Os componentes do conjunto membrana/eletrodos (MEA) das células a combustível de membrana de eletrólito polimérico/Polymer Electrolyte Membrane Fuel Cells (PEMFC) são sensíveis a impurezas, as quais podem vir do ar, do gás combustível e/ou da degradação dos componentes do módulo. Amônia, sulfeto de hidrogênio e monóxido de carbono são juntos os três principais subprodutos cotaminadores nos processos de geração de hidrogênio por reforma de combustíveis. Estes contaminadores afetam negativamente o desempenho das PEMFCs, assim é importante o entendimento destes efeitos para mitigá-los e introduzir a tecnologia das PEMFCs no mercado consumidor. Desta forma experimentos foram realizados visando diagnosticar os efeitos da amônia e do sulfeto de hidrogênio sobre os componentes do MEA das PEMFCs. Para a contaminação por sulfeto de hidrogênio foi provado, utilizando-se da técnica de cromatografia gasosa e de stripping, que a contaminação ocorre através da interação química e eletroquímica do contaminador com a superfície do catalisador de platina, e que estas interações ocorrem via um processo dissociativo e um processo oxidativos respectivamente. Estes processos de interação geram enxofre adsorvido sobre a superfície da platina, a qual é bloqueada para posterior oxidação de hidrogênio, gerando sobrepotenciais que reduzem a diferença de potencial da célula. Utilizando-se da técnica de cromatografia gasosa e agora de voltametria cíclica foi mostrado na PEMFC, que durante o processo de remoção do enxofre adsorvido a platina dióxido de enxofre é gerado. Ainda na PEMFC, foi mostrado utilizando-se da técnica de \"air bleed\" que maiores tolerâncias ao sulfeto de hidrogênio podem ser alcançadas, apesar de ser insignificante. Para o caso da contaminação da PEMFC por amônia, indiretamente foi mostrado, utilizando-se técnicas eletroquímicas solução de ácido perclórico, que amônia pode afetar a reação de redução de oxigênio pela sua adsorção sobre a superfície do catalisador, ou pelo bloqueio da mesma para posterior adsorção/redução de oxigênio. Em estudos de absorção de água e condutividade de membranas de NafionTM, sob diferentes frações catiônicas (prótons/amônio), em contato com água na fase vapor sob diferentes atividades, foi mostrado que quanto maior a concentração de íons contaminadores no eletrólito menor a quantidade de água absorvida e menor a condutividade da membrana. Também foi mostrado que se tais membranas fossem usadas como eletrólito em PEMFCs, o desempenho da célula seria afetado drasticamente por perdas ôhmicas. Também foi mostrado que sob contaminação por amônia, PEMFCs sofrem aumentos em resistências ôhmicas devido a reduções na condutividade do eletrólito, contudo foi provado que esta representa menos de dez por cento do total de perdas observadas no desempenho da célula. Desde estudo foi concluído que amônia afeta o desempenho das PEMFCs principalmente pela redução na atividade dos prótons na camada catalítica catódica, que causa reduções no potencial misto de equilíbrio da reação de redução de oxigênio, e portanto na diferença de potencial da célula. Finalmente foi provado indiretamente que amônia deixa a célula através do equilíbrio de amônio com água, o qual deslocado gera amônia, a qual deixa a célula junto com o fluxo de gás cotódico. / The Membrane Electrode Assembly components of a PEMFC are sensitive to impurities, which can came with the air or hydrogen stream, or from the degradation of the stack components. Ammonia, hydrogen sulfide and carbon monoxide are together the main sub-products of fuel reforming processes for generating hydrogen. These contaminants negatively affect the PEMFC performance, so it is important to understand what those effects are in order to mitigate them and introduce PEMFC technology in the mass market. Therefore, experiments were carried out to diagnose the effects hydrogen sulfide and ammonia have on the MEA components of PEMFCs. For contamination by hydrogen sulfide it was proved utilizing EMS and stripping techniques that the poisoning process happens by chemical and electrochemical interactions of the contaminant with the Platinum catalyst surface, and that these interactions happen by a dissociative and oxidative process, respectively. Those processes generate sulfur adsorbed on the Platinum surface, which blocks it for further hydrogen oxidation, generating overpotentials, which reduce the cell potential. Utilizing the EMS and now the cyclic voltammetry technique it was shown that during the process of removing sulfur from the Platinum surface one generates sulfur dioxide. Using the Air Bleed technique it was shown that higher tolerances of the PEMFC against hydrogen sulfide can be reached, despite being insignificant. For contamination of the cell by ammonia it was indirectly proved utilizing electrochemical techniques in perchloric acid solutions that ammonia can affect the oxygen reduction reaction by adsorbing on the catalyst surface, or by blocking the surface for further oxygen adsorption/reduction. Studying water uptake and ionic conductivity of Nafion membranes under many different cation fractions (proton/ammonium) in contact with water vapor at different temperatures and water activities, it was proved that the more ammonium one has in the membrane the less will be the water uptake and ionic conductivity of it. It was also shown that if those membranes were used as electrolyte in PEMFC the cell performance would be severely affected by ohmic losses. It was also shown that under ammonia exposure PEMFCs suffer by ohmic resistance increases due to the lowering in the ionic conductivity of the electrolyte, however it was proved that it represent less than ten percent of the observed losses in the cell performance. From this study it was concluded that ammonia mainly affect the PEMFC performance by lowering the cathode catalyst layer proton activity, which lowers the oxygen reduction reaction equilibrium potential, and then the cell potential. Finally it was indirectly proved that ammonia leaves the cell by the equilibrium of ammonium and water, which dislocated generates ammonia that leaves the cell together with the cathode gas stream.

