La séparation magnétique a reçu beaucoup d'attention en tant que technologie de séparation de catalyseurs solides, très efficace et rapide. De nombreuses études ont porté sur l'immobilisation de systèmes catalytiques actifs sur un support magnétique afin de les séparer par la simple application d'un aimant. Cependant, le développement de supports magnétiques s'avère limité à des nanoparticules (NPs) magnétiques encapsulées dans une silice, un polymère ou du carbone. La conception de nanocomposites magnétiques incorporant d'autres oxydes est donc intéressante afin d'élargir l'application de cette technologie de séparation dans le domaine de la catalyse. Dans ce contexte, des études de stabilité thermique ont été menées sur magnétite revêtue de silice (Fe3O4@SiO2) pour évaluer la possibilité de la calciner sans perdre les propriétés magnétiques du support. La calcination permettrait le dépôt de différents oxydes sur la surface de la silice, tels que l'oxyde de cérium et l'oxyde de titane. Il a été observé que le matériau Fe3O4@SiO2 calciné a conservé sa morphologie core-shell et ses propriétés magnétiques, tandis que sa surface spécifique at a augmenté de 6 odres de grandeur. Un processus a pu être développé pour le dépôt d'oxyde de cérium et d'oxyde de titane sur Fe3O4@SiO2. Des nanocatalyseurs aisément récupérables par séparation magnétique à base de Rh, Pd et Ru ont pu être préparés en utilisant ces supports de silice modifiés par dépôt de CeO2 et TiO2. Ces nanocatalyseurs obtenus ont été évalués en catalyse d'hydrogénation du cyclohexène, du benzène ou du phénol. L'étude de l'influence de chaque support sur l'activité catalytique des nanocatalyseurs a consitué l'objectif principal de cette thèse. Le dépôt des nanoparticules métalliques sur les supports pour l'obtention des catalyseurs actifs a été réalisé par deux approches différentes: l'imprégnation et l'immobilisation de sols contenant des NP métalliques préformées. Quant aux NPs métalliques colloïdales, elles ont été préparées par réduction de sels métalliques et par la décomposition de complexes organométalliques précurseurs. Des catalyseurs de rhodium préparés par imprégnation de rhodium (III) chlorure et réduction avec H2 ont montré des problèmes de reproductibilité qui ont été contournés en utilisant NaBH4 ou l'hydrazine comme agents réducteurs. La préparation des catalyseurs par l'immobilisation des NP colloïdales s'est avérée une alternative intéressante pour obtenir des catalyseurs très actifs de façon reproductible. Des nanoparticules de Pd, Rh et Ru ont été préparées par l'approche organométallique et immobilisées sur les supports Fe3O4@SiO2 calciné, Fe3O4@SiO2CeO2 et Fe3O4@SiO2TiO2. L'élimination de l'agent stabilisant pour les NPs de Rh déposées sur Fe3O4@SiO2CeO2 semble conduire à un état de surface différent comparativement aux autres supports car ce catalyseur s'est montré le plus actif vis-à-vis de l'hydrogénation du cyclohexène (TOF 125 000 h-1). Les catalyseurs à base de Rh, Pd et Ru ont été utilisées pour l'hydrogénation de phénol. Le palladium s'est avéré le catalyseur le plus sélectif envers la cyclohexanone, quel que soit le support utilisé. La formation de cyclohexanol a été renforcée avec le support fonctionnalisé par l'oxyde de titane et la production de cyclohexane par hydrodéoxygénation a eu lieu principalement avec le support de silice. / Magnetic separation has received a lot of attention as a robust, highly efficient and rapid catalyst separation technology. Many studies have focused on the immobilization of catalytic active species, but the development of magnetic supports has been limited to silica, polymer or carbon-coated magnetic nanoparticles (NPs). The design of magnetic nanocomposites and the incorporation of other oxides are thus highly welcome to broaden the application of this separation technology in the field of catalysis. In this context, studies of the thermal stability of silica coated magnetite (Fe3O4@SiO2) were performed to evaluate the possibility of calcining it without losing the magnetic properties of the support. The calcination would permit the deposition of different oxides on the silica surface, such as ceria and titania. The calcined Fe3O4@SiO2 material preserved its core-shell morphology and magnetic properties, and increased its surface area six times. A post-coating process was developed for the deposition of ceria and titania on