The ever increasing demand for a clean and renewable energy source has stimulated research for alternatives for the use of fossil fuels, which contribute significantly to global warming. The SO2 oxidation reaction was studied for production of hydrogen as a clean and renewable energy carrier. This reaction occurs at a lower standard electrode potential (0.158 V vs. SHE) than normal water electrolysis (1.23 V vs. SHE). This is a theoretical indication that the SO2 oxidation reaction has possible potential when compared to normal water electrolysis, since hydrogen production may occur at lower potentials and therefore lower cost. Rh was compared with Pt for the SO2 oxidation reaction since little research has been done on this catalyst and many studies exist in which Pt was used as catalyst. The oxygen reduction reaction and ethanol oxidation reaction were also included in this study to create a foundation for the catalysts studied, since the SO2 oxidation reaction is complicated by different adsorbed species that can form according to various mechanisms. The electrochemical techniques employed in this study to characterize the catalysts included cyclic voltammetry from which onset potentials and limiting current densities were determined, as well as from which some qualitative analysis was done. Linear polarization experiments were used during rotating disk electrode studies from which Levich and Koutecky-Levich analyses were done and the number of electrons transferred calculated and compared between the two catalysts. From the Koutecky-Levich analysis the kinetic current density was also obtained for use in Tafel analysis for further comparison between catalysts. It was found that Rh showed good behaviour for the oxygen reduction reaction when compared to Pt with similar onset potentials and limiting current densities. From Levich analysis it was concluded that both catalysts achieved diffusion limitation at high overpotentials. However, from the calculated number of electrons transferred it was evident that a difference in mechanism existed between catalysts and that the mechanism for both changed in the potential range studied, which is confirmed by the Tafel slopes. For the ethanol oxidation reaction it was shown that Rh exhibited very low catalytic activity in comparison with Pt. However, it was concluded from cyclic voltammetry and rotating disk electrode studies that more adsorbed species were present on the surface of Rh than on Pt. These results confirmed the possibility of using Rh as a co-catalyst together with Pt since it was shown from rotating disk electrode studies that low adsorption of ethanol and its oxidation products caused species to be transported away from the surface of the electrode during rotation. For the SO2 oxidation reaction it was found that Rh exhibited very poor catalytic activity together with being very susceptible to poisoning by adsorbed species. Pt showed very good behaviour, which corresponded well with what had been observed in literature. Levich analysis revealed that Pt did not exhibit diffusion limitation and Koutecky-Levich analysis revealed that a 2 electron reaction occurred on Pt, which corresponds with the SO2 oxidation reaction during which 2 electrons are transferred. It was, therefore, shown that Rh could exhibit good behaviour and act as a suitable catalyst in certain circumstances. However, for the SO2 oxidation reaction, which was the main focus of this study it was shown that Rh is not a suitable catalyst, either alone or as co-catalyst. / MSc (Chemistry), North-West University, Potchefstroom Campus, 2014

