The fate and mobility of boric acid in the environment is largely controlled by adsorption reactions with soil organic matter and soil minerals to form surface complexes (Marzadori et al., 1991; Su and Suarez, 1995; Yermiyahu et al., 1995; Peak et al., 2002). The effects of humic acid (HA) and dissolved CO2 on boric acid adsorption on amorphous (am)-Al(OH)3 were investigated as their influence on sorption is potentially important. Although a model system was used in the studies, the findings should be generally useful to better understand the mobility and bioavailability of boric acid in the soil ecosystems.<p>In this dissertation, boric acid adsorption on pure am-Al(OH)3 and 5% w/w HA coated am-Al(OH)3 were investigated both as a function of pH (4.5 11) and initial boric acid concentration (0 4.5 mmol L-1). Batch adsorption isotherm experiments were also conducted with samples exposed to atmospheric CO2 and anaerobic (N2) conditions to examine the effects of dissolved CO2 on boric acid adsorption. Both the pH envelope and the adsorption isotherm experiments showed that the HA coating on am-Al(OH)3 and the presence of dissolved CO2 decreased boric acid adsorption. <p>Raman spectroscopy and boron (B) K-edge X-ray Absorption Near Edge Structure (XANES) spectroscopy were used to investigate the coordination of boric acid adsorbed at mineral/water interfaces. The Raman spectroscopy was less successful than expected as there were difficulties in identifying B bands in the 5% w/w HA coated am-Al(OH)3 samples.<p>The B K-edge XANES spectroscopy yielded better results. The XANES spectra of boric acid adsorption samples showed that both trigonal BO3 and tetrahedral BO4 coordinated complexes are present on the pure and HA coated mineral surfaces. At pH 7.0 and 9.2, the adsorption of boric acid on am-Al(OH)3 is predominantly inner-sphere trigonal complexes; with minor amounts of inner-sphere tetrahedral complexes. Both macroscopic and spectroscopic experiments revealed that the combination of HA coating on am-Al(OH)3 and dissolved CO2 decreased boric acid adsorption compared to adsorption on pure am-Al(OH)3.<p>The discoveries in this dissertation contribute significantly in understanding the effects of HA and dissolved CO2 has on boric acid adsorption in the environment. Since B speciation and the stability of am-Al(OH)3 mineral and HA changes with pH, the bioavailability of B is expected to change as well with pH. The adsorption on boric acid on am-Al(OH)3 and/or HA coated am-Al(OH)3 is expected to decrease the amount of boric acid available to plants. Therefore the nutrient management regimen will have to be modified for soils that are high in natural organic matter, carbonate and/or aluminum hydroxyl species.

This thesis was devised as a fundamental study of the Li-S system by the use of 7Li Magic Angle Spinning (MAS) Nuclear Magnetic Resonance (NMR), X-ray Absorption Near-Edge Structure (XANES), and Non-Resonant Inelastic X-ray Scattering (NRIXS). The first part of this thesis is dedicated to the synthesis of solid state linear chain polysulfides in order to use them as reference compounds in the following experiments. 7Li NMR shows that Li2S and Li2S6 exhibit single but different Li environments, while the others stoichiometry targeted consist of a mixture of them. This is the first report of a stable solid-phase intermediate between elemental sulfur (α-S8) and Li2S. The second part of this thesis is based on operando XANES measurements made in the Argonne Photon Source (APS). Linear combination fit (LCF) analyses are performed to interpret the data; and, noticeably, the distinction between short-chain and long-chain polysulfides can be made due to the use of proper reference materials. The results reveal the first detailed observation of typical sulfur redox chemistry upon cycling, showing how sulfur fraction (under-utilization) and sulfide precipitation impact capacity. It also gives new insights into the differences between the charge and discharge mechanisms, resulting in the hysteresis of the cycling profile. Heat-treated PCNS/S exhibits a particular electrochemical signature, which has never explained. Operando XANES measurements at the sulfur K-edge are performed on heat-treated PCNS. Noticeably, the difference in the XANES signatures of the pristine and the recharged state shows the irreversible process that occurs during the first discharges. At last, electrolytes are investigated by the compilation of quantitative physico-chemical parameters on novel class of solvents that are glymes with non-polar groups and acetonitrile (ACN) complexed with LiTFSI. (ACN)2:LiTFSI attracts particular attention because of the particularly low Li2Sn solubility and. Its good electrochemical performance when mixed with 50 vol% HFE. Operando XANES proves the formation of polysulfides in this electrolyte, and the low energy feature evolution shows a more progressive mechanism involved in this electrolyte, which could be linked to the particularly low Li2Sn solubility.

