PGPRs and nitrogen-fixing legumes: a perfect team for efficient Cd phytoremediation?

Cadmium (Cd) is a toxic, biologically non-essential and highly mobile metal that has become an increasingly important environmental hazard to both wildlife and humans. In contrast to conventional remediation technologies, phytoremediation based on legume rhizobia symbiosis has emerged as an inexpensive decontamination alternative which also revitalize contaminated soils due to the role of legumes in nitrogen cycling. In recent years, there is a growing interest in understanding symbiotic legume rhizobia relationship and its interactions with Cd. The aim of the present review is to provide a comprehensive picture of the main effects of Cd in N-2-fixing leguminous plants and the benefits of exploiting this symbiosis together with plant growth promoting rhizobacteria to boost an efficient reclamation of Cd-contaminated soils.

Analytical strategies to solve problems in industrial and official laboratories

210 p.

Traditional part-time grazing: a more sustainable sheep milk and cheese production in the Basque Country

[EN] The concept of sustainability when referring to food production rests, in general, on 3 main aspects: 1) respect for the environment; 2) economic and social benefits for all involved in production; and 3) production of sufficient quantity of quality food at an accessible price. In this contribution we focus on the main aspects of the traditional sheep's milk and cheese production (under the Denomination of Origin Idiazabal Cheese) in the Basque Country that contribute primarily to its sustainability. It is based on the local latxa or carranzana breeds of sheep, adapted to the mountainous terrain. The sheepherder takes advantage of local resources to reduce management costs by combining indoor dry forage and concentrates with outdoor grazing throughout lactation, according to local pasture availability, and thus avoiding having to buy large amounts of feed. This system facilitates recycling of manure, fertilising pastures and forest at the same time. Use of local breeds helps maintain biodiversity of sheep breeds. Cheese is produced industrially (44.5% of the total cheese produced in 2008) from milk of many flocks, or artisanally (38.3%) by the sheepherders with the milk from their own flocks. Transforming their own milk into cheese is advantageous for the following reasons: 1) higher economic returns as compared to selling the milk to cheese factories because cheese price directly sold to consumers is more competitive than industrial cheese sold in supermarkets; 2) increases the value of women's work (over 80% of the cheese makers are women) in the community and their self-esteem; 3) it creates rural jobs and contributes to rural development; 4) we have demonstrated both with experimental and commercial flocks that part-time grazing allows the sheepherder to obtain high yields of milk, and cheese, of high nutritional and functional quality. Currently a less sustainable, intensive sheep's milk production with foreign, imported breeds kept indoors constantly is gaining favour among milk producers because of its perceived higher economic profitability.

Decarbonising urban transportation

18 p.

A dynamic CGE modelling approach for analyzing trade-offs in climate change policy options: the case of Green Climate Fund

38 p.

Konexio konikodun hortzetako inplanteak: ateratze indarraren zehaztapena. Eredu analitikoa eta saiakuntza esperimentalak

[EU]Txosten honetan konexio konikodun hortzetako inplante baten eraginkortasuna aztertzen da. Zehatzagoak izanik, inplante bat ahotik kanporatu ahal izateko beharrezkoa den indarra aztertu egiten da, kontuan hartuz aldagai horren balioa ezagutzea ezinbestekoa dela pazientearen osasuna eta konforta ziurtatzeko. Proiektu honek zein eremutan garrantzia edukiko duen ikusteko, lehenik eta behin testuingurua deskribatuko da. Horren ondoren helburu nagusiak eta onura zientifiko-tekniko zein ekonomikoak adieraziko dira. Helburuak lortzeko posibleak diren bide desberdinak aztertuko dira, eta bakoitzaren abantailak eta desabantailak kontuan hartuz kasu honi hobeto egokitzen zaion alternatiba aukeratuko da. Jarraian, metodo horri dagokion azalpenari ekingo zaio, proiektuaren garapenean egindako lanak pausoz pauso deskribatuz. Proiektuaren hasieratik amaierara arte egindako lanen planifikazioa era argi batean adierazteko Gantt diagrama erabiliko da. Bertan hiru etapa nagusi ezberdindu daitezke: saiakuntzen aurre-diseinua, kanpaina esperimentala eta emaitzen interpretazioa. Azkenik, egindako saiakuntzen eta analisien emaitzak laburbilduko dira, horiek dakartzaten ondorioak azalduz. Puntu honekin hasiera batean planteatutako helburuei erantzun bat emango zaie, eta proiektu honen ondoren jarraitu ahal izango diren hurrengo pausoak aipatuko dira.

Estudio técnico sobre la sistematización de herramientas informáticas en procesos de troquelería para automoción.

[ES]El presente estudio técnico tiene por objeto desarrollar y exponer la metodología empleada en el análisis CAD/CAE de piezas de chapa conformada en troquelería así como poner de manifiesto las ventajas de dicha técnica frente a las técnicas clásicas. Para ello, en él deben figurar una descripción general de dicha metodología, los objetivos de este estudio, los pasos para alcanzarlos y una distribución en forma de cronograma de las tareas que incluye el mismo. El estudio abarca dos partes claramente diferenciadas:  Descripción de un software CAD/CAE y sus múltiples beneficios en el diseño y desarrollo del producto  Desarrollo y exposición de un ejemplo sencillo Los contenidos del documento se estructuran de la siguiente forma: Inicialmente, se exponen los beneficios que reporta el uso de un programa CAE en empresas de conformado de chapa. A continuación, se describen las características generales de un software de elementos finitos. Finalmente se concluye con un caso ejemplo básico que ilustra las características expuestas anteriormente.

