Cette thèse porte sur l’étude et le développement d’électrocatalyseurs à base d’iridium pour la réaction de dégagement de dioxygène (OER) dans les électrolyseurs à membrane échangeuse de protons. En raison de la dégradation marquée des électrocatalyseurs en conditions OER, nous nous sommes particulièrement intéressés à la recherche d’un compromis optimal entre activité catalytique et stabilité. Différents électrocatalyseurs (supportés sur noir de carbone, supportés sur oxydes métalliques dopés et non-supportés) ont été synthétisés et caractérisés par des méthodes électrochimiques et physico-chimiques, notamment par spectroscopie photoélectronique X, microscopie électronique en transmission à localisation identique et spectrométrie de masse à plasma à couplage inductif. Les électrocatalyseurs supportés sont les moins stables en conditions OER, notamment du fait de l’agglomération, la coalescence, la dissolution et le détachement des nanoparticules d’oxyde d’iridium. Ces deux derniers mécanismes de dégradation sont exacerbés par la corrosion des supports carbonés et la dissolution des éléments composant les supports oxydes métalliques dopés. Les électrocatalyseurs non-supportés offrent ainsi le meilleur compromis entre activité et stabilité. Les degrés d’oxydation Ir(III) et Ir(V) ont été identifiés comme les plus actifs pour l’OER en électrolyte acide tandis que l’oxyde Ir(IV) est le plus stable, l’espèce la moins stable étant l’iridium métallique Ir(0). La dégradation des couches catalytiques en cellule d’électrolyse PEM ne semble impacter que très peu les performances globales d’électrolyse par rapport à la dégradation des collecteurs de courant. / This thesis focuses on the study and the development of iridium-based electrocatalysts for the oxygen evolution reaction (OER) in proton exchange membrane water electrolyzers. This work investigates in particular electrocatalyst degradation phenomena and aims at reaching an optimal OER activity-stability ratio. Various electrocatalysts (supported on high-surface area carbon, supported on doped-metal oxides and unsupported) have been synthetized and characterized by electrochemical and physico-chemical methods such as X-ray photoelectron spectroscopy, identical-location transmission electron microscopy and inductively coupled plasma mass spectrometry. Supported electrocatalysts feature stability limitations in OER conditions as revealed by agglomeration, coalescence, dissolution, and detachment of iridium oxide nanoparticles, these last two degradation mechanisms being amplified by corrosion of the carbon supports and dissolution of the elements composing the doped metal oxide supports. Unsupported electrocatalysts currently represent the best compromise between OER activity and stability. Ir(III) and Ir(V) oxides were shown to be the most active towards the OER while Ir(IV) oxide is the most stable, the least stable species being metallic iridium Ir(0). In real PEM water electrolyzers, the global electrolysis performance seems to be less impacted by the degradation of catalytic layers than the degradation of current collectors.

Alternative energy research into hydrogen production via water electrolysis addresses environmental and sustainability concerns associated with fossil fuel use. Renewable-powered electrolyzers are foreseen to produce hydrogen if energy and cost requirements are achieved. Electrocatalysts reduce the energy requirements of operating electrolyzers by lowering the reaction kinetics at the electrodes. Platinum group metals (PGMs) tend to be utilized as electrocatalysts but are not readily available and are expensive. Ni1-xMox alloys, as low-cost and earth-abundant transition metal nanoparticles (NPs), are emerging as promising electrocatalyst candidates to replace expensive PGM catalysts in alkaline media. Pure-phase cubic and hexagonal Ni1-xMox alloy NPs with increasing Mo content (0–11.4%) were synthesized as electrocatalysts for the hydrogen evolution reaction (HER). In general, an increase in HER activity was observed with increasing Mo content. The cubic alloys were found to exhibit significantly higher HER activity in comparison to the hexagonal alloys, attributed to the higher Mo content in the cubic alloys. However, the compositions with similar Mo content still favored the cubic phase for higher activity. To produce a current density of -10 mA/cm2, the cubic and hexagonal alloy NPs require over-potentials ranging from -62 to -177 mV and -162 to -242 mV, respectively. The cubic alloys exhibited over-potentials that rival commercial Pt-based electrocatalysts (-68 to -129 mV at -10 mA/cm2). The cubic Ni0.934Mo0.066 alloy NPs showed the highest alkaline HER activity of the electrocatalysts studied and therefore a patent application was submitted. Bulk Ni–Mo phases have been known as electrocatalysts for the HER for decades, while recently transition metal phosphides (TMPs) have emerged as stable and efficient PGM