Plasmonic Interactions at Close Proximity in Chiral Geometries: Route toward Broadband Chiroptical Response and Giant Enantiomeric Sensitivity

Chiral metamaterials can have diverse technological applications, such as engineering strongly twisted local electromagnetic fields for sensitive detection of chiral molecules, negative indices of refraction, broadband circular polarization devices, and many more. These are commonly achieved by arranging a group of noble-metal nanoparticles in a chiral geometry, which, for example, can be a helix, whose chiroptical response originates in the dynamic electromagnetic interactions between the localized plasmon modes of the individual nanoparticles. A key question relevant to the chiroptical response of such materials is the role of plasmon interactions as the constituent particles are brought closer, which is investigated in this paper through theoretical and experimental studies. The results of our theoretical analysis, when the particles are brought in close proximity are dramatic, showing a large red shift and enhancement of the spectral width and a near-exponential rise in the strength of the chiroptical response. These predictions were further confirmed with experimental studies of gold and silver nanoparticles arranged on a helical template, where the role of particle separation could be investigated in a systematic manner. The ``optical chirality'' of the electromagnetic fields in the vicinity of the nanoparticles was estimated to be orders of magnitude larger than what could be achieved in all other nanoplasmonic geometries considered so far, implying the suitability of the experimental system for sensitive detection of chiral molecules.

Metallic Nanoparticles Arranged in a Helical Geometry: Route Towards Strong and Broadband Chiro-optical Response

Recent advances in nanotechnology have paved ways to various techniques for designing and fabricating novel nanostructures incorporating noble metal nanoparticles, for a wide range of applications. The interaction of light with metal nanoparticles (NPs) can generate strongly localized electromagnetic fields (Localized Surface Plasmon Resonance, LSPR) at certain wavelengths of the incident beam. In assemblies or structures where the nanoparticles are placed in close proximity, the plasmons of individual metallic NPs can be strongly coupled to each other via Coulomb interactions. By arranging the metallic NPs in a chiral (e.g. helical) geometry, it is possible to induce collective excitations, which lead to differential optical response of the structures to right-and left circularly polarized light (e.g. Circular Dichroism - CD). Earlier reports in this field include novel techniques of synthesizing metallic nanoparticles on biological helical templates made from DNA, proteins etc. In the present work, we have developed new ways of fabricating chiral complexes made of metallic NPs, which demonstrate a very strong chiro-optical response in the visible region of the electromagnetic spectrum. Using DDA (Discrete Dipole Approximation) simulations, we theoretically studied the conditions responsible for large and broadband chiro-optical response. This system may be used for various applications, for example those related to polarization control of visible light, sensing of proteins and other chiral bio-molecules, and many more.

Zinc oxide based photocatalysis: tailoring surface-bulk structure and related interfacial charge carrier dynamics for better environmental applications

As an alternative to the gold standard TiO2 photocatalyst, the use of zinc oxide (ZnO) as a robust candidate for wastewater treatment is widespread due to its similarity in charge carrier dynamics upon bandgap excitation and the generation of reactive oxygen species in aqueous suspensions with TiO2. However, the large bandgap of ZnO, the massive charge carrier recombination, and the photoinduced corrosion-dissolution at extreme pH conditions, together with the formation of inert Zn(OH)(2) during photocatalytic reactions act as barriers for its extensive applicability. To this end, research has been intensified to improve the performance of ZnO by tailoring its surface-bulk structure and by altering its photogenerated charge transfer pathways with an intention to inhibit the surface-bulk charge carrier recombination. For the first time, the several strategies, such as tailoring the intrinsic defects, surface modification with organic compounds, doping with foreign ions, noble metal deposition, heterostructuring with other semiconductors and modification with carbon nanostructures, which have been successfully employed to improve the photoactivity and stability of ZnO are critically reviewed. Such modifications enhance the charge separation and facilitate the generation of reactive oxygenated free radicals, and also the interaction with the pollutant molecules. The synthetic route to obtain hierarchical nanostructured morphologies and study their impact on the photocatalytic performance is explained by considering the morphological influence and the defect-rich chemistry of ZnO. Finally, the crystal facet engineering of polar and non-polar facets and their relevance in photocatalysis is outlined. It is with this intention that the present review directs the further design, tailoring and tuning of the physico-chemical and optoelectronic properties of ZnO for better applications, ranging from photocatalysis to photovoltaics.

