952 resultados para Catalytic Selectivity
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This work describes further developments and applications of the catalytic asymmetric Fischer indolization. In the first part of this thesis, the development of an organocatalytic asymmetric synthesis of helicenes via a Fischer indolization is discussed. The application of a novel SPINOL-derived phosphoric acid, featuring extended π-surfaces as 3,3‘-substituents which can potentially participate in π-interactions with the polyaromatic intermediate, afforded the corresponding products in high yields and enantioselectivities. The second part of this work describes the development of a catalytic asymmetric dearomatizing synthesis of 1,4-diketones via an interrupted Fischer indolization. Employing aryl hydrazines with α-substituents next to the hydrazine group prevents the rearomatization which takes place in common Fischer indole syntheses, thus enabling the hydrolysis of the generated diimine species. In the presence of STRIP as catalyst, a variety of different 1,4-diketones could be obtained in generally high yields, diastereo- and enantioselectivities. The last part of this thesis deals with the development of an organocatalytic asymmetric stereodivergent synthesis of novel 3H- and 2H-pyrroles, applying an interrupted Fischer indolization and for the 2H-pyrroles a subsequent stereospecific [1,5]-alkyl shift. Employing STRIP as catalyst afforded the corresponding products in good to excellent yields and enantioselectivities. Preliminary biological investigations of these novel structure motifs in cell-based assays, monitoring biological signal transduction pathways showed an inhibition of the Hedgehog signaling pathway in a μM range.
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The reaction of the Schiff base (3,5-di-tert-butyl-2-hydroxybenzylidene)-2-hydroxybenzohydrazide (H3L) with a copper(II) salt of a base of a strong acid, i.e., nitrate, chloride or sulphate, yielded the mononuclear complexes [Cu(H2L)(NO3)(H2O)] (1), [Cu(H2L)Cl]center dot 2MeOH (2) and the binuclear complex [{Cu(H2L)}(2)(mu-SO4)]center dot 2MeOH (3), respectively, with H2L- in the keto form. Compounds 1-3 were characterized by elemental analysis, Infrared (IR) spectroscopy, Electrospray Ionisation-Mass Spectrometry (ESI-MS) and single crystal X-ray crystallography. All compounds act as efficient catalysts towards the peroxidative oxidation of cyclohexane to cyclohexyl hydroperoxide, cyclohexanol and cyclohexanone, under mild conditions. In the presence of an acid promoter, overall yields (based on the alkane) up to 25% and a turnover number (TON) of 250 (TOF of 42 h(-1)) after 6 h, were achieved.
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Due to diminishing petroleum reserves, unsteady market situation and the environmental concerns associated with utilization of fossil resources, the utilization of renewables for production of energy and chemicals (biorefining) has gained considerable attention. Biomass is the only sustainable source of organic compounds that has been proposed as petroleum equivalent for the production of fuels, chemicals and materials. In fact, it would not be wrong to say that the only viable answer to sustainably convene our future energy and material requirements remain with a bio-based economy with biomass based industries and products. This has prompted biomass valorization (biorefining) to become an important area of industrial research. While many disciplines of science are involved in the realization of this effort, catalysis and knowledge of chemical technology are considered to be particularly important to eventually render this dream to come true. Traditionally, the catalyst research for biomass conversion has been focused primarily on commercially available catalysts like zeolites, silica and various metals (Pt, Pd, Au, Ni) supported on zeolites, silica etc. Nevertheless, the main drawbacks of these catalysts are coupled with high material cost, low activity, limited reusability etc. – all facts that render them less attractive in industrial scale applications (poor activity for the price). Thus, there is a particular need to develop active, robust and cost efficient catalytic systems capable of converting complex biomass molecules. Saccharification, esterification, transesterification and acetylation are important