Os componentes do conjunto membrana/eletrodos (MEA) das células a combustível de membrana de eletrólito polimérico/Polymer Electrolyte Membrane Fuel Cells (PEMFC) são sensíveis a impurezas, as quais podem vir do ar, do gás combustível e/ou da degradação dos componentes do módulo. Amônia, sulfeto de hidrogênio e monóxido de carbono são juntos os três principais subprodutos cotaminadores nos processos de geração de hidrogênio por reforma de combustíveis. Estes contaminadores afetam negativamente o desempenho das PEMFCs, assim é importante o entendimento destes efeitos para mitigá-los e introduzir a tecnologia das PEMFCs no mercado consumidor. Desta forma experimentos foram realizados visando diagnosticar os efeitos da amônia e do sulfeto de hidrogênio sobre os componentes do MEA das PEMFCs. Para a contaminação por sulfeto de hidrogênio foi provado, utilizando-se da técnica de cromatografia gasosa e de stripping, que a contaminação ocorre através da interação química e eletroquímica do contaminador com a superfície do catalisador de platina, e que estas interações ocorrem via um processo dissociativo e um processo oxidativos respectivamente. Estes processos de interação geram enxofre adsorvido sobre a superfície da platina, a qual é bloqueada para posterior oxidação de hidrogênio, gerando sobrepotenciais que reduzem a diferença de potencial da célula. Utilizando-se da técnica de cromatografia gasosa e agora de voltametria cíclica foi mostrado na PEMFC, que durante o processo de remoção do enxofre adsorvido a platina dióxido de enxofre é gerado. Ainda na PEMFC, foi mostrado utilizando-se da técnica de \"air bleed\" que maiores tolerâncias ao sulfeto de hidrogênio podem ser alcançadas, apesar de ser insignificante. Para o caso da contaminação da PEMFC por amônia, indiretamente foi mostrado, utilizando-se técnicas eletroquímicas solução de ácido perclórico, que amônia pode afetar a reação de redução de oxigênio pela sua adsorção sobre a superfície do catalisador, ou pelo bloqueio da mesma para posterior adsorção/redução de oxigênio. Em estudos de absorção de água e condutividade de membranas de NafionTM, sob diferentes frações catiônicas (prótons/amônio), em contato com água na fase vapor sob diferentes atividades, foi mostrado que quanto maior a concentração de íons contaminadores no eletrólito menor a quantidade de água absorvida e menor a condutividade da membrana. Também foi mostrado que se tais membranas fossem usadas como eletrólito em PEMFCs, o desempenho da célula seria afetado drasticamente por perdas ôhmicas. Também foi mostrado que sob contaminação por amônia, PEMFCs sofrem aumentos em resistências ôhmicas devido a reduções na condutividade do eletrólito, contudo foi provado que esta representa menos de dez por cento do total de perdas observadas no desempenho da célula. Desde estudo foi concluído que amônia afeta o desempenho das PEMFCs principalmente pela redução na atividade dos prótons na camada catalítica catódica, que causa reduções no potencial misto de equilíbrio da reação de redução de oxigênio, e portanto na diferença de potencial da célula. Finalmente foi provado indiretamente que amônia deixa a célula através do equilíbrio de amônio com água, o qual deslocado gera amônia, a qual deixa a célula junto com o fluxo de gás cotódico. / The Membrane Electrode Assembly components of a PEMFC are sensitive to impurities, which can came with the air or hydrogen stream, or from the degradation of the stack components. Ammonia, hydrogen sulfide and carbon monoxide are together the main sub-products of fuel reforming processes for generating hydrogen. These contaminants negatively affect the PEMFC performance, so it is important to understand what those effects are in order to mitigate them and introduce PEMFC technology in the mass market. Therefore, experiments were carried out to diagnose the effects hydrogen sulfide and ammonia have on the MEA components of PEMFCs. For contamination by hydrogen sulfide it was proved utilizing EMS and stripping techniques that the poisoning process happens by chemical and electrochemical interactions of the contaminant with the Platinum catalyst surface, and that these interactions happen by a dissociative and oxidative process, respectively. Those processes generate sulfur adsorbed on the Platinum surface, which blocks it for further hydrogen oxidation, generating overpotentials, which reduce the cell potential. Utilizing the EMS and now the cyclic voltammetry technique it was shown that during the process of removing sulfur from the Platinum surface one generates sulfur dioxide. Using the Air Bleed technique it was shown that higher tolerances of the PEMFC against hydrogen sulfide can be reached, despite being insignificant. For contamination of the cell by ammonia it was indirectly proved utilizing electrochemical techniques in perchloric acid solutions that ammonia can affect the oxygen reduction reaction by adsorbing on the catalyst surface, or by blocking the surface for further oxygen adsorption/reduction. Studying water uptake and ionic conductivity of Nafion membranes under many different cation fractions (proton/ammonium) in contact with water vapor at different temperatures and water activities, it was proved that the more ammonium one has in the membrane the less will be the water uptake and ionic conductivity of it. It was also shown that if those membranes were used as electrolyte in PEMFC the cell performance would be severely affected by ohmic losses. It was also shown that under ammonia exposure PEMFCs suffer by ohmic resistance increases due to the lowering in the ionic conductivity of the electrolyte, however it was proved that it represent less than ten percent of the observed losses in the cell performance. From this study it was concluded that ammonia mainly affect the PEMFC performance by lowering the cathode catalyst layer proton activity, which lowers the oxygen reduction reaction equilibrium potential, and then the cell potential. Finally it was indirectly proved that ammonia leaves the cell by the equilibrium of ammonium and water, which dislocated generates ammonia that leaves the cell together with the cathode gas stream.

