Navegar na imagem e se reencontrar com o texto escrito: um estudo de caso exploratório do processamento leitor no ciberespaço

A presente dissertação é um estudo de caso com caráter exploratório (Rampazo, 2005; Babie, 2008). Na parte teórica, propomos a categorização triádica das imagens no ciberespaço, que é uma das contribuições deste trabalho para a área de estudos sobre leitura no ciberespaço. A investigação apresenta como objetivos acompanhar e analisar o processo leitor de um professor de espanhol como língua estrangeira no ciberespaço, tendo como foco a multimodalidade. Tais objetivos têm a função de nortear a resolução dos problemas de pesquisa, a saber: (a) como um professor de ELE lê no ciberespaço tendo em vista as imagens como aspectos da multimodalidade; (b) como esse professor transpõe sua própria atividade leitora e os materiais da internet para uma atividade de aula. Os instrumentos de coleta utilizados foram: entrevista, questionário, protocolos e gravações do GTK. O cruzamento entre 12 critérios de análise permitiu, dentre outros detalhes, observar que nosso sujeito lê textos verbais no ciberespaço movimentando o cursor do mouse como se fosse seus dedos sobre uma folha de papel a percorrer linha a linha da esquerda para a direita. Também percebemos que a experiência de leitura no ciberespaço (conhecimentos prévios) pode ser o fator que contribui para que o sujeito despreze as imagens de categorias mescladas (B e C) e prefira utilizar as imagens de categoria B, no caso, por exemplo, de acessar uma reportagem a partir de sua manchete em jornal eletrônico. Quanto à transposição de materiais para as aulas, percebemos que a formação acadêmica de nosso sujeito ao não direcionar discussões teóricas e metodológicas sobre as TICs e seu uso em sala de aula e sua realidade de trabalho podem ter contribuído para o modo como o sujeito transpõe os materiais da internet para as aulas. As adaptações e afastamentos desses materiais não são trabalhados em sala de aula. As imagens e links são retirados e o texto utilizado na atividade docente é uma mistura de vários materiais provenientes de diferentes países, mas sem a fonte especificada na aula. O papel que a formação tem para a vida profissional e para a práxis do professor não pode ser descartado. Defendemos que uma formação que seja direcionada às TICs deve fazer parte do currículo acadêmico

Optimización de la metodología para la producción de hongos comestibles

El cultivo de hongos comestibles saprófitos constituye un sistema de producción-consumo, que ha adquirido gran relevancia social, económica y ecológica. Con el fin de abaratar costes a la vez que aprovechar y reciclar residuos forestales, el objetivo de este trabajo se ha centrado en evaluar la viabilidad del aserrín de Eucalyptus globulus como soporte del cultivo en bolsa de Lentinula edodes (hongo comercializado conocido como Shiitake) y Agrocybe aegerita (hongo no comercializado comúnmente llamado Seta de Chopo). Se han evaluado 6 formulaciones, todas ellas con el aserrín como componente principal y con adición de diferentes suplementos: cereales (salvado y mijo), un controlador del pH (CaCO3) y un estimulador de crecimiento (CaSO4). Se ha determinado el crecimiento miceliar sobre cada uno de los sustratos, así como la producción de carpoforos (tanto en cantidad como en calidad) y la duración del periodo de fructificación. La mezcla más efectiva para la producción de L. edodes fue aquella que contenía yeso y azúcar mientras que para A. aegerita el salvado resultó ser el mejor suplemento.

Producción de hidrógeno por reformado catalítico en fase acuosa de disoluciones de metanol. Catalizador de Platino.

