15 resultados para Tri-orto-cresil fosfato (TOCP)

em Archivo Digital para la Docencia y la Investigación - Repositorio Institucional de la Universidad del País Vasco


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El cerámido 1-fosfato (C1P) es un potente estimulador de la proliferación celular e inhibidor de la apoptosis. Más recientemente se ha demostrado que el C1P es proinflamatorio y que además induce la migración celular. Todas estas características indican que el C1P puede estar implicado en la tumorogénesis. En el presente trabajo se estudiará si el C1P es capaz de estimular procesos implicados en la angiogénesis, o formación de nuevos vasos sanguíneos a partir de vasos preexistentes.

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[EN]Conjugated linoleic acid (CLA) has many potential healthful properties, and beef is naturally enriched with CLA. Simple and rapid methods to measure total CLA were investigated to enable sorting of beef carcasses with potential enhanced economic value. Direct alcohol extraction combined with measuring absorbance was simple, accurate and perhaps the most viable method for rapid carcass sorting compared to methods using saponification or methylation followed by extraction.

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El clorhidrato de tiaprida es una benzamida u ortopramida con efecto neuroléptico atípico. En el presente trabajo se estudia el efecto del clorhidrato de tiaprida sobre el consumo de oxígeno, glucosa, fosforilación oxidativa mitocondrial, actividad ATPasa y la interacción con diversos neurotransmisores en preparaciones de cortes de corteza de rata "in vitro". En relación con el MATERIAL Y METODOS, se determinó el consumo de oxígeno en cortes, homogeneizados y mitocondrias de cerebro de rata "in vitro" mediante técnica manométrica. La actividad ATPasa se determinó estimando el fosfato inorgánico liberado a partir del adenosín-trifosfato (ATP) en ausencia y en presencia de ouabaína. Se determinó el consumo de glucosa mediante el proceder de la glucosa-oxidasa y también se estudió la fosforilación oxidativa mitocondrial. Para el estudio de las interacciones con los neurotransmisores se recurrió a los cortes de cortaza cerebral de rata "in vitro". Se determinó el valor de la Concentración Inbitoria50 cuando el antagonismo era de tipo no competitivo. El clorhidrato de tiaprida a las concentraciones de 10-3, 10-4 y 10-5M disminuye el consumo de oxígeno de homogeneizados de cerebro de rata "in vitro", no desacopla la fosforilación oxidativa mitocondrial, no modifica el consumo de oxígeno y de glucosa de cortes de cerebro de rata "in vitro" incubados en solución de Krebs-Ringer fosfato normal, no inhibe la actividad ATPasa de membrana sodio-potasio dependiente, ni la actividad ATPasa no sensible a ouabaína. El clorhidrato de tiaprida a la concentración de 10-6M antagoniza el incremento de consumo de oxígeno inducido por la dopamina en cortes de cerebro de rata "in vitro" incubados en solución de Krebs-Ringer fosfato pH 7.4 con glucosa 10 mM, siendo este antagonismo de tipo no competitivo. El clorhidrato de tiaprida no modifica los efectos de histamina y serotonina sobre el consumo de oxígeno de cortes de cerebro de rata.

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Hyper-spectral data allows the construction of more robust statistical models to sample the material properties than the standard tri-chromatic color representation. However, because of the large dimensionality and complexity of the hyper-spectral data, the extraction of robust features (image descriptors) is not a trivial issue. Thus, to facilitate efficient feature extraction, decorrelation techniques are commonly applied to reduce the dimensionality of the hyper-spectral data with the aim of generating compact and highly discriminative image descriptors. Current methodologies for data decorrelation such as principal component analysis (PCA), linear discriminant analysis (LDA), wavelet decomposition (WD), or band selection methods require complex and subjective training procedures and in addition the compressed spectral information is not directly related to the physical (spectral) characteristics associated with the analyzed materials. The major objective of this article is to introduce and evaluate a new data decorrelation methodology using an approach that closely emulates the human vision. The proposed data decorrelation scheme has been employed to optimally minimize the amount of redundant information contained in the highly correlated hyper-spectral bands and has been comprehensively evaluated in the context of non-ferrous material classification

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230 p.

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225 p. : il. Texto en español con conclusiones en inglés

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Hasta hace poco, enfermedades como el cáncer o el Alzheimer eran interpretadas solo como mutaciones genéticas, es decir, cambios en la secuencia genética. Sin embargo, son muchos los que últimamente se interesan por la epigenética y por la relación con las enfermedades. La epigenética va más allá que la genética, se basa en los cambios reversibles del ADN y de las proteínas que se unen en él. Esto hace que, sin necesidad de alterar su secuencia, un gen pueda ser expresado o por el contrario quede silenciado. Uno de estos cambios epigenéticos es la metilación del ADN que consiste en una modificación química en el dinucleotido CpG (citosina-fosfato-guanina, es decir, donde una citosina es seguida de una guanina). Existen métodos experimentales para poder detectar la metilación, como por ejemplo, los métodos basados en la modificación del ADN con bisulfito y posterior análisis con arrays de ADN. El objetivo de este proyecto es imitar, mediante la simulación computacional y el estudio de distintas bases de datos, el comportamiento del sistema biológico, a fin de generar datos similares a los reales. Esta simulación de los datos reales permitirá, entre otras cosas, generar escenarios controlados en los que evaluar los métodos de análisis. Adicionalmente, el proceso de diseño permitirá explorar el proceso biológico que da lugar a los datos.

