At present, more than 80% of the world’s energy consumption and production of chemicals is originated from the use of fossil resources. There is a tremendous growing interest in utilising biomass molecules for energy provision due to their carbon neutrality. Lower alcohols such as methanol and ethanol if produced from biomass as transportation fuels as well as platform chemicals, can become strategically important for many energy/chemically starved countries. Currently, they are synthesised by indirect and inefficient processes. We show for the first time in this thesis study that ethylene glycol, the simplest representative of biomass-derived polyols, can be directly converted to these two lower alcohols by selective hydrogenolysis over modified Raney Ni and Cu catalysts in hydrogen atmosphere. This work provides essential information that may lead to the development of new catalysts for carbohydrate activation to methanol, a novel but important reaction concerning the important biomass conversion to transportable form of energy. Modification of electronic structure and the adsorption properties of Raney catalysts have therefore been achieved by blending with second metal(s). It is found that the activity and selectivity of this reaction can be significantly affected by this approach. In contrast, there is no subtle effect on methanol selectivity despite a great variation in the d-band centre positions of metal catalysts which show a distinctive effect on other products. Our result suggests that methanol is produced on specific surface sites independent from the other sites at an intrinsic rate and will not be converted to other products by the d-band alteration. On the other hand, it is reported in this thesis that a dramatic improvement in the combined selectivity to methanol/ethanol reaching 80% can be obtained over a Pd/Fe₃O₄ catalyst under relatively milder conditions (20 bar and 195 oC). This direct production of the non-enzymatic bio-alcohols is established over a carefully prepared co-precipitated Pd/Fe₃O₄ catalyst which gives a metallic phase of unexpectedly high dispersion ranging from small clusters to individual metal adatoms on defective iron oxide to give the required metal-support interaction for the novel synthesis. It is demonstrated that the small PdFe clusters on iron oxide surface provide the active species responsible for methanol production. In addition, a related Rh/Fe₃O₄ catalyst synthesised by co-precipitation is also shown to be selective for CO₂ and H₂ production from a direct methane-oxygen oxidation reaction. As a result, 2.7% conversion of methane with selectivity ratio of CO₂/H₂ = 4 in a mixed gas feed stream of CH₂/O₂ = 30 at 300 ^oC is obtained. The reaction is operated in a kinetically controlled regime at 300^oC, where the CO formation from reverse water gas shift reaction is greatly suppressed. It is evident that the Rh/Fe₃O₄ acts as an interesting bifunctional catalyst for this reaction. This catalyst firstly gives a high dispersion of Rh which is expected to deliver a higher surface energy with enhanced activity. The Rh metal surface provides catalytically active sites for dissociation of methane to adsorbed hydrogen and carbon atoms effectively, and active oxygen on metal surface readily catalyses the carbon atoms to CO. Following these elementary reactions, the surface oxygen from Fe₃O₄ subsequently converts it to CO₂ selectively at the metal-support interface. As a result, the novel study of catalytic biomass conversion and the discoveries of new catalysts are reported in this thesis.