alternatives. Specifically, Ni2P has demonstrated good HER activity and improved stability for both alkaline and acidic media. However, Ni2P electrocatalysts are a compromise between earth-abundance, performance (lower than Ni–Mo and PGMs) and stability. For the first time Ni–Mo–P electrocatalysts were synthesized with varying atomic ratios of Mo as electrocatalysts for alkaline HER. Specific phases, compositions and morphologies were studied to understand the intrinsic properties of TMPs leading to high HER activity. The Ni1.87Mo0.13P and Ni10.83Mo1.17P5 NPs were shown to be stable for 10 h at –10 mA cm-2 with over-potentials of –96 and –82 mV in alkaline media, respectively. The Ni1.87Mo0.13P and Ni10.83Mo1.17P5 NPs exhibited an improved performance over the synthesized Ni2P sample (–126 mV at –10 mA cm-2), likely a result of the overall phosphorous content and hetero-structured morphologies. A strong correlation between phase dependence and the influence of Mo on HER activity needs to be further investigated. Furthermore, understanding the intrinsic properties of electrocatalysts leading to high water splitting performance and stability can apply electrocatalysts in other research applications, such as photoelectrochemical (PEC) water splitting, water remediation and sustainable chemical processing applications. Contributions to photocatalytic water remediation and electrochemical chlorinated generation to halogenate pyridone-based molecules are reported. Electrochemical techniques were developed and reported herein to aid in understanding electrochemical performance, chemical mechanisms and the stability of electrocatalysts at the electrode-electrolyte interfaces.

Les électrocatalyseurs nanostructurés à base de fer, de carbone et d’azote (Fe/C/N) sont de bonnes alternatives au platine dans les piles à combustible acide. Les Fe/C/N sont synthétisés par pyrolyse laser et sont obtenus à partir de deux précurseurs de fer (FeOOH ou Fe(acac)3), de la pyridine, (avec ou sans méthilimidazole) en présence de NH3. La variation de la fraction volumique de NH3 (RNH3) est étudiée sur une large gamme. Les caractéristiques physico-chimiques des matériaux évoluent de façon monotone avec la variation de RNH3. Les analyses par XPS permettent d’identifier une phase assimilable à du nitrure de fer pour les fortes valeurs de RNH3. Les matériaux les plus actifs en éléctrochimie sont ceux contenant une phase de nitrure de fer. Ceci suggère que la présence de nitrure de fer, permet la formation de sites actifs pour la réduction de O2..L’utilisation de toluène (mélangé à de la pyridine ou à du méthylimidazole) en présence ou non de Fe(acac)3 permet d’obtenir de nouveaux matériaux Fe/C/N ou C/N. Les matériaux C/N moins actifs que ceux contenant du fer, indiquent la présence de sites actifs à base de fer. Des recuits sous Ar ou sous NH3 à 1100°C améliorent l’activité des matériaux. Elle est due à l’élimination de sites azotés inactifs et à la transformation de sites pyridiniques en sites graphitiques. Le recuit sous NH3, plus efficace que celui sous Ar, induit une augmentation de la surface spécifique (Sspé max > 1100 m²/g). Pour un même matériau recuit sous Ar ou sous NH3 la sélectivité de la réduction de O2 (n) atteint 3,70 e- contre 3,93 e- respectivement. Le plus actif d’entre eux atteint un Edép > 950mV/ENH. / Nanostructured Iron-nitrogen-carbon (Fe/N/C) electrocatalysts is a good substitute for platinum in acidic fuel cells. Laser pyrolysis synthesis allows to obtain iron nanocomposites (Fe/N/C). The reaction involves two iron precursors, FeOOH and Fe(acac)3, combined with pyridine (and possibly methylimidazole) in the presence of NH3. The effect of large range variations of NH3’s volume fraction (RNH3) in the reactions is studied. Physicochemical properties of the materials increase monotonically with RNH3. XPS analysis shows that an iron nitride phase appears when RNH3 increase, and electrochemical analysis shows that materials with this iron nitride phase are the most active ones. These results suggest that iron nitride presence triggers the formation of active sites for the oxygen reduction reaction (ORR).Finally, we synthetize new Fe/N/C, or N/C materials using toluene (mixed with pyridine or methylimidazole) in the presence or absence of Fe(acac)3. The obtained Fe/N/C materials are more active than the N/C materials which indicates that iron plays a role in the presence of active sites for the ORR. Annealing under Ar or NH3 at a temperature of 1100°C increases the activity of all the materials. This improvement is due to the suppression of inactive nitrogen sites, and the transformation of some pyridinic sites to graphitic sites. Annealing under NH3 is more effective under Ar beacuse of the increase of the specific surface area (Sspe max > 1100 m2/g). For the same material annealed under Ar versus NH3, the selectivity (n) of the ORR goes from 3.70 up to 3.93 e- respectively. The most active one reaches Edep > 950 mV/ENH.

