La thèse présentée traite principalement de l'influence de la composition et de l’état de surface d’électrodes à base de Ni sur la cinétique et le mécanisme des réactions d'oxydation/dégagement de l'hydrogène (HOR/HER) en milieu alcalin. En combinant les résultats de mesures électrochimiques avec une modélisation microcinétique, il a pu être montré que l'activité spécifique du Ni pour l’HOR/HER augmente jusqu'à 10 fois en présence à la fois d’oxydes de Ni et de Ni métallique à la surface de l'électrode. En outre, l'influence de l'addition d’un second métal aux électrocatalyseurs à base Ni sur leurs activités pour l’HOR/HER a été étudiée dans le cas des systèmes NiMo/C et NiCu/C. Dans les deux cas, une augmentation de l'activité spécifique a été observée par rapport à l'échantillon Ni/C de référence et a été attribuée à une diminution de l'énergie d'adsorption de l'hydrogène adsorbé sur Ni, espèce intermédiaire de l’HOR/HER. / The present thesis is mainly focused on the influence of the surface state of Ni electrodes on the kinetics and the mechanism of the hydrogen oxidation/evolution reactions (HOR/HER) in alkaline medium. By combining the results of electrochemical measurements with microkinetic modeling, it was shown that specific activity of Ni in the HOR/HER increases up to 10 times if along with metallic Ni, Ni oxide species are present on the electrode surface. In addition, the effect of the addition of a second metal to Ni electrocatalysts on their activity in the HOR/HER was investigated for NiMo/C and NiCu/C systems. In both cases an enhancement of specific activity was observed in comparison with the reference Ni/C sample, which was assigned to a decrease of the adsorption energy of the hydrogen intermediate on Ni participating in the HOR/HER.

A goal of the Swedish government is to increase the usage of renewable fuels and biomass-based fuels. Fuel cells, and especially the MCFC, are useful for these types of fuels. The Swedish market may benefit from the MCFC in two ways: increased efficiency of the biofuels and also utilisation of produced heat in district heating. Most of the commercial MCFC systems today are optimised for use with methane. The possibility to utilise biomass in Sweden makes it important to study how the MCFC may be adapted or optimised for good performance and low degradation with gas produced from biomass or other renewable fuels. This thesis is focused on methods that may be used to investigate and evaluate MCFC electrodes and electrolytes with renewable fuels i.e. CO2-containing gases. The methods and results are both experimental and mathematically modelled. The objectives of this thesis are to better understand how the performance of the anode is dependent on different fuels. Anode kinetics and the water-gas shift reaction have been investigated as well as the possibility to increase cell lifetime by increasing the initial electrolyte amount by having the anode as a reservoir. The effect of segregation of cations in the electrolyte during operation has also been studied. It was found that if the gas composition at the current collector inlet is in equilibrium according to the water gas-shift reaction the gas composition inside the electrode is almost uniform. However, if the gas is not in equilibrium then the concentration gradients inside the current collector have a large effect on the gas composition inside the electrode. The conversion of the gas in the gas flow channels according to the water-gas shift reaction depends on the gas flow rate. For an anode used in a gas mixture of humidified hydrogen and carbon dioxide that are not in equilibrium some solubility of Ni in a (Li/Na)2CO3 mixture was found. To have the anode act as an electrolyte reservoir to prolong cell lifetime the anode pore size should be carefully matched with that of the cathode and a bimodal pore-size distribution for the anode is preferable to have as good performance as possible for as large electrolyte filling degree interval as possible. Modelling results of segregation of cations in the electrolyte during operation indicate that the electrolyte composition changes during operation and that the lithium ions are enriched at the anode for both types of electrolyte used for the MCFC. The electrolyte composition changes are small but might have to be considered in long-time operation. The results from this thesis may be used to