Fe3O4@SiO2. Magnetically recoverable Rh, Pd and Ru nanocatalysts were prepared on the surface of the magnetic supports. The obtained catalysts were employed in hydrogenation of cyclohexene, benzene or phenol and the study of the influence of each support on the catalytic activity was the main objective of this thesis. For the deposition of the metallic nanoparticles on the supports in order to obtain the active catalysts two different approaches were followed: the impregnation and the sol immobilization of pre-formed metal NPs. Concerning the synthesis of the colloidal metal NPs, they were prepared either by reduction of metal salts or by decomposition of organometallic complexes. Rhodium catalysts prepared by impregnation of rhodium(III) chloride and reduction with H2 showed some reproducibility issues that were surpassed by using NaBH4 or hydrazine as reducing agents. The preparation of catalysts by the immobilization of colloidal NPs is an interesting alternative to obtain reproducible and very active catalysts. Nanoparticles of Pd, Rh and Ru were prepared by an organometallic approach and immobilized on calcined Fe3O4@SiO2, Fe3O4@SiO2CeO2 and Fe3O4@SiO2TiO2. The elimination of Rh stabilizing agent over ceria support appears to be different than in other supports and was the most active catalyst in the hydrogenation of cyclohexene (TOF 125,000 h-1). The Rh, Pd and Ru catalysts were employed in the hydrogenation of phenol. Palladium was the most selective catalyst to cyclohexanone, no matter the support used. The formation of cyclohexanol is enhanced in the support with titania and the hydrodeoxygenation to produce cyclohexane occurred mainly in the support with silica.

Treatment of fuel cell feed H2 for the removal of CO is important owing to the poisoning of the catalysts, thereby affecting the performance of the fuel cell. Strong and preferential adsorption of CO over the catalyst takes place resulting in a reduction of the power output of the cell. Therefore, it is important to treat the fuel cell feed H2 to reduce its CO content below the tolerable limit. Development of efficient catalysts for the treatment of synthesis gas for the removal of CO and and H2 enrichment of the gas to make it suitable for fuel cells is one of the two goals of this thesis. One of the various possible strategies for the removal of CO from the synthesis gas can be the use of the water-gas shift reaction. We have developed noble metal substituted ionic catalysts for catalyzing the water-gas shift reaction and have studied in detail the kinetics of the reactions by proposing the relevant reaction mechanisms. Solution combustion, a novel technique for synthesizing nanocrystalline materials, was used for the synthesis of all the catalysts. All the compounds synthesized were solid solutions of the noble metal ion and transition or rare earth metal oxide support. Three different supports were used, viz., CeO2, ZrO2 and TiO2. Substitution of Zr and Ti in CeO2 up to 15 at% was also carried out to obtain the compounds with enhanced oxygen storage capacity. All the compounds were characterized by X-ray diffraction, X-ray photoelectron spectroscopy and transmission electron microscopy. In some cases, where it was required, the use of FT-Raman spectroscopy was made for structural analysis. The compounds were nanocrystalline with metals substituted in ionic form in the support. The water-gas shift reaction was carried out over the synthesized catalysts with a reactant gas mixture that simulated the actual refinery gas composition. The variation of CO concentration with temperature was traced. The changes in the oxidation state of the metal showed the involvement of the various redox pairs over the reducible oxide like substituted CeO2 and TiO2. The mechanism of the reaction over ZrO2-based compounds was found to take place utilizing the surface hydroxyl groups. Rate expressions for the reactions over all the catalysts following different mechanisms were derived from the proposed elementary processes. Nonlinear regression was used for the estimation of various parameters describing the rate of reaction. Having established the high activity of Pt-ion substituted TiO 2 for the reactions, steam reforming of wood gas obtained from the gasification of Casuarina wood chips was carried out. The enrichment of the gas stream, which initially consisted of nearly 10% H 2 was carried out by