A complexidade da reação de redução do oxigênio (RRO) e suas perdas de potencial a fazem responsável por grande parte das perdas de eficiência nas células a combustível. Para esta reação o eletrocatalisador mais apropriado e com melhor desempenho é a Platina, um metal nobre e que torna alto o custo da tecnologia das células a combustível, aumentando as barreiras para entrar no mercado. Primeiramente o trabalho teve em vista reduzir a quantidade em massa de platina utilizada no cátodo, sendo substituída por óxidos de terras raras. Observando que os métodos mais comuns de síntese de eletrocatalisadores para a aplicação em células a combustível se realizam em enumeras etapas, este trabalho se propôs a preparar eletrocatalisadores através de etapas mais simples e que dependessem de menos etapas e tempo de preparo. Através da mistura física simples utilizando ultrassom foram preparados eletrocatalisadores de platina suportada em carbono com os óxidos das terras raras lantânio, cério e érbio, para o estudo em meia célula da RRO. O resultado do gráfico de Koutecky-Levich mostrou que entre os eletrocatalisadores preparados o Pt80Ce20/C foi o que apresentou atividade catalítica mais próxima da platina comercial BASF, sugerindo que a RRO aconteceu via 4 elétrons. Como encontrado na em alguns trabalhos da literatura, entre as terras raras aplicada no cátodo, o cério é o elemento que mais contribui para esta substituição, devido a sua capacidade de estocar e fornecer oxigênio. Esta característica é um grande atrativo para a RRO pois esta reação é primeira ordem em relação a concentração de oxigênio. O resultado mostrou que é possível diminuir a quantidade de platina mantendo atividade catalítica. / The complexity of the oxygen reduction reaction (ORR) and its potential losses make it responsible for the most part of efficiency losses at the Fuel Cells. For this reaction the electrocatalyst witch is most appropriated and shows better performance is platinum, a noble metal that elevates the cost, raising barriers for Fuel Cells technology to enter the market. First this work focuses on reducing the amount of platinum used in the cathode, by being replaced by rare earths. The most common methods of synthesis involves a large amount of steps and this work proposed to prepare the electrocatalyst through a simpler way that would not take so many steps and time to be done. Using an ultrasound mixer the electrocatalyst was prepared mixing platinum supported on carbon black and the rare earths lanthanum, cerium and erbium oxides to be applied in a half-cell study of the ORR. The Koutecky-Levich plots shows that among the electrocatalysts prepared the Pt80Ce20/C had the catalytic activity close to the commercial BASF platinum on carbon black, suggesting that the reaction was taken by the 4-electron path. As found in some works in literature, among the rare earth used to study the ORR, cerium is the one witch shows the better performance because it is able to store and provide oxygen. This feature is of great interest for the ORR because this reaction is first order to the oxygen concentration. Results show that is possible to reduce the amount of platinum maintaining the same electrocatalyst activity.

Submitted by Maicon Juliano Schmidt (maicons) on 2015-04-24T18:31:32Z No. of bitstreams: 1 Sérgio Aldrighi Raffi.pdf: 650009 bytes, checksum: 4e79b9049a00c613c2000ad34bab0732 (MD5) / Made available in DSpace on 2015-04-24T18:31:32Z (GMT). No. of bitstreams: 1 Sérgio Aldrighi Raffi.pdf: 650009 bytes, checksum: 4e79b9049a00c613c2000ad34bab0732 (MD5) Previous issue date: 2012-04-29 / Milton Valente / O objetivo desta pesquisa foi analisar a política de investimento estatal na geração de hidrogênio no Brasil no período 2002-2010. A partir da metodologia de pesquisa bibliográfica, constatou-se que os investimentos brasileiros em hidrogênio estão direcionados para dois segmentos: gerar energia nas células a combustível para suprir veículos e unidades estacionárias e gerar hidrogênio com o objetivo de produzir um combustível com um menor teor de enxofre. Por fim, a preocupação com o meio ambiente tem suscitado a procura por combustíveis mais eficientes e menos poluentes. Neste sentido, os investimentos estatais brasileiros em hidrogênio estão buscando a redução dos impactos ambientais ocasionados por combustíveis fósseis. / The objective of this research was to analyze the policy of state investment in hydrogen generation in Brazil in the period 2002-2010. From the research methodology literature, it was found that Brazilian investments in hydrogen are directed to two segments: power generation in fuel cells to supply vehicles and stationary units and generate hydrogen with the goal of producing a fuel with a lower content of sulfur. Finally, concern for the environment has raised the demand for more fuel efficient and less polluting. In this sense, the Brazilian state investment in hydrogen are seeking to reduce the environmental impacts caused by fossil fuels.

