The title chroman is useful in synthesis and as a water-soluble analog of γ-tocopherol, a member of the vitamin E family. This new synthesis of γ-trolox proceeds via selective aromatic demethylation of Trolox, the more easily available 2,5,7,8-tetramethyl homolog compound. This route is shorter than the previous synthesis, avoids the use of cyanide and methoxybutadiene, and requires no chromatography.

Diminishing petroleum reserves and environmental considerations have strengthened the demand for developing renewable fuel technologies. One alternative is deoxygenating plant oils, animal fats, and waste lipid streams to fuel-like hydrocarbons. These fuels offer a drop-in replacement to petroleum products while potentially becoming carbon neutral, satisfying both fuel and environmental concerns. This fuel is obtained through catalytic deoxygenation via either hydrodeoxygenation (HDO) or decarboxylation/ decarbonylation (deCOx). HDO requires problematic sulfided catalysts and extreme hydrogen pressures to convert lipids to fuel-like hydrocarbons. Therefore, this work focuses on the deCOx pathway, where hydrogen is not required for deoxygenation to take place. Generally, other authors use Pd or Pt as the active metals for deCOx; however, their cost can be industrially prohibitive. Recently, inexpensive Ni catalysts have shown comparable catalytic deCOx activity to Pd and Pt, albeit significant catalyst deactivation and catalytic cracking to undesirable products remain problematic. Therefore, this work aims to improve the activity, selectivity, and recyclability of supported Ni catalysts for the deCOx of lipids. Cu, Sn, and minimal amount of Pt were investigated as secondary promoter metals for Ni catalysts for deCOx. Deoxygenation of waste lipids such as brown grease and yellow grease was also accomplished in an industrially relevant fixed bed reactor.

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Devido ao efeito estufa, a produção de hidrogênio a partir da reação de reforma do bioetanol tem se tornado um assunto de grande interesse em catálise heterogênea. Os catalisadores à base de Pt são empregados nos processos de purificação de H2 e também em eletrocatalisadores das células a combustível do tipo membrana polimérica (PEMFC). O hidrogênio obtido a partir da reforma do etanol contém como contaminante o acetaldeído e pequenas quantidades de CO. Assim, pode-se prever que muitas reações podem ocorrer na presença de catalisadores de Pt durante o processo de purificação do H2 e mesmo no próprio eletrocatalisador. Desta forma, este trabalho tem como objetivo descrever o comportamento do acetaldeído na presença de catalisadores de Pt. Para tanto foram preparados dois catalisadores, Pt/SiO2 e Pt/USY, contendo 1,5% de metal em ambos. Também foi estudado um eletrocatalisador (comercial) de Pt suportado em carvão (Pt/C). Os catalisadores foram caracterizados através das técnicas de análise textural, difração de raios X (DRX), quimissorção de H2, reação de desidrogenação do ciclohexano, espectroscopia no infravermelho de piridina adsorvida, dessorção a temperatura programada de n-butilamina (TPD de n-butilamina), dessorção a temperatura programada de CO2 (TPD-CO2), análise termogravimétrica, microscopia eletrônica de varredura (MEV) e espectroscopia de dispersão de energia (EDS). Os testes catalíticos foram realizados entre as temperaturas de 50 e 350 C em corrente contendo acetaldeído, H2 e N2. Foi observado que as propriedades ácido-básicas dos suportes promovem as reações de condensação com formação de éter etílico e acetato de etila. O acetaldeído em catalisadores de Pt sofre quebra das ligações C-C e C=O. A primeira ocorre em uma ampla faixa de temperaturas, enquanto a segunda apenas em temperaturas abaixo de 200 C. A quebra da ligação C-C produz metano e CO. Já a quebra da ligação C=O gera carbono residual nos catalisadores, assim como espécies oxigênio, que por sua vez são capazes de eliminar o CO da superfície dos catalisadores. Nota-se que o tipo de suporte utilizado influencia na distribuição de produtos, principalmente a baixas temperaturas. Além disso, constatou-se que a descarbonilação não é uma reação sensível à estrutura do catalisador. Verificou-se também a presença de resíduos sobre os catalisadores, possivelmente oriundos não somente da quebra da ligação C=O, mas também de reações de polimerização / Due to the greenhouse effect, hydrogen production from bioethanol reforming is a very important subject in heterogeneous catalysis research. Pt based catalysts are employed in H2 purification processes and also as electrocatalysts of PEM (Proton Exchange Membrane) fuel cells. Hydrogen obtained from ethanol reforming may contain acetaldehyde and small amounts of CO as contaminants. This very reactive aldehyde can interact with Pt based catalysts during purification process, and also with the electrocatalyst. Therefore, this work aims to study the acetaldehyde behavior in the presence of platinum based catalysts under hydrogen atmosphere. Two catalysts named Pt/SiO2 and Pt/USY were prepared, containing 1,5% of Pt. A commercial Pt eletrocatayst supported on carbon (Pt/C) was also studied. The catalysts were characterized by textural analysis, XRD, H2 chemisorption, cyclohexane dehydrogenation reaction, pyridine IR, n-butylamine TPD, CO2 TPD, TGA/DTG, SEM and EDS. The catalytic tests were carried out in a fixed bed reactor at temperature range of 50-350 C, under acetaldehyde, H2 and N2 flow. It was observed that the acid-basic supports properties promoted condensation reactions with the formation of ethylic ether and ethyl acetate. Once in contact with Pt based catalysts, acetaldehyde undergoes C-C and C=O bond scissions. The former occurs at a wide temperature range, whereas the latter occurs only at low temperatures (< 200 C). The C-C bond scission (decarbonylation) produces methane and CO. The C=O bond scission generates carbon residues on the catalyst, as well as oxygen species, which in turn eliminate CO from the catalytic surface. It was noticed that the type of support influences products distribution, mainly at low temperatures. The data also show that decarbonylation is not a structure-sensitive reaction. Residues were observed on Pt/USY which were generated not only from C=O bond rupture, but also from acetaldehyde polymerization