Tungsten-based nanomaterials (WO3 & Bi2WO6): Modifications related to charge carrier transfer mechanisms and photocatalytic applications

Heterogeneous photocatalysis is an ideal green energy technology for the purification of wastewater. Although titania dominates as the reference photocatalyst, its wide band gap is a bottleneck for extended utility. Thus, search for non-TiO2 based nanomaterials has become an active area of research in recent years. In this regard, visible light absorbing polycrystalline WO3 (2.4-2.8 eV) and Bi2WO6 (2.8 eV) with versatile structure-electronic properties has gained considerable interest to promote the photocatalytic reactions. These materials are also explored in selective functional group transformation in organic reactions, because of low reduction and oxidation potential of WO3 CB and Bi2WO6 VB, respectively. In this focused review, various strategies such as foreign ion doping, noble metal deposition and heterostructuring with other semiconductors designed for efficient photocatalysis is discussed. These modifications not only extend the optical response to longer wavelengths, but also prolong the life-time of the charge carriers and strengthen the photocatalyst stability. The changes in the surface-bulk properties and the charge carrier transfer dynamics associated with each modification correlating to the high activity are emphasized. The presence of oxidizing agents, surface modification with Cu2+ ions and synthesis of exposed facets to promote the degradation rate is highlighted. In depth study on these nanomaterials is likely to sustain interest in wastewater remediation and envisaged to signify in various green energy applications. (C) 2015 Elsevier B.V. All rights reserved.

Primary and rechargeable zinc-air batteries using ceramic and highly stable TiCN as an oxygen reduction reaction electrocatalyst

Primary and secondary zinc-air batteries based on ceramic, stable, one dimensional titanium carbonitride (TiCN) nanostructures are reported. The optimized titanium carbonitride composition by density functional theory reveals their good activity towards the oxygen reduction reaction (ORR). Electrochemical measurements show their superior performance for the ORR in alkaline media coupled with favourable kinetics. The nanostructured TiCN lends itself amenable to be used as an air cathode material in primary and rechargeable zinc-air batteries. The battery performance and cyclability are found to be good. Further, we have demonstrated a gel-based electrolyte for rechargeable zinc-air batteries based on a TiCN cathode under ambient, atmospheric conditions without any oxygen supply from a cylinder. The present cell can work at current densities of 10-20 mA cm(2) (app. 10 000 mA g(-1) of TiCN) for several hours (63 h in the case of 10 mA cm(-2)) with a charge retention of 98%. The low cost, noble metal-free, mechanically stable and corrosion resistant TiCN is a very good alternative to Pt for metal-air battery chemistry.

Earth-abundant materials for solar hydrogen generation

A critical challenge for the 21st century is shifting from the predominant use of fossil fuels to renewables for energy. Among many options, sunlight is the only single renewable resource with sufficient abundance to replace most or all of our current fossil energy use. However, existing photovoltaic and solar thermal technologies cannot be scaled infinitely due to the temporal and geographic intermittency of sunlight. Therefore efficient and inexpensive methods for storage of solar energy in a dense medium are needed in order to greatly increase utilization of the sun as a primary resource. For this purpose we have proposed an artificial photosynthetic system consisting of semiconductors, electrocatalysts, and polymer membranes to carry out photoelectrochemical water splitting as a method for solar fuel generation.

This dissertation describes efforts over the last five years to develop critical semiconductor and catalyst components for efficient and scalable photoelectrochemical hydrogen evolution, one of the half reactions for water splitting. We identified and developed Ni–Mo alloy and Ni₂P nanoparticles as promising earth-abundant electrocatalysts for hydrogen evolution. We thoroughly characterized Ni–Mo alloys alongside Ni and Pt catalysts deposited onto planar and structured Si light absorbers for solar hydrogen generation. We sought to address several key challenges that emerged in the use of non-noble catalysts for solar fuels generation, resulting in the synthesis and characterization of Ni–Mo nanopowder for use in a new photocathode device architecture. To address the mismatch in stability between non-noble metal alloys and Si absorbers, we also synthesized and characterized p-type WSe₂ as a candidate light absorber alternative to Si that is stable under acidic and alkaline conditions.

