Wavy type Single Chamber Solid Oxide Fuel Cells (SC-SOFCs) have been shown to be conducive to improving the effective electrochemical reaction area contributing to higher performance, compared with planar type SC-SOFCs of the same diameter. This study presents a fabrication process for wavy type SC-SOFCs with a single fabrication step via co-sintering of a triple-layer structure. The monitoring and observation of the curvature evolution of bi- and triple-layer structures during co-sintering has resulted in an improved process with reduced manufacturing time and effort, as regards the co-sintering process for multi-layer structures. Investigation using in-situ monitoring helps different shrinkage behaviours of each porous layer to minimise mismatched stresses along with avoidance of severe warping and cracking. In the co-sintering of the multi-layer structures, the induced in-plane stresses contribute to curvature evolution in the structure, which can be utilised in the design of a curved multi-layer structure via the co-sintering process. For intermediate temperature SOFCs, the materials used are NiO/CGO for anode; CGO for electrolyte; and LSCF for cathode. These materials are tape-casted with 20μm thickness and assembled for bi- and triple-layer structures by hot pressing. Sintering mismatch stresses have been analysed in bi-layer structures, consisting of NiO/CGO-CGO and CGO-LSCF. The maximum sintering mismatch stress was calculated at interface of bi-layer structure in the top layer. In order to achieve the desired wavy type triple-layer structure, flexible green layers of each component were stacked up and laid on alumina rods to support the curvature during the process. In-situ observation, to monitor the shrinkage of each material and the curvature evolution of the structures, was performed using a long focus microscope (Infinity K-2). With these values, the main factors such as viscosity, shrinkage rate of each material, and curvature rate are investigated to determine the sintering mismatch stresses. This enables the prediction of curvature for triple-layer structure and the prediction is validated by in-situ monitoring of the triple-layer structure co-sintering process. Zero-deflection condition is confirmed to maintain initial shape during co-sintering and helps to minimise the development of undesired curvature in the triple-layer structure. Performance testing of the wavy cell was carried out in a methane-air mixture (CH4:O2 =1:1). In comparison with a planar SC-SOFC, it showed higher OCV which might be attributed to not only macro deformation, but also microstructural distribution affecting the effective gas diffusion paths and electrochemical active sites.

Single step co-sintering is proposed as a method to minimise the time and cost of fabricating solid oxide fuel cells (SOFCs). Such a methodology is attractive but challenging due to the differing sintering behaviours and thermal mismatch of the constituent materials of the anode, cathode and electrolyte in solid oxide fuel cells. As a result it is likely that compromises are made for one layer with respect to optimising another. The single chamber solid oxide fuel cell (SC-SOFC) has not seen widespread adoption due to poor selectivity and fuel utilisation, but relaxed some of the stringent SOFC requirements such as sealing, and the need for a dense electrolyte layer. Thus, to initiate the study into single step co-sintering, the single chamber SOFC is earmarked as the first candidate. The effect of single step co-sintering on cell performance is also an attractive area to investigate. Therefore, in this study, a new co-sintering process (single step co-sintering) was applied to fabricate three different types (in terms of the supporting structure) of planar SC-SOFCSs (the anode, cathode and electrolyte supported planar cells) and anode supported wavy types of SC-SOFC in order to reduce fabrication cost and time owing to effective fabrication process. In addition, their performances were tested to establish functionality of the sintered specimens as working electrochemical cells as well as to investigate the maximum performance possible with these cells under single chamber conditions. Moreover, it is also aimed to improve the performance of SC-SOFCs by extending TPB (Triple phase boundary) via wavy type. This study presents a single step co-sintering manufacturing process of planar and wavy single chamber solid oxide fuel cells with porous multilayer structures, consisting of NiO-CGO, CGO and CGO-LSCF as anode, electrolyte and cathode respectively. Pressure of 2 MPa, with the temperature at 60˚C for 5 minutes, was deemed optimal for the hot pressing of these layers. The best result of sintering profile was obtained with heating rate of 1˚C min-1 to 500˚C, 2˚C min-1 to 900˚C and 1˚C min-1 to 1200˚C with 1 hour dwelling; the cooling rate was 3˚C min-1. Hence anode supported SC-SOFC (thickness: 200:40:40 µm, thickness ratio: 10:2:2, anode (A): electrolyte (E): cathode (C)) was fabricated via a single co-sintering process, albeit with curvature formation at edges. Its performance was investigated in methane-oxygen mixtures at a temperature of 600˚C. Maximum open circuit voltage (OCV) and power density of the anode supported planar cell were obtained as 0.69 V and 2.83 mW cm-2, respectively, at a fuel-oxygen ratio of 1. Subsequently, anode thickness was increased to 800 µm and electrolyte thickness was reduced 20 µm (thickness ratio of cell 40:1:2) to obtain curvature-free anode-supported SOFCs with the help of a porous alumina cover plate placed on the top of the cell. The highest power density and OCV obtained from this cell was 30.69 mW cm-2 and 0.71 V, respectively, at the same mix ratio. In addition, the maximum residual stresses between cathode end electrolyte layers of anode supported cells after sintering were investigated using the fluorescence spectroscopy technique. The total mean residual stresses along the x-direction of the final anode