Comparative Microbial Dynamics in Crassostrea virginica and Crassostrea ariakensis

Considerations to introduce the Suminoe or Asian oyster Crassostrea ariakensis along the East Coast have raised many questions regarding ecology, economics, and human health. To date, research has focused primarily on the ecological and socioeconomic implications of this initiative, yet few studies have assessed its potential impact on public health. Our work compares the rates of bioaccumulation, depuration and post harvest decay of indicator organisms (such as E. coli) and Vibrio sp. between Crassostrea virginica and Crassostrea ariakensis in the laboratory. Preliminary results suggest that the rates of bioaccumulation of E. coli in Crassostrea ariakensis were significantly lower than those for Crassostrea virginica, depuration of E. coli was variable between the two species, and Crassostrea ariakensis post harvest decay rates of Vibrio sp. were significantly lower than Crassostrea virginica. This research provides coastal managers with insight into the response of Crassostrea ariakensis to bacteria, an important consideration for determining appropriate management strategies for this species. Further field-based studies will be necessary to elucidate the mechanisms responsible for the differences in rates of bioaccumulation and depuration. (PDF contains 40 pages)

Petrarca, el texto de Terencio y Pietro da Moglio

[ES] Terencio fue uno de los autores que mayor interés suscitaron en Petrarca desde un punto de vista filológico, y sabemos que glosó al menos alguno de los varios mss. terencianos que estaban en su biblioteca. No conservamos ningún Terencio anotado de su puño y letra, pero tenemos dos mss. que (gracias a las subscriptiones que contienen) sabemos descienden de un ejemplar petrarquesco: sin embargo, y debido sobre todo a la extraordinaria complejidad de la historia del texto terenciano, la relación entre ambos mss. no había podido aclararse ni, por tanto, se había progresado en la reconstrucción del Terencio de Petrarca. Las principales aportaciones del presente artículo podrían resumirse así: 1, se identifican nuevos mss. que descienden del Terencio de Petrarca y se demuestra (en contra de lo que habían sostenido expresamente Sabbadini y Billanovich) que la importante edición terenciana de Pietro da Moglio (muy difundida sobre todo en Italia) contiene el mismo texto que los mss. de Petrarca; 2, se sitúa el conjunto que conforman todos estos mss. en la tradición de Terencio, y esto permite mostrar que la labor filológica realizada por Petrarca sobre el texto de las comedias no consistió en intentar restablecer la colometría correcta (como venía defendiéndose hasta ahora a partir de las subscriptiones antes citadas), sino en saber apreciar un Terencio particularmente noble y, a través del cotejo con otros mss., proponer puntualmente una colometría alternativa (pues, en efecto, se han descubierto marcas métricas que parece deben asignarse a Petrarca); 3, gracias en buena parte a los mss. nuevamente identificados (muy en particular al ms. de Estocolmo), se han podido atribuir a Petrarca glosas que se encuentran en algunos de ellos, aunque distinguiendo entre apostillas del propio Petrarca y glosas que con seguridad se encontraban en su ejemplar pero que provienen de otros mss.

Earth-abundant materials for solar hydrogen generation

A critical challenge for the 21st century is shifting from the predominant use of fossil fuels to renewables for energy. Among many options, sunlight is the only single renewable resource with sufficient abundance to replace most or all of our current fossil energy use. However, existing photovoltaic and solar thermal technologies cannot be scaled infinitely due to the temporal and geographic intermittency of sunlight. Therefore efficient and inexpensive methods for storage of solar energy in a dense medium are needed in order to greatly increase utilization of the sun as a primary resource. For this purpose we have proposed an artificial photosynthetic system consisting of semiconductors, electrocatalysts, and polymer membranes to carry out photoelectrochemical water splitting as a method for solar fuel generation.