Estudo da desativação térmica de catalisadores à base de óxidos mistos de cério e zircônio

Em termos ambientais, os catalisadores automotivos se destacam pelos resultados altamente significativos alcançados após seu uso obrigatório em veículos leves. No entanto, as condições térmicas em que eles operam podem levar a um processo de perda de atividade significativa, após certo tempo de operação. Dentro desse contexto, este trabalho estudou o efeito da temperatura na desativação térmica de catalisadores automotivo modelo. Foram preparados catalisadores baseados em óxido misto de cério e zircônio na proporção 50% em mol de cério e zircônio (CZ). A partir dele foram produzidos os catalisadores Pd-CZ e Pd-CZ-LaAl. O catalisador Pd-CZ foi produzido pela impregnação do CZ com Pd na concentração de 0,5% m/m de CZ. O catalisador Pd-CZ-LaAl foi produzido a partir de uma mistura física do Pd-CZ com o suporte LaAl (alumina dopada com La na concentração de 1,9 % m/m de Al2O3), seguida de calcinação a 500˚C. Foram realizados envelhecimentos a 900C e 1200C em mufla com atmosfera oxidante por 12 e 36h. Os catalisadores foram caracterizados por um conjunto de técnicas físico-químicas. Foram realizadas análises de fisissorção de N2 para a medição da área específica e o estudo da evolução do diâmetro e volume de poros das amostras novas e envelhecidas. Análises de difração de raios X (DRX) foram feitas de forma a acompanhar possíveis transições de fases após o envelhecimento das amostras. Foi realizada análise química para validar a composição das amostras e ensaios de análise térmica para o catalisador CZ visando identificar a temperatura onde ocorre o fenômeno de segregação de fases. Realizaram-se ensaios de redução a temperatura programada (RTP) visando quantificar o consumo de hidrogênio e associá-lo à evolução da redutibilidade das amostras após o envelhecimento térmico. Finalmente, a avaliação catalítica foi realizada com base nas reações de oxidação do CO e do propano e de redução do NO pelo CO, através da obtenção de curvas de lightoff. As análises de DRX mostraram que o envelhecimento a 900C ocasionou alterações de fases da alumina, mas não foi verificada segregação de fases no CZ. Já a 1200C observou-se a referida segregação de fases, que coincide com a drástica queda na área específica das amostras, em alguns casos observando-se o colapso das propriedades texturais do catalisador. As análises de RTP mostraram que, em determinadas condições, o envelhecimento térmico promove a redutibilidade do sistema CZ e a introdução de Pd torna o catalisador mais facilmente redutível o que é evidenciado pelo deslocamento dos picos de redução para temperaturas mais baixas em comparação ao CZ puro. Os testes catalíticos mostraram que a introdução do Pd é um fator fundamental para a conversão do propano. Os catalisadores contendo Pd também converteram melhor o CO. Para os catalisadores envelhecidos a 1200C, o único resultado positivo foi no caso do Pd-CZ-LaAl que apesar deste tratamento térmico, ainda converteu o CO, propano e NO. Desta forma o catalisador Pd-CZ-LaAl apresentou resultados mais satisfatórios e isto evidencia que a mistura com LaAl melhora o desempenho e a estabilidade térmica do catalisador em altas temperaturas (acima de 300C).

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.

Estudo de catalisadores modelo à base de CeO2-ZrO2 dopado com cobre para controle de emissões de NOx

Convencionalmente, metais nobres são empregados como metais ativos em catalisadores automotivos, mas o uso de cobre vem sendo estudado pelo fato de promover sítios ativos para adsorção química e redução de NOx. Diante deste contexto, esta dissertação visa testar novas formulações de catalisadores, com foco em seu desempenho na reação de redução do NO pelo CO e sua seletividade a N2. Foram avaliados o método de adição de cobre no preparo e os teores de cobre utilizados na preparação. Os métodos de adição utilizados foram impregnação a seco (IS), reação em estado sólido (RS) e coprecipitação (CO). Os teores de cobre estudados ficaram entre 0,36 e 6,9% (m/m). Além disso, foi estudado o impacto no desempenho do catalisador após envelhecimento térmico a 950C por 12h. Foram empregadas as seguintes técnicas de caracterização textural e físico-química como espectrometria de absorção atômica, fisissorção de N2, difração de raios X, espectroscopia Raman e redução a temperatura programada. Os catalisadores também foram avaliados na reação de redução do NO pelo CO. A análise textural indicou que o método de coprecipitação levou a características texturais diferentes dos outros catalisadores. Análises de DRX mostraram a formação de CuO cristalino para teores iguais ou superiores a 3,3% (m/m) de cobre. As análises de Redução a Temperatura Programada (RTP) indicaram que ocorreu uma forte interação na interface entre o suporte e as espécies de cobre dispersas, acompanhada da diminuição da temperatura de redução do CuO e da redução parcial da céria em temperaturas mais baixas. Os testes catalíticos mostraram um melhor desempenho dos catalisadores (IS) que apresentaram conversões mais elevadas em menores temperaturas. Com relação ao envelhecimento, observou-se uma diminuição significativa da eficiência dos catalisadores. Uma comparação com catalisadores à base de metal nobre mostrou um bom desempenho dos catalisadores à base de cobre, com a vantagem destes apresentarem emissão de N2O restrita a baixas temperaturas