supported planar cell after sintering were measured to range from -488.688 MPa to -270.781 MPa. Determination of optimum thickness and thickness ratio of the cell with the defined ideal hot pressing and sintering conditions for single step co-sintering were carried out for cathode and electrolyte supported planar cells using similar fabrication processes. Their performance changes with thickness ratio were examined. The results show that the cathode and electrolyte supported planar cells can be obtained successfully via single step co-sintering technique with the help of alumina cover plates, as with the anode supported cell. In addition, an anode supported wavy SC-SOFC was fabricated via single step co-sintering and its performance was also investigated. The maximum power density and OCV from the final curvature free cathode supported planar cell (thickness: 60:20:800 µm, thickness ratio: 3:1:20, A:E:C) was measured to be 1.71 mW cm-2 and 0.20 V, respectively, at a fuel-oxygen ratio of 1.6. Likewise, the maximum OCV and power density were found to be 0.55 V and 29.39 mW cm-2, respectively, at a fuel-oxygen ratio of 2.6, for the final electrolyte supported curvature free planar cell (thickness: 60:300:40 µm, thickness ratio: 3:15:2, A:E:C). Furthermore, a maximum OCV of 0.43 V and power density of 29.7 mW cm-2 were found from the final anode supported wavy cell (thickness: 800:20:40 µm, thickness ratio: 40:1:2, A:E:C) at a fuel-oxygen ratio of 1. In essence, this study can be divided into five chapters. The first chapter addresses the overview of the research background, problem statement, aims and objective of this study as well as that of novelty and impact. In the second chapter, fundamental information is provided regarding SOFCs and SC-SOFCs in terms of working principles, main components including electrodes electrolytes, advantages and disadvantages, types, material used for each cell components, losses in the system, and so forth. Moreover, the second chapter also contains essential sintering information in order to understand how to approach sintering of ceramics or cermet to fabricate SC-SOFCs. The overall methodology of this study is explained in detail in the third chapter while experimental works are described in the chapter 4, chapter 5, chapter 6, chapter 7 and chapter 8. Chapter 5 also contains background for the fluorescence spectroscopy and a modelling technique for residual stress measurement between ceramic layers. The results of experiments with discussion session are also in the same chapter. The last chapter presents conclusions and the possible routes for future works of the study.

Dans les piles à combustible SOFC (Solid Oxide Fuel cell) de type monochambre (SC-SOFC), l’anode et la cathode, séparées par un électrolyte, sont situées dans une même chambre alimentée par un mélange de combustible et d’oxygène. L’électrolyte, n’ayant alors plus le rôle d’étanchéité entre les compartiments anodique et cathodique, peut être mis en forme par sérigraphie. Cependant, il est nécessaire d’avoir une barrière pour éviter la possible diffusion de l’hydrogène produit localement à l’anode vers la cathode, ce qui peut générer une chute de la tension. L’objectif de ce travail de thèse est de créer une barrière de diffusion localisée via la densification de la surface de l'électrolyte par un traitement laser. Le matériau sélectionné pour l’électrolyte est un oxyde mixte Ce0,9Gd0,1O1,95 (CGO) qui est déposé par sérigraphie sur une anode composite NiO-CGO. Deux types de lasers impulsionnels sont utilisés : un laser UV (λ = 248 nm) et un laser IR (λ = 1064 nm). Les caractérisations microstructurales réalisées ont permis de mettre en évidence les effets du traitement laser pour certaines combinaisons fluence – nombre de tirs, montrant un grossissement de grain de l’électrolyte ou bien des surfaces densifiées mais fissurées. Des modifications structurales et chimiques sur la surface ont été évaluées ainsi que la diffusion de gaz au travers des électrolytes modifiés tout comme leur conductivité électrique. Afin de mieux comprendre l'interaction laser-matière, une modélisation thermique a également été mise en œuvre. Finalement, les performances de piles SC-SOFC ont été améliorées pour les dispositifs présentant un grossissement de grain à la surface de l'électrolyte. / In single-chamber solid oxide fuel cells (SC-SOFC), anode and cathode are placed in a gas chamber where they are both exposed to a fuel/air mixture. Similarly to conventional dual-chamber SOFC, the anode and the cathode are separated by an electrolyte, but in the SC-SOFC configuration it does not play tightness role between compartments. For this reason, a porous electrolyte can be processed by screen printing. However, it is necessary to have a diffusion barrier to prevent the transportation of hydrogen produced locally at the anode to the cathode through the electrolyte that reduces fuel cell performances. This study aims to obtain directly a diffusion barrier through the surface densification of the electrolyte by a laser treatment. The material chosen for the electrolyte was cerium gadolinium oxide Ce0.9Gd0.1O1.95 (CGO) which is deposited by screen printing on a composite NiO-CGO anode. UV laser and IR laser irradiations were used at different fluences and number of pulses to modify the density of the electrolyte coating. Microstructural characterizations confirmed the modifications on the surface of the electrolyte for appropriate experimental conditions showing either grain growth or densified but cracked surfaces. Structural and chemical modifications on the surface were evaluated as well as the gas diffusion through the electrolytes and their electrical conductivity. In order to understand interaction between the laser and the material, thermal modelling was also developed. Finally, SC-SOFC performances were improved for the cells presenting grain growth at the electrolyte surface, particularly, the power density has been enhanced by a factor 2.

