Acrolein is an indispensable chemical intermediate with a rising demand in recent years. The concern of the increase of propylene prices due to the shrinking supply of nonrenewable crude oil makes the acid-catalyzed gas-phase glycerol dehydration to acrolein a prime candidate for research. Our analysis showed that the sustainable acrolein production from glycerol was both technically and economically viable. Alumina2700® (Al) and Silica1252® (Si) loaded with silicotungstic acid (HSiW) possessed distinct features while provided equally good acrolein yield (73.86mol% and 74.05mol%, respectively) optimally. Due to the unique non-equilibrium characteristics, non-thermal plasma (NTP) could promote a variety of chemical reactions; however, its application in a dehydration process remained blank. This study used the reaction of glycerol dehydration to acrolein to probe whether NTP could 1) improve acrolein yield during dehydration, 2) suppress the coke formation and regenerate the catalyst, and 3) modify the properties of the catalyst. The dielectric barrier discharge configuration was used to generate NTP; various NTP field strengths and also their interaction with temperature and the catalyst were investigated. The results showed that NTP improved the glycerol conversion and that NTP with a proper field strength increased acrolein selectivity. The optimal acrolein yields of 83.6 mol% and 83.1 mol% were achieved with 3.78 kV/cm NTP and 4.58 kV/cm NTP at 275°C for HSiW-Al and HSiW-Si, respectively. The application of NTP-O2 (5% oxygen in argon, 4.58 kV/cm) during glycerol dehydration significantly suppressed coke formation on HSiW-Si. NTP-O2 could regenerate the deactivated HSiW-Si at low temperatures by removing both soft and hard coke at various rates. NTP-O2 with higher field strength, at medium operation temperature (150ºC) and in argon atmosphere was more effective for coke removal/catalyst regeneration. Applying NTP to the catalyst fabrication showed some capabilities in modifying catalyst properties, including enlarging surface area, preserving mesopores, increasing acid strength and Brønsted acidity. NTP with argon as the discharge gas performed better in these modifications than NTP with air as the discharge gas.

Bacterial spores have remarkable resistance to a variety of harsh conditions, causing spoilage in food industry and becoming the primary bacterial agent in biowarfare and bioterrorism. In this study, inactivation mechanisms of Bacillus amyloliquefaciens (BA) spores by non-thermal plasma (NTP) were investigated by using Fourier-transform infrared spectroscopy (FTIR) as a major tool to exam spores after NTP treatment. Chemometric techniques, such as multivariate classification models based on soft independent modeling of Class Analogy (SIMCA) and Principal Component Analysis (PCA), were employed to identify functional group changes in FTIR spectra. The IR absorbance bands correlated to dipicolinic acid (DPA) decreased after NTP treatment indicating that DPA released and then reacted with reactive species generated by NTP and it was confirmed by nuclear magnetic resonance (NMR). Also IR absorbance bands corresponding to protein structure changed. FTIR combined with UV-Vis spectroscopy was used to monitor spore germination. Large amount of DPA released in a short time when spores germinated at 50°C, showing that DPA released in response to heating. NTP treated spores could germinate with little DPA release due to sub-lethal effects induced by plasma. Also an empirical model based on Weibull distribution was established to describe the spore germination process showing that NTP treated spores exhibited abnormal germination pattern. Inactivation mechanisms of NTP with air as feed gas was compared with high-pressure, wet heat, chemical treatment using chlorine dioxide (CD) and NTP with argon as feed gas. The results showed that few chemical changes in spores after autoclave and high pressure treatments, though protein structure changed. CD and NTP with air as feed gas inactivated spores by oxidation. DPA released after NTP with argon as feed gas treatment and it is possible that UV and charged particles accounts for the inactivation. This study provides in depth insight into the inactivation mechanism of NTP and information for optimizing NTP process.

