USP1 deubiquitinase: cellular functions, regulatory mechanisms and emerging potential as target in cancer therapy

12 p.

Design of an optimised wheel profile for rail vehicles operating on two track gauges

This paper sets out an optimum synthesis methodology for wheel profiles of railway vehicles in order to secure good dynamic behaviour with different track configurations. Specifically, the optimisation process has been applied to the case of rail wheelsets mounted on double gauge bogies, that move over two different gauges, which also have different types of rail: the Iberian gauge (1668 mm) and the UIC gauge (1435 mm). Optimisation is performed using Genetic Algorithms and traditional optimisation methods in a complementary way. The objective function used is based on an ideal equivalent conicity curve which ensures good stability on straight sections and also proper negotiation of curves. To this end the curve is constructed in such a way that it is constant with a low value for small lateral wheelset displacements (with regard to stability), and increases as the displacements increase (to facilitate negotiation of curved sections). Using this kind of ideal conicity curve also enables a wheel profile to be secured where the contact points have a larger distribution over the active contact areas, making wear more homogeneous and reducing stresses. The result is a wheel profile with a conicity that is closer to the target conicity for both gauges studied, producing better curve negotiation while maintaining good stability on straight sections of track. The paper shows the resultant wheel profile, the contact curves it produces, and a number of dynamic analyses demonstrating better dynamic behaviour of the synthesised wheel on curved sections with respect to the original wheel.

Role of G protein coupled inwardly rectifier K+ channels (GIRK) on the neurobiology depression

353 págs.

Clinical factors associated with a Candida albicans Germ Tube Antibody positive test in Intensive Care Unit patients

Background: Poor outcomes of invasive candidiasis (IC) are associated with the difficulty in establishing the microbiological diagnosis at an early stage. New scores and laboratory tests have been developed in order to make an early therapeutic intervention in an attempt to reduce the high mortality associated with invasive fungal infections. Candida albicans IFA IgG has been recently commercialized for germ tube antibody detection (CAGTA). This test provides a rapid and simple diagnosis of IC (84.4% sensitivity and 94.7% specificity). The aim of this study is to identify the patients who could be benefited by the use of CAGTA test in critical care setting. Methods: A prospective, cohort, observational multicentre study was carried out in six medical/surgical Intensive care units (ICU) of tertiary-care Spanish hospitals. Candida albicans Germ Tube Antibody test was performed twice a week if predetermined risk factors were present, and serologically demonstrated candidiasis was considered if the testing serum dilution was >= 1: 160 in at least one sample and no other microbiological evidence of invasive candidiasis was found. Results: Fifty-three critically ill non-neutropenic patients (37.7% post surgery) were included. Twenty-two patients (41.5%) had CAGTA-positive results, none of them with positive blood culture for Candida. Neither corrected colonization index nor antifungal treatment had influence on CAGTA results. This finding could corroborate that the CAGTA may be an important biomarker to distinguish between colonization and infection in these patients. The presence of acute renal failure at the beginning of the study was more frequent in CAGTA-negative patients. Previous surgery was statistically more frequent in CAGTA-positive patients. Conclusions: This study identified previous surgery as the principal clinical factor associated with CAGTA-positive results and emphasises the utility of this promising technique, which was not influenced by high Candida colonization or antifungal treatment. Our results suggest that detection of CAGTA may be important for the diagnosis of invasive candidiasis in surgical patients admitted in ICU.