Neste trabalho avaliou-se a influência das condições operacionais da célula a combustível microbiana (CCM) na remoção de matéria orgânica de águas residuárias e na geração de energia elétrica direta. As Hipóteses 1, 2 e 3 verificaram respectivamente as influências do tempo de detenção hidráulica (TDH), das condições mesofílica (25 ºC) e termofílica (55 ºC) de temperatura e da razão de recirculação (R) do efluente no cátodo da CCM (0, 1, 3 e 5) na geração de energia elétrica, na adesão e na comunidade microbiana e na remoção de DQO em CCM sem membrana de íon seletiva alimentada com água residuária sintética a base de sacarose. As Hipóteses 1, 2 e 3 foram aceitas. A redução do TDH permitiu maior geração de energia e dominância na comunidade microbiana e menor adesão da comunidade microbiana ao eletrodo. Enquanto que longos TDH removeram mais DQO, porém geraram menores valores de tensão elétrica. As condições termofílicas apresentaram maiores valores de tensão elétrica gerada e maior dominância da comunidade microbiana e menor adesão microbiana ao eletrodo e eficiência de remoção de DQO. A constante cinética aparente em condição termofílica ( 0,035 h-1) foi duas vezes menor que em condição mesofílica ( 0,083 h-1). O aumento da R melhorou a geração de energia e a remoção de DQO, pois houve melhor transferência de massa do meio líquido para os microrganismos e do meio gasoso para liquido e menor concentração de biomassa aderida ao eletrodo do cátodo aumentando a tensão elétrica gerada. Na Hipótese 4, verificou-se o uso e o efeito do TDH no tratamento de vinhaça de cana de açúcar em CCM sem membrana trocadora de íon seletivo operada em condição termofílica. A CCM foi capaz de remover a matéria orgânica da vinhaça de cana de açúcar e gerar energia elétrica direta, validando a Hipótese 4. As hipóteses 5, 6 e 7 avaliaram as influências da relação DQO, nitrogênio e fósforo da água residuária de produção de vinho, do tempo de retenção celular (TRC) e da configuração do eletrodo no desempenho de CCM de duas câmaras usando membrana de íon seletivo. Acataram-se as hipóteses 5, 6 e 7. O desbalanceamento entre DQO, nitrogênio e fósforo da água residuária de produção de vinho é um dos principais obstáculos para o uso desta tecnologia e a relação de DQO:N:P de 700:10:1 tem elevado potencial para gerar energia elétrica direta em CCM, embora não seja eficiente na remoção de matéria orgânica. A geração de energia aumenta com a redução do TRC, visto que há seleção dos microrganismos eletrogênicos e aumento da carga orgânica volumétrica específica reduzindo a competição por substrato. Entretanto, o TRC não influenciou a remoção de matéria orgânica, pois somente uma pequena parte da DQO foi removida similar em todos os TRC. As características físicas do eletrodo como a porosidade, a rugosidade e a densidade de área do eletrodo e a biocompatibilidade do eletrodo são fatores determinantes para aumentar o desempenho da CCM. Entre os eletrodos estudados, o feltro de carbono foi o melhor material encontrado. / In this work the influence of the operational conditions of the microbial fuel cell (MFC) were evaluated in organic matter removal from wastewater treatment and in the power generation. Hypotheses 1, 2 and 3 respectively checked the influences of hydraulic retention time (HRT), of mesophilic and thermophilic conditions (25 °C and 55 °C, respectively) and the recirculation ratio (R) of the effluent in cathode of MFC (0, 1, 3 and 5) in the power generation, microbial adhesion and community and COD removal of membraneless MFC fed with synthetic wastewater based on sucrose. Hypotheses 1, 2 and 3 have been accepted. Reducing the HRT increased the power generation and the dominance in microbial community and decreased the COD removal efficiency and microbial adhesion to the electrode. Long HRT more efficiently removed the organic matter but generated lower voltages. The thermophilic conditions yielded a more dominant microbial community that favored power generation compared with the mesophilic conditions because of reduced microbial adhesion to the electrode. The COD removal efficiencies were higher under mesophilic conditions than under thermophilic conditions due to the higher apparent kinetic constant at mesophilic conditions (0.083 h-1) than in thermophilic conditions (0.035 h-1). Increasing the R improved the power generation and the COD removal, because the mass transfer in the liquid medium for microorganisms was improved and the biomass adhered to the cathode electrode decreased increasing the voltage. In Hypothesis 4, the use and effect of HRT in treating sugar cane vinasse in membraneless MFC operated at thermophilic conditions were evaluated. The CCM was able to remove the COD of sugarcane vinasse and generate electricity directly, confirming the hypothesis 4. Hypotheses 5, 6 and 7 assessed the influences of COD, nitrogen and phosphorus ratio in winery wastewater, of sludge retention time (SRT) and of electrode configuration in dual chamber MFC. Hypotheses 5, 6 and 7 were adopted. The misbalance between COD, nitrogen and phosphorus from winery wastewater is a major obstacle to the use of this