Many zeolites are deployed in various industrial processes owing to their robust catalytic performance and hydrothermal stability. Reactions in zeolites are catalyzed via framework aluminum. The Si/Al ratio is a metric that describes the relative aluminum content in zeolites. However, several researchers noted that the proximity of aluminum in the framework could impact the catalyst output [1–3]. In this work, the influence of paired acid sites is examined in ZSM-22. The 1-dimensional nature of ZSM-22 allows for direct assessment of aluminum proximity without the influence of channel intersection. Theoretical investigations via static density functional theory (DFT) optimization calculations on isolated and paired BAS in ZSM-22 revealed a potential increase in deprotonation potential energy (DPE), indicating a weaker acid with closer aluminum sites. One specific paired model, however, suggested stronger acid behavior, likely due to unfavorable proton-proton interactions influenced by proximity and orientation. Additionally, ammonia adsorption calculations inferred improved adsorption by isolated models, possibly due to unfavorable ammonium-proton interactions in the paired models. Reaction state calculations of ethylene and propylene oligomerization suggested enhanced stabilization of reactant molecules in paired sites. The synthesis of ZSM-22 showed sensitivity to precursor ratios and conditions, but pure samples were successfully achieved through iterative optimization. Catalytic testing of ethylene oligomerization with these samples, classified by their Si/Al ratios and unique fractions of paired acid sites, showed a correlation between higher fractions of paired BAS and increased catalytic activity and selectivity. Samples with higher fractions of paired BAS displayed a higher activity and selectivity for heavier hydrocarbons, explained by the enhanced adsorption capacity of paired BAS for larger reactant molecules, prompting further oligomerization and enhanced catalytic activity. Our findings demonstrate the impact of BAS proximity in dictating the activity and selectivity in ZSM-22 and provide valuable insights for designing more efficient industrial zeolite-based catalysts.

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La distillation fractionnée des coupes pétrolières brutes se révèle insuffisante, pour répondre seule aux besoins en carburants et génère de fortes quantités de distillats à longue chaîne carbonée (C20-C50). Cette coupe d’hydrocarbures peu valorisable est ainsi transformée en molécules hydrocarbonées plus légères, par le biais de deux procédés : le craquage catalytique en lit fluidisé ou l’hydrocraquage. Ce dernier permet le craquage sélectif des hydrocarbures essentiellement en gazole et kérosène. Les catalyseurs acides utilisés sont « bifonctionnels » : une matrice zéolithique USY (zéolithe Y ultra-stabilisée) favorise le craquage des hydrocarbures, pendant qu’un sulfure mixte ou un métal noble greffé catalyse les réactions d’hydrogénation et de déshydrogénation. L’objectif de ce travail de thèse consiste à maximiser la sélectivité en distillats moyens, en diminuant le temps de séjour des molécules d’hydrocarbures dans la structure zéolithique, afin de réduire les réactions de surcraquage. Pour cela, il a été choisi de synthétiser directement des nanocristaux de zéolithe Y sans agent organique structurant, avec un rapport Si/Al le plus élevé possible. Cette propriété leur confère une meilleure stabilité lors des post-traitements, indispensables pour atteindre le rapport Si/Al des zéolithes USY actuellement utilisées. Grâce à l’élaboration d’une nouvelle stratégie de synthèse, des nanocristaux compris entre 20 et 90 nm avec un rapport Si/Al variant de 2,2 à 2,6 ont été obtenus. Puis, l’obtention de la forme protonée de ces nanocristaux (90 nm) a été étudiée et des mesures d’acidité ont également été effectuées. / The fractionated distillation of crude oil is not sufficient to cover all the fuel needs and produces large amounts of long chain carbon distillates (C20-C50). Thus, these hydrocarbons are transformed into lighter hydrocarbon molecules by two processes: fluid catalytic cracking or hydrocracking. The latter allows the selective cracking of hydrocarbons essentially in gas oil and kerosene. The acid catalysts used are “bifunctional”: a zeolite matrix USY (ultra-stabilized zeolite Y) performs the hydrocarbons cracking, at the same time a sulfide or a noble metal catalyzes hydrogenation and dehydrogenation reactions. The aim of this work is to maximize the selectivity to middle distillates by decreasing the residence time of hydrocarbon molecules in the zeolite framework. For this, it was chosen to directly synthesize zeolite Y nanocrystals with the highest possible Si/Al ratio, in a SDA-free medium. This property gives them a better stability during the post-treatments essential to reach the Si/Al ratio of the currently used USY zeolite. Thanks to a new synthesis strategy, nanocrystals between 20 and 90 nm with a Si/Al ratio varying from 2.2 to 2.6 were obtained. Then, the protonated form of these nanocrystals (90 nm) was studied and acidity measurements were also carried out.