Polymer electrolyte membrane (PEM) fuel cells have increasingly become promising green energy sources for automobile and stationary cogeneration applications but its success in commercialization depends on performance optimization and manufacturing cost. The activation losses, expensive platinum catalyst, and water flooding phenomenon are the key factors currently hindering commercialization of PEM fuel cells. These factors are associated with the cathode catalyst layer (CCL), which is about ten micrometers thick. Given the small scale of this layer, it is extremely difficult to study transport phenomena inside the catalyst layer experimentally, either intrusively or non-intrusively. Therefore, mathematical and numerical models become the only means to provide insight on the physical phenomena occurring inside the CCL and to optimize the CCL designs before building a prototype for engineering application. In this thesis research, a comprehensive two-phase mathematical model for the CCL has been derived from the fundamental conservation equations using a volume-averaging method. The model also considers several water transport and physical processes that are involved in the CCL. The processes are: (a) electro-osmotic transport from the membrane to the CCL, (b) back-diffusion of water from the CCL to the membrane, (c) condensation and evaporation of water, and (d) removal of liquid water to the gas flow channel through the gas diffusion layer (GDL). A simple analytical model for the activation overpotential in the CCL has also been developed and an optimization study has been carried out using the analytical activation overpotential formulation. Further, the mathematical model has been simplified for the CCL and an analytical approach has been provided for the liquid water transport in the catalyst layer. The volume-averaged mathematical model of the CCL is finally implemented numerically along with an investigation how the physical structure of a catalyst layer affects fuel cell performance. Since the numerical model requires various effective transport properties, a set of mathematical expressions has been developed for estimating the effective transport properties in the CCL and GDL of a PEM fuel cell. The two-dimensional (2D) numerical model has been compared with the analytical model to validate the numerical results. Subsequently, using this validated model, 2D numerical studies have been carried out to investigate the effect of various physical and wetting properties of CCL and GDL on the performance of a PEM fuel cell. It has been observed that the wetting properties of a CCL control the flooding behavior, and hydrophilic characteristics of the CCL play a significant role on the cell performance. To investigate the effect of concentration variation in the flow channel, a three-dimensional numerical simulation is also presented.

Polymer electrolyte membrane (PEM) fuel cells have increasingly become promising green energy sources for automobile and stationary cogeneration applications but its success in commercialization depends on performance optimization and manufacturing cost. The activation losses, expensive platinum catalyst, and water flooding phenomenon are the key factors currently hindering commercialization of PEM fuel cells. These factors are associated with the cathode catalyst layer (CCL), which is about ten micrometers thick. Given the small scale of this layer, it is extremely difficult to study transport phenomena inside the catalyst layer experimentally, either intrusively or non-intrusively. Therefore, mathematical and numerical models become the only means to provide insight on the physical phenomena occurring inside the CCL and to optimize the CCL designs before building a prototype for engineering application. In this thesis research, a comprehensive two-phase mathematical model for the CCL has been derived from the fundamental conservation equations using a volume-averaging method. The model also considers several water transport and physical processes that are involved in the CCL. The processes are: (a) electro-osmotic transport from the membrane to the CCL, (b) back-diffusion of water from the CCL to the membrane, (c) condensation and evaporation of water, and (d) removal of liquid water to the gas flow channel through the gas diffusion layer (GDL). A simple analytical model for the activation overpotential in the CCL has also been developed and an optimization study has been carried out using the analytical activation overpotential formulation. Further, the mathematical model has been simplified for the CCL and an analytical approach has been provided for the liquid water transport in the catalyst layer. The volume-averaged mathematical model of the CCL is finally implemented numerically along with an investigation how the physical structure of a catalyst layer affects fuel cell performance. Since the numerical model requires various effective transport properties, a set of mathematical expressions has been developed for estimating the effective transport properties in the CCL and GDL of a PEM fuel cell. The two-dimensional (2D) numerical model has been compared with the analytical model to validate the numerical results. Subsequently, using this validated model, 2D numerical studies have been carried out to investigate the effect of various physical and wetting properties of CCL and GDL on the performance of a PEM fuel cell. It has been observed that the wetting properties of a CCL control the flooding behavior, and hydrophilic characteristics of the CCL play a significant role on the cell performance. To investigate the effect of concentration variation in the flow channel, a three-dimensional numerical simulation is also presented.

