Valoración nutricional en pacientes quirúrgicos

[ES] Numerosos estudios han demostrado que muchos de los pacientes que ingresan en Cirugía presentan signos de malnutrición. En el presente trabajo se estudió re t rospectivamente la valoración nutricional de 116 pacientes. Los resultados muestran que sólo en el 29,3% de los enfermos se determinaron parámetros antropométricos, en el 19% parámetros bioquímicos y en el 25% parámetros inmunológicos de interés nutricional. Cabe destacar que, como también indican otros autores, la valoración nutricional no constituye todavía un procedimiento habitual en la práctica clínica.

Extrafiscalidade e meio ambiente: O tributo como instrumento de proteção ambiental. Reflexões sobre a tributação ambiental no Brasil e na Costa Rica.

O objeto central da pesquisa dirige-se à análise do papel que pode desempenhar o tributo como um dos instrumentos jurídicos que podem ser utilizados pelo Estado com a finalidade de proteger o meio ambiente e promover o desenvolvimento sustentável. O trabalho analisa a introdução da variável ambiental no sistema tributário do Brasil e da Costa Rica. Considerando o caráter poliédrico da questão ambiental, a pesquisa foi estruturada em cinco capítulos, desenvolvidos a partir de quatro perspectivas, todas elas interligadas entre si: 1. A perspectiva ética-ambiental. No primeiro capítulo é feita uma reflexão sobre a crise ambiental que caracteriza a sociedade de risco e sobre os postulados éticos que devem nortear a relação do ser humano com a natureza. Sustenta-se que o discurso ético deve ser um referente necessário no debate da questão ambiental. A ética deve ser o ponto de partida para o desenho e implementação de instrumentos jurídicos cuja finalidade seja a defesa do meio ambiente; 2. A perspectiva constitucional ambiental. No segundo capítulo analisa-se o direito ao meio ambiente ecologicamente equilibrado, direito fundamental da terceira dimensão, fundamentado no valor da solidariedade e que passa a ser estabelecido como um direito fundamental em diversas Constituições Políticas a partir da década dos setenta do século passado; 3. A perspectiva econômica ambiental. No terceiro capítulo reflete-se sobre a estreita relação existente entre economia e meio ambiente, sobre as externalidades ambientais, o papel do Estado como regulador das atividades econômicas, a ideia de desenvolvimento sustentável, e sobre os instrumentos de regulação ambiental. 4. A perspectiva tributária ambiental. A partir da base preliminar exposta nos três primeiros capítulos, nos capítulos quatro e cinco é analisado o tema da tributação ambiental. No capítulo quatro são realizadas considerações sobre o fundamento e as finalidades dos tributos. Destaca-se que a fiscalidade ambiental pode ser implementada através de tributos ambientais em sentido estrito próprio -, de finalidade extrafiscal, ou através de tributos ambientais em sentido amplo impróprio -, caracterizados pela introdução de elementos ambientais na tributação ordinária, que produzem efeitos extrafiscais. É feita uma reflexão sobre os princípios que orientam e limitam a extrafiscalidade ambiental, as críticas realizadas aos tributos ambientais, os elementos do tributo ambiental estrito sensu, e sobre algumas das experiências tributário ambientais de maior relevância no direito comparado. Finalmente, no último capítulo, a partir do marco de referência prévio analisa-se o estado da tributação ambiental no Brasil e na Costa Rica. São descritas as principais figuras tributárias de caráter ambiental existentes nos ordenamentos jurídicos do Brasil e da Costa Rica, e reflete-se sobre as características da tributação ambiental em ambos os países. São realizadas recomendações que poderão ser consideradas nos procedimentos para propor e implementar tributos ambientais, e são realizadas algumas observações com o intuito de elaborar uma proposta para esverdear o sistema tributário do Brasil e da Costa Rica. A tese pretende ser um contributo para o debate sobre ao papel que pode desempenhar a tributação ambiental, como uma das possíveis respostas ao uso inconsciente da natureza, e como instrumento para promover uma consciência ambiental que vise o desenvolvimento sustentado.

Valoración actuarial de daños personales y lucro cesante

El objetivo del presente trabajo es el de establecer las directrices de una valoración actuarial en los diversos casos en los que puede ser requerido en caso de litigio e intentar tras realizar una lectura completa de este trabajo tener una visión más cercana y comprensible de lo que al principio podría verse como algo fuera del entendimiento de alguien sin una formación y conocimiento actuarial, sin embargo, con unos conocimientos actuariales básicos el objetivo es que sea sencillo y aporte una visión general de la valoración actuarial. Se compone de una parte teórica donde se define y se desglosan los factores del lucro cesante a tener en cuenta para la realización de su valoración, así mismo, se muestran distintas metodologías, y finalmente se encuentra la parte práctica donde se realizan varias hipótesis, todas ellas con su definición y detallándose su labor en la valoración; y un intervalo de supuestos prácticos que engloba los sucesos más comunes en la vida real. En definitiva, el objetivo del presente trabajo además de entender el procedimiento para la valoración del actuario es tras realizar una lectura completa del trabajo comprender la importancia del papel del actuario, al ser éste la persona encargada de lograr la justicia y equidad social, consiguiendo con sus conocimientos actuariales que aquella persona que se haya visto perjudicada económicamente por el suceso sea resarcida justamente.

