4 research outputs found

    Hétérogénéisation de catalyseurs moléculaires à base de nickel au sein de matériaux poreux pour l'oligomérisation de l'éthylÚne

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    Ethylene α-oligomers are used in copolymerization with ethylene to modulate the properties of polyethylene. With an increased availability of shale gas, and therefore of ethylene, it has become highly economically viable to produce selectively α-oligomers from this gas. However, despite a spread use of various catalysts in industry, based on Ti, Fe, Ni, etc. with different ligands, homogeneous catalysis could present certain limitations such as the presence of metal particles or a lack of catalyst stability. Therefore, not only heterogeneous catalysts enable to separate products from the catalyst more easily, it also allows to control the shape of the catalyst, while obtaining isolated active sites preventing them from interaction between them leading to deactivation. Macroligands enable to bridge the gap between homogeneous catalysis and heterogeneous catalysis by preserving catalytic activities and selectivities obtained in homogeneous catalysis, while obtaining isolated active sites. During this thesis work, two types of macroligands were synthesized and characterized, Metal-Organic Frameworks (MOFs) and Porous Organic Polymers (POPs), with bipyridyl coordination sites: the MOF UiO-67-bpy and the POPs Bpy-MP-1, Bpy-MP-2 and Bpy-MP-3. The bipyridyl sites within their structure were coordinated with nickel(II) chloride complexes in order to obtain isolated active sites. Given the fact that ill-defined active sites could be obtained with UiO-67-bpy-based catalysts, a series of catalyst have been synthesized with Bpy-MP-1 and Bpy-MP-2 macroligands. These series were characterized and it can be assessed, for the Bpy-MP-1-based catalysts, that the bipyridyl sites within the structure are coordinated with nickel(II) chloride complexes. However, traces of Pd originating from their C-C coupling Pd-catalyzed synthesis pathway were found within their structure, which can cause side reactions and deactivation of catalyst by interaction between Pd and Ni active sites. Therefore a new POP obtained by radical polymerization, Bpy-MP-3, enabled to prepare a series of catalyst with different loadings of nickel. These series were fully characterized and it can be also assessed that the bipyridyl sites within their structure are coordinated with nickel(II) chloride complexes. These four series of catalysts were tested for ethylene oligomerization and for given conditions, the catalyst series obtained with Bpy-MP-3 enabled to obtain TOFs (above 10 000 mmololigomers.mmolnickel-1.h-1) than its homogeneous counterpart Ni(bpy)Cl2 and its heterogeneous counterparts UiO-67-bpy, Bpy-MP-1 et Bpy-MP-2. However, despite being highly active for ethylene oligomerization and selective in butene, Bpy-MP-3-based catalysts are also highly active for ethylene polymerization, decreasing the global selectivity in oligomers and causing the deactivation of the catalyst. Different possible causes were elucidated concerning the origin of the uncontrolled polymerization reaction during this thesis work. It was also proved that the same type of active sites within the catalyst was capable of both oligomerizing and polymerizing ethylene at the same time. However, a result proved in homogeneous catalysis was successfully adapted in heterogeneous catalysis: the addition of PPh3 during the reaction enabled to stop ethylene polymerization and promote ethylene oligomerization. Based on that result, a MOF-808-DPPB and a Phos-MP-3 POP, both phosphine-based and not bipyridyl-based anymore, were synthesized and characterized to evaluate the ability of the macroligands to oligomerize ethylene and not polymerize it. This present work enables to present promising perspectives for the selective ethylene oligomerization with UiO-67-bpy and MOF-808-DPPB MOFs and with Bpy-MP-1, Bpy-MP-2, Bpy-MP-3 et Phos-MP-3 POPs. Their structure versatility offer large perspectives regarding the modulation of their activity and their selectivity towards ethylene