984 resultados para NiO-MgO-ZrO(2) catalysts


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The research of new catalysts for the hydrogen production described in this thesis was inserted within a collaboration of Department of Industrial Chemistry and Materials of University of Bologna and Air Liquide (Centre de Recherche Claude-Delorme, Paris). The aim of the work was focused on the study of new materials, active and stable in the hydrogen production from methane, using either a new process, the catalytic partial oxidation (CPO), or a enhanced well-established process, the steam methane reforming (SMR). Two types of catalytic materials were examined: 1) Bulk catalysts, i.e. non-supported materials, in which the active metals (Ni and/or Rh) are stabilized inside oxidic matrix, obtained from perovskite type compounds (PVK) and from hydrotalcite type precursors (HT); 2) Structured catalysts, i.e. catalysts supported on materials having high thermal conductivity (SiC and metallic foams). As regards the catalytic partial oxidation, the effect of the metal (Ni and/or Rh), the role of the metal/matrix ratio and the matrix formulation of innovative catalysts obtained from hydrotalcite type precursors and from perovskites were examined. In addition, about steam reforming process, the study was carried out first on commercial type catalysts, examining the deactivation in industrial conditions, the role of the operating conditions and the activity of different type of catalysts. Then, innovative materials bulk (PVK and HT) and structured catalysts (SiC and metallic foam) were studied and a new preparation method was developed.

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Fog oases, locally named Lomas, are distributed in a fragmented way along the western coast of Chile and Peru (South America) between ~6°S and 30°S following an altitudinal gradient determined by a fog layer. This fragmentation has been attributed to the hyper aridity of the desert. However, periodically climatic events influence the ‘normal seasonality’ of this ecosystem through a higher than average water input that triggers plant responses (e.g. primary productivity and phenology). The impact of the climatic oscillation may vary according to the season (wet/dry). This thesis evaluates the potential effect of climate oscillations, such as El Niño Southern Oscillation (ENSO), through the analysis of vegetation of this ecosystem following different approaches: Chapters two and three show the analysis of fog oasis along the Peruvian and Chilean deserts. The objectives are: 1) to explain the floristic connection of fog oases analysing their taxa composition differences and the phylogenetic affinities among them, 2) to explore the climate variables related to ENSO which likely affect fog production, and the responses of Lomas vegetation (composition, productivity, distribution) to climate patterns during ENSO events. Chapters four and five describe a fog-oasis in southern Peru during the 2008-2010 period. The objectives are: 3) to describe and create a new vegetation map of the Lomas vegetation using remote sensing analysis supported by field survey data, and 4) to identify the vegetation change during the dry season. The first part of our results show that: 1) there are three significantly different groups of Lomas (Northern Peru, Southern Peru, and Chile) with a significant phylogenetic divergence among them. The species composition reveals a latitudinal gradient of plant assemblages. The species origin, growth-forms typologies, and geographic position also reinforce the differences among groups. 2) Contradictory results have emerged from studies of low-cloud anomalies and the fog-collection during El Niño (EN). EN increases water availability in fog oases when fog should be less frequent due to the reduction of low-clouds amount and stratocumulus. Because a minor role of fog during EN is expected, it is likely that measurements of fog-water collection during EN are considering drizzle and fog at the same time. Although recent studies on fog oases have shown some relationship with the ENSO, responses of vegetation have been largely based on descriptive data, the absence of large temporal records limit the establishment of a direct relationship with climatic oscillations. The second part of the results show that: 3) five different classes of different spectral values correspond to the main land cover of Lomas using a Vegetation Index (VI). The study case is characterised by shrubs and trees with variable cover (dense, semi-dense and open). A secondary area is covered by small shrubs where the dominant tree species is not present. The cacti area and the old terraces with open vegetation were not identified with the VI. Agriculture is present in the area. Finally, 4) contrary to the dry season of 2008 and 2009 years, a higher VI was obtained during the dry season of 2010. The VI increased up to three times their average value, showing a clear spectral signal change, which coincided with the ENSO event of that period.

