Biomass Gasification - Process analysis and dimensioning aspects for downdraft units and gas cleaning lines

In such territories where food production is mostly scattered in several small / medium size or even domestic farms, a lot of heterogeneous residues are produced yearly, since farmers usually carry out different activities in their properties. The amount and composition of farm residues, therefore, widely change during year, according to the single production process periodically achieved. Coupling high efficiency micro-cogeneration energy units with easy handling biomass conversion equipments, suitable to treat different materials, would provide many important advantages to the farmers and to the community as well, so that the increase in feedstock flexibility of gasification units is nowadays seen as a further paramount step towards their wide spreading in rural areas and as a real necessity for their utilization at small scale. Two main research topics were thought to be of main concern at this purpose, and they were therefore discussed in this work: the investigation of fuels properties impact on gasification process development and the technical feasibility of small scale gasification units integration with cogeneration systems. According to these two main aspects, the present work was thus divided in two main parts. The first one is focused on the biomass gasification process, that was investigated in its theoretical aspects and then analytically modelled in order to simulate thermo-chemical conversion of different biomass fuels, such as wood (park waste wood and softwood), wheat straw, sewage sludge and refuse derived fuels. The main idea is to correlate the results of reactor design procedures with the physical properties of biomasses and the corresponding working conditions of gasifiers (temperature profile, above all), in order to point out the main differences which prevent the use of the same conversion unit for different materials. At this scope, a gasification kinetic free model was initially developed in Excel sheets, considering different values of air to biomass ratio and the downdraft gasification technology as particular examined application. The differences in syngas production and working conditions (process temperatures, above all) among the considered fuels were tried to be connected to some biomass properties, such elementary composition, ash and water contents. The novelty of this analytical approach was the use of kinetic constants ratio in order to determine oxygen distribution among the different oxidation reactions (regarding volatile matter only) while equilibrium of water gas shift reaction was considered in gasification zone, by which the energy and mass balances involved in the process algorithm were linked together, as well. Moreover, the main advantage of this analytical tool is the easiness by which the input data corresponding to the particular biomass materials can be inserted into the model, so that a rapid evaluation on their own thermo-chemical conversion properties is possible to be obtained, mainly based on their chemical composition A good conformity of the model results with the other literature and experimental data was detected for almost all the considered materials (except for refuse derived fuels, because of their unfitting chemical composition with the model assumptions). Successively, a dimensioning procedure for open core downdraft gasifiers was set up, by the analysis on the fundamental thermo-physical and thermo-chemical mechanisms which are supposed to regulate the main solid conversion steps involved in the gasification process. Gasification units were schematically subdivided in four reaction zones, respectively corresponding to biomass heating, solids drying, pyrolysis and char gasification processes, and the time required for the full development of each of these steps was correlated to the kinetics rates (for pyrolysis and char gasification processes only) and to the heat and mass transfer phenomena from gas to solid phase. On the basis of this analysis and according to the kinetic free model results and biomass physical properties (particles size, above all) it was achieved that for all the considered materials char gasification step is kinetically limited and therefore temperature is the main working parameter controlling this step. Solids drying is mainly regulated by heat transfer from bulk gas to the inner layers of particles and the corresponding time especially depends on particle size. Biomass heating is almost totally achieved by the radiative heat transfer from the hot walls of reactor to the bed of material. For pyrolysis, instead, working temperature, particles size and the same nature of biomass (through its own pyrolysis heat) have all comparable weights on the process development, so that the corresponding time can be differently depending on one of these factors according to the particular fuel is gasified and the particular conditions are established inside the gasifier. The same analysis also led to the estimation of reaction zone volumes for each biomass fuel, so as a comparison among the dimensions of the differently fed gasification units was finally accomplished. Each biomass material showed a different volumes distribution, so that any dimensioned gasification unit does not seem to be suitable for more than one biomass species. Nevertheless, since reactors diameters were found out quite similar for all the examined materials, it could be envisaged to design a single units for all of them by adopting the largest diameter and by combining together the maximum heights of each reaction zone, as they were calculated for the different biomasses. A total height of gasifier as around 2400mm would be obtained in this case. Besides, by arranging air injecting nozzles at different levels along the reactor, gasification zone could be properly set up according to the particular material is in turn gasified. Finally, since gasification and pyrolysis times were found to considerably change according to even short temperature variations, it could be also envisaged to regulate air feeding rate for each gasified material (which process temperatures depend on), so as the available reactor volumes would be suitable for the complete development of solid conversion in each case, without even changing fluid dynamics behaviour of the unit as well as air/biomass ratio in noticeable measure. The second part of this work dealt with the gas cleaning systems to be adopted downstream the gasifiers in order to run high efficiency CHP units (i.e. internal engines and micro-turbines). Especially in the case multi–fuel gasifiers are assumed to be used, weightier gas cleaning lines need to be envisaged in order to reach the standard gas quality degree required to fuel cogeneration units. Indeed, as the more heterogeneous feed to the gasification unit, several contaminant species can simultaneously be present in the exit gas stream and, as a consequence, suitable gas cleaning systems have to be designed. In this work, an overall study on gas cleaning lines assessment is carried out. Differently from the other research efforts carried out in the same field, the main scope is to define general arrangements for gas cleaning lines suitable to remove several contaminants from the gas stream, independently on the feedstock material and the energy plant size The gas contaminant species taken into account in this analysis were: particulate, tars, sulphur (in H2S form), alkali metals, nitrogen (in NH3 form) and acid gases (in HCl form). For each of these species, alternative cleaning devices were designed according to three different plant sizes, respectively corresponding with 8Nm3/h, 125Nm3/h and 350Nm3/h gas flows. Their performances were examined on the basis of their optimal working conditions (efficiency, temperature and pressure drops, above all) and their own consumption of energy and materials. Successively, the designed units were combined together in different overall gas cleaning line arrangements, paths, by following some technical constraints which were mainly determined from the same performance analysis on the cleaning units and from the presumable synergic effects by contaminants on the right working of some of them (filters clogging, catalysts deactivation, etc.). One of the main issues to be stated in paths design accomplishment was the tars removal from the gas stream, preventing filters plugging and/or line pipes clogging At this scope, a catalytic tars cracking unit was envisaged as the only solution to be adopted, and, therefore, a catalytic material which is able to work at relatively low temperatures was chosen. Nevertheless, a rapid drop in tars cracking efficiency was also estimated for this same material, so that an high frequency of catalysts regeneration and a consequent relevant air consumption for this operation were calculated in all of the cases. Other difficulties had to be overcome in the abatement of alkali metals, which condense at temperatures lower than tars, but they also need to be removed in the first sections of gas cleaning line in order to avoid corrosion of materials. In this case a dry scrubber technology was envisaged, by using the same fine particles filter units and by choosing for them corrosion resistant materials, like ceramic ones. Besides these two solutions which seem to be unavoidable in gas cleaning line design, high temperature gas cleaning lines were not possible to be achieved for the two larger plant sizes, as well. Indeed, as the use of temperature control devices was precluded in the adopted design procedure, ammonia partial oxidation units (as the only considered methods for the abatement of ammonia at high temperature) were not suitable for the large scale units, because of the high increase of reactors temperature by the exothermic reactions involved in the process. In spite of these limitations, yet, overall arrangements for each considered plant size were finally designed, so that the possibility to clean the gas up to the required standard degree was technically demonstrated, even in the case several contaminants are simultaneously present in the gas stream. Moreover, all the possible paths defined for the different plant sizes were compared each others on the basis of some defined operational parameters, among which total pressure drops, total energy losses, number of units and secondary materials consumption. On the basis of this analysis, dry gas cleaning methods proved preferable to the ones including water scrubber technology in al of the cases, especially because of the high water consumption provided by water scrubber units in ammonia adsorption process. This result is yet connected to the possibility to use activated carbon units for ammonia removal and Nahcolite adsorber for chloride acid. The very high efficiency of this latter material is also remarkable. Finally, as an estimation of the overall energy loss pertaining the gas cleaning process, the total enthalpy losses estimated for the three plant sizes were compared with the respective gas streams energy contents, these latter obtained on the basis of low heating value of gas only. This overall study on gas cleaning systems is thus proposed as an analytical tool by which different gas cleaning line configurations can be evaluated, according to the particular practical application they are adopted for and the size of cogeneration unit they are connected to.

