Cette thèse s’intéresse à la conversion du glycérol en acide lactique (AL) et 1,2-propanediol (1,2-PDO) par catalyse hétérogène. Le mécanisme de la réaction fait débat, particulièrement au sujet de la première étape, qui peut être une déshydratation ou une déshydrogénation. Il est attendu que ces étapes élémentaires soient influencées par le pH et la nature de l’atmosphère. Ces paramètres ont donc été étudiés expérimentalement, en présence d’un catalyseur au rhodium supporté sur charbon. D’autre part, il y avait un manque de connaissances sur le comportement du glycérol à la surface métallique du catalyseur. Une approche théorique sur une surface modèle a donc été mise en oeuvre dans le champ de la théorie de la fonctionnelle de la densité (DFT), pour examiner les étapes élémentaires et calculer les états de transition correspondants. La combinaison de ces études a montré que la déshydrogénation du glycérol en glycéraldéhyde est la première étape de la réaction sur le catalyseur Rh/C en milieu basique sous atmosphère d’hélium et d’hydrogène. Cette étude a ensuite été étendue à un catalyseur iridium supporté sur charbon, qui a mené à de meilleurs rendements en 1,2-PDO et AL. L’utilisation de ce métal supporté sur carbonate de calcium a permis d’améliorer le rendement en AL, mais l’activité est plus faible. Cependant, ce catalyseur s’est révélé relativement actif dans l’eau à pH neutre, ce qui pourrait conduire à une synthèse plus verte de l’AL. Enfin, les aspects prédictifs de la chimie théorique ont été examinés, pour voir si la réactivité de ce polyol complexe (du point de vue de la chimie théorique) pouvait être modélisée par celle d’un monoalcool sur la surface. / This thesis reports a study of the heterogeneously catalysed conversion of glycerol into 1,2-propanediol (1,2-PDO) and lactic acid (LA). The mechanism and the first step of the reaction are especially debated, as it can be either dehydration or dehydrogenation. It is expected that these elementary steps can be influenced by pH variations and by the nature of the gas phase. These parameters were consequently investigated experimentally in the presence of a carbon supported rhodium catalyst. On the other hand, there was a lack of knowledge in the behaviour of glycerol at the surface of the metallic catalyst. A theoretical approach on a model Rh(111) surface was thus implemented in the framework of Density Functional Theory (DFT) to look over the alementary reactions and to calculate the corresponding transition states. The combination of experimental and theoretical results has shown that dehydrogenation into lyceraldehyde is the first step of the reaction on the Rh/C catalyst in basic media under He or H2 atmosphere. The study was then extended to carbon supported iridium catalyst that lead to the best 1,2-PDO and LA yields. The use of iridium catalyst supported on calcium carbonate allowed obtaining higher yields in LA, but catalytic performances were lower. This latter catalyst was surprisingly quite active when performing the reaction in neutral water, which provides opportunities for a greener synthesis of LA. Last, the predictive aspects of the theoretical chemistry were investigated to determine whether the reactivity of this polyalcohol can be modelized by the reactivity of a simpler monoalcohol on the surface.

Ce travail de thèse porte sur la synthèse de carbures de molybdène sur support afin de tester leurs performances catalytiques dans des réactions d’hydrogénation. Dans ce but, la conversion d'acide succinique en phase aqueuse dans un réacteur discontinu et du dioxyde de carbone en phase gazeuse dans un réacteur à flux continu, ont été effectuées. Les catalyseurs ont été préparés par la méthode de carburation par réduction en température programmée, pendant laquelle des paramètres ont été modifiés conduisant à différents rapports molybdène/carbone. Les différents catalyseurs testés dans cette réaction étaient actifs pour la conversion de l'acide succinique en gamma-butyrolctone et, plus remarquablement, en acide butyrique, ce dernier n'était pas obtenu en quantités significatives avec des catalyseurs à base de métaux précieux. L’augmentation de la conversion d’acide succinique avec une sélectivité plus élevée en acide butyrique a été faite avec les catalyseurs contenant plus de carbone, préparés en augmentant la vitesse spatiale horaire gazeuse. Les intermédiaires ont été ensuite convertis en tétrahydrofurane, butanol, 1,4-butanediol et butane. La désactivation observée lors de recyclage du catalyseur a été principalement attribuée à une diminution de la quantité de molybdène et de carbone carbidique, démontrée par l'analyse XPS. Des essais préliminaires de ces catalyseurs dans l'hydrogénation du dioxyde de carbone ont montré qu'ils fonctionnaient principalement en tant que catalyseurs pour la réaction du gaz à l’eau inverse, et l'excès de carbone entrave l'activité catalytique d'une manière opposée à la réaction en phase aqueuse. Le support semble jouer un rôle dans la réactivité des catalyseurs, la conversion du dioxyde de carbone ainsi que la sélectivité en méthane et méthanol, qui ont augmenté dans l'ordre suivant: carbure de molybdène sur support DT51 TiO2> P25 TiO2 ˜ ZrO2 / This work focuses on the synthesis of supported molybdenum carbides and evaluating their catalytic performance in succinic acid hydrogenation reactions in aqueous phase using batch reactor and carbon dioxide hydrogenation in gas phase using continuous flow reactor. The catalysts were prepared by the temperature programmed reduction carburization method, where the parameters were modified leading to different molybdenum to carbon ratios. The different catalysts