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H2 demand is continuously increasing since its many relevant applications, for example, in the ammonia production, refinery processes or fuel cells. The Water Gas Shift (WGS) reaction (CO + H2O = CO2 + H2 DeltaH = -41.1 kJ.mol-1) is a step in the H2 production, reducing significantly the CO content and increasing the H2 one in the gas mixtures obtained from steam reforming. Industrially, the reaction is carried out in two stages with different temperature: the first stage operates at high temperature (350-450 °C) using Fe-based catalysts, while the second one is performed at lower temperature (190-250 °C) over Cu-based catalysts. However, recently, an increasing interest emerges to develop new catalytic formulations, operating in a single-stage at middle temperature (MTS), while maintaining optimum characteristics of activity and stability. These formulations may be obtained by improving activity and selectivity of Fe-based catalysts or increasing thermal stability of Cu-based catalysts. In the present work, Cu-based catalysts (Cu/ZnO/Al2O3) prepared starting from hydrotalcite-type precursors show good homogeneity and very interesting physical properties, which worsen by increasing the Cu content. Among the catalysts with different Cu contents, the catalyst with 20 wt.% of Cu represents the best compromise to obtain high catalytic activity and stability. On these bases, the catalytic performances seem to depend on both metallic Cu surface area and synergetic interactions between Cu and ZnO. The increase of the Al content enhances the homogeneity of the precursors, leading to a higher Cu dispersion and consequent better catalytic performances. The catalyst with 20 wt.% of Cu and a molar ratio M(II)/M(III) of 2 shows a high activity also at 250 °C and a good stability at middle temperature. Thus, it may be considered an optimum catalyst for the WGS reaction at middle temperature (about 300 °C). Finally, by replacing 50 % (as at. ratio) of Zn by Mg (which is not active in the WGS reaction), better physical properties were observed, although associate with poor catalytic performances. This result confirms the important role of ZnO on the catalytic performances, favoring synergetic interactions with metallic Cu.

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2-Phenoxyethanol (ethylene glycol monophenyl ether) is used as solvent for cellulose acetate, dyes, inks, and resins; it is a synthetic intermediate in the production of plasticizers, pharmaceuticals, and fragrances. Phenoxyethanol is obtained industrially by reaction of phenol with ethylene oxide, in the presence of an homogeneous alkaline catalyst, typically sodium hydroxide. The yield is not higher than 95-96%, because of the formation of polyethoxylated compounds. However, the product obtained may not be acceptable for use in cosmetic preparations and fragrance formulations, due to presence of a pungent “metallic” odor which masks the pleasant odor of the ether, deriving from residual traces of the metallic catalyst. Here we report a study aimed at using ethylene carbonate in place of ethylene oxide as the reactant for phenoxyethanol synthesis; the use of carbonates as green nucleophilic reactants is an important issue in the context of a modern and sustainable chemical industry. Moreover, in the aim of developing a process which might adhere the principles of Green Chemistry, we avoided the use of solvents, and used heterogeneous basic catalysts. We carried out the reaction by using various molar ratios between phenol and ethylene carbonate, at temperatures ranging between 180 and 240°C, with a Na-mordenite catalyst. Under specific conditions, it was possible to obtain total phenol conversion with >99% yield to phenoxyethanol in few hours reaction time, using a moderate excess of ethylene carbonate. Similar results, but with longer reaction times, were obtained using a stoichiometric feed ratio of reactants. One important issue of the research was finding conditions under which the leaching of Na was avoided, and the catalyst could be separated and reused for several reaction batches.