This dissertation was undertaken to study two different subjects both related to molecular decomposition by applying a shock tube and non-thermal plasma to decompose selected hydrocarbons. The first approach to molecular decomposition concerned thermal decomposition and oxidation of highly diluted nitromethane (NM) in a shock tube. Reflected shock tube experiments on NM decomposition, using mixtures of 0.2 to 1.5 vol% NM in nitrogen or argon were performed over the temperature range 850-1550 K and pressure range 190-900 kPa, with 46 experiments diluted in nitrogen and 44 diluted in argon. By residual error analysis of the measured decomposition profiles it was found that NM decomposition (CH3NO2 + M -> CH3 + NO2 + M, where M = N2 /Ar) corresponds well to a law of first order. Arrhenius expressions corresponding to NM diluted either in N2 or in Ar were found as kN2 = 1017.011×exp(-182.6 kJ/mole / R×T <cm3/mole×s> and kAr = 1017.574×exp(-207 kJ/mole / R×T )<cm3/mole×s>, respectively. A new reaction mechanism was then proposed, based on new experimental data for NM decomposition both in Ar and N2 and on three previously developed mechanisms. The new mechanism predicts well the decomposition of NM diluted in both N2 and Ar within the pressure and temperature range covered by the experiments. In parallel to, and following the decomposition experiments, oxidative experiments on the ignition delay times of NM/O2/Ar mixtures were investigated over high temperature and low to high pressure ranges. These experiments were carried out with eight different mixtures of gaseous NM and oxygen diluted in argon, with pressures ranging between 44.3-600 kPa, and temperatures ranging between 842-1378 K. The oxidation experiments were divided into different categories according to the type of decomposition signals achieved. For signals with and without emission, the apparent quasi-constant activation energy was found from the correlations, to be 64.574 kJ/mol and 113.544 kJ/mol, respectively. The correlations for the ignition delay for time signals with and without emission were deduced as τemission = 0.3669×10-2×[NM]-1.02[O2]-1.08×[Ar]1.42×exp(7767/T) and τno emission = 0.3005×10-2×[NM]-0.28[O2]0.12×[Ar]-0.59×exp(13657/T), respectively. The second approach to molecular decomposition concerned the application of non-thermal plasma to initiate reactions and decompose/oxidize selected hydrocarbons, methane and propane, in air. Experiments with a gliding arc discharge device were performed at the university of Orléans on the decomposition/reforming of low-to stoichiometric concentration air/CH4 mixtures. The presented results show that complete reduction of methane could be obtained if the residence time in the reactor was sufficiently long. The products of the methane decomposition were mainly CO2, CO and H2O. The CH4 conversion rate showed to increase with increasing residence time, temperature of the operating gas, and initial concentration of methane. To achieve complete decomposition of CH4 in 1 m3 of a 2 vol% mixture, the energy cost was about 1.5 kWh. However, the formation of both CO and NOx in the present gliding discharge system was found to be significant. The produced amount of both CO (0.4-1 vol%) and NOx (2000-3500 ppm) were in such high quantities that they would constitute an important pollution threat if this process as of today was to be used in large scale CH4 decomposition. Further experimental investigations were performed on self-built laboratory scale, single- and double dielectric-barrier discharge devices as a means of removing CH4 and C3H8 from simulated reactive inlet mixtures. The different discharge reactors were all powered by an arrangement of commercially available Tesla coil units capable of high-voltage high-frequency output. The results from each of the different experiments are limited and sometimes only qualitative, but show a tendency that the both CH4 and C3H8 are reduced in a matter of a 3-6 min. retention time. The most plausible mechanism for explaining the current achievements is the decomposition by direct electron impact.