The ever increasing demand for a clean and renewable energy source has stimulated research for alternatives for the use of fossil fuels, which contribute significantly to global warming. The SO2 oxidation reaction was studied for production of hydrogen as a clean and renewable energy carrier. This reaction occurs at a lower standard electrode potential (0.158 V vs. SHE) than normal water electrolysis (1.23 V vs. SHE). This is a theoretical indication that the SO2 oxidation reaction has possible potential when compared to normal water electrolysis, since hydrogen production may occur at lower potentials and therefore lower cost. Rh was compared with Pt for the SO2 oxidation reaction since little research has been done on this catalyst and many studies exist in which Pt was used as catalyst. The oxygen reduction reaction and ethanol oxidation reaction were also included in this study to create a foundation for the catalysts studied, since the SO2 oxidation reaction is complicated by different adsorbed species that can form according to various mechanisms. The electrochemical techniques employed in this study to characterize the catalysts included cyclic voltammetry from which onset potentials and limiting current densities were determined, as well as from which some qualitative analysis was done. Linear polarization experiments were used during rotating disk electrode studies from which Levich and Koutecky-Levich analyses were done and the number of electrons transferred calculated and compared between the two catalysts. From the Koutecky-Levich analysis the kinetic current density was also obtained for use in Tafel analysis for further comparison between catalysts. It was found that Rh showed good behaviour for the oxygen reduction reaction when compared to Pt with similar onset potentials and limiting current densities. From Levich analysis it was concluded that both catalysts achieved diffusion limitation at high overpotentials. However, from the calculated number of electrons transferred it was evident that a difference in mechanism existed between catalysts and that the mechanism for both changed in the potential range studied, which is confirmed by the Tafel slopes. For the ethanol oxidation reaction it was shown that Rh exhibited very low catalytic activity in comparison with Pt. However, it was concluded from cyclic voltammetry and rotating disk electrode studies that more adsorbed species were present on the surface of Rh than on Pt. These results confirmed the possibility of using Rh as a co-catalyst together with Pt since it was shown from rotating disk electrode studies that low adsorption of ethanol and its oxidation products caused species to be transported away from the surface of the electrode during rotation. For the SO2 oxidation reaction it was found that Rh exhibited very poor catalytic activity together with being very susceptible to poisoning by adsorbed species. Pt showed very good behaviour, which corresponded well with what had been observed in literature. Levich analysis revealed that Pt did not exhibit diffusion limitation and Koutecky-Levich analysis revealed that a 2 electron reaction occurred on Pt, which corresponds with the SO2 oxidation reaction during which 2 electrons are transferred. It was, therefore, shown that Rh could exhibit good behaviour and act as a suitable catalyst in certain circumstances. However, for the SO2 oxidation reaction, which was the main focus of this study it was shown that Rh is not a suitable catalyst, either alone or as co-catalyst. / MSc (Chemistry), North-West University, Potchefstroom Campus, 2014

A novel study on the investigation of three very common atmospheric sulphur species relevant to the Mpumalanga Highveld subregion was conducted. Long-term in situ measurements were applied in the diurnal and seasonal evaluation of the observed sulphur species. Ambient pollutant concentrations and surface meteorological data were collected at an air quality monitoring station at Elandsfontein. Elandsfontein air quality monitoring station was ideal for the observations due to its high elevation within the Mpumalanga Province surrounded by few rolling hills and negligible windbreaks which easily allows for extensive plume-contact with the surface during convective daytime mixing. The temporal characteristics of the sulphur species have been assessed relative to one another with varying meteorological conditions. The diurnal and seasonal concentration variations were used to describe the physical characteristics exhibited by the compounds over Elandsfontein. Pollution roses were used to target the source of the major release points and areas of these sulphur species