In Hinblick auf den stetig steigenden Bedarf der chemischen Industrie an Grundstoffchemikalien und der teilweise unsicheren Versorgung mit Erdöl und Erdgas ist es notwendig alternative Rohstoffe und Verwertungspfade für die Bereitstellung von Basischemikalien zu finden. Ziel der vorliegenden Arbeit war die Untersuchung der Hydrogenolyse von Lignin in niedermolekulare Produkte unter Verwendung geeigneter Salzschmelzen. Es konnte gezeigt werden, dass Lignin in Zinkchlorid/Kaliumchloridschmelzen in niedermolekulare Produkte abgebaut werden kann. Hierbei erwiesen sich der Einsatz eines entsprechenden Eutektikums und einer Alternativschmelze mit niedrigem Schmelzpunkt als hilfreich. Durch den Einsatz verschiedener Apparaturen wurden Untersuchungen in statischer und dynamischer Atmosphäre durchgeführt. Es ergaben sich während der Untersuchung Abhängigkeiten der Hydrogenolyse von verschiedenen Reaktionsparametern. Optima der Umsetzung hinsichtlich der Reaktionsparameter Temperatur, Zeit und Ligninanteil in der Schmelze wurden herausgearbeitet. Die Ausbeute an gewünschten Flüssigprodukten wurde, im Untersuchungsbereich, an diesen Punkten maximiert. Gleichzeitig war die Rückstands- und Gasbildung eingeschränkt. Es konnten Erkenntnisse eines komplexen Systems der Abhängigkeiten der Ausbeuten an Reaktionsprodukten von den Parametern der Untersuchung gewonnen werden. Die Hydrogenolyse von Lignin führte zur Aromatisierung fester Residuen sowie zur Abreicherung von Sauerstofffunktionalitäten. Komplexe Reaktionsmechanismen bewirkten den Abbau von Methoxyl-, Carboxyl- und Hydroxylgruppen der Ligninstruktur. Carbeniumionmechanismen konnten als wichtige Reaktionen zur Spaltung von Ether Arylbindungen identifiziert werden. Die Freisetzung von Monomeren und die Polymerisation anderer Intermediäre sind durch Sekundärreaktionen denkbar. Die gebildeten Flüssigprodukte bestanden hauptsächlich aus Monoaromaten (v.a. Guajakole und Kresole) und wenigen Polyaromaten. Die Selektivität der Bildung einzelner Verbindungen war gering, d.h. die Flüssigprodukte sind eine heterogene Mischung mit geringen Konzentrationen der Einzelsubstanzen. Die Unterschiede in der Struktur der Ausgangslignine bildeten sich auch in der Zusammensetzung der Flüssigprodukte ab. / In view of the steadily increasing demand of the chemical industry to base chemicals and the partial uncertain supply of crude oil and gas, it is necessary to find alternative raw materials and conversion routes for the provision of basic chemicals. The aim of the present work was to investigate the hydrogenolysis of lignin in low molecular weight products using appropriate molten salt media. It could be demonstrated that lignin can be convert in low molecular weight products using zinc chloride/potassium chloride molten salt media. The use of an appropriate eutectic melt and of an alternative melt with low melting point proved helpful. By the use of different apparatus investigations in static and dynamic atmosphere could be carried out. During the investigation dependencies of the hydrogenolysis of various reaction parameters are submitted. Optima of the hydrogenolysis regarding to reaction temperature, time and lignin content at the melt could be identified. The yields were maximized at these points in the range of investigation. Concurrently formation of gases and residues were suppressed. Some evidence of a complex system of the dependencies of the yields of reaction products are obtained from the parameters of the investigation. Hydrogenolysis of lignin leads to aromatic solid residues and to a loss of oxygen containing structures. Structures containing methoxyl-, carboxyl- and hydroxyl groups are degraded by various complex reaction mechanisms. Mechanisms of the formation of carbonium ions were identified as important reactions of the cleavage of ether aryl bonds. Secondary reactions caused the liberation of monomers and polymerisation of some intermediaries. The resulting liquid products consist mainly of monoaromatics (guaiacols and cresols) and less of polyaromatics. The selectivity of the formation of single compounds was low, i.e. the liquid products constitute a heterogenous mixture with low concentrations of the single compounds. The structural differencies of the feedstock lignins also showed at the composition of the liquid products.