La découpe de wafers génère des quantités importantes de déchets de silicium de grade solaire qui ne sont pas revalorisés actuellement à cause de la contamination lors du procédé de découpe. Les travaux présentés dans ce manuscrit portent sur l’étude de la purification de déchets de silicium solaire à l’aide d’un procédé assisté par une torche à plasma d’arc non transféré. Cette étude a été menée selon une double approche numérique et expérimentale. Les calculs numériques ont été réalisés à l’aide d’un code de calcul de mécanique des fluides. Ils sont utilisés pour dimensionner la configuration expérimentale et pour comprendre l’influence des paramètres opératoires sur l’écoulement gazeux et le traitement des particules. L’étude expérimentale a consisté à ’injecter des déchets pulvérulents de silicium (sciures de silicium, poudre de concassage) dans un jet de plasma sous atmosphère contrôlée puis à les collecter dans un creuset chaud. La désoxydation et la décarburation de déchets de silicium, notamment de la sciure issue de la découpe des wafers, a été mise en évidence à l’aide du procédé développé. Toutefois, l’élimination des impuretés métalliques dans les sciures de silicium n’a pas été démontrée lors de cette étude. Les résultats expérimentaux et numériques ont mis en évidence que la désoxydation est améliorée avec un jet de plasma lent ainsi qu’avec une teneur en air résiduelle limitée dans la zone de traitement. La carboréduction de la silice ainsi que la volatilisation de la silice par oxydation du silicium semblent être les deux mécanismes de purification mis en jeu lors du procédé. / Wafer manufacturing produces large amounts of solar-grade silicon waste that is not currently recovered because of its contamination during the slicing process. This work deals with the purification of silicon waste using a non-transferred arc plasma process. It was carried out by using a double approach combining numerical simulations and experiments. The former were done using a computational fluid dynamics (CFD) code and made it to size the experimental configuration and understand the effect of process parameters on gas flow fields and powder treatment. The experimental study consisted in injecting powdered silicon waste (sawdust silicon, crushed powder) into the plasma jet under controlled atmosphere and collecting the treated material in a hot crucible. Decarburization and deoxidation of silicon waste, including sawdust resulting from wafer slicing, was achieved by the developed method. However, the removal of metal impurities in silicon sawdust was not demonstrated in this study. The experimental and numerical results showed that deoxidation was improved with a low-velocity plasma jet and limited air content in the area of treatment. Silica carboreduction and silica volatilization by silicon oxidation seemed to be the two mechanisms involved in the purification process.

Ce travail porte sur l’étude de la propagation de décharges couronnes impulsionnelles à pression atmosphérique dans les milieux poreux et/ou alvéolaires. Face à la complexité des phénomènes mis en jeu, liés aux interactions entre la décharge et les surfaces du matériau qui la confine, nous proposons l’étude de décharges confinées par des structures élémentaires. L’étude du confinement radial des décharges, assuré par un large panel de capillaires, a été réalisée. Des diagnostics électriques et optiques de pointe permettent d’étudier la propagation de la décharge au sein des différents capillaires. La corrélation entre ces diagnostics a même permis des mesures de vitesse de propagation au sein de capillaires opaques. Les résultats montrent que la propagation de la décharge dépend grandement de la géométrie des capillaires et des paramètres électriques de génération de la décharge. Dans le cas de sections carrées ou rectangulaires, les arêtes induisent un renforcement local du champ qui attire la décharge. Dans le cas de capillaires cylindriques, le diamètre interne est le paramètre crucial qui détermine aussi bien la structure de la décharge que sa vitesse de propagation. Quelle que soit la nature du capillaire, la propagation présente alors une vitesse optimale à tout autre paramètre constant pour une valeur donnée du diamètre interne. Dans le cas du verre, la vitesse est maximale pour un diamètre interne de 200 µm. L’épaisseur et la permittivité diélectrique du capillaire possèdent également une influence sur la propagation de la décharge radialement confinée. Ainsi, diminuer l’épaisseur ou la permittivité diélectrique engendre une accélération de la décharge. Si l’épaisseur est très faible, la décharge peut même se déconfiner pour se propager à l’extérieur du capillaire. Une étude spectroscopique complémentaire montre que la réduction du diamètre de confinement implique une augmentation de la température du plasma, ce qui pourrait contribuer à l’obtention de ce profil de vitesse en fonction du diamètre de confinement. L’étude du confinement axial des décharges a ensuite été réalisée en insérant des membranes de différentes natures et caractéristiques, perpendiculairement à l’axe pointe plan. Les résultats montrent que la décharge présente une propagation en trois étapes : pointe/membrane, radialement au voisinage de la membrane, puis membrane/plan. Dans cette étude, nous avons mis en évidence l’importance du critère poreux