chemical processes in the valorization chain of biomasses (and several biomass components) for production of platform chemicals, transportation fuels, food additives and materials. In the current work, various novel acidic carbons were synthesized from wastes generated from biodiesel and allied industries, and employed as catalysts in the aforementioned reactions. The structure and surface properties of the novel materials were investigated by XRD, XPS, elemental analysis, SEM, TEM, TPD and N2-physisorption techniques. The agro-industrial waste derived sulfonic acid functionalized novel carbons exhibit excellent catalytic activity in the aforementioned reactions and easily outperformed liquid H2SO4 and conventional solid acids (zeolites, ion-exchange resins etc). The experimental results indicated strong influence of catalyst pore-structure (pore size, pore-volume), concentration of –SO3H groups and surface properties in terms of the activity and selectivity of these catalysts. Here, a large pore catalyst with high –SO3H density exhibited the highest esterification and transesterification activity, and was successfully employed in biodiesel production from fatty acids and low grade acidic oils. Also, a catalyst decay model was proposed upon biodiesel production and could explain that the catalyst loses its activity mainly due to active site blocking by adsorption of impurities and by-products. The large pore sulfonated catalyst also exhibited good catalytic performance in the selective synthesis of triacetin via acetylation of glycerol with acetic anhydride and out-performed the best zeolite H-Y with respect to reusability. It also demonstrated equally good activity in acetylation of cellulose to soluble cellulose acetates, with the possibility to control cellulose acetate yield and quality (degree of substitution, DS) by a simple adjustment of reaction time and acetic anhydride concentration. In contrast, the small pore and highly functionalized catalysts obtained by hydrothermal method and from protein rich waste (Jatropha de-oiled waste cake, DOWC), were active and selective in the esterification of glycerol with fatty acids to monoglycerides and saccharification of cellulosic materials, respectively. The operational stability and reusability of the catalyst was found to depend on the stability of –SO3H function (leaching) as well as active site blocking due to adsorption of impurities during the reaction. Thus, our results corroborate the potential of DOWC derived sulfated mesoporous active carbons as efficient integrated solid acid catalysts for valorization of biomass to platform chemicals, biofuel, bio-additive, surfactants and celluloseesters.
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Catch effort data on which fisheries management regulations are sometimes based are not available for most lakes in Uganda. However, failure to regulate fishing gears and methods has been a major cause of collapse of fisheries in the country. Fisheries have been damaged by destructive and non-selective fishing gears and methods such as trawling and beach seining, by use of gill nets of mesh size which crop immature fish and by introduction of mechanised fishing. Selectivity of gears used to crop Lates niloticus L.(Nile perch), Oreochromis niloticus L. (Nile tilapia) and Rastrineobola argentea Pellegrin (Mukene) which are currently the most important commercial species in Uganda were examined in order to recommend the most suitable types, sizes and methods that should be used in exploiting these fisheries. Gill nets of less than 127 mm mainly cropped immature Nile tilapia and Nile perch. To protect these fisheries, the minimum mesh size of gill nets should be set at 127 mm. Seine nets of 5 mm caught high proportions in immature Mukene while those of 10 mm caught mainly mature Mukene. When operated inshore, both sizes caught immature Nile perch and Nile tilapia as by-catch. To protect the Mukene fishery and avoid catching immature bye-catch, a minimum mesh size of the Mukene net should be 10 mm operated as Lampara type net offshore, but since most fishermen have been using 5 mm seine nets for over five years the minimum size should not be allowed to drop below 5 mm pending further thorough investigations. Beach seining and trawling are destructive to fisheries and should be prohibited until data that may justify their use is available.