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Vätgas kan framställas från förnybara energikällor genom vattenelektrolys med anjonbytande membran (AEMWE). AEMWE har vissa fördelar jämfört med traditionell alkalisk vattenelektrolys och elektrolysmed protonledande membran. Till exempel finns det möjlighet att använda alkalisk elektrolyt (även rent vatten) och billiga platinagruppsmetallfria katalysatorer tillsammans med ett anjonbytesmembran. Den största utmaningen med tekniken är att uppnå utmärkt och stabil prestanda för membran och elektroder. AemionTM anjonbytande membran (AEMs) av olika tjocklek, vattenupptag och kapacitet undersöktes i ett AEMWE system med 5 cm2 elektrodarea. Elektrokemisk prestanda hos dessa kommersiella AEM studerades med hjälp av porösa nickel elektroder. Bland de undersökta membranen visade AF2-HWP8-75-X stabil prestanda med en högfrekvent resistans (HFR) på 90 mΩ•cm2 och kunde nå en strömtäthet på 0,8 A/cm2 vid 2,38 V med 1 M KOH vid 60 ˚C.  AEMWE med AF2-HWP8-75-X och olika elektrodkombinationer undersöktes under samma driftsförhållanden. En elektrodkombination med Raney-Ni och NiFeO som katod respektive anod visade bäst prestanda under utvärderingen och gav en strömtäthet på 1,06 och 3,08 A/cm2 vid 2,00 respektive 2,32 V. KOH-lösningens temperatur och koncentration sänktes till 45 ˚C respektive 0,1 M för att undersöka effekten av driftsparametrar på flödescellens prestanda. Flödescellen uppvisade god stabilitet under de nya driftsförhållandena, men dess prestanda minskade avsevärt. Den nådde en strömtäthet på 0,8 A/cm2 vid 2,25 V. / Hydrogen can be produced from renewable energy sources using a novel anion exchange membrane water electrolysis (AEMWE) system. AEMWE has some benefits over the currently used state-of-the-art alkaline and proton exchange membrane water electrolysis systems. For instance, there is a possibility of using alkaline electrolytes (even pure water) and low-cost platinum-group-metal free catalysts together with an ion exchange membrane. However, the main challenge is that the AEMWE system should show excellent and stable performance, depending on the stability of the membrane and the electrodes. AemionTM anion exchange membranes (AEMs) of different thickness and water uptake capacity were investigated using a 5 cm2 AEMWE system. The electrochemical behaviour of these commercial AEMs was studied using nickel (Ni) felt electrodes. Among the investigated AEMs, the AF2-HWP8-75-X showed stable performance with a high frequency resistance (HFR) of 90 mΩ•cm2 and was able to reach a current density of 0.8 A/cm2 at 2.38 V using 1 M KOH at 60 ˚C.  AEMWE systems based on AF2-HWP8-75-X and different electrode combinations were examined under the same operating conditions. An electrode combination with Raney-Ni and NiFeO as cathode and anode, respectively, showed the best performance during the degradation test and provided a current density of 1.06 and 3.08 A/cm2 at 2.00 and 2.32 V, respectively. The operating temperature and concentration of the KOH solution were reduced to 45 ˚C and 0.1 M, respectively, to study the effect of operating parameters on the flow cell performance. The flow cell showed good stability under the new operating conditions, but its performance was reduced significantly. It reached a current density of 0.8 A/cm2 at 2.25 V.

