972 resultados para diferencia
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El propileno es un monómero muy versátil y es la materia prima para una amplia gama de polímeros, intermedios y productos químicos. Esta versatilidad se debe a su estructura química: al igual que el etileno, el propileno contiene un doble enlace carbono - carbono, pero a diferencia de éste, el propileno contiene también un grupo metil - alílico (un grupo metilo adyacente a un doble enlace), otorgando a los químicos, diseñadores catalíticos e ingenieros dos distintas alternativas para llevar a cabo las trasformaciones químicas, por lo que son más numerosos los derivados del propilen o que del etileno (Plotkin, 2005).
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A criança, nos primeiros anos de vida, entra em contato com a leitura pela via lúdica, no seio familiar. Ao ingressar na escola, nas séries iniciais, continua exposta a textos que têm como característica principal o lúdico e o prazeroso. Com o avançar das séries, a postura em relação à leitura vai mudando e passa a mote para a apresentação e desenvolvimento dos conteúdos curriculares. O gosto pela leitura que aproximou o discente do texto é aos poucos deixado de lado. O aluno vai perdendo o interesse pela leitura e já é lugar comum na escola, quiçá na sociedade atual, dizer que o aprendiz não gosta de ler, não sabe ler com competência, por isso, não consegue acompanhar as exigências escolares. Na prática docente, observa-se que os alunos leem, visto as numerosas publicações destinadas aos jovens, não leem o que a escola quer. Tal constatação leva a questionamentos acerca do problema e a pensar em um caminho para resgatar no discente a curiosidade, o gosto e o prazer pela leitura de um bom texto, fato corroborado pelos PCNs. Com o intuito de trabalhar essa nuança da leitura, que está relegada a segundo plano pela escola, decidiu-se pelo desenvolvimento de uma oficina de leitura com alunos do 8 ano do Ensino Fundamental de uma escola pública da cidade do Rio de Janeiro, organizada por gêneros textuais trabalhados um por vez, e levar os alunos a ler textos originais e completos, fugindo à fragmentação do livro didático. A seleção do material de leitura foi feita pela pesquisadora e, quando necessário, foi solicitada a colaboração dos jovens, além da utilização dos recursos disponíveis na escola. Adotou-se as posições teóricas de Mikhail Bakhtin (2006) acerca de língua, fala e enunciação; dialogismo e polifonia para corroborar as afirmações. No que se refere a texto, discurso e gêneros textuais, se tomou como base o trabalho de Coutinho (2004) e Marcuschi (2008). Para analisar as questões que envolvem leitura, principalmente, a escolar, foram consultados os PCNs e o trabalho de Silva (1998). Dentre outros. As atividades da oficina levaram à reflexão sobre as práticas de leitura na escola, pois, mesmo os PCNs propondo uma abordagem sociointeracionista, na realidade, não funciona. O livro didático ainda é a base do trabalho do professor. Outra forma de apresentação do texto em outros ambientes promoveu um trabalho produtivo no qual a maioria se envolveu e saiu da condição de leitores passivos a ativos e participativos. Houve diversas dificuldades, porém, ficou a certeza que se fez a diferença e se resgatou muito do leitor adormecido em cada aluno participante. As afirmações valem para esse pequeno grupo da investigação, não se podendo generalizar
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Comunicación presentada en JEL 2013 - X Jornadas de Economía Laboral (Madrid, 11 y 12 de Julio de 2013)
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Objetivos: Estudiar cómo afecta a la concentración de determinados factores de crecimiento presentes en los sueros la filtración (utilizado como método de esterilización) y el tratamiento por calor (utilizado para la inactivación del complemento). Además de estudiar el efecto de un bioadhesivo (ácido hialurónico, HaNa), aplicado solo o conjuntamente con el suero rico en factores de crecimiento (s-PRGF), sobre la capacidad de las células de epitelio corneal (HCE) para proliferar y migrar. Materiales y métodos: Se midió mediante kits ELISA comerciales la concentración en las diferentes condiciones de filtración y calentamiento de las siguientes biomoléculas EGF (Epidermal Growth Factor), VEGF (Vascular Endothelial Growth Factor), HGF (Hepatocyte Growth Factor), PDGF (Platelet-derived Growth Factor) y la Fibronectina. Teniendo en cuenta el papel de la proliferación y migración celular en los procesos de cicatrización se han realizado dos ensayos diferentes in vitro: un ensayo MTT para estudiar la viabilidad y la proliferación celular y el método de la herida (Scratch wound-healing assay) para determinar la capacidad migratoria de células bajo ciertos tratamientos: BSA (Bovine Serum Albumin) al 1% como control, FBS (Fetal Bovine Serum) al 10%, s-PRGF al 45%, s-PRGF al 45% con HaNa 0,1% y HaNa al 0,1% Resultados: En el caso de la filtración, se observa una mayor pérdida de factores utilizando un filtro con una membrana de PVDF (Durapore®) para todos los factores estudiados. El calentamiento produce una reducción de la concentración superior al 50% en el caso del HGF y EGF, manteniéndose constante en el caso del VEGF.La mezcla de diferentes muestras con el complemento inactivado para formar un pool no presenta cambios en la concentración al compararlo con la media de las muestras utilizadas. Por tanto, la utilización de un pool del hemoderivado no supone perdida de factores de crecimiento, haciendo de ello un procedimiento perfectamente aceptable para los ensayos celulares. El tratamiento con s-PRGF y el combinado con el bioadhesivo promueven la proliferación y migración de las células de epitelio corneal humano(HCE) in vitro de manera similar, no encontrándose diferencias estadísticamente significativas entre ambos. Conclusiones: La adicción del bioadhesivo no produce efecto tóxico en las células, sin embargo, no se han encontrado efectos beneficiosos en cuanto a proliferación y migración se refiere. A este respecto, creemos que hay que dar un paso más haciendo comprobaciones in vivo, ya que, a diferencia de la experimentación in vitro los componentes de los hemoderivados no están indefinidamente en contacto con las células sino por un espacio de tiempo muy reducido. Por ello, la concentración de factores de crecimiento en la aplicación in vivo es especialmente importante, y no sería conveniente reducirla mediante procedimientos físicos como la filtración o el calentamiento.