ou non de la membrane. Dans le cas poreux, la propagation de la décharge dans l’ensemble du gap est continue, même pour des pores de l’ordre de la dizaine de µm. Dans le cas non poreux, la propagation est discontinue, et il est nécessaire pour assurer la propagation dans l’ensemble du gap qu’un ré-allumage ait lieu de l’autre côté de la membrane. Après l’instant de l’impact sur la membrane, la décharge marque un arrêt qui correspond à la réorganisation des charges et à la restructuration du champ électrique dans le gap. Elle se propage ensuite radialement au voisinage de la membrane en plusieurs fronts d’ionisation. Si les conditions de claquage sont réunies dans le volume membrane/plan, alors un ré-allumage apparaît à partir de la membrane pour atteindre le plan. L’étude de ces ré-allumages semble montrer l’importance de la position de la membrane au sein de l’espace inter-électrodes et de la dynamique des charges aux surfaces de la membrane. Plus on diminue la distance membrane/plan, plus il est facile d’en observer. Nous montrons également que la diminution de la permittivité diélectrique de la membrane ou l’augmentation de son épaisseur, semble augmenter la probabilité de ces ré-allumages. Dans le cas poreux, nous avons également mis en évidence l’influence de la taille des pores de la membrane sur l’ensemble des étapes de propagation. Lorsque la porosité est inférieure à 100 µm la propagation de la décharge est ralentie du fait de la difficulté de la décharge à traverser directement le matériau. / This study is an attempt to understand the mechanisms involved in the propagation of pulsed corona discharges at atmospheric pressure inside porous and/or alveolar media. Due to the complexity of these phenomena which hardly depends on plasma/surface interactions, the study was focused first on the propagation inside basic structures of confinement, before doing it in more complex media, such as monolithic cordierites or foams. Therefore, capillaries have been used to radially confine the discharge propagation. Thanks to highly resolved optical and current diagnostics, we succeed in describing precisely the propagation. A correlation of these diagnostics allowed us to measure propagation velocity inside opaque media. Results show that geometry is the key parameter which both governs the discharge structure and the propagation velocity. Electrical parameters of the discharge ignition have a great role in the propagation also. In case of square and rectangular capillaries, the local electric field enhancement due to edges attracts the discharge. In case of round capillaries, the internal diameter becomes the key parameter which governs the pattern of the discharge and its velocity. Whatever the kind of capillary used, the velocity of propagation shows an optimal value for a given internal diameter, at all others parameters constants. In case of glass capillaries, this maximum value is obtained for a 200 µm internal diameter. Parameters such as wall thickness or dielectric permittivity have also an influence on the propagation velocity. The decrease of the thickness or the dielectric permittivity implies an increase of the propagation velocity. If the thickness is small enough, we observe that the discharge is able to propagate outside the tube. A complementary spectroscopic study of that kind of discharge shows that the plasma temperature depends on the internal diameter, and warming observed for smallest internal diameters could contribute to the internal diameter/velocity of propagation relation. The study of the axial confinement of the propagation of the discharge has been made thanks to different kinds of dielectric membranes, perpendicularly inserted between the electrodes. Results show that the propagation of the discharge is a three step process: tip to membrane propagation, radial propagation near the membrane surfaces, and membrane to plane propagation under specific conditions. The porous feature of the membrane has a key role in the propagation. In case of porous membranes, the whole propagation in the gap is continuous, even for the smallest porosities under investigations (~10µm). In case of non porous films, the propagation by three step processes is no more continuous, and the propagation in the entire gap needs a re-ignition of the discharge on the other side of the membrane. After its impact on the membrane, the discharge stops on the dielectric while the charges and the electric field are self reorganized. Then a radial propagation of several ionization waves starts near the membrane surface. If the disruptive voltage is reached behind the obstacle, a re-ignition could occur in the membrane/plane gap and reach the cathode. Investigation on these reignition conditions shows that the key parameters seem to be the position of the membrane inside the gap and the dynamics of the surface charges on the membrane. Closer is the membrane to the plane, higher is the probability of seeing re-ignitions. Results also show that the decrease of the dielectric permittivity or the increase of the membrane thickness leads to more re-ignition events. In case of porous membrane, the pore size is the main parameter which will influence the propagation. When the pore size is below 100 µm, the discharge propagation is slower due to the discharge difficulties to penetrate totally inside the material.