tested were active in converting succinic acid to gamma butyrolctone and more remarkably butyric acid which is not reported in significant quantities in this reaction with precious metal based catalysts. The catalysts containing more carbon contents that were prepared by increasing the gas hourly space velocity showed higher activity in converting succinic acid and higher selectivity to butyric acid. The intermediates were then converted to tetrahydrofuran, butanol, 1,4-butanediol and butane gas. The deactivation observed while recycling the catalyst was mainly attributed to a decrease in the amounts of carbidic molybdenum and carbidic carbon, as demonstrated by XPS analysis. Preliminary tests for these catalysts in carbon dioxide hydrogenation showed that they functioned mainly as reverse water gas shift catalysts, and the excess of carbon hinders the catalytic activity in an opposite manner of the reaction in aqueous phase. The support seems playing a role in the reactivity of the catalysts, carbon dioxide conversion as well as methane and methanol selectivity increased in the order: molybdenum carbide supported on DT51 TiO2 > P25 TiO2 ˜ ZrO2

Methods were developed for the determination of methylmercury in natural waters and sediments based on steam distillation and aqueous phase ethylation followed by gas chromatography-atomic fluorescence spectrometry. The methods were shown to be free from measurable artefactual methylation of inorganic mercury and offered improved sample throughput over existing methods. Improvements were made to existing methods for the determination of total mercury in biota, sediments and natural waters and dissolved mercury species in natural waters. These methods were applied to the study of mercury cycling in two remote field sites. The cycling of mercury species was studied in Lake Murray in Western Province, Papua New Guinea, which has been historically noted as a region of high mercury concentrations in fish. Concentrations of methylmercury and total mercury in the water column were found to be variable and consistent with non-contaminated lake systems. Concentrations of methylmercury and total mercury in the sediments were also found to be low, except for in the south of the lake, which was influenced by an intermittent supply of water and sediments with elevated mercury concentrations from the Strickland River. Methylmercury concentrations in the sediments were generally higher in the backwater areas due to littoral processes. The low concentrations of methylmercury in the sediments and waters were inconsistent with other systems previously studied in the northern hemisphere, showing a link between high mercury concentrations in fish and high concentrations of methylmercury in waters or sediments. Therefore, the biota of Lake Murray were studied in order to account for the differences between this and other systems. A study was conducted of the stable isotope ratios of carbon and nitrogen in biota from Lake Murray to elucidate key food-web interactions. This study revealed that the dominant carbon source for fish in the lake is plankton, although algae and macrophytes may also be involved in the food-web. The methylmercury bioaccumulation factors between trophic levels were similar to those measured in temperate systems of the northern hemisphere. The high concentrations of methylmercury, observed in piscivorous fish, were shown to be a consequence of the complex food-web and the number of trophic levels in the food-chains. The cycling of mercury species was studied in Lake Gordon and Lake Pedder in southwest Tasmania, which has recently been identified as being in a region of high mercury concentrations in trout and eels. The concentrations of total mercury were found to be reasonably uniform in the waters of both lakes, spatially and temporally. The concentrations of methylmercury in the waters were seasonally variable, and were consistently lower in Lake Pedder than in Lake Gordon. Dilution of methylmercury concentrations by precipitation direct to the lake surface, probably accounts for the most of the difference in methylmercury concentrations between the lakes. Owing to the long residence time of water in Lake Gordon, this reservoir mixes inputs of water with varying methylmercury concentrations. Concentrations of total mercury and methylmercury in submerged soils were low and depth profiles of mercury species in the water column did not show evidence of a gradient of mercury concentrations due to releases from the sediments. The concentrations of methylmercury observed in the water column are consistent with the concentrations observed in the fish. A budget of the mercury inputs and outputs to Lake Gordon showed that in-lake processes and sources in the catchment areas both contributed significantly to the concentrations of methylmercury in the lake. The methylation of mercury in Lake Gordon appeared to mainly occur in the surface waters (< 10 m) and was not consistent with processes leading to the methylation of mercury at the oxic/anoxic boundary observed in seepage lakes in Wisconsin. The concentrations of total mercury and methylmercury in bogs in the catchment areas of Lakes Gordon and Pedder, were high and governed by the concentration of organic matter in the sediments. The processes involved in the supply of mercury species from the Lake Gordon and Lake Pedder catchments appear to be similar to those in drainage lakes in the temperate and boreal regions of the northern hemisphere. The formation of the Lake Gordon and Lake Pedder reservoirs appears to have had little impact on the mean annual concentrations of methylmercury released to the downstream environment.