better understand how the MCFC may be used for operation with renewable fuels and how electrodes may be designed to prolong cell lifetime. / Ett av den svenska regeringens mål är att öka användandet av förnyelsebara bränslen och bränslen från biomassa. Bränsleceller och framförallt MCFC är användbara för dessa typer av bränslen. Den svenska marknaden kan dra fördelar av MCFC på två sätt; ökad bränsleutnyttjandegrad och utnyttjande av producerad värme för fjärrvärme. De flesta kommersiella MCFC-systemen idag är optimerade för användning av metan. Möjligheten att använda biomassa på den svenska marknaden gör det viktigt att studera hur MCFC kan anpassas eller optimeras för bra prestanda och låg degradering för användning med gas från biomassa eller andra förnyelsebara bränslen. Fokus i denna avhandling är på metoder som kan användas för att undersöka och utvärdera MCFC-elektroder och -elektrolyter med förnyelsebara bränslen, dvs. gaser innehållande CO2. Metoderna och resultaten är både experimentella och matematiskt modellerade. Målet med denna avhandling är att bättre förstå hur anodens prestanda beror på användningen av olika bränslen. Anodens kinetik och vattengasskiftreaktionen har studerats liksom möjligheten att förlänga cellens livstid genom att öka den initiala mängden elektrolyt medelst användning av anoden som reservoar. Effekten av segregation av katjoner i elektrolyten under last har också undersökts. Om gassammansättningen är i jämvikt enligt vattengasskiftreaktionen vid inloppet till strömtilledaren kommer gassammansättningen att vara nära uniform inuti elektroden. Om ingående gas inte är i jämvikt kommer stora koncentrationsgradienter uppkomma i strömtilledaren och påverka gassammansättningen i elektroden. Omsättningen med avseende på vattenskiftreaktionen av gasen i flödeskanalen verkar vara beroende av gasens flödeshastighet. För en anod som används i en uppfuktad blandning av vätgas och koldioxid som inte är i jämvikt befanns det att Ni har en viss löslighet i (Li/Na)2CO3. För att kunna använda anoden som reservoar för elektrolyt för att förlänga livstiden för MCFC skall anodens porstorleksfördelning överensstämma med katodens och ha en bimodal porstorleksfördelning för att ge en tillräckligt god prestanda i ett så stort elektrolytfyllnadsgradsintervall som möjligt. Modelleringsresultat för segregering av katjoner i elektrolyten under drift visar att litiumjoner anrikas i anoden för båda typerna av elektrolyt som används i MCFC. Elektrolytkoncentrationsförändringarna är små men kan behövas tas i beaktande vid långa driftstider. Denna avhandlings resultat kan användas för att bättre förstå hur MCFC skall anpassas för drift med förnyelsebara bränslen och hur elektroder kan utformas för att förlänga livstiden. / QC 20100630

Kyoto University (京都大学) / 0048 / 新制・課程博士 / 博士(工学) / 甲第17555号 / 工博第3714号 / 新制||工||1566(附属図書館) / 30321 / 京都大学大学院工学研究科機械理工学専攻 / (主査)教授 中部 主敬, 教授 牧野 俊郎, 教授 小森 悟 / 学位規則第4条第1項該当

La pile à combustible directe à borohydrures (DBFC en anglais), qui est une sous-catégorie des piles à combustible alcalines, bénéficie des avantages de son combustible, le borohydrure de sodium (NaBH4), qui confère à ce système des caractéristiques thermodynamiques et énergétiques très intéressantes. Cependant, la réaction d’électrooxydation de NaBH4 (BOR en anglais) est très complexe et reste à ce jour encore peu étudiée et mal comprise sur la majorité des électrocatalyseurs (la plupart étant sous forme de nanoparticules métalliques supportées sur des noirs de carbone). De plus, de récentes études ont montré l’agressivité du milieu alcalin sur la durabilité des électrocatalyseurs conventionnels, révélant une grande perte de surface catalytique active, due principalement à un détachement des nanoparticules du support carboné. Dans ce contexte, ces travaux de thèse se sont orientés vers trois axes d’étude : (i) l’étude de la BOR sur des électrocatalyseurs à base de palladium dans des conditions proches des conditions réelles de fonctionnement de la DBFC ; (ii) l’étude de l’impact de la structure de l’anode sur les performances globales de la DBFC, et (iii) l’étude du mécanisme de dégradation d’électrocatalyseurs à base de métaux nobles dans un environnement alcalin. Les expérimentations ont été réalisées en étroite collaboration avec le U.S. Naval Research Laboratory (Washington, USA).Les résultats obtenus ont montré qu’une grande