The first part of the thesis presents a study based on the forest biorefinery concept, which involves converting a pulp mill into a multi-purpose biofuels, biomaterials, and biopower production facility in which these products are produced in an environmentally compatible and sustainable manner. A key challenge in this process is the recovery of lignin from process streams such that it can be utilized in a variety of innovative green chemistry processes The first study examines the fundamental chemical structure of LignoBoost derived lignin recovered from Kraft pulping streams using an acid precipitation/washing methodology. Functional group analysis and molecular weight profiles were determined by nuclear magnetic resonance (NMR) and size exclusion chromatography. These findings gave valuable insight into the physical properties and the determining chemical properties of this currently underutilized, renewable bioresource. The second study is based on the future second generation bioethanol production process, where ethanol produced from lignocellulosic materials will bring about the co-production of significant amounts of under-utilized lignin. The study examines the potential of conventional heterogeneous and novel homogeneous catalysts for the selective cleavage of the aryl-O-aryl and aryl-O-aliphatic linkages of ethanol organosolv lignin to convert it from a low grade fuel to potential fuel precursors or other value added chemicals. The experimental data demonstrated that aryl-O-aryl and aryl-O-aliphatic linkages could be cleaved and the hydrogenated lignin had a decrease in oxygen functionality and the formation of products with lower oxygen content. The second part of this thesis reports the development and optimization of a novel qualitative method for the determination of the various types of hydroxyl groups present in biodiesel production streams. In the first study, the use of 2-chloro-4,4,5,5-tetramethyl-1,3,2-dioxaphospholane as a phosphitylation reagent for quantitative ³¹P-NMR analysis of the hydroxyl groups in biodiesel process samples has been developed. Subsequently a characteristic chemical shifts library is developed with model compounds to provide quantitative data on the concentration of biodiesel precursors, intermediates and final product. The last part of this thesis depicts the results of an industrial trial based on the novel biodiesel analytical method developed earlier.

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>

The work described in this thesis focuses on the cleavage of the β-O-4′ bond, which is the most abundant interunit linkage in the lignin polymer. In the first part, three methods based on palladium catalysis have been developed and their applicability has been verified using lignin model compounds. A transfer hydrogenolysis of the β-O-4′ bond using formic acid as a mild hydrogen donor together with a base. An aerobic oxidation of the benzylic alcohol motif in the β-O-4′ linkage to generate a key intermediate in the cleavage reaction was performed. A redox neutral cleavage of the β-O-4′ bond was accomplished in which no stoichiometric reducing or oxidizing agents were added. In the second part of the thesis, a mechanistic study is presented. The corresponding ketone from a dehydrogenation reaction of the benzylic alcohol motif was identified to be the key intermediate. This ketone and its enol tautomer was found to be responsible for the β-O-4′ bond cleavage reaction under the employed reaction conditions. In the final part of this thesis, the methodologies have been applied to native lignin. The depolymerization reaction was combined with organosolv pulping. This approach was successful, and together with cellulose and hemicellulose, propenyl aryls were generated in excellent yields directly from wood. In this transformation, the lignin derived molecules have been reduced by an endogenous hydrogen donor from the wood.

Orientador: : Carlos Roque Duarte Correia / Tese (doutorado) - Universidade Estadual de Campinas, Instituto de Química / Made available in DSpace on 2018-08-24T05:38:03Z (GMT). No. of bitstreams: 1 Martinez_PabloDavidGrigol_D.pdf: 10635816 bytes, checksum: b6d50b746463694bb1ef50352d36d1e3 (MD5) Previous issue date: 2013 / Resumo: O emprego de enecarbamatos endocíclicos como substratos na organocatálise foi avaliado na primeira parte deste trabalho. Explorou-se a ação catalítica de ácidos fosfóricos na reação de Friedel-Crafts envolvendo enecarbamatos di e trissubstiuídos como eletrófilos. Foram empregados indóis, furanos, naftol e sesamol como nucleófílos neste tipo de reação. Foi possível desenvolver um protocolo operacional simples e em condições brandas capaz de fornecer bons rendimentos. A diastereosseletividade observada com enecarbamatos trissubstituídos favoreceu o produto trans numa faixa de 2,7:1 até 95:5. Usando ácidos fosfóricos quirais, a enantiosseletividade também foi verificada, atingindo-se excesso enantiomérico