen de los procesos institucionales y los antecedentes o motivaciones que los generan y guían.

Does rating shopping exist in spanish securitization issues?

[EN] Debt issue credit ratings can lead to conflicts of interest as the issuer itself is entrusted with contracting and compensating the rating agency. Into the bargain, the credit rating agency may be involved in designing the issues that the same agency subsequently rates. Credit rating agencies thus could have incentives to rate issues advantageously. Given the economic importance of this issue, in this paper we have proposed to analyze this phenomenon, known as rating shopping in academic literature, for Spanish market securitization issues for the period of time comprehensive from January 1993 to December 2011. In sum 3,665 published ratings are been analysed, for an issued nominal amount of 791,090 million Euros. The results show an association between the credit rating agency contracted and the mean rating awarded. Significant differences are observed in the ratings associated to the contracting manager (or special purpose vehicle SPV- manager firm), to the number of ratings or to the type of collateral. Furthermore, a pattern compatible with rating shopping was observed for some types of collateral: abnormally high market shares associated with certain agencies awarding unusually generous ratings. However, this phenomenon is not seen to be widespread on the rating market associated to Spanish securitization issues.

Informe sobre la Seguridad Alimentaria en la prensa del País Vasco en 2014

La demanda de información sobre los alimentos que consumimos es cada vez mayor y, con la actual facilidad de acceso a la información, cobra cada vez mayor importancia la difusión de la información de manera clara y veraz. Por este motivo se debe garantizar a la ciudadanía el acceso a la información de la manera más neutra y rigurosa posible, para que pueda entenderla e interpretarla y genere una opinión al respecto. En seguridad alimentaria se hace imprescindible contar con una estrategia de comunicación, basada en una actitud proactiva y que cumpla los principios básicos de apertura, transparencia e independencia. De ello dependerá la percepción que tenga la población sobre las cuestiones de seguridad alimentaria. Para ello, es necesario conocer el tratamiento que dan los medios de comunicación a los temas de seguridad alimentaria, las fuentes de información utilizadas habitualmente, la calidad y el rigor del contenido de las noticias y el enfoque que les dan a las noticias sobre riesgos y alertas alimentarias. El conocimiento de esta información es esencial para que los gestores puedan orientar la estrategia de comunicación en seguridad alimentaria. Este es el tercer año que se realiza este estudio de Seguridad Alimentaria en la Prensa del País Vasco‚ lo que además de proporcionarnos la información sobre las cuestiones de Seguridad Alimentaria que el público recibe a través de este medio, nos va a permitir estudiar la tendencias del tratamiento de esta información por parte de la prensa escrita en el País Vasco durante los tres últimos años.

La vegetación de la Comunidad Autónoma del País Vasco. Leyenda del mapa de series de vegetación a escala 1:50.000

Índice: 1. Marco geográfico. El medio físico: - Situación, extensión y límites. - Estructura, morfología y relieve. - Rasgos generales de los Pirineos. - Los Montes Vasco-Cantábricos. - La depresión del Ebro. 2. Los cambios de la vegetación en el tiempo: paleogeobotánica o geobotánica histórica: - Introducción. Las glaciaciones del Cuaternario. - La vegetación de Europa en el Terciario. - El tránsito Plioceno-Pleistoceno y el Pleistoceno antiguo. - El Pleistoceno medio y reciente. - El Tardiglaciar y el Holoceno. - La expansión de Fagus sylvatica en el Holoceno. - La Península Ibérica. 3. El clima actual del la Comunidad Autónoma del País Vasco y regiones limítrofes: - El régimen climático general del territorio noribérico. - La ubicación geográfica. - Centros de acción. - El contexto geográfico. - La clasificación bioclimática. - El paisaje vegetal a través de las unidades bioclimáticas: macroclimas, bioclimas y pisos bioclimáticos. - El macroclima Templado. - El macroclima Mediterráneo. 4. Biogeografía: - Biogeografía: definición y concepto. - Corionomía. - Biogeografía del norte-centro de la Península Ibérica. - Descripción y caracterización de las principales unidades biogeográficas. 5. Flora de la CAPV y territorios limítrofes: - La flora eurosiberiana. - La flora mediterránea. - La flora endémica. 6. Series, Geoseries y Geopermaseries de Vegetación de la Comunidad Autónoma del País Vasco: - Los cambios de la vegetación en escala temporal reducida: dinamismo y sucesión. Concepto de Serie, Geoserie y Geopermaserie de Vegetación - Series climatófilas y temporihigrófilas. - Geoseries fluviales. - Halogeopermaseries (Geopermaseries costeras): los sistemas costeros. - Saxigeopermaseries (Geopermaseries rupícolas): crestas, acantilados y gleras. - Higrogeopermaseries (Geopermaseries higrófilas): turberas, charcas y lagunas.

La lucha de bandos en el País Vasco: de los Parientes Mayores a la Hidalguía Universal. Guipúzcoa, de los bandos a la Provincia (s. XIV a XVI)

La historiografía tradicional acuñó el término Lucha de Bandos para referirse a los enfrentamientos internobiliarios que tuvieron lugar en el País Vasco entre el bando de los oñacinos y el de los gamboínos durante los siglos XIV y XV. La renovación historiográfica que fue cuajando durante los primeros años 70 demostró, sin embargo, que semejantes enfrentamientos ocultaban otros que contraponían a los grupos sociales antagónicos tanto en el mundo rural como en las villas en una amplia tipología de conflictos hasta el punto que, en la actualidad, tendemos a equiparar Lucha de Bandos y conflictividad social. Los trabajos que recoge este libro son el resultado de un nuevo acercamiento al problema, a la luz de las nuevas propuestas que durante los últimos años han aportado otros autores en el tratamiento de problemas similares en otras latitudes. En su mayoría fueron presentados los días 4 y 5 de diciembre de 1997 en Vitoria durante un Symposium sobre la Lucha de Bandos en el País Vasco. Con una especial atención al caso guipuzcoano, se abordan, entre otras, distintas cuestiones relacionadas con la historiografía, las fuentes, la definición y significado de Pariente Mayor, las bases materiales de su poder, la constitución de oligarquías municipales en las villas, los movimientos migratorios, la “revolución de los precios” o la dimensión política de la hidalguía universal. En conjunto se ofrece una visión diacrónica que observa las transformaciones sociales, económicas y políticas que conoció la sociedad guipuzcoana al final de la Lucha de Bandos, al compás del nacimiento y de los primeros pasos de una “sociedad igualitaria”.