Aquatic insects as target organisms for the study of effects of projected climate change in the British Isles

One of the objectives of the Terrestrial Initiative in Global Environmental Research is to assess the sensitivity of British plant and animal species to climate change. The first phase of the program involved the identification of criteria for selecting species suitable for the study of effects of projected climate change in the British Isles. Apart from shallow ponds, annual temperature ranges of 0 to 25 C in temperate freshwater habitats are narrower than those in most temperate terrestrial habitats. Although freshwater organisms have to exist within a narrower range than their terrestrial equivalents, few species can survive throughout their life cycle over the whole temperature range. Field studies on the effects of natural and artificial thermal discharges into streams and rivers have shown that increases in water temperature affect aquatic insects at both the species and community level. Although field data provide valuable information, a more productive approach is to determine experimentally the requirements of different species. Although there are just over 1850 species of aquatic insects in the British Isles, detailed quantitative information on the relationship between temperature and development of eggs, larvae and pupa is available for relatively few species. One exception is the egg stage of stoneflies (Plecoptera). The range for egg hatching in stoneflies clearly show that some species could be threatened while others could benefit from a defined increase in water temperature as a result of climate change. A critical review of the available data on this group would produce a set of equations that could be used to predict the ecological effects of climate change on this group of indicator species.

Impacto da campanha de vacinação para influenza em uma empresa

A influenza é uma das doenças respiratórias agudas mais prevalentes e importante causa de absenteísmo e presenteísmo. Entretanto, a eficácia vacinal para influenza pode alcançar 80% quando há elevada correspondência entre cepas vacinais e circulantes. Por este motivo, a empresa há anos promove campanha de vacinação, contudo, sem estimar sua efetividade (eficácia na redução da carga da doença) e o impacto econômico (produtividade) para o aprimoramento de sua política de saúde ocupacional. Considerou-se que a efetividade da campanha seria determinada pela eficácia vacinal previamente demonstrada em estudos randomizados, pelo grau de acurácia diagnóstica ou de triagem dos casos, pelo nível de adesão do profissional de saúde ao registro no prontuário e do paciente ao informar a ocorrência dos sintomas e pela cobertura vacinal alcançada. Com os objetivos de avaliar a efetividade e impacto econômico da campanha de vacinação para influenza, optou-se por um desenho estudo observacional de coorte histórico com características de estudo de intervenção baseado em dados históricos da campanha de 2008 e informações individuais sobre a frequência de sintomas respiratórios e absenteísmo, idade, gênero, função (administrativa e operacional) e renda, comorbidades relevantes e tabagismo, obtidas mediante revisão de prontuário dos 12 meses subsequentes, comparadas entre os grupos de vacinados e não-vacinados (qui-quadrado e test t) e analisadas por regressão logística, e estimada a fração prevenível (proporção de episódios potenciais de influenza evitados pela vacinação). Foram analisados os prontuários de 2.425 trabalhadores (1.651 não-vacinados e 754 vacinados) correspondendo à cobertura de 31,1%. A prevalência de influenza observada foi de 10,4% e a vacinação foi efetiva entre os trabalhadores (RR=0,51; IC95% 39-67), quando considerados os sintomas de alta probabilidade de influenza. A fração prevenível foi 0,09 (9 casos evitados a cada 100 trabalhadores vacinados). A campanha de vacinação foi mais efetiva e provocou maior impacto econômico entre os trabalhadores em regime operacional.