A reação de redução de oxigênio (RRO) foi estudada em eletrocatalisadores formados por nanopartículas de óxidos puros e mistos de metais de transição de Mn, Co e Ni, além de estrutura tipo espinel, e por nanopartículas de Ag, Au e Ag3M (M= Au, Pt, Pd e Cu) suportadas em carbono Vulcan, em eletrólito alcalino. Os óxidos de metais de transição foram sintetizados por decomposição térmica de seus respectivos nitratos e as nanopartículas a base de prata e ouro foram sintetizadas por redução química com borohidreto. Os eletrocatalisadores foram caracterizados por Difratometria e Espectroscopia de Absorção de Raios X (somente para os óxidos de transição). Os materiais a base de óxidos de manganês, mostraram-se com alta atividade para a RRO, para os quais os resultados espectroscópicos in situ evidenciaram a ocorrência da redução do Mn(IV) para Mn(III), na região de início da RRO. Assim, as atividades eletrocatalíticas foram associadas à ocorrência da transferência de elétrons do Mn(III) para o O2. Entretanto, apresentaram forte desativação após ciclagem potenciodinâmica, o que foi associado à formação da fase Mn3O4, conforme indicado por difratometria de Raios X, após os experimentos eletroquímicos, que é eletroquimicamente inativa. Já o material formado pela estrutura do tipo espinel de MnCo2O4 apresentou alta atividade e estabilidade frente à ciclagem e à RRO. A alta atividade eletrocatalítica foi relacionada a ocorrência do par redox CoII/CoIII em maiores valores de potencial em relação ao CoOx e MnOx, devido a interações entre os átomos de Co e Mn no reticulo espinélico. Contrariamente ao observado nos óxidos com maior quantidade de manganês, o espinel mostrou-se altamente estável, o que foi associada à não alteração de sua estrutura no intervalo de potenciais que a RRO ocorre. Para os materiais bimetálicos a base de prata e ouro, os experimentos eletroquímicos indicaram maior atividade eletrocatalítica para o material de Ag3Au/C. Neste caso, a alta atividade foi associada a dois efeitos principais: (i) a um efeito sinergético, no qual os átomos de ouro atuam na região de ativação, favorecendo a adição de hidrogênio e os átomos vizinhos de prata proporcionam a quebra da ligação O-O, conduzindo a RRO pelo caminho de quatro elétrons por molécula de O2; (ii) ao aumento força da ligação Ag-O, devido à interação da Ag com o Au, resultando em maior atividade para a quebra da ligação O-O, aumentando a atividade da Ag para a RRO, em relação à atividade da Ag pura. Assim, a RRO apresentou menor sobrepotencial e maior número de elétrons em Ag3Au/C, quando comparado com as demais nanopartículas bimetálicas. / The oxygen reduction reaction (ORR) was studied on electrocatalysts composed by pure and mixed transition metal oxides of Mn, Co, and Ni, including spinel-like structures, and by Ag, Au, and Ag3M/C (M= Au, Pt, Pd e Cu) bimetallic nanoparticles, in alkaline electrolyte. The transition metal oxides were synthesized by thermal decomposition of their nitrates, and the silver and gold-based nanoparticles by chemical reduction using borohydride. The electrocatalysts were characterized by X-Ray Diffraction and X-Ray Absorption Spectroscopy (in the case of the metal oxides). The manganese-based oxide materials showed high activity for the ORR, in which the in situ spectroscopic results evidenced the Mn(IV) to Mn(III) reduction, in the range of the ORR onset. In this case, the electrocatalytic activities were correlated to the transfer of electron from Mn(III) to O2. However, they presented strong deactivation after several potentiodynamic cycles, which was ascribed to the formation of the electrochemically inactive phase of Mn3O4, as indicated by the XRD results, after the electrochemical experiments. On the other hand, the MnCo2O4 spinel-like material showed high activity and stability for the ORR. Its high electocatalytic activity was attributed to the CoII/CoIII redox pair, taking place at higher potentials, in relation to that of the CoOx e MnOx pure phases, due to the Co and Mn interactions in the spinel lattice. Contrarily to the behavior observed for the manganese-based materials, the spinel oxide presented high stability, which was ascribed to the non alteration of its crystallographic structure in the range of potentials tha the ORR takes place. For the Au and Ag-based materials, the electrochemical experiments indicated higher electrocatalytic activities for Ag3Au/C. In this case, its higher activity as associated to two main aspects: (i) to a synergetic effect, in which the gold atoms act in the activation region, facilitating the hydrogen addition, and the neighboring Ag atoms promoting the O-O bond breaking, leading the ORR to the 4-electrons pathway; (ii) to the increased Ag-O bond strength, due to the electronic interaction between Ag and the Au atoms, resulting in a faster O-O bond breaking, enhancing the electrocatalytic activity of the Ag atoms in the Ag3Au/C nanoparticle, in relation to that on the pure Ag. Therefore, the ORR presented lower overpotential and higher number of electrons in the Ag3Au/C electrocatalyst, when compared to the other investigated bimetallic nanoparticles.