de 20% até o momento, fato que demonstra a potencialidade da metodologia. Posteriormente, realizou-se um estudo sobre a preparação de aminoálcoois a pela hidrogenólise de 2-aril-3-epoxipirrolidinas. Esses substratos foram obtidos pela arilação de Heck-Matsuda em enecarbamatos derivados do ácido L-piroglutâmico como etapa chave. Observou-se que a estereoquímica dos substituintes da pirrolidina apresentou decisiva influência para as condições reacionais e rendimento da hidrogenólise, permitindo em alguns casos a clivagem de até duas ligações numa única reação. Os aminoálcoois obtidos a partir desta metodologia foram utilizados na síntese concisa da 2-epi-bulgecinina bem como de bases esfingóides exemplificada na síntese de análogo da esfingosina / Abstract: In the first part of this work, the use of endocyclic enecarbamates as substrates in organocatalysis was evaluated. The effect of phosphoric acids as catalysts in promoting Friedel-Crafts reactions involving di and trisubstituted enecarbamates as electrophiles was explored. Different arenes were employed as nucleophiles like indols, furans, naftol and sesamol. It was possible to develop a simple protocol with mild conditions and good yields. The diastereoselectivity observed with trisubstituted enecarbamates favored the trans product in a range of 2.7:1 to 95:5. By using chiral phosphoric acids, the enantioselectivity achieved, so far, was 20% ee, evidencing the potentiality of this methodology. Later, hydrogenolysis reactions over 2-aryl-3-epoxypyrrolidines were performed to prepare aminoalcohols. The key step to synthesize the former pyrrolidines was the Heck-Matsuda reaction of enecarbamates obtained from L-pyroglutamic acid. The stereochemistry of the substituents in the hydrogenolytic step did influence the experimental conditions and yields, allowing in some cases two bonds cleavage in one pot. The aminoalcohols prepared in this methodology were used in a short synthesis of 2-epibulgecinine and in preparation of sphingoid bases exemplified in the synthesis of sphingosine analogue / Doutorado / Quimica Organica / Doutor em Ciências

No description available.

Surface Organometallic Chemistry (SOMC) is an excellent approach to erase the gap between homogeneous and heterogeneous catalysis by grafting the molecular organometallic complex on various oxide surfaces, forming well-defined and single-site catalysts. This strategy allows for better characterization as well as the improvement and development of existing and new catalysts. These surface species could promote a wide range of catalytic applications (i.e., metathesis of hydrocarbons, hydrogenolysis of alkanes, and olefin polymerization reactions) depending on the metal center and its coordination sphere. In particular, the grafting of alkylated organometallic complexes of groups 4, 5, and 6 metals on the surface oxide is a thermodynamically favored reaction generally leading to strongly bonded well-defined surface species, which are highly reactive catalysts. This thesis has focused on the preparation, characterization, and catalytic investigation of different supported complexes that contain methyl, alkyl, and alkylidyne ligands. The first part compares the catalytic activity of [(≡Si−O−)W(-CH3)5] and [(≡Si-O-)Mo(≡CtBu)(-CH2tBu)2] surface species experimentally and by DFT calculations in the metathesis reactions of linear classical and functionalized olefins. Both pre-catalysts perform almost equally in the α-olefin metathesis reaction. However, in the functionalized olefin metathesis reaction, W pre-catalyst provides selective metathesis products and performs much better than Mo that gives a range of isomerization products. The second part deals with the synthesis and characterization of [(THF)2Zr(-CH3)4] and its grafting on silica support for the first time. The generated surface species [(≡Si−O−)Zr(CH3)3(THF)2] and [(≡Si−O−)2Zr(CH3)2(THF)2] are used for the conversion of CO2 and propylene oxide to cyclic propylene carbonates achieving a TON of 4227. The third part describes the first synthesis and characterization of the highly unstable homoleptic [Ti(-CH3)4] without any coordinating solvent. This complex was stabilized by grafting on SiO2-700, yielding two fully characterized surface species [(≡Si-O-)TiMe3] and [(≡Si-O-Si≡)(≡Si-O-)TiMe3], which were used in the hydrogenolysis reaction of propane and n-butane, with TONs of 419 and 578, respectively. Finally, the fourth part reports the immobilization and characterization of [TiMe2Cl2], an intermediate in the synthesis of [Ti(-CH3)4], on SiO2-700 resulting in [(≡Si-O-)TiMeCl2] and [(≡Si-O-)TiMe2Cl] surface species. These complexes reacted with a demethylating Lewis acid agent (BARF), forming the corresponding cationic Ti species [(≡Si-O-)TiMeCl]+ and [(≡Si-O-)TiCl2]+. Both neutral and cationic complexes were tested in the ethylene polymerization reaction affording linear HDPE with high molecular weights of 500,367 and 486,612 g/mol.