El objetivo que persigue la línea de investigación en la que se engloba este trabajo es la obtención de hidrógeno desde disoluciones acuosas de metanol (aproximadamente del 10% de metanol), considerando estos compuestos como una forma de almacenar hidrógeno y obtenerlo a baja temperatura “on-board” en un vehículo mediante el reformado en fase acuosa. El reto es conseguir un sistema catalítico de pequeño volumen y rápida respuesta a las demandas de hidrógeno con elevado rendimiento y calidad apropiada (<10 ppm de CO) para las pilas de combustible PEM. Los objetivos planteados en el siguiente trabajo se centran en la preparación y caracterización de un catalizador de platino soportado en alúmina, y la puesta en marcha de un reactor discontinuo de mezcla perfecta a presión para la evaluación de catalizadores en el proceso de reformado en fase líquida.

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

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

Síntesis de catalizadores orgánicos : síntesis de organocatalizadores quirales basados en la estructura de BINOL

Se define como quiralidad a la propiedad de un objeto de no ser superponible con su imagen especular. Así, cuando una molécula posee dicha propiedad , surgen dos isómeros configuracionales conocidos como enantiómeros . A la mezcla 1:1 de enantiómeros se le llama mezcla racémica o racemato y se caracteriza por no ser ópt icamente activa . Ambos enantiómeros presentes en la mezcla tienen las mismas propiedades físicas y químicas a excepción de su actividad óptica , aunque su comportamiento frente a dianas biológicas puede variar dependiendo del enantiómero

Valoración de bio-oil completo por craqueo catalítico en condiciones de la unidad FCC de refinería

351 p.

IKASNABAR 2014 International Conference. Microcontents, miniMOOCs and mLearning

[ES]Ikasnabar es una conferencia para hablar de tendencias en educación, sobre las nuevas tecnologías en el ámbito educativo y conocer personas que están generando buenas ideas y prácticas en su quehacer diario. Este libro intenta recoger todo ello con las contribuciones de autores noveles y de renombre que buscan la excelencia en los procesos de enseñanza-aprendizaje. Tres tendencias importantes de aprendizaje se están expandiendo. Microcontenidos, aprendizaje móvil y MOOCs son la cara de una misma moneda: microaprendizaje con contenido rico, abierto y desmenuzado. A medida que el consumo de Internet desde dispositivos móviles aumenta, el aprendizaje móvil con tecnologías como HTML5, software para MOOC, plataformas de contenidos de vídeo, etc., están siendo algunas de las claves de la nueva revolución en el ámbito educativo. El microcontenido hace referencia a los pequeños trozos de información digital en un estado permanente de flujo y circulación. Es a menudo un único tema, limitado en longitud, que se consume rápidamente y con frecuencia limitado por el software o por el dispositivo. Se trata de la puesta en común de recursos. Se basa en la interacción humano-a-humano con los medios de comunicación de Internet. El otro tema central de esta conferencia es el de los MOOC realizados por los profesores que quieren tomar ventaja en el comienzo de esta nueva era de la educación abierta con calidad. MOOCs son, básicamente, cursos abiertos y es necesario recordar los puntos esenciales de este tipo de instrucción. Los miniMOOCs son alternativas con menos horas en el proceso de aprendizaje. Hoy en día, un buen MOOC podrá ser la mejor tarjeta de presentación para profesores, expertos y estudiantes. Vivimos en tiempos de cambio con ámbitos en los que se mezcla el aprendizaje formal e informal, y las universidades y colegios deberíamos estar atentos a esto.

Pediatría para la cooperación

La mayor parte de las niñas y niños del planeta nace y muere en lugares carentes de adecuada atención sanitaria, lejos de hospitales y universidades. Hemos querido fusionar el mundo académico, clínico y de la cooperación, sumando ciencia, voluntades e incertidumbres, con la intención de que de esta mezcla pudiera surgir una herramienta útil para quienes se acercan desde el ámbito de la sanidad a la cooperación infantil. Si el recurso más valioso de cada pueblo son las personas y la mayor riqueza es el conocimiento, contribuir a la formación en cuidados sanitarios de la infancia debiera ser la mejor de las inversiones.

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.