steam reforming and H2-rich stream was obtained with H2 as high as 40% by volume in the treated gas. The second motive behind this thesis was to test the activity of the noble-metal substituted ionic catalysts for the treatment of the exhaust gas coming out of a fuel cell. In the fuel cell utilizing H2, the exhaust gases contain certain amount of unreacted H2, which can not be recovered or utilized economically. However, the gases are combustible and H 2 has to be removed in order to make the gas clean. We have shown high activity of the combustion-synthesized ionic compounds for catalytic combustion of H2. All the compounds showed high activity for H2 combustion and complete removal of H2 was possible. The rates were found to increase with an decrease in H2:O2 ratio and complete conversion of H2 was possible within 100 oC with air. A mathematical model was developed for the kinetics of catalytic H2 combustion based on the elementary processes that were proposed using the spectroscopic evidences. CO tolerant capacity of the catalysts was also tested. It was found that the temperature requirement for most of the catalysts increased with the introduction of CO. However, it was still possible to obtain complete conversions within 200 oC. To summarize, fuel cell processing systems utilizing H 2 remained central to the study. Treatment of the gases, both before and after reaction from the fuel cell was carried out over noble metal-substituted ionic catalyst, synthesized by solution combustion technique. Mechanisms of the reactions were proposed on the basis of spectroscopic evidences and the kinetic rate parameters were estimated using non-linear regression.

Ce travail rapporte l’étude des processus de désactivation et des modifications d’un catalyseur Ir supportésur cérine en vaporeformage de l’éthanol. Différentes causes de désactivation ont été identifiées selon lesconditions opératoires : température, temps de contact et temps de réaction. La désactivation initiale,rapide mais limitée a été attribuée à la restructuration de surface de la cérine et à la formation d’unemonocouche d’intermédiaires de type acetate, carbonate et hydroxyls. En parallèle, une désactivationlente et progressive a été mise en évidence, ayant pour origine les changements structurels de l’interfaceentre la cérine et l’iridium, liés au frittage des particules d’iridium et à la restructuration profonde de lacérine. Par contre, la formation continue, à température modérée, d’une couche de carbone encapsulantissu de la polymérisation d’intermédiaires C2 n’a pas semblé contribuer significativement à ladésactivation du catalyseur dans nos conditions opératoires. Pour limiter ce phénomène de désactivation,des modifications ont été apportées au catalyseur. Le dopage du catalyseur par PrOx a permis defortement améliorer la capacité de stockage de l’oxygène et la stabilité thermique du catalyseur,entraînant une augmentation de son activité et de sa stabilité en vaporeformage de l’éthanol. Lecatalyseur Ir/CeO2 a ensuite subi une mise en forme de la cérine (nano-tubes), avec une influencesignificative sur l'activité et la stabilité en vaporeformage de l’éthanol, liée à des effets structuraux. Unemodélisation simplifiée de ces divers phénomènes a également contribué à soutenir les propositionsoriginales de ce travail. / The objective of the thesis was to analyze the ageing processes and the modifications of an Ir/CeO2catalyst for steam reforming of ethanol. Over a model Ir/CeO2 catalyst, the initial and fast deactivationwas ascribed to ceria surface restructuring and the build-up of intermediates monolayer (acetate,carbonate and hydroxyl groups). In parallel, a progressive and slow deactivation was found to come fromthe structural changes at the ceria/Ir interface linked to Ir sintering and ceria restructuring. Theencapsulating carbon, coming from C2 intermediates polymerization, did not seem too detrimental to theactivity in the investigated operating conditions. By doping ceria with PrOx, the oxygen storage capacityand thermal stability were greatly promoted, resulting in the enhanced activity and stability. The Ir/CeO2catalyst was then modified by changing the shape of ceria. It was found that the shape and therefore thestructure of ceria influenced the activity and stability significantly. A simplified modeling of theseprocesses has contributed to support the new proposals of this work.