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Philosophiae Doctor - PhD / Ammonia has attracted attention as a possible fuel for direct fuel cells since it is easy to handle under low pressure, costs only slightly higher than methanol and can easily be cracked down into hydrogen and nitrogen. At low temperature, ammonia oxidation on noble metal electrodes is a sluggish reaction and efficient catalysts are required to convert ammonia to nitrogen and hydrogen at reasonable reaction rates. In this thesis, I present polycrystalline and oriented nanoalloys synthesised at room temperature in aqueous media and their catalytic effects on the oxidation of ammonia. The electro-oxidation of ammonia on palladium-goldsilver (PdAuAgNPs) ternary nanoalloys was systematically studied in alkaline solution of potassium hydroxide (KOH) by cyclic voltammetry (CV). The PdAuAg nanoalloys were prepared through a facile synthesis with ascorbic acid as a reductant and polyvinylpyrrolidone (PVP) as a stabilising agent from aqueous solutions of PdCh/HAuCI4.3H20/AgN03 mixtures. UV-visible spectroscopy was used to confirm the complete reduction of the metal ions; absorption peaks observed at 260 nm, 285 nm and 420 nm for Ag", Au3+ and Pd2+ ions respectively, disappeared after reduction indicating a complete reduction of the metal ions to zero-valent nanoparticles. High resolution transmission electron microscopy (HR TEM) revealed the formation of crystalline nonaggregated 25-35 nm sized nanoalloys. The elemental composition of the nanoalloys measured using energy dispersive X-ray spectroscopy (EDX) showed the presence of the three elements; Pd, Au and Ag. The well-dispersed non-agglomerated PdAuAg nanoalloys exhibited a reduced overpotential and a 33%, 400%,82% and 54% increase in current density for ammonia electro-oxidation compared to Pd, PdAg, PdAu nanoparticles and bare Pt electrode, respectively. The much improved current density of the well-dispersed PdAuAg nanoalloys is attributed to the increased electrochemically active surface area of the nanoalloys. This electro catalytic behaviour of the PdAuAg nanoalloys for ammonia oxidation in KOH solutions provides a promising route for development of low-cost and high performance electro catalyst for electro-oxidation of ammoniaMoreover, ammonia oxidation on platinum surfaces has been found to be a very structure sensitive reaction which takes place almost exclusively on Pt(100) surfaces. I report for the first time the preparation of sodium polyacrylate-capped Pt(100)Pd, pte 1OO)Au, pte 1OO)Ir, Pt(IOO)Rh, Pt(100)PdAu, Pt(100)IrAu, Pt(IOO)PdIr and Pt(IOO)RhAu nanoalloys. The reduction of the metal ions to nanoparticles was confirmed by UV-visible spectroscopy while the shapes and the structures of the nanoparticles were studied using HRTEM and CV. HRTEM analysis showed well distributed non-agglomerated 5-20 nm semi-spherical and cubic nanoalloys with lattice fridges on their surfaces indicating the crystalline nature of the nanoalloys. Pt(100) nanoalloy systems showed particles with triangular and cubic shapes. The existence of the preferentially cubic shaped nanoparticles in the samples indicated that the nanoalloys had some (100) sites orientation/a significant amount of (100) sites at their surfaces. The CV of the nanoparticles in the hydrogen adsorption/desorption region (-200 mV to 100 mV vs. Ag! AgCl) was used to obtain qualitative information about the surface structure of the nanoparticles. The voltammogram of oriented Pt(100) nanoparticles showed very clearly the presence of adsorption states associated with (110) sites, (100) domains and (l00) sites at -131 mV, -34 mV and 29 mV, respectively. The companson of this voltammetric profile with that obtained for a Pt(100) single crystal electrode clearly points out that the synthesised Pt nanoparticles have a high density of (100) sites. However, the peak that was observed at 29 mV in the CV of Pt(100) nanoparticles was not present in the vo ltammo grams of the Pt(100) nanoalloy systems confirming the formation of the nanoalloys. The results reported in this work demonstrate the importance of controlling the intrinsic structural properties of Pt nanoparticles; in terms of nature of the active sites and the effect of adding adatoms (such as Au, Pd, Rh, Ir) in order to understand their catalytic properties. The electrochemical activities of these nanoparticles for ammonia oxidation in basic medium showed an increase of over 100% current density compared to Pt electrode. Pt(lOO)RhAu nanoalloys showed the highest catalytic properties while Pt(lOO)PdAu had the lowest as shown in the trend: Pt(lOO)RhAu > Pt(lOO)PdIr > Pt(lOO) > Pt(lOO)IrAu > Pt(lOO)Pd> Pt(lOO)Rh > Pt(lOO)Au > Pt(lOO)Ir > Pt(lOO)PdAu. The synthesised oriented nanoalloys were further interrogated towards the oxidation of hydrazine as a fuel for hydrazine fuel cells. The oriented Pt(lOO) nanoparticles and Pt(lOO) nanoalloy systems exhibited over 1000% increase in current density and reduced oxidation overpotential compared to bare glassy carbon electrode. These excellent catalytic properties are attributed to the increased surface area and the presence of (100) sites which favour the oxidation of hydrazine.

