Steroid sulfatase (STS) catalyzes the desulfation of sulfated steroids such as estrone sulfate to the corresponding steroid such as estrone. Inhibitors of STS are believed to have potential for treating estrogen-dependent breast cancer. A new class of potential irreversible suicide inhibitors of STS, based on aryl sulfates bearing a monofluoromethyl or difluoromethyl group ortho to the sulfate group, was synthesized. Key to the success of these syntheses was the use of new sulfation methodology recently developed in the Taylor group. A new and efficient route to 4-formyl estrone, a time-dependent, irreversible STS inhibitor, is also reported. Several new classes of potential, reversible STS inhibitors were synthesized. These compounds are analogs of known STS substrates in which the sulfate group is replaced with an ???,??????-difluoromethylenesulfonamide group, a boronic acid group or a sulfinic acid group. We also report the synthesis of estrone sulfate analogs that bear a carboxylate moiety at the 17-position and a sulfate surrogate at the 3-position. It is anticipated that these compounds will inhibit STS by interacting with Arg98 which lies at the periphery of the active site. Key to the success of this synthesis was the use of the t-butyl group as a protecting group for the 2-position of estrone. Finally, our preliminary investigations into the synthesis of a new class of chiral electrophilic fluorinating agents are presented. These reagents are based on a chiral binaphthyl sulfonimide scaffold and are expected to be capable of performing enantioselective electrophilic fluorinations. Such reagents may be useful in synthesizing organofluorines of biological significance including STS inhibitors.

Steroid sulfatase (STS) catalyzes the desulfation of sulfated steroids such as estrone sulfate to the corresponding steroid such as estrone. Inhibitors of STS are believed to have potential for treating estrogen-dependent breast cancer. A new class of potential irreversible suicide inhibitors of STS, based on aryl sulfates bearing a monofluoromethyl or difluoromethyl group ortho to the sulfate group, was synthesized. Key to the success of these syntheses was the use of new sulfation methodology recently developed in the Taylor group. A new and efficient route to 4-formyl estrone, a time-dependent, irreversible STS inhibitor, is also reported. Several new classes of potential, reversible STS inhibitors were synthesized. These compounds are analogs of known STS substrates in which the sulfate group is replaced with an ,-difluoromethylenesulfonamide group, a boronic acid group or a sulfinic acid group. We also report the synthesis of estrone sulfate analogs that bear a carboxylate moiety at the 17-position and a sulfate surrogate at the 3-position. It is anticipated that these compounds will inhibit STS by interacting with Arg98 which lies at the periphery of the active site. Key to the success of this synthesis was the use of the t-butyl group as a protecting group for the 2-position of estrone. Finally, our preliminary investigations into the synthesis of a new class of chiral electrophilic fluorinating agents are presented. These reagents are based on a chiral binaphthyl sulfonimide scaffold and are expected to be capable of performing enantioselective electrophilic fluorinations. Such reagents may be useful in synthesizing organofluorines of biological significance including STS inhibitors.