Os eletrocatalisadores Pd/C, Pd/C-15%ATO, PdAu/C-15%ATO (90:10, 70:30 e 50:50), PdIr/C-15%ATO (90:10, 70:30 e 50:50) e PdAuIr/C-15%ATO (90:5:5, 70:20:10 e 50:45:5) foram preparados pelo método de redução por borohidreto de sódio. Esses eletrocatalisadores foram caracterizados por espectroscopia de energia dispersiva de raios X (EDX), difração de raios X (DRX) e microscopia eletrônica de transmissão (MET), enquanto que as atividades eletrocatalíticas para a oxidação eletroquímica do ácido fórmico em meios ácido e alcalino foram investigadas por voltametria cíclica, cronoamperometria e experimentos em células a combustível de ácido fórmico direto (DFAFC) em meios ácido e alcalino a 100 ºC e 60 ºC, respectivamente. Os difratogramas de raios X dos eletrocatalisadores PdAu/C-15%ATO, PdIr/C-15%ATO e PdAuIr/C-15%ATO mostraram a presença de fase de estrutura cúbica de Pd (cfc), ligas de Pd-Au, Pd-Ir e Pd-Au-Ir, fases de carbono e SnO2. As micrografias eletrônicas de transmissão indicaram que as nanopartículas foram bem distribuídas sobre o suporte C-ATO e apresentaram alguns aglomerados. Os estudos eletroquímicos para oxidação de ácido fórmico foram realizados utilizando a técnica de camada fina porosa. Todos os eletrocatalisadores preparados foram testados em células a combustível unitárias alimentadas diretamente por ácido fórmico. Nos estudos comparativos entre os melhores eletrocatalisadores, o eletrocatalisador PdAuIr/C-15%ATO (50:45:5) em meios ácido e alcalino apresentou uma atividade eletrocatalítica superior para a oxidação eletroquímica do ácido fórmico em temperatura ambiente em comparação com o eletrocatalisador Pd/C-15%ATO e os outros eletrocatalisadores binários e ternários preparados. Os experimentos em uma DFAFC unitária ácida e alcalina, também, indicaram que o eletrocatalisador PdAuIr/C-15%ATO (90:5:5) apresentou melhor desempenho para oxidação eletroquímica do ácido fórmico a 100 ºC (meio ácido) e a 60 ºC (meio alcalino), respectivamente, em comparação com os demais eletrocatalisadores sintetizados. Esses resultados indicaram que a adição de Au e Ir ao Pd favorece a oxidação eletroquímica do ácido fórmico, esse efeito pode ser atribuído ao mecanismo bifuncional (a presença de ATO (Sb2O5·SnO2), óxidos de Au e Ir) associados ao efeito eletrônico (ligas de Pd-Au-Ir (cfc)). / Pd/C, Pd/C-15%ATO, PdAu/C-15%ATO (90:10, 70:30 e 50:50), PdIr/C-15%ATO (90:10, 70:30 e 50:50) and PdAuIr/C-15%ATO (90:5:5, 70:20:10 e 50:45:5) electrocatalysts were prepared by sodium borohydride reduction method. These electrocatalysts were characterized by energy dispersive X-ray spectroscopy (EDS), X-ray diffraction (XRD), transmission electron microscopy (TEM) and the electrocatalytic activity toward formic acid electrochemical oxidation in acid and alkaline media was investigated by cyclic voltammetry (CV), chroamperometry (CA) and experiments on direct formic acid fuel cell (DFAFC) at 100 ºC and 60 ºC, respectively. X-ray diffractograms of PdAu/C-15%ATO, PdIr/C-15%ATO and PdAuIr/C-15%ATO electrocatalysts showed the presence of Pd (fcc) phase, Pd-Au, Pd-Ir and Pd-Au-Ir alloys, carbon and SnO2 phases. TEM micrographs indicated that the nanoparticles were well distributed on the C-ATO support and showed some agglomerates. The electrochemical studies for the formic acid oxidation were performed using a thin porous coating technique. All the electrocatalysts prepared were tested in single fuel cells directly fed with acid formic. The PdAuIr/C-15%ATO (50:45:5) electrocatalyst in acid and alkaline media showed the higher electrocatalytic activity