Aerogeles, nuevas rutas de síntesis

Con este proyecto se pretende encontrar una ruta de procesado para obtener materiales semejantes a los aerogeles. El procedimiento se basa en la sublimación a temperatura ambiente de un sólido adsorbido en el interior de un gel de sílice.

Algoritmo para la identificación de las ganancias óptimas del algoritmo de control de posición de un mecanismo de cinemática paralela

[ES]Este trabajo presenta un algoritmo automatizado cuyo resultado es la determinación de las ganancias óptimas del lazo de control de un mecanismo de cinemática paralela. En concreto se ha aplicado al mecanismo 5R, aunque el método es válido para cualquier otro mecanismo introduciendo el modelo mecatrónico correspondiente. Permite disponer de un procedimiento para poder elegir en un futuro la combinación de motor y reductora más apropiada para un determinado mecanismo evitando realizar adquisiciones sobredimensionadas, como ocurrió con el mecanismo en cuestión.

La estratigrafía analítica: 25 años de ensayo y aprendizaje en el análisis e interpretación del registro arqueológico

Homenaje a Georges Laplace, realizado en Vitoria-Gasteiz el 13,14 y 15 de noviembre de 2012. Edición a cargo de Aitor Calvo, Aitor Sánchez, Maite García-Rojas y Mónica Alonso-Eguíluz.

Propiedades catalíticas de la lipasa B de Candida antarctica inmovilizada en soportes magnéticos. Actividad hidrolítica en medios acuosos

Los enzimas son piezas fundamentales en el correcto funcionamiento de cualquier sistema biológico. Gracias a su naturaleza proteica y a las estructuras tridimensionales complejas que son capaces de adoptar, estas moléculas actúan como catalizadores de reacciones químicas. L a función de los enz imas es disminuir la energía de activación de la reacción, aumentando de este modo la velocidad de reacción. L o s enzimas no alteran el balance e nergético de las reacciones en que intervienen, ni modifican, por lo tanto, el equilibrio de la reacción . Por este motivo, en las reacciones catalizadas por enzimas se observa una mayor rapidez a la hora de alcanzar el equilibrio. La ciencia que estudia l a velocidad de las reacciones químicas que son catalizadas por enzimas es la cinética enzimática , e n la cual , las moléculas sobre las que actúan los enzimas se denominan sustratos y las moléculas resultantes de la conversión productos. El estudio de la cin ética de un enzima permite explicar los detalles de su mecanismo catalítico, su papel en el metabolismo o incluso cómo se controla su actividad en la célula. Las dos propiedades más importantes a la hora de trabajar con enzimas son: el tiempo que tarda en saturarse con un sustrato en particular y la velocidad máxima de reacción que puede alcanzar. Para el estudio de estas propiedades en el laboratorio se realizan los ensayos enzimáticos. El procedimiento a seguir en estos casos es medir la aparición de un producto o la desaparición de un sustrato frente al tiempo.

Estudio de los sueros ricos en factores de crecimiento y de su efecto sobre células de epitelio corneal