In order to achieve a more stable and highly proton conducting membrane that is also cost effective, the perfluoroalkyl benzenesulfonylimides (PFSI) polymers are proposed as electrolyte for Proton Exchange Membrane Fuel Cells. 4-(trifluoromethyl)-2-diazonium perfluoro-3, 6-dioxa-4-methyl-7-octene benzenesulfonyl imide (I) is synthesized from Nafion monomer via a 5-step schematic reaction at optimal reaction conditions. This diazonium PFSI zwitterionic monomer can be further subjected to polymerization. The loss of the diazonium N2+ functional group in the monomer is believed to form the covalent bond between the PFSI polymer electrolyte and carbon electrodes support. All the intermediates and final products were characterized using 1H NMR, 19F NMR and IR spectrometry.

Nitrogen-rich porous organic frameworks show great promise for use as acid-doped proton conducting membranes, due to their high porosity, excellent chemical and thermal stability, ease of synthesis, and high nitrogen content. Aided by very high surface area and pore volume, the material has the ability to adsorb high amounts of H3PO4 into its network, which creates a proton rich environment, capable of facile proton conduction. The morphology and chemical environment, doping behavior, and proton conduction of these materials were investigated. With such high acid-doping, ex-situ studies revealed that under anhydrous conditions, PA@BILP-16 (AC) produced a proton conductivity value of 5.8 x 10-2 S cm-1 at 60 °C and PA@ALP-6 showed a slightly higher value of 5.91 x 10-2 S cm-1 at 60 °C. With such promising results, in-situ experiments with various analogues are scheduled to be conducted in the near future.

Abstract not available

Remote area power supply (RAPS) is a potential early market for renewable energy - hydrogen systems because of the relatively high costs of conventional energy sources in remote regions. Solar-hydrogen RAPS systems commonly employ photovoltaic panels, a Proton Exchange Membrane (PEM) electrolyser, a storage for hydrogen gas, and a PEM fuel cell. Unitised Regenerative Fuel Cells (URFCs) use the same hardware for both electrolyser and fuel cell functions. Since both of these functions are not required simultaneously in a solar hydrogen RAPS system, URFCs based on PEM technology provide a promising opportunity for reducing the cost of the hydrogen subsystem used in renewable-energy hydrogen systems for RAPS. URFCs also have potential applications in the areas of aerospace, submarines, energy storage for central grids, and hydrogen cars. In this thesis, a general theoretical relationship between cell potential and current density of a single-cell PEM URFC operating in both fuel-cell (FC) and electrolyser (E) modes is developed using modified Butler-Volmer equations for both oxygen- and hydrogen-electrodes, and accounting for mass transport losses and saturation behaviour in both modes, membrane resistance to proton current, and membrane and electrode resistances to electron current. This theoretical relationship is used to construct a computer model based on Excel and Visual Basic to generate voltage-current (V-I) polarisation curves in both E and FC modes for URFCs with a range of membrane electrode assembly characteristics. The model is used to investigate the influence on polarisation curves of varying key parameters such charge transfer coefficients, exchange current densities, saturation currents, and membrane conductivity. A method for using the model to obtain best-fit values for electrode characteristics corresponding to an experime ntally-measured polarisation curve of a URFC is presented. The experimental component of the thesis has involved the design and construction of single PEM URFCs with an active area of 5 cm2 with a number of different catalyst types and loadings. V-I curves for all these cells have been measured and the performance of the cells compared. The computer model has then been used to obtain best-fit values for the electrode characteristics for the URFCs with single catalyst materials active in each mode on each electrode for the corresponding experimentally-measured V-I curves. Generally values have been found for exchange current densities, charge transfer coefficients, and saturation current densities that give a close fit between the empirical and theoretically-generated curves. The values found conform well to expectations based on the catalyst loadings, in partial confirmation of the validity of the modelling approach. The model thus promises to be a useful tool in identifying electrodes with materials and structures, together with optimal catalyst types and loadings that will improve URFC performance. Finally the role URFCs can play in developing cost-competitive solar- hydrogen RAPS systems is discussed, and some future directions for future URFC research and development are identified.