relative to the Elandsfontein monitoring station. Gas and particle concentrations were analysed in relation to varying meteorological parameters with a view to ascertaining the sulphur transformation and concentration distribution in the planetary boundary layer. Particulate sulphate distribution has been modelled through multivariate regression analyses in relation to three meteorological parameters, namely, wind speed, relative humidity and ambient temperature for the various seasons observed over southern Africa. This study has shown that hydrogen sulphide, sulphur dioxide and sulphate species are present throughout the year in the Mpumalanga Highveld at notably significant levels. The presence of ambient particulate sulphate has been shown to result from the combination of chemical interactions during long-range aerosol transport; atmospheric recirculation processes shown from back trajectories over the southern Africa sub-region, as well as the variation in the removal mechanisms and rates for the different seasons throughout the year. These transport and removal processes all contribute to the overall sulphur mass balance in the planetary boundary layer. Dosage of the three sulphur species was evaluated to provide data for sulphur pollution loading that could form a basis for health and vii environmental impact assessments over the area. In view of the characteristic patterns displayed by particulate sulphate, multivariate mathematical models have been developed on a seasonal basis with variations in meteorological parameters. This was seen to predict an accuracy of up to 70 % of the particulate sulphate loading for different seasons over the South African Highveld. In order to understand the chemical interactions of atmospheric sulphur species, it is important to be able to predict the route taken and expected products of transformation on any given condition. Theoretical analyses of the chemical thermodynamic properties of the known reacting species and a well-established approach were used in predicting reaction paths and establishing the possible and feasible products of chemical transformation in relation to the ambient temperature. The determination of reaction paths and possible products of chemical transformation provides a measure of the relative importance of the reacting species and the mechanism of reaction. Gas-, aqueous-phase and radical reactions involving sulphur (IV) were investigated with a view to establishing their relative importances. Thermochemical properties of several sulphur-containing compounds not available in the literature have been generated for evaluation of Gibbs free energy (ΔG) and enthalpy (ΔH). An electronic energy structural approach has been applied to model for ΔG and ΔH of 88 sulphur species in 90 chemical reactions comprising gas-phase, aqueousphase and radical reactions. Modelling was evaluated for their relative importances over a temperature range of –100 °C to +100 °C. The temperature range is well above the known tropospheric temperature range to account for variations in the atmospheric environment. To further comprehend the chemistry of sulphur with regards to distribution of the species in the atmosphere, a kinetic model is developed and incorporated into a dispersion model. The kinetic evaluation of the oxidation rate of SO2 to sulphate has been determined with advection and dispersion over the Elandsfontein area. Gas-phase transformation with advection and dispersion has been used to evaluate the extent of the distribution of SO2 relative to the major contributing sources. The dry deposition was considered to be the dominant removal mechanism. It was assumed that the reaction rate was second order in concentration and that the rate of deposition was first order. The oxidation rates obtained for the seasons were 10.9 % h-1 for summer; 8.83 % h-1 for autumn; 6.56 % h-1 for winter; viii 10.8 % h-1 for spring, while an overall rate of 9.6 % h-1 was obtained for the one year study period. The transformation rate model produced a reaction constant and an activation energy of 4.92 x 10-6 μg m-3 s-1 and 36.54 kJ kg-1 for summer; 3.939 x 10-6 μg m-3 s-1 and 43.89 kJ kg-1 for autumn; 2.90 x 10-6 μg m-3 s-1 and 115.69 kJ kg-1 for winter; 4.82 x 10-6 μg m-3 s-1 and 43.29 kJ kg-1 for spring, while for the year 4.29 x 10-6 μg m-3 s-1 and 34.31 kJ kg-1. A Gaussian puff unsteady state Lagrangian dispersion model with reflection at the surface and inversion layer was applied for concentration diffusion. The Lagrangian dispersion model with dry deposition was a better prediction of the observed data than the models from previous studies using a first order rate constant with or without deposition rate.