<p>Compounds labelled with ¹¹C (<i>β</i>⁺, t_1/2 = 20.4 min) are used in positron emission tomography (PET), which is a quantitative non-invasive molecular imaging technique. It utilizes computerized reconstruction methods to produce time-resolved images of the radioactivity distribution in living subjects. </p><p>The feasibility of preparing [¹¹C]methyl iodide from [¹¹C]methane and iodine via a single pass through a non-thermal plasma reactor was explored. [¹¹C]Methyl iodide with a specific radioactivity of 412 ± 32 GBq/µmol was obtained in 13 ± 3% decay-corrected radiochemical yield within 6 min via catalytic hydrogenation of [¹¹C]carbon dioxide (24 GBq) and subsequent iodination, induced by electron impact. </p><p>Labelled ethyl-, propyl- and butyl iodide was synthesized, within 15 min, via palladium-mediated carbonylation using [¹¹C]carbon monoxide. The carbonylation products, labelled carboxylic acids, esters and aldehydes, were reduced to their corresponding alcohols and converted to alkyl iodides. [1-¹¹C]Ethyl iodide was obtained via palladium-mediated carbonylation of methyl iodide with a decay-corrected radiochemical yield of 55 ± 5%. [1-¹¹C]Propyl iodide and [1-¹¹C]butyl iodide were synthesized via the hydroformylation of ethene and propene with decay-corrected radiochemical yields of 58 ± 4% and 34 ± 2%, respectively. [1-¹¹C]Ethyl iodide was obtained with a specific radioactivity of 84 GBq/mmol from 10 GBq of [¹¹C]carbon monoxide. [1-¹¹C]Propyl iodide was synthesized with a specific radioactivity of 270 GBq/mmol from 12 GBq and [1-¹¹C]butyl iodide with 146 GBq/mmol from 8 GBq. </p><p>Palladium-mediated hydroxycarbonylation of acetylene was used in the synthesis of [1-¹¹C]acrylic acid. The labelled carboxylic acid was converted to its acid chloride and subsequently treated with amine to yield <i>N-</i>[<i>carbonyl</i>-¹¹C]benzylacrylamide. In an alternative method, [<i>carbonyl</i>-¹¹C]acrylamides were synthesized in decay-corrected radiochemical yields up to 81% via palladium-mediated carbonylative cross-coupling of vinyl halides and amines. Starting from 10 ± 0.5 GBq of [¹¹C]carbon monoxide, <i>N-</i>[<i>carbonyl</i>-¹¹C]benzylacrylamide was obtained in 4 min with a specific radioactivity of 330 ± 4 GBq/µmol. </p>

Compounds labelled with 11C (β+, t1/2 = 20.4 min) are used in positron emission tomography (PET), which is a quantitative non-invasive molecular imaging technique. It utilizes computerized reconstruction methods to produce time-resolved images of the radioactivity distribution in living subjects. The feasibility of preparing [11C]methyl iodide from [11C]methane and iodine via a single pass through a non-thermal plasma reactor was explored. [11C]Methyl iodide with a specific radioactivity of 412 ± 32 GBq/µmol was obtained in 13 ± 3% decay-corrected radiochemical yield within 6 min via catalytic hydrogenation of [11C]carbon dioxide (24 GBq) and subsequent iodination, induced by electron impact. Labelled ethyl-, propyl- and butyl iodide was synthesized, within 15 min, via palladium-mediated carbonylation using [11C]carbon monoxide. The carbonylation products, labelled carboxylic acids, esters and aldehydes, were reduced to their corresponding alcohols and converted to alkyl iodides. [1-11C]Ethyl iodide was obtained via palladium-mediated carbonylation of methyl iodide with a decay-corrected radiochemical yield of 55 ± 5%. [1-11C]Propyl iodide and [1-11C]butyl iodide were synthesized via the hydroformylation of ethene and propene with decay-corrected radiochemical yields of 58 ± 4% and 34 ± 2%, respectively. [1-11C]Ethyl iodide was obtained with a specific radioactivity of 84 GBq/mmol from 10 GBq of [11C]carbon monoxide. [1-11C]Propyl iodide was synthesized with a specific radioactivity of 270 GBq/mmol from 12 GBq and [1-11C]butyl iodide with 146 GBq/mmol from 8 GBq. Palladium-mediated hydroxycarbonylation of acetylene was used in the synthesis of [1-11C]acrylic acid. The labelled carboxylic acid was converted to its acid chloride and subsequently treated with amine to yield N-[carbonyl-11C]benzylacrylamide. In an alternative method, [carbonyl-11C]acrylamides were synthesized in decay-corrected radiochemical yields up to 81% via palladium-mediated carbonylative cross-coupling of vinyl halides and amines. Starting from 10 ± 0.5 GBq of [11C]carbon monoxide, N-[carbonyl-11C]benzylacrylamide was obtained in 4 min with a specific radioactivity of 330 ± 4 GBq/µmol.