D. Tech. (Department of Mechanical Engineering, Faculty of Engineering and Technology), Vaal University of Technology. / On account of their lightweight, low-cost, corrosion resistance, and good formability, conductive polymer composites (CPCs) are promising for the production bipolar plate (BP) for polymer electrolyte membrane fuel cell (PEMFC). However, a high conductive filler loading is needed to impart the required level of electrical conductivity to the insulating polymer matrix and as a consequence, the toughness of the plate deteriorates considerably. By using immiscible blend of polymers that have complementary hardness and ductility as matrix, with conducting multi-fillers of different morphologies, it is possible to optimize the matrix strength characteristics and favour the formation of conducting network to produce CPC meeting BP performance standards. Of course, a lot will depend on the formulation of the most favourable composition and production variables. In this regard, polypropylene-epoxy and polyethylene-epoxy blends, filled with zero- and two-dimensional carbon forms – graphite, carbon black (CB), and graphene (Gr) – were investigated over an extensive range of compositions and compression moulding pressures, in this study. Several compounding runs (using melt mixing), at different stages, followed by compression molding, were done. The goal is to obtain combination of composite formulation and processing conditions that will produce the most promising combination of properties for BP application. In the first stage of the investigations, by using thermogravimetric analysis, two-stage decomposition behavior of PP-epoxy and PE-epoxy blends was revealed, which confirms the immiscibility of PP and PE with epoxy resin. Scanning electron microscope (SEM) micrographs of the PP-epoxy and PE-epoxy blends revealed a co-continuous structure, which can be attributed to the close-to-symmetric composition of the blend and compatibilizers added. Preferential localization of synthetic graphite (SG), CB, and Gr in the polymer blends was also revealed by the SEM micrographs. This confirms the fact that CPCs based on PP-epoxy and PE-epoxy blends can be explored further. PP-epoxy and PE-epoxy blends filled with only SG, 30 – 80 wt %, were produced and characterized for their electrical conductivity and flexural properties. In-plane electrical conductivity ranged from 12.09 to 68.03 Scm-1 for PP-epoxy/SG and 11.68 to 72.96 Scm-1 for PE-epoxy/SG composites produced. These are higher than values reported for several single matrix polymer composites at similar filler loadings. With reference to the United States Department of Energy performance targets for BPs, PE-epoxy/SG composites performed better in terms of electrical conductivity, while PP-epoxy/SG composites exhibited better flexural properties. Thereafter, using SG and CB double filler, PE-epoxy/SG/CB composites performed better than PP-epoxy/SG/CB composites in terms of electrical conductivity, while PP-epoxy/SG/CB composites exhibited superior flexural properties than the PE-epoxy/SG/CB composites at similar filler loadings. However, with respect to the DOE targets, composites based on PP-epoxy blend exhibited a more promising combination of electrical conductivity and flexural properties than PE-epoxy blend matrix. PP-epoxy filled with SG/CB was studied further, by using graphene (Gr) as second minor filler. In-plane and through plane electrical conductivities as well as thermal conductivity and thermal diffusivity of the PP-epoxy/SG/CB/Gr composites increased as total filler content was increased from 65 to 85 wt%. It implies that more conductive networks between filler particles were formed. Also, flexural strength, flexural modulus, and impact strength decreased as the total filler content increased from 65 to 85 wt%. The reduced flexural properties could be due to increased agglomeration of CB and Gr, and poor filler wetting at higher filler loadings and low matrix material, which leads to the formation of microvoids and a reduction of the load bearing capacity of composites. With respect to the DOE targets, PP-EP/SG/CB/Gr composite with 80 wt% (i.e., PP/EP/73G/6.2CB/0.8Gr) filler has the best combination of properties. Further improvement in properties of the PP-EP/SG/CB/Gr composite with 80 wt% filler was achieved by molding at higher pressures. As molding pressure was increased from 4.35 to 13.05 MPa, in-plane electrical conductivity increased from 116.31 to 144.99 Scm-1, while flexural strength increased from 29.62 to 42.57 MPa, satisfying the performance requirement targets for bipolar plates.