concentration en NaBH4 entraine un ralentissement de la cinétique de la réaction, due en partie à un fort empoisonnement de la surface catalytique. Par ailleurs, des marqueurs d’activité pour la BOR ont été proposés. Ensuite, l’utilisation d’électrodes à gradient de catalyseurs s’est avérée être une solution prometteuse pour mieux valoriser l’hydrogène produit via des réactions secondaires à la BOR. Enfin, l’utilisation de la spectroscopie infrarouge à transformée de Fourier couplée à de la microscopie électronique en transmission à localisation identique a permis de détecter la formation de carbonates au cours d’un test de vieillissement accéléré d’électrocatalyseurs à base de métaux nobles en milieu alcalin. Ce mécanisme explique, en partie, le détachement des nanoparticules observé au cours du test. / The direct borohydride fuel cell (DBFC), a subclass of alkaline fuel cells, benefits from the advantages of its fuel, sodium borohydride (NaBH4), which exhibits very interesting thermodynamic and energetic characteristics. However, the NaBH4 electrooxidation reaction (BOR) is very complex; to date it remains poorly studied and understood on many electrocatalysts (most of them are in the form of metal nanoparticles supported on carbon black). In addition, recent studies reported the aggressiveness of the alkaline medium on the durability of conventional carbon-supported electrocatalysts, revealing a large loss of the active catalytic surface, mainly due to the detachment of nanoparticles from the carbon support. In this context, this thesis focused on three main areas of study: (i) the study of the BOR on palladium-based electrocatalysts in conditions close to the real operating conditions of the DBFC; (ii) the study of the impact of the anode structure on the overall performance of the DBFC, and (iii) the study of the degradation mechanism of noble metal electrocatalysts in alkaline environment. The experiments were carried out in close collaboration with the U.S. Naval Research Laboratory (Washington, USA).The results obtained showed that a high concentration of NaBH4 leads to a decrease of the reaction kinetics, due in part to poisoning of the catalytic surface. In addition, activity markers for the BOR have been proposed. Then, the use of catalysts-gradient electrodes proved to be a promising solution to better valorize the hydrogen produced via side reactions of the BOR. Finally, the use of Fourier transform infrared spectroscopy coupled with identical-location transmission electron microscopy enabled to detect the formation of carbonates during the accelerated stress test of carbon-supported noble metal electrocatalysts in alkaline medium, explaining, in part, the detachment of nanoparticles observed during the test.

The pressure on clean and sustainable energy supplies is increasing. In this regard energy conversion by electrochemical processes plays a major role, for both fuel cell reactions and electrolysis reactions. The sulphur dioxide oxidation reaction (SOR) is a common reaction found in the Hybrid Sulphur Cycle (HyS) and the HyS is a way to produce large-scale hydrogen (H2). The problem with the use of the HyS and fuel cells is the cost involved as large amounts of Pt are required for effective operation. The aim of the study was to determine whether there was an alternative catalyst which was more efficient and cost-effective than Pt. The oxygen reduction reaction (ORR), the ethanol oxidation reaction (EOR) and SOR were studied by means of different electrochemical techniques (cyclovoltammetry (CV), linear polarization (LP) and rotating disk electrode (RDE)) on polycrystalline platinum (Pt) and palladium (Pd). The SRR and EOR are common reactions occurring at the cathode and anode, respectively, in fuel cells and these reactions have been investigated extensively. The reason for studying the reactions was as a preparation for the SOR. This study compared polycrystalline Pt and Pd for the different reactions, with the main focus on the SOR as Pd is considerably cheaper than Pt, and for the SOR polycrystalline Pd has by no means been investigated intensively. Polycrystalline Pt and Pd were compared by different electrochemical techniques and analyses. The Koutecky-Levich and Levich analyses were used to (i) calculate the number of e- involved in the relevant reaction, (ii) to determine whether the reaction was mass transfer controlled