technology and COD:N:P ratio of 700:10:1 had high potential to generate power in MFC, although it is not effective in removing organic matter. The power generation increases with the reduction of the SRT, since there were the selection of bioeletrogenic microorganisms and increased the volumetric organic load rate reducing competition for substrate. However, the SRT did not affect the removal of organic matter, because only a small part of COD was removed regardless of SRT. Physical characteristics of the electrode as porosity, roughness and the electrode area density and the biocompatibility of the electrode are key factors to increase the performance of CCM. The carbon felt was the best studied material having the highest values of porosity, roughness and the electrode area density.

Nessa pesquisa foram testadas tanto CCM com membranas e sem membranas que tinham por característica reproduzir sistemas de tratamento de esgoto sanitário. A etapa experimental desse trabalho foi dividida entre o Brasil (ensaios com CCM sem a MTP e utilizando esgoto sanitário) e Portugal (ensaios com CCM tradicionais de uma e duas câmaras, utilizando água residuária sintética e a bactéria Lactobacillus pentosus). A execução em dois locais diferentes resultou em um maior aprofundamento e desenvolvimento da pesquisa. As CCM foram avaliadas principalmente quanto ao potencial elétrico e eficiência da degradação de compostos orgânicos (esgoto sanitário e água residuária sintética). Para os dados obtidos no Brasil, as três configurações apresentaram maior diferença na potência em função do modo de operação. A operação intermitente apresentou a maior potência (11 mW/m2) para a CCM cilíndrica de fluxo ascendente, enquanto que operação continua a maior potência (4,2 mW/m2) foi obtida para a CCM retangular de fluxo horizontal, a qual também apresentava uma maior facilidade na manutenção quanto aos eletrodos (adição/remoção). A CCM cúbica de fluxo ascendente devido a sua concepção simples demandava um sistema complementar para o aumento da remoção de DQO. Apesar da baixa potência mensurada para os ensaios realizados no Brasil há de se pontuar que os mesmos foram obtidos para reatores sem membranas e utilizando o esgoto sanitário, o qual apresentou grande sazonalidade. Para a etapa realizada em Portugal, foi possível realizar quinze diferentes ensaios e mais um ensaio específico de crescimento. A maior potência (10,37 mW/m2) foi obtida para CCM de câmara dupla operada de modo contínuo para um tempo de detenção hidráulico (TDH) de 20 horas. A maior potência obtida para a CCM de câmara única foi de 5,53 mW/m2 quando houve a adição do extrato de levedura (função teórica de mediador). A potência da CCM, na maioria das vezes, esteve relacionada à proporção de sólidos voláteis e totais, SV/ST, quantidade de bactérias, pH, características de operação e por fim a configuração da CCM. O ensaio de crescimento revelou a correlação da potência em função da quantidade de bactérias inseridas da massa do biofilme (SV) e mostra-se como uma ferramenta na avaliação da potência das CCM. / In this research were tested MFC with membranes and without membrane that aimed to reproduce the characteristics of sewage treatment systems. The experimental phase of this work was divided between Brazil (MFC membrane-less using sewage) and Portugal (MFC tests with traditional single and dual chamber, using synthetic wastewater and Lactobacillus pentosus bacteria). The performance in two different locations resulted in a further deepening and development of research. The MFC were evaluated primarily on the electric potential and efficiency of degradation of organic compounds (sewage and synthetic wastewater). For data obtained in Brazil, the three patterns showed greater difference in power as a function of the operating mode. The intermittent operation showed the highest power (11 mW/m2) for the MFC cylindrical upflow, while operation continues the increased power (4.2 mW/m2) was obtained for the rectangular horizontal flow CCM, which also had an easier maintenance as the electrodes (addition/removal). The upflow cubic MFC because of its simple design required a complementary system to increase the COD removal. Despite the low power measured for tests conducted in Brazil there to point out that they were obtained for reactors without membranes and using the sanitary sewer, which showed a high seasonality. To step held in Portugal, was possible fifteen different tests and more individual test growth. The higher power (10.37 mW/m2) was obtained for MFC dual chamber continuously operated for a hydraulic retention time (HRT) of 20 hours. The greater potency obtained for the single chamber MFC was 5.53 mW/m2 when there was the addition of yeast extract (theoretical mediator function). The potency of MFC, most often been related to the proportion of total solids and volatile, VS/TS, the amount of bacteria, pH, operating characteristics, and finally the configuration of the MFC. The growth assay revealed the correlation power as a function of the quantity of bacterial biofilm mass inserted (VS) and shows up as a tool in assessing the potency of the MFC.