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Here, we present the adaptation and optimization of (i) the solvothermal and (ii) the metal-organic chemical vapor deposition (MOCVD) approach as simple methods for the high-yield synthesis of MQ2 (M=Mo, W, Zr; Q = O, S) nanoparticles. Extensive characterization was carried out using X-ray diffraction (XRD), scanning and transmission electron micros¬copy (SEM/TEM) combined with energy dispersive X-ray analysis (EDXA), Raman spectroscopy, thermal analyses (DTA/TG), small angle X-ray scattering (SAXS) and BET measurements. After a general introduction to the state of the art, a simple route to nanostructured MoS2 based on the decomposition of the cluster-based precursor (NH4)2Mo3S13∙xH2O under solvothermal conditions (toluene, 653 K) is presented. Solvothermal decomposition results in nanostructured material that is distinct from the material obtained by decomposition of the same precursor in sealed quartz tubes at the same temperature. When carried out in the presence of the surfactant cetyltrimethyl¬ammonium bromide (CTAB), the decomposition product exhibits highly disordered MoS2 lamellae with high surface areas. The synthesis of WS2 onion-like nanoparticles by means of a single-step MOCVD process is discussed. Furthermore, the results of the successful transfer of the two-step MO¬CVD based synthesis of MoQ2 nanoparticles (Q = S, Se), comprising the formation of amorphous precursor particles and followed by the formation of fullerene-like particles in a subsequent annealing step to the W-S system, are presented. Based on a study of the temperature dependence of the reactions a set of conditions for the formation of onion-like structures in a one-step reaction could be derived. The MOCVD approach allows a selective synthesis of open and filled fullerene-like chalcogenide nanoparticles. An in situ heating stage transmission electron microscopy (TEM) study was employed to comparatively investigate the growth mechanism of MoS2 and WS2 nanoparticles obtained from MOCVD upon annealing. Round, mainly amorphous particles in the pristine sample trans¬form to hollow onion-like particles upon annealing. A significant difference between both compounds could be demonstrated in their crystallization conduct. Finally, the results of the in situ hea¬ting experiments are compared to those obtained from an ex situ annealing process under Ar. Eventually, a low temperature synthesis of monodisperse ZrO2 nanoparticles with diameters of ~ 8 nm is introduced. Whereas the solvent could be omitted, the synthesis in an autoclave is crucial for gaining nano-sized (n) ZrO2 by thermal decomposition of Zr(C2O4)2. The n-ZrO2 particles exhibits high specific surface areas (up to 385 m2/g) which make them promising candidates as catalysts and catalyst supports. Co-existence of m- and t-ZrO2 nano-particles of 6-9 nm in diameter, i.e. above the critical particle size of 6 nm, demonstrates that the particle size is not the only factor for stabilization of the t-ZrO2 modification at room temperature. In conclusion, synthesis within an autoclave (with and without solvent) and the MOCVD process could be successfully adapted to the synthesis of MoS2, WS2 and ZrO2 nanoparticles. A comparative in situ heating stage TEM study elucidated the growth mechanism of MoS2 and WS2 fullerene-like particles. As the general processes are similar, a transfer of this synthesis approach to other layered transition metal chalcogenide systems is to be expected. Application of the obtained nanomaterials as lubricants (MoS2, WS2) or as dental filling materials (ZrO2) is currently under investigation.

