Wind-hydrogen systems for remote area power supply are an early niche application of sustainable hydrogen energy. Optimal direct coupling between a wind turbine and an electrolyser stack is essential for maximum electrical energy transfer and hydrogen production. In addition, system costs need to be minimised if wind-hydrogen systems are to become competitive. This paper investigates achieving near maximum power transfer between a fixed pitched variable-speed wind turbine and a Proton Exchange Membrane (PEM) electrolyser without the need for intervening voltage converters and maximum power point tracking electronics. The approach investigated involves direct coupling of the wind turbine with suitably configured generator coils to an optimal series-parallel configuration of PEM electrolyser cells so that the I-V characteristics of both the wind turbine and electrolyser stack are closely matched for maximum power transfer. A procedure for finding these optimal con figurations and hence maximising hydrogen production from the system is described. For the case of an Air 403 400 W wind turbine located at a typical coastal site in south-eastern Australia and directly coupled to an optimally configured 400 W stack of PEM electrolysers, it is estimated that up to 95% of the maximum achievable energy can be transferred to the electrolyser over an annual period. The results of an extended experiment to test this theoretical prediction for an actual Air 403 wind turbine are reported. The implications of optimal coupling between a PEM electrolyser and an aerogenerator for the performance and overall economics of wind-energy hydrogen systems for RAPS applications are discussed.

Fuel cells are a promising alternate power source of electricity. Despite of sig- nificant improvement that was reached by research throughout recent decades, the technology is not still ready to large scale commercial use. The catalyst of fuel cell (FC) should be still investigated due to fact that the only reliable functional catalyst is Platinum, a noble and expensive metal, which makes the use of this technology not competitive. In this thesis, investigation of Platinum doped ceria catalyst and its modification prepared by physical technique of deposition which is magnetron sputtering is presented. The catalyst was studied using standard sur- face analytic techniques (PES, SEM, AFM, XANES) as well as electrochemical measurement (CV, PEIS). The principal part of this thesis reports direct analyses of catalyst in fuel cell using an individually designed fuel cell test station. Con- sidering the high power density (PD) about 1 W cm−2 and substantially higher specific power per gram of Platinum (SP) 1.6 kW mg−1 in comparison with com- mercial Pt-Ru/Pt-C reference catalyst and additionally the relatively longtime stability, the sputtered Platinum doped cerium oxide based catalyst was found a suitable catalyst for PEM FC. Moreover, possible substitution of Pt and CeO2 by other elements was shown. Beside of...

The electrical energy output and the performance of a PEM fuel cell is dependent on the ion transfer in the fuel cell. The ion transport mechanism in the electrolyte cell membrane is dependent on the charge site in the membrane. The charge sites increases with an increase in the hydration of the membrane, this shows that the water content of the membrane is important to facilitate the ion transfer in the electrolyte membrane, hence proper management of water is essential to the operation of the PEM fuel cell system, to achieve these a proper balance of the water transport within the PEM fuel cell is needed for the optimum operation of the PEM fuel cell membrane. This work is based on an assessment of the humidity management effect on the performance of the PEM fuel cell. If the fuel cell membrane is over hydrated with water, it results in over flooding of cell membrane, which causes activation losses and H+ ion cross over losses in the fuel cell, and if the membrane is poorly hydrated it results in poor hydration of the membrane which causes concentration loss, and very low ion conductivity. The water balance system of the fuel cell is such that water vapour is present in the air at the inlet, the water is also used for H+ ion transport from the anode to the cathode, the excess water in the cathode is back diffused in to the anode, at the cathode it is also produced from the chemical reaction of the fuel cell, at the exits water it is evaporated at both the anode and cathode of the cell, and finally with the use of water mass balance we determine the mass of the water which is injected into the fuel cell to meet up the water demand for the hydration of the membrane. This work analyses how these parameters, the operating temperature, relative humidity of air, the inlet temperature, the pressure drop in the cell membrane, the operating temperature, the membrane thickness and the stoichiometry of air affects the water content of the cell membrane. The results from this work showed that a proper management of the PEM fuel cell is of central importance to control the membrane hydration and ensure proper performance of the fuel cell.