at high overpotentials and (iii) whether the reaction mechanism changed with potential. Next the kinetic current density ( k) was calculated from Koutecky-Levich analyses, which was further used for Tafel slope analyses. If it was not possible to carry out the analyses, the activation energy (Ea) was used to determine the electrocatalytic activity of the catalyst. The electrocatalytic activity was also determined by comparing onset potentials (Es), peak potentials (Ep) and limited/maximum current density ( b/ p) of each catalyst. This study was only a preliminary study for the SOR and therefore, further studies are certainly required. It seemed Pd shows better electrocatalytic activity than Pt for the SRR in an alkaline electrolyte because of similar Es, but Pd produced a higher cathodic current density. Pt showed a lower Es than Pd for the SRR in an acid electrolyte, but Pd delivered a higher cathodic current density. This, therefore, means that the SRR in an acid electrolyte is kinetically more favourable on Pd than on Pt. For the EOR better electrocatalytic activity was obtained with Pd than with Pt in an alkaline electrolyte due to higher current densities at lower potentials and Pd showed lower Ea values than Pt in the potential range normally used for fuel cells. Pd was inactive for EOR in an acid electrolyte, while a reaction occurred on Pt. A possible reason for this observation may be due to the H2 absorbing strongly on Pd thus blocking the active positions on the electrode surfaces, preventing further reaction. Pd showed higher electrocatalytic activity for the SOR due to lower Es and higher current densities at low potentials. From the RDE studies it was established that the SRR in an alkaline electrolyte on polycrystalline Pt and Pd was mass transfer controlled at low potentials (high overpotentials), but the SRR in an acid electrolyte was only mass transfer controlled on Pt. The SOR was not mass transfer controlled on polycrystalline Pt and Pd at high potentials (high overpotentials). These assumptions were confirmed by Levich analysis. Using Koutecky-Levich analysis, it was determined that the reaction mechanism on polycrystalline Pt and Pd changed with potential for SRR in an alkaline electrolyte and the SOR. For the SRR in an acid electrolyte the reaction mechanism remained constant with changes in potential on polycrystalline Pd, but the reaction mechanism on polycrystalline Pt changed with potential. These assumptions were confirmed by the number of e-, calculated using Koutecky-Levich analyses. Levich and Koutecky-Levich analyses were not performed for EOR as an increase in rotation speed did not produce an increase in current density. Tafel slope analyses were conducted by making use of overpotentials and k, where possible. As in the case of ethanol, it was not possible to execute Koutecky-Levich analyses and, therefore, it was not possible to perform Tafel slope analyses using k. Tafel slope analyses for the EOR was therefore performed with normal current densities at 0 rotations per minute (rpm). The reaction mechanisms on Pt and Pd for the SRR in alkaline and acidic electrolytes differed due to different Tafel slopes. Pt and Pd displayed similar Tafel slopes for the EOR in alkaline electrolyte, thus suggesting that the reaction mechanisms on Pt and Pd were the same. For the SOR it seemed that the reaction mechanism on Pt and Pd were similar because of similar Tafel slopes. This was only a preliminary and comparative study for polycrystalline Pt and Pd, and the reaction mechanism was not further studied by means of spectroscopic techniques. / MSc (Chemistry), North-West University, Potchefstroom Campus, 2014

The pressure on clean and sustainable energy supplies is increasing. In this regard energy conversion by electrochemical processes plays a major role, for both fuel cell reactions and electrolysis reactions. The sulphur dioxide oxidation reaction (SOR) is a common reaction found in the Hybrid Sulphur Cycle (HyS) and the HyS is a way to produce large-scale hydrogen (H2). The problem with the use of the HyS and fuel cells is the cost involved as large amounts of Pt are required for effective operation. The aim of the study was to determine whether there was an alternative catalyst which was more efficient and cost-effective than Pt. The oxygen reduction reaction (ORR), the ethanol oxidation reaction (EOR) and