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La catalyse joue un rôle essentiel dans de nombreuses applications industrielles telles que les industries pétrochimique et biochimique, ainsi que dans la production de polymères et pour la protection de l’environnement. La conception et la fabrication de catalyseurs efficaces et rentables est une étape importante pour résoudre un certain nombre de problèmes des nouvelles technologies de conversion chimique et de stockage de l’énergie. L’objectif de cette thèse est le développement de voies de synthèse efficaces et simples pour fabriquer des catalyseurs performants à base de métaux non nobles et d’examiner les aspects fondamentaux concernant la relation entre structure/composition et performance catalytique, notamment dans des processus liés à la production et au stockage de l’hydrogène. Dans un premier temps, une série d’oxydes métalliques mixtes (Cu/CeO2, CuFe/CeO2, CuCo/CeO2, CuFe2O4, NiFe2O4) nanostructurés et poreux ont été synthétisés grâce à une méthode améliorée de nanocasting. Les matériaux Cu/CeO2 obtenus, dont la composition et la structure poreuse peuvent être contrôlées, ont ensuite été testés pour l’oxydation préférentielle du CO dans un flux d’hydrogène dans le but d’obtenir un combustible hydrogène de haute pureté. Les catalyseurs synthétisés présentent une activité et une sélectivité élevées lors de l’oxydation sélective du CO en CO2. Concernant la question du stockage d’hydrogène, une voie de synthèse a été trouvée pour le composét mixte CuO-NiO, démontrant une excellente performance catalytique comparable aux catalyseurs à base de métaux nobles pour la production d’hydrogène à partir de l’ammoniaborane (aussi appelé borazane). L’activité catalytique du catalyseur étudié dans cette réaction est fortement influencée par la nature des précurseurs métalliques, la composition et la température de traitement thermique utilisées pour la préparation du catalyseur. Enfin, des catalyseurs de Cu-Ni supportés sur silice colloïdale ou sur des particules de carbone, ayant une composition et une taille variable, ont été synthétisés par un simple procédé d’imprégnation. Les catalyseurs supportés sur carbone sont stables et très actifs à la fois dans l’hydrolyse du borazane et la décomposition de l’hydrazine aqueuse pour la production d’hydrogène. Il a été démontré qu’un catalyseur optimal peut être obtenu par le contrôle de l’effet bi-métallique, l’interaction métal-support, et la taille des particules de métal.
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Portugal’s Northeast production of sheep and goats are based on the exploitation of landscape by-products such as spontaneous native vegetation and agriculture leftovers. Shepherds tend the flocks throughout grazing itineraries every day, crossing a mosaic of patches of varied land uses. During the journey, the shepherd acts together with the sheep and goats to select each patch in creating an ordered sequence of land uses. The focus of the research is on the land-use composition of the grazing itineraries; determinate how they depend on the patterns of the landscape mosaic. It is utilized a data set of 26 monthly herd’s itineraries, 13 of sheep and 13 of goats, to investigate the relationship of the land uses crossed by the flocks and the land uses of the landscape, evaluating the land-use preferences and selectivity of the sheep and goats. It is utilized the divergences in the time spent and distance travelled by the herds and the area of the land uses in the landscape, the chi-square test to relate the preferred land used and the season, and the discriminate analysis to distinguish the preferences and the selectivity of the herd of sheep and the herd of goats. The herds of the sheep and the goats presented different land-use preferences over the seasons and the discriminant analysis shows that they have different landscape preferences. The herd of sheep has the highest selectivity indexes for the annual irrigated crops, the agricultural complex systems and the agroforestry land uses. The highest selectivity indexes for the herd of goats were found for the deciduous forest, the agriculture with natural and semi-natural spaces and the shrublands land uses. It was concluded that the landscape management for sheep and goats herding has to be different: the agricultural land uses are essential to the flocks of sheep and the forest land uses are decisive to the flocks of goats.
Catalytic asymmetric synthesis of alfa,alfa-disubstituted alfa-thio- and alfa-amino acid derivatives
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449 p.
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Four magnetic carbon nanotube samples (CNTs: undoped, completely N-doped and two selectively N-doped) have been synthesized by chemical vapor deposition. The materials were tested in the catalytic wet peroxide oxidation (CWPO) of highly concentrated 4 nitrophenol solutions (4-NP, 5 g L-1). Relatively mild operating conditions were considered (atmospheric pressure, T = 50 ºC, pH = 3), using a catalyst load of 2.5 g L-1 and the stoichiometric amount of H2O2 needed for the complete mineralization of 4-NP. N doping was identified to influence considerably the CWPO performance of the materials. In particular, undoped CNTs, with a moderate hydrophobicity, favor the controllable and efficient decomposition of H2O2 into highly reactive hydroxyl radicals (HO•), thus showing high catalytic activity for 4-NP degradation. On the other hand, the completely N-doped catalyst, fully hydrophilic, favors a quick decomposition of H2O2 into non-reactive O2 and H2O species. The selectively N-doped amphiphilic catalysts, i.e. hybrid structures containing undoped sections followed by N-doped ones, provided intermediate results, namely: a higher N content favored H2O2 decomposition towards non-reactive H2O and O2 species, whilst a lower N content resulted in the formation of HO•, increasing 4-NP mineralization. Catalyst stability and reusability were also investigated by consecutive CWPO runs.