No description available.

A new type of fuel cell architecture, the fuel cell ribbon, is presented. The fuel cell ribbon architecture relies on the gas diffusion layer (GDL) to conduct electrical current in-plane to adjacent cells or collector terminals. The potential advantages of the fuel cell ribbon architecture with respect to conventional fuel cell stacks include reduced manufacturing costs, reduced weight, reduced volume, and reduced component cost. The critical component of fuel cell ribbon assemblies, the gas diffusion media, is investigated herein. Analytical models which focus on the electrical loses within the gas diffusion media of the novel architecture are developed. The materials and treatments necessary to fabricate novel gas diffusion media for fuel cell ribbon assemblies are presented. Experimental results for the novel gas diffusion media of are also presented. One dimensional and two dimensional analytical models were developed for the fuel cell ribbon. The models presented in this work focus on the losses associated with the transport of the electrons in fuel cell ribbon assemblies, rather than the complex system of equations that governs the rate of electron production. The 1-D model indicated that the GDL used in ribbon cells must exhibit an in-plane resistance which is approximately an order of magnitude lower than the resistance of gas diffusion media typically used in conventional fuel cells. A 2-D model was developed with which a parametric study of GDL properties and ribbon cell dimensions was performed. The parametric study indicated that ribbon cells of useful size can be constructed using novel diffusion media that offer reduced resistivity, and that the ribbon cells can produce as much as 80-85% of the power density produced in a conventional fuel cell. Novel gas diffusion media for fuel cell ribbons that have the necessary characteristics suggested by the analytical study were developed.. Properties and performance for a commercially available gas diffusion media, ELAT, were measured as a reference for the novel media developed. The increased thickness PAN (ITPN) series diffusion media was constructed of PAN based fibers exhibiting similar resistive properties to the fibers used in ELAT. The ITPN series of materials were woven in a manner which made them approximately twice the thickness of ELAT, effectively reducing their in-plane resistance to half the resistance exhibited by ELAT. The coarsely woven pitch (CWPT) series of materials were constructed in a manner which yielded a similar number of fibers in the plane of the material to ELAT and a similar material thickness to ELAT, but the fibers used were mesophase pitch based fibers which exhibit a resistivity of approximately one-tenth the resistivity of the fibers used to make the ELAT and ITPN materials. The reduction in fiber resistivity led to the CWPT material having an in-plane resistance an order of magnitude lower than ELAT. The widely used ELAT material exhibited an in-plane resistance of 0.39 Ω/sq., a through-plane area specific resistance of 0.007 Ω-cm2, and a Darcy permeability coefficient of 8.1 Darcys. The novel diffusion materials exhibited in-plane resistances in the range of 0.18-0.036 Ω/sq., through-plane area specific resistances in the range of 0.017-0.013 Ω-cm2, and Darcy permeability coefficients in the range of 30-150 Darcys. Experiments were performed to validate the analytical model and to prove the feasibility of fuel cell ribbon concept. When the novel gas diffusers were adhered to a catalyzed membrane and tested in a ribbon test assembly utilizing serpentine flow channels and in-plane current collection, a range of performance was achieved between 0.28-0.4 A/cm2 at a cell output potential of 0.5 V. In contrast, when ELAT was adhered to a catalyzed membrane and tested in the fixture requiring in-plane conduction, a current density of 0.21 A/cm2 was achieved at 0.5 V. Additionally, the 2-D finite element model was used to predict the performance of a ribbon cell based on the cells performance when a conventional method of through-plane conduction was utilized. The agreement between the experimental data and the model predictions was very good for the ELAT and ITPN materials, whereas the predictions for the CWPT materials showed more significant deviation which was likely due to mass transport and contact resistance effects. / Master of Science

