Esta Tese descreve a preparação de novos eletrodos modificados (EMs) fazendo uso de um método novo, a deposição de partículas de metais nobres, como níquel, paládio e platina sobre partículas de metais comuns, como cobre e ferro. Este método leva aos denominados EMs mistos, que podem apresentar características diferentes e mais eficientes que os EMs Ni, Pd e Pt já estudados, sendo a principal aplicação nas reações de hidrogenação eletrocatalítica (HEC) de substratos orgânicos insaturados. A preparação dos EMs mistos se inicia pelo recobrimento da superfície do eletrodo de trabalho com um filme polimérico. O polímero usado foi o poli-(éter alílico do ácido p-benzenossulfônico), um filme aniônico com boa estabilidade química e mecânica, que pode fazer troca iônica de seus íons H+ por cátions metálicos. Este filme é preparado por varreduras de voltametria cíclica de uma solução do respectivo monômero, que se oxida eletroquimicamente iniciando a reação química de polimerização. Os metais cobre e ferro são introduzidos ao polímero pelo método de troca iônica/redução eletroquímica, onde o EM é mergulhado em uma solução saturada de um sal de cobre ou de ferro para ocorrer a troca iônica. Em seguida, estes íons são reduzidos eletroquimicamente por varreduras de voltametria cíclica, usando uma faixa de potencial adequada. Para se preparar os EMs mistos, mergulhou-se estes EMs (Cu ou Fe) na solução do banho electroless de níquel, paládio e platina. Por esta metodologia partículas destes metais nobres são depositadas pelo processo de deposição metálica electroless (DME), que faz uso de um agente redutor, hipofosfito de sódio, para reduzir os íons destes metais de forma adequada nos EMs Cu ou Fe e onde se espera obter grande área superficial. Os EMs mistos preparados foram: Cu/Ni, Cu/Pd, Cu/Pt, Fe/Ni, Fe/Pd e Fe/Pt. A caracterização dos metais dos EMs mistos foi feita indiretamente por geração eletroquímica de hidrogênio (GH) de uma solução ácida e diretamente pelas técnicas de Difração de Raios X e Microscopia de Varredura Eletrônica (MEV). O processo de deposição metálica foi investigado por medidas de potencial de circuito aberto, realizadas durante a deposição dos metais nobres que indicou a ocorrência do processo de DME em alguns casos e DG (deposição galvânica) em outros. Devido a alguns resultados do processo de deposição metálica, foi estudado o mecanismo de catalise na deposição direta das partículas de níquel, paládio e platina pela redução química por hipofosfito dos íons correspondentes. Preparou-se EMs Ni, Pd e Pt por dois métodos: troca iônica/redução eletroquímica e troca iônica/redução química catalisada pelo filme. Estes foram caracterizados por GH e utilizando o ácido p-toluenossulfônico como modelo, estudos de espectroscopia na região UV/Vis. foram realizados. Estas medidas comprovaram a catálise, pois os EMs preparados por redução química apresentaram melhores resultados para a GH e as análises de UV/Vis. mostraram a forte ligação existente entre os grupos sulfonatos do polímero e os íons metálicos bivalentes, ligação essencial para ocorrer a catálise do filme. Verificou-se que as partículas dos metais nobres podiam estar sendo depositadas por DME ou por DG seguido de DME, mas que em todos os casos ocorria a deposição causada pela catálise do filme. A reatividade dos EMs mistos foi avaliada por um estudo cinético, onde HECs de alguns substratos orgânicos foram realizadas e acompanhadas por medidas de UV/Vis. durante as reações. Obteve-se a constante de velocidade (k) destas reações, as quais foram comparadas entre si e encontrou-se como o EM misto mais eficiente o Cu/Pt. As ks das reações deste EM foram comparadas com ks de outros EMs de Pt, já estudados em nossos laboratórios. / This thesis describes the preparation of new modified electrodes (MEs) using the method of noble metal particles deposition like nickel, palladium and platinum in the surface of commum metals particles as cooper and iron. This new electrodes were denominated mixed MEs, and can show different caractheristics and present higher efficiency than others already