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Novel magnetic carbon xerogels consisting of interconnected carbon microspheres with iron and/or cobalt microparticles embedded in their structure were developed by a simple route. As inferred from the characterization data, materials with distinctive properties may be directly obtained upon inclusion of iron and/or cobalt precursors during the sol-gel polymerization of resorcinol and formaldehyde, followed by thermal annealing. The unique properties of these magnetic carbon xerogels were explored in the catalytic wet peroxide oxidation (CWPO) of an antimicrobial agent typically found throughout the urban water cycle – sulfamethoxazole (SMX). A clear synergistic effect arises from the inclusion of cobalt and iron in carbon xerogels (CX/CoFe),the resulting magnetic material revealing a better performance in the CWPO of SMX at the ppb level(500 microg L−1) when compared to that of monometallic carbon xerogels containing only iron or cobalt.This effect was ascribed to the increased accessibility of highly active iron species promoted by the simultaneous incorporation of cobalt.The performance of the CWPO process in the presence of CX/CoFe was also evaluated in environmentally relevant water matrices, namely in drinking water and secondary treated wastewater, considered in addition to ultrapure water. It was found that the performance decreases when applied to more complex water and wastewater samples. Nevertheless, the ability of the CWPO technology for the elimination of SMX in secondary treated wastewater was unequivocally shown, with 96.8% of its initial content being removed after 6 h of reaction in the presence of CX/CoFe, at atmospheric pressure, room temperature(T = 25◦C), pH = 3, [H2O2]0= 500 mg L−1and catalyst load = 80 mg L−1. A similar performance (97.8% SMX removal) is obtained in 30 min when the reaction temperature is slightly increased up to 60◦C in an ultra-pure water matrix. Synthetic water containing humic acid, bicarbonate, sulphate or chloride, was also tested. The results suggest the scavenging effect of the different anions considered, as well as the negative impact of dissolved organic matter typically found in secondary treated wastewater, as simulated by the presence of humic acid.An in-situ magnetic separation procedure was applied for catalyst recovery and re-use during reusability cycles performed to mimic real-scale applications. CWPO runs performed with increased SMX concentration (10 mg L−1), under a water treatment process intensification approach, allowed to evalu-ate the mineralization levels obtained, the antimicrobial activity of the treated water, and to propose adegradation mechanism for the CWPO of SMX.
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Aiming to introduce a multiresidue analysis for the trace detection of pesticide residues belonging to organophosphorus and triazine classes from olive oil samples, a new sample preparation methodology comprising the use of a dual layer of “tailor-made” molecularly imprinted polymers (MIPs) SPE for the simultaneous extraction of both pesticides in a single procedure has been attempted. This work has focused on the implementation of a dual MIP-layer SPE procedure (DL-MISPE) encompassing the use of two MIP layers as specific sorbents. In order to achieve higher recovery rates, the amount of MIP layers has been optimized as well as the influence of MIP packaging order. The optimized DL-MISPE approach has been used in the preconcentration of spiked organic olive oil samples with concentrations of dimethoate and terbuthylazine similar to the maximum residue limits and further quantification by HPLC. High recovery rates for dimethoate (95%) and terbuthylazine (94%) have been achieved with good accuracy and precision. Overall, this work constitutes the first attempt on the development of a dual pesticide residue methodology for the trace analysis of pesticide residues based on molecular imprinting technology. Thus, DL-MISPE constitutes a reliable, robust, and sensitive sample preparation methodology that enables preconcentration of the target pesticides in complex olive oil samples, even at levels similar to the maximum residue limits enforced by the legislation.