In many catalytic systems, the activity and selectivity of supported metal catalysts or extended metal surface catalysts would be affected by the metal surface structure, and this phenomenon is called structure sensitivity. Generally, structure sensitivity is led by the change of geometric and electronic properties of the metal on the surface. The variation of metal nuclearity and metal-support interactions are effective ways to change the geometric and electronic properties of the supported metal catalyst, leading to different types of the active sites exposing on the support that would take effect on catalyzing the reaction. In this work, a series of supported Ir catalysts (on MgAl2O4 and SiO2) with different particle sizes less than 3 nm were utilized for hydrogenolysis of n-butane and ethane to study the structure sensitivity as well as the potential reaction pathways. The results indicate that the activity of n-butane hydrogenolysis increases as Ir particle size increases in the small particle size range (0.7–1.4 nm) and then drops when the Ir particle size further increases and the Ir single atoms might be inactive for hydrogenolysis after the post-reaction analysis. The selectivity of n-butane hydrogenolysis is dominated by central and one terminal C–C bond cleavage on the n-butane molecules at low temperature range. The selectivity to central C–C bond cleavage is highly dependent on the size of Ir and increases with a decrease in particle size down to ~1.4 nm but remains constant with further decrease in size. The hydrogenolysis of ethane shows a similar trend in the small size range but the activity is much lower than n-butane, which supports the low level of series reaction pathway in the case of n-butane hydrogenolysis. In addition to Ir nuclearity, the effect of electronic properties was also studied on another series of Ir catalysts supported on ZnAl2O4, in which zinc replace the magnesium within the same spinel structure. The characterization results including HAADF-STEM and volumetric CO chemisorption show the difference of Ir nuclearity in the subnanometer regime and nanoparticles (~1.4 nm), while XPS and DRIFTS indicate the difference of electronic properties from metal-support interaction on the two Ir catalysts with the same nuclearity but reduced at different temperatures. Acetylene hydrogenation is structure sensitive on Ir/ZnAl2O4 catalysts and the activity and selectivity are mainly determined by Ir nuclearity instead of the difference in electronic properties. The Ir single atoms and subnanometer clusters are more selective to the target product of C2H4 but less active than large Ir nanoparticles as there might be more π-bonded adsorption than di-σ bonded adsorption for C2H2 on the Ir single atoms and subnanometer clusters. / Doctor of Philosophy / The supported metal catalyst is a kind of effective substance that could help increase the reaction rate when being properly utilized in the reaction. From the industry point of view, the best thing is to maximize the catalyst productivity and minimize the expense so that the economic benefit could be magnified. The catalyst effectiveness in a certain reaction might be different when the surface structure of the catalyst varies. Usually, only the fraction of the surface metals could take effect. As the particle size of the catalyst decreases, the fraction of the surface atoms that contain active sites drastically changes, leading to a different catalytic performance and probably lower cost with improved efficiency for metal utilization. Therefore, it is very significant for the researchers to study the reaction structure sensitivity on the same series of catalysts with different particle sizes. Also, by understanding the reaction mechanism and fundamentals of the catalytic system, it would be possible for the researchers to rationally design the catalysts aiming at higher efficiency and lower cost. In this work, the reaction of hydrogenolysis that cleaves the C–C bonds within the alkanes molecules was studied on the supported Ir catalysts (Ir/MgAl2O4 and Ir/SiO2) with different particle sizes ranging from mostly single atoms, subnanometer clusters to nanoparticles. For n-butane hydrogenolysis, it is found that the selectivity to the target product of ethane is weakly dependent on particle size when smaller than 1.4 nm but decreases as the size further increases. Meantime, the activity is highest on the catalyst with surface-average particle size of 1.4 nm. Therefore, Ir size of ~1.4 nm is optimum for activity and selectivity to ethane. The series of Ir/ZnAl2O4 catalysts was tested for structure sensitivity by another probe reaction, semi-hydrogenation of acetylene. The adsorbed acetylene molecules could be hydrogenated by adding two hydrogen to form the adsorbed ethylene before desorption or further hydrogenation to form ethane. Our results show the Ir single atoms and subnanometer clusters are more selective to the target product of ethylene but less active than the large nanoparticles. With the understanding of structure sensitivity, researchers are able to rationally design the catalysts based on their necessity for certain reactions.