The development of a test apparatus for proton exchange membrane fuel cells is presented. The design of the prototype device is provided in detail along with a description of the apparatus. The evaluation of the functionality and effectiveness of the device included measurement of a polarization curve for a 5-cell, 1 kW stack. An effective test apparatus is imperative for stack performance testing, model evaluation, and investigation of new fuel cell technology. This apparatus was designed to measure and control the mass flow rates of the reactant gases, gas pressures, gas temperatures, gas relative humidity, stack temperature, stack current, and the coolant water flow rate. Additionally, the test apparatus can measure the stack voltage, coolant water resistivity, coolant water temperature change across the stack, and the coolant water pressure drop across the stack. The apparatus was shown to provide adequate control of all necessary variables for stack performance evaluation. / Master of Science

Philosophiae Doctor - PhD / Fuel cells are long term solution for global energy needs. In current fuel cell technologies, Proton Exchange Membrane (PEM) fuel cells are known for quick start-up and ease of operation compared to other types of fuel cells. Operating PEM fuel cells at high temperature show promising applications for stationary combined heat and power application (CHP). The high operating temperature up to 160°C allows waste heat to be recovered for co-generation or tri-generation purposes. The commercially available PEM fuel cells operating at 160⁰C can tolerate up to 3% CO without significant loss of performance, making HT-PEM fuel cell viable choice when reformate is used. In reality these advantages convert to very little balance-of-plant compared to Nafion® based fuel cells operating at 60°C. However, there are some problems that prevent high temperature fuel cells from large scale commercialization. The cathode is said to have sluggish reaction kinetics and high cell potentials and operating temperature during fuel cell start-up may cause severe degradation. The formation of liquid water during the shut-down can cause the phosphoric acid to leach from the cell during operation. Efforts are being made to reduce the cost and increase the durability of fuel cell components (such as catalyst and membrane) at high temperatures. Apart from degradation issues, the problems are related to cost and performance. The performance of the PEM fuel cells depends on a lot of factors such as fuel cell design and assembly, operating conditions and the flow field design used on the cathode and anode plates. The flow field geometry is one important factor influencing the performance of fuel cells. The flow fields have significant effect on pressure and flow distribution inside the fuel cell. A homogeneous distribution of the reactant gases over the active catalyst surface leads to improved electrochemical reactions and thus enhances the performance of the fuel cell. So, the design of flow fields is one of the important issues for performance improvement of PEM fuel cell in terms of power density and efficiency. There are different types of flow fields available for PEM fuel cells such as serpentine, pin, interdigitated and straight flow fields but the most obvious choice is multiple serpentine. The same can be used for high temperature PEM fuel cell (HT-PEMFC) application with ease because of absence of liquid water during the high temperature operation and no need for complex water management.