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O objectivo principal deste trabalho foi estudar as propriedades e comportamento de polioxotungstatos (POM) do tipo Keggin com interesse em catálise oxidativa. Os estudos efectuados centraram-se no comportamento electroquímico dos aniões em meio não aquoso, na estabilidade das suas estruturas em diferentes meios, na sua capacidade de catalisar a oxidação de diferentes substratos orgânicos e na sua eficácia em oxidar, de forma selectiva, um modelo não fenólico da lenhina. Efectuou-se, igualmente, o estudo estrutural de diversos aniões pela técnica de EXAFS. Neste trabalho, prepararam-se e caracterizaram-se alguns dos sais de tetra-n-butilamónio (TBA) dos polioxotungstatos estudados: compostos de Keggin, TBAx[XW12O40], lacunares, TBAxHy[XW11O39], mono-substituídos, TBAxHy[XW11M(H2O)O39]·nH2O, com X= P e Si e M = CoII, NiII, ZnII, CuIl, RuIII, MnIII e FeIII e os compostos com mistura de átomos adenda TBAx[XW11VO40]·nH2O (X = P e Si). Seleccionou-se este conjunto de polioxotungstatos de forma a efectuar-se um estudo comparativo da influência da natureza do heteroátomo central (P e Si) e dos metais de transição M nas propriedades estudadas. O conjunto de sais de TBA dos silicotungstatos estudados mostraram ser isoestruturais, apresentando a mesma estrutura dos fosfotungstatos análogos. O comportamento electroquímico dos polioxotungstatos foi estudado em soluções de acetonitrilo por voltametria cíclica e electrólise a potencial controlado. Verificou-se a ocorrência de vários processos mono-electrónicos de oxi-redução, reversíveis ou quasi-reversíveis, associados aos átomos de WVI/V e a alguns dos metais de transição. Os metais em estado de oxidação +3 reduziram-se mais facilmente do que os átomos de WVI. O metal CuII apresentou um comportamento diferente dos outros metais de transição. Este metal, na estrutura do POM, reduziu-se a CuI, proporcionando a observação do anião [PW11CuIO39]6- pela primeira vez. A redução posterior do CuI conduziu à formação de Cu0, que se depositou na superfície do eléctrodo. A re-oxidação do cobre a CuII conduziu à reconstituição da estrutura do POM, nas condições estudadas. Constatou-se que a ocorrência de protões na fórmula molecular dos POMs influenciou o seu comportamento electroquímico. Para os compostos que apresentam protões, a redução dos átomos de tungsténio ocorreu a potenciais menos negativos do que para aqueles que não apresentam protões na sua fórmula. Para os primeiros observou-se a transferência global de um maior número de electrões no mesmo intervalo de potencial, originando soluções fortemente azuladas. Quando os catiões tetra-n-butilamónio foram substituídos por catiões de menor dimensão, como Li+ e Na+, ocorreu a formação de pares iónicos com os polianiões [PW12O40]3- e [SiW11VO40]5-, originando um aumento do potencial de redução. Não houve evidência da formação de pares iónicos com os catiões TBA+. Este foi o primeiro estudo sistemático do comportamento electroquímico dos aniões lacunares e mono-substituídos em meio não aquoso. Estudou-se a estrutura dos polioxotungstatos em sais de TBA e em soluções de acetonitrilo. A aplicação da técnica de EXAFS ao estudo deste tipo de compostos em solução foi realizada pela primeira vez. Pela análise estrutural nos sólidos verificou-se que, a natureza do metal de transição M e do átomo central X, na estrutura do POM, influenciam o tamanho dos vários octaedros que o constituem. Não se observaram diferenças significativas nas estruturas dos polianiões em solução. A estabilidade da estrutura dos polioxometalatos na presença de um excesso de H2O2, em soluções de acetonitrilo/H2O foi analisada por espectroscopia de absorção de EXAFS, RMN de 31P, IV e espectrofotometria de absorção no UV-Vis. De uma forma geral, os POMs em que o átomo central da estrutura é o Si apresentaram maior estabilidade do que os POMs correspondentes com átomo de P no centro. Em solução de acetonitrilo, na ausência de H2O2, todos os aniões mostraram ser estáveis durante vários dias. Em solução, na presença de H2O2 em excesso (H2O2/POM = 1300), o anião lacunar [PW11O39]7- não é