A study was carried out on the selection of processing condition that would yield Mg-Ti with most favourable hydrogenation properties. Processing routes under consideration were / mechanical milling under inert atmosphere, reactive milling i.e. milling under hydrogen atmosphere, ECAP (equal channel angular pressing) and thermal plasma synthesis. Structure resulting from each of these processing routes was characterized with respect to size reduction, coherently diffracting volume and the distribution of Ti catalyst. Mechanical milling yielded a particulate structure made up of large Mg agglomerates with embedded Ti fragments with a uniform distribution. Mg agglomerates have sizes larger than 100 &micro / m which arises as a result of a balance between cold welding process and ductile fracture. Repeated folding of Mg particles entraps Ti fragments inside the Mg agglomerates resulting in a very uniform distribution. Coherently diffracting volumes measured by X-ray Rietveld analysis have small sizes ca. 26 nm which implies that the agglomerates typically comprise 1011 crystallites. Mechanical milling under hydrogen, i.e. reactive milling, led to drastic reduction in particle size. Mg and Ti convert to MgH2 and TiH2 which are milled efficiently due to their brittleness resulting in particle sizes of sub-micron range. Hydrogenation experiments carried out on Mg-10 vol % Ti milled under argon yields enthalpy and entropy values of -76.74 kJ/mol-H2 and -138.64 J/K.mol-H2 for absorption and 66.54 kJ/mol H2 and 120.12 J/K.mol H2 for desorption, respectively. For 1 bar of hydrogen pressure, this corresponds to a hydrogen release temperature of 280 &deg / C. This value is not far off the lowest desorption temperature reported for powder processed Mg based alloys. ECAP processing is a bulk process where the powders, consolidated in the first pass, have limited contact with atmosphere. This process which can be repeated many times lead to structural evolution similar to that of milling, but for efficient mixing of phases it was necessary to employ multi-pass deformation. An advantage of ECAP deformation is strain hardening of the consolidated powders which has improved milling ability. Based on this, a new route was proposed for the processing of ductile hydrogen storage alloys. This involves several passes of ECAP deformation carried out in open atmosphere and a final milling operation of short duration under inert atmosphere. The plasma processing yields Mg particles of extremely small size. Evaporation of Mg-Ti powder mixture and the subsequent condensation process yield Mg particles which are less than 100 nm. Ti particles, under the current experimental condition used, have irregular size distribution but some could be quite small, i.e. in the order of a few tens of nanometers. Of the four processing routes, it was concluded that both reactive milling and thermal plasma processing are well suited for the production of hydrogen storage alloys. Reactive milling yield particles in submicron range and plasma processing seems to be capable of yielding nanosize Mg particles which, potentially, could be decorated with even smaller Ti particles.

It is the need of the hour to reduce the pollutants which poison our atmosphere and harm our health. The diesel engines are the most efficient IC engines in the world today, but paradoxically, they are also the engines which create the largest amounts of NOx, the pollutant that is most difficult to control with the existing technologies. In fact, the existing technologies are unable to meet the increasingly stringent standards for NOx. Even in bio-diesels, which in the future may be adopted as an important alternative fuel, NOx is the major pollutant. Thus not having a safe and stable method for NOx removal from the diesel exhaust stream is a cause for concern. In this thesis, there has been an attempt to address this issue by means of non-thermal plasma and catalysts. In this thesis, first the performance of the three sources was evaluated individually, along with two different HV electrodes, a helical wire and a straight wire. Secondly, the efficiencies of these three different types of sources were compared. Thirdly, a catalyst (Red Mud) and an adsorbent (NaZSM5) were cascaded with the plasma reactor to enhance the performance of the NOx removal process with the AC source as it gave the best results. All the experiments were performed with real diesel engine exhaust. The conclusions drawn from the experiments are as follows: The helical electrode consumes much lower power than the straight electrode. Therefore it is energy efficient. It also causes corona inception at lower voltages due to the strong non-uniformity of its electric field. The drawbacks of the helical electrode are an excess production of NO2 .it also does not work with the HFAC source, because at high frequency, the voltage doesn’t build up owing to the presence of only a dielectric medium of 2 mm thickness between the two electrodes. The performances of the 3 sources were compared. The HVAC unit gave the best NOx removal, followed by the MPC and finally, the HFAC source. The differences in efficiencies were related to both the magnitude of the peak voltage achieved by each device and the time period. It was also seen that when the voltage was high, a better efficiency can be achieved with lower power consumption. The comparison of the sources leads us to conclude that the high voltage AC source can be used as an economic alternative for NOx control. This is because a standard AC unit is easily available at higher voltages, and contains less electrical or mechanical complexity, whereas a pulsed source is comparatively expensive and complex. The NaZSM5 zeolite showed excellent removal at room temperature as an adsorbent when cascaded after the AC source, by reducing the NO2 levels consistently. The Red Mud showed reasonable catalytic activity at 400 C with the AC source. It was also efficient in compensating for the increase in the NO2 and CO concentration in the plasma atmosphere. Hence, both Red Mud and ZSM 5 are good candidates for a hybrid plasma-adsorbent or plasma-catalyst system. The combination better NOx/CO removal is the AC energization coupled with spiral electrode with either ZSM-5 or red mud. Scaling up the plasma/ plasma- catalyst system for handling higher flow rates will be the main task next. A method to optimize the source and load matching for better power transfer to the plasma reactor from the different sources also need to be developed. The design of the compact high frequency AC source must be upgraded for higher powers.

