In this thesis, we present the investigation of influence of methanol crossover, which significantly decreases the performance of DMFC (Direct Methanol Fuel Cell). Additionally the poisoning effect occurs on the cathode side. The durability of cathode catalyst exposed by methanol vapor is studied. Moreover, the regene- rative behavior after exposition has been found. The comparison of commercial catalyst with our own sputtered Pt and PtCo and PtRu thin layers as cata- lyst is presented. Obtained results have shown that PtCo is reasonable compro- mise between pure Pt, which has high performance, and PtRu, which is tolerant to methanol poisoning. Future research should further evaluate the advantages of PtCo cathode catalyst prepared by standard procedures and its market poten- tial in comparison with PtRu. 1

Células a combustível de óxido sólido suportadas no eletrólito de zircônia estabilizada com ítria (YSZ) foram fabricadas usando a técnica do recobrimento por rotação (spin-coating) para deposição de catodos de manganita de lantânio dopada com estrôncio (LSM) e anodos compósitos de níquel e YSZ (Ni-YSZ). Parâmetros microestruturais dos eletrodos, tais como espessura, tamanho médio de partículas e temperatura de sinterização foram otimizados, visando reduzir a resistência de polarização da célula e melhorar o seu desempenho. Estes estudos serviram de base para a fabricação de células com camada catalítica para uso com etanol direto. Sobre o anodo Ni-YSZ da célula foi depositada uma camada catalítica de céria dopada com gadolínia (CGO) com 0,1% em peso de irídio (Ir-CGO). A camada catalítica visa reformar o etanol antes do seu contato com o anodo Ni-YSZ, evitando o depósito de carbono na superfície do Ni que inviabiliza o uso de combustíveis primários contendo carbono nestas células a combustível. Inicialmente, a célula a combustível foi testada com etanol e as melhores condições de operação foram determinadas. Em seguida, as células unitárias foram testadas com etanol sem adição de água por períodos de tempo de até 390 horas. As células a combustível a etanol direto com camada catalítica operam no modo de reforma interna gradual, apresentando boa estabilidade e densidades de corrente similares às obtidas na operação com hidrogênio. Após a operação das células a combustível a etanol direto, análises de microscopia eletrônica de varredura mostraram que não houve formação significativa de depósitos de carbono na superfície do Ni, indicando que a camada catalítica de Ir-CGO foi efetiva para operação com o etanol. Testes de células a combustível a etanol direto sem a camada catalítica revelaram uma rápida degradação nas horas iniciais de operação com formação de grandes quantidades de depósitos de carbono identificados visualmente. Considerando-se a operação estável com etanol a seco por tempos relativamente longos de operação, os resultados alcançados representam um avanço significativo e apontam para o desenvolvimento de células a combustível a etanol direto usando-se os componentes tradicionais com a adição de uma camada catalítica. / Yttria-stabilized zirconia (YSZ) electrolyte supported solid oxide fuel cells were fabricated with spin-coated strontium-doped lanthanum manganite (LSM) cathodes and Ni-YSZ cermet anodes. The microstructural parameters of the electrodes such as thickness, average particle size, and sintering temperature were optimized to decrease the polarization resistance of the single cells and to improve their electrochemical performance. These preliminar studies provided the basis for the fabrication of single fuel cells with a catalytic layer of gadolinia-doped ceria (CGO) and 0.1 wt% iridium (Ir-CGO) deposited onto the anode. The catalytic layer aims at the stable operation with dry (direct) ethanol; it avoids the contact of the alcohol with the anode, preventing the anode degradation by carbon deposition. Initially, the single cells were tested with ethanol and optimized operating parameters were determined. Then, the single cells were operated with anhydrous ethanol for periods of time up to 390 hours. The single cells with catalytic layer operate by the gradual internal reforming of ethanol, with good stability and delivering similar electric current densities as the ones measured using hydrogen as fuel. After single cell operation on direct ethanol, scanning electron microscopy analyses identified no significant carbon deposition on the surface of Ni, indicating that the Ir-CGO catalytic layer was effective for the reforming of ethanol. Such results were compared to the ones of standard single cells operating on dry ethanol, which showed a fast degradation and the formation of large amounts of carbon deposits. Considering the rather stable performance of single cells running on dry ethanol for relatively long times, such results represent a significant advance towards the development of direct ethanol solid oxide fuel cells using the standard components and a catalytic layer.