SOR were studied by means of different electrochemical techniques (cyclovoltammetry (CV), linear polarization (LP) and rotating disk electrode (RDE)) on polycrystalline platinum (Pt) and palladium (Pd). The SRR and EOR are common reactions occurring at the cathode and anode, respectively, in fuel cells and these reactions have been investigated extensively. The reason for studying the reactions was as a preparation for the SOR. This study compared polycrystalline Pt and Pd for the different reactions, with the main focus on the SOR as Pd is considerably cheaper than Pt, and for the SOR polycrystalline Pd has by no means been investigated intensively. Polycrystalline Pt and Pd were compared by different electrochemical techniques and analyses. The Koutecky-Levich and Levich analyses were used to (i) calculate the number of e- involved in the relevant reaction, (ii) to determine whether the reaction was mass transfer controlled at high overpotentials and (iii) whether the reaction mechanism changed with potential. Next the kinetic current density ( k) was calculated from Koutecky-Levich analyses, which was further used for Tafel slope analyses. If it was not possible to carry out the analyses, the activation energy (Ea) was used to determine the electrocatalytic activity of the catalyst. The electrocatalytic activity was also determined by comparing onset potentials (Es), peak potentials (Ep) and limited/maximum current density ( b/ p) of each catalyst. This study was only a preliminary study for the SOR and therefore, further studies are certainly required. It seemed Pd shows better electrocatalytic activity than Pt for the SRR in an alkaline electrolyte because of similar Es, but Pd produced a higher cathodic current density. Pt showed a lower Es than Pd for the SRR in an acid electrolyte, but Pd delivered a higher cathodic current density. This, therefore, means that the SRR in an acid electrolyte is kinetically more favourable on Pd than on Pt. For the EOR better electrocatalytic activity was obtained with Pd than with Pt in an alkaline electrolyte due to higher current densities at lower potentials and Pd showed lower Ea values than Pt in the potential range normally used for fuel cells. Pd was inactive for EOR in an acid electrolyte, while a reaction occurred on Pt. A possible reason for this observation may be due to the H2 absorbing strongly on Pd thus blocking the active positions on the electrode surfaces, preventing further reaction. Pd showed higher electrocatalytic activity for the SOR due to lower Es and higher current densities at low potentials. From the RDE studies it was established that the SRR in an alkaline electrolyte on polycrystalline Pt and Pd was mass transfer controlled at low potentials (high overpotentials), but the SRR in an acid electrolyte was only mass transfer controlled on Pt. The SOR was not mass transfer controlled on polycrystalline Pt and Pd at high potentials (high overpotentials). These assumptions were confirmed by Levich analysis. Using Koutecky-Levich analysis, it was determined that the reaction mechanism on polycrystalline Pt and Pd changed with potential for SRR in an alkaline electrolyte and the SOR. For the SRR in an acid electrolyte the reaction mechanism remained constant with changes in potential on polycrystalline Pd, but the reaction mechanism on polycrystalline Pt changed with potential. These assumptions were confirmed by the number of e-, calculated using Koutecky-Levich analyses. Levich and Koutecky-Levich analyses were not performed for EOR as an increase in rotation speed did not produce an increase in current density. Tafel slope analyses were conducted by making use of overpotentials and k, where possible. As in the case of ethanol, it was not possible to execute Koutecky-Levich analyses and, therefore, it was not possible to perform Tafel slope analyses using k. Tafel slope analyses for the EOR was therefore performed with normal current densities at 0 rotations per minute (rpm). The reaction mechanisms on Pt and Pd for the SRR in alkaline and acidic electrolytes differed due to different Tafel slopes. Pt and Pd displayed similar Tafel slopes for the EOR in alkaline electrolyte, thus suggesting that the reaction mechanisms on Pt and Pd were the same. For the SOR it seemed that the reaction mechanism on Pt and Pd were similar because of similar Tafel slopes. This was only a preliminary and comparative study for polycrystalline Pt and Pd, and the reaction mechanism was not further studied by means of spectroscopic techniques. / MSc (Chemistry), North-West University, Potchefstroom Campus, 2014

