Synthetic fuels produced using the Fischer-Tropsch technology will play an important role in the future of the transportation sector. The Fischer-Tropsch synthesis (FTS) allows converting synthesis gas (CO + H2) into fuels of outstanding quality. The synthesis gas can be obtained from different carbon sources: natural gas, coal and biomass. In order to maximize the yield of middle distillates, the process is carried out in two main steps: the FT-synthesis that produces long-chain hydrocarbons (waxes) and a hydrocracking step, to selectively convert the waxes into fuels. Diesel produced by this process is characterized by excellent combustion properties and reduced harmful tailpipe emissions compared to conventional diesel. Due to the growing interest in synthetic fuel production, from the industry and the academia, and to the peculiar characteristics of the Fischer-Tropsch products, research in hydrocracking has received renewed attention. Catalysts for the hydrocracking of long-chain paraffins have been the subject of the present work, which is the summary of four scientific publications. Noble metals supported on acid carriers have been compared, especially for what regards the mechanisms through which hydrocracking proceeds. The catalysts were synthesized and characterized by various techniques, including N2 physisorption, H2 chemisorption, TEM, pyridine adsorption FTIR, ammonia TPD, etc. It was shown that catalytic activity is mainly dependent on the acid support used; that selectivity is strongly dependent on conversion, high conversion favoring highly branched cracking products. Two main reaction routes were observed: bifunctional hydrocracking and hydrogenolytic cracking. Platinum-containing catalysts showed high selectivity towards the latter, while palladium/silica-alumina behaved as pure bifunctional catalysts. Catalyst deactivation was investigated and initial sintering of metal particles was observed. Coking was also a cause of deactivation. Formation of coke deposits was highly dependent on the metal loading of the catalysts. Metal loading also influenced catalyst selectivity, especially in the case of platinum/silica-alumina catalysts. Monofunctional hydrogenolysis on the platinum particles, superimposed to the bifunctional mechanism was observed. This route increased selectivity towards linear hydrocarbons and methane, with increasing amounts of platinum. The specific rate of hydrogenolysis was constant for different loadings of platinum on the same acid silica-alumina support. Using a different, less acid, support negatively affected the hydrogenolytic activity of the platinum catalytic sites. It was concluded that metal-support interactions might play an important role in the catalytic properties of platinum surfaces. This work has contributed to increasing the knowledge about hydrocracking of long-chain alkanes and pointed out some features that might have practical interest in the application of this technology to synthetic-fuel production. / Syntetiska drivmedel tillverkade genom Fischer-Tropsch teknologin kommer i framtiden att ha en betydande roll för transportsektorn. Fischer-Tropsch syntesen (FTS) möjliggör omvandling av syntesgas (CO + H2) till högkvalitativa bränslen. Syntesgasen kan erhållas från olika kolkällor: naturgas, kol och biomassa. För att maximera utbytet av medeldestillat, utförs processen i två huvudsteg: FT-syntes som producerar långa kolväten (vaxer) och ett hydrokrackning steg, för att selektivt omvandla vaxerna till bränslen. Diesel som produceras med denna process kännetecknas av utmärkta förbränningsegenskaper och ger upphov till minskade utsläpp av skadliga ämnen jämfört med vanlig diesel. På grund av det växande intresset för syntetiska bränslen, både från industrin och den akademiska världen, och av de speciella egenskaperna hos Fischer-Tropsch-produkter, har forskningen i vätekrackning fått förnyad uppmärksamhet. Ämnet för detta arbete, som är en sammanfattning av fyra vetenskapliga publikationer, är katalysatorer för hydrokrackning av långkedjiga paraffiner. Ädelmetaller uppburna på sura bärare har jämförts, särskilt vad gäller vätekrackningsmekanismer. Katalysatorerna preparerades och karaktäriserades med hjälp av olika tekniker, bland andra N2 fysisorption, H2 kemisorption, TEM, pyridin adsorption FTIR, ammoniak TPD, etc. Det visade sig att den katalytiska aktiviteten är främst beroende av surheten hos bärarmaterialet, att selektivitet är starkt beroende av omsättningen, där hög omsättning gynnar flergrenade krackningsprodukter. Två huvudsakliga reaktionsvägar observerades: bifunktionell vätekrackning och hydrogenolytisk crackning. Platinakatalysatorer visade hög selektivitet mot det senare, medan katalysatorer med palladium på kiseloxid-aluminiumoxid uppträdde som rena bifunktionella katalysatorer. Katalysatordeaktivering undersöktes och sintring av metallpartiklar observerades. Koksning var också en orsak till deaktivering. Koksbildning var starkt beroende av metallhalten i katalysatorerna. Metallhalten påverkade också selektivitet, särskilt för platina-kiseloxid-aluminiumoxidkatalysatorer. Monofunktionellt hydrogenolys på platinapartiklarna, observerades utöver den bifunktionella mekanismen. Med denna reaktionsväg ökade selektivitet mot linjära kolväten och metan, med ökande platinahalter på katalysator. Den specifika reaktionshastigheten för hydrogenolys var konstant för olika platinahalter på en sur kiseloxid-aluminiumoxidbärare. Den hydrogenolytiska aktiviteten hos platina katalytiska säten påverkas negativt när en mindre sur bärare användes. Slutsatsen var att interaktioner mellan metallen och bäraren kan spela en viktig roll för de katalytiska egenskaperna hos platina ytor. Detta arbete har bidragit till att öka kunskapen om vätekrackning av långkedjiga alkaner och påpekade vissa funktioner som kan ha praktiskt intresse vid tillämpningen av denna teknik för produktionen av syntetiska bränslen. / <p>QC 20131007</p>

Os manguezais sÃo ecossistemas entremarÃs produtivos e biologicamente importantes que ocorrem em regiÃes tropicais e subtropicais do mundo. Ãreas de manguezais nÃo perturbados fornecem habitats para uma variedade de plantas, animais e microrganismos. Estes ecossistemas recebem materiais sedimentares do mar e continente, tornando-se uma Ãrea de transiÃÃo com elevada produtividade. Importantes processos, tais como ciclagem de nutrientes, estÃo diretamente conectados à atividade e diversidade das comunidades microbianas dos solos do manguezal. No entanto, devido a sua localizaÃÃo estratÃgica, manguezais tÃm sido amplamente impactados por todo o mundo. A compreensÃo da estrutura e das funÃÃes das comunidades microbianas e suas adaptaÃÃes Ãs alteraÃÃes ambientais resultantes de xenobiÃticos, alteraÃÃes climÃticas e a prÃtica industrial, tais como a exploraÃÃo petrolÃfera, à essencial para manter ou restabelecer funÃÃes desejÃveis do ecossistema. Dessa forma, o presente estudo investigou a estrutura de comunidades bacterianas de amostras de solos do manguezal da Barra Grande, Icapuà (37 20âW, 4 40âS), por mÃtodo independente de cultivo usando Polimorfismo do Tamanho de Fragmentos de RestriÃÃo Terminal (T-RFLP) e tambÃm avaliou o mÃtodo dependente de cultivo (enriquecimento) para isolar cepas de bactÃrias com potencial para degradar petrÃleo e n-Hexadecano. Um total de trÃs pontos foi amostrado ao longo do manguezal, com 150 metros de distÃncia entre cada um deles. Temperatura, pH, salinidade, matÃria orgÃnica e granulometria dos solos foram medidas. AnÃlises de T-RFLP foram feitas apÃs a digestÃo de DNA genÃmico com as enzimas HhaI e MspI e o nÃmero e diversidade de Unidades TaxonÃmicas Operacionais (OTU) de cada amostra foi analisado pelo programa T-Align (Applied Biosystems). A cepa selecionada para testes de diferentes concentraÃÃes de n-Hexadecano foi identificada pelo seqÃenciamento do gene do rRNA 16S. Esta cepa foi tambÃm avaliada em relaÃÃo à susceptibilidade a radiaÃÃo UV e antibiÃticos. Os resultados mostraram que as comunidades bacterianas de solos do manguezal sÃo semelhantes em nÃmero de OTUs, mas diferem em composiÃÃo. Provavelmente a peculiaridade das variÃveis fÃsico-quÃmicas e granulometria do solo sÃo responsÃveis pelas diferenÃas na composiÃÃo e estrutura das comunidades bacterianas. Dezoito cepas de bactÃrias foram isoladas de culturas de enriquecimento com petrÃleo e quatro cepas mostraram potencial particular para degradar n-Hexadecano. Uma cepa identificada como Acinetobacter sp. IC18 foi caracterizada como uma boa degradadora de hidrocarboneto, pois foi capaz de degradar 1% do n-Hexadecano em 48 horas. Esta cepa tambÃm utilizou cerca de 30% de uma concentraÃÃo total de 20% (v/v) de n-Hexadecano durante o mesmo perÃodo de incubaÃÃo. AlÃm disso, IC18 foi susceptÃvel a vÃrios antibiÃticos e resistente à radiaÃÃo UV. Em conclusÃo, a estrutura da comunidade bacteriana de solos do manguezal da Barra Grande parece nÃo ser afetada pela presenÃa da exploraÃÃo petrolÃfera em IcapuÃ. AlÃm disso, os solos deste manguezal sÃo colonizados por vÃrias cepas com potencial para degradar hidrocarbonetos, que à particularmente interessante em virtude do risco de derramamentos de petrÃleo.