Les piles à combustible de type PEMFC constituent un maillon essentiel du cycle utilisant l'hydrogène comme vecteur d'énergie afin de permettre l'utilisation des énergies renouvelables. Cependant, leur développement connaît encore des limitations en termes de performances initiales, de coût et de durabilité. Cette thèse se concentre sur les couches actives des électrodes dont le catalyseur, souvent du platine, peut représenter jusqu'à 25% du coût global. Un des enjeux a ainsi été de mieux comprendre le fonctionnement de ces électrodes, qui peut être inhomogène, afin d'améliorer la distribution du platine dans la couche active et optimiser son utilisation. Pour cela, des électrodes « architecturées », c'est-à-dire avec des chargements en platine variables au sein de la couche active, ont été réalisées grâce à la flexibilité de deux procédés d'impression : le jet d'encre et la sérigraphie. Une adaptation de la formulation des encres catalytiques et des paramètres d'impression a permis la mise en œuvre de ces deux procédés et la réalisation de couches actives présentant une large gamme de chargements en catalyseur (0,05mgPt/cm² à 0,5mgPt/cm²). Différentes distributions de platine ont été étudiées et comparées à des couches actives uniformes: dans le plan d'une part, à l'échelle dent/canal de la plaque bipolaire et à l'échelle entrée/sortie, et dans l'épaisseur d'autre part. Les architectures ont permis de mettre en évidence différentes contributions de la couche active suivant sa localisation sous la plaque bipolaire et ainsi de proposer des modifications de sa structure qui peuvent être réalisées grâce aux procédés d'impression. Par ailleurs, la durabilité des structures les plus pertinentes a été évaluée par des essais de longue durée qui ont montré qu'il est possible de réduire la pente de dégradation par la modification de la distribution du platine. / PEM fuel cells stand for an essential link in the cycle using hydrogen as an energy carrier.However, their development is still limited by initial performance, costs and durability.This study focuses on the electrode catalyst layer which contains most of the time platinum, anexpensive catalyst that can represent 25% of the overall cost of a system. Thus, one of the issues hasbeen to provide a better understanding of electrode operating, which can be heterogeneous. The aim ofthis study is particularly to enhance platinum distribution in the catalyst layer to optimize itsutilization.Architectured electrodes, that is to say with variable platinum loading inside the catalyst layerhave been developed thanks to the flexibility of two printing processes : inkjet printing and screenprinting. The adjustment of catalyst ink formulation and printing parameters enabled to fabricatecatalyst layers with a wide range of platinum loading, from 0,05mgPt/cm² to 0,5mgPt/cm². Severalplatinum distributions were compared to uniform catalyst layers at different scales: the scale of ribsand channels and of gas inlet and oultet of bipolar plate, as well as through the catalyst layer thickness.Electrodes architecture enabled to point out different contribution of catalyst layers according to itslocalizing under the bipolar plate and to suggest modifications of its structure that provide an increaseof performance.Otherwise, the estimation of lifetime of several architectures thanks to ageing tests in loadcycling mode showed that these structures enabled to reduce their performance decay rate.