Emerging contaminants are defined as synthetic or naturally occurring chemicals or microorganisms that are not currently regulated but have the potential to enter the environment and cause adverse ecological and/or human health effects. With recent development in analytical techniques, emerging contaminants have been detected in wastewater, source water, and finished drinking water. These environmental occurrence data have raised public concern about the fate and ecological impacts of such compounds. Concerns regarding emerging contaminants and the many chemicals that are in use or production necessitate a task to assess their potential health effects and removal efficiency during water treatment. Advanced oxidation processes (AOPs) are attractive and promising technologies for emerging contaminant control due to its capability of mineralizing organic compound via reactions with highly active hydroxyl radicals. However, the nonselective reactivity of hydroxyl radicals and the radical chain reactions make AOPs mechanistically complex processes. In addition, the diversity and complexity of the structure of a large number of emerging contaminants make it difficult and expensive to study the degradation pathways of each contaminant and the fate of the intermediates and byproducts. The intermediates and byproducts that are produced may pose potential effects to human and aquatic ecosystems. Consequently, there is a need to develop first-principle based mechanistic models that can enumerate reaction pathway, calculate concentrations of the byproducts, and estimate their human effects for both water treatment and reuse practices. This dissertation develops methods to predict reaction rate constants for elementary reactions that are identified by a previously developed computer-based reaction pathway generator. Many intermediates and byproducts that are experimentally identified for HO* induced reactions with emerging contaminants include common lower molecular weight organic compounds on the basis of several carbons. These lower carbon intermediates and byproducts also react with HO* at relatively smaller reaction rate constants (i.e., k < 109 M-1s-1) and may significantly affect overall performance of AOPs. In addition, the structures of emerging contaminants with various functional groups are too complicated to model. As a consequence, the rate constant predictors are established based on the conventional organic compounds as an initial approch. A group contribution method (GCM) predicts the aqueous phase hydroxyl radical reaction rate constants for compounds with a wide range of functional groups. The GCM is a first comprehensive tool to predict aqueous phase hydroxyl radical reaction rate constants for reactions that include hydrogen-atom abstraction from a C-H bond and/or a O-H bond by hydroxyl radical, hydroxyl radical addition to a C=C unsaturated bond in alkenes and aromatic compounds, and hydroxyl radical interaction with sulfur-, nitrogen-, or phosphorus-atom-containing compounds. The GCM shows predictability; factor of difference of 2 from literature-reported experimental values. The GCM successfully predicts the hydroxyl radical reaction rate constants for a limited number of emerging contaminants. Linear free energy relationships (LFERs) bridge a kinetic property with a thermochemical property. The LFERs is a new proof-of-concept approach for Ab initio reaction rate constants predictors. The kinetic property represents literature-reported and our experimentally obtained hydroxyl radical reaction rate constants for neutral and ionized compounds. The thermochemical property represents quantum mechanically calculated aqueous phase free energy of activation. Various Ab initio quantum mechanical methods and solvation models are explored to calculate the aqueous phase free energy of activation of reactantas and transition states. The quantum mechanically calculcated aqueous phase free energies of activation are within the acceptable range when compared to those that are obtained from the experiments. These approaches may be applied to other reaction mechanisms to establish a library of rate constant predictions for the mechanistic modeling of AOPs. The predicted kinetic information enables one to identify important pathways of AOP mechanisms that are initiated by hydroxyl radical, and can be used to calculate concentration profiles of parent compounds, intermediates and byproducts. The mechanistic model guides the design of experiments that are used to examine the reaction mechanisms of important intermediates and byproducts and the application of AOPs to real fields.

[Truncated abstract] To date, many subsurface contaminant modelling studies have focused on increasing model complexity and measurement requirements to improve model accuracy and widen model application. However, due to the highly complex and heterogeneous nature of flow in the subsurface, the greater benefit in model development may lie in decreasing complexity by identifying key processes and parameters, simplifying the relationships that exist between them, and incorporating these relationships into simple models that recognise or quantify the inherent complexity and uncertainty. To address this need, this study aims to identify and isolate the key processes and parameters that control dense nonaqueous phase liquid (DNAPL) and aqueous phase migration through single, onedimensional fractures. This is a theoretical representation which allows the study of processes through conceptual and mathematical models. Fracture systems typically consist of multiple two-dimensional fractures in a three-dimensional network; however, these systems are computationally and conceptually demanding to investigate and were outside of the scope of this study. This work initially focuses on DNAPL migration in single, one-dimensional fractures. The similitude techniques of dimensional and inspectional analysis are performed to simplify the system and to develop breakthrough time scale factors. This approach relies heavily on the limitations of the equation used for the analysis and on the difficulty in representing variable aperture scenarios. The complexity of the conceptual model is then increased by embedding the fracture in a two-dimensional, porous matrix. ... These tools can be readily applied by the field investigator or computer modeller to make order-of-magnitude estimates of breakthrough times, reduce or target measurement requirements, and lessen the need to employ numerical multiphase flow models. To determine the implications of the results found in the one-dimensional studies to applications at the field scale, the complexity of the conceptual model was increased to a single, two-dimensional, planar fracture embedded in a three-dimensional porous matrix. The focus of this study was not DNAPL breakthrough times but the relative importance and interaction of different mass transport processes and parameters on plume migration and evolution. Observations clearly show that estimates of the size, location and concentration of the plume is highly dependent on the geologic media, the temporal and spatial location and resolution of measurements, and on the history, mass and location of the DNAPL source. In addition, the processes controlling mass transport (especially matrix diffusion and back diffusion) act in combination at the field scale in ways not always expected from an analysis of processes acting individually at smaller spatial and temporal scales. Serious concerns over the application of the common '1% Rule of Thumb' to predict DNAPL presence and the use of remediation efforts that rely largely on natural attenuation are raised. These findings have major implications for the field worker and computer modeller, and any characterisation, monitoring or remediation program development needs to be sensitive to these findings.