De nombreuses molécules médicamenteuses ne sont pas traitées efficacement par les techniques classiques utilisées dans les stations d'épuration et s’accumulent dans les milieux naturels. L’objectif de cette thèse a été de développer un procédé d’oxydation avancée utilisant un plasma non thermique généré par décharge électrique pour le traitement de molécules médicamenteuses et d’identifier le schéma de dégradation d’une des molécules d’étude, à savoir le paracétamol. Les traitements ont été réalisés à l’aide de deux réacteurs : un réacteur multi-pointes avec le plasma au contact direct du liquide à traiter et un réacteur fil-cylindre avec le plasma en amont du liquide à traiter. Des taux de conversion supérieurs à 80% ont pu être obtenus avec des rendements énergétiques, qui peuvent atteindre 8g/kWh et 39 g/kWh pour le paracétamol et l’ésoméprazole, respectivement. La décharge électrique créée entre une pointe et le liquide a été caractérisée par la spectroscopie d’émission optique afin d’observer la présence des espèces oxydantes produites par le plasma et d’estimer la température du milieu faiblement ionisé. Les espèces produites dans le liquide lors de la dégradation du paracétamol et de l’ésoméprazole qui ont été identifiées par la technique HRMS, entre autres, sont principalement des acides carboxyliques ainsi que des produits azotés. L’identification des voies de production pour la formation des principaux produits ont été étudiés particulièrement à l’aide de nombreuses méthodes chimiques comme HPLC/MS, MS/MS, et de différents marquages de paracétamol. Il a été prouvé que les principaux acides carboxyliques produits proviennent de la rupture du cycle aromatique. En conclusion, cette étude nous a permis d’obtenir des rendements énergétiques de traitement des deux molécules d’étude comparables à ceux retrouvés en littérature, et surtout d’établir un chemin de dégradation du paracétamol. / Many drug molecules are not effectively treated by conventional techniques used in wastewater treatment plants and accumulate in natural environments. The objective of this thesis was to develop an advanced oxidation process using a non-thermal plasma generated by electric discharge for the treatment of drug molecules (paracetamol and esomeprazole). The NTP treatments were carried out using two reactors: a multiple needle-to-plate reactor with the plasma in direct contact with the liquid to be treated and a wire-cylinder reactor with the plasma up stream of the liquid to be treated. Conversion rates higher than 80% have been obtained with energy yields, which can reach 8 g/kWh and 39 g/kWh for paracetamol and esomeprazole, respectively. The electrical discharge created between the need leand the liquid has been characterized by optical emission spectroscopy to observe the presence of the oxidative species produced by the plasma and to estimate the temperature of the ionized medium. The species produced in the liquid during the degradation of paracetamol and esomeprazole have been identified by the HRMS technique. The produced species, are mainly carboxylic acids as well as nitrogen products. The identification of production pathways for the formation of the main products has been studied particularly using numerous chemical methods such as HPLC/MS, MS/MS, and different labelling of paracetamol. It has been proven that the main carboxylic acids produced come from the breaking of the aromatic ring. In conclusion, this study allowed us to obtain energy efficiencies of treatment of the two study molecules comparable to those found in literature, and especially to establish a pathways of degradation of paracetamol.