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Von aromatischen Aldehyden abgeleitete α-Aminonitrile können ohne die Anwendung von Schutzgruppen in α-Position deprotoniert werden, wenn keine lithiumhaltigen Basen verwendet werden. Ziel der vorliegenden Arbeit war es, die Reaktionen deprotonierter α-Aminonitrile mit Elektrophilen zu untersuchen. Die Addition von α-Aminocarbanionen an Imine führt unter intramolekularer Eliminierung von HCN zu Endiaminen, die sich in einer Eintopfsynthese abhängig von der Aufarbeitung in 1,2-Diamine oder 1,2-Diimine umwandeln lassen. Die nach Oxidation durch Luftsauerstoff erhaltenen Diimine können mit dem Reduktionsmittel BH3·THF diastereoselektiv reduziert werden. Es hat sich hier gezeigt, dass durch Zugabe einer katalytischen Menge an NaBH4 hauptsächlich die syn-Diamine erhalten werden, der Zusatz von Phthalsäure wiederum liefert bevorzugt die anti-Produkte. In beiden Fällen wird das Produkt in quantitativer Ausbeute erhalten. So konnte also eine effektive diastereoselektive Reduktionsmethode entwickelt werden, die eine freie Wahl der syn- oder anti-Konfiguration ermöglicht. Um enantiomerenreine 1,2-Diamine zu erhalten, wurden verschiedene Methoden getestet. Sowohl auxiliargesteuerte Synthesen mit einem N-Glycosyl-Aminonitril oder mit chiralen Sulfinyliminen als auch die Reduktion durch chirale Borverbindungen (CBS-Katalysatoren, Triacyloxyborhydrid oder Diisopinocamphenylboran), Transferhydrierungen mit chiralen Difluortitanocen-, Noyori- oder Organophosphat-Katalysatoren sowie enantioselektive Hydrierungen mit chiralen Übergangsmetall-katalysatoren waren jedoch nicht erfolgreich. Die Umsetzung der 1,2-Diimine mit Chlormethylethern oder -estern liefert die entsprechenden unsymmetrischen Imidazoliumsalze. Diese konnten zu N-heterocyclischen Carbenen deprotoniert und erfolgreich als Liganden in Suzuki- und Heck-Reaktionen eingesetzt werden. Durch die 1,2-Addition α-deprotonierter Streckerprodukte und anschließende Reduktion im Eintopfverfahren konnten 1,2-Aminoalkohole in mäßigen bis guten Ausbeuten dargestellt werden. Die Umsetzung von α-Aminocarbanionen mit N-Acyliminen erlaubt zudem die Synthese tetrasubstituierter Imidazole und trisubstituierter Oxazole in drei beziehungsweise vier Stufen: Die zunächst gebildeten α-Amino-α-acylaminopropionitrile können isoliert und in Gegenwart von Base einer Retro-Strecker-Reaktion unterworfen werden. Abhängig vom Substitutionsmuster schließt sich in manchen Fällen nach der Eliminierung von HCN direkt die Cyclisierung zum Imidazol an. Nicht cyclisierte Intermediate lassen sich durch Dehydratisierung mit PCl5 zu Imidazolen umsetzen, aber auch unter sauren Bedingungen zu α-Acylaminoketonen hydrolysieren, welche wiederum durch Einwirkung von PCl5 in Oxazole überführt werden können. Auf diese Weise wurden Imidazole und Oxazole in moderaten bis hohen Gesamtausbeuten hergestellt.

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Due to the high price of natural oil and harmful effects of its usage, as the increase in emission of greenhouse gases, the industry focused in searching of sustainable types of the raw materials for production of chemicals. Ethanol, produced by fermentation of sugars, is one of the more interesting renewable materials for chemical manufacturing. There are numerous applications for the conversion of ethanol into commodity chemicals. In particular, the production of 1,3-butadiene whose primary source is ethanol using multifunctional catalysts is attractive. With the 25% of world rubber manufacturers utilizing 1,3-butadiene, there is an exigent need for its sustainable production. In this research, the conversion of ethanol in one-step process to 1,3-butadiene was studied. According to the literature, the mechanisms which were proposed to explain the way ethanol transforms into butadiene require to have both acid and basic sites. But still, there are a lot of debate on this topic. Thus, the aim of this research work is a better understanding of the reaction pathways with all the possible intermediates and products which lead to the formation of butadiene from ethanol. The particular interests represent the catalysts, based on different ratio Mg/Si in comparison to bare magnesia and silica oxides, in order to identify a good combination of acid/basic sites for the adsorption and conversion of ethanol. Usage of spectroscopictechniques are important to extract information that could be helpful for understanding the processes on the molecular level. The diffuse reflectance infrared spectroscopy coupled to mass spectrometry (DRIFT-MS) was used to study the surface composition of the catalysts during the adsorption of ethanol and its transformation during the temperature program. Whereas, mass spectrometry was used to monitor the desorbed products. The set of studied materials include MgO, Mg/Si=0.1, Mg/Si=2, Mg/Si=3, Mg/Si=9 and SiO2 which were also characterized by means of surface area measurements.