Synthétiser de l'éthylène glycol et du propylène glycol à partir de ressources renouvelables est un défi pour une chimie durable. L'hydrogénolyse des alditols (xylitol et sorbitol) issus de la biomasse lignocellulosique en glycols est une possibilité. Cette réaction a été effectuée en milieu aqueux dans des conditions opératoires sévères (200°C ; 60 bar H2) en présence d'un catalyseur hétérogène à base de ruthénium (3%Ru/C) et d'une base homogène (Ca(OH)2). Après avoir fait l'étude détaillée des différents mécanismes intervenant au cours de la réaction (épimérisation, décarbonylation, rétro-aldol, etc.), nous avons déterminé un ratio molaire permettant d'obtenir une activité de 93 h-1 et une forte sélectivité en glycols (55%) et en glycérol (15%). Au-delà de ce ratio, le lactate est produit majoritairement au détriment du propylène glycol. Des catalyseurs bifonctionnels (Ru/oxyde basique/C) ont été développés pour s'affranchir de la base homogène. Le catalyseur 3%Ru/MnO(19%)/C présente une forte activité (384 h-1) pour une sélectivité en glycols et en glycérol de 35% et 17%. Cependant une lixiviation du Mn se produit au cours de la réaction en raison de la production de faibles quantités de carboxylates. L'utilisation d'un solvant binaire H2O : ROH (ROH : MeOH ; EtOH ; 1-PrOH et 1-BuOH) en présence d'un catalyseur Ru/MnO/C, a permis d'augmenter les sélectivités en glycols et glycérol jusqu'à 70%. Cependant le dépôt de coke en surface désactive le catalyseur. Des catalyseurs d'oxydes mixtes à base de Mn (ex. : Ru-MnOX-Al) ont également permis d'augmenter la sélectivité en glycols et glycérol jusqu'à 60% pour une activité de 60 h-1 tout en limitant la lixiviation du Mn / The synthesis of ethylene and propylene glycols from renewables is a great challenge for a green chemistry. The hydrogenolysis of alditols (i.e. xylitol and sorbitol) from lignocellulosic biomass into glycols is an interesting process. This reaction was investigated in aqueous media under harsh operating conditions (200°C; 60 bar H2) over Ru-based heterogeneous catalyst (i.e. 3%Ru/C) and a homogeneous basic promotor (i.e. Ca(OH)2). The kinetic studies revealed that several reactions can occur such as epimerization, decarbonylation or retro-aldol. An optimal molar ratio Rmol(OH-/alditol) of 0.13 led to the highest selectivities to glycols (55%) and glycerol (15%) for an activity of 93 h-1. Beyond this ratio, lactate was principally produced to the detriment of propylene glycol. Bifunctional catalysts (Ru/basic oxide/C) were synthetized in order to perform this reaction in neutral conditions. 3%Ru/MnO(19%)/C showed a high activity (384 h-1) and high selectivities to glycols (37%) and glycerol (17%). However, Mn leaching occurred during the reaction (70%) due to the production of small amount of carboxylates. The use of binary solvent H2O: ROH with ROH: MeOH; EtOH; 1-PrOH and 1-BuOH, enhanced the Ru/MnO/C behavior with selectivities to glycols and glycerol up to 70% in spite of the coke formation on the catalysts. Mn-based mixed oxide catalysts in presence of Ru (i.e. Ru-MnOX-Al) were synthetized and led to high selectivities to glycols and glycerol (60%) with an average activity of 60 h-1. The stability of these catalysts was enhanced by decreasing the substrate concentration