Banco de Datos Hesperia de Lenguas Paleohispánicas (BDHESP) II. Numimática paleohispánica

El Banco de Datos de Lenguas Paleohispánicas Hesperia tiene como finalidad la catalogación y la difusión de los textos escritos en las antiguas lenguas locales de la Península Ibérica, con exclusión del fenicio, el griego y el latín. El presente volumen es la versión impresa –a fecha de 2015– de una de las bases de datos que integra dicho banco: la correspondiente a la epigrafía monetal. Recoge las leyendas monetales redactadas en una lengua paleohispánica (fundamentalmente ibérico y celtibérico) tanto de la Península Ibérica cuanto del sureste de las Galias, incluidas las redactadas en latín y griego en las emisiones bilingües. Dada la controvertida lectura y adscripción lingüística de los rótulos “libiofenicios”, estos no son tomados en consideración. Las fichas están ordenadas alfabéticamente y agrupan todos los rótulos monetales correspondientes a una misma ceca, designada convencionalmente mediante una o varias de las leyendas toponímicas más frecuente, independientemente de su morfología (p. ej.: untikesken, salduie, kalakorikos o turiazu). Cada ficha presenta cuatro apartados: “Generalidades”, “Leyendas”, “Lengua y escritura” y “Bibliografía”.

Fundamentos de la construcción del pensamiento sociológico de Émile Durkheim

513 p.

Traditional budgeting during financial crisis

[EN] This study examines the evolution of budgeting practices in the extremely difficult Spanish economic environment. In order to analyse if companies are still maintaining their budgeting process and if, right now, they are facing more difficulties in forecasting accurate indicators, two similar web surveys were addressed over two periods of time, firstly in 2008 at the beginning of the financial crisis, and secondly in 2013 after five years of a downward trend. In addition, in-depth interviews were conducted to investigate how companies brought more flexibility to their budgeting process in order to cope with environmental uncertainty. The survey indicates that 97% of respondents are still using a traditional budgeting process being this result similar to the one found in 2008. However, 2013 showed that the reliance on forecasted information is being increasingly questioned. Furthermore the study revealed that the respondents are bringing more flexibility to their processes, being able to modify the objectives once the budget is approved and to obtain new resources outside the budgeting process. This paper contributes to revealing information about difficulties in setting reliable objectives in a turbulent environment and provides data about the evolution of budgeting practices over five years during an austere economic crisis.

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.

El capital social de las minorías religiosas en el País Vasco

328 p.

Modelización de procesos hidrológicos y de contaminación por nitratos mediante dos códigos numéricos (SWAT y MOHID). Cuenca agrícola del río Alegría (País Vasco)

245 p.+ anexos

Historia del cuidado y del papel de la enfermería durante la Guerra Civil Española: España y País Vasco : revisión Bibliográfica

[Es]La labor cuidadora es conocida desde la antigüedad y así lo demuestran los estudios realizados. En el transcurso de la historia ha existido una evolución en el concepto de la salud-enfermedad. Y a su vez la enfermería ha sufrido trasformaciones importantes, situándose hoy en día en la posición en la que se la conoce. Diferentes acontecimientos favorecieron ésta evolución, como los conflictos bélicos. Por ello se realiza un estudio durante la Guerra Civil Española (1936-1939), para conocer la situación de la enfermería en la época, los cuidados que ofrecieron las/los enfermeras/os, la importancia de la colaboración social para la realización de estos cuidados y el consecuente beneficio de todo ello. Dedicando una sección al País vasco. Se realiza una revisión bibliográfica recurriendo principalmente a fuentes primarias para la obtención de documentación. Dando como resultado, un estudio histórico de carácter analítico-sintético. Se obtiene como resultado una visión global de la labor cuidadora de enfermeras/os, del voluntariado y de la ayuda internacional en el transcurso del conflicto. Destaca la importancia de la formación, la disciplina, los reglamentos y guías. Resulta imprescindible señalar el importante papel que desarrolló la Cruz Roja durante todo el conflicto. El conocimiento sobre el importante papel de la enfermería y los cuidados aplicados durante la guerra, contribuye a una reflexión personal de la importancia que éstas tuvieron, y demuestra la necesidad de una indagación más profunda y amplia.

Análisis de la innovación tecnológica en las empresas del País Vasco

[ES]La innovación tecnológica es una estrategia por la que han apostado muchas de las empresas vascas en los últimos años, ya que aporta muchos beneficios tanto para las empresas, como para el sistema económico de la región. Además, las administraciones públicas han apoyado estas estrategias desde hace más de 30 años impulsando distintas medidas en cada fase. Con el fin de conocer cuál ha sido la evolución de la innovación tecnológica y su tendencia para los siguientes años, el presente trabajo analiza los factores relacionados con la innovación tecnológica en el País Vasco.

La aplicación del principio de igualdad de oportunidades de mujeres y hombres al personal al servicio de la Administración de Justicia de la Comunidad Autónoma del País Vasco

611 p.