Supramolecular approaches to organized luminescent nanostructures for sensing, labeling and imaging applications

The common thread of this thesis is the will of investigating properties and behavior of assemblies. Groups of objects display peculiar properties, which can be very far from the simple sum of respective components’ properties. This is truer, the smaller is inter-objects distance, i.e. the higher is their density, and the smaller is the container size. “Confinement” is in fact a key concept in many topics explored and here reported. It can be conceived as a spatial limitation, that yet gives origin to unexpected processes and phenomena based on inter-objects communication. Such phenomena eventually result in “non-linear properties”, responsible for the low predictability of large assemblies. Chapter 1 provides two insights on surface chemistry, namely (i) on a supramolecular assembly based on orthogonal forces, and (ii) on selective and sensitive fluorescent sensing in thin polymeric film. In chapters 2 to 4 confinement of molecules plays a major role. Most of the work focuses on FRET within core-shell nanoparticles, investigated both through a simulation model and through experiments. Exciting results of great applicative interest are drawn, such as a method of tuning emission wavelength at constant excitation, and a way of overcoming self-quenching processes by setting up a competitive deactivation channel. We envisage applications of these materials as labels for multiplexing analysis, and in all fields of fluorescence imaging, where brightness coupled with biocompatibility and water solubility is required. Adducts of nanoparticles and molecular photoswitches are investigated in the context of superresolution techniques for fluorescence microscopy. In chapter 5 a method is proposed to prepare a library of functionalized Pluronic F127, which gives access to a twofold “smart” nanomaterial, namely both (i)luminescent and (ii)surface-functionalized SCSSNPs. Focus shifts in chapter 6 to confinement effects in an upper size scale. Moving from nanometers to micrometers, we investigate the interplay between microparticles flowing in microchannels where a constriction affects at very long ranges structure and dynamics of the colloidal paste.