La biomasse végétale (source de carbone renouvelable) peut être utilisée pour fabriquer des carburants liquides et produits de base pour la chimie. Ainsi depuis environ une dizaine d'années, se développe le procédé APHDO (Aqueous Phase HydroDeOxygenation) de transformation directe en phase aqueuse de polyols d'origine lignocellulosique (comme le sorbitol) en alcanes valorisables (C5-C6). Ce procédé repose sur une catalyse hétérogène bifonctionnelle métal/acide et fait intervenir des ruptures compétitives de liaisons C-C et C-O. L'objectif de la thèse est de mettre au point des systèmes bimétalliques supportés actifs et sélectifs pour la transformation du sorbitol en hexane. La modification d'un catalyseur de référence Pt/SiO2-Al2O3 par ajout de Re, Ir, Pd, Rh et Ru est effectuée par trois techniques de synthèse : co-imprégnation, imprégnations successives et dépôt par réduction catalytique. Les performances des catalyseurs bimétalliques sont comparées à isoconversion de sorbitol à celles des catalyseurs monométalliques parents pour un test catalytique réalisé en autoclave, avec une solution aqueuse à 10% massique de sorbitol, à 240°C et 60 bar de pression totale sous H2. Les produits se répartissent en phase gaz (CO2, alcanes en C1-C6) et liquide (composés oxygénés). Le sorbitane et l'isosorbide sont majoritairement formés en phase liquide, le dernier étant un intermédiaire clé de la transformation du sorbitol dans cette étude. Les catalyseurs Pt-Ru/SiO2-Al2O3 s'avèrent les plus sélectifs pour la réaction, celui préparé par imprégnations successives conduisant à une plus forte proportion de C6 en phase gaz comparé aux deux monométalliques Pt/SiO2-Al2O3 et Ru/SiO2-Al2O3. / Plant Biomass (renewable source of carbon) can be used to make liquid fuels and basic products of chemistry. So, from about ten years, the APHDO (Aqueous Phase HydroDeOxygenation) process is developed for the direct transformation in aqueous phase of polyols from Biomass (such as sorbitol) into renewable alkanes (C5-C6). This process involves a metal/acid bifunctional heterogeneous catalysis and competitive C-O and C-C bond cleavages. The aim of the PhD work is to develop supported bimetallic systems active and selective for the transformation of sorbitol into hexane. The modification of a reference Pt/SiO2-Al2O3 catalyst by addition of Re, Ir, Pd, Rh and Ru is carried out by three synthesis methods: co-impregnation, successive impregnations and deposit by catalytic reduction. The performances of bimetallic catalysts are compared at sorbitol isoconversion to those of the parent monometallic catalysts for a catalytic test carried out in an autoclave with an aqueous solution of sorbitol (10 wt%) at 240°C and 60 bar total pressure under dihydrogen. The products are distributed in the gas phase (CO2, C1-C6 alkanes) and in the liquid phase (oxygenated compounds). Sorbitan and isosorbide are predominantly formed in the liquid phase, the latter being a key intermediate of sorbitol transformation in this study. Pt-Ru/SiO2-Al2O3 catalysts are the most selective for the reaction, the one prepared by successive impregnations leads to a higher proportion of C6 in gaseous phase compared to both monometallic Pt/SiO2-Al2O3 and Ru/SiO2-Al2O3 catalysts.