Zirconium tetrachloride (ZrF4) is extensively used in the manufacturing of zirconium metal. The concept of producing zirconium tetrafluoride from dissociated zircon and ammonium bifluoride is well established at the South African Nuclear Energy Corporation (Necsa) State Owned Company (SOC) Limited. Zirconium and hafnium are always found in the same minerals. In nuclear application zirconium is used for structural construction and as a cladding material for fuel, because of the low thermal neutron absorption, while hafnium is used as control rod in nuclear reactor, because of the high thermal neutron absorption. The methods of separating hafnium from zirconium prefer the use of ZrCl4 than ZrF4. This is because of the high solubility in both aqueous solutions and organic solvents and low sublimation temperature of ZrCl4, while ZrF4 is almost insoluble in organic solvent and has a high sublimation temperature. Thermodynamic evaluations showed that chlorinating ZrF4 with either CaCl2, KCl, LiCl or NaCl respectively was not favourable, while chlorinating ZrF4 with either BeCl2 or MgCl2 was favourable. But due to cost consideration chlorinating ZrF4 with BeCl2 was not investigated. A thermogravimetric apparatus was used to investigate the isothermal and the non-isothermal kinetics of chlorinating analytical grade ZrF4 with MgCl2. The thermogravimetric apparatus revealed that chlorination of ZrF4 commence at temperature above 350°C. Isothermal kinetics of chlorinating analytical grade ZrF4 with MgCl2 was investigated at temperatures of 400, 450, 480, 500°C. The reaction progressed towards completion prematurely before the isothermal temperatures were reached, due to a low heating rate of 20 °C/minutes was used to heat up the reaction mixture to the desired isothermal temperatures. As a result, the isothermal kinetics could not be determined. Heating rates of 5, 10, 15 and 20 °C/minutes were used to investigate the non-isothermal kinetics. The apparent activation energy of chlorinating ZrF4 with MgCl2 varied significantly when the non-isothermal kinetics was investigated. The variation was due to changes in the reaction mechanism. As a result, rate law of chlorinating ZrF4 with MgCl2 could not be determined due to variation of the apparent activation energy. Crude ZrF4 prepared at Necsa SOC ltd. was chlorinated with MgCl2, a mixture of MgCl2 and KCl, a mixture of MgCl2 and LiCl, and a mixture of MgCl2 and NaCl respectively. Chlorination of the crude ZrF4 was conducted at temperatures of 400, 450 and 500°C respectively. The aim of chlorinating the crude ZrF4 was to investigating the effect of the chlorinating on the purity of the produced ZrCl4. A batch reactor was used in this study. The reactor was divided into two sections, namely the reaction zone and the condensation zone. The diameter of the condensation zone was larger than that of the reaction zone. Reactants were placed into the reaction zone and the products were collected at the reaction zone and the condensation zone. Samples were collected from these products and analysed using for X-Ray Diffraction analysis (XRD) and Inductive Coupled Plasma Optical Emissions Spectroscopy (ICP-OES). XRD was used to identify the compounds that were present in the products and ICP-OES was used to determine the concentration of the elements that were present in the products. The analysis of the results obtained showed that the highest recovery of zirconium in the products collected from the condensation zone, the sublimed products, was achieved by chlorinating ZrF4 with MgCl2 at 500°C. About 80% was recovered. About 96% of the concentration of the impurities in the sublimed products was reduced when ZrF4 was chlorinated with a mixture of MgCl2 and LiCl at 450°C. About 36% of hafnium in the sublimed products was reduced when ZrF4 was chlorinated with a mixture of MgCl2 and NaCl at 400°C. / Chemical Engineering / M.Tech. (Chemical Engineering)

En raison de leurs nombreux avantages, les matériaux polymères sont aujourd'hui reconnus comme des éléments essentiels de notre quotidien. Ils composent une quantité importante d'objets de la vie courante dans lesquels ils ont souvent substitué les substances naturelles initialement utilisées. Néanmoins, pour une utilisation dans le domaine de l’emballage, ces matériaux présentent des contraintes non négligeables qui nécessitent une recherche permanente. L’amélioration et l’optimisation des propriétés d’imprimabilité, barrières aux gaz et de machinabilité représentent un enjeu crucial pour répondre aux nouvelles réglementations, législations mais aussi phénomènes sociétaux et exigences industrielles. La solution d'étude retenue ici est de traiter la