Devido ao efeito estufa, a produção de hidrogênio a partir da reação de reforma do bioetanol tem se tornado um assunto de grande interesse em catálise heterogênea. Os catalisadores à base de Pt são empregados nos processos de purificação de H2 e também em eletrocatalisadores das células a combustível do tipo membrana polimérica (PEMFC). O hidrogênio obtido a partir da reforma do etanol contém como contaminante o acetaldeído e pequenas quantidades de CO. Assim, pode-se prever que muitas reações podem ocorrer na presença de catalisadores de Pt durante o processo de purificação do H2 e mesmo no próprio eletrocatalisador. Desta forma, este trabalho tem como objetivo descrever o comportamento do acetaldeído na presença de catalisadores de Pt. Para tanto foram preparados dois catalisadores, Pt/SiO2 e Pt/USY, contendo 1,5% de metal em ambos. Também foi estudado um eletrocatalisador (comercial) de Pt suportado em carvão (Pt/C). Os catalisadores foram caracterizados através das técnicas de análise textural, difração de raios X (DRX), quimissorção de H2, reação de desidrogenação do ciclohexano, espectroscopia no infravermelho de piridina adsorvida, dessorção a temperatura programada de n-butilamina (TPD de n-butilamina), dessorção a temperatura programada de CO2 (TPD-CO2), análise termogravimétrica, microscopia eletrônica de varredura (MEV) e espectroscopia de dispersão de energia (EDS). Os testes catalíticos foram realizados entre as temperaturas de 50 e 350 C em corrente contendo acetaldeído, H2 e N2. Foi observado que as propriedades ácido-básicas dos suportes promovem as reações de condensação com formação de éter etílico e acetato de etila. O acetaldeído em catalisadores de Pt sofre quebra das ligações C-C e C=O. A primeira ocorre em uma ampla faixa de temperaturas, enquanto a segunda apenas em temperaturas abaixo de 200 C. A quebra da ligação C-C produz metano e CO. Já a quebra da ligação C=O gera carbono residual nos catalisadores, assim como espécies oxigênio, que por sua vez são capazes de eliminar o CO da superfície dos catalisadores. Nota-se que o tipo de suporte utilizado influencia na distribuição de produtos, principalmente a baixas temperaturas. Além disso, constatou-se que a descarbonilação não é uma reação sensível à estrutura do catalisador. Verificou-se também a presença de resíduos sobre os catalisadores, possivelmente oriundos não somente da quebra da ligação C=O, mas também de reações de polimerização / Due to the greenhouse effect, hydrogen production from bioethanol reforming is a very important subject in heterogeneous catalysis research. Pt based catalysts are employed in H2 purification processes and also as electrocatalysts of PEM (Proton Exchange Membrane) fuel cells. Hydrogen obtained from ethanol reforming may contain acetaldehyde and small amounts of CO as contaminants. This very reactive aldehyde can interact with Pt based catalysts during purification process, and also with the electrocatalyst. Therefore, this work aims to study the acetaldehyde behavior in the presence of platinum based catalysts under hydrogen atmosphere. Two catalysts named Pt/SiO2 and Pt/USY were prepared, containing 1,5% of Pt. A commercial Pt eletrocatayst supported on carbon (Pt/C) was also studied. The catalysts were characterized by textural analysis, XRD, H2 chemisorption, cyclohexane dehydrogenation reaction, pyridine IR, n-butylamine TPD, CO2 TPD, TGA/DTG, SEM and EDS. The catalytic tests were carried out in a fixed bed reactor at temperature range of 50-350 C, under acetaldehyde, H2 and N2 flow. It was observed that the acid-basic supports properties promoted condensation reactions with the formation of ethylic ether and ethyl acetate. Once in contact with Pt based catalysts, acetaldehyde undergoes C-C and C=O bond scissions. The former occurs at a wide temperature range, whereas the latter occurs only at low temperatures (< 200 C). The C-C bond scission (decarbonylation) produces methane and CO. The C=O bond scission generates carbon residues on the catalyst, as well as oxygen species, which in turn eliminate CO from the catalytic surface. It was noticed that the type of support influences products distribution, mainly at low temperatures. The data also show that decarbonylation is not a structure-sensitive reaction. Residues were observed on Pt/USY which were generated not only from C=O bond rupture, but also from acetaldehyde polymerization