Cette thèse s’est déroulée dans le cadre du projet FONGEOSEC, qui vise à développer la filière de la géothermie profonde en France avec la conception d’un démonstrateur d’une centrale de production d’énergie géothermique dans le bassin Rhénan. Ce projet est piloté par Fonroche Géothermie, qui gère un consortium de plus de dix acteurs du milieu académique et industriel. Le financement du projet est réalisé avec participation de l’Agence de l’Environnement et de la Maîtrise de l’Énergie (ADEME). Ainsi, les travaux exposés dans ce document se sont intéressés à la caractérisation thermodynamique des fluides géothermaux (saumures chaudes contenant des gaz dissous) de la région ciblée par le projet. Il est nécessaire de déterminer la solubilité de chacun des gaz dissous dans ces saumures aux conditions de pression, température et salinité de l’exploitation géothermique. Des modèles thermodynamiques de prévision des équilibres entre phases liquide et vapeur peuvent être utilisés pour estimer ces solubilités. Néanmoins, en absence des mesures expérimentales dans les conditions de pression, température et salinité d’intérêt, pour effectuer la régression de paramètres de ces modèles, il sera difficile d’obtenir avec précision ces solubilités à partir de simulations. Ainsi, cette thèse est centrée sur l’étude expérimentale des solubilités des gaz dans des saumures représentatives des fluides du bassin Rhénan. La gamme de pression de FONGEOSEC va de 6.0 MPa à 40.0 MPa pour des températures de 333.15 K et 453.15 K. Le dispositif expérimental utilisé dans cette thèse fonctionne dans ces conditions. Les gaz dissous dans les saumures visées par le projet sont constitués essentiellement de dioxyde de carbone (CO2), puis d’azote (N2) et enfin de méthane (CH4) en plus faibles quantités. Les sels dissous dans ces fluides sont surtout du chlorure de sodium et du chlorure de calcium, à molalité de 1.2 mol NaCl-0.2 mol CaCl2.Kg H2O-1. Dans cette thèse, nous avons effectué la détermination expérimentale de la solubilité du dioxyde de carbone dans des saumures typiques du bassin Rhénan aux conditions de pression et de température du projet FONGEOSEC. Des réflexions sont proposées quant à une méthodologie d’analyse de solubilité du méthane et de l’azote dans des phases aqueuses. Nous observons aussi que dans les conditions de pression et température de fond du puits, la solubilité du dioxyde de carbone dans les saumures typiques du bassin Rhénan est la plus élevée parmi toutes les conditions caractérisées. Une étude du sating-out effect dans ces saumures est également proposée dans cette thèse. Enfin, il est remarqué que le modèle de Pitzer (Pitzer.dat sur PhreeqC) semble prédire de façon correcte nos mesures expérimentales à 333.15 K, mais il perd son efficacité à 453.15 K. Dans cette condition, le modèle E-NRTL (Simulis®) semblerait être plus approprié. / This thesis was part of the FONGEOSEC project, which aims to develop the deep geothermal energy sector in France through the the design of a geothermal power pilot plant on the Upper Rhine Graben. This project is controled by Fonroche Géothermie, which manages a consortitium of more than ten academic and industrial partners. The French Environment & Energy Management Agency (ADEME) participates at the fundings of the project.Therefore, the work exposed in this document concerns the thermodynamic characterisation of geothermal fluids (hot brines containing dissolved gases) from the target region of this project. It is thus necessary to determine the solubility of each gas dissolved in these brines at the pressure, temperature and salinity conditions of geothermal energy exploitation.Thermodynamic models that predict liquid-vapour phase equilibrium can be used to estimate these solubilities. However, if there is a lack of experimental measures on the pressure, temperature and salinity conditions of interest, it will not be possible to regress these models interaction parameters and, therefore, it will be difficult to have precise solubility results from these thermodynamic simulations. Thus, this thesis has focused on the experimental study of gas solubilities in brines representing the Upper Rhine Graben fluids. The pressure range of the FONGEOSEC project goes from 6.0 MPa to 40.0 MPa for temperatures of 333.15 K and 453.15 K. The experimental setup used on this thesis can operate at these conditions. Dissolved gases in the brines concerned by this project are mainly composed by carbon dioxyde (CO2), and then by nitrgen (N2) and methane (CH4) at lower quantitites. Dissolved salts in these fluids are basically chloride sodium and chloride calcium, at molalities of 1.2 mol NaCl-0.2 mol CaCl2.Kg H2O-1.On the scope of this thesis, we have performed the experimental determination of carbon dioxyde solubility in Upper Rhine Graben-type brines at the pressure and temperature conditions of the FONGEOSEC project. We propose a discussion about an analysis methodology for measuring nitrogen and methane solubility in aqueous phases. We also observed that at the pressure and temperature conditions found at the bottom of the production well, carbon dioxyde solubility in the Upper Rhine Graben-type brines reaches its highest value among all the conditions studied in this thesis. A salting-out effect study in these brines is also proposed in this document. Finally, it is noticed that the Pitzer model (Pitzer.dat at PhreeqC) seems to predict properly our experimental data at 333.15 K, but it is less efficient at 453.15 K. In this condition, the E-NRTL model (Simulis®) seems to be more appropriate.