This dissertation describes efforts over the last five years to develop critical semiconductor and catalyst components for efficient and scalable photoelectrochemical hydrogen evolution, one of the half reactions for water splitting. We identified and developed Ni–Mo alloy and Ni₂P nanoparticles as promising earth-abundant electrocatalysts for hydrogen evolution. We thoroughly characterized Ni–Mo alloys alongside Ni and Pt catalysts deposited onto planar and structured Si light absorbers for solar hydrogen generation. We sought to address several key challenges that emerged in the use of non-noble catalysts for solar fuels generation, resulting in the synthesis and characterization of Ni–Mo nanopowder for use in a new photocathode device architecture. To address the mismatch in stability between non-noble metal alloys and Si absorbers, we also synthesized and characterized p-type WSe₂ as a candidate light absorber alternative to Si that is stable under acidic and alkaline conditions.

Temperature controlled filamentation in argon gas

Temperature controlled filamentation is experimentally demonstrated in a temperature gradient gas-filled tube. The proper position of the tube is heated by a furnace and two ends of the tube are cooled by air. The experimental results show that multiple filaments are shrunken into a single filament or no filament only by increasing the temperature at the beginning of the filament. This technique offers another degree of freedom of controlling the filamentation and opens a new way for intense monocycle pulse generation through gradient temperature in a noble gas.

Self-compression of femtosecond pulses in argon with a power close to the self-focusing threshold

Self-compression of femtosecond pulses in noble gases with an input power close to the self-focusing threshold has been investigated experimentally and theoretically. It is demonstrated that either multiphoton ionization (MPI) or space time focusing and self-steepening effects can induce pulse shortening, but they predominate at different beam intensities during the propagation. The latter effects play a key role in the final pulse self-compression. By choosing an appropriate focusing parameter, action distance of the space time focusing and self-steepening effects can be lengthened, which can promote a shock pulse structure with a duration as short as two optical cycles. It is also found that, for our calculation cases in which an input pulse power is close to the self-focusing threshold, either group velocity dispersion (GVD) or multiphoton absorption (MPA) has a negligible influence on pulse characteristics in the propagation process.

Filamentation control in the temperature gradient argon gas

A novel technique of controlling the evolution of the filamentation was experimentally demonstrated in an argon gas-filled tube. The entrance of the filament was heated by a furnace and the other end was cooled with air, which resulted in the temperature gradient distribution along the tube. The experimental results show that multiple filaments are merged into a single filament and then no filament by only increasing the temperature at the entrance of the filament. Also, the filament can appear and disappear after increasing the local temperature and input pulse energy in turn. This technique offers another degree of freedom to control the filamentation and opens a new way for multi-mJ level monocycle pulse generation through filamentation in the noble gas.

Electrical resistance and thermoelectric power of the metastable phases in tellurium-base alloys

By using techniques of rapid quenching from the melt, metastable phases have been obtained in ternary alloys which contain tellurium as a major component and two of the three noble metals (Cu, Ag, Au) as minor components. The metastable phases found in this investigation are either simple cubic or amorphous. The formation of the simple cubic phase is discussed. The electrical resistance and the thermoelectric power of the simple cubic alloy (Au₃₀Te₇₀) have been measured and interpreted in terms of atomic bondings. The semiconducting properties of a metastable amorphous alloy (Au₅Cu₂₅Te₇₀) have been measured. The experimental results are discussed in connection with a theoretical consideration of the validity of band theory in an amorphous solid. The existence of extrinsic conduction in an amorphous semiconductor is suggested by the result of electrical resistance and thermoelectric power measurements.

Estudo da desativação térmica de catalisadores à base de óxidos mistos de cério e zircônio