The assessment of performance for PEM Fuel Cells (PEMFC) at the stack, Single Repeating Unit (SRU), and Membrane Electrode Assembly (MEA) level is dominated by the evaluation of polarization curves. However, polarization curves do not provide adequate detail as to the origin of the inefficiencies of the fuel cell performance and information on these sources of origin are critical to understand and address topics such as material selection, optimal operating conditions, and overall robust and reliable cell and stack design characteristics. To the purpose of understanding the origin of the inefficiencies underlying the fuel cell polarization curve a series of additional experimental and analysis techniques must be applied and from the resultant data the origin of the inefficiencies can then be assigned to kinetic, ohmic, and mass transport loss categorizations. Further, through a combination of the diagnostic methods further resolution can be implied down to the contribution of the individual components to the relative voltage loss categories. In this topic, a methodology will be presented and discussed that achieves and demonstrates this process.

Το ενδιαφέρον για την ανάπτυξη νέων καθοδικών ηλεκτροδίων για χρήση τους σε κυψέλες καυσίμου στερεού ηλεκτρολύτη (SOFCs) ενδιάμεσων θερμοκρασιών (600-800oC) γίνεται ολοένα και μεγαλύτερο, δεδομένου ότι η απόδοση των συμβατικών καθόδων La1-xSrxMnO3-δ δεν είναι ικανοποιητική σε θερμοκρασίες χαμηλότερες των 800oC. Περοβσκιτικά υλικά με γενικό τύπο La1-x-ySrxCozFe1-zO3-δ αποτελούν υποσχόμενη εναλλακτική λύση, εξαιτίας της υψηλής ηλεκτρονικής και ιοντικής τους αγωγιμότητας. Η μικτή τους αυτή αγωγιμότητα έχει ως αποτέλεσμα τη διεύρυνση της ζώνης αντίδρασης και την ταχύτερη κινητική της αντίδρασης αναγωγής του οξυγόνου. Στην παρούσα εργασία πραγματοποιήθηκε ηλεκτροχημικός χαρακτηρισμός με φασματοσκοπία σύνθετης αντίστασης, μετρήσεις πυκνότητας ρεύματος-υπέρτασης και κυκλική βολταμετρία, περοβσκιτικών καθοδικών ηλεκτροδίων La1-x-ySrxCo2Fe0.8O3-δ και La1-x-ySrxFeO3-δ σε επαφή με CGO/YSZ. Από την ανάλυση των πειραμάτων σύνθετης αντίστασης προέκυψε ως κύριο συμπέρασμα ότι ανάλογα με τη θερμοκρασία, τη μερική πίεση οξυγόνου και την πόλωση, τα χαρακτηριστικά σύνθετης αντίστασης του ηλεκτροδίου La0.8Sr0.2Co0.2Fe0.8O3-δ καθορίζονται από μέχρι τρεις διαφορετικές διεργασίες, οι οποίες αναγνωρίστηκαν ως αγωγή ιόντων οξυγόνου διά του ηλεκτροδίου, διαφασική μεταφορά φορτίου με συμμετοχή ατομικού οξυγόνου και διάχυση O2 στην αέρια φάση. Με ανάλυση μετρήσεων πυκνότητας ρεύματος ως προς την υπέρταση και το δυναμικό του ηλεκτροδίου, προσδιορίστηκαν επίσης, οι τιμές των ηλεκτροκινητικών παραμέτρων (πυκνότητα ρεύματος ανταλλαγής, συντελεστές μεταφοράς) που αφορούν στην ηλεκτροχημική αντίδραση αναγωγής του οξυγόνου και η αγωγιμότητα πόλωσης ως συνάρτηση του εφαρμοζόμενου δυναμικού για διάφορες θερμοκρασίες. Η τεχνική της κυκλικής βολταμετρίας εφαρμόστηκε για χαρακτηρισμό των παραπάνω περοβσκιτικών ηλεκτροδίων (x = 0.2; 0.4 και y = 0; 0.02), προκειμένου να αναγνωριστούν οι ηλεκτροχημικές διεργασίες που λαμβάνουν χώρα υπό συνθήκες πόλωσης. Η εμφάνιση κορυφών ρεύματος στα κυκλοβολταμογραφήματα, σε μία ευρεία περιοχή θερμοκρασιών, μερικών πιέσεων οξυγόνου και ρυθμών σάρωσης του δυναμικού, συσχετίστηκε με ηλεκτροχημικές αντιδράσεις αναγωγής-οξείδωσης ιόντων σιδήρου ή/και κοβαλτίου αλλά και με οξείδωση-αναγωγή ειδών οξυγόνου. Τέλος, αξιολογήθηκε η καταλυτική ενεργότητα περοβσκιτικών οξειδίων με γενικό τύπο La1-x-ySrxCozFe1-zO3-δ για πλήρη οξείδωση CO και CH4. Ως κύριο συμπέρασμα προέκυψε ότι τα περοβσκιτικά οξείδια LSCF παρουσιάζουν υψηλότερη καταλυτική ενεργότητα σε σχέση με τα οξείδια LSF. / Recently, there has been a lot of focus on the development of new cathode materials for use in intermediate temperature (600–800°C) solid oxide fuel cells, since the conventional cathodes based on La1–xSrxMnO3–δ do not perform satisfactorily below 800°C. Iron- and cobalt-containing perovskites La1–x–ySrxCozFe1–zO3–δ have recently attracted significant attention as promising alternative cathode materials for IT-SOFCs, mainly due to their high mixed (electronic and ionic) conductivity, which results in enlargement of the available electrochemically active