Standard geochemical analysis methods, such as aqueous geochemistry analysis and mineralogical analysis, frequently are utilized to evaluate the effectiveness of passive treatment systems, though they do not necessarily provide information regarding the mechanism of removal. Two emerging analytical techniques have shown promise by providing additional information to improve characterization of treatment systems: X-ray absorption spectroscopy (XAS) and stable isotope analysis. In this thesis, these novel analytical techniques were integrated with standard geochemical measurements to better characterize contaminated sites as well as potential treatment technologies used to mitigate aqueous contaminant mobility. Laboratory experiments were used to evaluate the removal of Se(VI) form simulated groundwater using granular Fe0 (GI) and organic carbon (OC). Greater than 90 % removal of Se(VI) was observed for systems containing GI after 5 days of reaction time and only 15 % removal was observed in systems containing OC. Synchrotron radiation-based XAS analysis of the treatment materials indicated the presence of both Se(IV) and Se(0) on the edges of GI grains after 6 hours reaction time, with no evidence of oxidized Se after 5 days of reaction. Several analytical techniques were integrated to characterize sediment contaminated with Hg and other contaminants through previous industrial practices. Analysis of the sediment by XAS indicated the possible presence of mercury selenide and copper sulfide. Resuspension tests were performed in oxic and anoxic conditions to simulate the effects of changing geochemical conditions of Hg release from sediments during dredging operations. The results indicated a higher release of Hg under oxic conditions in some sediment locations, suggesting that oxidative degradation of organic carbon or oxidative dissolution of Hg sulfides contributed to Hg release. The treatment of aqueous Hg(II) was evaluated with a variety of treatment media, including clay and GI. Treatment with GI was rapid, with 90 % removal observed after 2 hours reaction time. Extended X-ray absorption fine structure (EXAFS) analysis indicated the presence of Hg-O bonding on GI, suggesting that Hg was bound to Fe oxides formed on the surface of corroded GI. A new conceptual model for tracking the stable isotope fractionation of sulfur was coupled to the reactive transport model MIN3P to determine the effects of secondary transformations on sulfur cycling in passive treatment systems. Minor differences were noted when comparing the transport model-derived fractionation factor to calculations using a simplified Rayleigh distillation model, possibly indicating the effect of SO4 precipitation. The incorporation of stable isotope modeling provides a framework for the modeling of other isotope systems in treatment technologies.