Em termos ambientais, os catalisadores automotivos se destacam pelos resultados altamente significativos alcançados após seu uso obrigatório em veículos leves. No entanto, as condições térmicas em que eles operam podem levar a um processo de perda de atividade significativa, após certo tempo de operação. Dentro desse contexto, este trabalho estudou o efeito da temperatura na desativação térmica de catalisadores automotivo modelo. Foram preparados catalisadores baseados em óxido misto de cério e zircônio na proporção 50% em mol de cério e zircônio (CZ). A partir dele foram produzidos os catalisadores Pd-CZ e Pd-CZ-LaAl. O catalisador Pd-CZ foi produzido pela impregnação do CZ com Pd na concentração de 0,5% m/m de CZ. O catalisador Pd-CZ-LaAl foi produzido a partir de uma mistura física do Pd-CZ com o suporte LaAl (alumina dopada com La na concentração de 1,9 % m/m de Al2O3), seguida de calcinação a 500˚C. Foram realizados envelhecimentos a 900C e 1200C em mufla com atmosfera oxidante por 12 e 36h. Os catalisadores foram caracterizados por um conjunto de técnicas físico-químicas. Foram realizadas análises de fisissorção de N2 para a medição da área específica e o estudo da evolução do diâmetro e volume de poros das amostras novas e envelhecidas. Análises de difração de raios X (DRX) foram feitas de forma a acompanhar possíveis transições de fases após o envelhecimento das amostras. Foi realizada análise química para validar a composição das amostras e ensaios de análise térmica para o catalisador CZ visando identificar a temperatura onde ocorre o fenômeno de segregação de fases. Realizaram-se ensaios de redução a temperatura programada (RTP) visando quantificar o consumo de hidrogênio e associá-lo à evolução da redutibilidade das amostras após o envelhecimento térmico. Finalmente, a avaliação catalítica foi realizada com base nas reações de oxidação do CO e do propano e de redução do NO pelo CO, através da obtenção de curvas de lightoff. As análises de DRX mostraram que o envelhecimento a 900C ocasionou alterações de fases da alumina, mas não foi verificada segregação de fases no CZ. Já a 1200C observou-se a referida segregação de fases, que coincide com a drástica queda na área específica das amostras, em alguns casos observando-se o colapso das propriedades texturais do catalisador. As análises de RTP mostraram que, em determinadas condições, o envelhecimento térmico promove a redutibilidade do sistema CZ e a introdução de Pd torna o catalisador mais facilmente redutível o que é evidenciado pelo deslocamento dos picos de redução para temperaturas mais baixas em comparação ao CZ puro. Os testes catalíticos mostraram que a introdução do Pd é um fator fundamental para a conversão do propano. Os catalisadores contendo Pd também converteram melhor o CO. Para os catalisadores envelhecidos a 1200C, o único resultado positivo foi no caso do Pd-CZ-LaAl que apesar deste tratamento térmico, ainda converteu o CO, propano e NO. Desta forma o catalisador Pd-CZ-LaAl apresentou resultados mais satisfatórios e isto evidencia que a mistura com LaAl melhora o desempenho e a estabilidade térmica do catalisador em altas temperaturas (acima de 300C).

The separation of atomic and molecular gases from helium by cataphoresis

The cataphoretic purification of helium was investigated for binary mixtures of He with Ar, Ne, N₂, O₂, CO, and CO₂ in DC glow discharge. An experimental technique was developed to continuously measure the composition in the anode end-bulb without sample withdrawal. Discharge currents ranged from 10 ma to 100 ma. Total gas pressure ranged from 2 torr to 9 torr. Initial compositions of the minority component in He ranged from 1.2 mole percent to 7.5 mole percent.

The cataphoretic separation of Ar and Ne from He was found to be in agreement with previous investigators. The cataphoretic separation of N₂, O₂, and CO from He was found to be similar to noble gas systems in that the steady-state separation improved with (1) increasing discharge current, (2) increasing gas pressure, and (3) decreasing initial composition of the minority component. In the He-CO₂ mixture, the CO₂ dissociated to CO plus O₂. The fraction of CO₂ dissociated was directly proportional to the current and pressure and independent of initial composition.

The experimental results for the separation of Ar, Ne, N₂, O₂, and CO from He were interpreted in the framework of a recently proposed theoretical model involving an electrostatic Peclet number. In the model the electric field was assumed to be constant. This assumption was checked experimentally and the maximum variation in electric field was 35% in time and 30% in position. Consequently, the assumption of constant electric field introduced no more than 55% variation in the electrostatic Peclet number during a separation.