Eletrodeposição de ligas Zn-Co por corrente contínua e pulsada simples, a partir de banhos ambientalmente não agressivos

Revestimentos produzidos a partir de ligas de Zn-Co são comumente utilizados em indústrias (aeronáutica, de isoladores elétricos e automobilística, por exemplo) devido à sua ótima resistência à corrosão, principalmente quando comparados aos tradicionais revestimentos de Zn puro. Na co-deposição de zinco com metais, como o ferro, cobalto e níquel, ocorre o que se chama de deposição anômala, onde o metal menos nobre (zinco) é preferencialmente depositado, independente do modo de corrente aplicada (contínua ou pulsada). Recentemente, diversos trabalhos relacionam a produção de eletrodepósitos de liga Zn-Co a partir de banhos ambientalmente não agressivos, a fim de substituir os banhos alcalinos extremamente tóxicos, a base de cianeto. Na presente dissertação foram produzidos revestimentos de ligas de Zn-Co sobre substrato de aço carbono, empregando corrente contínua ou corrente pulsada simples, a partir de banhos contendo diferentes concentrações de Co2+ (0,05 mol/L e 0,10mol/L), 0,05 mol/l de Zn2+ e citrato de sódio (0,10 mol/L) como agente complexante, sob condições agitadas. Quatro diferentes valores de densidade de corrente (10 A/m2, 20 A/m2, 40 A/m2 e 80 A/m2) e de frequência de pulso (100 Hz, 500 Hz, 1000 Hz, 2000 Hz) foram aplicados para a produção da liga a partir dos dois banhos, tendo como objetivo avaliar a influência dos parâmetros de deposição(concentração de Co (II), densidade de corrente aplicada e, no caso de deposição por corrente pulsada simples, também da frequência de pulso), nas variáveis eficiência de corrente catódica, composição da liga, densidade de corrente de corrosão, microestrutura e morfologia dos depósitos de liga Zn-Co. As cores das camadas obtidas variaram do cinza claro ao escuro, quase sempre sem brilho, independente do modo de corrente empregado. Foi verificado que o processo normal de eletrodeposição foi prevalente na produção de revestimentos por corrente contínua, enquanto que apenas deposição anômala foi observada quando do uso de corrente pulsada. A maior eficiência de corrente catódica (60%) foi obtida, para corrente contínua, nas condições de menor concentração de Co2+ (0,05 mol/L) e maior densidade de corrente (80 A/m2). Nestas mesmas condições foi determinada uma eficiência de corrente catódica de 98% para corrente pulsada simples na freqüência de 2000 Hz. Maiores teores do metal mais nobre (cobalto) foram alcançados em maiores densidades de corrente para todas as condições empregadas. Os revestimentos assim obtidos apresentavam os menores valores de tamanho de grão, para cada uma das soluções estudadas. Os demais parâmetros estudados também influenciaram na granulometria e na morfologia das ligas obtidas. Revestimentos com melhor resistência à corrosão, contendo teores de cobalto entre aproximadamente 8 e 10% m/m, foram produzidos a partir do banho com maior concentração de Co2+, sob corrente pulsada simples

Materiais tipo hidrotalcita contendo Cu como precursores de catalisadores para a redução de NO pelo CO