Zusammenfassend konnte im Rahmen dieser Arbeit das Synthesepotential von Cyclohexadienen und Cyclohexenen deutlich erweitert werden. Die Darstellung der 1-Alkylcyclohexa-2,5-dien-1-carbonsäuren erfolgte mittels Birch-Reduktion in flüssigem Ammoniak und anschließender Umsetzung der intermediär entstehenden Dianionen mit Alkylhalogeniden. So konnte ausgehend von verschiedenen Benzoesäurederivaten eine Reihe interessanter Cyclohexadiene in sehr guten Ausbeuten synthetisiert werden. Erstmals gelangen säurekatalysierte Decarbonylierungen von Cyclohexadiencarbonsäuren, was die einfache Synthese substituierter Aromaten in ausgezeichneten Ausbeuten ermöglichte. In dieser Arbeit wird der Reaktionsmechanismus vorgestellt, welcher durch den Nachweis von Kohlenmonoxid in der Gasphase der Reaktionslösung durch IR-Spektroskopie untermauert wird. Bei der säurekatalysierten Umsetzung von 3-alkylsubstituierten Cyclohexadien-carbonsäuren entstanden neben den erwarteten Aromaten Lactone in ca. 50% Ausbeute. Schließlich zeigen die untersuchten Singulettsauerstoff-En-Reaktionen, der im ersten Teil dargestellten Cyclohexadiene und Lactone, durchweg hohe Regioselektivitäten und lieferten durch elektrostatische Wechselwirkungen und konformative Effekte zum Teil sehr gute Diastereoselektivitäten. Die auxiliarkontrollierte Photooxygenierungen von Cyclohexenon welches mit verschiedenen Weinsäureestern ketalisiert wurde, zeigten jedoch keine bevorzugte p-Facialität des Singulettsauerstoffs. / In this dissertation thesis it was possible to extend the synthetical potential of cyclohexadienes and cyclohexenes with partially newly developed and very efficient synthetic pathways. The alkylcyclohexadiene carboxylic acids were synthesized in good yields via well known Birch-reduction procedure in liquid ammonia from a broad variety of substituted benzoic acid derivatives. A wide range of alkylhalides were subsequently added to the resulting dianion. We were able to decarbonylize the cyclohexadienes through acid catalyses, which leads to ipso-substituted aromatics in excellent yields. The study presents the postulated mechanism, which is supported by the proof of carbon monoxide in the gas phase of the reactionmixture with IR-spectroscopy. When 3-alkylsubstituted cyclohexadiene carboxylic acids were subjected to the acid catalyses they gave lactones in up to 50% yield as side products of the aromatization product.The cyclohexadienes and lactones were used as substrates in singlet oxygen-en-reactions with photochemically induced singulet oxygen. The products showed high regioselectivitiy and partially high diastereoselectivity which is caused by electrostatic interaction and conformativ effects of the reaction intermediates. Experiments to induce auxiliary controlled photooxygenations of cyclohexenones, which were ketalysed with different chiral tartaric acid esters leaded to poor diastereoselectivity and a diverse mixture of isomers.