studied, being their principal application in electrocatalytic hydrogenation (ECH) of unsaturated organic substrates. The surface electrode were coated with the polymer poly-(ether allyl p-benzenesulfonic), an anionic film with good chemical and mechanic stability that can undergoes ion exchange of ions H+ by metallic cations. This film is prepared by anodic oxidation of the monomer using voltammetric cycles, producing a cation radical initiador of a chain reaction polymerization. Cooper and iron metals are incorporated in the polymer by ion exchange/ electrochemical reduction; the ME were dipped in saturated solution of cooper or iron salt to produce the ion exchange. The ions are then electrochemically reduced. The preparation of mixed MEs is carried out by electrolessly deposidated Ni, Pd or Pt. This methodology use NaH2PO2, to reduce the metal ions. This procedure deposits Ni, Pd and Pt in the surface of Cu or Fe MEs with an expected higher superficial area. The mixed Cu/Ni, Cu/Pd, Cu/Pt, Fe/Ni, Fe/Pd e Fe/Pt MEs were prepared. The characterization of the MEs metals was made indirectly by electrochemically hydrogen generation from an acid solution (HG) and directly by SEM-EDX and Ray X Diffraction analysis. The metallic deposition process was investigated by open circuit during the deposition of nobles metals that indicate the occurrence of electroless deposition (EMD) process in some cases or spontaneous displacement reaction (galvanic deposition - GD) in others. Despite the two mechanisms related above, a catalytic process would occur. To rut in evidence this third process Ni, Pd and Pt MEs were prepared by two methods: ion exchange/electrochemical reduction and ion exchange/chemical reduction catalyzed by the film. The resulting MEs were characterized by HG and spectroscopy in the UV/Vis. For this last analysis, p-toluenossulfonic acid was used as model and the results proved the catalytic mechanism. UV spectroscopy analysis showed strong bonds between the p-toluenossulfonic and the noble metal salts. So particles of noble metals can be deposited not only by EMD or GD but in all cases occur the deposition by film catalysis too. The reactivity of mixed MEs was done by kinetic study, where ECH of some organic substrates were carried out and monitored by UV/Vis spectroscopy. The constant rate (k) of the reactions was calculated and compared with the others mixed MEs. The ks of this ME were compared with the ks of other Pt MEs, already studied. The more reactive of them was the Cu/Pt ME.

Neste trabalho, foi estudada a decomposição catalítica do metano sobre catalisadores coprecipitados, à base de Co-Al, para produção de hidrogênio e nanotubos de carbono. Foram testados catalisadores com diferentes proporções de cobalto e alumínio, bem como o efeito da adição de outros metais bivalentes (Mg, Ni, Zn ou Cu) ao sistema Co-Al. Os catalisadores foram caracterizados por TGA-DTA, DRX, TPR, TPO e imagens de MEV. As reações foram conduzidas em uma termobalança operando como reator diferencial, com 10 mg de catalisador. A faixa de temperatura analisada foi de 500-750°C. Os melhores resultados em termos de atividade e estabilidade foram obtidos com o catalisador Co66Al33. A adição de outros metais bivalentes não melhorou o desempenho do catalisador, principalmente porque esses metais afetaram a redutibilidade do catalisador. Para o catalisador que apresentou os melhores resultados (Co66Al33), foram realizados testes em diferentes temperaturas e condições reacionais. Os resultados mostraram que a forma de ativação afeta o desempenho deste catalisador, de forma que o catalisador pré-ativado produziu maiores quantidades de hidrogênio, nas reações a 550, 600 e 700°C. No entanto, a 650°C, a amostra autoativada teve desempenho semelhante à pré-ativada, inclusive mostrando-se mais ativa após certo tempo de reação. A caracterização do carbono depositado mostrou que todos os catalisadores produziram nanotubos de carbono. As imagens de microscopia eletrônica por varredura (MEV) mostraram a presença de filamentos mais longos e abundantes na amostra Co50Al50. As análises de