Οι κυψέλες καυσίμου είναι ηλεκτροχημικές διατάξεις οι οποίες επιτρέπουν την απευθείας μετατροπή της ελεύθερης χημικής ενέργειας ενός καυσίμου σε ηλεκτρική. Οι κυψέλες καυσίμου πολυμερικής μεμβράνης (ΡΕΜ) αποτελούν μία υποσχόμενη τεχνολογία που βρίσκεται κοντά στο στάδιο της εμπορευματοποίησης. Το κυριότερο καύσιμο που χρησιμοποιείται στις κυψέλες καυσίμου είναι το υδρογόνο, το οποίο παράγεται συνήθως από αναμόρφωση υδρογονανθράκων ή αλκοολών. Το μονοξείδιο του άνθρακα που παράγεται επίσης κατά την διαδικασία της αναμόρφωσης αποτελεί ένα σημαντικό άλυτο πρόβλημα στις κυψέλες ΡΕΜ, καθώς η ρόφησή του στην άνοδο της κυψέλης προκαλεί την υποβάθμιση της λειτουργίας της. Το φαινόμενο της ηλεκτροχημικής ενίσχυσης συνίσταται στην μη-φαρανταϊκή τροποποίηση της ενεργότητας ενός καταλύτη που βρίσκεται σε επαφή με έναν στερεό ηλεκτρολύτη, ως αποτέλεσμα της μετακίνησης προωθητικών ειδών από τον ηλεκτρολύτη προς την καταλυτική διεπιφάνεια μετάλλου/αερίου, που προκαλείται από την επιβολή ρεύματος ή δυναμικού μεταξύ του καταλύτη και ενός ηλεκτροδίου αναφοράς. Στην παρούσα διατριβή μελετήθηκε η ηλεκτροχημική ενίσχυση της οξείδωσης μίγματος αναμόρφωσης μεθανόλης από ανόδους πλατίνας και χρυσού μίας κυψέλης ΡΕΜ. Αποδείχθηκε πως η ηλεκτροχημική ενίσχυση επηρεάζεται σημαντικά από το διαχεόμενο διαμέσου της πολυμερικής μεμβράνης οξυγόνο, όπως επίσης και από τις συνθήκες λειτουργίας της κυψέλης καυσίμου. Επίσης μελετήθηκε η ηλεκτρική απόδοση ανόδων πλατίνας και χρυσού παρουσία CO. Προσδιορίστηκαν οι τιμές της ενθαλπίας ρόφησης του CO στα ηλεκτρόδια πλατίνας και χρυσού, καθώς και οι τιμές της ενέργειας ενεργοποίησης της απομάκρυνσης του CO από το κάθε ηλεκτρόδιο. Επίσης μελετήθηκε η επίδραση της θερμοκρασίας στο φαινόμενο της πολλαπλότητας μονίμων καταστάσεων κατά την λειτουργία κυψελών ΡΕΜ. Παρατηρήθηκε εξασθένηση του φαινομένου με την αύξηση της θερμοκρασίας, σε συμφωνία με τις προβλέψεις του μοντέλου γ. / Fuel cells are electrochemical devices which convert chemical energy of a fuel directly to electricity. Polymer electrolyte membrane (PEM) fuel cells are close to commercialization. The most common fuel used is hydrogen, which is usually produced via hydrocarbons or alcohol reforming. However, during this process, carbon monoxide is formed as well, adsorbs strongly on the anode of the cell and thus impairs significantly its performance. The electrochemical promotion effect is a phenomenon where application of constant current or potential between a catalyst supported on a solid electrolyte and a reference electrode, leads to non-Faradaic changes in catalytic activity. In this thesis, it was studied the electrochemical promotion of oxidation of a methanol reformate mixture on platinum and gold anodes of a PEM fuel cell. It was found that electrochemical promotion is influenced by oxygen crossover through the polymer membrane and also by the cell operating conditions. Moreover, the electrical efficiency of platinum and gold anodes in presence of CO was studied and the values of the heat of CO adsorption on each anode and the activation energies of CO removal were estimated. Finally, the effect of temperature on the phenomenon of steady-state multiplicities was studied. It was found that increasing the temperature, the phenomenon of multiplicities is suppressed in agreement with the gama model.