Synthese und Photochemie von Dendrimeren mit stilbenoiden Chromophoren

Dendrimere spielen als strukturtreue Nanopartikel eine herausragende Rolle. Ziel dieser Arbeit war, Dendrimere mit einer hohen Dichte an photoaktiven Chromophoren herzu-stellen und zu untersuchen. Dazu wurden die terminalen Aminogruppen von Poly(propylenimin)dendrimeren 1. und 2. Generation, Astramol DAB-Am-4R und DAB-Am-8R, mit Stilbenen und Styrylstilbenen als Chromophor verknüpft. Mittels Wittig-Horner- und Heck-Reaktion wurden (E)-Stilbene aufgebaut, die auf der einen Seite drei Propoxygruppen zur Verbesserung der Löslichkeit und auf der anderen Seite eine passende Funktionalität zur Verknüpfung mit dem dendritischen Core tragen. Als Verknüpfungsmethoden wurden die Verknüpfung als Amid (PSDA), Schiffsche Base (PSDS) und Harnstoff (PSDH) getestet. Die Schiffschen Basen wurden außerdem zur Erhöhung der Hydrolysestabilität zum sekundären Amin reduziert (PSDR und PQDR). Durch die Verknüpfung mit dem Core werden die stilbenoiden Chromophore sehr stark photoaktiviert. Das beruht auf einem Singulett-Energietransfer (Förster-Mechanismus) von Chromophor zu Chromophor. Dieser Prozeß konkurriert zu den Deaktivierungsprozessen, verlängert die mittlere S1-Lebensdauer und erhöht somit die Chancen der Photochemie. Der Styrylstilben-Chromophor hat darüber hinaus einen erheblichen Teil seiner UV-Absorbtion bereits im Tageslicht und photopolymerisiert daher bereits im Tageslicht. Vor allem bei den Dendrimeren 2. Generation stellte sich die Frage nach der vollständigen, d.h. achtfachen Umsetzung; das Core sollte als Knäuel vorliegen, die Arme zum Teil nach innen gefaltet und somit dem Reaktand nur bedingt zugänglich. Auch dort konnten unter optimierten Reaktionsbedingungen alle Aminogruppen umgesetzt werden. Die vollständige Umsetzung der Dendrimere wurde mittels NMR und massenspektroskopischen Methoden untersucht. Bei den Absorptionsspektren der Dendrimere 1. Generation ändert sich die Lage der Maxima je nach Art der Verknüpfung der Chromophore mit dem Core. Die Verlängerung des Chromophors um eine Styryleinheit bedingt eine beträchtliche Rotverschiebung. Die Lage der Emissionsmaxima differiert stärker als die Lage der Absorptionsmaxima. Den geringsten Stokes-Shift weist der Harnstoff auf, dann folgt das sekundäre Amin, dann die Schiffsche Base. Dies weist auf unterschiedlich relaxierte S1-Geometrien hin. Die Verbindungen PSDS1, PSDR1 und PSDH1 aus 3,4,5-Tripropoxystilbeneinheit und Astramol-Core 1. Generation DAB-Am-4 wurden in einer Konzentration von 10-5 mol/L belichtet. Der vollständige Photoabbau durch Belichtung in Chloroform mit einer Xenon-Lampe erfolgte ohne jeglichen Filter innerhalb von zehn Minuten (PSDH1), 20 Minuten (PSDR1) und einer Stunde (PSDS1). Allen drei Verbindungen gemeinsam ist das Entstehen eines intermediären neuen Maximums geringer Intensität, das um etwa 100 nm bathochrom verschoben ist. Das Harnstoffsystem weist außerdem ein weiteres intermediäres Maximum bei 614 nm auf. Diese Maxima können (laut früherer Untersuchungen) durch Oxidation entstandenen chinoiden Strukturen zugeordnet werden, deren Lebensdauer (im Sekundenbereich) zu kurz für eine NMR-Charakterisierung ist. PSDR1 wurde außerdem bei höheren Konzentrationen (10-4 und 10-3 mol/L) mit einer Quecksilberlampe mit Pyrex-Filter (lambda > 300 nm) belichtet. Dabei wird, wie erwartet, eine Verbreiterung der NMR-Signale beobachtet. Es bildet sich zunächst cis-Stilben. Außerdem läßt sich bei 4.3 ppm ein Signal beobachten, das von inter- oder intramolekular gebildeten Methinprotonen herrührt. Auch wenn laut MOPAC- und Kraftfeldrechnung die Doppelbindungen ungünstig für eine [pi2s + pi2s]-Cyclodimerisierung zueinander stehen, kann im photochemisch angeregten Zustand eine Geometrie vorherrschen, die die intramolekulare Kopf-Kopf-Cyclobutanbildung ermöglicht. Die massenspektrometrischen Untersuchungen der Belichtungsprodukte (FD, ESI, MALDI-TOF) zeigen als höchste Masse lediglich das Monomer. Allerdings kann dadurch nicht auf eine rein intramolekulare Reaktion geschlossen werden. Die fortschreitende statistische CC-Verknüpfung kann schnell zu vernetzten Nanopartikeln führen, die im Massenspektrometer nicht fliegen. Die NMR-Spektren der mit zunehmender Vernetzung immer schlechter löslich werdenden Teilchen belegen die Oligomerisierung.