La méthode à privilégier pour améliorer dans les zéolithes la diffusion des réactifs, des intermédiaires réactionnels et des produits est de raccourcir la longueur du chemin diffusionnel, c'est-à-dire de diminuer la taille des cristaux. La croissance des cristallites est fonction de la composition du gel de synthèse, du temps de cristallisation, de la température, etc. La maîtrise de cette croissance permet d'obtenir un large éventail de taille pouvant aller de plusieurs micromètres à seulement quelques dizaines de nanomètres. Dorénavant, il est possible de limiter le chemin diffusionnel à seulement 3 mailles élémentaires en inhibant lors de la synthèse hydrothermale la croissance des cristaux dans une direction privilégiée. Pour cela l'utilisation d'agent structurant organique très particulier de type géminé s'avère indispensable et donne dans le cas de la zéolithe de type *BEA un matériau hiérarchisé avec des cristaux zéolithiques de 4 nm d'épaisseur séparés par des mésopores structurés et réguliers. La morphologie de ce matériau ressemble à une éponge de mer.<br>Deux réactions modèles, hydroisomérisation du n-héxadécane et transformation de l'éthanol en hydrocarbures, démontrent que la diffusion des réactifs et des produits sont optimisées dans les nanoéponges de bêta. La stabilité et la sélectivité du catalyseur se trouvent alors améliorées au détriment, étonnamment, de l'activité. Cela vient du fait que l'extrême diminution de l'épaisseur des cristallites conduit à une augmentation du nombre d'aluminium en bouche de pores qui sont, bien que très accessibles, incapables de catalyser les réactions d'isomérisation et de craquage. Les aluminium proche de la surface externe, contrairement à ceux situés au cœur du cristal ne bénéficient pas des effets longues distances ce qui les rend moins forts. / The method to ameliorate the diffusion of reactants, reaction intermediates, and products inside the zeolite is by shortening the diffusion path length, i.e., crystals size. The growth of the crystals is a function of gel composition synthesis, crystallization time, temperature, etc. The mastering of this growth allows to obtain a wide range of the size which ranges from several micrometers to a few tens of nanometers. It is possible now to limit the diffusion path to only three unit cells by inhibiting the crystals' growth in one direction during the hydrothermal synthesis. For that, the use of a peculiar organic surfactant geminate is indispensable, it gives a hierarchical material with zeolitic crystals of 4 nm thickness separated by structured and regular mesopores in the case of *BEA type zeolite. The morphology of this material resembles a sea sponge.<br>Two reaction models, n-hexadecane hydroisomerization and ethanol transformation to hydrocarbons, demonstrate that the reactants and the products diffusion was optimized in the beta nanosponges. Surprisingly the catalyst stability and selectivity were improved instead of activity. In fact this is due to the extreme reducing of the zeolite crystals’ thickness that leads to increase the aluminum number in the pore mouth, which although very accessible, but incapable to catalyze the isomerization and cracking reactions. The aluminums near the external surface, in contrary to those in the crystal heart, do not benefit from the long distance effects, which makes them weaker.

En raison de la complexité de leur composition, l’étude de l’oxydation des gazoles et des carburants biodiesel nécessite de choisir des molécules modèles représentant ces mélanges. Dans ce contexte nous avons sélectionné deux molécules pouvant représenter les gazoles : le n-décane, souvent considéré comme molécule modèle des paraffines contenues dans les gazoles, et le n-hexadécane, molécule de référence pour l’estimation de l’indice cétane, ainsi que deux molécules représentant les carburants biodiesel : le palmitate de méthyle (C17H34O2, ester méthylique saturé) et l’oléate de méthyle (C19H36O2, ester méthylique insaturé). L’étude de l’oxydation de ces molécules a été menée en réacteur auto-agité par jets gazeux, à une richesse de 1, des températures comprises entre 550 et 1100 K, à pression atmosphérique et à un temps de passage constant de 1,5 s. La formation d’un nombre important d’espèces a été observée parmi lesquelles figurent des oléfines, des diènes, des esters méthyliques insaturés, des éthers cycliques avec différentes tailles de cycle, des cétones et des aldéhydes. Grâce à deux nouvelles versions du logiciel EXGAS, des mécanismes cinétiques détaillés de l’oxydation des molécules étudiées ont été générés et validés par comparaison avec les résultats expérimentaux. Enfin, une comparaison de la réactivité du n-décane, du n-hexadécane, du palmitate de méthyle et de l’oléate de méthyle et des quantités de produits formées (dont certains polluants) a été effectuée / Because of the complexity of their compositions, the study of the oxidation of diesel and biodiesel fuels requires choosing model molecules (surrogates) representing the real mixtures. In this context, we have selected two molecules to represent the diesel fuel: n-decane, usually considered as model molecule of paraffin contained in diesel fuel, and n-hexadecane, molecule of reference for the estimation of the cetane number, and two molecules representing biodiesel fuel: methyl palmitate (C17H34O2, a saturated methyl ester) and methyl oleate (C19H36O2, an unsaturated methyl ester). The study of oxidation of these molecules has been conducted in a jet-stirred reactor, with an equivalence ratio of 1, temperatures between 550 and 1100 K, at atmospheric pressure and for a constant residence time of 1.5 sec. The formation of a large number of species has been observed which includes olefins, dienes, unsaturated methyl esters, cyclic ethers with different size of ring, ketones and aldehydes. Using two new versions of EXGAS software, detailed kinetic mechanisms for the oxidation of the studied molecules were generated and validated by comparaison with experiemental results. Finally, a comparison of the reactivity of n-decane, n-hexadecane, methyl palmitate and methyl oleate and amounts of formed products (including some pollutants) has been performed