Thesis (M.S.)--Ohio University, June, 2007. / Title from PDF t.p. Includes bibliographical references.

Bioelectrochemical systems couple the oxidation of an electron donor at the anode with the reduction of an electron acceptor at the cathode, using microorganisms to catalyse one or both reactions. When the overall reaction is exergonic, a power output is generated and the system is referred to as microbial fuel cell (MFC); when power is added to the system and hydrogen is produced at the cathode through electrolysis of water, the system is referred to as microbial electrolysis cell (MEC). This PhD thesis is principally focused on the microbial fuel cells technology. Microbial fuel cells are regarded as a sustainable technology for electric energy generation from the oxidation of organic substrates contained in wastewater. The rising need for renewable energy sources and sanitation has encouraged intense research in this novel technology. Nevertheless, up untill now the interest has been primarily focused on the anodic oxidation of organic matter contained in wastewater. However, in addition to organics, wastewater also contains other pollutants, such as soluble nitrogen compounds, for which specific treatment is required. In conventional wastewater treatment systems, the organics available in the wastewater are typically used as electron donor during denitrification. However, a considerable fraction (>50%) of the chemical oxygen demand (COD) is still oxidized aerobically due to the large recirculation flows from the nitrification to the denitrification stages required in anoxic/aerobic configurations to allow for low nitrate levels in the final effluent. This increased COD demand is normally fulfilled by supplementary COD addition, with consequent increase of treatment costs. Alternatively, microorganisms can use inorganic carbon substrates and inorganic electron donors such as hydrogen for denitrification. However, the use of compressed hydrogen is hampered by its low solubility. As a solution, electrochemical hydrogen production permits in situ delivery of the electron donor and is advantaged by simplified control and dissolution of H2. The energy requirements to provide reducing power for denitrification can be decreased if bacteria use the electrode directly as electron donor without intermediate hydrogen production in bioelectrochemical systems. However, fundamental knowledge on bioelectrochemical denitrification is still lacking, therefore, this PhD thesis aims to fill some of these knowledge gaps and to solve some of the bottlenecks of the use of biocathodes. In particular, the goals of this work are: (i) to produce a suitable microbial community able to use the cathode as the sole electron donor during denitrification; (ii) to engineer a bioelectrochemical system able to couple the cathodic denitrification with the oxidation of organics at the anode; (iii) to characterize and quantify the electron losses during anodic and cathodic processes; (iv) to develop a bioelectrochemical system that maximises the nitrogen removal by integrating the nitrification stage into the cathode; finally, (v) to provide an insight into the structural properties of the biofilm performing nitrogen removal at the cathode. The results reveal that microbes can effectively utilize the electrode as electron donor for nitrate reduction to gaseous nitrogen at a redox potential that excludes intermediate production of hydrogen. Measurements revealed that acetoclastic methanogenesis and bacterial growth were responsible for causing the major electron losses at the anode. Adjusting the anodic potential did not achieve a significant overall reduction of the electron losses. At the cathode, the charge transfer efficiencies were instead very high, with the losses only due to the generation of nitrous oxide. Moreover, adjustments of the cathode potential resulted in higher efficiency. High carbon and nitrogen removal was obtained with a COD demand for denitrification as low as 2.4 g per g nitrogen denitrified, which is much lower than typically observed in heterotrophic–based nitrogen removal technologies (>7 g g 1). Nitrogen was removed at rates up to 0.256 kg N m-3 d-1, which is comparable to other autotrophic denitrification processes. Simultaneous nitrification and denitrification was observed in a combined system with cathodic aeration, at bulk dissolved oxygen (DO) levels up to 5 mg L-1, which is considerably higher than normally considered feasible for the process. Confocal laser scanning microscope analysis revealed the existence of a structured biofilm where putative nitrifying organisms occupied the outer layers in contact with the aerated bulk liquid, and putative denitrifying organisms occupy the layers closer to the electrode. These findings are significant in the field of bioelectrochemical systems as they help to unravel some of the complex questions relating to biocathodes. Additionally, the system provides an attractive option to achieve a very high level of nitrogen removal from wastewater with low COD/N ratios due to the selective utilisation of the COD for the denitrification reaction via the electrical transfer of reducing equivalents from the anode to the cathode. However, this research creates new questions, particularly regarding the mechanisms of electron transfer at the cathode. Also a number of practical design and optimisation challenges need to be overcome before wider applications can be considered.