Dans cette étude nous avons cherché à évaluer les paramètres et les mécanismes gouvernant la réactivité des catalyseurs à base de cérium lors de la dégradation des colorants textiles, seuls ou en mélange binaire, dans le cadre du procédé Fenton/photo-Fenton. Dans ce but, 5 séries de catalyseurs à base de cérium ont été testées pour déterminer les effets respectifs : (i) de la surface spécifique de CeO2 commercial (SBET = 11, 101,5 ; 148 ; 235 et 284 m2/g), (ii) du dopage au zirconium (oxydes mixtes CexZr1-xO2 avec différentes teneurs en cérium (x = 0 ; 0,2 ; 0,5 ; 0,8 ; 1)), (iii) d’un traitement de sulfatation de CexZr1-xO2 par H2SO4, et (iv) de l’imprégnation de CeO2 par différents métaux (M = Ba, Bi, La, V et Mo). Les propriétés texturales, structurales et chimiques des catalyseurs à base de cérium étudiés ont été dans la plupart des cas caractérisées par porosimétrie à l’azote, DRX, Raman, XPS, FTIR/ATR, DR-UV-Vis et ATG. Les cinétiques de décoloration et de minéralisation de l’Orange II en présence de CeO2 et H2O2 dépendent fortement de la surface spécifique des catalyseurs ainsi que des paramètres opératoires (présence d’irradiation UV-Vis, pH, température, concentration initiale en catalyseur et en H2O2). Par comparaison avec les colorants pris séparément, l’adsorption compétitive de l’Orange II et de l’Acide Vert 25 sur les mêmes sites d’adsorption à pH = 3 réduit les taux de dégradation des deux colorants en mélange. En revanche, l’association de l’Orange et du Vert de Malachite en paires d’ion, permet d’améliorer la cinétique apparente de dégradation du Vert de Malachite d’un facteur 5. Dans ce cas, la réaction de Fenton et la coagulation-floculation contribuent simultanément à l’élimination de deux colorants de charge opposée en présence du système CeO2/H2O2. De plus, les performances des oxydes mixtes Ce-Zr dans le procédé Fenton hétérogène sont étroitement liées à leurs caractéristiques texturales, structurales et chimiques. Les analyses effectuées ont permis de vérifier les phases cristallines des oxydes mixtes de révéler la formation de solutions solides. Le traitement de sulfatation conduit à la diminution de la surface spécifique et l’augmentation de la taille des cristallites des oxydes riches en Ce. La dissolution de CeO2 lors de sulfatation suivie par formation d’une phase amorphe Ce(SO4)2 à la surface du catalyseur a été mise en évidence. Le traitement de sulfatation ainsi que le dopage au Zr permettent d’augmenter la densité de surface en sites réduits Ce(III). Les études en spectroscopies DR-UV-Vis, FTIR/ATR et Raman relatives à l’adsorption et l’activation d’H2O2 par les oxydes mixtes ont permis de mettre en évidence l’existence d’espèces Ce-peroxo de surface, comme intermédiaires pour générer les radicaux hydroxyles. La détermination quantitative de ces espèces par TPD-MS s’est avérée utile pour mieux comprendre les performances catalytiques des oxydes mixtes modifiés ou non. La concentration en Ce de surface, la densité de défauts Ce(III) (augmenté par dopage et le traitement de sulfatation) et la surface spécifique semblent être à cet égard parmi les paramètres les plus influents sur l’activité. L’imprégnation de CeO2 par différents métaux n’a pas montré un impact positif sur la réactivité de ce matériau en procédé Fenton. Un mécanisme général d’activation d’H2O2 a été proposé sur la base des résultats expérimentaux obtenus et la littérature. De point de vue mécanistique, les analyses spectroscopiques par ATR/FTIR et UV-Vis montrent que l’adsorption de l’Orange II à la surface du catalyseur est fortement dépendante du pH du milieu et se fait par des interactions électrostatiques. Le mécanisme de dégradation de l’Orange II, en phase liquide et à la surface du catalyseur, a été étudié par différentes techniques (DR-UV-VIS et ATR/IR, HPLC et GC/MS) / In this work, the parameters and mechanisms governing the reactivity of cerium based materials towards the degradation of textile dyes, taken separately or in binary mixture, in Fenton/photo-Fenton process have been investigated. For this purpose, five sets of catalysts were performed in order to determine the respective effects of : (i) the specific surface area of commercial CeO2 (SBET = 11, 101,5 ; 148 ; 235 and 284 m2/g); (ii) the zirconia doping ((CexZr1-xO2 with different Ce content (x = 0 ; 0,2 ; 0,5 ; 0,8 ; 1)); (iii) the treatment with H2SO4 ; and (iv) the impregnation of different metals in CeO2 (M = Ba, Bi, La, V and Mo). The textural, structural and chemical properties of the studied ceria-based materials were systematically characterized by nitrogen porosimetry, Raman, XRD, XPS, ATR/FTIR, DR-UV-Vis and TGA. Discoloration and mineralization kinetics of Orange II dye in presence of CeO2/H2O2 system are strongly related to the surface area of catalysts and other parameters (UV-Vis irradiation, pH, temperature, concentration of catalyst and H2O2). The presence of another dye with similar (Acid Green 25) or opposite charge (Malachite Green) can also influence