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In order to match the more stringent environmental regulations, heterogenization of traditional homogeneous processes is one of the main challenges of the modern chemical industry. Great results have been achieved in the fields of petrochemicals and base chemicals, whereas in fine chemical industry most of the synthetic procedures are based on multistep processes catalyzed by homogeneous catalysts mainly used in stoichiometric amounts. In the fine chemicals manufacture not so much efforts have been devoted to the investigation of suitable solid catalysts for the development of greener processes, then this sector represent a very attractive field of research. In this context, the present work deals with the extensive investigation of the possibility to heterogenize existing processes, in particular two different classes of reactions have been studied: alkylation of aromatic and heteroaromatic compounds and selective oxidation of aromatic alcohols. Traditional solid acid catalysts, such as zeolites, clays and alumina have been tested in the gas phase alkylation of 1,2-methylendioxybenzene, core building block of many drugs, pesticides and fragrances. The observed reactivity were clarified through a deep FTIR investigation complemented by ab initio calculation. The same catalysts were tested in the gas phase isopropylation of thiophene with the aim of clearly attribute the role of the reaction parameters in the reaction proceeding and verify the possibility to enhance the selectivity of one of the two possible isomers. Finally various Au/CeO2 catalysts were tested in the synthesis of benzaldehyde and piperonal, two aldehydes largely employed in the manufacture of fine chemical products, through liquid phase oxidation of the corresponding alcohols in very mild conditions.

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The demand of energy, fuels and chemicals is increasing due to the strong growth of some countries in the developing world and the development of the world economy. Unfortunately, the general picture derived sparked an exponential increase in crude oil prices with a consequent increase of the chemical, by-products and energy, depleting the global market. Nowadays biomass are the most promising alternative to fossil fuels for the production of chemicals and fuels. In this work, the development of three different catalytic processes for the valorization of biomass-derived has been investigated. 5-hydroxymethylfurfural oxidation was studied under mild reaction condition using gold and gold/copper based catalysts synthetized from pre-formed nanoparticles and supported onto TiO2 and CeO2. The analysis conducted on catalysts showed the formation of alloys gold/copper and a strong synergistic effect between the two metals. For this reason the bimetallic catalysts supported on titania showed a higher catalytic activity respect to the monometallic catalysts. The process for the production of 2,5-bishydroxymethyl furan (BHMF) was also optimized by means the 5-hydroxymethylfurfural hydrogenation using the Shvo complex. Complete conversion of HMF was achieved working at 90 °C and 10 bar of hydrogen. The complex was found to be re-usable for at least three catalytic cycles without suffering any type of deactivation. Finally, the hydrogenation of furfural and HMF was carried out, developing the process of hydrogen transfer by using MgO as a catalyst and methanol as a hydrogen donor. Quantitative yields to alcohols have been achieved in a few hours working in mild condition: 160 °C and at autogenous pressure. The only by-products formed were light products such as CO, CO2 and CH4 (products derived from methanol transformation), easily separable from the reaction solution depressurizing the reactor.

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A causa delle questioni economiche ed ambientali legate alla sostenibilità dei processi petrolchimici, recentemente l'industria chimica ha focalizzato il proprio interesse nello sviluppo di processi per la produzione di chemicals, che utilizzino materiali di partenza rinnovabili. L'etanolo, prodotto per via fermentativa, sembra essere uno dei bio-building block più promettenti e versatili e può essere utilizzato per numerose applicazioni. È noto da tempo che l’etanolo può reagire su catalizzatori costituiti da ossidi misti con caratteristiche acido-base a dare numerosi composti chimici tra cui acetaldeide, 1,3-butadiene, 1-butanolo e 2-butenale. Nonostante il lungo impiego dell’etanolo nell’industria chimica, il meccanismo di formazione di composti C4 a partire da etanolo è ancora però materia di dibattito. Il meccanismo generalmente accettato si basa sulle seguenti reazioni chiave: deidrogenazione di etanolo ad acetaldeide e condensazione aldolica di due molecole di acetaldeide. Tuttavia in letteratura sono riportate anche altre proposte alternative. In questo lavoro è stato studiato il processo di trasformazione di etanolo su catalizzatori a base di MgO e sistemi misti Mg/SiO, attraverso esperimenti di reattività condotti in un micro-impianto da laboratorio, al fine di fare chiarezza sul meccanismo di formazione di composti C4 a partire da etanolo. In particolare è stato condotto uno studio meccanicistico utilizzando MgO come catalizzatore modello, materiale che possiede esclusivamente proprietà basiche, ritenute essenziali per catalizzare la condensazione di molecole C2. Inoltre, è stata investigata l’influenza delle caratteristiche acido-base del catalizzatore sulla selettività del processo di conversione di etanolo, studiandone la reattività su materiali costituiti da ossidi misti Mg/Si/O, con diverso rapporto atomico tra i due cationi.