Η ηλεκτροχημική ενίσχυση της κατάλυσης (EPOC ή αλλιώς μη-φαρανταϊκή τροποποίηση της καταλυτικής ενεργότητας, φαινόμενο NEMCA) είναι ένα φαινόμενο όπου εφαρμογή μικρών ρευμάτων ή δυναμικών (±2V) σε ένα καταλύτη που είναι υποστηριγμένος σε ένα ηλεκτρολύτη, ιοντικό ή μικτό ιοντικό-ηλεκτρονικό αγωγό, μπορεί να επιφέρει τροποποιήσεις στην καταλυτική ενεργότητα αλλά και εκλεκτικότητα, με τρόπο ελεγχόμενο, αντιστρεπτό και έως ένα βαθμό προβλέψιμο. Η ηλεκτροχημική ενίσχυση έχει βρεθεί, με χρήση διαφόρων τεχνικών, ότι πηγάζει από την ηλεκτροχημικά ελεγχόμενη παροχή ενισχυτικών ιοντικών ειδών από το φορέα-ηλεκτρολύτη στα καταλυτικά σωματίδια. Στο πρώτο κεφάλαιο της παρούσας διατριβής γίνεται μια εκτεταμένη αναφορά στους στερεούς ηλεκτρολύτες, στις ιδιότητες τους και τους τομείς στους οποίους χρησιμοποιούνται με ιδιαίτερη σημασία στη σταθεροποιημένη με οξείδιο του υττρίου ζιρκονία (YSZ), που αποτελεί ένα πολύ συχνά χρησιμοποιούμενο αγωγό ιόντων οξυγόνου. Επίσης, εισάγονται οι έννοιες της μετανάστευσης (spillover) και της αντίστροφης μετανάστευσης (backspillover), οι οποίες χρησιμοποιούνται στην ερμηνεία και την κατανόηση του φαινομένου της ηλεκτροχημικής ενίσχυσης και των αλληλεπιδράσεων μετάλλου-φορέα (MSI). Στο δεύτερο κεφάλαιο γίνεται εισαγωγή στις γενικές αρχές του φαινομένου της ηλεκτροχημικής ενίσχυσης όπου παρουσιάζονται μερικά παραδείγματα εφαρμογής του και γίνεται ανασκόπηση όλων των εργασιών που έχουν εμφανιστεί στη βιβλιογραφία και αφορούν στο συγκεκριμένο φαινόμενο. Συζητείται, επίσης, η μελέτη του φαινομένου με χρήση διαφόρων πειραματικών τεχνικών, όπως ηλεκτροκινητικών πειραμάτων δυναμικής απόκρισης, μετρήσεων έργου εξόδου, κυκλικής βολταμμετρίας, XPS, TPD και STM, καθώς και θεωρητικών μελετών, με σκοπό την κατανόηση της αρχής του φαινομένου σε ατομικό επίπεδο καθώς και την επίλυση σημαντικών προβλημάτων που αφορούν στην ετερογενή κατάλυση. Με βάση τα αποτελέσματα από τις ανωτέρω μελέτες, παρουσιάζεται το μαθηματικό μοντέλο που έχει αναπτυχθεί και εξηγεί τα παρατηρούμενα φαινόμενα σε μοριακό επίπεδο καθώς και οι πρόσφατα εδραιωμένοι κανόνες που το διέπουν. Στο τρίτο κεφάλαιο παρουσιάζεται η αξιοποίηση του φαινομένου της ηλεκτροχημικής ενίσχυσης στην αντιμετώπιση ενός εκ των δυσκολότερων και προκλητικότερων προβλημάτων της ετερογενούς κατάλυσης που είναι η αναγωγή του μονοξειδίου του αζώτου (ΝΟ) από αιθυλένιο παρουσία υψηλής περίσσειας (10%) οξυγόνου. Στην μελέτη χρησιμοποιήθηκε ένας πρόσφατα ανεπτυγμένος και βελτιωμένος για την παρούσα διατριβή, μονολιθικός ηλεκτροχημικά ενισχυόμενος αντιδραστήρας (monolithic electrochemically promoted reactor, MEPR) εξοπλισμένος με 22 ηλεκτροχημικά καταλυτικά στοιχεία του τύπου Rh/YSZ/Pt με μικρό πάχος ηλεκτροδίων (~40 nm). Βρέθηκε, δε, ότι η βέλτιστη λειτουργία επιτυγχάνεται σε χαμηλές θερμοκρασίες (220-240οC) με σημαντική ηλεκτροχημική ενίσχυση ακόμα και κάτω από τις ανωτέρω ισχυρά οξειδωτικές συνθήκες (λόγος αέρα-καυσίμου=16.7, περίσσεια οξυγόνου=9.43). Σε αυτό το στενό θερμοκρασιακό εύρος η εκλεκτικότητα προς Ν2 που επετεύχθη από τα Rh/YSZ/Pt ηλεκτροκαταλυτικά στοιχεία, είναι περίπου 100% ενώ η παραγωγή των ανεπιθύμητων CO, ΝΟ2, Ν2Ο ήταν σχεδόν μη-ανιχνεύσιμη. Στο τέταρτο κεφάλαιο μελετάται η χρήση λεπτών καταλυτικών ηλεκτροδίων Pt σκελετικής δομής (Pt-skeletal/YSZ/Au) στην έκταση του φαινομένου της ηλεκτροχημικής ενίσχυσης, χρησιμοποιώντας την πρότυπη αντίδραση οξείδωσης αιθυλενίου, στον μονολιθικό ηλεκτροχημικά ενισχυόμενο αντιδραστήρα. Βρέθηκε ότι και τέτοιου τύπου ηλεκτρόδια – καταλυτικά υμένια είναι ιδιαίτερα καταλυτικά ενεργά και είναι δυνατό να ενισχυθούν ηλεκτροχημικά σε μεγάλο βαθμό. Επίσης, ο