To aid in the design of new cataphoretic systems, the following design criteria were developed and tested in detail: (1) electric field independent of discharge current, (2) electric field directly proportional to total pressure, (3) ion fraction of impurity directly proportional to discharge current, and (4) ion fraction of impurity independent of total pressure. Although these assumptions are approximate, they enabled the steady-state concentration profile to be predicted to within 25% for 75% of the data. The theoretical model was also tested with respect to the characteristic time associated with transient cataphoresis. Over 80% of the data was within a factor of two of the calculated characteristic times.

The electrostatic Peclet number ranged in value from 0.13 to 4.33. Back-calculated ion fractions of the impurity component ranged in value from 4.8x10^-6 to 178x10^-6.

Optimización de la cantidad y localización de Pt en catalizadores Pt/HBeta para hidrocraqueo de poliestireno en disolución

El objetivo general de este trabajo es avanzar en la optimización de catalizadores de platino para el hidrocraqueo de poliestireno en fase líquida en una sola etapa, hacia la obtención de combustibles líquidos, dentro de las diferentes alternativas para la valorización de residuos plásticos. Mediante este proceso, se pretende minimizar la cantidad de residuos plásticos que se destinan a vertedero, en el marco de la Directiva 2008/98/CE, como solución efectiva y eco-eficiente a su inevitable generación. En estudios previos, se ha determinado que catalizadores de platino soportados sobre zeolita HBeta resultaban adecuados para esta aplicación. Por otro lado, un profundo estudio de las distintas etapas de transferencia de materia, combinando resultados experimentales con correlaciones empíricas, ha permitido definir condiciones experimentales en las que se puede trabajar en régimen cinético, lo que resulta fundamental para trabajar en el diseño de catalizadores. Partiendo de estos resultados, los objetivos específicos del trabajo se han enfocado en:  Minimizar la cantidad de platino a emplear en un catalizador de Pt/HBeta para esta aplicación, teniendo en cuenta que se trata de un metal noble y que, por lo tanto, encarece el precio de los catalizadores de forma muy importante. Se trata, en este caso, de mantener adecuados niveles de actividad y, sobre todo, selectividad hacia los productos deseados. La selectividad, desde el punto de vista del platino, se relaciona principalmente, para el caso del poliestireno, con la presencia de productos de hidrogenación del monómero.  Optimizar el método de incorporación del platino al catalizador. El planteamiento, en este caso, es que, dado el elevado tamaño de las moléculas de polímero, la reacción de hidrocraqueo tendrá lugar, casi exclusivamente, sobre la superficie externa del catalizador, y la hidrogenación del monómero puede alcanzar una capa algo más profunda. En cualquier caso, parece evidente que el platino depositado en las capas más profundas del catalizador permanecerá desaprovechado, y sería interesante obtener una distribución de tipo “egg-shell”.

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.

Águas pluviais para usos não potáveis em escolas municipais: estudo de caso na região da baixada de Jacarepaguá, RJ.