Nessa pesquisa foram testadas tanto CCM com membranas e sem membranas que tinham por característica reproduzir sistemas de tratamento de esgoto sanitário. A etapa experimental desse trabalho foi dividida entre o Brasil (ensaios com CCM sem a MTP e utilizando esgoto sanitário) e Portugal (ensaios com CCM tradicionais de uma e duas câmaras, utilizando água residuária sintética e a bactéria Lactobacillus pentosus). A execução em dois locais diferentes resultou em um maior aprofundamento e desenvolvimento da pesquisa. As CCM foram avaliadas principalmente quanto ao potencial elétrico e eficiência da degradação de compostos orgânicos (esgoto sanitário e água residuária sintética). Para os dados obtidos no Brasil, as três configurações apresentaram maior diferença na potência em função do modo de operação. A operação intermitente apresentou a maior potência (11 mW/m2) para a CCM cilíndrica de fluxo ascendente, enquanto que operação continua a maior potência (4,2 mW/m2) foi obtida para a CCM retangular de fluxo horizontal, a qual também apresentava uma maior facilidade na manutenção quanto aos eletrodos (adição/remoção). A CCM cúbica de fluxo ascendente devido a sua concepção simples demandava um sistema complementar para o aumento da remoção de DQO. Apesar da baixa potência mensurada para os ensaios realizados no Brasil há de se pontuar que os mesmos foram obtidos para reatores sem membranas e utilizando o esgoto sanitário, o qual apresentou grande sazonalidade. Para a etapa realizada em Portugal, foi possível realizar quinze diferentes ensaios e mais um ensaio específico de crescimento. A maior potência (10,37 mW/m2) foi obtida para CCM de câmara dupla operada de modo contínuo para um tempo de detenção hidráulico (TDH) de 20 horas. A maior potência obtida para a CCM de câmara única foi de 5,53 mW/m2 quando houve a adição do extrato de levedura (função teórica de mediador). A potência da CCM, na maioria das vezes, esteve relacionada à proporção de sólidos voláteis e totais, SV/ST, quantidade de bactérias, pH, características de operação e por fim a configuração da CCM. O ensaio de crescimento revelou a correlação da potência em função da quantidade de bactérias inseridas da massa do biofilme (SV) e mostra-se como uma ferramenta na avaliação da potência das CCM. / In this research were tested MFC with membranes and without membrane that aimed to reproduce the characteristics of sewage treatment systems. The experimental phase of this work was divided between Brazil (MFC membrane-less using sewage) and Portugal (MFC tests with traditional single and dual chamber, using synthetic wastewater and Lactobacillus pentosus bacteria). The performance in two different locations resulted in a further deepening and development of research. The MFC were evaluated primarily on the electric potential and efficiency of degradation of organic compounds (sewage and synthetic wastewater). For data obtained in Brazil, the three patterns showed greater difference in power as a function of the operating mode. The intermittent operation showed the highest power (11 mW/m2) for the MFC cylindrical upflow, while operation continues the increased power (4.2 mW/m2) was obtained for the rectangular horizontal flow CCM, which also had an easier maintenance as the electrodes (addition/removal). The upflow cubic MFC because of its simple design required a complementary system to increase the COD removal. Despite the low power measured for tests conducted in Brazil there to point out that they were obtained for reactors without membranes and using the sanitary sewer, which showed a high seasonality. To step held in Portugal, was possible fifteen different tests and more individual test growth. The higher power (10.37 mW/m2) was obtained for MFC dual chamber continuously operated for a hydraulic retention time (HRT) of 20 hours. The greater potency obtained for the single chamber MFC was 5.53 mW/m2 when there was the addition of yeast extract (theoretical mediator function). The potency of MFC, most often been related to the proportion of total solids and volatile, VS/TS, the amount of bacteria, pH, operating characteristics, and finally the configuration of the MFC. The growth assay revealed the correlation power as a function of the quantity of bacterial biofilm mass inserted (VS) and shows up as a tool in assessing the potency of the MFC.