The fate and mobility of boric acid in the environment is largely controlled by adsorption reactions with soil organic matter and soil minerals to form surface complexes (Marzadori et al., 1991; Su and Suarez, 1995; Yermiyahu et al., 1995; Peak et al., 2002). The effects of humic acid (HA) and dissolved CO2 on boric acid adsorption on amorphous (am)-Al(OH)3 were investigated as their influence on sorption is potentially important. Although a model system was used in the studies, the findings should be generally useful to better understand the mobility and bioavailability of boric acid in the soil ecosystems.<p>In this dissertation, boric acid adsorption on pure am-Al(OH)3 and 5% w/w HA coated am-Al(OH)3 were investigated both as a function of pH (4.5 11) and initial boric acid concentration (0 4.5 mmol L-1). Batch adsorption isotherm experiments were also conducted with samples exposed to atmospheric CO2 and anaerobic (N2) conditions to examine the effects of dissolved CO2 on boric acid adsorption. Both the pH envelope and the adsorption isotherm experiments showed that the HA coating on am-Al(OH)3 and the presence of dissolved CO2 decreased boric acid adsorption. <p>Raman spectroscopy and boron (B) K-edge X-ray Absorption Near Edge Structure (XANES) spectroscopy were used to investigate the coordination of boric acid adsorbed at mineral/water interfaces. The Raman spectroscopy was less successful than expected as there were difficulties in identifying B bands in the 5% w/w HA coated am-Al(OH)3 samples.<p>The B K-edge XANES spectroscopy yielded better results. The XANES spectra of boric acid adsorption samples showed that both trigonal BO3 and tetrahedral BO4 coordinated complexes are present on the pure and HA coated mineral surfaces. At pH 7.0 and 9.2, the adsorption of boric acid on am-Al(OH)3 is predominantly inner-sphere trigonal complexes; with minor amounts of inner-sphere tetrahedral complexes. Both macroscopic and spectroscopic experiments revealed that the combination of HA coating on am-Al(OH)3 and dissolved CO2 decreased boric acid adsorption compared to adsorption on pure am-Al(OH)3.<p>The discoveries in this dissertation contribute significantly in understanding the effects of HA and dissolved CO2 has on boric acid adsorption in the environment. Since B speciation and the stability of am-Al(OH)3 mineral and HA changes with pH, the bioavailability of B is expected to change as well with pH. The adsorption on boric acid on am-Al(OH)3 and/or HA coated am-Al(OH)3 is expected to decrease the amount of boric acid available to plants. Therefore the nutrient management regimen will have to be modified for soils that are high in natural organic matter, carbonate and/or aluminum hydroxyl species.

No description available.

Thèse doctorat : Images et Systèmes : Villeurbanne, INSA : 2007. / Titre provenant de l'écran-titre. Bibliogr. p. 167-175.

The focus of this thesis was on the synthesis, characterization and application of ceria nanocubes. This thesis is divided into two main sections; the first section investigates the electronic properties of ceria nanocubes, and the second explores their catalytic applications towards alcohol oxidation reactions. The first project of this thesis consisted of the X-ray characterization of hydrothermally synthesized ceria nanocubes of various sizes. For the first time, the electronic properties of such nanocubes were systematically studied using high resolution XPS and XANES. It was found that the concentration of Ce3+ present within the nanocubes was independent of the particle size, as well as the Ce precursor used during synthesis. Throughout the analysis of the Ce 3d and 4d XPS spectra, it was observed that the surface of the ceria nanocube samples was undergoing photoreduction/damage over time. This damage was attributed to the samples’ exposure to high intensity X-ray radiation. This was confirmed through examination of the Ce M4,5- and N4,5-edge XANES spectra. From these results, it was clear that the concentration of Ce3+ on the surface of the ceria nanocubes was independent of particle size. This fact may become important when investigating their potential catalytic activity. The second project of this thesis concentrated on the analysis of the catalytic activity of a variety of CeO2, Au and Au/CeO2 catalysts towards the oxidation of benzyl alcohol. The low temperature oxidation reactions were studied using 1H NMR spectroscopy. It was observed that Au NPs, Au/bulk CeO2, and Au/CeO2 nanocubes in water and K2CO3 were active catalysts for this oxidation reaction at 60°C in both air and O2 (g) atmospheres. Surprisingly, however, the Au/bulk CeO2 and Au/CeO2 nanocube catalysts showed very similar activities. It was also found that ceria nanocubes alone, and Au25(SR)18/bulk CeO2 showed no activity for this reaction under similar conditions. It was determined that below a substrate to catalyst ratio of ~ 1500:1, the Au/CeO2 catalysts, which showed the highest activities, were mass-transport limited with respect to the O2 in the system. The turnover frequencies of the supported catalysts were approximately double those of the unsupported NPs. Furthermore, these reactions have indicated that activating Au25(SR)18/CeO2 for catalysis is a non-trivial task, and more work needs to be done to understand the activation of such clusters.