A captação de águas pluviais não constitui nova estratégia ou tecnologia. No entanto, recentemente tem sido proposta em regiões bem desenvolvidas ou em desenvolvimento (peri-urbanas) em resposta a grandes períodos de estiagens, aumento da demanda por água, maior conscientização pública das enchentes urbanas e sua gênese e, aumento do interesse em práticas de construções sustentáveis, que integram também o uso racional da água. As escolas constituem uma importante fundação da nação, e tem influência no desenvolvimento da sociedade e da sensibilização/ conscientização sobre as questões ambientais. Muitos dos usos da água nas escolas envolvem usos menos nobres da água. Neste contexto, nessa dissertação de mestrado além da análise de marcos legais nesse assunto, foi realizada pesquisa de opinião (entrevista e questionário) junto a atores que interferem no processo decisório da utilização das águas pluviais nas escolas para fins não potáveis. Foram observadas as condições físicas-construtivas das escolas do município do Rio de Janeiro, sobretudo na região da 7a. CRE, que abrange a região da Baixada de Jacarepaguá, área de expansão da cidade. Foi implementada uma unidade para coleta e caracterização da qualidade das águas pluviais, além da caracterização e estudo dos volumes de primeiro descarte (first flush). Os parâmetros de qualidade da água pH, T, OD, ORP, Tu, STD, Condutividade e Salinidade, foram observados com auxílio de sonda multiparâmetros e, através de análise laboratorial de acordo com o Standard Methods, os coliformes termotolerantes. No estudo de percepção foi verificada uma grande aceitação do aproveitamento de águas pluviais para fins não potáveis, embora diretores de escola tenham apresentado informações/percepção divergentes sobre consumo e contas de água das escolas, de sua coordenadoria. Na análise dos parâmetros de qualidade da água versus registros pluviométricos foi observada variabilidade nos eventos pluviométricos observados que limitaram a correlação entre os mesmos, e acabou limitando as conclusões dos estudos de volumes para primeira lavagem e descarte (first flush). Os resultados da pesquisa permitem recomendar a implementação de políticas públicas para aproveitamento de águas pluviais para fins não potáveis nas escolas, mas, com o devido apoio tecnológico. Recomenda-se o aperfeiçoamento e automatização do sistema de coleta de águas pluviais para os estudos de first-flush e otimização dos volumes de descarte.

Quanto en caso de amores: a relação (extra)conjugal em três autos de Gil Vicente

Don Duardos, como comprovam as palavras preambulares da Copilaçam de 1586, surge como uma obra de viragem no tocante à produção teatral de Gil Vicente. Seria um serviço oferecido ao novo rei, D. João III, um serviço qualitativamente diferente do até então exercido. A diferença reside, segundo Vicente, no tratamento da temática amorosa, uma vez que sob o reinado de D. Manuel quanto en caso de amores apenas teria trabalhado com personagens das camadas baixas da sociedade, enquanto no novo serviço colocaria em cena figuras do estrato nobre. A presente dissertação empreende uma análise de três canônicos autos vicentinos, que tematizam a relação (extra)conjugal: Auto da Índia (1509) representado sob os auspícios da rainha D. Leonor de Lencastre , Tragicomedia de Don Duardos (1522) e Farsa de Inês Pereira (1523) tecidos durante o reinado de D. João III. Buscou-se comparar as protagonistas das referidas farsas e o modo como se desenvolvem suas relações extramatrimoniais, com o objetivo de evidenciar-lhes os pontos de convergência e divergência. Procurou-se, no Don Duardos, revelar a existência de uma escala de perfeição na qual se inserem as três diferentes relações amorosas apresentadas na peça. Sempre que pertinente, foram ressaltadas as alusões, por aproximação ou oposição, aos preceitos do amor cortês ditados pelo Tratado de André Capelão. Foi possível observar que somente os personagens não-nobres dão vazão aos anseios sexuais e mantêm relações adulterinas e que o fato de Gil Vicente se mostrar condescendente para com essas figuras ameniza o comportamento infiel das mesmas. Notou-se também que o autor condena de modo impiedoso a falsa galanteria praticada essencialmente por escudeiros ambiciosos e falsos cortesãos e que é a figura do cavaleiro, como se pôde perceber no Don Duardos, um modelo não somente na guerra, mas também no amor

Estudo de catalisadores modelo à base de CeO2-ZrO2 dopado com cobre para controle de emissões de NOx