surface de matériaux commerciaux. Les différents traitements plasma, relativement bien maitrisés sur ce type de matériaux, ont été combinés avec des procédés de fluoration, plus originaux. La fluoration directe est ainsi apparue comme une solution privilégiée du fait de son efficacité avérée sur ce type de matériaux. La maitrise des différents paramètres intrinsèques à chaque procédé a permis d’identifier l’unicité de chaque traitement et combinaison afin d’ajuster, non seulement la morphologie, mais surtout la composition de surface des films traités en fonction des propriétés ciblées. Des caractérisations spectroscopiques ont tout d’abord été mises en place pour identifier les mécanismes associés à chacun de ses traitements seuls ou combinés. La morphologie des surfaces a également été caractérisée par des techniques classiques de microscopie. Enfin, l’étude des propriétés résultantes et leur stabilité dans le temps ont permis de mettre en évidence l’intérêt de ces procédés pour améliorer les propriétés actuelles des films d’emballages et leur stabilité ; notamment leur imprimabilité, et leur comportement barrière aux gaz. / Currently, polymeric materials are currently well-recognized as essential elements of our daily life due to the advantages that they exhibit, in which they can replace the originally natural products. However, the use of these materials for packaging applications has still significant drawbacks. The interest of research on polymeric materials is potentially required in order to provide a good compromise of properties such as printability, gas barrier and machinability. Aims are to follow the new regulations, laws, but also societal phenomena and industrial phenomena.In this study, surface treatments were directly applied on material polymers dedicated to packaging applications. Plasma treatments, relatively well mastered, were combined with original fluorination processes. In comparison, direct fluorination was effectively used to increase polymer properties. Each treatment and their combination were carried out with various intrinsic parameters under control to adjust both surface morphology and surface composition of treated polymers according to targeted film properties.Spectroscopic characterizations were first monitored to identify the mechanisms associated with each treatment (alone or in combination). Surface morphology was also observed on standard microscopic techniques. The resulting properties and their long-termed stability were carried. These studies highlight the effectiveness of those treatments to improve the current properties of packaging films and stability: including printability, and barrier properties.

Zirconium tetrachloride (ZrF4) is extensively used in the manufacturing of zirconium metal. The concept of producing zirconium tetrafluoride from dissociated zircon and ammonium bifluoride is well established at the South African Nuclear Energy Corporation (Necsa) State Owned Company (SOC) Limited. Zirconium and hafnium are always found in the same minerals. In nuclear application zirconium is used for structural construction and as a cladding material for fuel, because of the low thermal neutron absorption, while hafnium is used as control rod in nuclear reactor, because of the high thermal neutron absorption. The methods of separating hafnium from zirconium prefer the use of ZrCl4 than ZrF4. This is because of the high solubility in both aqueous solutions and organic solvents and low sublimation temperature of ZrCl4, while ZrF4 is almost insoluble in organic solvent and has a high sublimation temperature. Thermodynamic evaluations showed that chlorinating ZrF4 with either CaCl2, KCl, LiCl or NaCl respectively was not favourable, while chlorinating ZrF4 with either BeCl2 or MgCl2 was favourable. But due to cost consideration chlorinating ZrF4 with BeCl2 was not investigated. A thermogravimetric apparatus was used to investigate the isothermal and the non-isothermal kinetics of chlorinating analytical grade ZrF4 with MgCl2. The thermogravimetric apparatus revealed that chlorination of ZrF4 commence at temperature above 350°C. Isothermal kinetics of chlorinating analytical grade ZrF4 with MgCl2 was investigated at temperatures of 400, 450, 480, 500°C. The reaction progressed towards completion prematurely before the isothermal temperatures were reached, due to a low heating rate of 20 °C/minutes was used to heat up the reaction mixture to the desired isothermal temperatures. As a result, the isothermal kinetics could not be determined. Heating rates of 5, 10, 15 and 20 °C/minutes were used to investigate the non-isothermal kinetics. The apparent activation energy of chlorinating ZrF4 