oligomerization.Les α-oligomĂšres de l’éthylĂšne sont utilisĂ©s en copolymĂ©risation avec l’éthylĂšne afin de moduler les propriĂ©tĂ©s du polyĂ©thylĂšne. Avec une disponibilitĂ© accrue en gaz de schiste, il est intĂ©ressant de produire sĂ©lectivement des α-olĂ©fines Ă  partir de l'Ă©thylĂšne. MalgrĂ© une utilisation rĂ©pandue en industrie, la catalyse homogĂšne de cette rĂ©action peut prĂ©senter certaines limites comme la prĂ©sence de rĂ©sidus mĂ©talliques ou un manque de stabilitĂ© des catalyseurs. Ainsi, la catalyse hĂ©tĂ©rogĂšne prĂ©sente cette facilitĂ© de sĂ©paration du catalyseur et du milieu rĂ©actionnel mais permet aussi de contrĂŽler la forme des catalyseurs, tout en obtenant des sites actifs ben dĂ©finis Ă©vitant la dĂ©sactivation du catalyseur par interaction des sites actifs entre eux. Les macroligands permettent d’établir une passerelle entre catalyse homogĂšne et hĂ©tĂ©rogĂšne afin de conserver les activitĂ©s catalytiques et les sĂ©lectivitĂ©s obtenues en homogĂšne tout en obtenant des sites actifs isolĂ©s. Durant ce travail de thĂšse, deux types de macroligands, les Metal-Organic Frameworks (MOFs) et les PolymĂšres Organiques Poreux (POPs) prĂ©sentant des sites de coordination bipyridyl ont Ă©tĂ© synthĂ©tisĂ©s et caractĂ©risĂ©s : le MOF UiO-67-bpy et les POPs Bpy-MP-1, Bpy-MP-2 et Bpy-MP-3. Les sites bipyridyl au sein de leur structure ont Ă©tĂ© coordinnĂ©s avec diffĂ©rents taux de chlorure de nickel(II) afin d’obtenir des sites actifs isolĂ©s. Des sites actifs non-contrĂŽlĂ©s sont obtenus avec le MOF UiO-67-bpy et une sĂ©rie de catalyseurs a Ă©tĂ© synthĂ©tisĂ©e Ă  partir de Bpy-MP-1 et Bpy-MP-2. Ces sĂ©ries ont Ă©tĂ© caractĂ©risĂ©es et pour les catalyseurs obtenus Ă  partir de Bpy-MP-1, il a Ă©tĂ© montrĂ© que les sites bipyridyls au sein de la structure sont coordinnĂ©s par des complexes de chlorure de nickel(II). Cependant, les traces de Pd retrouvĂ©es dans les matĂ©riaux Bpy-MP-1 et Bpy-MP-2, liĂ© Ă  leur mĂ©thode de synthĂšse catalysĂ©e au Pd peut entraĂźner des rĂ©actions secondaires, des interactions entre sites actifs de Pd et de Ni et causer la dĂ©sactivation du catalyseur. Ainsi, un nouveau POP a Ă©tĂ© synthĂ©tisĂ© par polymĂ©risation radicalaire, le Bpy-MP-3. Une sĂ©rie de catalyseurs infiltrĂ©es avec diffĂ©rents taux de nickel a Ă©tĂ© synthĂ©tisĂ©e Ă  partir de ce matĂ©riau et caractĂ©risĂ©e. Comme pour les catalyseurs obtenus Ă  partir de Bpy-MP-1, les sites bipyridyls du Bpy-MP-3 sont coordinnĂ©s par des complexes de chlorure de nickel(II). Ces quatre sĂ©ries de catalyseurs ont Ă©tĂ© testĂ©es en oligomĂ©risation de l’éthylĂšne et pour des conditions donnĂ©es, la sĂ©rie obtenue avec le Bpy-MP-3 prĂ©sente une activitĂ© plus importante (supĂ©rieure Ă  10 000 mmololigomĂšres.mmolnickel-1.h-1) que son homologue homogĂšne Ni(bpy)Cl2 et ses homologues hĂ©tĂ©rogĂšnes UiO-67-bpy, Bpy-MP-1 et Bpy-MP-2. Cependant, les catalyseurs Ă  base de Bpy-MP-3 sont Ă©galement trĂšs actifs en polymĂ©risation de l’éthylĂšne, entraĂźnant des limites diffusionnelles au sein des catalyseurs durant la rĂ©action et rĂ©duisant la sĂ©lectivitĂ© globale en oligomĂšres. DiffĂ©rentes voies d’investigation ont Ă©tĂ© Ă©lucidĂ©es durant ce travail de thĂšse sur l’origine possible de cette polymĂ©risation non-contrĂŽlĂ©e. Il a Ă©tĂ© prouvĂ© qu’un mĂȘme site actif au sein des catalyseurs Ă  base de Bpy-MP-3 Ă©tait responsable d’oligomĂ©riser et de polymĂ©riser l’éthylĂšne. Plus tard, il a Ă©tĂ© prouvĂ© qu’en ajoutant des Ă©quivalents de PPh3 durant la rĂ©action, cette polymĂ©risation peut ĂȘtre stoppĂ©e et l’oligomĂ©risation favorisĂ©e. À partir de ce dernier rĂ©sultat, le MOF-808-DPPB et un POP, le Phos-MP-3, tous deux avec des sites de phosphine, ont synthĂ©tisĂ©s et caractĂ©risĂ©s afin d’évaluer la capacitĂ© de ces macroligands Ă  oligomĂ©riser sĂ©lectivement l’éthylĂšne. Ces travaux permettent de montrer que les matĂ©riaux poreux infiltrĂ©s au nickel, tels que les MOFs UiO-67-bpy et MOF-808-DPPB et les POPs Bpy-MP-1, Bpy-MP-2, Bpy-MP-3 et Phos-MP-3 sont des matĂ©riaux prometteurs pour l’oligomĂ©risation de l’éthylĂšne et offrent de larges perspectives de travail pour moduler leur activitĂ© et leur sĂ©lectivitĂ©