Die chemische Zusammensetzung und die physikalischen Eigenschaften von troposphärischen Gasen, Partikeln und Wolken hängen aufgrund zahlreicher Prozesse stark voneinander ab. Insbesondere chemische Multiphasenprozesse in Wolken können die physiko-chemischen Eigenschaften der Luft und troposphärischer Partikel klein- und großräumig verändern. Diese chemische Prozessierung des troposphärischen Aerosols innerhalb von Wolken beeinflusst die chemischen Umwandlungen in der Atmosphäre, die Bildung von Wolken, deren Ausdehnung und Lebensdauer, sowie die Transmissivität von einfallender und ausgehender Strahlung durch die Atmosphäre. Damit sind wolken-chemische Prozesse relevant für das Klima auf der Erde und für verschiedene Umweltaspekte. Daher ist ein umfassendes Verständnis dieser Prozesse wichtig. Die explizite Behandlung chemischer Reaktionen in der Flüssigphase stellt allerdings eine Herausforderung für atmosphärische Computermodelle dar. Detaillierte Beschreibungen der Flüssigphasenchemie werden deshalb häufig nur für Boxmodelle verwendet. Regionale Chemie-Transport-Modelle und Klimamodelle berücksichtigen diese Prozesse meist nur mit vereinfachten chemischen Mechanismen oder Parametrisierungen. Die vorliegende Arbeit hat zum Ziel, den Einfluss der chemischer Mehrphasenprozesse innerhalb von Wolken auf den Verbleib relevanter Spurengase und Partikelbestandteile mit Hilfe des state‑of‑the‑art 3D-Chemie-Transport-Modells COSMO-MUSCAT zu untersuchen. Zu diesem Zweck wurde das Model um eine detaillierte Beschreibung chemischer Prozesse in der Flüssigphase erweitert. Zusätzlich wurde das bestehende Depositionsschema verbessert, um auch die Deposition von Nebeltropfen zu berücksichtigen. Die durchgeführten Modellerweiterungen ermöglichen eine bessere Beschreibung des troposphärischen Multiphasensystems. Das erweiterte Modellsystem wurde sowohl für künstliche 2D-Bergüberströmungsszenarien als auch für reale 3D-Simulationen angewendet. Mittels Prozess- und Sensitivitätsstudien wurde der Einfluss (i) des Detailgrades der verwendeten Mechanismen zur Beschreibung der Flüssigphasenchemie, (ii) der Größenauflösung des Tropfenspektrums und (iii) der Tropfenanzahl auf die chemischen Modellergebnisse untersucht. Die Studien belegen, dass die Auswirkungen der Wolkenchemie aufgrund ihres signifikanten Einflusses auf die Oxidationskapazität in der Gas- und Flüssigphase, die Bildung von organischer und anorganischer Partikelmasse sowie die Azidität der Wolkentropfen und Partikel in regionalen Chemie-Transport-Modellen berücksichtigt werden sollten. Im Vergleich zu einer vereinfachten Beschreibung der Wolkenchemie führt die Verwendung des detaillierten chemischen Flüssigphasenmechanismus C3.0RED zu verringerten Konzentrationen wichtiger Oxidantien in der Gasphase, einer höheren Nitratmasse in der Nacht, geringeren nächtlichen pH-Werten und einer veränderten Sulfatbildung. Darüber hinaus ermöglicht eine detaillierte Wolkenchemie erst Untersuchungen zur Bildung sekundärer organischer Partikelmasse in der Flüssigphase. Die größenaufgelöste Behandlung der Flüssigphasenchemie hatte nur geringen Einfluss auf die chemischen Modellergebnisse. Schließlich wurde das erweiterte Modell für Fallstudien zur Feldmesskampagne HCCT‑2010 genutzt. Zum ersten Mal wurde dabei ein chemischer Mechanismus mit der Komplexität von C3.0RED verwendet. Die räumlichen Effekte realer Wolken z. B. auf troposphärische Oxidantien oder die Bildung anorganischer Masse wurden untersucht. Der Vergleich der Modellergebnisse mit verfügbaren Messungen hat viele Übereinstimmungen aber auch interessante Unterschiede aufgezeigt, die weiter untersucht werden müssen. / In the troposphere, a vast number of interactions between gases, particles, and clouds affect their physico-chemical properties, which, therefore, highly depend on each other. Particularly, multiphase chemical processes within clouds can alter the physico-chemical properties of the gas and the particle phase from the local to the global scale. This cloud processing of the tropospheric aerosol may, therefore, affect chemical conversions in the atmosphere, the formation, extent, and lifetime of clouds, as well as the interaction of particles and clouds with incoming and outgoing radiation. Considering the relevance of these processes for Earth\''s climate and many environmental issues, a detailed understanding of the chemical processes within clouds is important. However, the treatment of aqueous phase chemical reactions in numerical models in a comprehensive and explicit manner is challenging. Therefore, detailed descriptions of aqueous chemistry are only available in box models, whereas regional chemistry transport and climate models usually treat cloud chemical processes by means of rather simplified chemical mechanisms or parameterizations. The present work aims at characterizing the influence of chemical cloud processing of the tropospheric aerosol on the fate of relevant gaseous and particulate aerosol constituents using the state-of-the-art 3‑D chemistry transport model (CTM) COSMO‑MUSCAT. For this purpose, the model was enhanced by a detailed description of aqueous phase chemical processes. In