oxidação a temperatura programada (TPO) indicaram que os nanotubos de carbono são de parede simples (SWNT). Para o catalisador Co66Al33, as análises de TPO indicaram maior produção de SWNT por parte das amostras pré-ativadas. / In this work, we studied the catalytic decomposition of methane over coprecipitated Co-Al based catalysts, for production of hydrogen and carbon nanotubes. Tests were performed with catalysts containing different Co-Al molar ratios, as well as with addition of other divalent metals (Mg, Ni, Zn, or Cu) to Co-Al system. The samples were characterized by TGA-DTA, XRD, TPR, TPO and SEM images. Activity tests were carried out in a thermobalance, operating as a differential reactor, with 10 mg of catalyst. The temperature range studied was 500-750°C. The best results in terms of activity and stability were obtained with the catalyst Co66Al33. Addition of other divalent metals did not improve the catalyst performance, mainly because these metals affected the catalyst reducibility. For the best results sample (Co66Al33), additional tests were performed at different temperatures and reaction conditions. Results showed that the activation method affects the catalyst performance, so as pre-activated sample produced more hydrogen than auto-activated sample, at 550, 600 and 700°C of reaction temperature. Nevertheless, at 650°C, auto-activated sample had performance almost similar to the pre-activated sample, even showing higher activity after a period of reaction. Characterization of deposited carbon showed that all catalysts produced carbon nanotubes. The images of scanning electron microscopy (SEM) showed formation of longer and abundant filaments in the sample Co50Al50. Temperature programmed oxidation analyses indicated that filaments are single walled carbon nanotubes (SWNT). For the catalyst Co66Al33, TPO analyses indicated a higher production of SWNT by pre-activated samples.

abstract: Widespread use of chlorinated solvents for commercial and industrial purposes makes co-occurring contamination by 1,1,1-trichloroethane (TCA), trichloroethene (TCE), and 1,4-dioxane (1,4-D) a serious problem for groundwater. TCE and TCA often are treated by reductive dechlorination, while 1,4-D resists reductive treatment. Aerobic bacteria are able to oxidize 1,4-D, but the biological oxidation of 1,4-D could be inhibited TCA, TCE, and their reductive transformation products. To overcome the challenges from co-occurring contamination, I propose a two-stage synergistic system. First, anaerobic reduction of the chlorinated hydrocarbons takes place in a H2-based hollow-fiber “X-film” (biofilm or catalyst-coated film) reactor (MXfR), where “X-film” can be a “bio-film” (MBfR) or an abiotic “palladium-film” (MPfR). Then, aerobic removal of 1,4-D and other organic compounds takes place in an O2-based MBfR. For the reductive part, I tested reductive bio-dechlorination of TCA and TCE simultaneously in an MBfR. I found that the community of anaerobic bacteria can rapidly reduce TCE to cis-dichloroethene (cis-DCE), but further reductions of cis-DCE to vinyl chloride (VC) and VC to ethene were inhibited by TCA. Also, it took months to grow a strong biofilm that could reduce TCA and TCE. Another problem with reductive dechlorination in the MBfR is that mono-chloroethane (MCA) was not reduced to ethane. In contrast, a film of palladium nano-particles (PdNPs), i.e., an MPfR, could the simultaneous reductions of TCA and TCE to mainly ethane, with only small amounts of intermediates: 1,1-dichloroethane (DCA) (~3% of total influent TCA and TCE) and MCA (~1%) in continuous operation. For aerobic oxidation, I enriched an ethanotrophic culture that could oxidize 1,4-D with ethane as the primary electron donor. An O2-based MBfR, inoculated with the enriched ethanotrophic culture, achieved over 99% 1,4-D removal with ethane as the primary electron donor in continuous operation. Finally, I evaluated two-stage treatment with a H2-based MPfR followed by an O2-MBfR. The two-stage system gave complete removal of TCA, TCE, and 1,4-D in continuous operation. / Dissertation/Thesis / Masters Thesis Civil, Environmental and Sustainable Engineering 2018