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.INTRODUCCIÓN. 1.1. COMPUESTOS 1,3 - DICARBONÍLICOS. METILENOS ACTIVOS. Los compuestos 1,3 - dicarbonílicos son uno de los bloques sintéticos más utilizados a lo largo de la historia de la síntesis orgánica. Esto se debe a sus múltiples centros de reactividad: dos centros reactivos electrófilos y hasta cinco centros nucleófilos, como se puede ver en la Figura 1, que permiten r ealizar infinidad de secuencias de reacciones para generar moléculas complejas. 1 R R O O Figura 1 . Centros reactivos de los compuestos 1,3 - dicarbonílicos. Se conoce un gran número de reacciones para esta familia de compuestos pero en este texto nos vamos a centrar en estudiar tres casos especialmente característicos por el potencial sintético que proporcionan, y que están muy relacionados con el hecho de que los hidrógenos de la agrupación metilénica son especialmente ácidos. Por ejemplo, el pKa de estos protones, en el caso del malonato de dietilo es de 13 unidades, mientras que el de su éster simple es de 24. 2 Esta notable diferencia en la acidez se explica fácilmente por la diferente estabilidad de los aniones enolatos correspondientes para los que la deslocalización de carga por resonancia está más extendida en el primer caso (Figura 2). Figura 2 . Representación de las formas resonantes del anión enolato malonato de dietilo. EtO OEt O O - EtO OEt O O EtO OEt O - O Nu Nu Nu Nu Nu E E 2 Las reacciones más conocidas que se aprovechan de esta característica estructural son, probablemente, la reacción de Knoevenagel, la síntesis malónica y acetilacética y un buen número de reacciones multicomponente, para los que haremos unos comentarios particulares en los siguientes apartados
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Índice: - Formulación Lagrangiana. - Formulación Hamiltoniana. - Ecuación de Hamilton-Jacobi. - Teoría de Perturbaciones. - Sistemas Continuos. - Mecánica y Geometría Diferencia
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Nerea Aresti ha analizado la contribución de científicos e intelectuales católicos en la modernización de la sociedad española, probando que la categoría de género es fundamental para el análisis de la historia. Nuevas imágenes de masculinidad y feminidad basadas en principios biológicos y médicos se constituyeron en una pieza clave de la cultura liberal. En este proceso, figuras como Gregorio Marañón magnificaron la diferencia sexual a expensas de la igualdad, ayudando a crear una noción de liberalismo totalmente peculiar. Este libro no es un libro más. Se trata de un estudio brillante que representa un verdadero punto de inflexión en su campo.
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En la última década Mindfulness ha despertado gran interés como tratamiento terapéutico en la salud psicológica. Está inmerso en lo que ya se denominan Terapias de Tercera Generación, donde la aceptación es el concepto en cuál se centra. Existen varios programas en los que se aplica esta terapia y se han realizado estudios para numerosas aplicaciones clínicas, dando evidencia científica al respecto. El objetivo de esta revisión narrativa es la de conocer la eficacia de la aplicación de la terapia Mindfulness para reducir los síntomas de ansiedad en personas adultas de Atención Primaria. Para ello, se revisan los fundamentos teóricos y mecanismos de acción de Mindfulness, y de qué manera actúa en los trastornos de ansiedad. Dentro de este marco, se expone en la discusión la aplicación de la terapia en Atención primaria y la posibilidad de ser una herramienta para el profesional de Enfermería. Finalmente, se concluye que Mindfulness tiene un efecto moderado para reducir los niveles de ansiedad, aunque sin gran diferencia respecto a las Terapias Cognitivo Conductuales utilizadas hasta el momento. Se observa una necesidad de mayor evidencia científica que respalde la idoneidad de la aplicación de Mindfulness en personas adultas de Atención Primaria para reducir los niveles de ansiedad. Y siendo esta terapia una herramienta idónea para ofrecer por parte del personal de Enfermería, existen pocos estudios en los que Enfermer@s sean los que aplican Mindfulness
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[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.
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361 p.