Convencionalmente, metais nobres são empregados como metais ativos em catalisadores automotivos, mas o uso de cobre vem sendo estudado pelo fato de promover sítios ativos para adsorção química e redução de NOx. Diante deste contexto, esta dissertação visa testar novas formulações de catalisadores, com foco em seu desempenho na reação de redução do NO pelo CO e sua seletividade a N2. Foram avaliados o método de adição de cobre no preparo e os teores de cobre utilizados na preparação. Os métodos de adição utilizados foram impregnação a seco (IS), reação em estado sólido (RS) e coprecipitação (CO). Os teores de cobre estudados ficaram entre 0,36 e 6,9% (m/m). Além disso, foi estudado o impacto no desempenho do catalisador após envelhecimento térmico a 950C por 12h. Foram empregadas as seguintes técnicas de caracterização textural e físico-química como espectrometria de absorção atômica, fisissorção de N2, difração de raios X, espectroscopia Raman e redução a temperatura programada. Os catalisadores também foram avaliados na reação de redução do NO pelo CO. A análise textural indicou que o método de coprecipitação levou a características texturais diferentes dos outros catalisadores. Análises de DRX mostraram a formação de CuO cristalino para teores iguais ou superiores a 3,3% (m/m) de cobre. As análises de Redução a Temperatura Programada (RTP) indicaram que ocorreu uma forte interação na interface entre o suporte e as espécies de cobre dispersas, acompanhada da diminuição da temperatura de redução do CuO e da redução parcial da céria em temperaturas mais baixas. Os testes catalíticos mostraram um melhor desempenho dos catalisadores (IS) que apresentaram conversões mais elevadas em menores temperaturas. Com relação ao envelhecimento, observou-se uma diminuição significativa da eficiência dos catalisadores. Uma comparação com catalisadores à base de metal nobre mostrou um bom desempenho dos catalisadores à base de cobre, com a vantagem destes apresentarem emissão de N2O restrita a baixas temperaturas

A representação social do cuidado ao paciente soropositivo ao HIV/Aids entre profissionais de saúde

Este estudo tem como objetivo identificar a estrutura representacional do cuidado em saúde ao paciente soropositivo ao HIV/Aids entre os profissionais da equipe de saúde, descrever a representação do cuidado em saúde através das abordagens estrutural e processual, analisar o cuidado em saúde a partir das representações construídas por essa equipe e discutir a mudança de conhecimentos e práticas de cuidado em saúde a partir das representações. Pesquisa qualitativa, descritiva e exploratória, orientada pela Teoria das Representações Sociais. Os sujeitos do estudo foram profissionais de saúde atuantes em instituições públicas no Rio de Janeiro, sendo na primeira etapa, 148 profissionais de 20 instituições e, na segunda, 23 de duas instituições. A coleta de dados deu-se através de questionários de caracterização, evocações livres e entrevista semiestruturada. A análise dos dados utilizou o quadro de quatro casas a partir do software EVOC 2003, a análise de similitude e a análise lexical pelo software Alceste 4.10. Com relação à estrutura da Representação, destaca-se que o Núcleo Central foi composto por: amor, acolhimento, informação, respeito, adesão-tratamento e não-discriminação, que indicam uma dimensão relacionada aos aspectos afetivos, práticos e funcionais do cuidado. Na zona de contraste, ressalta-se a presença da proteção-profissional. A partir da análise de similitude foi possível perceber a tendência à centralidade do léxico amor. Ele organiza a representação e possui forte ligação com o termo solidariedade. Na análise realizada pelo Alceste, foram definidas seis classes: A constituição da equipe de saúde e o processo de cuidar: definições, práticas e dificuldades; As práticas de proteção adotadas pelos profissionais frente ao HIV; As formas de enfrentamento diante do diagnóstico positivo ao HIV; Atitudes profissionais: avaliações e julgamentos; As memórias sociais sobre a aids: origem, circulação, informação e imagens e, por fim, A epidemia de aids nos dias atuais. Conclui-se que a representação social do cuidado entre profissionais de saúde tem, em sua estrutura e organização, a interação sustentada por uma arqueologia que se liga aos considerados sentimentos nobres e às ações de abnegação e de superação humanas, tendo como elemento central o amor que caracteriza suas ações e influencia sua práxis. A importância da oferta desse cuidado amoroso está em sua relação com a humanização das ações assistenciais, atendendo à demanda do indivíduo durante a manifestação da doença, respeitando sua singularidade como ser humano e facilitando seu processo de adoecimento e busca pela melhoria da saúde.