Το Η2 είναι το ελαφρύτερο και πλέον άφθονο στοιχείο στη φύση. Βρίσκεται παντού στη γη, στο νερό, στα ορυκτά καύσιμα και σε όλα τα έμβια όντα. Αν το Η2 αξιοποιηθεί κατάλληλα και χρησιμοποιηθεί για τροφοδοσία των κελιών καυσίμου, θα ελαχιστοποιηθεί η εξάρτηση του σύγχρονου πολιτισμού από τα ορυκτά καύσιμα, με συνεπακόλουθο τη μείωση των εκπομπών βλαβερών αερίων στην ατμόσφαιρα. Η χαμηλή θερμοκρασία λειτουργίας των κελιών καυσίμου πολυμερούς ηλεκτρολύτη (PEMFCs) προσφέρει πολλά πλεονεκτήματα και σε συνδυασμό με την υψηλή πυκνότητα ισχύος που αποδίδουν, τα καθιστά κύριους υποψήφιους για εφαρμογή στην αυτοκίνηση. Ωστόσο, η χαμηλή θερμοκρασία εγείρει και σημαντικά προβλήματα, όπως η χρήση ευγενών μετάλλων για την επιτάχυνση των αντιδράσεων και η ευαισθησία σε φαινόμενα δηλητηρίασης. Το κυριότερο δηλητήριο είναι το CO, βασικό παραπροϊόν των διεργασιών παραγωγής H2 από τους υδρογονάνθρακες, οι οποίοι προς το παρόν αποτελούν την κύρια πηγή του. Στην παρούσα διδακτορική διατριβή εξετάστηκαν τα φαινόμενα δηλητηρίασης από το CO της ανόδου του PEMFC. Καθώς το CO δεσμεύεται ισχυρότερα στην επιφάνεια του Pt από το καύσιμο Η2, η παρουσία του στην τροφοδοσία ακόμα και σε ίχνη απενεργοποιεί δραματικά τη λειτουργία της ανόδου. Έτσι, μελετήθηκαν διμεταλλικά και τριμεταλλικά καταλυτικά συστήματα, βασισμένα στο Pt, για την πιθανή αντιμετώπιση του προβλήματος, διαμέσου εξασθένισης του δεσμού Pt-CO ή ενίσχυσης της ηλεκτροχημικής οξείδωσής του από το Η2Ο, που είναι άφθονο στο περιβάλλον ενός PEMFC. Στο κεφάλαιο 1 περιγράφονται οι βιβλιογραφικές πληροφορίες για την τεχνολογία του Η2, όπως μέθοδοι παραγωγής του, καθαρισμού του και αποθήκευσης/μεταφοράς του. Στο κεφάλαιο 2 αναφέρονται οι βασικές αρχές λειτουργίας των κελιών καυσίμου, όσον αφορά στη θερμοδυναμική και στην κινητική, στα είδη τους και στις πιθανές εφαρμογές τους. Στο κεφάλαιο 3 γίνεται εκτενής περιγραφή των δομικών στοιχείων που απαρτίζουν ένα PEMFC, και βιβλιογραφική ανασκόπηση των καταλυτικών συστημάτων που έχουν μελετηθεί για τις βασικές αντιδράσεις. Στο κεφάλαιο 4 περιγράφονται συνοπτικά οι μέθοδοι χαρακτηρισμού και ανάλυσης καθώς και οι πειραματικές διατάξεις που χρησιμοποιήθηκαν. Στο κεφάλαιο 5 εξετάστηκε η επίδραση του υποστρώματος TiO2 στα χαρακτηριστικά του Pt, όσον αφορά την αλληλεπίδρασή του με το CO, σε διάταξη μονής κυψέλης καυσίμου. Παρουσιάστηκε αυξημένη ενεργότητα για την ηλεκτροοοξείδωση του CO και ασθενέστερη αλληλεπίδρασή του με την επιφάνεια του Pt, συντελώντας σε ενεργοποιημένη ρόφηση. Στο κεφάλαιο 6 με φασματοσκοπία υπερύθρου μελετήθηκαν τα χαρακτηριστικά της ρόφησης/εκρόφησης του CO σε μια σειρά καταλυτών Pt-Mo σε υπόστρωμα TiO2. Παρουσία των οξειδίων του Mo η θερμοκρασία εκρόφησης του CO ήταν σημαντικά μειωμένη σε σχέση με μονομεταλλικό Pt, υποδεικνύοντας ασθενέστερο δεσμό του CO με την καταλυτική επιφάνεια. Ωστόσο, παρουσία H2 ο δεσμός ισχυροποιείται, με αποτέλεσμα η εκρόφηση να πραγματοποιείται σε υψηλότερη θερμοκρασία. Αυτό εξηγήθηκε με βάση την ανταγωνιστική αντίδραση του H2 με τις οξειδικές ομάδες, τόσο του υποστρώματος TiO2, όσο και των οξειδίων του Mo. Στο κεφάλαιο 7 εξετάστηκε η οξείδωση του CO σε καταλύτη Pt4Mo/C, δεδομένου του αποσταθεροποιητικού ρόλου του Mo στα χαρακτηριστικά της αλληλεπίδρασης με το CO. Έτσι, αναγνωρίστηκε η ικανότητα των οξειδίων του Mo να διασπούν το Η2Ο σε δυναμικά που συμπίπτουν με τη λειτουργία της ανόδου ενός PEMFC, ενώ παρουσίασαν ενεργότητα για την οξείδωση του CO σε συνθήκες ανοιχτού κυκλώματος διαμέσου της αντίδρασης μετατόπισης με ατμό σε χαμηλή θερμοκρασία μέχρι και 60οC. Ωστόσο, η παραπάνω ιδιότητες δεν ήταν κατανεμημένες ομοιόμορφα στην καταλυτική επιφάνεια, παρά μόνο στη διεπιφάνεια Pt/MoOx, ενώ οι θέσεις μονομεταλλικού Pt παρουσίασαν έντονα φαινόμενα δηλητηρίασης. Επιπλέον, το Mo παρουσιάστηκε ευαίσθητο σε φαινόμενα διάλυσης στο όξινο υδατικό περιβάλλον του PEMFC για δυναμικά μεγαλύτερα από 0.2 V. Στο κεφάλαιο 8 μελετήθηκε η αλληλεπίδραση του CO με τριμεταλλικό καταλύτη Pt-Ru-Co σε σύγκριση με εμπορικό PtRu/C. Ο τριμεταλλικός καταλύτης παρουσιάστηκε ενεργότερος, με χαμηλότερη φαινόμενη ενέργεια ενεργοποίησης για την οξείδωση ροφημένου CO, εμφανίζοντας ισχυρότερη εξάρτηση από το εφαρμοζόμενο δυναμικό. / Hydrogen is the lighter and more abundant element in nature. It is everywhere in earth, water, fossil fuels and in all the living creatures. If H2 