for acid formic electro-oxidation at room temperature compared to the Pd/C-15%ATO and others binary and ternary electrocatalysts prepared. The experiments in an acid and alkaline single DFAFC also showed that PdAuIr/C-15%ATO (90:5:5) electrocatalyst exhibited higher performance for formic acid oxidation at 100 ºC and 60 ºC, respectively, in comparison with the others electrocatalysts synthesized. These results indicated that the addition of Au and Ir to Pd promote the formic acid electrochemical oxidation, which could be attributed to the bifunctional mechanism (the presence of ATO (Sb2O5·SnO2), Au and Ir oxides species) associated to the electronic effect (Pd-Au-Ir alloys (fcc)).

Este trabalho teve como objetivo investigar eletrocatalisadores de baixo custo à base de carbeto de tungstênio, carbono e ferro submetidos a diferentes processos de nitretação quanto à atividade catalítica para reação de redução do oxigênio (RRO) nos eletrólitos ácido e alcalino. Os catalisadores foram divididos em três séries distintas, a primeira compreendendo aqueles onde houve variação da carga de carbeto de tungstênio em relação ao suporte de carbono, que foram impregnados com o complexo Fe2+(2,4,6-Tris(2-piridil)-1,3,5-Triazina)2, [Fe(TPTZ)2]2+ e tratados em duas temperaturas diferentes, 700 e 800 oC em atmosfera de nitrogênio. Na segunda série foi mantida constante a carga de carbeto de tungstênio (30% de W/C, m/m) sendo que esta mescla foi preparada usando carbonos dopados previamente com três fontes distintas de nitrogênio (HNO3, NH3 e HNO3/NH3); isto foi seguido pela incorporação do complexo Fe[TPTZ]2+ e pelos mesmos tratamentos térmicos acima mencionados. Na terceira série, os eletrocatalisadores foram preparados com três tipos de carbonos (Vulcan, Ketjenblack e Monarch), aos quais foi incorporado o complexo Fe[TPTZ]2+, seguido pelo tratamento térmico a 800 °C em atmosfera de nitrogênio e então por dopagem com amônia a 950 °C. As três séries de eletrocatalisadores sintetizados neste trabalho foram cuidadosamente caracterizadas por espectroscopia infra-vermelho e UV-Visível, difratometria de raio-x, microscopia eletrônica de transmissão, energia dispersiva de raios-x, espectroscipia Raman, espectroscopia fotoeletrônica de raios-x. As investigações eletroquímicas foram realizadas por voltametria cíclica (VC) e pelo levantamento de curvas de polarização de estado estacionário para a RRO, usando a técnica de eletrodo de disco/anel rotatório, com materiais catalíticos formando filmes finos depositados no eletrodo de disco. Nas três séries de catalisadores foram desenvolvidos materiais com bom desempenho para a RRO. Nos estudos da primeira série de catalisadores, notou-se que o material mais ativo foi aquele formado por WC-FeNx/C com 30 % de W/C e 5% de Fe pirolisado a 800 °C. Na segunda série foi observado que os desempenhos dos catalisadores variaram de acordo com o tipo de protocolo de nitretação, presença de ferro e temperatura de tratamento térmico. Em eletrólito alcalino, os eletrocatalisadores apresentaram maiores desempenhos, que resultaram bastante próximos em relação ao do catalisador de Pt dispersa em carbono usado como referência. Na terceira série de eletrocatalisadores investigados, verificou-se que o melhor desempenho obtido foi com o catalisador com carbono Monarch com amônia, cuja atividade catalítica resultou superior à dos demais, devido ao maior número de estruturas ativas FeNx e N/C formadas pelo tratamento com amônia. Os resultados nos meios ácido e alcalino para a primeira e segunda séries de eletrocatalisadores