αντιδραστήρας λειτούργησε επιτυχώς και παρατηρήθηκε ηλεκτροχημική ενίσχυση, υπό υψηλές ογκομετρικές παροχές (25 l/min), με ταχύτητες χώρου αντιδραστήρα που είναι κοντά σε αυτές που λειτουργούν οι βιομηχανικοί αντιδραστήρες (12000 h-1). Στο πέμπτο κεφάλαιο παρουσιάζεται η ηλεκτροχημική ενίσχυση της αντίδρασης υδρογόνωσης του CO2 με στόχο την παραγωγή μεθανίου χρησιμοποιώντας ηλεκτροχημικά στοιχεία του τύπου Rh/YSZ/Pt. Βρέθηκε ότι η αντίδραση μπορεί να ενισχυθεί σε μεγάλο βαθμό και επιπλέον να τροποποιηθεί και η εκλεκτικότητά της σε CΗ4 που είναι και το επιθυμητό προϊόν. Στο έκτο κεφάλαιο παρουσιάζεται η μελέτη της αντίδραση οξείδωσης του SO2 προς SO3, μιας πολύ σημαντικής αντίδρασης από βιομηχανική (παραγωγή H2SO4) αλλά περιβαλλοντική άποψη, με χρήση του φαινομένου της ηλεκτροχημικής ενίσχυσης, σε λεπτά (~40 nm) ηλεκτροχημικά στοιχεία του τύπου Pt/YSZ/Au. Βρέθηκε πως ηλεκτροχημική ενίσχυση μπορεί να επιτευχθεί ακόμα και σε πολύ υψηλές ογκομετρικές παροχές (30 l/min), όπου αντιστοιχούν σε ταχύτητες χώρου αντιδραστήρα (14000 h-1) πολύ κοντά σε αυτές που λειτουργούν οι βιομηχανικοί αντιδραστήρες και να επιτευχθούν σχετικά υψηλές μετατροπές SO2. / Electrochemical Promotion of Catalysis (EPOC or Non-Faradaic Electrochemical Modification of Catalytic Activity, NEMCA effect) is a phenomenon where the application of small currents or potentials (±2V) alters the activity and selectivity of catalysts supported on ionic or mixed ionic-electronic conductors and modifies the catalytic activity and selectivity, in a controllable, reversible and to some extend predictable manner. As shown by numerous surface science techniques, including STM, electrochemical promotion is due to electrochemically controlled migration (backspillover) of promoting or poisoning ionic species (Oδ- in the case of YSZ) between the ionic or mixed ionic-electronic conductor and the gas exposed catalytic surface. The utilization of electrochemical promotion of catalysis, in order to tackle one of the most difficult and challenging problems of heterogeneous catalysis, which is the NO reduction under high excess oxygen (10%), has been performed. This gas mixture is a typical mixture in a lean-burn engine (or Diesel engine) exhaust. In this study, a recently developed and improved monolithic electrochemically promoted reactor (MEPR) has been used, equipped with 22 thin (~40 nm catalyst-electrode thickness) electrochemical catalytic elements Rh/YSZ/Pt type. It was found that there is an optimum operation temperature of the reactor, in the range from 220oC to 240oC, where the maximum electropromotion effect occurs, even under these extremely oxidizing conditions (air/fuel ratio = 16.7 and oxygen excess = 9.43%). In this narrow temperature window the selectivity to N2 was almost 100% since the production of the undesired N2O and NO2 was almost undetectable. Also, the use of thin catalytic Pt electrodes with skeletal structure (Ptskeletal/ YSZ/Au) was examined in the MEPR for the model reaction of C2H4 oxidation. It was found that such skeletal structure electrodes are catalytically active and can be electropromoted even under high gas flow rates (25 l/min) or high space velocity (HSV~12000 h-1), close to those that the industrial reactors operate. The electrochemical promotion of the CO2 hydrogenation reaction was also examined, towards methane production using Rh/YSZ/Pt type electrochemical catalytic elements. It was found that the reaction rates can be enhanced and similarly the selectivity to CH4 which found to increase upon polarization. Finally, the effect of electrochemical promotion was examined in the study of the SO2 oxidation to SO3 reaction, which is a very important reaction by industrial (H2SO4 production) and environmental point of interest. The monolithic reactor was equipped with 5 or 22 thin (~40 nm) Pt/YSZ/Au type electrocatalytic elements. It was found that electrochemical promotion can be obtained by positive polarization even under high hourly space velocities (14000 h-1), close to those that the industrial reactors operate, with relatively high SO2 conversions.

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.