can be properly extracted and utilized as a fuel in fuel cells, the dependence of the global economy on fossil fuels will be minimized, resulting in significant attenuation of the greenhouse gases emissions in the atmosphere. The low operation temperature of the polymer electrolyte membrane fuel cells (PEMFCs) offers a lot of advantages. In combination with the high power density yielded by the PEMFCs renders them as the main candidates for application in automotive industry. However, the low temperature raises significant problems, such as the use of noble metals for the acceleration of the basic reactions and the susceptibility in poisoning phenomena. The basic poison is carbon monoxide (CO), one of the main side-products of H2 production from fossil fuels, which for the moment is the main source of H2. In this thesis, the poisoning phenomena of the PEMFCs anode electrocatalysts from CO were investigated. Since CO is bounded on the surface of Pt stronger than the H2 fuel, its presence in the fuel feed in ppm levels deactivates the anode electrocatalyst. In order to eliminate this problem, bimetallic and ternary catalytic systems, based on Pt, were studied with the aim to reduce the Pt-CO bond strength or to promote the electrocatalytic oxidation of CO by water, which is abundant in the PEMFC environment. In chapter 1 is reported the literature information about H2 technology, such as H2 production and cleaning methods and the transport and storage infrastructure. In chapter 2, the basic thermodynamic and kinetic rules of fuel cells operation are referred together with the types of fuel cells and the possible applications. In chapter 3 the structural characteristics of the PEMFCs are outlined and the basic catalytic systems that have been studied for the fuel cell reactions are reviewed. The catalysts’ characterization methods, as well as the experimental procedures utilized in this thesis, are briefly described in chapter 4. In chapter 5 the effect of TiO2 support on the CO chemisorption’s and oxidative properties of Pt was investigated in a single PEMFC configuration. The activity of the CO electrooxidation reaction was enhanced and the Pt-CO bond was destabilized comparing to a commercial Pt/C catalyst. In chapter 6 the CO adsorption/desorption properties were studied by Infrared Spectroscopy, on a series of Pt-Mo catalysts supported on anatase TiO2. The presence of Mo oxides on the catalyst surface reduces significantly the CO desorption temperature in comparison to monometallic TiO2 supported Pt, suggesting the weak CO bonding on the catalytic surface. However, in the presence of H2, the Pt-CO bond strengthens, resulting in higher CO desorption temperature for all the catalysts tested. This was explained on the basis of competitive reaction of H2 with the oxidic surface species, originating from the TiO2 support and the surface Mo oxides. The CO electrooxidation activity of a Pt4Mo/C catalyst is described in chapter 7, considering the destabilizing effect of Mo on the Pt-CO bond. The surface Mo oxide species were able to dissociate H2O at potential values that coincide with the potential window of the PEMFC anode operation. This catalyst oxidized CO under open circuit conditions through the water gas shift reaction and at temperature as low as 60oC. However, the catalytic activity was not homogeneously distributed on the entire catalyst surface, but it was located at the Pt/MoOx interface, with the monometallic Pt sites to be strongly susceptible to CO poisoning. Furthermore, Mo was sensitive to dissolution phenomena in the hydrous acidic environment of the PEMFC for potentials higher than 0.2 V vs. rhe. Finally, in chapter 8 is described the interaction of CO with a ternary Pt-Ru-Co catalyst surface, in comparison to a commercial PtRu/C catalyst. The ternary catalyst was more active for the adsorbed CO electrooxidation, with a lower apparent activation energy than the bimetallic commercial one. The ternary catalyst exhibited zero reaction order with respect to CO partial pressure, while the PtRu/C showed negative reaction order due to competitive adsorption of CO and oxidic species for the same catalytic sites. The kinetic rate constant of the CO electrooxidation reaction for the ternary catalyst showed stronger dependence on the applied potential.