Neste trabalho avaliou-se a influência das condições operacionais da célula a combustível microbiana (CCM) na remoção de matéria orgânica de águas residuárias e na geração de energia elétrica direta. As Hipóteses 1, 2 e 3 verificaram respectivamente as influências do tempo de detenção hidráulica (TDH), das condições mesofílica (25 ºC) e termofílica (55 ºC) de temperatura e da razão de recirculação (R) do efluente no cátodo da CCM (0, 1, 3 e 5) na geração de energia elétrica, na adesão e na comunidade microbiana e na remoção de DQO em CCM sem membrana de íon seletiva alimentada com água residuária sintética a base de sacarose. As Hipóteses 1, 2 e 3 foram aceitas. A redução do TDH permitiu maior geração de energia e dominância na comunidade microbiana e menor adesão da comunidade microbiana ao eletrodo. Enquanto que longos TDH removeram mais DQO, porém geraram menores valores de tensão elétrica. As condições termofílicas apresentaram maiores valores de tensão elétrica gerada e maior dominância da comunidade microbiana e menor adesão microbiana ao eletrodo e eficiência de remoção de DQO. A constante cinética aparente em condição termofílica ( 0,035 h-1) foi duas vezes menor que em condição mesofílica ( 0,083 h-1). O aumento da R melhorou a geração de energia e a remoção de DQO, pois houve melhor transferência de massa do meio líquido para os microrganismos e do meio gasoso para liquido e menor concentração de biomassa aderida ao eletrodo do cátodo aumentando a tensão elétrica gerada. Na Hipótese 4, verificou-se o uso e o efeito do TDH no tratamento de vinhaça de cana de açúcar em CCM sem membrana trocadora de íon seletivo operada em condição termofílica. A CCM foi capaz de remover a matéria orgânica da vinhaça de cana de açúcar e gerar energia elétrica direta, validando a Hipótese 4. As hipóteses 5, 6 e 7 avaliaram as influências da relação DQO, nitrogênio e fósforo da água residuária de produção de vinho, do tempo de retenção celular (TRC) e da configuração do eletrodo no desempenho de CCM de duas câmaras usando membrana de íon seletivo. Acataram-se as hipóteses 5, 6 e 7. O desbalanceamento entre DQO, nitrogênio e fósforo da água residuária de produção de vinho é um dos principais obstáculos para o uso desta tecnologia e a relação de DQO:N:P de 700:10:1 tem elevado potencial para gerar energia elétrica direta em CCM, embora não seja eficiente na remoção de matéria orgânica. A geração de energia aumenta com a redução do TRC, visto que há seleção dos microrganismos eletrogênicos e aumento da carga orgânica volumétrica específica reduzindo a competição por substrato. Entretanto, o TRC não influenciou a remoção de matéria orgânica, pois somente uma pequena parte da DQO foi removida similar em todos os TRC. As características físicas do eletrodo como a porosidade, a rugosidade e a densidade de área do eletrodo e a biocompatibilidade do eletrodo são fatores determinantes para aumentar o desempenho da CCM. Entre os eletrodos estudados, o feltro de carbono foi o melhor material encontrado. / In this work the influence of the operational conditions of the microbial fuel cell (MFC) were evaluated in organic matter removal from wastewater treatment and in the power generation. Hypotheses 1, 2 and 3 respectively checked the influences of hydraulic retention time (HRT), of mesophilic and thermophilic conditions (25 °C and 55 °C, respectively) and the recirculation ratio (R) of the effluent in cathode of MFC (0, 1, 3 and 5) in the power generation, microbial adhesion and community and COD removal of membraneless MFC fed with synthetic wastewater based on sucrose. Hypotheses 1, 2 and 3 have been accepted. Reducing the HRT increased the power generation and the dominance in microbial community and decreased the COD removal efficiency and microbial adhesion to the electrode. Long HRT more efficiently removed the organic matter but generated lower voltages. The thermophilic conditions yielded a more dominant microbial community that favored power generation compared with the mesophilic conditions because of reduced microbial adhesion to the electrode. The COD removal efficiencies were higher under mesophilic conditions than under thermophilic conditions due to the higher apparent kinetic constant at mesophilic conditions (0.083 h-1) than in thermophilic conditions (0.035 h-1). Increasing the R improved the power generation and the COD removal, because the mass transfer in the liquid medium for microorganisms was improved and the biomass adhered to the cathode electrode decreased increasing the voltage. In Hypothesis 4, the use and effect of HRT in treating sugar cane vinasse in membraneless MFC operated at thermophilic conditions were evaluated. The CCM was able to remove the COD of sugarcane vinasse and generate electricity directly, confirming the hypothesis 4. Hypotheses 5, 6 and 7 assessed the influences of COD, nitrogen and phosphorus ratio in winery wastewater, of sludge retention time (SRT) and of electrode configuration in dual chamber MFC. Hypotheses 5, 6 and 7 were adopted. The misbalance between COD, nitrogen and phosphorus from winery wastewater is a major obstacle to the use of this technology and COD:N:P ratio of 700:10:1 had high potential to generate power in MFC, although it is not effective in removing organic matter. The power generation increases with the reduction of the SRT, since there were the selection of bioeletrogenic microorganisms and increased the volumetric organic load rate reducing competition for substrate. However, the SRT did not affect the removal of organic matter, because only a small part of COD was removed regardless of SRT. Physical characteristics of the electrode as porosity, roughness and the electrode area density and the biocompatibility of the electrode are key factors to increase the performance of CCM. The carbon felt was the best studied material having the highest values of porosity, roughness and the electrode area density.