estável, transformando-se no anião de Venturello, {PO4[W(O)(O2)2]4}3-, após a formação de [PW12O40]3-, como produto intermediário. Em relação aos aniões substituídos [PW11M(H2O)O39]p-, M = MnIII, RuIII, FeIII, CoII e ZnII, verificou-se o seguinte na presença de H2O2: os aniões com MnIII e CoII transformaram-se no anião de Keggin, [PW12O40]3-. Os aniões de RuIII e FeIII mantiveram as suas estruturas e o anião de ZnII decompôs-se em {HPO4[W(O)(O2)2]2}2- e fosfato. Para estes casos de não estabilidade estrutural, o processo de decomposição foi mais rápido na presença de maiores conteúdos de água. Pela análise de EXAFS, na presença de um menor excesso de H2O2 (H2O2/POM = 70) e apenas 8% de parte aquosa, verificou-se que os aniões substituídos por MnIII mantiveram a sua estrutura, embora o ligando H2O, coordenado ao Mn, tivesse sido substituído por um grupo oxo no polianião [SiW11Mn(H2O)O39]5-, e por um grupo peroxo no polianião [PW11Mn(H2O)O39]4-. O anião com RuIII, nestas condições, também mostrou substituir o seu ligando H2O por um grupo peroxo ou hidrogenoperoxo. Os polioxotungstatos mono-substituídos e lacunares mostraram ser catalisadores eficientes para a oxidação de cis-cicloocteno, geraniol e ciclooctano com H2O2. A maior novidade deste trabalho residiu na actividade catalítica apresentada pelos silicotungstatos estudados, contrariando o que é referido na literatura. Outro aspecto inovador foi o elevado valor de conversão obtido para a oxidação de ciclooctano. Este substrato foi oxidado com 74% de conversão, após 2h de reacção e com 80% de selectividade para o hidroperóxido de ciclooctilo, na presença do anião [PW11Fe(H2O)O39]4-. Os restantes produtos de reacção foram o ciclooctanol e a ciclooctanona. Os silicotungstatos apresentaram maior selectividade para o hidroperóxido de ciclooctilo do que os fosfotungstatos. O geraniol foi completamente oxidado após 3h de reacção, com 82% de selectividade para o 2,3-epoxigeraniol, na presença do anião [PW11Mn(H2O)O39]4-. O cis-cicloocteno foi oxidado ao seu epóxido, com 92% de conversão ao fim de 5h de reacção, na presença do anião lacunar [PW11O39]7-. O estudo da capacidade oxidativa do anião [SiW11VO40]5- foi analisada utilizando-se um modelo não fenólico da lenhina, a anisoína. Estudaram-se as condições favoráveis à obtenção de uma reacção selectiva para o anisilo, de forma a poder estudar-se a cinética da reacção. A estequiometria da reacção mostrou ser de 1:2 anisoína/POM. As ordens de reacção foram determinadas pelo método das velocidades iniciais e, a partir destes resultados, conheceu-se que o POM não estava envolvido no passo que limita a velocidade da reacção, sendo esta limitada pela transformação da anisoína. O estudo realizado sobre o efeito isotópico sugeriu que o passo que limitou a velocidade de reacção correspondeu à enolação da anisoína. Desta forma, observou-se pela primeira vez, que o POM oxida um modelo não fenólico da lenhina por via de enolação.
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Bimetallic alloys are increasingly used in heterogeneous catalysis. This interest is explained by the emergence of new features that are absent in the parent single metals. Synergistic effects between the two combined elements create a more efficient catalyst. One of the most challenging aspect of multicomponent materials in catalysis is the ability to fine-tune the catalytic properties of an alloy by controlling the nature and composition of the surface [1]. For example, the gold/silver alloy combines a high activity and a large selectivity for a broad range of oxidation reaction.It is well established that the surface composition of alloys may deviate from that of the bulk phase. Surface enrichment has also important consequences in some applications of heterogeneous catalysis. In some cases, the thermal and chemical treatments can lead to opposite trends regarding the nature of the metal prone to surface enrichment. Using atom probe tomography we aim to link the physicochemical conditions the composition of the very first atomic layers of bimetallic catalysts and eventually to fine-tune the catalytic features of the latter.