the discoloration kinetics of Orange II. Comparing with single dye solutions, the degradation efficiency of both Orange II and Acid Green 25 were reduced in the mixture due to the competitive adsorption of both anionic dyes onto the same surface Ce sites. However, the discoloration of Malachite Green was enhanced in the presence of Orange II due to the simultaneous contribution of both coagulation/flocculation and Fenton-like process. It is suggested that a Malachite Green ion is electrostatically attracted by an Orange II ion at pH = 3. In addition, the performance of the mixed oxides in the heterogeneous Fenton process is strongly related to their textural, structural and chemical properties. Briefly, characterizations by XRD and Raman spectroscopy indicate that these nanosized mixed oxides can be considered as good quality solid solutions and possess structural properties consistent with the known phase diagram of CexZ1-xO2. The sulfation treatment mostly affects the Ce rich catalysts by increasing the crystallite size and lowering the specific surface area. The dissolution of ceria during sulfation followed by formation of Ce(SO4)2 amorphous phase on catalyst surface was investigated by UV-Vis and TGA analysis. Sulfation treatment as well as doping ceria with Zr increases the amount of reduced sites Ce (III) and defect sites.DR-UV-Vis, FTIR/ATR and Raman spectroscopic studies for adsorption and activation of H2O2 on mixed oxides show the formation of surface Ce-peroxo species as intermediate to generate hydroxyl radicals. The relative amounts of these species on the mixed oxides and/or not modified was indirectly determined using TPD-MS, giving rather good indication about the performances of catalysts towards the degradation of dye. The concentration of surface Ce, the density of defects Ce(III) sites (increased by doping and sulfation treatment) and the surface area appear to be among the most important parameters affecting the catalytic activity. Impregnation of ceria with different metals did not show a positive effect on the reactivity of this material in Fenton process. A possible mechanism for the activation of H2O2 was discussed in details according to all the experimental results and to the literature. From a mechanistic viewpoint, it is shown using FTIR/ATR and liquid UV-Vis spectroscopic measurements that the adsorption of the anionic dye is highly pH-dependent and proceeds via electrostatic interactions with surface metal centers. A possible pathway for Orange degradation is proposed on the basis of qualitative and quantitative detection of intermediate compounds, in liquid phase and on catalyst surface, using various techniques (FTIR/ATR, DR-UV-VIS, HPLC and GC/MS)

Composite materials formed from two or more functionally different materials offer a versatile avenue to create a tailored material with well defined traits. Within this dissertation research, multi-functional composites were synthesized based on organic and inorganic materials. The functionally of these composites was experimentally tested and a semi-empirical model describing the sedimentation behavior of these particles was developed. This first objective involved the fabrication of microcomposites consisting of titanium dioxide (TiO2) nanoparticles confined within porous, microgels of a thermo-responsive polymer for use in the photocatalytic treatment of wastewater. TiO2 has been shown to be an excellent photocatalyst with potential applications in advanced oxidative processes such as wastewater remediation. Upon UV irradiation, short-lived electron-hole pairs are generated, which produce oxidative species that degrade simple organic contaminants. The rapid sedimentation of these microcomposites provided an easy gravimetric separation after remediation. Methyl orange was used as a model organic contaminant to investigate the kinetics of photodegradation under a range of concentrations and pH conditions. Although after prolonged periods of UV irradiation (~8-13 hrs), the titania-microgels also degrade, regeneration of the microcomposites was straightforward via the addition of polymer microgels with no loss in photocatalytic activity of the reformed microcomposites. The second objective within this dissertation involved the systematic development of abrasive microcomposite particles containing well dispersed nanoparticles of ceria in an organic/inorganic hybrid polymeric particle for use in chemical mechanical polishing/planarization (CMP). A challenge in IC fabrication involves the defect-free planarization of silicon oxide films for successful multi-layer deposition. Planarization studies conducted with the microcomposites prepared in this research, yield very smooth, planar surfaces with removal rates that rival those of inorganic oxides slurries typically used in industry. The density and size of these ceria-microgel particles could be controlled by varying the temperature or composition during synthesis, leading to softer or harder polishing when desired.