Influência de agentes clareadores na rugosidade de compósitos dentários

O clareamento dental é o meio disponível mais simples, comum e conservador para o cirurgião-dentista proporcionar aos pacientes o padrão de cor de seus dentes mais desejado. Em alguns casos, os dentes que vão ser clareados podem apresentar restaurações realizadas com compósitos dentais, que são mais suscetíveis a alterações químicas, quando comparados a outros materiais restauradores. Alguns estudos mostraram que diferentes concentrações de agentes clareadores levaram a um aumento significativo da rugosidade superficial e das porosidades em compósitos dentais. Este estudo avaliou o efeito de dois agentes clareadores (Whiteness HP Blue 20%, Whiteness HP Max) sobre a rugosidade superficial de dois compósitos dentais, um micro-híbrido (Esthet X, Denstply) e outro nanoparticulado (Z 350, 3M ESPE). Um total de oito corpos de prova (9 x 2 mm) foram confeccionados com auxílio de uma matriz de teflon, sendo divididos em 4 grupos (Esthet X + Whiteness HP Blue 20%; Esthet X + Whiteness HP Max; Z 350 + Whiteness HP Blue 20%; Z 350 + Whiteness HP Max), sendo n=2. Os corpos de prova foram armazenados em saliva artificial neutra e, após 24 horas, foram polidos com discos de óxido de Alumínio (Sof-lex, 3M ESPE). Após sete dias de imersão salivar, cada corpo de prova foi levado a um microscópio de força atômica para obtenção do valor inicial de rugosidade superficial (Ra em nm). Em seguida, sem remover o corpo de prova do microscópio, o agente clareador foi aplicado sobre a superfície do corpo de prova, segundo as instruções do fabricante, de modo que permitisse uma posterior observação da mesma área do corpo de prova observada inicialmente, para obtenção do valor final de rugosidade superficial. Imagens em duas e três dimensões foram obtidas de cada corpo de prova para observação de alterações da topografia. Os resultados foram tratados estatisticamente por ANOVA e pelo teste de contraste Student-Newman-Keuls (p < 0,05). Não houve alteração significativa na rugosidade superficial (Ra) dos corpos da prova de compósitos micro-híbrido e nanoparticulado, submetidos aos agentes clareadores Whiteness HP Blue 20% e Whiteness HP Maxx. No entanto, independente do agente clareador utilizado, foram observadas maiores alterações topográficas nas imagens de microscopia de força atômica da superfície do compósito micro-híbrido do que nas imagens do nanoparticulado.

Estudo aleatório e controlado do uso clínico de um primer autocondicionante na colagem de bráquetes ortodônticos

O uso de primers autocondicionantes tem sido proposto como uma alternativa para a redução de passos clínicos. O objetivo deste estudo clínico aleatório e controlado foi avaliar a performance de um sistema autocondicionante (Transbond Plus Self-Etching Primer, 3M Unitek - SEP) comparado a um sistema multipasso convencional (Transbond XT, 3M Unitek - TBXT) de colagem ortodôntica, durante um período de 12 meses. Vinte e oito pacientes participaram deste estudo, sendo estes alocados aos grupos SEP ou TBXT de forma aleatória, através de randomização em bloco. Um total de 548 bráquetes metálicos (Micro-Arch, prescrição Alexander, GAC International, Bohemia, NY) foram colados com uso da pasta adesiva Transbond XT (3M Unitek), sendo todos os produtos manuseados de acordo com as recomendações dos fabricantes. Foram totalizados 276 bráquetes no grupo controle e 272 no segundo. Curvas de sobrevivência Kaplan-Meier e o teste log-rank (p<0,05) foram utilizados para comparar o percentual de falhas adesivas para as duas técnicas. Ao final do período foram verificadas trinta e duas falhas adesivas (bráquetes descolados), sendo 19 (6,98%) falhas quando utilizado o primer autocondicionante (SEP) e 13 (4,71%) quando usado o primer convencional (TBXT). Não houve diferença significante entre a sobrevivência dos bráquetes entre os dois grupos avaliados (log-rank test, p=0,311). Quando a influência de gênero do paciente, arco dentário e tipo dentário (anterior ou posterior) foram analisados, somente o tipo dentário foi achado significante. Bráquetes de dentes posteriores apresentaram uma maior probabilidade de falha adesiva que os colados em dentes anteriores (p=0,013) Os autores concluem que o primer autocondicionante pode ser utilizado para colagem direta de bráquetes ortodônticos sem que sua sobrevivência clínica seja afetada.