area, and their high oxygen surface exchange coefficients. In the present work electrochemical characterisation was carried out on porous La1–x–ySrxCo0.2Fe0.8O3–δ (LSCF) and La1–x–ySrxFeO3–δ (LSF) cathode electrodes deposited via screen-printing on the CGO layer of a CGO/YSZ electrolyte, using AC impedance spectroscopy, current density vs. electrode overpotential measurements, and cyclic voltammetry. From the analysis of the experimental results it was concluded that depending on temperature, oxygen partial pressure and polarization, the impedance characteristics of the La0.8Sr0.2Co0.2Fe0.8O3-δ electrode are determined by up to three different processes, which were identified as ionic conduction in the electrode bulk, interfacial charge transfer and gas phase diffusion, respectively. The values of the electrokinetic parameters of the electrochemical oxygen reduction as well as the polarization conductance, were determined as a function of the applied electrode potential at different temperatures, based on the analysis of current density vs. electrode overpotential measurements. Cyclic voltammetry technique was used in order to identify the electrochemical processes taking place under cathodic polarization on the basis of differences in the features of the cyclic voltammograms with changing conditions. Depending on the electrode, temperature, oxygen partial pressure and potential sweep rate, the appearance of current peaks was related to the electrochemical redox of B-sites and concomitant stoichiometry change as well as to the competing reaction of electrochemical oxygen redox, taking also into account the competitive action of chemical reactions which may occur in the presence of O2. Finally, the present work aimed to the assessment of the catalytic activity of these perovskite oxides for CO and CH4 combustion and it was found that LSCF perovskites were more catalytically active than LSF perovskites.

Three mathematical models, two of primary alkaline battery cathode discharge, and one of primary alkaline battery discharge, are developed, presented, solved and investigated in this thesis. The primary aim of this work is to improve our understanding of the complex, interrelated and nonlinear processes that occur within primary alkaline batteries during discharge. We use perturbation techniques and Laplace transforms to analyse and simplify an existing model of primary alkaline battery cathode under galvanostatic discharge. The process highlights key phenomena, and removes those phenomena that have very little effect on discharge from the model. We find that electrolyte variation within Electrolytic Manganese Dioxide (EMD) particles is negligible, but proton diffusion within EMD crystals is important. The simplification process results in a significant reduction in the number of model equations, and greatly decreases the computational overhead of the numerical simulation software. In addition, the model results based on this simplified framework compare well with available experimental data. The second model of the primary alkaline battery cathode discharge simulates step potential electrochemical spectroscopy discharges, and is used to improve our understanding of the multi-reaction nature of the reduction of EMD. We find that a single-reaction framework is able to simulate multi-reaction behaviour through the use of a nonlinear ion-ion interaction term. The third model simulates the full primary alkaline battery system, and accounts for the precipitation of zinc oxide within the separator (and other regions), and subsequent internal short circuit through this phase. It was found that an internal short circuit is created at the beginning of discharge, and this self-discharge may be exacerbated by discharging the cell intermittently. We find that using a thicker separator paper is a very effective way of minimising self-discharge behaviour. The equations describing the three models are solved numerically in MATLABR, using three pieces of numerical simulation software. They provide a flexible and powerful set of primary alkaline battery discharge prediction tools, that leverage the simplified model framework, allowing them to be easily run on a desktop PC.