Este trabalho teve o objetivo de verificar a existência de correlação entre as concentrações de amônia no município de São Paulo e as concentrações dos poluentes regulamentados associados à emissão veicular. Foi testada a correlação estatística entre as concentrações de amônia e os seguintes parâmetros: fumaça, partículas inaláveis finas, monóxido de carbono, dióxido, monóxido e óxidos de nitrogênio; temperatura e umidade relativa do ar. Os dados utilizados foram fornecidos pela CETESB e medidos na Estação Pinheiros no período de abril/12 a setembro/13. Os resultados obtidos nas análises foram que as concentrações diárias de amônia variaram de 1,3 g/m³ (limite de detecção do método) a 40,0 g/m³, sendo que a média aritmética das concentrações desse período foi de 14,3 g/m³ ± 9,5 g/m³ e a mediana de 14,1 g/m³. Esse valor de média é muito próximo às encontradas em Santiago, Roma, Cidade do México, Pequim e Xian, e os maiores valores diários de amônia foram observados entre novembro/2012 e fevereiro/2013 e as concentrações médias por dia da semana apontaram uma variação entre 12,1 g/m³ a 19,0 g/m³, sendo que a maior média foi observada no domingo. Na comparação com os poluentes atmosféricos, foram observadas algumas tendências de comportamento semelhantes em determinados períodos, porém as correlações foram muito fracas. Com relação aos parâmetros meteorológicos, observou-se que quando ocorreu a máxima de temperatura, o valor de concentração de amônia também foi elevado, porém nos dias em que as concentrações de amônia foram mais altas, as máximas de temperatura não foram as mais elevadas. A correlação encontrada entre a amônia e temperatura foi muito fraca e nos dias com os maiores percentuais de umidade relativa do ar apresentaram valores baixos de concentração de amônia. Não foi possível identificar correlação significante entre concentrações de amônia em relação aos demais poluentes atmosféricos de influência veicular e aos parâmetros meteorológicos temperatura e umidade relativa do ar. Portanto, para o período estudado, as emissões veiculares não influenciaram as concentrações de amônia presentes na região de estudo. Assim, sugere-se o prosseguimento do monitoramento de amônia no ar e estudos posteriores, tendo em vista o aumento de veículos com catalisadores veiculares que podem ocasionar emissão de amônia. / The general objective of this study was to verify the existence of correlation between the ammonia concentrations in São Paulo city and the concentrations of regulated pollutants associated with vehicle emissions. The concentration of air pollutants: black smoke, fine particulate matter, carbon monoxide and nitrogen dioxide, monoxide and oxides; temperature and relative humidity were statistically tested. CETESB measured the pollutants data at Pinheiros Station from April/12 to September/13. The daily ammonia concentrations ranged from 1.3 g/m³ (method detection limit) to 40.0 g/m³ and the average concentrations of this period was 14.3 g/m³ ± 9.5 g/m³ and the median 14.1 g/m³. This average value is very close to those found in Santiago, Rome, Mexico City, Beijing and Xi\'an, the largest daily ammonia values were observed between November/2012 and February/2013, and the average concentrations by day of week pointed a variation between 12.1 to 19.0 g/m³. The highest average was observed on Sunday. In the comparison between the atmospheric pollutants and air temperature and humidity some similar trends behavior were observed in certain periods, but the correlations were very weak. It was not possible to identify a significant correlation between ammonia concentration with air pollutants vehicular influence and meteorological parameters temperature and relative humidity. Therefore, for the period studied, vehicle emissions did not affect the concentrations of ammonia present in the study area. It is suggested to continue the monitoring of ammonia in the air and further studies due to the increase of vehicles equipped with catalysts, which can cause emission of ammonia.