addition, the deposition schemes were improved in order to account for the deposition of cloud droplets of ground layer clouds and fogs. The conducted model enhancements provide a better insight in the tropospheric multiphase system. The extended model system was applied for an artificial mountain streaming scenario as well as for real 3‑D case studies. Process and sensitivity studies were conducted investigating the influence of (i) the detail of the used aqueous phase chemical representation, (ii) the size-resolution of the cloud droplets, and (iii) the total droplet number on the chemical model output. The studies indicated the requirement to consider chemical cloud effects in regional CTMs because of their key impacts on e.g., oxidation capacity in the gas and aqueous phase, formation of organic and inorganic particulate mass, and droplet acidity. In comparison to rather simplified aqueous phase chemical mechanisms focusing on sulfate formation, the use of the detailed aqueous phase chemistry mechanism C3.0RED leads to decreased gas phase oxidant concentrations, increased nighttime nitrate mass, decreased nighttime pH, and differences in sulfate mass. Moreover, the treatment of detailed aqueous phase chemistry enables the investigation of the formation of aqueous secondary organic aerosol mass. The consideration of size-resolved aqueous phase chemistry shows only slight effects on the chemical model output. Finally, the enhanced model was applied for case studies connected to the field experiment HCCT-2010. For the first time, an aqueous phase mechanism with the complexity of C3.0RED was applied in 3‑D chemistry transport simulations. Interesting spatial effects of real clouds on e.g., tropospheric oxidants and inorganic mass have been studied. The comparison of the model output with available measurements revealed many agreements and also interesting disagreements, which need further investigations.

Remediation of contaminated groundwater remains a high-priority national goal in the United States. Water is essential to life, and new sources of water are needed for an expanding population. Groundwater remediation remains a significant technical challenge despite decades of research into this field. New approaches are needed to address the most severely-polluted aquifers, and cost-effective solutions are required to meet remediation objectives that protect human health and the environment. Source reduction combined with Monitored Natural Attenuation (MNA) is a remediation strategy whereby the source of contamination is aggressively treated or removed and the residual groundwater plume depletes due to natural processes in the subsurface. The USEPA requires long-term performance monitoring of groundwater at MNA sites over the remediation timeframe, which often takes decades to complete. Presently, computational tools are lacking to adequately integrate source remediation with economic models. Furthermore, no framework has been developed to highlight the tradeoff between the degree of remediation versus the level of benefit within a cost structure. Using the Natural Attenuation Software (NAS) package developed at Virginia Tech, a set of formulae have been developed for calculating the TOR for petroleum-contaminated aquifers (specifically tracking benzene and MTBE) through statistical techniques. With the knowledge of source area residual saturation, groundwater velocity, and contaminant plume source length, the time to remediate a site contaminated with either benzene or MTBE can be determined across a range of regulatory maximum contaminant levels. After developing formulae for TOR, an integrated and interactive decision tool for framing the decision analysis component of the remediation problem was developed. While MNA can be a stand-alone groundwater remediation technology, significant benefits may be realized by layering a more traditional source zone remedial technique with MNA. Excavation and soil vapor extraction when applied to the front end of a remedial action plan can decrease the amount of time to remediation and while generally more expensive than an MNA-only approach, may accrue long-term economic advantages that would otherwise be foregone. The value of these research components can be realized within the engineering and science communities, as well as through government, business and industry, and communities where groundwater contamination and remediation are of issue. Together, these tools constitute the Sâ ªEâ ªEâ ªPâ ªAGE paradigm, founded upon the concept of sound science for an environmental engineering, effectual economics, and public policy agenda. The TOR formulation simplifies the inputs necessary to determine the number of years that an MNA strategy will require before project closure and thus reduces the specialized skills and training required to perform a numerical analysis that for one set of conditions could require many hours of simulation time. The economic decision tool, that utilizes a life cycle model to evaluate a set of feasible alternatives, highlights the tradeoffs between time and economics can be realized over the lifetime of the remedial project. / Ph. D.