Στην παρούσα διατριβή μελετήθηκε η μοριακή δομή και καταλυτική ενεργότητα καταλυτών V2O5/TiO2 και CrOx/TiO2 για την αντίδραση καταλυτικής αναγωγής των NO με χρήση NH3 (αντίδραση SCR) καθώς και καταλυτών V2O5-Cs2SO4/SiO2 (καταλύτες υγρής υποστηριγμένης φάσης) για την αντίδραση οξείδωσης του διοξειδίου του θείου. Η μελέτη της μοριακής δομής έγινε με χρήση in-situ φασματοσκοπία Raman υπό διάφορες αέριες συνθήκες (O2, NH3/N2, NH3/NO/N2, NH3/NO/O2/N2, 8% H2O/O2/N2, SO2/N2, SO2/O2/N2) και θερμοκρασίες. Γενικά σε χαμηλές φορτίσεις, σχηματίζονται αρχικά απομονωμένα τετραεδρικά βαναδικά (ή χρωμικά) είδη και αυξανόμενης της φόρτισης οδηγούμαστε στο σχηματισμό διμερών/ ολιμερών αλυσίδων. Η in-situ φασματοσκοπία ESR έδωσε συμπληρωματικές πληροφορίες για την μοριακή δομή των V4+, Cr5+ & Cr3+ ειδών, σε οξειδωτικές και αναγωγικές συνθήκες. Τέλος, η μελέτη της συμπεριφοράς της συχνότητας αναστροφής (TOF) στους καταλύτες βαναδίου έδειξε ότι η αντίδραση επιταχύνεται κατά την παρουσία γειτονικών κέντρων βαναδίου. Οι καταλύτες βαναδίου / καισίου είναι οι μοναδικοί στο είδος τους καταλύτες υποστηριγμένης υγρής φάσης, όπου σε συνθήκες αντίδρασης, η ενεργός φάση βρίσκεται υγρή ή διαλυμένη σε ένα μη πτητικό διάλυμα που “φιλοξενείται” στους πόρους του υποστρώματος. Η in-situ μελέτη Raman έδειξε ότι το ενεργό είδος για την καταλυτική οξείδωση του SO2 είναι τα βαναδικά οξοθειϊκά σύμπλοκα (VO)2O(SO4)44-. / In this ph.d. thesis, the molecular structure and catalytic reactivity of V2O5/TiO2 and CrOx/TiO2 catalysts was studied for the SCR reaction. Furthermore, the molecular structure of the unique SLP catalysts V2O5-Cs2SO4/SiO2 was studied for the reaction of the oxidation of SO2. This study was performed by the use of in-situ Raman spectroscopy in various “real” gas conditions (O2, NH3/N2, NH3/NO/N2, NH3/NO/O2/N2, 8% H2O/O2/N2, SO2/N2, SO2/O2/N2) and temperatures. In general, at low loadings isolated species are formed, and as the loading is increased, the formation of dimeric / oligomeric species is favoured. In situ ESR spectroscopy gave supplementary information about the structure of V4+, Cr5+ & Cr3+ species in oxidative / reductive environment. The behaviour of TOF numbers showed that the reaction is accelerated in the presence of neighbour vanadium centers (in case of vanadium catalysts). Finally, the vanadium / caesium catalysts are the unique in their kind molten salt catalysts, were in reaction conditions, the active phase is in liquid form or dissolved in a non-volatile solution which is “hosted” inside the pores of the support. Activation of these catalysts, following exposure to a SO2/O2/N2 mixture, results in uptake of SO3 and formation of a pyrosulfate molten salt which – as shown by in-situ Raman spectroscopy – vanadium occurs predominantly in the form if binuclear (VO)2O(SO4)44- which are considered to be the active species for the reaction.

This work reports on the cobalt pyridinoporphyrazinate (CoTmtppa) as a platinum-group metal-free catalyst for hydrogen evolution and oxidation reactions with the possibility of use in hydrogen energy and hydrogen potentiometric sensing. A different interaction of CoTmtppa with various electrode substrates, highly oriented pyrolytic graphite (HOPG) and annealed gold (Au(111)), affects its electrocatalytic behaviour in hydrogen reactions. The formation of a hydride-type complex with the bonding of hydrogen atoms to cobalt centre is supposed to be the rate-determining step. In the case of hydrogen evolution, the maximum catalytic activity of mediator was reached at pH = 11,0, when the HOPG/CoTmtppa showed overpotential decrease by 300 mV and an almost 60-fold increase of current densities compared to HOPG. The electrocatalytic activity of Au(111)/CoTmtppa resulted in a further decrease of overpotential by 175 mV in comparison with HOPG/Co(I)Tmtppa. The electrochemical oxidation of hydrogen was found to depend on hydrogen source which was electrochemically generated on-site or molecular hydrogen supplied from an external source. In the case of electrochemically generated hydrogen, the maximum activity of HOPG/CoTmtppa was reached at pH = 2.1 and an additional it was observed 50 % increase in current...