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The aim of my PhD research project was to investigate new and more sustainable routes, compared to those currently used, for the production of adipic acid (AA). AA is a very important chemical intermediate. The main use of AA is the production of Nylon-6,6 fibers, resins, polyesters, plasticizers. My project was divided into two parts: 1. The two-step oxidation of cyclohexene, where the latter is first oxidized into trans-1,2-cyclohexanediol (CHD) with aqueous hydrogen peroxide, and then the glycol is transformed into AA by reaction with molecular oxygen. Various catalysts were investigated in this process, both heterogeneous (alumina-supported Ru(OH)x and Au nanoparticles supported on TiO2, MgO and Mg(OH)2) and homogeneous (polyoxometalates). We also studied the mechanism of CHD oxidation with oxygen in the presence of these catalysts. 2. Baeyer-Villiger oxidation of cyclohexanone with aqueous hydrogen peroxide into ɛ-caprolactone, as a first step on the way to produce AA. Study on the mechanism of the uncatalyzed (thermal) oxidation of cyclohexanone were also carried out. Investigation on how the different heterogeneous catalysts affect the formation of the reaction products and their distribution was done.

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The work described in this thesis deals with the development of the asymmetric organocatalytic conjugate addition reaction of 1,3-dicarbonyl compounds to ortho-quinone methides. Due to their instability, these synthetically appealing intermediates have not been fully exploited in catalytic asymmetric settings. In this work, the instability of ortho-quinone methides is overcome by their generation in situ under mild basic conditions, starting from the corresponding sulfonyl derivatives. The bifunctional catalysts used are able to activate both substrates for the reaction, by means of a synergic action of the two catalytic sites, inducing at the same time high enantioselection in the addition step. The reaction leads to the generation of a 2-alkylphenolic framework, featuring a chiral centre at the benzylic position. In particular, the employment of acetylacetone and Meldrum acid as nucleophiles has allowed the obtainment of 4H-chromenes and chroman-2-ones in good yields and generally excellent enantioselectivities. These compounds are synthetic precursors of several natural products, some of which showing interesting biological activity, and of some active pharmaceutical ingredients used in commercial drugs.

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The main research theme of this dissertation is the synthesis of g- and b-carbolines using a metal-catalyzed [2+2+2] cycloaddition strategy of tethered alkynyl-ynamides (diynes) with nitriles. g- and b-carbolines form the core of a large group of natural product and represent important targets for organic chemists. Many of these carbolines showed pharmacological effects ranging from anti-tumor to anxiolytic and anti-HIV activity. A model study with N-Ethynyl-N-tosyl-2-(2-phenylethynyl)aniline and methyl cyanoformate showed that rhodium-based catalysts promote efficiently the reaction. A further optimization showed that the regioselectivity of the reaction can be tuned by the choice of the solvent or by the catalytic system. Application to a larger scope of diynes showed that the regioselectivity strongly depends on the type of substitution of the alkynyl moieties, giving regioselectivities in the range g:b = 1/0 to g:b = 0/1. This [2+2+2] cycloaddition approach for the synthesis of the g- and b-carboline cores was successfully applied to the first total synthesis of Isoperlolyrine and the total synthesis of Perlolyrine. Extension of this strategy to heterocumulenes as cycloaddition partners allowed the synthesis of a g-carbolinone, a thiopyrano[3,4-b]indol-3-imine and thiopyranothiones.