Objetivos: Estudiar cómo afecta a la concentración de determinados factores de crecimiento presentes en los sueros la filtración (utilizado como método de esterilización) y el tratamiento por calor (utilizado para la inactivación del complemento). Además de estudiar el efecto de un bioadhesivo (ácido hialurónico, HaNa), aplicado solo o conjuntamente con el suero rico en factores de crecimiento (s-PRGF), sobre la capacidad de las células de epitelio corneal (HCE) para proliferar y migrar. Materiales y métodos: Se midió mediante kits ELISA comerciales la concentración en las diferentes condiciones de filtración y calentamiento de las siguientes biomoléculas EGF (Epidermal Growth Factor), VEGF (Vascular Endothelial Growth Factor), HGF (Hepatocyte Growth Factor), PDGF (Platelet-derived Growth Factor) y la Fibronectina. Teniendo en cuenta el papel de la proliferación y migración celular en los procesos de cicatrización se han realizado dos ensayos diferentes in vitro: un ensayo MTT para estudiar la viabilidad y la proliferación celular y el método de la herida (Scratch wound-healing assay) para determinar la capacidad migratoria de células bajo ciertos tratamientos: BSA (Bovine Serum Albumin) al 1% como control, FBS (Fetal Bovine Serum) al 10%, s-PRGF al 45%, s-PRGF al 45% con HaNa 0,1% y HaNa al 0,1% Resultados: En el caso de la filtración, se observa una mayor pérdida de factores utilizando un filtro con una membrana de PVDF (Durapore®) para todos los factores estudiados. El calentamiento produce una reducción de la concentración superior al 50% en el caso del HGF y EGF, manteniéndose constante en el caso del VEGF.La mezcla de diferentes muestras con el complemento inactivado para formar un pool no presenta cambios en la concentración al compararlo con la media de las muestras utilizadas. Por tanto, la utilización de un pool del hemoderivado no supone perdida de factores de crecimiento, haciendo de ello un procedimiento perfectamente aceptable para los ensayos celulares. El tratamiento con s-PRGF y el combinado con el bioadhesivo promueven la proliferación y migración de las células de epitelio corneal humano(HCE) in vitro de manera similar, no encontrándose diferencias estadísticamente significativas entre ambos. Conclusiones: La adicción del bioadhesivo no produce efecto tóxico en las células, sin embargo, no se han encontrado efectos beneficiosos en cuanto a proliferación y migración se refiere. A este respecto, creemos que hay que dar un paso más haciendo comprobaciones in vivo, ya que, a diferencia de la experimentación in vitro los componentes de los hemoderivados no están indefinidamente en contacto con las células sino por un espacio de tiempo muy reducido. Por ello, la concentración de factores de crecimiento en la aplicación in vivo es especialmente importante, y no sería conveniente reducirla mediante procedimientos físicos como la filtración o el calentamiento.

El régimen jurídico de los suelos contaminados en la Comunidad Autónoma del País Vasco

689 p.

Utilización de la lógica borrosa en la selección de personas e ideas para la participación en programas públicos de ayuda a la creación de empresas

[ES] Se propone en este trabajo un modelo de control borroso que ayude a filtrar y seleccionar las solicitudes de subvención que pueda recibir una institución pública en un programa de fomento para la creación y desarrollo de nuevas iniciativas empresariales. Creemos que la utilización de la lógica borrosa presenta ventajas sobre los procedimientos ordinarios ya que nos movemos en un escenario de actuación complejo y vago. El control borroso introduce el conocimiento de los expertos de un modo muy natural mediante variables lingüísticas y procesos de inferencia propios del lenguaje ordinario, lo que facilita la toma de decisiones en situaciones complejas. Nuestro modelo considera por un lado la idea empresarial y por otro la persona . Los indicadores y criterios que los expertos consideran relevantes para la evaluación de la subvención son modelados mediante variables lingüísticas y tratados como antecedentes y consecuentes de un motor de inferencia borroso, cuya salida nos proporciona la valoración final de la solicitud. Al final de nuestro trabajo resolvemos un caso práctico sencillo para aclarar el procedimiento.

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.

Diseño en 3D, análisis hidrodinámico y cálculo del escantillonado de una embarcación de 24 metros de eslora fabricada con materiales compuestos.

Se desarrolla el procedimiento de diseño en 3D de una embarcación de eslora menor de 24 metros y la posterior determinación de su escantillonado siguiendo las indicaciones de la norma internacional ISO 12215 para la construcción de cascos y escantillones de pequeñas embarcaciones. Se analizan también las ventajas y desventajas de la construcción del casco de un velero con fibra de vidrio y fibra natural de lino. Para llevar a cabo el diseño 3D a partir de los planos 2D de la embarcación se ha utilizado el software Rhinoceros. Los cálculos hidrostáticos, hidrodinámicos y el comportamiento en la mar se han estudiado con el programa Maxsurf, ampliamente utilizado en el sector naval.

Nanocomposites de Poliuretanos Elastoméricos y Nanotubos de Carbono Multipared

218p. -- Tesis con mención "Doctor europeus" realizada en el periodo de Octubre 2005-Mayo 2010, en el Grupo "Materiales+Tecnologías" (GMT).

Measurement of polycyclic aromatic hydrocarbons in ambient air by fluorescence spectroscopic techniques

250 p. + anexos

Estudio de la resolución del problema de posición de mecanismos planos de cadena cerrada usando la Proyección cinemática de Study.

[ES]El presente documento versa sobre el desarrollo y posteriores resultados de un estudio elaborado en el campo de la cinemática teórica. Se plantea como objetivo del estudio mostrar las posibles ventajas que puede aportar el uso de la proyección cinemática tanto al análisis como a la síntesis de mecanismos. Los resultados obtenidos reflejan que la metodología propuesta para el análisis es adecuada para mecanismos sencillos, pero puede no serlo tanto para mecanismos de varios lazos cinemáticos. En cuanto al procedimiento propuesto para la síntesis, pese a obtenerse unos interesantes resultados, aún queda mucho por avanzar en ese campo.