Polysulfurated aromatic compounds: preparation and photophysical properties

The aim of this thesis was the synthesis and photophysical characterization of some new polysulfurated aromatic compounds: this class of molecules can offer intriguing properties, potentially useful for the construction of new materials for optoelectronic devices. Two main families of compounds have been synthesized: the first is represented by a series of small molecular asterisks, with peripheral aromatic units, showing luminescence in solid phase or in highly rigid conditions. All compounds with peripheral substituents display an AIE behavior (Aggregation Induced Emission) with radiative deactivation of the triplet states. Taking inspiration from these smaller asterisks, a larger molecule with the same geometry has been designed, decorated with terpyridyl moieties as the outermost units: this compound shows great affinity for the coordination of several transition metal ions, changing luminescence properties after the interaction with zinc ions. With the same intentions, a tetrasulfurated pyrene-core molecule with terpyridyl external units has been synthesized and isolated: this ligand exhibits good coordination capabilities towards transition metal ions, giving rise to luminescent nanoaggregates upon addition of zinc(II), characterized by DLS and AFM microscopy. In addition a NIR emission is recorded after coordination of neodymium(III), showing evidence of an intramolecular energy transfer process.

Catalytic processes for the transformation of ethanol into acetonitrile

This thesis deals with the transformation of ethanol into acetonitrile. Two approaches are investigated: (a) the ammoxidation of ethanol to acetonitrile and (b) the amination of ethanol to acetonitrile. The reaction of ethanol ammoxidation to acetonitrile has been studied using several catalytic systems, such as vanadyl pyrophosphate, supported vanadium oxide, multimetal molibdates and antimonates. The main conclusions are: (I) The surface acidity must be very low, because acidity catalyzes several undesired reactions, such as the formation of ethylene, and of heavy compounds as well. (II) Supported vanadium oxide is the catalyst showing the best catalytic behaviour, but the role of the support is of crucial importance. (III) Both metal molybdates and antimonates show interesting catalytic behaviour, but are poorly active, and probably require harder conditions than those used with the V oxide-based catalysts. (IV) One key point in the reaction network is the rate of reaction between acetaldehyde (the first intermediate) and ammonia, compared to the parallel rates of acetaldehyde transformation into by-products (CO, CO2, HCN, heavy compounds). Concerning the non-oxidative process, two possible strategies are investigated: (a) the ethanol ammonolysis to ethylamine coupled with ethylamine dehydrogenation, and (b) the direct non-reductive amination of ethanol to acetonitrile. Despite the good results obtained in each single step, the former reaction does not lead to good results in terms of yield to acetonitrile. The direct amination can be catalyzed with good acetonitrile yield over catalyst based on supported metal oxides. Strategies aimed at limiting catalyst deactivation have also been investigated.

New catalytic processes for the upgrading of furfural and 5-hydroxymethylfurfural to chemicals and fuels

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.

Neuroökonomie = (Neuroeconomics): Neuronale Mechanismen ökonomischer Entscheidungen

Ökonomische Entscheidungen sind ebenso wie alltägliche Entscheidungen von der Aktivität von Hirnregionen abhängig, die zur Kontrolle verschiedener Teilschritte der Entscheidung beitragen. Aktivierung und Desaktivierung dieser Hirnregionen können mit Hilfe moderner bildgebender Verfahren, wie z.B. der funktionellen Magnet-Resonanz-Tomographie (fMRI) dargestellt werden. Die vorliegende Publikation gibt einen Überblick über das interdisziplinäre wissenschaftliche Arbeitsgebiet der „Neuroökonomie“ – einem jungen Forschungsfeld der Neurowissenschaften. Dieser Überblick ist auf sieben Hauptaspekte ökonomischer und finanzieller Entscheidungen fokusiert: 1. In welcher Weise werden ökonomische Parameter wie Wert und Nutzen einer Belohnung, Gewinn oder Verlust, Risiko und Ungewissheit in spezifischen Hirnregionen abgebildet? 2. In welcher spezifischen Weise tragen anatomisch definierte Areale des Gehirns zum Entscheidungsprozess bei? 3. In welcher Weise sind die Entscheidungsprozesse durch Läsion entscheidungsrelevanter Areale des Gehirns gestört? 4. In welcher Weise sind Hirnregionen, die an den Prozessen der Entscheidung beteiligt sind, miteinander vernetzt, um durch Interaktion die Entscheidung herbeizuführen? 5. In welcher Weise ist der Entscheidungsprozess von Persönlichkeitseigenschaften, von genetischen Variationen neuronaler Funktionen und von physiologischer Regulation, z.B. durch Hormone bestimmt? 6. In welcher Weise hängt der Entscheidungsprozess vom sozialen und kulturellen Umfeld des Entscheiders ab? 7. Auf welche Weise werden bei unvollständiger Information über die Optionen der Entscheidung Heuristiken oder Intuitionen genutzt, und in welcher Weise sind Entscheidungen durch Biases beeinflussbar? Der zentrale Teil dieser Publikation gibt einen zusammenfassenden Überblick (review) über die Ergebnisse neuroökonomischer Studien, die die fMRI-Technik nutzen (bis Juni 2010).