    Molecular Rhodium Complex within N‐Rich Porous Polymer Macroligand as Heterogeneous Catalyst for the Visible‐Light Driven CO2 Photoreduction

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    The heterogenization of molecular catalysts within a porous solid acting as macroligand can advantageously open access to enhanced stability and productivity, and thus to more sustainable catalytic process. Herein, a porous organic polymer (POP) made through metal‐free polymerization using bipyridine repeating units is reported. This N‐rich POP is an efficient macroligand for the heterogenization of molecular rhodium complexes. The intrinsic catalytic activity of the heterogenized catalyst is slightly higher than that of its homogeneous molecular counterpart for formic acid production as a unique carbon‐containing product. The heterogenization of the rhodium catalysts enables recycling for a total productivity of up to 8.3 g of formic acid per gram of catalyst after 7 reuses using visible light as the sole energy source

    Rhodium-based metal–organic polyhedra assemblies for selective CO2 photoreduction

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    Heterogenization of molecular catalysts via their immobilization within extended structures often results in a lowering of their catalytic properties due to a change in their coordination sphere. Metal–organic polyhedra (MOP) are an emerging class of well-defined hybrid compounds with a high number of accessible metal sites organized around an inner cavity, making them appealing candidates for catalytic applications. Here, we demonstrate a design strategy that enhances the catalytic properties of dirhodium paddlewheels heterogenized within MOP (Rh-MOP) and their three-dimensional assembled supramolecular structures, which proved to be very efficient catalysts for the selective photochemical reduction of carbon dioxide to formic acid. Surprisingly, the catalytic activity per Rh atom is higher in the supramolecular structures than in its molecular sub-unit Rh-MOP or in the Rh-metal–organic framework (Rh-MOF) and yields turnover frequencies of up to 60 h–1 and production rates of approx. 76 mmole formic acid per gram of the catalyst per hour, unprecedented in heterogeneous photocatalysis. The enhanced catalytic activity is investigated by X-ray photoelectron spectroscopy and electrochemical characterization, showing that self-assembly into supramolecular polymers increases the electron density on the active site, making the overall reaction thermodynamically more favorable. The catalyst can be recycled without loss of activity and with no change of its molecular structure as shown by pair distribution function analysis. These results demonstrate the high potential of MOP as catalysts for the photoreduction of CO2 and open a new perspective for the electronic design of discrete molecular architectures with accessible metal sites for the production of solar fuels

    Heterogenization of a Molecular Ni Catalyst within a Porous Macroligand for the Direct C-H Arylation of Heteroarenes

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    International audienceDirect C–H functionalization catalyzed by a robust and recyclable heterogeneous catalyst is highly desirable for sustainable fine chemical synthesis. Bipyridine units covalently incorporated into the backbone of a porous organic polymer were used as a porous macroligand for the heterogenization of a molecular nickel catalyst. A controlled nickel loading within the porous macroligand is achieved, and the nickel coordination to the bipyridine (bpy) sites is assessed at the molecular level using IR and solid-state NMR spectroscopy. The heterogenized Ni-bpy catalyst was successfully applied to the direct and fully selective C2 arylation of benzothiophenes, thiophene, and selenophene, as well as for the arylation of free NH-indole. Recyclability of the catalyst was achieved by employing hydride activators to reach a cumulative turnover number of more than 300 after seven cycles of catalysis, which corresponds to a total productivity of 12 g of 2-phenylbenzothiophene, chosen as model target biaryl, per gram of catalyst
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