L'aérosol atmosphérique a des effets sur le changement climatique global et un impact sanitaire non-négligeables. Dans l'aérosol atmosphérique terrestre, les composés organiques représentent une fraction importante. Du fait de l'extrême complexité de cette fraction organique et des processus dynamiques qui l'animent, une fraction non négligeable de celle-ci n'est pas clairement identifiée à ce jour malgré des techniques d'analyses toujours plus nombreuses. Dans cette thèse, nous avons voulu explorer la richesse d'information fournie par une technique innovante : la spectrométrie de masse à haute résolution (HRMS). La haute résolution du LTQ-Orbitrap fournit une extrême précision sur la masse des molécules analysées et permet d'en identifier les formules brutes. Tout d'abord, nous avons utilisé cette nouvelle méthode de caractérisation afin d'élucider en laboratoire des mécanismes de production de l'aérosol se déroulant en phase aqueuse. Associée à une caractérisation par RMN, la HRMS nous permet d'identifier des voies de fabrication de composés de faible poids moléculaires (acides carboxyliques, aldéhydes, cétone) ainsi que des composés à haut poids moléculaire : les oligomères formés se transforment en HULIS au cours de leur vieillissement. Le fait que la méthacroléine (MACR) et la méthyl-vinyl-cétone (MVK), les deux principaux produits d'oxydation de l'isoprène, forment des AOS en phase aqueuse avait été précédemment montré. Ce travail montre que les précurseurs des AOS sont différents selon l'isomère et que les séries d'oligomères formées atteignent 1400 Da.. L'étude HRMS des produits permet de proposer un mécanisme radicalaire d'oligomérisation de la MVK. L'analyse HRMS des produits de la MACR montre qu'en plus du mécanisme valable pour la MVK, la réactivité de la MACR engendre co-polymérisation et production d'Hulis. Une signature HRMS des Hulis a été mise en évidence. Ensuite, nous avons utilisé les méthodes de traitement de données HRMS pour tenter de les appliquer à l'identification d'aérosol ambiant. Les composés organiques représentent la fraction majeure des particules de l'aérosol atmosphérique ; une grande partie reste mal identifiée. Une compréhension détaillée des sources et des procédés de transformations est nécessaire. L'investigation de la composition chimique des particules de matière fine et ultrafine peut être apporter par HRMS. L'ESI-Orbitrap apporte une description moléculaire qui détermine les propriétés chimiques et physiques de l'aérosol organique. Les particules ont été échantillonnées selon leur taille respective. Les prélèvements ont été fait à Grenoble en été et en hiver. Une comparaison saisonnière permet d'identifier des signatures chimiques différentes. Enfin, une intercomparaison est établie avec des échantillons d'une troisième campagne prélevées en proximité routière: MOCOPO. / Atmospheric aerosol has an important impact on the radiative balance of Earth. Organics compounds represent the major fraction of atmospheric aerosol particles; a large part is still not well characterized. A detailed understanding of the sources, transformations processes and fates of organics aerosols is needed. This work investigates the ability of the ESI-Orbitrap to characterize organics molecules of aerosol. Firstly, experimental and analytical methods were developed to unveil mechanistic ambiguities that were previously shown. Methacrolein (MACR) and methyl vinyl ketone (MVK) (the two main gas phase atmospheric oxidation products of isoprene) were known to form oligomers and secondary organic aerosol (SOA) upon aqueous phase OHoxidation and subsequent water evaporation. For the two precursors, ESI-MS analysis of the reacting solutions brought clear evidence for the formation of oligomer systems having a mass range of up to 1400 Da.. Taking advantage of the regularities observed in the oligomer systems, the ESI-HRMS data were used to propose stoichiometries for more than 75% of the observed signal. Moreover, we show here that MACR oligomers aging give rise to HULIS production. In addition, global estimates of secondary organic aerosol (SOA) formation flux show that current descriptions miss a large fraction of the sources. This gaping underestimation has been linked to a poor understanding of aerosol functionalization in the atmosphere and lead to the formation of a new conceptual framework for the description of the aerosol, based on volatility versus polarity plots. This new framework is almost exclusively based on High Resolution Time of Flight Aerosol Mass Spectrometer(HR-Tof-AMS) data, as this instrument gives access to average H:C, N:C and O:C ratios for the bulk aerosol. The AMS estimates for O:C and H:C ratios are thus based on heavy fragmentation of organics followed by stoichiometry attribution on those fragments. Given the resolution of the HR-ToF-AMS, such an attribution is not feasible above a certain mass, making fragmentation a necessary aspect of the measurement. Conversely, Orbitrap-HRMS provide a resolution of 100,000 at m/z 400, with a mass range 50 – 2000 amu, enabling stoichiometry retrieval up to higher masses than the AMS. Coupled to a “soft” electrospray ionization method, Orbitrap-HRMS gives O:C and H:C ratios on entire molecules in the analysed mixture. We used samples from three contrasted field campaigns: the two first at an urban kerbside site in summer and in winter, the third one in the roadway vicinity (Grenoble, France). Accelerated Solvent Extraction provides a clear overview of the chemical composition of organic extracts from aerosol particles collected at different season at an urban site. The elemental composition was obtained within 2-5 ppm, on the range 150-300 m/z. However, this study shows that both ionization polarity were needed to get a complete picture of the chemical composition of the samples. We showed that Esi-Orbitrap-HRMS allows to compute a statistical distribution of the elementary ratios that is different from a simple average value. Keywords: HRMS, SOA.