Development of innovative catalysts for the hydrodechlorination to fluoroethers

In this work the hydrodechlorination of CF3OCFClCF2Cl to produce unsaturated CF3OCF=CF2 was studied over a series of supported metal catalysts. Currently this molecule is produced from the precursor CF3OCFClCF2Cl by dechlorination with zinc powder. An important cost on the economic and environmental balance is represents by the large amount of ZnCl2 produced and to be disposed of. A new approach, based on gas-phase hydrodechlorination over supported catalysts can lead to a new sustainable process. During the feasibility step of this project, substantially two kind of materials were studied: metals supported over activated carbon and Pd/Cu species supported over MCM-41 mesoporous silica. Observed catalytic performances were strongly dependent on the metal and support used. All carbon-supported Ru, Pd, and bimetallic catalysts are fairly active and yielded the target product CF3OCF=CF2, the higher selectivity being obtained with ruthenium- and palladium-based materials. Nevertheless, Ru-based catalysts showed poor stability and this deactivation may be attributed to the deposition of chlorinated organic species blocking the active sites. On the other hand, palladium-containing catalysts showed high stability. Ru/Pd and Pd/Cu bimetallic catalysts exhibited long-term selectivity and stability, highlighting the possibility for these materials to be employed in the CF3OCF=CF2 production process. During the second part of this thesis, a series of bimetallic meso-structured Pd/Cu MCM-41 catalysts were studies to overcome possible mass transfer limitations. The materials were obtained by different synthesis methods. The incorporation of Pd and Cu during MCM-41 synthesis, did not destroy the typical hexagonal array and ordered pore system of MCM-41. However, the calcination for the removal of the template provoked significant segregation of oxides. The impregnation leads to pore-occlusion and formation of Cu particles and large bimetallic PdCu species. Larger metal particles leads to lower CF3OCFClCF2Cl conversion, while the monometallic particles can decrease the selectivity to CF3OCF=CF2, fostering the dehalogenation to CF3OCH=CF2.

Deidrogenazione catalitica di idrocarburi per la produzione di H2 "on-board"

Lo studio della deidrogenazione catalitica di idrocarburi affronta uno dei problemi principali per l'applicazione delle fuel cells in aeromobili. La conversione di miscele di idrocarburi in H2 può essere eseguita in loco, evitando le difficoltà di stoccaggio dell'idrogeno: l'H2 prodotto è privo di CO e CO2 e può essere alimentato direttamente alle celle a combustibile per dare energia ai sistemi ausiliari, mentre i prodotti deidrogenati, mantenendo le loro originali caratteristiche possono essere riutilizzati come carburante. In questo un lavoro è stato effettuato uno studio approfondito sulla deidrogenazione parziale (PDH) di diverse miscele di idrocarburi e carburante avio JetA1 desolforato utilizzando Pt-Sn/Al2O3, con l'obiettivo di mettere in luce i principali parametri (condizioni di reazione e composizione di catalizzatore) coinvolti nel processo di deidrogenazione. Inoltre, la PDH di miscele idrocarburiche e di Jet-A1 ha evidenziato che il problema principale in questa reazione è la disattivazione del catalizzatore, a causa della formazione di residui carboniosi e dell’avvelenamento da zolfo. Il meccanismo di disattivazione da residui carboniosi è stato studiato a fondo, essendo uno dei principali fattori che influenzano la vita del catalizzatore e di conseguenza l'applicabilità processo. Alimentando molecole modello separatamente, è stato possibile discriminare le classi di composti che sono coinvolti principalmente nella produzione di H2 o nell’avvelenamento del catalizzatore. Una riduzione parziale della velocità di disattivazione è stata ottenuta modulando l'acidità del catalizzatore al fine di ottimizzare le condizioni di reazione. I catalizzatori Pt-Sn modificati hanno mostrato ottimi risultati in termini di attività, ma soffrono di una disattivazione rapida in presenza di zolfo. Così, la sfida finale di questa ricerca era sviluppare un sistema catalitico in grado di lavorare in condizioni reali con carburante ad alto tenore di zolfo, in questo campo sono stati studiati due nuove classi di materiali: Ni e Co fosfuri supportati su SiO2 e catalizzatori Pd-Pt/Al2O3.

Catalysts and processes for next-generation H2 production

The present study is focused on the development of new VIII group metal on CeO2 – ZrO2 (CZO) catalyst to be used in reforming reaction for syngas production. The catalyst are tested in the oxyreforming process, extensively studied by Barbera [44] in a new multistep process configuration, with intermediate H2 membrane separation, that can be carried out at lower temperature (750°C) with respect the reforming processes (900 – 1000°C). In spite of the milder temperatures, the oxy-reforming conditions (S/C = 0.7; O2/C = 0.21) remain critical regarding the deactivation problems mainly deriving from thermal sintering and carbon formation phenomena. The combination of the high thermal stability characterizing the ZrO2, with the CeO2 redox properties, allows the formation of stable mixed oxide system with high oxygen mobility. This feature can be exploited in order to contrast the carbon deposition on the active metal surface through the oxidation of the carbon by means of the mobile oxygen atoms available at the surface of the CZO support. Ce0.5Zr0.5O2 is the phase claimed to have the highest oxygen mobility but its formation is difficult through classical synthesis (co-precipitation), hence a water-in-oil microemulsion method is, widely studied and characterized. Two methods (IWI and bulk) for the insertion of the active metal (Rh, Ru, Ni) are followed and their effects, mainly related to the metal stability and dispersion on the support, are discussed, correlating the characterization with the catalytic activity. Different parameters (calcination and reduction temperatures) are tuned to obtain the best catalytic system both in terms of activity and stability. Interesting results are obtained with impregnated and bulk catalysts, the latter representing a new class of catalysts. The best catalysts are also tested in a low temperature (350 – 500°C) steam reforming process and preliminary tests with H2 membrane separation have been also carried out.