Influência do acabamento e polimento na resistência à flexão de uma cerâmica odontológica

Avaliou-se a influência de dois sistemas de acabamento e polimento na resistência à flexão de uma cerâmica feldspática EX-3 (Noritake). Para isto, confeccionou-se blocos cerâmicos com medidas em conformidade com a ISO 6872/1995. Em seguida obteve-se o glaze natural. A padronização da rugosidade superficial foi conferida com auxílio de um rugosímetro, e os blocos foram então divididos em cinco grupos. O Grupo I (controle) foi testado com glaze. Para os testes realizados nos demais grupos, os blocos receberam um tratamento de asperização por meio de uma ponta diamantada 4137 (KG Sorensen). Em seguida foram polidos com diferentes protocolos. No grupo II, o sistema de polimento dura white (Shofu). No grupo III, o sistema de polimento dura white (shofu) associado a uma pasta diamantada aplicada com disco de feltro. No grupo IV o sistema de polimento Exa Cerapol (Edenta) e no grupo V, este mesmo sistema mais pasta diamantada aplicada com disco de feltro. Após os procedimentos de acabamento e polimento, foi avaliada a rugosidade conseguida (Ra), para se avaliar a eficácia dos métodos testados. A análise estatística por ANOVA (p ≤ 0,05) mostrou não haver diferença estatisticamente significante entre os grupos (G2=3,820,58; G3=3,550,61; G4=4,050,40; G5=3,950.47) . Feito isto, os corpos-de-prova foram submetidos a um ensaio mecânico de resistência à flexão em três pontos, e também neste caso, os resultados depois de tratados estatisticamente não demonstraram diferenças estatísticas entre os grupos glazeados e os grupos que receberam tratamento (G1=132,126,9 MPa; G2=123,317,4 MPa; G3=114,519,3 MPa; G4=104,211,9 MPa e G5=104,719,1 MPa) . Após a realização destas avaliações, tornou-se possível concluir que o uso dos sistemas de acabamento e polimento testados neste trabalho permite obter superfícies com rugosidade similar a obtida com o glaze natural e não interferem na resistência à flexão da cerâmica utilizada.

A interpretação de texto na escola: o sentido pode ser outro

A presente pesquisa objetiva auxiliar o professor no trabalho da interpretação, articulando a academia e a escola. Buscou-se entender melhor o que é interpretação e o que pode ser ensinado ao aluno para que a pratique com mais proficiência. Partiu-se da hipótese de que não há uma metodologia precisa para o ensino de interpretação. Para testá-la, aplicou-se uma atividade de interpretação baseada na crônica Povo, de Luis Fernando Verissimo, retirada de um livro didático, às turmas de 8o ano do Ensino Fundamental e 2o ano do Ensino Médio de 4 colégios públicos do Rio de Janeiro (Cap UERJ, Cap UFRJ, CMRJ e CP II) Analisou-se como os alunos respondiam às questões propostas. Pretende-se mostrar, conforme a teoria de Orlandi (2002: 64), que interpretar não é atribuir sentidos, mas explicar como o texto produz sentidos, inclusive, sentidos que podem ser sempre outros, divergentes do esperado pelo livro didático ou pelo gabarito do professor. Imaginava-se que os resultados fossem semelhantes; toda via, o EF obteve 40% de acertos, enquanto o EM obteve 60,7%. Apesar dos resultados diferentes, foi possível realizar a atividade em duas séries tão distintas, porque a seleção do texto é de interesse de ambas. Identificaram-se a inferência, a polissemia, a metáfora e o contexto como elementos que auxiliam a interpretação, pois se fizeram presente na análise dos dados, mostrando que é possível praticá-los. Logo, apesar de não haver uma metodologia precisa e seriada para o desenvolvimento da interpretação, não significa que não haja o que se possa trabalhar. Defende-se que esses elementos podem ser aplicados em todas as séries e o que irá se diferenciar é o grau de complexidades dos textos, que mudam a cada série. É necessário trabalhar a interpretação em sala de aula com respaldo teórico, operacionalizá-la, apontando estratégias, oferecendo subsídios aos alunos. O presente trabalho busca lançar luz sobre um campo profícuo justamente por tratar de um tema complexo com várias divergências de pensamento e nomenclaturas e, ao mesmo tempo, tão relevante, porque, além de fazer parte da vida estudantil, ultrapassa os muros da escola

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.