Dentre os óxidos de nitrogênio, o N2O é um gás do efeito estufa altamente nocivo. Devido ao potencial contaminante que este possui, torna-se importante a implementação de processos capazes de reduzir a sua emissão, bem como a dos NOx. Tradicionalmente, têm-se empregado catalisadores baseados em metais nobres, porém estes apresentam como principal desvantagem o elevado custo. Desse modo, sempre houve o interesse pelo uso de outros tipos de catalisadores e metais neste sistema de reação. Nesse contexto, na presente dissertação procurou-se sintetizar precursores de catalisadores tipo hidrotalcita Cu-AlCO3 e avaliar o seu desempenho na reação de redução do NO pelo CO, visando melhorar a atividade e a seletividade a N2. Foram estudados diversos parâmetros de síntese e diferentes composições. Os parâmetros mais influentes na síntese foram a relação molar H2O/(Al+Cu) e a temperatura de secagem do sólido, cujos melhores valores foram 434 e 25C, respectivamente. Testaram-se dois sólidos, o primeiro composto pela fase hidrotalcita quase pura e o segundo com uma clara mistura entre fases hidrotalcita e malaquita. As análises térmica e química revelaram presença da fase malaquita em ambos os materiais com porcentagens de 14 e 40%, respectivamente. Os resultados de difração de raios X indicaram a presença da fase CuO para os catalisadores provenientes da calcinação dos materiais tipo hidrotalcita, porém a espectroscopia Raman evidenciou a presença de Cu2O no catalisador proveniente do material com maior mistura de fases. Os ciclos redox mostraram uma melhora na redutibilidade dos catalisadores após um ciclo de oxidação-redução. Além disso, foi estudado o impacto do envelhecimento térmico a 900C por 12 h no desempenho dos catalisadores. Pelos resultados de teste catalítico os melhores desempenhos foram alcançados pelos catalisadores envelhecidos, contudo o catalisador proveniente do precursor mais puro apresentou-se melhor tanto novo como envelhecido em termos de menor rendimento de N2O. Uma comparação com catalisadores à base de metal nobre mostrou um bom desempenho dos catalisadores à base de cobre, com a vantagem destes apresentarem menor emissão de N2O em temperaturas menores

Tunable Ag surface-plasmon-resonance wavelength and its application on the photochromic behavior of TiO2-Ag films

Surface and bulk plasmon resonance of noble metal particles play an essential role in the multicolor photochromism of semiconductor systems containing noble metal particles, Here we examined several key parameters affecting surface plasmon resonance wavelength (SPRW) of Ag particles and investigated the relation between surface plasmon and photochromic reaction wavelength. From the transmission spectra of sandwiched (TiO2/Ag/TiO2) and overcoated (Ag/TiO2) films deposited on quartz substrates at room temperature by rf helicon magnetron sputtering, we demonstrated that the SPRW can be made tunable by changing the surrounding media and thickness of the metal layer. The coloration and bleaching in visible light region due to photochromism were clearly observed for the films inserted with a 0.55 nm Ag layer.

贵金属（Au, Ag, Pt, Pd）纳米材料的可控合成及性能研究

功能化的贵金属纳米材料的设计和可控制备在材料科学研究领域引起了人们广泛的关注。贵金属纳米材料的光学、电学、磁学和催化等物理和化学性质不但与其大小有关，而且还与其形貌息息相关。因此寻求简单而有效的低温溶液合成途径以实现对贵金属纳米材料的尺寸和形貌控制尤为重要。本论文的主要研究内容可以归纳如下： (1)在水溶液中利用种子生长方法分别制备了核壳Au-Pd/Pt三金属复合纳米粒子和三层的核壳AuAg复合纳米粒子。这些纳米粒子的尺寸和组成可以通过改变金种子的加入量来加以调控。 (2)通过种子生长和取代沉积相结合的方法制备了具有金核铂/银双金属壳的铃铛状纳米粒子。通过扫描电子显微镜、透射电子显微镜和X-射线光电子能谱对所得纳米粒子的尺寸、结构和组成进行了表征。 (3)以二肽甘氨酰甘氨酸作为模板合成了具有[111]取向的单晶银纳米片。通过改变实验条件探讨了片状银纳米结构的形成机理。片状银纳米结构的产率可达到80%，反应物之间的摩尔比对产物的尺寸和形貌有至关重要的作用。 (4)将K3[Fe(CN)6]和Na2S2O3的混合溶液进行水热处理，得到了具有立方体形貌的FeIIIFeIII(CN)6（柏林绿）微晶。实验结果显示K3[Fe(CN)6]和Na2S2O3的摩尔比及其浓度对所得产物的尺寸、形貌和组成有决定性的作用。 (5)在室温下通过混合3, 3', 5, 5'-四甲基联苯胺和氯铂酸，成功合成了有机-无机杂化的纳米纤维。纳米纤维的尺寸和形状可以通过改变反应物的比和浓度加以控制。基于不同的实验结果，提出了纳米纤维的可能形成机理。