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.

Aporte adicional de energía renovable geotérmica a instalación con cogeneración en hospital existente.

[ES]Este proyecto tiene como objetivo apoyar a la generación de energía por cogeneración mediante una fuente de energía renovable. Se pretende plantear una solución que satisfaga parte de las necesidades básicas del Hospital Universitario de Álava, en su sede del Hospital de Santiago, de una forma económicamente rentable. Este proyecto se enmarca dentro de los esfuerzos en la promoción de energías renovables que comenzaron con el protocolo Kioto, al que le siguieron los objetivos Europa 20/20/20. Se realizará un acercamiento a la utilización de la energía renovable geotérmica como fuente de energía que disminuye el impacto ambiental. El edificio hospitalario considerado ya cuenta con un sistema de generación energética con cogeneración, considerada dentro del régimen especial, por la utilización de energía residual para procesos que de otra manera hubieran requerido consumo de combustible. Se plantearán diferentes alternativas para la generación de energía térmica con geotermia, que al ser de origen renovable, es una fuente de energía de combustibles no fósiles, y se demostraran sus beneficios analizando cómo mejora la huella de carbono del hospital con la propuesta. Finalmente, para valorar si se trata de un proyecto viable se planteará el estudio económico analizando el presupuesto y análisis de rentabilidad.

Gender equality in life insurance

[EN]This project is going to study the implications of the gender of an individual in the rate-setting process of life insurance. In order to do so there is a review of the continuous changes that have taken place in the national and European legislation following the enactment of the Directive 2004/113/EC, as well as its consequences from the prohibition to differentiate the premiums and benefits on the grounds of gender. In this area, the evolution of the Spanish insurance sector and the influence of the new legislation are examined. Furthermore, there is an analysis of the differences between men and women, which to some extent have a direct impact in the management and development of the life insurance companies. Finally, methods to calculate the premium and the benefits are proposed with the purpose of preventing the restrictions imposed by the Directive 2004/113/EC. In order to check the repercussions of the use of unisex tables a comparison is made between the premiums obtained for a whole life insurance by allocating the same weighing to the actuarial male and female mortality tables and those that would result if the distinction by gender were allowed.

La igualdad de género en el seguro de enfermedad

El presente trabajo tiene como objetivo estudiar la relevancia del uso del sexo a la hora de tarificar y calcular prestaciones en el seguro de salud en base a la promulgación de la Directiva 2004/113/CE, que prohíbe su utilización al considerarlo discriminatorio. Se analiza el valor de la variable sexo como indicador del perfil de riesgo de los consumidores en el seguro de enfermedad, haciendo hincapié en el ámbito del gasto obstétrico, en las primas de las mujeres en edad de embarazo y en el empleo de factores alternativos razonables que determinen el riesgo. Se estudian a su vez los efectos y consecuencias de la Directiva 2004/113/CE y la sentencia Test-Achats en el ámbito asegurador, así como el impacto producido concretamente en la tarificación y suscripción de los seguros de salud en España, analizando la evolución del sector durante el periodo de implantación de dichos documentos.

Sarean dantzan: Youtubeko bideoen erabilgarritasuna Lehen Hezkuntzan

[eus] Lanaren helburu nagusia hauxe izan da: Lehen Hezkuntzako ikastetxeetan gehien dantzatzen diren, eta Youtubeko bideoetan agertzen diren, euskal dantzen erabilera aztertzea eta balioztatzea. Horretarako, Lehen Hezkuntzako eskolek eta dantza taldeek ekoiztutako dantzak behatu dira. Ikerketa hau egiteko etnografia birtualaren metodoa erabili da. Emaitzei erreparatuz, esan daiteke, eskoletako dantza gutxi dagoela Interneten, eta euskal dantzek ikasleen formakuntzan onurak edo laguntzak eskaintzen dituztela; izan ere, ikasleen garapen integralean beharrezkoak diren faktoreak lantzea eskatzen baitute. Gainera, euskal dantzei esker, ikasleek bere herriaren ondare kulturala ezagutzeko eta gozatzeko aukera izango dute.

The use of role-play games in teaching: The International Climate Negotiation Game

This paper presents a role-play game designed by the authors, which focuses on international climate negotiations. The game has been used at a university with students all drawn from the same course and at summer schools with students from different levels (undergraduate, master’s and doctoral students and post-doctoral researchers) and different knowledge areas (economics, law, engineering, architecture, biology and others). We discuss how the game fits into the process of competence-based learning, and what benefits games, and role-play games in particular, have for teaching. In the game, students take on the role of representatives of national institutions and experience at first hand a detailed process of international negotiation concerned with climate change.

Energy retrofits in social housing. Analysis of its thermal behaviour.

468 p.