Bitumen-derived heavy gas oil contains large amounts of sulfur (~4.0 wt.%) and nitrogen (~0.4 wt.%), which need to be lowered before it becomes suitable as a feedstock for refineries. The most widely used upgrading process is hydrotreating, and the conventional catalyst used for hydrotreating is Ni or Co and Mo or W supported on γ-Al2O3. Additionally, environmentally driven regulations impose strict limits on sulfur and nitrogen levels in transportation fuels. Therefore, the main focus of this work was to enhance the activity of a NiMo supported catalyst through its modification and to improve its selectivity to removal of bulky sulfur- and nitrogen-containing compounds from heavy gas oil under industrial hydrotreating conditions. This work was divided into four phases, and this thesis summarizes the research outcomes of each phase. The first phase examined the effects of chelating ligands, specifically, ethylenediaminetetraacetic acid (EDTA), on hydrotreating activity and the sulfidation mechanism. EDTA was seen to have a beneficial effect on hydrotreating activity. Detailed mechanistic aspects of interactions between support and EDTA, EDTA and metallic species, support and metal, support and active phase, and metallic species and metallic species at different reaction conditions, were also studied. Characterization by XANES revealed that the presence of a chelating agent delayed nickel sulfidation, which was the main cause of improvement in hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) activities. It also showed that EDTA plays a role in redistribution of active phases during sulfidation and favors the formation of octahedral molybdenum oxides. The second phase studied the effects of support modification and combinations of different supports and EDTA. In this phase, several mesoporous materials, including M-SBA-15 (M= Al, Ti and Zr), mesoporous mixed metal oxides (TiO2-Al2O3, ZrO2-Al2O3 andSnO2-Al2O3) and mesoporous metal oxides (ZrO2, Al2O3), were synthesized and used as support materials for a NiMo catalyst. NiMo/M-SBA-15 catalysts showed higher HDS and HDN activities and, the increase in activity is attributed to incorporation of heteroatoms in an SBA-15 matrix, which resulted in increase in metal support interaction, acidic strength and dispersion of active metals. The addition of EDTA to these catalysts helps in the formation of octahedral molybdenum oxide, which are easily reducible during sulfidation. This is evident from the XANES Mo LIII-edge study of the oxide catalysts. The increase in hydrodenitrogenation (HDN), hydrodesulfurization (HDS) and hydrodearomatization (HDA) activities as compared to that shown by the NiMo/γ-Al2O3 catalyst were also observed on addition of EDTA in large-pore, high-surface-area mesoporous zirconia supported NiMo catalysts. The incorporation of different metal oxides in alumina, as in the case of mixed metal oxides, resulted in a change in acidic strength and metal support interactions. It was observed with acridine-FTIR analysis that the catalysts with higher acidic strength tightly held acridine at high temperatures. This implies that catalysts with higher acidity are prone to inhibition by nitrogen-containing compounds present in feed, which will affect catalytic activity. The HDS and HDN activities for hydrotreating of heavy gas oil suggest that mesoporous alumina and titania-alumina supported catalysts perform better as compared to the conventional NiMo/γ-Al2O3 catalyst. Therefore, the effects of EDTA to Ni molar ratio (EDTA/Ni = 0 to 2) on the activities of the NiMo/MesoAl2O3 and NiMo/MesoTiO2-Al2O3 catalysts were studied, and EDTA was observed to have a negative impact on catalytic activity for these catalysts. This is attributed to a decrease in the active metal dispersion in these catalysts caused by the addition of EDTA. The catalysts NiMo/MesoAl2O3 and NiMo/MesoTiO2-Al2O3 without EDTA showed high active metal dispersion due to their high surface area and ordered structure. The third phase studied the combined effects of phosphorus and EDTA on the hydrotreating activity of NiMo supported catalysts. The effects of method of phosphorus addition (sequential and co-impregnation method) were also studied. When phosphorus was added using a co-impregnation method, as in the catalyst NiMoP/MesoAl2O3(CI), an increase in HDN, HDA and HDS activities was observed. However, the catalysts containing both EDTA and phosphorus showed a decrease in HDS and HDN activities. The fourth phase included a kinetic study using the Power Law and L-H models. The catalyst, NiMoP/mesoAl2O3(CI), was found to have higher HDN and HDS activities as compared to a conventional γ-Al2O3 supported catalyst containing phosphorus.