Atmospheric heterogeneous reactions of N 2 O 5 and NO 3 radicals with mineral dust particles

Die heterogenen Reaktionen von N2O5 bzw. NO3 auf mineralischen Staubpartikeln wurden untersucht, um deren Einfluss auf den Abbau atmosphärischer Stickoxide (NOx) sowie auf die chemische Veränderung der Staubpartikel während ihres Transportes durch die Atmosphäre besser verstehen zu können. Die experimentellen Studien wurden bei Atmosphärendruck, Raumtemperatur und unterschiedlichen relativen Luftfeuchten durchgeführt. Der Aufnahmekoeffizient γ(N2O5) von N2O5 auf dispergiertem Staub aus der Sahara wurde zu 0,020 ± 0,002 (1σ) bestimmt, unabhängig von der relativen Feuchte (0 - 67 %) sowie der N2O5-Konzentration (5x1011 - 3x1013 Moleküle cm-3).rnDie Analyse der Reaktionsprodukte in der Gasphase sowie auf der Partikeloberfläche führt zu der Annahme, dass N2O5 auf der Staubpartikeloberfläche zu Nitrat hydrolysiert wird. Es konnte kein Einfluss der relativen Feuchte auf den Aufnahmekoeffizienten ermittelt werden, was durch das vorhandene interlamellare Wasser, welches bis zu 10 % der Partikelmasse betragen kann, erklärbar ist. Der gemessene Wert des Aufnahmekoeffizienten ist unabhängig von der Eingangs-N2O5-Konzentration, was sich über die sehr große innere Oberfläche der Partikel erklären lässt. Dennoch ließ sich durch eine vorherige Konditionierung der Partikel mit gasförmigem HNO3, was eine Nitratanreicherung an der Oberfläche bewirkt, die Effizienz der N2O5-Aufnahme auf die Staubpartikel reduzieren. Zusätzliche Studien befassten sich mit der Bestimmung des Aufnahmekoeffizienten von N2O5 auf Illit-Partikeln und auf Teststaub aus Arizona. Bei einer relativen Luftfeuchte von 0 % wurden für γ(N2O5) Werte von 0,084 ± 0,019 (1σ) für Illit und von 0,010 ± 0,001 (1σ) für Arizona Teststaub ermittelt.rnUnter Anwendung einer neuartigen Messmethode, die auf der zeitgleichen Messung der Konzentrationsabnahme von NO3 und N2O5 relativ zueinander beruht, wurde das Verhältnis γ(NO3)/γ(N2O5) der Aufnahmekoeffizienten von NO3 und N2O5 auf Saharastaub zu 0,9 ± 0,4 (1σ) bestimmt. Dieser Wert war unabhängig von der relativen Feuchte, den NO3- und N2O5-Konzentrationen sowie der Reaktionszeit, obwohl eine Oberflächendeaktivierung für beide Spurenstoffe beobachtet wurde.

The synthesis of maleic anhydride: study of a new process and improvement of the industrial catalyst

Maleic anhydride is an important chemical intermediate mainly produced by the selective oxidation of n-butane, an industrial process catalyzed by vanadyl pyrophosphate-based materials, (VO)2P2O7. The first topic was investigated in collaboration with a company specialized in the production of organic anhydrides (Polynt SpA), with the aim of improving the performance of the process for the selective oxidation of n-butane to maleic anhydride, comparing the behavior of an industrial vanadyl pyrophosphate catalysts when utilized either in the industrial plant or in lab-scale reactor. The study was focused on how the catalyst characteristics and reactivity are affected by the reaction conditions and how the addition of a dopant can enhance the catalytic performance. Moreover, the ageing of the catalyst was studied, in order to correlate the deactivation process with the modifications occurring in the catalyst. The second topic was produced within the Seventh Framework (FP7) European Project “EuroBioRef”. The study was focused on a new route for the synthesis of maleic anhydride starting from an alternative reactant produced by fermentation of biomass:“bio-1-butanol”. In this field, the different possible catalytic configurations were investigated: the process was divided into two main reactions, the dehydration of 1-butanol to butenes and the selective oxidation of butenes to maleic anhydride. The features needed to catalyze the two steps were analyzed and different materials were proposed as catalysts, namely Keggin-type polyoxometalates, VOPO4∙2H2O and (VO)2P2O7. The reactivity of 1-butanol was tested under different conditions, in order to optimize the performance and understand the nature of the interaction between the alcohol and the catalyst surface. Then, the key intermediates in the mechanism of 1-butanol oxidehydration to MA were studied, with the aim of understanding the possible reaction mechanism. Lastly, the reactivity of the chemically sourced 1-butanol was compared with that one of different types of bio-butanols produced by biomass fermentation.