Στην παρούσα διατριβή αναπτύχθηκε ένα μοντέλο βασιζόμενο σε πρώτες αρχές με σκοπό την περιγραφή και την πρόβλεψη της πρωτονιακής αγωγιμότητας των πλήρως ενυδατωμένων μεμβρανών Nafion (το κυριότερο υλικό που χρησιμοποιείται ως ηλεκτρολύτης στις κυψέλες καυσίμου τύπου PEM) και των ιδιαίτερων χαρακτηριστικών αυτής, όπως τη γραμμική εξάρτηση από το πάχος της μεμβράνης, το δυναμικό του κελιού και τη μερική πίεση του υδρογόνου. Το μοντέλο εστιάζει στη μετανάστευση των πρωτονίων που είναι συνδεδεμένα στις σουλφονομάδες και χρησιμοποιεί την κατανομή φορτίου Poisson-Boltzmann γύρω από κάθε πρωτόνιο, σε συνδυασμό με την εξίσωση Gamow, που δίνει την πιθανότητα να συμβεί το φαινόμενο σήραγγος σε παραβολικό φράγμα δυναμικού. Προτείνεται ότι το μήκος που διανύεται κατά την πραγματοποίηση του φαινομένου σήραγγος ισούται με το μήκος κύματος του πρωτονίου και ότι κάθε πρωτόνιο περιβάλλεται από το νέφος Debye-Hückel. Το μοντέλο, που δεν εμπεριέχει προσαρμόσιμες παραμέτρους, λύνεται αναλυτικά και οι προβλέψεις του είναι σε ημιποσοτική συμφωνία με το πείραμα. Στις προβλέψεις αυτές συμπεριλαμβάνεται η τάξη μεγέθους της αγωγιμότητας, η γραμμική εξάρτηση της αγωγιμότητας με το πάχος της μεμβράνης, η εκθετική εξάρτηση από το δυναμικό και η ισχυρή εξάρτηση με τη μερική πίεση του υδρογόνου. Μελετήθηκε η κινητική, οι ταλαντώσεις και η ηλεκτροχημική ενίσχυση της οξείδωσης του CO σε καταλυτικό υμένιο Pt εναποτεθειμένο σε YSZ, χρησιμοποιώντας ως βάση την απόλυτη κλίμακα του ηλεκτροδίου του οξυγόνου. Βρέθηκε ότι η ηλεκτροχημική ενίσχυση είναι μικρή (ρ<3, Λ~300) όταν οι τιμές του δυναμικού του καταλύτη, UWR, είναι ανάμεσα σε 0.2 και 0.4 V και πολύ σημαντική (ρ~9, Λ~1500) όταν το UWR υπερβαίνει την τιμή 0.4 V. Η απότομη αλλαγή που παρατηρείται κατά την μετάβαση στην έντονη ηλεκτροχημική ενίσχυση συνοδεύεται και από απότομη αλλαγή στην κινητική της αντίδρασης και στο δυναμικό του καταλύτη. Μέσω της σύγκρισης των πειραματικών αποτελεσμάτων του κεφαλαίου και ανεξάρτητων μετρήσεων του έργου εξόδου μεταβάλλοντας το δυναμικό του καταλύτη για το ίδιο σύστημα, βρέθηκε ότι η μετάβαση οφείλεται στην έντονη μετανάστευση προωθητικών ειδών, Ο2-, από τη YSZ στην επιφάνεια του καταλύτη και την συνεπαγόμενη δημιουργία μιας πυκνής αποτελεσματικής διπλοστιβάδας στη διεπιφάνεια του καταλύτη με τα αέρια αντιδρώντα. Τέλος εξετάστηκε μια τροποποιημένη κυψέλη καυσίμου τύπου PEM η οποία λειτουργεί σε συνθήκες δηλητηρίασης από CO κατά την τριοδική λειτουργία. Στο τριοδικό κελί καυσίμου τύπου PEM εκτός της ανόδου και της καθόδου εισάγεται ένα τρίτο ηλεκτρόδιο το οποίο δημιουργεί ένα επιπλέον βοηθητικό κύκλωμα το οποίο λειτουργεί με ηλεκτρολυτικά ρεύματα και επιτρέπει τη λειτουργία της κυψέλης σε δυναμικά μεταξύ της ανόδου και της καθόδου ανέφικτα κατά τη συμβατική λειτουργία. Βρέθηκε ότι είναι δυνατό να ενισχυθεί η συνολική θερμοδυναμική ενεργειακή απόδοση όταν χρησιμοποιείται ως καύσιμο μίγμα αναμόρφωσης μεθανόλης που αντιστοιχεί σε συνθήκες έντονης δηλητηρίασης από CO. / In the present work a first principles model was developed to describe and predict the protonic conductivity of fully hydrated Nafion membranes and its peculiar non-linear dependence on membrane thickness, potential and PH2. The model focuses on the surface migration of protons between adjacent sulfonate groups and utilizes the Poisson-Boltzmann charge distribution around each proton combined with the basic Gamow equation of quantum mechanics for proton tunneling, for parabolic potential barrier. It was shown that the proton tunneling distance equals the proton wavelength and that each proton surrounded by its Debye-Hückel cloud behaves as a leaking nanobattery. The model, which contains no adjustable parameters, is solved analytically and its predictions are in semiquantitative agreement with experiment, including the magnitude of the conductivity, its linear increase with membrane thickness, its exponential increase with potential and its strong dependence on partial pressure of hydrogen. Moreover it was investigated the kinetics, rate oscillations and electrochemical promotion of CO oxidation on Pt deposited on YSZ using a standard oxygen reference electrode. It was found that electropromotion is small (ρ<3) when the catalyst potential UWR, is between 0.2 and 0.4V and very pronounced (ρ~9, Λ~1500) when UWR exceeds 0.4V. This sharp transition in the electropromotion behavior is accompanied by an abrupt change in reaction kinetics and in catalyst potential. It was shown via comparison with independent catalyst potential–catalyst work function measurements that the transition corresponds to the onset of extensive O2- spillover from YSZ onto the catalyst surface, and concomitant establishment of an effective double layer at the catalyst-gas interface, which is the cause of the highly active electropromoted state Furthermore it was studied a modified PEM fuel cell running in CO poisoning conditions by the triode operation. In addition to the anode and cathode, the triode PEM fuel cell introduces a third electrode together with an auxiliary circuit which is run in the electrolytic mode and permits fuel cell operation under previously inaccessible anode-cathode potential differences. It was found that it is possible to enhance the overall thermodynamic efficiency when it is used a methanol reformate mixture as a fuel, which corresponds to intense CO poisoning conditions.