贵金属纳米粒子的化学合成和自组装纳米结构

一般来说，构筑自组装结构，需要首先构筑基本单元（BuildingBlocks）。广义来讲，原（离）子、分子、原子团、超分子、高分子、生物分子、纳米粒子以及其他尺度的粒子基元都可以充当自组装的基本单元。基本单元在一定条件下会自发聚集生成具有一定功能的材料一或器件。本文关心的是在纳米尺度（1-100纳米）范围内构筑贵金属纳米粒子自组装纳米结构。具体地说，我们侧重贵金属（金、银）纳米粒一子的化学合成，控制贵金属纳米粒子组装成特定的纳米结构（纳米粒子集合体），研究纳米粒子和纳米结构的等离子共振吸收和电化学特性。本文从以下几个方面展开叙述如下：（1）使用两相法，用相对廉价的阳离子表面活性剂十六烷基三甲基澳化按作为保护剂，合成了稳定的金纳米粒子。系统研究了该粒子在各种条件下的自组装过程：溶剂挥发诱导的自组装、双功能分子桥联的自组装和施加力场条件下的受迫自组装。（2）发现阳离子表面活性剂一四辛基漠化钱可以直接诱导水溶性带负电荷的金纳米粒子从水溶液到甲苯相的相转移。更有趣的是，相转移具有尺寸效应，利用尺寸效应可能会实现对某些多分散金纳米粒子进行尺寸精馏。（3）系统研究了小分子桥联的金纳米粒子的可控组装及等离子学和电化学特性。我们发现硫瑾染料分子、钴卟啉梁料分子、刚性分子导线、碘离子都可以作为连接金纳米粒子的，分子胶水。使用类似建筑学上的“砖块胶泥组装”策略可以在纳米尺度莎围内搭筑纳米建筑。所制备的纳米建筑具有可调节的等离子吸收和电催化特性。（4）使用微分脉冲伏安技术研究了银纳米粒子表面组装体在水溶液中的库仑阻塞现象。（5）分子膜支撑的金纳米粒子二维阵列具有纳米阵列电极行为，控制纳米粒子的组装调节了电极界面的异相电子转移动力学。（6）为了解决分子纳米表面修饰的聚集问题，我们发展了固定化纳米表面修饰的方法。该方法适用于分子单层、双层和多层分子自组装系统，并且可以直接进行光学和电化学表征。在纳米表面受限的分子自组装系统表现出了一些有趣的电化学特性。

Unique properties of Ir/ZSM-5 catalyst for NO reduction with CO in the presence of excess oxygen

The reduction of NO with CO in the presence of excess oxygen was investigated over different noble metal catalysts for probing the relationship between catalytic properties and adsorption behaviors. Among the four precious metal catalysts investigated, Ir/ZSM-5 was found to be the only active one for NO reduction with CO under lean conditions. With the decreasing of the Ir content, higher NO conversion and CO selectivity was obtained. Temperature-programmed reaction (TPR) studies of NO/H-2/O-2 and NO/CO/O-2 showed that the Pt/ZSM-5 was active when H-2 was used as the reductant, whereas, the Ir/ZSM-5 was active when CO was the reducing agent. This difference is due to the different mechanisms of the two reactions. Temperature-programmed desorption (TPD) of NO, CO and O-2 showed that NO could dissociate more easily over the Ir/ZSM-5 than on the Pt/ZSM-5, while the oxidation of CO by O-2 proceeded more rapidly on the Pt/ZSM-5 than on the Ir/ZSM-5. The presence of excess O-2 inhibited drastically the dissociation of NO, which is considered as the key step for the NO-CO reaction. The high dissociation rate of NO over the Ir/ZSM-5 is visualized as the key factor for its superior high activity in NO reduction with CO under lean conditions. (C) 2002 Elsevier Science B.V. All rights reserved.