Die Rolle von Myosin 9b und LFA-1 in Dendritischen Zellen für die DC,T-Zellinteraktion und die Induktion einer Immunantwort

In dieser Arbeit wurde zum Einen, die Interaktionsphysiologie zwischen verschiedenen DC-Populationen und naiven sowie regulatorischen T-Zellen analysiert. Dabei wurde die Kontaktdauer und Häufigkeit bestimmt sowie die daraus folgende Aktivierung der T-Zellen in einer 3D-Kollagenmatrix. rnZum zweiten wurde die Rolle des Aktin-Motorproteins Myosin 9b, bei der Zellmigration sowie bei der DC-T-Zellinteraktion und der Ausbildung von Immunantworten untersucht. Myo9b KO DC weisen in vitro in einer Kollagenmatrix sowie in vivo einen gestörten Migrationsphänotyp auf. Auch die Interaktion mit T-Zellen ist verändert und sie induzieren eine reduzierte T-Zellaktivierung in einer 3D-Umgebung sowie eine geringere Immunreaktion in vivo. Die Zugabe pharmakologischer Inhibitoren der Rho-Signalkaskade konnte die Migration und das T-Zellstimulierungspotential wiederherstellen. rnZum Dritten wurde analysiert, welche Bedeutung die konstitutive Aktivierung des Adhäsionsmoleküls LFA-1 auf DC (LFA-1 d/d) hat. LFA-1 d/d DC zeigten verlängerte Interaktionszeiten mit T-Zellen, gefolgt von einer reduzierten T-Zellproliferation in einer Kollagenmatrix. Durch die Inhibition von aktivem LFA-1 auf den DC mittels blockierender Antikörper konnte eine Normalisierung der Interaktionsparameter und T-Zellproliferation auf Wildtyp-Niveau wiederhergestellt werden. Durch ein Ausschalten von CYTIP in WT DC und dem damit einhergehenden Verlust der Deaktivierbarkeit von LFA-1 über Cytohesin wurde ebenfalls eine erhöhte Interaktionszeit mit T-Zellen und eine reduzierte T-Zellproliferation beobachtet.rn

Induktion von Pro-Autophagie-Signalen durch einen extra- oder intrazellulären Alpha-Toxin-Angriff

Autophagie ist ein konservierter, kataboler Mechanismus in allen eukaryoten Zellen. Unter anderem wird ihm eine wichtige Rolle als zellautonomer Abwehrmechanismus gegen Mikroorganismen zugeschrieben; von manchen Infektionserregern wird er jedoch unterlaufen oder sogar genutzt. Der stärkste Auslöser der Autophagie ist ein Mangel an Nährstoffen, insbesondere Aminosäuren. Über die Deaktivierung der Kinase mTORC1 und die Phosphorylierung des eukaryoten Translationsinitiationsfaktors eIF2α hemmt die Nährstoffknappheit die Proteinbiosynthese und aktiviert gleichzeitig Autophagie. Wie Mikroorganismen, insbesondere Bakterien, Autophagie auslösen oder manipulieren, ist derzeit Gegenstand intensiver Forschung. Modifikationen an Mikroben oder Phagosomen und Adapterproteine, die diese Veränderungen und Komponenten des Autophagieapparates erkennen, scheinen jedenfalls bei der selektiven Erkennung durch die Autophagie-Maschinerie wichtig zu sein. rnIn der vorliegenden Dissertationsarbeit wird die Rolle des membranporenbildenden α-Toxins von Staphylococcus aureus für die Induktion von Autophagie beleuchtet. Zum einen erwies sich die Akkumulation von (EGFP)-LC3(II), einem Marker der Autophagosomen, um intrazelluläre S. aureus als abhängig von α-Toxin. Zweitens, genügt extrazellulär appliziertes α-Toxin um (EGFP)-LC3(II)-positive Endosomen zu induzieren. Während der Angriff aus dem extrazellulären Raum jedoch binnen kurzer Zeit eine fokale Kumulation von phosphoryliertem eIF2α an der Plasmamembran induziert, die an der Internalisierung des Toxins beteiligt ist, findet sich am phagosomalen Kompartiment keine Toxin-abhängige Anhäufung von p-eIF2α oder proximalen Autophagieregulatoren. Dies impliziert, dass Toxin-Angriff auf die Plasmamembran, nicht aber auf das Phagosom, zu einer Reaktion führt, wie sie bei massivem Nährstoffmangel zu beobachten ist. Obwohl keine α-Toxin-abhängige Kumulation von p-eIF2α bei einem Angriff aus dem Phagosom erfolgt, findet sich um α-Toxin-produzierende Bakterien eine massive Kumulation von LC3 und Adapterprotein p62/Sequestosome1. Dies deutet daraufhin, dass der Ort des Angriffs - Plasmamembran oder Phagosom – für den Autophagie-induzierenden Mechanismus wichtig sein könnte. Der unterschiedliche Effekt auf die zellulären Ionenkonzentrationen, den ein Angriff auf die Plasmamembran oder auf ein Phagosom auslösen würde, bietet hierfür eine mögliche Erklärung. Die Aktivierung der Autophagie über Adapterproteine könnte dann als back-up Mechanismus fungieren, der auch dann greift, wenn eine Invasion ohne Schädigung der Plasmamembran erfolgt. Ein cross-talk der beiden Induktionswege ist angesichts der Bedeutung von p62 für die selektive und die Hunger-assoziierte Autophagie gut möglich; sezerniertes Toxin könnte durch die Aktivierung der basalen Autophagie Adapter-basierte Mechanismen verstärken.