La pile à combustible Solid Oxide Fuel Cell (PAC-SOFC) est un système de production d’énergie « propre » qui permet de convertir de l’hydrogène en énergie électrique en ne rejetant que de l’eau. Une nouvelle configuration appelée « monochambre » semble être particulièrement attrayante compte tenu de ces nombreux avantages sur la configuration bi-chambre classique : simplification de fabrication, baisse de la température de fonctionnement, utilisation d’hydrocarbures comme combustible… La mise en place d’un tel système implique le développement de nouveaux matériaux d’électrodes satisfaisants à de nouveaux critères. L’évaluation en condition réaliste de 7 matériaux de cathode potentiels par diverses caractérisations structurale, texturale et catalytique à mis en évidence la difficulté de développer un matériau possédant toutes les caractéristiques requises. Ainsi, un matériau présentant le meilleur compromis est proposé. Une bibliothèque de 15 catalyseurs supportés (3 métaux et 5 supports différents) a ensuite été développée. Ces catalyseurs, ayant pour but d’être intégrés dans l’anode de la pile pour réaliser le reformage d’hydrocarbures, ont été évalués selon une approche combinatoire en condition réaliste (présence d’hydrocarbure, d’eau, de dioxyde de carbone), ce qui a permis de sélectionner les catalyseurs imprégnés de platine, plus robuste notamment en présence d’eau. Finalement, le couplage de la spectroscopie d’impédance avec la chromatographie en phase gaz a permis d’évaluer le comportement électrochimique d’une nouvelle architecture anodique comportant un catalyseur issu de la bibliothèque. Les tests ont montré que l’ajout d’un catalyseur est bénéfique pour la diminution des résistances de polarisation anodiques par production localisée d’hydrogène à partir d’hydrocarbure. / Solid Oxide Fuel Cell is a device for “clean” electricity production from chemical energy. The new configuration called “single-chamber” seems to be very attractive with several advantages over bi-chamber conventional configuration: easier manufacturing, lowering of working temperature, possible use of hydrocarbons as fuel… Such configuration involves the development of new electrode materials satisfying new requirements. The evaluation of 7 potential cathode materials through several characterizations has shown that a compromise has to be found since one material does not exhibit all the requested features. A library of 15 supported catalysts (3 metals and 5 supports) was developed. These catalysts, aimed at be located inside the anodic cermet, were evaluated through a combinatorial approach in realistic condition (presence of hydrocarbon, water, carbon dioxide). Platinum-based catalysts are found the most robust, especially in presence of water. Finally, innovative coupling of electrochemical impedance spectroscopy with gas chromatography measurements was carried out to characterise a new anodic architecture with an enclosed Pt-based catalyst previously evaluated. Tests revealed the beneficial effect of the catalyst insertion over anodic polarisation resistance by hydrogen production from hydrocarbon.