This diploma thesis studies magneto-optical (MO) response of epitaxial thin films of Co-doped ceria. Thin films were characterized by XPS, LEED, STM, spectroscopic ellipsometry and measurement of MO activity. The work focuses on studying MO response of the films depending on film thickness, cobalt concentration, oxidation state of cerium and chemical state of cobalt. Spectra of MO response consist of low energy region where the MO activity is mediated by transitions from defect induced states to conduction band and high energy region where a peak of MO activity appears which we attribute to transitions from valence band to conduction band. In this work we qualitatively explain the effects of the physico- chemical states of the thin films on the structure of the obtained MO spectra, mainly on the appearance of the MO activity in the low energy region, and on the changes of the position of the MO peak. Compared to other preparation methods the epitaxial thin films allow achieving a shift of the MO peak in the direction of higher photon energy.

This diploma thesis studies magneto-optical (MO) response of epitaxial thin films of Co-doped ceria. Thin films were characterized by XPS, LEED, STM, spectroscopic ellipsometry and measurement of MO activity. The work focuses on studying MO response of the films depending on film thickness, cobalt concentration, oxidation state of cerium and chemical state of cobalt. Spectra of MO response consist of low energy region where the MO activity is mediated by transitions from defect induced states to conduction band and high energy region where a peak of MO activity appears which we attribute to transitions from valence band to conduction band. In this work we qualitatively explain the effects of the physico- chemical states of the thin films on the structure of the obtained MO spectra, mainly on the appearance of the MO activity in the low energy region, and on the changes of the position of the MO peak. Compared to other preparation methods the epitaxial thin films allow achieving a shift of the MO peak in the direction of higher photon energy.

No description available.

Katalytisk förbränning är en lovande teknik för användning vid kraftgenerering, särskilt för gasturbiner. Genom att använda katalytisk förbränning kan man nå mycket låga emissioner av kväveoxider (NOX), kolmonoxid (CO) och oförbrända kolväten (UHC) samtidigt, vilket är svårt vid konventionell förbränning. Förutom att man erhåller låga emissioner, kan katalytisk förbränning stabilisera förbränningen och kan därmed användas för att uppnå stabil förbränning för gaser med låga värmevärden. Denna avhandling behandlar huvudsakligen högtemperaturdelen av den katalytiska förbränningskammaren. Kraven på denna del har visat sig svåra att nå. För att den katalytiska förbränningskammaren ska kunna göras till ett alternativ till den konventionella, måste katalysatorer med bättre stabilitet och aktivitet utvecklas. Målet med denna avhandling har varit att utveckla katalysatorer med högre aktivitet och stabilitet, lämpliga för högtemperaturdelen av en katalytisk förbränningskammare för förbränning av naturgas. En mikroemulsionsbaserad framställningsmetod utvecklades för att undersöka om den kunde ge katalysatorer med bättre stabilitet och aktivitet. Bärarmaterial som är kända för sin stabilitet, magnesia och hexaaluminat, framställdes med den nya metoden. Mikroemulsionsmetoden användes också för att impregnera de framställda materialen med de mer aktiva materialen perovskit (LaMnO3) och ceriumdioxid (CeO2). Det visade sig att mikroemulsionsmetoden kan användas för att framställa katalysatorer med bättre aktivitet jämfört med de konventionella framställningsmetoderna. Genom att använda mikroemulsionen för att lägga på aktiva material på bäraren erhölls också en högre aktivitet jämfört med konventionella beläggningsstekniker. Eftersom katalysatorerna ska användas under lång tid i förbräningskammaren utfördes också en åldringsstudie. Som jämförelse användes en av de mest stabila materialen som rapporterats i litteraturen: LMHA (mangan-substituerad lantan-hexaaluminat). Resultaten visade att LMHA deaktiverade mycket mer jämfört med flera av katalysatorerna innehållande ceriumdioxid på hexaaluminat