Bio-inspired polymer-supported nitrido molybdenum(VI) complexes for ammonia synthesis − reactivity towards protons and electrons : EPR investigations on paramagnetic molybdenum(V) and copper(II) complexes

Die biologische Stickstofffixierung durch Molybdän-haltige Nitrogenasen sowie die Erforschung des zugrundeliegenden komplexen Mechanismus (N2-Aktivierung an Metall-Zentren, 6-fache Protonierung und Reduktion, N–N Bindungsspaltung unter Bildung von Ammoniak) ist von erheblichem Interesse. Insbesondere Molybdän-Komplexe wurden bereits erfolgreich als Modellverbindungen für die Untersuchung elementarer Einzelschritte der N2-Aktivierung eingesetzt. Durch die Verwendung von Triamidoamin-Liganden ist es Schrock et al. sogar gelungen mehrere Katalysezyklen zu durchlaufen und einen Mechanismus zu formulieren. Trotz der sterisch anspruchsvollen Substituenten in den Schrock-Komplexen ist die Umsatzrate dieses homogenen Katalysators, aufgrund Komplex-Deaktivierung infolge intermolekularer Reaktionen wie Dimerisierung und Disproportionierung, limitiert. In der vorliegenden Arbeit wurden einige dieser Herausforderungen angegangen und die aktiven Spezies auf einer Festphase immobilisiert, um intermolekulare Reaktionen durch räumliche Isolierung der Komplexe zu unterdrücken.rnEin Polymer-verankertes Analogon des Schrock Nitrido-Molybdän(VI)-Komplexes wurde auf einem neuen Reaktionsweg synthetisiert. Dieser beinhaltet nur einen einzigen Reaktionsschritt, um die funktionelle Gruppe „MoN“ einzuführen. Protonierung des immobilisierten Nitrido-Molybdän(VI)-Komplexes LMoVIN (L = Polymer-verankerter Triamidoamin-Ligand) mit 2,6-Lutidinium liefert den entsprechenden Imido-Molybdän(VI)-Komplex. Durch anschließende Ein-Elektronen-Reduktion mit Cobaltocen wird der Polymer-angebundene Imido-Molybdän(V)-Komplex erhalten, bewiesen durch EPR-Spektroskopie (g1,2,3 = 1.989, 1.929, 1.902). Durch die Immobilisierung und die effektive räumliche Separation der Reaktionszentren auf der Festphase werden bimolekulare Nebenreaktionen, die oft in homogenen Systemen auftreten, unterdrückt. Dies ermöglicht zum ersten Mal die Darstellung des Imido-Molybdän(V)-Intermediates des Schrock-Zyklus.rnEPR-Spektren des als Spin-Label eingeführten immobilisierten Nitrato-Kupfer(II)-Komplexes wurden unter verschiedenen Bedingungen (Lösungsmittel, Temperatur) aufgenommen, wobei sich eine starke Abhängigkeit zwischen der Zugänglichkeit und Reaktivität der immobilisierten Reaktionszentren und der Art des Lösungsmittels zeigte. Somit wurde die Reaktivität von LMoVIN gegenüber Protonen und Elektronen, welches zur Bildung von NH3 führt, unter Verwendung verschiedener Lösungsmittel untersucht und optimiert. Innerhalb des kugelförmigen Polymers verläuft die Protonierung und Reduktion von LMoVIN stufenweise. Aktive Zentren, die sich an der „äußeren Schale“ des Polymers befinden, sind gut zugänglich und reagieren schnell nach H+/e− Zugabe. Aktive Zentren im „Inneren des Polymers“ hingegen sind schlechter zugänglich und zeigen langsame diffusions-kontrollierte Reaktionen, wobei drei H+/e− Schritte gefolgt von einer Ligandenaustausch-Reaktion erforderlich sind, um NH3 freizusetzen: LMoVIN  LMoVNH  LMoIVNH2  LMoIIINH3 und anschließender Ligandenaustausch führt zur Freisetzung von NH3.rnIn einem weiteren Projekt wurde der Bis(ddpd)-Kupfer(II)-Komplex EPR-spektroskopisch in Hinblick auf Jahn−Teller-Verzerrung und -Dynamik untersucht. Dabei wurden die EPR-Spektren bei variabler Temperatur (70−293 K) aufgenommen. Im Festkörperspektrum bei T < 100 K erscheint der Kupfer(II)-Komplex als gestreckter Oktaeder, wohingegen das EPR-Spektrum bei höheren Temperaturen g-Werte aufzeigt, die einer pseudo-gestauchten oktaedrischen Kupfer(II)-Spezies zuzuordnen sind. Diese Tatsache wird einem intramolekularen dynamischen Jahn−Teller Phänomen zugeschrieben, welcher bei 100 K eingefroren wird.