Células a combustível de óxido sólido suportadas no eletrólito de zircônia estabilizada com ítria (YSZ) foram fabricadas usando a técnica do recobrimento por rotação (spin-coating) para deposição de catodos de manganita de lantânio dopada com estrôncio (LSM) e anodos compósitos de níquel e YSZ (Ni-YSZ). Parâmetros microestruturais dos eletrodos, tais como espessura, tamanho médio de partículas e temperatura de sinterização foram otimizados, visando reduzir a resistência de polarização da célula e melhorar o seu desempenho. Estes estudos serviram de base para a fabricação de células com camada catalítica para uso com etanol direto. Sobre o anodo Ni-YSZ da célula foi depositada uma camada catalítica de céria dopada com gadolínia (CGO) com 0,1% em peso de irídio (Ir-CGO). A camada catalítica visa reformar o etanol antes do seu contato com o anodo Ni-YSZ, evitando o depósito de carbono na superfície do Ni que inviabiliza o uso de combustíveis primários contendo carbono nestas células a combustível. Inicialmente, a célula a combustível foi testada com etanol e as melhores condições de operação foram determinadas. Em seguida, as células unitárias foram testadas com etanol sem adição de água por períodos de tempo de até 390 horas. As células a combustível a etanol direto com camada catalítica operam no modo de reforma interna gradual, apresentando boa estabilidade e densidades de corrente similares às obtidas na operação com hidrogênio. Após a operação das células a combustível a etanol direto, análises de microscopia eletrônica de varredura mostraram que não houve formação significativa de depósitos de carbono na superfície do Ni, indicando que a camada catalítica de Ir-CGO foi efetiva para operação com o etanol. Testes de células a combustível a etanol direto sem a camada catalítica revelaram uma rápida degradação nas horas iniciais de operação com formação de grandes quantidades de depósitos de carbono identificados visualmente. Considerando-se a operação estável com etanol a seco por tempos relativamente longos de operação, os resultados alcançados representam um avanço significativo e apontam para o desenvolvimento de células a combustível a etanol direto usando-se os componentes tradicionais com a adição de uma camada catalítica. / Yttria-stabilized zirconia (YSZ) electrolyte supported solid oxide fuel cells were fabricated with spin-coated strontium-doped lanthanum manganite (LSM) cathodes and Ni-YSZ cermet anodes. The microstructural parameters of the electrodes such as thickness, average particle size, and sintering temperature were optimized to decrease the polarization resistance of the single cells and to improve their electrochemical performance. These preliminar studies provided the basis for the fabrication of single fuel cells with a catalytic layer of gadolinia-doped ceria (CGO) and 0.1 wt% iridium (Ir-CGO) deposited onto the anode. The catalytic layer aims at the stable operation with dry (direct) ethanol; it avoids the contact of the alcohol with the anode, preventing the anode degradation by carbon deposition. Initially, the single cells were tested with ethanol and optimized operating parameters were determined. Then, the single cells were operated with anhydrous ethanol for periods of time up to 390 hours. The single cells with catalytic layer operate by the gradual internal reforming of ethanol, with good stability and delivering similar electric current densities as the ones measured using hydrogen as fuel. After single cell operation on direct ethanol, scanning electron microscopy analyses identified no significant carbon deposition on the surface of Ni, indicating that the Ir-CGO catalytic layer was effective for the reforming of ethanol. Such results were compared to the ones of standard single cells operating on dry ethanol, which showed a fast degradation and the formation of large amounts of carbon deposits. Considering the rather stable performance of single cells running on dry ethanol for relatively long times, such results represent a significant advance towards the development of direct ethanol solid oxide fuel cells using the standard components and a catalytic layer.

Les couches catalytiques avec une structure ordonnée à base de nanoparticules de Pt supportées sur des nanofilaments de carbone verticalement alignés ont montré des performances intéressantes grâce à l’amélioration des propriétés du transport de matière et à une meilleure utilisation du Pt. Des études électrochimiques combinées à une modélisation mathématique ont mis en évidence l’influence du transport de protons sur les processus d’oxydo-réduction, la cinétique et le mécanisme de réduction de l’O2 (ORR), et sur H2O2 qui s’échappe des couches pendant l’ORR. Nous avons montré que (i) les protons sont impliqués dans l’étape limitante de la réaction, (ii) pour un pH ≥ 3, un plateau de courant limité par la diffusion des protons est observé et, (iii) pour un pH ≥ 3, le mécanisme de l’ORR implique non seulement les ions hydroniums mais aussi les molécules d’eau. L’intégration de ces couches catalytiques dans des PEMFCs haute température a ensuite été étudiée. Les performances obtenues sont légèrement plus basses que celles des couches conventionnelles. Un travail d’optimisation reste donc à accomplir pour améliorer les performances. / Ordered catalytic layers based on vertically aligned carbon nanofilaments with Pt nanoparticles demonstrate high efficiency for oxygen transport and Pt utilization in the catalytic layer. Electrochemical studies combined with mathematical modeling confirm the influence of the proton transport on surface red-ox processes, the kinetics and the mechanism of the O2 reduction (ORR), and on the H2O2 escape. We show that (i) protons are involved in the rate-determining step of the O2 reduction, (ii) for pH ≥ 3, a plateau corresponding to the diffusion-limited current of protons is observed and, (iii) for pH ≥ 3, the mechanism of the ORR involves not only the hydronium ions but also water molecules. The integration of these catalytic layers in high temperature PEMFCs was then studied. The performance is slightly lower than that for conventional layers. An optimization work is required to improve the performance.

Construed bachelor work features into problems hydrogen fuel articles and survey on low-temperature fuell elements with polymeric electrolyte (PEMFC). Basic sight work is study feature catalyzers on base MnOx on real fuel cell type PEMFC. Exit are then measured characteristic this way creation fuel cell.