with MgCl2 varied significantly when the non-isothermal kinetics was investigated. The variation was due to changes in the reaction mechanism. As a result, rate law of chlorinating ZrF4 with MgCl2 could not be determined due to variation of the apparent activation energy. Crude ZrF4 prepared at Necsa SOC ltd. was chlorinated with MgCl2, a mixture of MgCl2 and KCl, a mixture of MgCl2 and LiCl, and a mixture of MgCl2 and NaCl respectively. Chlorination of the crude ZrF4 was conducted at temperatures of 400, 450 and 500°C respectively. The aim of chlorinating the crude ZrF4 was to investigating the effect of the chlorinating on the purity of the produced ZrCl4. A batch reactor was used in this study. The reactor was divided into two sections, namely the reaction zone and the condensation zone. The diameter of the condensation zone was larger than that of the reaction zone. Reactants were placed into the reaction zone and the products were collected at the reaction zone and the condensation zone. Samples were collected from these products and analysed using for X-Ray Diffraction analysis (XRD) and Inductive Coupled Plasma Optical Emissions Spectroscopy (ICP-OES). XRD was used to identify the compounds that were present in the products and ICP-OES was used to determine the concentration of the elements that were present in the products. The analysis of the results obtained showed that the highest recovery of zirconium in the products collected from the condensation zone, the sublimed products, was achieved by chlorinating ZrF4 with MgCl2 at 500°C. About 80% was recovered. About 96% of the concentration of the impurities in the sublimed products was reduced when ZrF4 was chlorinated with a mixture of MgCl2 and LiCl at 450°C. About 36% of hafnium in the sublimed products was reduced when ZrF4 was chlorinated with a mixture of MgCl2 and NaCl at 400°C. / Chemical Engineering / M.Tech. (Chemical Engineering)

Des carbones dérivés de carbures à porosité monodisperse et nanocentrée autour de 0,6 nm ont été préparés par fluoration de carbures via l’arrachement sélectif de l’élément métallique et le maintien de l’empreinte carbonée initiale. Les carbures précurseurs ont été choisis parmi deux des classes de carbures à savoir interstitiels pour le carbure de titane et de niobium et covalents pour le carbure de silicium. La fluoration directe procédant sous flux d’une atmosphère de fluor pur apparait comme étant la seule méthode de fluoration apte à déstabiliser les poudres cristallisées. Appliquée au carbure de titane, des matériaux à teneur variable en carbone et en trifluorure de titane ont été obtenus et caractérisés structuralement par Diffraction des Rayons X quantitative, spectroscopies IR et Raman et leur texture sondée par Microscopie Electronique à Balayage et à Transmission et isothermes d’adsorption à l’azote à 77K. Ils ont aussi été évalués comme matériau d’électrode de supercondensateurs. La fluoration du carbure de silicium pour la stabilisation d’une phase carbonée est plus difficile et seule l’abaissement de la cristallinité du carbure par l’utilisation d’une mise en forme de type couche mince combinée à une méthode de fluoration alternative par décomposition de l’agent fluorant XeF2 ont permis d’obtenir une couche mince de carbone nanostructurée valorisable comme lubrifiant solide et aux propriétés de mouillabilité modulables. / Carbide-derived Carbons (CDC) with monodisperse ultramicroporosity have been prepared by carbide fluorination thanks to selective etching of metallic element. The chosen carbides precursors were titanium and niobium carbides, and silicon carbides from interstitial and covalent carbide family, respectively. Direct fluorination proceeding by a pure flow of 1 atm. of molecular fluorine is the only fluorination way which leads to the transformation of the powdered and highly crystallized carbide into some carbons. Materials with different ratio of carbon and solid titanium trifluoride were successfully obtained by direct fluorination of titanium carbide, characterized by quantitative XRD, IR and Raman spectroscopies and Scanning and Transmission Electronic Microscopies and used in supercapacitors. The direct fluorination of silicon carbide in order to form carbon is more difficult because of the competition between carbon formation and its degradation into gaseous carbon fluorides. To success in our goal, thin film morphology was used as precursor. However, an accurate fluorination way is needed and decomposition of XeF2 fluorinating agent was chosen. Thin films with variable thickness of nanostructured carbon at the surface were obtained and used as solid lubricant with tunable wettability properties.