Sistemas SCR y NSR-SCR para DeNOx en corrientes de escape diésel: Formulaciones, cinética y modelización

314 p.

Reutilización de escoria negra de acería como soporte en biofiltros para la eliminación de H2S del biogás.

[EN]Due to the limitations associated with fossil fuels it is necessary to promote energy sources that are renewable as well as eco-friendly, such as biogas generated in anaerobic digesters. The biogas, composed principally of methane and CO2, is the result of the biodegradation of organic matter under anaerobic conditions. Its use as fuel is limited by the presence of minority compounds such as hydrogen sulphide (H2S); therefore, its pre-treatment is necessary. Currently there are various technologies for the removal of H2S from a gas stream, but most of them are based on physic-chemical treatments which have a number of drawbacks as reactive consumption, generation of secondary flows, etc. Biofiltration has been used as an efficient and low cost alternative to conventional purification processes, and excellent results for the degradation of H2S have been obtained. However process can be limited due to the progressive ageing of the support material, along with the loss of nutrients and other specific characteristics necessary for the good development of biomass. The purpose of this project is to develop a mixed support consisting of a mixture of an organic material and an inorganic support for its application in the removal of the H2S from biogas. This support material helps to optimize the characteristics of the bed and extend its lifespan. The development of such material will contribute to the implementation of biofiltration for treating biogas from anaerobic digesters for its use as biofuel. The inorganic material used is electric arc furnace (EAF) black slag, a by-product generated in large quantities in the production of steel in the Basque Country. Although traditionally the slag has been used in civil engineering, its physicochemical characteristics make it suitable for reuse as a filter medium in biofiltration. The main conclusion drawn from the experimental results is that EAF black slag is a suitable co-packing material in organic biofilters treating H2S-polluted gaseous streams. High pollutant removal rates have been achieved during the whole experimental period. The removal capacity recorded in biofilters with less inorganic material was higher than in those with higher slag portion. Nevertheless, all the biofilters have shown a satisfactory response even at high inlet loads (48 g·m-3·h-1), where the RE has not decreased over 82%.

Early life history studies of Yellowfin tuna, Thunnus albacares. I. Food selection of Yellowfin tuna, Thunnus albacares, larvae reared in the laboratory. II. Age validation and growth of Yellowfin tuna, Thunnus albacares, larvae reared in the laboratory