En la presente tesis doctoral se realiza un estudio detallado sobre el mecanismo de la reacción de reducción de oxígeno (ORR) en electrodos monocristalinos de platino. Para ello, se han realizado medidas electroquímicas usando la configuración de electrodo rotatorio de menisco colgante (HMRDE) con superficies con distinta estructura superficial y variando condiciones de la disolución de trabajo como el pH, fuerza iónica o la ausencia o presencia de bromuros. La conclusión principal que se extra de estos experimentos es la posibilidad de la existencia de un punto de bifurcación en el mecanismo, implicando el intermedio OOH, antes de la formación de peróxido de hidrógeno. Además, también se estudia la ORR y la reacción de oxidación de ácido fórmico en electrodos monocristalinos de Pt en presencia de acetonitrilo, como estudio previo al estudio de estas reacciones en disolventes orgánicos con pequeñas cantidades de agua. Por último, se estudia la ORR en un Aza-CMP, lo cual permite obtener información fundamental que se puede aplicar en estudios sobre el mecanismo de la ORR en los sitios activos de materiales de carbón funcionalizados con nitrógeno.

Au cours des dernières années, le développement des batteries Li-ion a révolutionné nos modes de vie. Compte tenu de la croissance exponentielle en batteries, le besoin se répercute sur les matériaux de base, qui sont entre autres, synthétisés à partir de sels de lithium de haute pureté. Nemaska Lithium, une entreprise partenaire du projet, est reconnue en tant que nouveau producteur d’hydroxyde de lithium, par l’entremise d’un procédé électromembranaire breveté. Comparativement au procédé conventionnel, la solution mise en place est l’une des méthodes la plus économique et écologique à l’échelle mondiale. Dans le but de diminuer encore plus les coûts énergétiques du procédé, l’usage d’une anode dépolarisée à l’hydrogène ((ADH); H2(g) ⇄ 2H+(aq) +2é; E=0,00 V) est considérée. Cette approche demande une certaine compréhension et optimisation de l’électrode à des fins d’adaptation pour l’électrolyse. Ainsi, ce travail tant fondamental qu’appliqué a été réalisé afin d’étudier les phénomènes se produisant à l’ADH. Dans un premier temps, une étude portée sur la cinétique de réaction de l’oxydation de l’hydrogène à l’aide d’une électrode à disque tournant est réalisée. L’influence d’ions lithium et d’une couche catalytique composite sur l’efficacité de la réaction a ainsi pu être démontrée. L’identification des limitations du système a ensuite permis l’optimisation de l’ADH à l’aide d’un plan d’expérience. L’ADH est composée d’un ionomère, d’un catalyseur et d’un support à catalyseur, qui ont des propriétés intrinsèques ayant un impact direct sur l’efficacité et la durabilité de celle-ci. Conséquemment, pour une étude de performance et d’optimisation, plusieurs configurations d’assemblage d’électrode à membrane (MEA) ont été considérées visant à faire varier les proportions des différentes composantes avec un plan d’expérience. Ce projet a ainsi permis l’étude menant à une meilleure compréhension d’une nouvelle technologie d’électrolyse membranaire. / In recent years, the development of Li-ion batteries has revolutionized our lifestyles. Given the exponential demand for batteries, the requirement is for base materials, which are synthesized from high-purity lithium salts. Nemaska Lithium, a partner in the project, is recognized as a new producer of lithium hydroxide, using a patented electromembrane process. Compared to the conventional process, this solution is one of the most economical and environmentally friendly methods worldwide. In order to further reduce the energy costs of the process, the use of a hydrogen depolarized anode ((HDA); H2(g) ⇄ 2H+(aq) +2é; E0=0,00 V) is considered. This approach requires some understanding and optimization of the electrode for electrolysis adaptations. Thus, this fundamental and applied work was conducted to study the phenomena occurring at the HDA. First, a study on the kinetics of the hydrogen oxidation reaction using a rotating disk electrode is performed. The influence of lithium ions and a composite catalytic layer on the efficiency of the reaction was demonstrated. The identification of system limitations allowed the optimization of the DHA using a design of experiment. The components of a HDA have intrinsic properties which have a direct impact on its efficiency and durability. They consist of an ionomer, a catalyst, and a catalyst support. Consequently, for a performance and optimization study, several membrane electrode assembly (MEA) configurations were considered in order to vary the proportions of the different components with a design of experiment. This study provided a better understanding and development of this new membrane electrolysis technology.