En combinant expérimentations et calculs ab initio, nous proposons une étude rationnelle des mécanismes de désoxygénation de molécules modèles pertinentes (heptanoate d'éthyle et heptanal) afin de fournir des guides pour définir des systèmes catalytiques optimaux pour l'hydrotraitement de matières premières renouvelables (huiles végétales, graisses animales). L'hydrotraitement d'huiles végétales, par la réaction de désoxygénation, est une voie alternative à la transestérification et peut être envisagée pour obtenir une base gazole de haute qualité. La transformation des composés oxygénés modèles a été étudiée sous une pression totale de 1.5 MPa, à une température de 523 K, dans un réacteur à lit fixe en présence de différents sulfures de métaux de transition massiques (SMT). Cette étude a mis en évidence l'influence de la nature phase sulfure sur la sélectivité des voies de désoxygénation (hydrodésoxygénation (HDO) et/ou décarbonylation/ décarboxylation (DCO)) ainsi que la réactivité particulière du sulfure de rhodium lors de la transformation de l'heptanoate d'éthyle. À l'inverse, quelle que soit la phase sulfure utilisée, la transformation de l'heptanal suit principalement la voie HDO. Dans nos conditions réactionnelles, l'heptanal a été identifié comme un intermédiaire de cette voie de désoxygénation. L'effet promoteur du cobalt et du nickel sur l'activité du sulfure de molybdène monométallique a été observé lors de la transformation de l'heptanal. La relation entre les activités en désoxygénation et en HDO et l'énergie de liaison métal-soufre (E(MS)) calculée ab initio des solides suit une courbe en volcan. Le sulfure mixte NiMoS (0.43), qui présente une E(MS) intermédiaire (127 kJ.mol-1), est le SMT le plus actif pour les deux réactions. Le catalyseur bimétallique CoMoS (0.1) présente la sélectivité HDO/DCO la plus élevée. À l'aide des résultats catalytiques et de calculs ab initio, deux mécanismes réactionnels sont proposés pour les voies de réactions HDO et DCO / By combining well defined experiments and density functional theory (DFT) calculations, we propose a rational understanding of the deoxygenation mechanisms of relevant oxygenate molecules (ethyl heptanoate and heptanal) so as to provide guides to define optimal catalytic systems for the hydrotreating of renewable feedstocks (vegetable oils, animals fats). The hydrotreatment of vegetable oils, with the deoxygenation reaction, is an alternative route to transesterification and can be used to obtain high quality diesel. The transformation of oxygenated model compounds was studied under a total pressure of 1.5 MPa, at 523 K, in a fixed bed reactor over various unsupported transition metal sulfide catalytic phases (TMS). Results have shown the influence of the sulfide phase on the selectivity for deoxygenation reaction (hydrodeoxygenation (HDO) and/or decarbonylation/ decarboxylation (DCO)) and the specific reactivity of the rhodium sulfide for the transformation of ethyl heptanoate. The study of the transformation of heptanal shows the reaction of deoxygenation is preferentially following the HDO pathway over all the catalysts. In our reaction conditions, heptanal was identified as a reaction intermediate of this deoxygenation pathway. The promoting effect of cobalt and nickel on the activity of monometallic molybdenum sulphide was observed for the transformation of heptanal. The relation between the deoxygenation and HDO rates and the ab initio calculated sulphur-metal bond energy E(MS) in the bulk TMS is following a volcano curve. Bimetallic sulfide NiMoS (0.43), with an intermediate E(MS) (127 kJ.mol-1), is found as the most active TMS for both reactions. The maximum of the HDO/DCO selectivity is obtained for the mixed catalyst CoMoS (0.1). Thanks to catalytic results and ab initio calculations, two reaction pathways are proposed for HDO and DCO reactions

No description available.

Formaldehyde is a chemical used widely in the manufacture of building materials. A remarkable example is represented by the Lucite two-step Alpha technology for the large scale production of methyl methacrylate (MMA), the essential building block of all acrylic-based products. Esters and ketones are important intermediates in the manufacture of acrylate esters therefore α-hydroxymethylenation of carbonyl compounds using formaldehyde as a one carbon alkylating agent and subsequent dehydration to the corresponding methylenated derivatives has been explored in the current work. We report a novel catalytic approach for the synthesis of methyl methacrylate (MMA) via one-pot α-methylenation of methyl propanoate (a chemical intermediate of the ALPHA process) with formaldehyde, generated in situ by Ru-catalysed dehydrogenation of methanol. Elucidation of the mechanism involved in the catalytic dehydrogenation of methanol along with the collateral alcohol decarbonylation reaction was gained through a combined experimental and DFT study. The development of an alternative process where anhydrous formaldehyde is produced in situ would provide a simplification over the current second step of the ALPHA technology where the formaldehyde is initially produced as formalin, subsequently dehydrated to afford anhydrous formaldehyde in order to ensure high selectivity to MMA. As an alternative approach, ketones, in particular 3-pentanone and 2-butanone, were targeted as potential substrates in order to overcome some of the problems related to competing reactions that occur at the ester group. Hydroxymethylenation, followed by dehydration and Baeyer-Villager oxidation, possibly catalysed by enzymes to reverse the normal selectivity, leads to the formation of acrylate esters. The catalytic reaction is enabled by a gold carbene hydroxide complex in such a way that the substrate undergoes C-H activation and the nascent metal alkyl acts as a nucleophile towards the electrophilic formaldehyde, supplied in the form of alcoform* (solution of paraformaldehyde in methanol).