English: Food selection of first-feeding yellowfin tuna larvae was studied in the laboratory during October 1992. The larvae were hatched from eggs obtained by natural spawning of yellowfin adults held in sea pens adjacent to Ishigaki Island, Okinawa Prefecture, Japan. The larvae were fed mixed-prey assemblages consisting of size-graded wild zooplankton and cultured rotifers. Yellowfin larvae were found to be selective feeders during the first four days of feeding. Copepod nauplii dominated the diet numerically, by frequency of occurrence and by weight. The relative importance of juvenile and adult copepods (mostly cyclopoids) in the diet increased over the 4-day period. Rotifers, although they comprised 31 to 40 percent of the available forage, comprised less than 2.1 percent of the diet numerically. Prey selection indices were calculated taking into account the relative abundances of prey, the swimming speeds of yellowfin larvae and their prey, and the microscale influence of turbulence on encounter rates. Yellowfin selected for copepod nauplii and against rotifers, and consumed juvenile and adult copepods in proportion to their abundances. Yellowfin larvae may select copepod nauplii and cyclopoid juveniles and adults based on the size and discontinuous swimming motion of these prey. Rotifers may not have been selected because they were larger or because they exhibit a smooth swimming pattern. The best initial diet for the culture of yellowfin larvae may be copepod nauplii and cyclopoid juveniles and adults, due to the size, swimming motion, and nutritional content of these prey. If rotifers alone are fed to yellowfin larvae, the rotifers should be enriched with a nutritional supplement that is high in unsaturated fatty acids. Mouth size of yellowfin larvae increases rapidly within the first few days of feeding, which minimizes limitations on feeding due to prey size. Although yellowfin larvae initiate feeding on relatively small prey, they rapidly acquire the ability to add relatively large, rare prey items to the diet. This mode of feeding may be adaptive for the development of yellowfin larvae, which have high metabolic rates and live in warm mixed-layer habitats of the tropical and subtropical Pacific. Our analysis also indicates a strong potential for the influence of microscale turbulence on the feeding success of yellowfin larvae. --- Experiments designed to validate the periodicity of otolith increments and to examine growth rates of yellowfin tuna larvae were conducted at the Japan Sea-Farming Association’s (JASFA) Yaeyama Experimental Station, Ishigaki Island, Japan, in September 1992. Larvae were reared from eggs spawned by captive yellowfin enclosed in a sea pen in the bay adjacent to Yaeyama Station. Results indicate that the first increment is deposited within 12 hours of hatching in the otoliths of yellowfin larvae, and subsequent growth increments are formed dailyollowing the first 24 hours after hatching r larvae up to 16 days of age. Somatic and otolith gwth ras were examined and compared for yolksac a first-feeding larvae reared at constant water tempatures of 26�and 29°C. Despite the more rapid develo of larvae reared at 29°C, growth rates were nnificaifferent between the two treatments. Howeve to poor survival after the first four days, it was ssible to examine growth rates beyond the onset of first feeding, when growth differences may become more apparent. Somatic and otolith growth were also examined for larvae reared at ambient bay water temperatures during the first 24 days after hatching. timates of laboratory growth rates were come to previously reported values for laboratory-reared yelllarvae of a similar age range, but were lower than growth rates reported for field-collected larvae. The discrepancy between laboratory and field growth rates may be associated with suboptimal growth conditions in the laboratory. Spanish: Durante octubre de 1992 se estudió en el laboratorio la seleccalimento por larvaún aleta amarillmera alimentación. Las larvas provinieron de huevos obtenidosel desove natural de aletas amarillas adultos mantenidos en corrales marinos adyacentes a la Isla Ishigaki, Prefectura de Okinawa (Japón). Se alimentó a las larvas con presas mixtas de zooplancton silvestre clasificado por tamaño y rotíferos cultivados. Se descubrió que las larvas de aleta amarilla se alimentan de forma selectiva durante los cuatro primeros días de alimentación. Los nauplios de copépodo predominaron en la dieta en número, por frecuencia de ocurrencia y por peso. La importancia relativa de copépodos juveniles y adultos (principalmente ciclopoides) en la dieta aumentó en el transcurso del período de 4 días. Los rotíferos, pese a que formaban del 31 al 40% del alimento disponible, respondieron de menos del 2,1% de la dieta en número. Se calcularon índices de selección de presas tomando en cuenta la abundancia relativa de las presas, la velocidad de natación de las larvas de aleta amarilla y de sus presas, y la influencia a microescala de la turbulencia sobre las tasas de encuentro. Los aletas amarillas seleccionaron a favor de nauplios de copépodo y en contra de los rotíferos, y consumieron copépodos juveniles y adultos en proporción a su abundancia. Es posible que las larvas de aleta amarilla seleccionen nauplios de copépodo y ciclopoides juveniles y adultos con base en el tamaño y movimiento de natación discontinuo de estas presas. Es posible que no se hayan seleccionado los rotíferos a raíz de su mayor tamaño o su patrón continuo de natación. Es posible que la mejor dieta inicial para el cultivo de larvas de aleta amarilla sea nauplios de copépodo y ciclopoides juveniles y adultos, debido al tamaño, movimiento de natación, y contenido nutritivo de estas presas. Si se alimenta a las larvas de aleta amarilla con rotíferos solamente, se debería enriquecerlos con un suplemento nutritivo rico en ácidos grasos no saturados. El tamaño de la boca de las larvas de aleta amarilla aumenta rápidamente en los primeros pocos días de alimentación, reduciendo la limitación de la alimentación debida al tamaño de la presa. Pese a que las larvas de aleta amarilla inician su alimentación con presas relativamente pequeñas, se hacen rápidamente capaces de añadir presas relativamente grandes y poco comunes a la dieta. Este modo de alimentación podría ser adaptivo para el desarrollo de larvas de aleta amarilla, que tienen tasa metabólicas altas y viven en hábitats cálidos en la capa de mezcla en el Pacífico tropical y subtropical. Nuestro análisis indica también que la influencia de turbulencia a microescala es potencialmente importante para el éxito de la alimentación de las larvas de aleta amarilla. --- En septiembre de 1992 se realizaron en la Estación Experimental Yaeyama de la Japan Sea- Farming Association (JASFA) en la Isla Ishigaki (Japón) experimentos diseñados para validar la periodicidad de los incrementos en los otolitos y para examinar las tasas de crecimiento de las larvas de atún aleta amarilla. Se criaron las larvas de huevos puestos por aletas amarillas cautivos en un corral marino en la bahía adyacente a la Estación Yaeyama. Los resultados indican que el primer incremento es depositado menos de 12 horas después de la eclosión en los otolitos de las larvas de aleta amarilla, y que los incrementos de crecimiento subsiguientes son formados a diario a partir de las primeras 24 horas después de la eclosión en larvas de hasta 16 días de edad. Se examinaron y compararon las tasas de crecimiento somático y de los otolitos en larvas en las etapas de saco vitelino y de primera alimentación criadas en aguas de temperatura constante entre 26°C y 29°C. A pesar del desarrollo más rápido de las larvas criadas a 29°C, las tasas de crecimiento no fueron significativamente diferentes entre los dos tratamientos. Debido a la mala supervivencia a partir de los cuatro primeros días, no fue posibación, uando las diferencias en el crecimiento podrían hacerse más aparentes. Se examinó también el crecimiento somático y de los otolitos para larvas criadas en temperaturas de agua ambiental en la bahía durante los 24 días inmediatamente después de la eclosión. Nuestras estimaciones de las tasas de crecimiento en el laboratorio fueron comparables a valores reportados previamente para larvas de aleta amarilla de edades similares criadas en el laboratorio, pero más bajas que las tasas de crecimiento reportadas para larvas capturadas en el mar. La discrepancia entre las tasas de crecimiento en el laboratorio y el mar podría estar asociada con condiciones subóptimas de crecimiento en el lab