som framställts med den utvecklade mikroemulsionstekniken. / Catalytic combustion is a promising technology for power applications, especially gas turbines. By using catalytic combustion ultra low emissions of nitrogen oxides (NOX), carbon monoxide (CO) and unburned hydrocarbons (UHC) can be reached simultaneously, which is very difficult with conventional combustion technologies. Besides achieving low emission levels, catalytic combustion can stabilize the combustion and thereby be used to obtain stable combustion with low heating-value gases. This thesis is focused on the high temperature part of the catalytic combustor. The level of performance demanded on this part has been proven hard to achieve. In order to make the catalytic combustor an alternative to the conventional flame combustor, more stable catalysts with higher activity have to be developed. The objective of this work was to develop catalysts with higher activity and stability, suitable for the high-temperature part of a catalytic combustor fueled by natural gas. A microemulsion-based preparation method was developed for this purpose in an attempt to increase the stability and activity of the catalysts. Supports known for their stability, magnesia and hexaaluminate, were prepared using the new method. The microemulsion method was also used to impregnate the prepared material with the more active materials perovskite (LaMnO3) and ceria (CeO2). It was shown that the microemulsion method could be used to prepare catalysts with better activity compared to the conventional methods. Furthermore, by using the microemulsion to apply active materials onto the support a significantly higher activity was obtained than when using conventional impregnation techniques. Since the catalysts will operate in the catalytic combustor for extended periods of time under harsh conditions, an aging study was performed. One of the most stable catalysts reported in the literature, LMHA (manganese-substituted lanthanum hexaaluminate), was included in the study for comparison purposes. The results show that LMHA deactivated much more strongly compared to several of the catalysts consisting of ceria supported on lanthanum hexaaluminate prepared by the developed microemulsion method. / QC 20101104

Research on the cure and early detection of diseases such as diabetes, Alzheimer's, and Parkinson's is becoming of great interest due to the increasing number of people affected by them every year. An accurate and quick detection of various damaging species is highly critical in treatments of such diseases not only for exploring possible cures but also for early detection. If these diseases are detected during the initial stages than the possibility of curing them is much higher. Motivated by this, many researchers today have developed numerous types of sensing devices that can detect various physiological and biological compounds. However, most of these sensors are enzyme based. They have several setbacks such as the lack of sensitivity, restricted selectivity, short shelf life, and biological fouling. To overcome these obstacles, we examine the use of nanoceria modified Pt and Au electrodes for the detection of glucose and reactive oxygen species such as hydrogen peroxide. Amperometric detection of glucose and hydrogen peroxide is critical for biological applications for diabetes and possible Alzheimer's and Parkinson's patients. This dissertation focuses on the exploration of non-enzymatic detection of glucose and reactive oxygen species which has the prospective to be used for biological applications, in addition to an investigation of an odor control technology that uses these reactive oxygen species for the treatment of wastewater plants. The combination of bi-metallic composites with nanoceria showed increased oxidation ability towards glucose and hydrogen peroxide. The following dissertation expands on the relationship between bi-metallic nanoceria composite materials and its electro-oxidation of glucose and hydrogen peroxide towards biological sensing along with an investigation of an odor control technology that utilizes generates hydroxyl radical fine particle mist for the degradation of hydrogen sulfide odor in wastewater treatment plants.