Encircled energy measurement for focusing lens based on scanning Hartmann test

The encircled energy of a focusing lens is one of the parameters directly affecting the target efficiency in high-power laser facilities. The direct measurement method of the encircled energy for the focusing lens based on the scanning Hartmann test is proposed in this paper. With the scanning Hartmann test setup, the information in the whole aperture of the focusing lens can be achieved. The encircled energy can be obtained by analyzing the spot diagram on the focal plane of the focusing lens. In experiments, the encircled energy of an aspheric focusing lens is measured using this method. The measurement result is in good agreement with that derived from measurement data by an interferometer and the difference is 7.7%. (C) 2006 Elsevier GmbH. All rights reserved.

Financial and Economic Report of a Specific Business Group

As a result of the natural evolution of the economy, ever-changing, unpredictable and cyclical, companies must adapt as far as possible to the changes that have taken place in order to continue with their normal operating activities. Likewise, they should also try to maintain a structure for long-term growth, trying at all times to generate the maximum value. The main objective of this project is to provide financial advisory services to a business group, trying to forward solutions and measures that according to the author can be effective. For this end, the situation of the group in question is analysed from early 2008 to the present day, examining its evolution, what steps have been taken together with their corresponding results and the economic-financial situation of the company at the end of last year. Contact with the company was kept throughout the process of analysis and assessment trying to take advantage of the feedback generated so that the appropriate measures can be adopted if the management considers it to be adequate.

Avaliação de uma resina polimérica contendo nanopartículas de prata

Neste trabalho foi testada a eficiência antimicrobiana de um nanocompósito de prata preparado a partir da modificação da resina comercial Lewatit VPOC1800 (contendo grupos sulfônicos) para três espécies de bactérias (Staphylococcus aureus, Pseudomonas aeruginosa e Escherichia coli.) cuja estrutura e composição das camadas externas da parede celular são distintas. Em termos da susceptibilidade aos biocidas essa diferença pode significar um fator importante de estudo. A avaliação da atividade biocida foi feita através de experimento que estimou a zona de inibição proporcionada pela atividade da resina sobre as bactérias estudadas. A resina mostrou eficiência biocida que aparentemente não é afetada pelas diferenças morfológicas das bactérias estudadas. Uma série de teste em batelada foi realizado com o intuito de se verificar a massa da resina e o tempo de contato ideal com a solução a ser descontaminada, chegando aos valores de 0,2g e 1minuto. As diferentes concentrações bacterianas utilizadas no estudo não influenciaram na atividade antimicrobiana da resina. Um estudo em coluna foi realizado para se averiguar o ponto de saturação do compósito, observando-se que a curva de ruptura da resina segue um tendência exponencial crescente igual a todas as espécies estudas, atingindo a saturação em aproximadamente 2250 mL

A field guide for Agency staff operating the SIMRAD EY500 portable scientific echosounder. 2nd draft 3rd August 1999

This manual has been produced by members of the national acoustics group (NAG) and represents the first in a series of outputs designed to promote co-ordination and consistency in Agency hydroacoustic surveys. It is designed as a field guide for Agency staff operating the SIMRAD EY500 portable scientific echosounder. It should be simplistic enough for the newcomer to EY500 to be able to set up and run a mobile hydroacoustic survey with some knowledge of the supporting theory. It should act as guidance for standardisation of survey procedures providing a concise list of settings and recommendations that can be used as a quick reference guide in the field. This manual condenses 5 years of practical experience of surveying fish populations using Simrad hardware and software for surveying large rivers and still waters throughout England and Wales. This document should be used as a companion to the manufacturers instruction manual and not act as a substitute for it.