Development of the heterogeneous catalysts for the production of levulinic acid from furfuryl alcohol

207 p.

Proceso de pirólisis y reformado en línea para la producción de H2 a partir de residuos plásticos

266 p.

Mescla conceptual em O Pasquim

Este estudo, de cunho cognitivista, trata do humor e da ironia multimodal em cinco capas do jornal O Pasquim. Nele, constam análises sobre a percepção da ironia e do humor presente nas capas das edições n 187, 271, 514, 654 e 668, e a discussão sobre o papel do contexto histórico, da imagem e do texto como gatilho para a formulação de mesclas. O trabalho também postula configurações de mesclas a partir dos sentidos construídos por quatro grupos distintos de colaboradores, um grupo formado por leitores jovens à época de publicação das capas, e outros três grupos de jovens universitários, tendo o primeiro grupo visualizado a imagem e depois o texto que compunha a capa, o segundo acessado primeiro o texto e depois a imagem e o último visualizado as capas completas. Para tanto, foram utilizados alguns dos principais conceitos da linguística cognitiva, a saber, frames, domínio, mesclagem e metáfora conceptual, além de estudos relativos à ironia e humor. Também é proposta uma nova configuração para mesclas irônicas, apresentando a fusão dos inputs de entrada e dos espaços de reação esperada e confrafactual, cunhados por Coulson (2005) no modelo de estruturação do espaço