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[ES]En este trabajo se analiza el proceso de fabricación de tubos de acero sin soldadura en la planta de Tubos Reunido Industrial (en lo sucesivo TRI) en la localidad alavesa de Amurrio. Además, se acompaña el análisis con puntualizaciones sobre las alternativas aplicables en cada paso del proceso y la conveniencia de aplicarlas en la planta estudiada. De esta manera se realiza un estudio de los procesos y equipos requeridos para los distintos pasos que se dan para fabricar tubos de acero sin soldadura de gran calidad a partir de chatarra de acero. Así mismo, dada la importancia de la calidad y el medio ambiente en la estrategia de TRI, se aporta también en este trabajo un resumen de los métodos utilizados en estas áreas.

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Este proyecto constituye un estudio acerca de la eficacia de dos óxidos de hierro, goethita y akaganeita en la eliminación de ciertos aniones presentes en el agua: cloruro, clorato, fluoruro, fosfato, nitrato y sulfato. Se evaluará la capacidad de adsorción y el porcentaje de eliminación de aniones de los dos óxidos, así como del material resultante de su soporte sobre carbón activo.

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El agua es un bien necesario para la vida . Por ello, la problemática del tratamient o de agua es un tema de gran interés a nivel mundial. Las desviaciones que se pueden producir en el sistema de potabilización actual hacen necesario encontrar nuevos métodos para la eliminación de las sustancias tóxicas que puedan estar presentes en el medio. De ntro de estas sustancia s tóxicas destacan los aniones inorgánicos debido, en gran medida , al impacto de la actividad hu mana sobre las reservas de agua, p ara su eliminación existen numerosas alternati vas. N o obstante, diversos estudios plantean el uso de los óxidos de hierro ya q ue han demostrado ser eficaces para la eliminación de un gran rango de sustancias , por este motivo , se decide trabajar con ellas. Para aumentar la eficacia de eliminación , los óxidos son soportados a un mineral de arcilla, la montmorillonita. El objetivo principal de este trabajo es el análisis de la eficacia de varios óxidos de hierro asociados a un mineral de arcilla para eliminar una batería de aniones tóxicos c ompuesta por cloruro, clorato, fluor uro, fosfato, nitrato y sulfato de una muestra de agua

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Chelon labrosus lazuna oso erabilia da kutsaduraren eragina aztertzeko organismo zentinela bezala, oso kutsatuta dauden itsaso zabaleko zein itsasadarretako uretan bizirauteko gai baita. Kutsatzaileek zelulen, ehunen eta organismoen transkripzio-profilen aldaketa eragin dezaketela ondo deskribatuta dago. Aldaketa hauek neurtzeko, gene-espresioaren normalizazioa burutu behar da. Eskuarki, normalizazio prozesua burutzeko, metabolismo orokorreko geneak erabiltzen dira, hau da, erreferentzia geneak. Gene hauek, zelularen oinarrizko funtzioak garatzeko beharrezkoak diren geneak dira eta zelula guztietan konstitutiboki adierazi ohi dira. Aurretik egin diren zenbait ikerketetan ordea, gene hauen transkripzio maila egoera esperimentalen, ehun motaren, garapen fasearen edota zelularen zikloaren arabera aldatu egiten dela behatu da. Hortaz, erreferentzia geneen transkripzio mailen aldaketak, aztergai den itu genearen interpretazio okerra eman dezake. Hori dela eta, azken urte hauetan, beste metodo batzuk garatzen ari dira geneen transkripzio maila normalizatzeko, esaterako, QuanT-it OliGreen metodoa. Testuinguru honetan, Chelon labrosus lazunean toxikologia-analisiak egiteko gehien erabiltzen diren erreferentzia geneen transkripzio-profilak aztertu dira indibiduo ar zein emeetan ugalketa zikloaren zeharreko fase gametogeniko desberdinetan (bost guztira). Horretarako, erreferentzia gene bat, itu gene kontsideratuz, normalizazioa beste erreferentzia geneekiko zein QuanT-it OliGreen metodotik lortutako emaitzekiko burutu da. Azterturiko geneak β-aktina (BA), 18S RNA erribosomikoa (18S rRNA), 1-α elongazio faktorea (EF-1-α) eta glizeraldehido-3-fosfato deshidrogenasa (GAPDH) izan dira. Aztergai zeuden erreferentzia geneen transkripzio maila qRT-PCR bidez kuantifikatu ondoren, aurretik aipatutako bi metodoekiko normalizatu ziren. Normalizazioa erreferentzia geneekiko egin zenean, itu gene berak transkripzio-profil desberdinak aurkeztu zituen normalizaziorako erabili zen erreferentzia genearen arabera. QuanT-it OliGreen metodoaren bidezko normalizazioa egin zenean berriz, aztertutako erreferentzia gene guztien transkripzio-profila, fase gametogenikoen arabera aldatzen zela ondorioztatu zen. Beraz, itu gene baten transkripzio-profilaren azterketa egin nahi denean QuanT-it OliGreen metodoa erreferentzia geneak erabiltzea baino fidagarriagoa da.

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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.