Microbial electrochemical systems (MESs) have attracted much research attention in recent years due to their promising applications in renewable energy generation, bioremediation, and wastewater treatment. In a MES, microorganisms interact with electrodes via electrons, catalyzing oxidation and reduction reactions at the anode and the cathode. The bacterial community of a high power mixed consortium MESs (maximum power density is 6.5W/m��) was analyzed by using denature gradient gel electrophoresis (DGGE) and 16S DNA clone library methods. The bacterial DGGE profiles were relatively complex (more than 10 bands) but only three brightly dominant bands in DGGE results. These results indicated there are three dominant bacterial species in mixed consortium MFCs. The 16S DNA clone library method results revealed that the predominant bacterial species in mixed culture is Geobacter sp (66%), Arcobacter sp and Citrobacter sp. These three bacterial species reached to 88% of total bacterial species. This result is consistent with the DGGE result which showed that three bright bands represented three dominant bacterial species. Exoelectrogenic bacterial strain SX-1 was isolated from a mediator-less microbial fuel cell by conventional plating techniques with ferric citrate as electron acceptor under anaerobic conditions. Phylogenetic analysis of the 16S rDNA sequence revealed that it was related to the members of Citrobacter genus with Citrobacter sp. sdy-48 being the most closely related species. The bacterial strain SX-1 produced electricity from citrate, acetate, glucose, sucrose, glycerol, and lactose in MFCs with the highest current density of 205 mA/m�� generated from citrate. Cyclic voltammetry analysis indicated that membrane associated proteins may play an important role in facilitating electron transfer from the bacteria to the electrode. This is the first study that demonstrates that Citrobacter species can transfer electrons to extracellular electron acceptors. Citrobacter strain SX-1 is capable of generating electricity from a wide range of substrates in MFCs. This finding increases the known diversity of power generating exoelectrogens and provids a new strain to explore the mechanisms of extracellular electron transfer from bacteria to electrode. The wide range of substrate utilization by SX-1 increases the application potential of MFCs in renewable energy generation and waste treatment. Anode properties are critical for the performance of microbial electrolysis cells (MECs). Inexpensive Fe nanoparticle modified graphite disks were used as anodes to preliminarily investigate the effects of nanoparticles on the performance of Shewanella oneidensis MR-1 in MECs. Results demonstrated that average current densities produced with Fe nanoparticle decorated anodes were up to 5.9-fold higher than plain graphite anodes. Whole genome microarray analysis of the gene expression showed that genes encoding biofilm formation were significantly up-regulated as a response to nanoparticle decorated anodes. Increased expression of genes related to nanowires, flavins and c-type cytochromes indicate that enhanced mechanisms of electron transfer to the anode may also have contributed to the observed increases in current density. The majority of the remaining differentially expressed genes were associated with electron transport and anaerobic metabolism demonstrating a systemic response to increased power loads. The carbon nanotube (CNT) is another form of nano materials. Carbon nanotube (CNT) modified graphite disks were used as anodes to investigate the effects of nanostructures on the performance S. oneidensis MR-1 in microbial electrolysis cells (MECs). The current densities produced with CNT decorated anodes were up to 5.6-fold higher than plain graphite anodes. Global transcriptome analysis showed that cytochrome c genes associated with extracellular electron transfer are up-expressed by CNT decorated anodes, which is the leading factor to contribute current increase in CNT decorated anode MECs. The up regulated genes encoded to flavin also contribute to current enhancement in CNT decorated anode MECs. / Graduation date: 2013

Carbon supported PtNi nanoparticles were prepared by hydrazine reduction of Pt and Ni precursor salts under different conditions, namely by conventional heating (PtNi-1), by prolonged reaction at room temperature (PtNi-2) and by microwave assisted reduction (PtNi-3). The nanocomposites were characterized by XRD, EDX, XPS and TEM and used as electrocatalysts in direct methanol fuel cell (DMFC) reactions. Investigations into the mechanism of PtNi nanoparticle formation revealed that platinum nanoparticle seeding was essential for the formation of the bimetallic nanoparticles. The average particle size of PtNi prepared by microwave irradiation was the lowest, in the range of 2.9 – 5.8 nm. The relative rates of electrooxidation of methanol at room temperature as measured by cyclic voltammetry showed an inverse relationship between catalytic activity and particle size in the following order PtNi-1 < PtNi-2 < PtNi-3. / Singapore-MIT Alliance (SMA)