Reforma catalítica de nafta é um dos processos mais importantes para a produção de gasolina de alta octanagem, hidrocarbonetos aromáticos e hidrogênio na indústria de petróleo e petroquímica. Para predizer os rendimentos e as propriedades dos produtos ou mesmo melhorar as condições de processo é recomendado descrever o processo matematicamente em termos de modelos cinéticos. A nafta tem um grande número de compostos com número de carbonos variando de cinco a doze, assim, um modelo considerando todos os componentes e reações, é complexo. Modelos baseados em lumps costumam agrupar os compostos em isômeros de mesma natureza. Neste trabalho, é proposto um modelo cinético de uma unidade comercial de reforma catalítica com regeneração contínua de catalisador (CCR Continuous Catalyst Regeneration) capaz de predizer o perfil de temperatura e a de composição dos produtos ao longo do reator. O modelo é baseado na análise de hidrocarbonetos parafínicos, naftênicos e aromáticos e na temperatura de carga. A cinética envolve 24 reações modeladas como de pseudo-primeira ordem e 19 componentes. Os parâmetros cinéticos foram estimados usando dados de uma unidade da Petrobras, localizada em Cubatão-SP. O modelo proposto descreve a operação de quatro reatores com fluxo radial representando-os como um reator de fluxo pistonado (PFR Plug Flow Reactor), pois nas condições de operação os efeitos de dispersão radial e axial são assumidos desprezíveis. Os resultados mostram que o modelo pode ser usado para prever os rendimentos de benzeno, tolueno, xileno e hidrogênio. Para os demais compostos os resultados demonstram a necessidade de sofisticação da abordagem. O modelo representa de forma adequada a variação da concentração dos compostos e da temperatura ao longo do inventário de catalisador. / Naphtha catalytic reforming is one of the most important processes for producing high octane gasoline, aromatic products and hydrogen in petroleum and petrochemical industries. To predict yield and properties of the products or even improve the process conditions it is recommended to mathematically describe the process in terms of kinetic models. The naphtha feedstock has a large number of compounds with carbon number ranging from five to twelve. Thus, a detailed kinetic model considering all the components and reactions is complex. Lumping models are used to group the compounds in terms of isomers of the same nature. A kinetic and reactor model of a commercial naphtha continuous catalytic reforming process is proposed to predict temperature profile and products composition. The model is based on paraffins, naphthenes and aromatics analysis and reformer inlet temperature. Kinetics involves 24 pseudo-first-order rate reactions with 19 compounds. All parameters were estimated from industrial data of a Petrobras Refinery at Cubatão-SP. The reactor model describes four radial flow reactors represented by a PFR, due to the fact that under typical reformer operating conditions, radial and axial dispersion effects were found to be negligible. Simulation results demonstrate good agreements between model predictions and actual plant data for benzene, toluene, xylenes and hydrogen. For the remaining compounds, the model output suggests the need for approach sophistication. Nevertheless, the model adequately represents

The goal of this research was to quantify the degradation experienced by a polymer electrolyte fuel cell after storage at subzero temperatures ranging from 0 to -40°C. The performance loss was determined by comparing the polarization and other applicable power curves before and after the subzero storage cycle. The causes of this performance degradation were investigated by the use of Scanning Electron Microscope, Energy Dispersive x-ray Spectroscopy, and porosity scanning technologies. It was found that there are two distinct types of degradation experienced by the membrane. The first type was identified as a variance of the actual voltage - current relationship of the cell. The membrane experienced a 2 - 15% power reduction depending on the load applied to the cell. This mode of degradation only pertained to the initial freeze/thaw cycle and was not observed after any number of subsequent cycles. The cause of this type of degradation has been hypothesized to be related to the delamination of the proton exchange, gas diffusion, and micro porous layers. The second type of degradation was only observed during the subsequent cycles, and mainly affected the high power regions of the operating range. A 5% reduction in current density and power output was observed as a result of further freeze/thaw cycles. Mass transport limitations may have been caused by the destruction of the meso-porous gas diffusion and micro-porous layers. The pore size, volume, and membrane surface area were quantified using a B.E.T. porosity scanner. The results showed that the pore diameter of the catalyst and proton exchange layer did not increase significantly. The porosity scanner did indicate that a pore volume increased by a factor of ten and was confirmed by the surface area measurements of the membrane. The S.E.M. investigations allowed visual inspection of the membrane's structural integrity. Physical separation of the catalyst and gas diffusion layers was observed in the experimental sample, while a more homogeneous assembly was seen in the control sample.