L’économie actuelle repose sur l’utilisation d’énergies fossiles dont les réserves sont limitées. En plus, l’utilisation de ces ressources a un impact négatif sur l’environnement dû à l’émission des gaz polluants et du CO2. Il est donc nécessaire de remplacer les ressources fossiles par les énergies renouvelables. Les énergies renouvelables peuvent être facilement converties en électricité pour une utilisation directe, mais l’électricité ne peut pas être stockée en grande quantité. Dans ce contexte, l’hydrogène pourrait servir de vecteur énergétique. Il est possible de produire de l’hydrogène par électrolyse de l’eau. L’hydrogène sera ensuite utilisé via une pile à combustible pour fournir de l’électricité et de la chaleur. Ce procédé ne produit que de l’eau qui va être re-consommé ensuite par l’électrolyse.Ce travail de thèse est axé sur la production d’hydrogène par électrolyse de l’eau en milieu acide par la technologie PEM (proton exchange membrane). L’objectif est de remplacer le platine, catalyseur de la réduction à la cathode par des complexes de cobalt de type cobalt-oxime.Le premier chapitre traite différents aspects de l’électrolyse de l’eau et différents catalyseurs étudiés dans la littérature.Le second chapitre décrit différentes techniques expérimentales utilisées pour caractériser les complexes étudiés.Le chapitre trois décrit la synthèse et l’activité catalytique des complexes de cobalt-oxime en solution dans l’acétonitrile vis-à-vis de la réduction des protons en hydrogène.Le chapitre quatre présente les premiers travaux obtenus en utilisant les complexes de cobalt-oxime à la place du platine dans les électrolyseurs PEM. / Today's economy is base on the use of fossil fuels, whose reserves are limited. In addition, the use of these resources has a negative impact on the environment due to the emission of polluting gases and CO2. Therefore it is necessary to replace fossil fuels by renewable energy. Renewable energy can be easily converted to electricity to direct use, but electricity can not be stored in large quantities. In this context, hydrogen could be used as an energy carrier. It is possible to produce hydrogen by electrolysis of water. Hydrogen is then used via a fuel cell to supply electricity and heat. This process produces only water which will then be re-used by the electrolysis.This thesis focuses on hydrogen production by water electrolysis in acidic medium by the PEM (proton exchange membrane) technology. The goal is to replace the platinum, catalyst for proton reduction at the cathode by cobalt-oxime complexes.The first chapter describes various aspects of water electrolysis and different catalyst studied in the literature.The second chapter describes different characterization techniquesChapter three describes the synthesis and catalytic activity of the complexes of cobalt-oxime in solution in acetonitrile towards proton reduction into hydrogen.Chapter four presents the early work obtained using cobalt complexes oxime instead of platinum in PEM electrolyzers.

La production d’hydrogène et de dioxygène par électrolyse PEM (PEM « Proton Exchange Membrane ») de l’eau s’effectue grâce à la présence de métaux nobles dans les couches catalytiques: à la cathode, le platine supporté sur du carbone est généralement utilisé (les chargements en métaux nobles sont faibles de l’ordre de 0,5 mg/cm²) ; à l’anode, la production d’oxygène s’effectue à des potentiels élevés (> 1,6 V vs. ESH). Les oxydes de métaux nobles sont utilisés seuls dans la couche active anodique et servent à la fois de catalyseurs et de conducteurs électroniques. Comme ils sont parmi les métaux les plus denses, pour obtenir une continuité électrique de la couche anodique, les chargements doivent être très élevés, de l’ordre de 2-3 mg/cm².Cette thèse propose ainsi de développer de nouveaux matériaux supports stables électrochimiquement et bons conducteurs électroniques pour séparer les fonctions de catalyse et de conduction électronique. Pour cela, des assemblages membrane électrodes intégrant des particules de titane comme support de catalyseur anodique ont été préparés dans notre laboratoire. Testés en mono-cellule de 25 cm², leurs principales caractéristiques ont été déterminées par voltampérométrie cyclique, spectroscopie d’impédance et grâce à des courbes de polarisations à différentes températures. La comparaison des résultats obtenus entre ces anodes « innovantes » et celles à base de catalyseur seul a permis de mettre en évidence la présence d’un chargement anodique seuil de 0,5 mg/cm² en dessous duquel la présence d’un support de catalyseur est nécessaire pour assurer la percolation électrique. Grâce à l’utilisation de ce support de catalyseur bon marché, les chargements anodiques ont pu être réduits jusqu’à des valeurs aussi faibles que 0,1 mg/cm² IrO2, soit une réduction de dix fois au minimum par rapport aux taux généralement employés dans la littérature, tout en maintenant des performances identiques. / It is expected that PEM water electrolysis will play a significant role in the hydrogen society as a key process for producing hydrogen from renewable energy sources but before this, substantial cost reductions are still required. Because of the high acidity of membrane materials used in PEM water electrolysers, expensive noble-metals or their oxides are required as electrocatalysts (platinum for hydrogen evolution and iridium for oxygen evolution). As the oxygen evolution reaction takes place with a large overpotential (anodic potential > 1.6 V) only few materials can be used to avoid corrosion. In state-of-the-art, noble metal oxides are generally used alone in the active layer with typical loadings of 2-3 mg/cm² and act as both catalyst and electronic conductor.In order to reduce the noble metal loadings and keep a good electronic conductivity of the catalytic layer, iridium can be supported onto a conductive and electrochemical stable material support. To gain more insights, several MEAs with anodes made of pure iridium oxide or 50 wt % IrO2/Ti anodes have been prepared and characterized using cyclic voltammetry and impedance spectroscopy, and by measuring polarization curves at different operating temperatures. Without the catalyst support, anodic loadings can be reduced down to 0,5 mg/cm² without any degradation in the electrochemical performances. By using anodes made of iridium oxide and titanium particles, further reductions of anodic loading can be made down to 0.1 mg/cm² with performances similar to those obtained with conventional loadings of several mg cm-2.