sugerem a ocorrência de um mecanismo indireto (2e- + 2e-), ou seja, em meio ácido (alcalino) primeiro o O2 reduz para H2O2 (HO2 ) e depois de H2O2 (HO2 ) para H2O. Os sítios predominantemente envolvidos na catálise da reação são WC e FeNx em meio ácido e WC e N/C em meio alcalino. Finalmente, para a terceira série de eletrocatalisadores o mecanismo reacional em meio ácido envolve um mecanismo direto de 4e-, com participação importante dos sítios ativos de Fe-N2. / This work aims to investigate low cost electrocatalysts based on tungsten carbide, carbon and iron submitted to different nitriding processes for the catalytic activity for the oxygen reduction reaction (ORR) in acid and alkaline electrolytes. The catalysts were divided into three distinct series, the first one comprising those with different tungsten carbide loads with respect to the carbon support, which were impregnated with the Fe2+ (2,4,6-Tris (2-pyridyl) - 1,3,5-triazine)2, [Fe (TPTZ)]2+, complex and treated at two different temperatures, 700 and 800 oC in nitrogen atmosphere. In the second series, the tungsten carbide load (30% W/C, m/m) was kept constant but this mixture was prepared using previously doped carbons using three different sources of nitrogen (HNO3, NH3 and HNO3/NH3); this was followed by the incorporation of the Fe[TPTZ]2+ complex and by the same heat treatments as mentioned above. In the third series, the electrocatalysts were prepared with three carbon types (Vulcan, Ketjenblack and Monarch), to which the Fe[TPTZ]2+ complex was added, followed by heat treatment at 800 °C under nitrogen and then by nitriding using a flow of ammonia at 950 °C. The three series of electrocatalysts synthesized in this work were carefully characterized by infra-red and UV-Visible spectroscopy, x-ray diffraction, transmission electron microscopy, x-ray energy dispersive, Raman spectroscopy, x-ray photoelectron spectroscopy. The electrochemical investigations were performed by cyclic voltammetry (CV) and by measurements of steady-state polarization curves for ORR using rotating ring-disc electrode technique, with catalytic materials forming thin films deposited on the disc. In the three catalyst series, materials with good performance for the ORR were developed. In the studies of the first series of catalysts, it was seen that the most active material was that formed by WC-FeNx/C with 30%W/C and 5% Fe pyrolyzed at 800 ° C. In the second series it was observed that the performances of the catalysts varied according to the type of nitriding protocol, presence of iron and temperature of heat treatment. The electrocatalysts showed higher performances in alkaline electrolyte, which were very close to that of a reference Pt/C catalyst. In the third series of electrocatalysts, the best performance was obtained with the Monarch carbon catalyst heat-treated with ammonia, whose catalytic activity was higher than all others, due to the greater number of FeNx and N/C active structures formed by the treatment with ammonia. The results in acidic and alkaline conditions for the first and second series of electrocatalysts suggest the occurrence of an indirect ORR mechanism (2e- + 2e-), that is, in acid (alkaline) media first O2 is reduced to H2O2 (HO2) followed by the reduction of H2O2 (HO2). The active sites predominantly involved in the reaction electrocatalysis are WC and FeNx in acid media and WC e N/C in alcaline media. Finally, for the third series of electrocatalysts, the acidic reaction involves a direct 4e- mechanism, having important participation of the Fe-N2 active sites.