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Les sulfilimines et les sulfoximines sont des motifs structuraux dont l’intérêt synthétique est grandissant, notamment du fait de leurs applications en chimie médicinale et en agrochimie. Les travaux rapportés dans cet ouvrage décrivent le développement de nouvelles méthodes de synthèse efficaces pour la production de ces unités atypiques. Ces méthodes sont basées sur la réactivité d’une source d’azote électrophile, vis-à-vis de thioéthers et de sulfoxydes. L’utilisation d’un complexe métallique introduit en quantité catalytique a permis de favoriser le processus réactionnel. En tirant bénéfice de l’expertise de notre groupe de recherche sur le développement de réactions d’amination stéréosélectives de liaisons C-H et d’aziridination de styrènes, nous avons d’abord étudié la réactivité des N-mésyloxycarbamates comme source d’azote électrophile. Après avoir optimisé sa synthèse sur grande échelle, ce réactif chiral a été utilisé dans des réactions d’amination de thioéthers et de sulfoxydes, catalysées par un dimère de rhodium (II) chiral. Un processus diastéréosélectif efficace a été mis au point, permettant de produire des sulfilimines et des sulfoximines chirales avec d’excellents rendements et sélectivités. Au cours de l’optimisation de cette méthode de synthèse, nous avons pu constater l’effet déterminant de certains additifs sur la réactivité et la sélectivité de la réaction. Une étude mécanistique a été entreprise afin de comprendre leur mode d’action. Il a été observé qu’une base de Lewis telle que le 4-diméthylaminopyridine (DMAP) pouvait se coordiner au dimère de rhodium(II) et modifier ses propriétés structurales et redox. Les résultats que nous avons obtenus suggèrent que l’espèce catalytique active est un dimère de rhodium de valence mixte Rh(II)/Rh(III). Nous avons également découvert que l’incorporation de sels de bispyridinium avait une influence cruciale sur la diastéréosélectivité de la réaction. D’autres expériences sur la nature du groupe partant du réactif N-sulfonyloxycarbamate nous ont permis de postuler qu’une espèce nitrénoïde de rhodium était l’intermédiaire clé du processus d’amination. De plus, l’exploitation des techniques de chimie en débit continu nous a permis de développer une méthode d’amination de thioéthers et de sulfoxydes très performante, en utilisant les azotures comme source d’azote électrophile. Basée sur la décompositon photochimique d’azotures en présence d’un complexe de fer (III) simple et commercialement disponible, nous avons été en mesure de produire des sulfilimines et des sulfoximines avec d’excellents rendements. Le temps de résidence du procédé d’amination a pu être sensiblement réduit par la conception d’un nouveau type de réacteur photochimique capillaire. Ces améliorations techniques ont permis de rendre la synthèse plus productive, ce qui constitue un élément important d’un point de vue industriel.
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An accurate characterization of the rhodium specimen was obtained via FIM experiments. Reaction behaviors between H2 and CO2 were observed in FEM mode at 700 K. At this temperature, CO desorption occurs, preventing CO+H2 reaction. Surface is mainly recovered by oxygen; reaction with hydrogen occurs. Finally, we can identify the reaction as the Reverse Water Gas Shift.
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Les macrolactones sont des squelettes structuraux importants dans de nombreuses sphères de l’industrie chimique, en particulier dans les marchés pharmaceutiques et cosmétiques. Toutefois, la stratégie traditionnelle pour la préparation de macrolactones demeure incommode en requérant notamment l’ajout (super)stœchiométrique d’agents activateurs. Conséquemment, des quantités stœchiométriques de sous-produits sont générées; ils sont souvent toxiques, dommageables pour l’environnement et nécessitent des méthodes de purification fastidieuses afin de les éliminer. La présente thèse décrit le développement d’une macrolactonisation efficace catalysée au hafnium directement à partir de précurseurs portant un acide carboxylique et un alcool primaire, ne générant que de l’eau comme sous-produit et ne nécessitant pas de techniques d’addition lente et/ou azéotropique. Le protocole a également été adapté à la synthèse directe de macrodiolides à partir de mélanges équimolaires de diols et de diacides carboxyliques et à la synthèse de dimères tête-à-queue de seco acides. Des muscs macrocycliques ainsi que des macrolactones pertinentes à la chimie médicinale ont pu être synthétisés avec l’approche développée. Un protocole pour l’estérification directe catalysée au hafnium entre des acides carboxyliques et des alcools primaires a aussi été développé. Différentes méthodes pour la macrolactonisation catalytique directe entre des alcools secondaires et des acides carboxyliques ont été étudiées. En outre, la stratégie de séparation de phase en macrocyclisation en débit continu a été appliquée lors de la synthèse totale formelle de la macrolactone ivorenolide A. Les étapes-clés de la synthèse incluent une macrocyclisation par le couplage d’alcynes de Glaser-Hay et une réaction de métathèse d’alcènes Z-sélective.