Standard geochemical analysis methods, such as aqueous geochemistry analysis and mineralogical analysis, frequently are utilized to evaluate the effectiveness of passive treatment systems, though they do not necessarily provide information regarding the mechanism of removal. Two emerging analytical techniques have shown promise by providing additional information to improve characterization of treatment systems: X-ray absorption spectroscopy (XAS) and stable isotope analysis. In this thesis, these novel analytical techniques were integrated with standard geochemical measurements to better characterize contaminated sites as well as potential treatment technologies used to mitigate aqueous contaminant mobility. Laboratory experiments were used to evaluate the removal of Se(VI) form simulated groundwater using granular Fe0 (GI) and organic carbon (OC). Greater than 90 % removal of Se(VI) was observed for systems containing GI after 5 days of reaction time and only 15 % removal was observed in systems containing OC. Synchrotron radiation-based XAS analysis of the treatment materials indicated the presence of both Se(IV) and Se(0) on the edges of GI grains after 6 hours reaction time, with no evidence of oxidized Se after 5 days of reaction. Several analytical techniques were integrated to characterize sediment contaminated with Hg and other contaminants through previous industrial practices. Analysis of the sediment by XAS indicated the possible presence of mercury selenide and copper sulfide. Resuspension tests were performed in oxic and anoxic conditions to simulate the effects of changing geochemical conditions of Hg release from sediments during dredging operations. The results indicated a higher release of Hg under oxic conditions in some sediment locations, suggesting that oxidative degradation of organic carbon or oxidative dissolution of Hg sulfides contributed to Hg release. The treatment of aqueous Hg(II) was evaluated with a variety of treatment media, including clay and GI. Treatment with GI was rapid, with 90 % removal observed after 2 hours reaction time. Extended X-ray absorption fine structure (EXAFS) analysis indicated the presence of Hg-O bonding on GI, suggesting that Hg was bound to Fe oxides formed on the surface of corroded GI. A new conceptual model for tracking the stable isotope fractionation of sulfur was coupled to the reactive transport model MIN3P to determine the effects of secondary transformations on sulfur cycling in passive treatment systems. Minor differences were noted when comparing the transport model-derived fractionation factor to calculations using a simplified Rayleigh distillation model, possibly indicating the effect of SO4 precipitation. The incorporation of stable isotope modeling provides a framework for the modeling of other isotope systems in treatment technologies.

Doctor of Philosophy (PhD) / The toxicity of platinum anticancer drugs presents a major obstacle in the effective treatment of tumours. Much of the toxicity stems from a lack of specificity of the drugs for the sites at which they are able to exert maximum anticancer activity. An improved understanding of the behaviour of the drugs in the tumour environment may assist in the rational design of future platinum anticancer agents with enhanced specificity and reduced toxicity. In the work presented herein, the specificity of two classes of platinum anticancer agents was assessed (platinum(IV) cisplatin analogues and platinum(II) anthraquinone complexes). The interaction of the platinum(IV) agents with DNA, believed to be their main cellular target, was examined using XANES spectroscopy. This experiment was designed to assess the ability of the drugs to interact with DNA and thus exert their anticancer activity. It was shown that the platinum(IV) complexes were not reduced by DNA during 48 hr incubation. It was not possible to conclusively determine whether the interaction of the complexes with DNA was direct or platinum(II) catalysed, or whether interaction had occurred at all. The distribution of platinum(II) anthraquinone complexes and their corresponding anthraquinone ligands in tumour cells (A2780 ovarian and DLD-1 colon cancer cell lines) was investigated. The cytotoxicity of the compounds in DLD-1 cells was also assessed. It was found that the compounds were efficiently taken up into the cells and entered the lysosomal compartments almost exclusively. This suggested that the cytotoxicity of the drugs was caused by lysosomal disruption, or that the platinum complexes were degraded, leaving a platinum species to enter the cell nuclei and interact with DNA. Alternatively, the complexes may bind to proteins and transport into the nuclei of the cells, though with their fluorescence quenched by the protein. The penetration and distribution of platinum(IV) complexes was assessed in DLD-1 multicellular tumour spheroids (established models of solid tumours) using a number of synchrotron techniques, including micro-tomography, micro-SRIXE, and micro-XANES. The complexes were found to be capable of penetrating throughout the entire volume of the spheroids. Micro-XANES indicated that in central and peripheral spheroidal regions, bound platinum species were present largely as platinum(II).