Le domaine du transport aérien est en plein effort de réduction de ses émissions de gaz à effet de serre. Les PEMFC sont sérieusement envisagées afin d'introduire d'avantage d'énergie électrique à bord des avions. On se propose d'étudier la faisabilité de la propulsion d'avions légers alimentés par des systèmes pile à combustible hybridés. On étudie plus spécifiquement un système hybride PEMFC / Batteries Li-Ion produisant un total de 40 kW (20 kW PàC + 20 kW Li-Ion) permettant de propulser un avion léger biplace. Le premier aspect de cette étude est la navigabilité des PEMFC, c'est à dire leur aptitude à fonctionner en milieu aérien. Le second aspect est l'architecture électrique du système hybride, son dimensionnement et son comportement lors de différents profils de vol. Des essais expérimentaux en altitude sont menés et permettent de quantifier la diminution des performances de PàC aérobies liée à la diminution de pression ambiante. Grâce à ces essais et à un modèle numérique de PàC, on compare les technologies aérobies et anaérobies pour différents profils de vol. Un bilan des masses et des volumes associé à chacune de ces deux technologies est dressé. Par ailleurs, des essais en inclinaisons de systèmes PEMFC sont réalisés. L'hybridation directe de PEMFC avec des batteries Lithium est étudiée numériquement et expérimentalement. Un modèle Matlab Simulink de PàC et de batteries Lithium est développé afin de prédire le comportement du système hybride direct et de le dimensionner. Enfin, un banc expérimental d'hybridation directe est réalisé et des essais sont menés, révélant l'intérêt de cette architecture innovante. / The domain of air transport is working at reducing its emissions of greenhouse gases. PEMFC are seriously considered as electrical source for future aircraft. The present study focusses on the feasibility of propulsion of a light aircraft powered by hybridized PEMFC systems. The hybrid PEMFC / Li-Ion batteries system studied here produces 40 kW (20 kW PEMFC + 20 kW Li-Ion) and should be able to power a two-seat light aircraft. The first part of the study is dedicated to PEMFC airworthiness, meaning their capacity to work properly in aeronautical conditions. The second part is dedicated to the hybrid system electrical architecture, its dimensioning and its response to various flight profiles. Aerobic PEMFC performance loss due to drop in ambient pressure is quantified thanks to experiments at various altitude. Thanks to these measurements and to a numerical model, aerobic and anaerobic PEMFC are compared according to various flight profiles. A mass and volume balance of each technology is drawn up. In addition, inclination tests of PEMFC systems are performed. Direct hybridization of PEMFC and Li-Ion batteries is studied numerically and experimentally. A Matlab Simulink model of PEMFC and battery is developed in order to forecast the hybrid system's response and to size it. Finally, an experimental bench is settled up and tests are led, proving the interest of such an innovative architecture.