Porous, conductive metallic nanostructures are required in several fields, such as energy conversion, low-cost sensors etc. This thesis reports on the development of an electrocatalytically active and conductive membrane for use in Polymer Electrolyte Membrane Fuel Cells (PEMFCs) and fabrication of low-cost substrates for Surface Enhanced Raman Spectroscopy (SERS). One of the main challenges facing large-scale deployment of PEMFCs currently is to fabricate a catalyst layer that minimizes platinum loading, maximizes eletrocatalytically active area, and maximizes tolerance to CO in the feed stream. Modeling the kinetics of platinum catalyzed half cell reactions occurring in a PEMFC using the kinetic theory of gases and incorporating appropriate sticking coefficients provides a revealing insight that there is scope for an order of magnitude increase in maximum current density achievable from PEMFCs. To accomplish this, losses due to concentration polarization in gas diffusion layers, which occur at high current densities, need to be eliminated. A novel catalyst design, based on a porous metallic nanostructure, which aims to overcome the limitations of concentration polarization as well as minimize the amount of platinum loading in PEMFCs is proposed. Fabrication steps involving controlled in-plane fusion of self-assembled arrays of core-shell gold-platinum nanoparticles (Au@Pt) is envisioned. The key steps involved being the development of a facile synthesis route to form Au@Pt nanoparticles with tunable platinum shell thicknesses in the 5 nm size range, the formation of large-scale 2D arrays of Au@Pt nanoparticles using guided self-assembly, and optimization of an RF plasma process to promote in-plane fusion of the nanoparticles to form porous, electrocatalytically active and electrically conductive membranes. This thesis consists of seven chapters. The first chapter provides an introduction into the topic of PEMFCs, some perspective on the current status of research and development of PEMFCs, and an outline of the thesis. The second chapter provides an overview on the methods used, characterization techniques employed and protocols followed for sample preparation. The third chapter describes the modelling of a PEMFC using the Kinetic theory of gases to arrive at an estimate of the maximum feasible current density, based on the kinetics of the electrocatalytic reactions. The fourth chapter presents the development of a simple protocol for synthesizing Au@Pt nanoparticles with control over platinum shell thicknesses from the sub monolayer coverage onwards. The results of spectroscopic and microscopic characterization establish the uniformity of coating and the absence of secondary nucleation. Chapter five describes the formation of a nanoporous, electrocatalytically active membrane by self-assembly to form bilayers of 2D arrays of Au@Pt nanoparticles and subsequent fusion using an RF plasma based process. The evolution of the electrocatalytic activity and electrical conductivity as a function of the duration of RF plasma treatment is monitored for Au@Pt nanoparticles with various extent of platinum coating. Spectroscopic, microscopic, electrical and cyclic voltammetry characterization of the samples at various stages were used to understand the structural evolution with RF plasma treatment duration and discussed. Next durability studies were carried out on the nanoporous, Au@Pt bilayer nanoparticle array with an optimum composition of Pt/Au atomic ratio of 0.88 treated to 16 minutes of argon plasma exposure. After this the novel catalyst membrane design of PEM fuel cell is revisited. Two different techniques are proposed so that the thin, nanoporous, metallic catalyst membrane achieves horizontal electronic resistance equivalent to that of the conventional gas diffusion layer with catalyst layer. The first technique proposes the introduction of gold coated polymeric mesh in between the thin, nanoporous, metallic catalyst membrane and bipolar plate and discusses the advantages. Later the gold coated polymeric mesh is introduced in a conventional membrane electrode assembly and efficiency of the polarization curves probed with and without the introduction of gold coated polymeric mesh. The second technique describes the results of fabrication of a nanoporous metallic membrane using multiple layers of 2D Au@Pt nanoparticle arrays at an optimum composition of Pt/Au atomic ratio of 0.88 to reduce the horizontal electronic resistance. Preliminary studies on the permeability of water through such membranes supported on a porous polycarbonate filter membrane are also presented. In chapter six, a simple reactive inkjet printing process for fabricating SERS active silver nanostructures on paper is presented. The process adapts a simple room temperature protocol, using tannic acid as the reducing agent, developed earlier in our group to fabricate porous silver nanostructures on paper using a commercial office inkjet printer. The results of SERS characterization, spectroscopic and microscopic characterizations of the samples and the comparison of the substrate’s long-term performance with respect to a substrate fabricated using sodium borohydride as the reducing agent is discussed. Preliminary findings on attempts to fabricate a conductive silver network using RF plasma induced fusion area also presented. Chapter seven provides a summary of the results, draws conclusions and a perspective on work required to accomplish the goals of incorporating the porous metallic nanostructures into PEMFCs.