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The research work has dealt with the study of new catalytic processes for the synthesis of fine chemicals belonging to the class of phenolics, namely 2-phenoxyethanol and hydroxytyrosol. The two synthetic procedures investigated have the advantages of being much closer to the Green Chemistry principles than those currently used industrially. In both cases, the challenge was that of finding catalysts and methods which led to the production of less waste, and used less hazardous chemicals, safer solvents, and reusable heterogeneous catalysts. In the case of 2-phenoxyethanol, the process investigated involves the use of ethylene carbonate (EC) as the reactant for phenol O-hydroxyethylation, in place of ethylene oxide. Besides being a safer reactant, the major advantage of using EC in the new synthesis is the better selectivity to the desired product achieved. Moreover, the solid catalyst based on Na-mordenite was fully recyclable. The reaction mechanism and the effect of the Si/Al ratio in the mordenite were investigated. In the case of hydroxytyrosol, which is one of the most powerful natural antioxidants, a new synthetic procedure was investigated; in fact, the method currently employed, the hydrolysis of oleuropein, an ester extracted from the waste water processing of the olive, makes use of large amounts of organic solvents (hexane, ethyl acetate), and involves several expensive steps of purification. The synthesis procedure set up involves first the reaction between catechol and 2,2-dimethoxyacetaldehyde, followed by the one-pot reduction of the intermediate to give the desired product. Both steps were optimized, in terms of catalyst used, and of reaction conditions, that allowed to reach ca 70% yield in each step. The reaction mechanism was investigated and elucidated. During a 3-month period spent at the University of Valencia (with Prof. A. Corma’s group), a process for the production of diesel additives (2,5-bis(propoxymethyl)furan) from fructose has been investigated.

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Anguzykline sind eine große Gruppe von Naturstoffen. Ihnen ist gemein, dass sie eine Benz[a]anthracen-Struktur besitzen oder dass sie in der Biosynthese aus einer Verbindung mit einem solchem Grundgerüst hervorgegangen sind. Viele Vertreter der Anguzykline sind bioaktive Substanzen mit insbesondere antibiotischer Wirkung. In dieser Arbeit wurde eine flexible, modulare Synthese für Anguzykline erarbeitet. Eine Schlüsselreaktion stellte die intramolekulare [2+2+2]-Zykloaddition aus Triinen zu Phthaliden dar. Die in dieser Umwandlung eingesetzten Triine enthalten eine Diin- und eine Monoinkomponente, die über eine Esterbindung miteinander verknüpft sind. Die intramolekulare [2+2+2]-Zyklotrimerisierung wurde an zwei verschiedenen Strukturen der Triinsysteme untersucht: Zum einen Triine, in denen Nona-2,8-diinsäuren mit 1-Aryl-propargylalkoholen verknüpft waren und zum anderen Substrate, in denen die Propargylsäureester von 1-Aryl-nona-2,8-diin-1-olen gebildet wurden. Für die Umsetzung wurden zwei verschiedene Katalysatoren verwendet. Neben dem Wilkinsonkatalysator wurde der Rutheniumkatalysator [Cp*RuCl(cod)] eingesetzt. Beide Katalysatoren sind für die Reaktion geeignet und ergänzen sich hinsichtlich der verschiedenen Triinsysteme. Die Phthalide dienten als Intermediate für den Aufbau eines Tetrahydrobenz[a]anthrachinon-Grundgerüst. Zum Aufbau dieser Struktur wurde eine Synthesesequenz zur Gerüstumlagerung vorgestellt und die Synthesemethode auf verschiedene Vertreter der Anguzyklin-Familie angewendet. Besonderes Augenmerk wurde auf die Synthese des Urdamycinon B gelegt, in dem das Grundgerüst C-glykosidisch mit einem Olivosesubstituenten verknüpft ist.