Nitrous oxide (N2O) is an inexpensive and readily available non-toxic rocket motor oxidizer. It is the most commonly used oxidizer for hybrid bipropellant rocket systems, and several bipropellant liquid rocket designs have also used nitrous oxide. In liquid form, N2O is highly stable, but in vapor form it has the potential to decompose exothermically, releasing up to 1865 Joules per gram of vapor as it dissociates into nitrogen and oxygen. Consequently, it has long been considered as a potential "green" replacement for existing highly toxic and dangerous monopropellants. This project investigates the feasibility of using the nitrous oxide decomposition reaction as a monopropellant energy source for igniting liquid bipropellant and hybrid rockets that already use nitrous oxide as the primary oxidizer. Because nitrous oxide is such a stable propellant, the energy barrier to dissociation is quite high; normal thermal decomposition of the vapor phase does not occur until temperatures are above 800 C. The use of a ruthenium catalyst decreases the activation energy for this reaction to allow rapid decomposition below 400 C. This research investigates the design for a prototype device that channels the energy of dissociation to ignite a laboratory scale hybrid rocket motor.

Includes summary. Includes bibliographies.

<p>This thesis contains seven papers dealing with iridium and ruthenium based catalytic asymmetric reductions, either of ketones into chiral alcohols, or olefins into chiral alkanes. The first part of the thesis describes how we have designed and evaluated new bicyclic ligands containing either <i>N</i>,<i>S</i> or <i>N</i>,<i>N</i> chelating atoms. The ligands have been evaluated in the asymmetric Ir-catalyzed transfer hydrogenation of acetophenone. The complexes evaluated induced good enentioselectivity of the product. Moreover we have also utilized a commercially available chiral diamine (QCD-amine) as a ligand in the Ru-catalyzed hydrogenation of prochiral ketones, with excellent enantioselectivity for some of the substrates used. As part of this work we investigated, both theoretically and experimentally, the mechanism of this hydrogenation. Based on these results we have proposed a new reaction mechanism for this type of hydrogenations which involves active participation of the solvent in the catalytic cycle. The last part of the thesis describes the design, synthesis and evaluation of <i>N</i>,<i>P</i> and <i>N</i>₂<i>C</i>-carbene,<i>N</i> ligands for the Ir-catalyzed hydrogenation of carbon-carbon double bonds. The selectivities obtained in these investigations are among the best reported so far for a broad variation of substrates. A selectivity model for this hydrogenation has been derived and used in the rationalization of the results. As a part of this work we have synthesized and evaluated a new class of substrates, vinyl silanes, and showed that the scope of the hydrogenation reaction can be expanded to this new substrate class.</p>

Detection of chromium and vanadium is of interest for biomedical and environmental applications. The two metals have narrow limits between being essential and toxic for humans. Ultra-sensitive techniques have been studied to measure Cr and V at low concentrations found in human blood and environmental samples. Bismuth film and mercury-alloy electrodes have been developed as alternatives to traditional Hg-based electrodes for Cr and V detection. While catalytic adsorptive stripping voltammetry (CAdSV) has been used to detect Cr and V, little is known about the process. The mechanisms of CAdSV have been probed to provide a better understanding of its exceptional sensitivity and selectivity. Near-real time monitoring of plume gas constituents is desired as a diagnostic tool for combustion efficiency, ensuring safe testing conditions and observing releases of green house gasses. Ground testing rockets is a crucial preliminary step that ensures their performance during critical space missions. Optical sol-gel sensors for carbon dioxide have been developed for remote sensing applications. They are inexpensive and are compatible with the harsh environments encountered during rocket plume tests. The sensors are a viable approach to compliment current infrared (IR) measurements for real-time carbon dioxide detection. Additional work on kerosene and isopropyl alcohol sensing has been explored for incorporation into a multi-analyte sensing platform.