Le projet présenté dans ce mémoire a pour objectif de développer un système de récupération d’énergie des gaz d’échappement d’un véhicule à essence. Constitué de piles à combustible à oxyde solide (SOFC) en configuration monochambre, le dispositif doit convertir l’énergie chimique des gaz imbrûlés en électricité. Son fonctionnement en aval du catalyseur trois voies permettrait de compléter son action dépolluante tout en améliorant l’efficacité énergétique du véhicule. Par opposition aux piles SOFC dites conventionnelles, les piles SOFC monochambres ne nécessitent pas de scellement étanche entre les compartiments et fonctionnent sous un mélange gazeux composé d’hydrocarbures et d’oxygène. L’empilement en stack de plusieurs cellules est simplifié et plus compact, son intégration au cœur du pot d’échappement est donc plus simple. Ce concept a été précédemment étudié dans la littérature et le présent projet a pour but d’améliorer les performances délivrées en optimisant certains paramètres : la géométrie de pile et les matériaux d’électrodes et d’électrolyte. De plus, un mélange gazeux plus représentatif des conditions réelles a été défini et utilisé tout au long du projet. Une étude préliminaire sur les matériaux sous forme de poudre a permis de réaliser un premier choix parmi quatre matériaux de cathode et de définir les conditions de fonctionnement théoriques des cellules. Ensuite, les cellules complètes ont été mises en forme puis étudiées sous mélange gazeux. Une densité maximale de puissance de 25 mW.cm-2 à 550°C pour une cellule Ni-CGO/CGO/LSCF-CGO a ainsi pu être obtenue. / This study aims at developing a system able to recover energy from exhaust gases of a thermal engine. Composed of Solid Oxide Fuel Cells (SOFC) in a single chamber configuration, the device has to convert chemical energy of gases into electricity. Embedded in the exhaust line at the exit of the three-way catalyst, the stack of single chamber SOFC will complete the reduction of toxic gases emissions with an improvement of the vehicle energy efficiency.Unlike conventional SOFC, single chamber SOFC do not require any gastight sealing between compartments and work in a mixed atmosphere composed of hydrocarbon and oxygen. Stack assembly is thus simplified and more compact; insertion into the exhaust line is therefore easier. This concept has been previously studied in the literature and this work aims at enhancing performances through the optimisation of some parameters such as cell geometry and cell components materials.Moreover, a more representative gas mixture of actual compositions in the exhaust line has been defined and used all along this project. A preliminary study on the raw materials has allowed to make a first selection among four cathode materials and to define theoretical working conditions of our cells. Afterwards, cells have been elaborated and then studied in the selected gas mixture. A maximum power density of 25 mW.cm-2 has been obtained at 550°C for a Ni-CGO/CGO/LSCF-CGO cell.

Cette étude est consacrée au développement d’une pile à combustible à oxyde solide (SOFC) de type monochambre. Contrairement à une pile SOFC conventionnelle, le système monochambre fonctionne dans un mélange de gaz hydrocarbure/air ce qui permet de s’affranchir des contraintes d’étanchéités. Le principe de fonctionnement est basé sur la différence d’activité catalytique entre l’anode et la cathode : l’anode doit être sélective à l’oxydation des hydrocarbures et la cathode à la réduction de l’oxygène. La configuration monochambre implique cependant de nouvelles contraintes concernant notamment la stabilité des matériaux sous mélange hydrocarbure/air à haute température.L’objectif de cette thèse est d’optimiser les performances d’une pile monochambre fonctionnant sous mélange méthane/oxygène et d’améliorer la compréhension de ce système.Les différents éléments d’une pile (électrolyte, cathode, anode) ont été caractérisés sous mélange méthane/oxygène. Quatre matériaux de cathodes (LSM, BSCF, SSC, LSCF) ont été comparés au niveau de leur activité catalytique, stabilité, conductivité électrique et résistance de polarisation. Une étude catalytique de l’anode a été réalisée afin d’identifier les réactions chimiques qui se produisent. Une étude de pile complète en géométrie électrolyte support a permis de sélectionner le matériau de cathode LSCF. Cette étude a également mis en évidence la nécessité de diminuer l’épaisseur de l’électrolyte, la géométrie anode support a donc été étudiée. La première pile anode support a présentée une anode inhomogène et un électrolyte poreux. Des travaux ont été menés afin d’homogénéiser l’anode et de diminuer la porosité de l’électrolyte. En optimisant les conditions de fonctionnement (température et rapport CH4/O2), une densité de puissance maximale de 160 mW.cm-2 a été obtenue. / This study is devoted to the development of a single-chamber solid oxide fuel cell. Contrary to a conventional solid oxide fuel cell, a single chamber fuel cell works under a hydrocarbon/air mixture with no more sealing needed. The working principle of this device is based on the difference of catalytic activity between the anode and the cathode: the anode must be selective to hydrocarbon oxidation and the cathode to oxygen reduction. With single-chamber geometry, chemical stability of materials has to be taken into account under hydrocarbon/air mixture at high temperature.The goal of this work is to optimize the performances of a single-chamber cell working under methane/oxygen mixture and to improve this device comprehension.Each part of the cell (electrolyte, anode, cathode) was characterized under methane/oxygen mixture. Four cathode materials (LSM, BSCF, SSC, LSCF) were compared regarding their catalytic activity, stability, electrical conductivity and polarization resistance. The catalytic activity of the anode was studied in order to identify the chemical reactions happening. A study of electrolyte supported cells showed that LSCF material is the most suitable cathode. Furthermore, this study showed that the electrolyte was too thick; the anode supported configuration was studied. The first anode supported cell showed an inhomogeneous anode and a porous electrolyte. From that, a study of the homogeneity of the anode and the densification of the electrolyte was performed. A maximum power density of 160mW.cm-2 was obtained by optimizing the working conditions of the cells (temperature and CH4/O2 ratio).