L’objectif de cette étude est de préparer des catalyseurs bimétalliques Ni-X/SiO2, de les caractériser, et de comparer leur activité en hydrogénation du styrène en éthylbenzène,ainsi que leur sélectivité en hydrogénation de la double liaison oléfinique du styrène, par rapport à l’hydrogénation du noyau benzénique. L’élément X est greffé de manière contrôlée sur le nickel, et est choisi selon son électronégativité, soit inférieure (Zr), soit égale (Sn), soit supérieure (Au) à celle du nickel, dans le but d’étudier les effets géométriques et/ou électroniques qu'il pourrait induire. Parmi les échantillons préparés, le catalyseur Ni-Au/SiO2s’est révélé presque aussi actif que le catalyseur non dopé et nettement plus sélectif dans l’hydrogénation du styrène en éthylbenzène. / The aim of the present study is to prepare silica-supported Ni-X bimetallic catalysts, tocharacterize them, and to compare their catalytic activity in the hydrogenation of styrene, as well as their selectivity in the hydrogenation of the styrene’s olefinic double bond instead of the hydrogenation of the aromatic ring. The element X is grafted in a controlled way on the supported nickel particles, and is chosen according to its electronegativity, which is eitherlower (Zr), or equivalent (Sn), or higher (Au) than the electronegativity of Ni, in order to study the geometrical and/or electronic effects due to the doping of Nickel. Among the prepared samples, the Ni-Au/SiO2 catalyst has exhibited high activity and high selectivity in the hydrogenation of styrene into ethylbenzene, which makes the doping of Ni by Au apromising alternative for PyGas selective hydrogenation catalysts.

Foram realizados experimentos de homopolimerização de estireno e copolimerização de estireno-divinilbenzeno em solução e suspensão aquosa pelos métodos convencional (FRP) e mediado por nitróxido (NMRP). Objetivou-se atingir um maior grau de entendimento sobre estes sistemas em relação ao que se tem na literatura. Para isto, três modelos matemáticos foram avaliados através de validação com os dados obtidos nos experimentos. Os experimentos foram conduzidos em reator de batelada isotérmico. As principais variáveis exploradas neste trabalho foram: temperatura de reação, concentração inicial de divinilbenzeno, diluição inicial da mistura de monômeros e técnicas de polimerização (FRP e NMRP). Os modelos matemáticos foram intitulados: Modelo A, Modelo B e Modelo C. O Modelo A consiste de um balanço de espécies não poliméricas e grupos poliméricos. A determinação das massas moleculares médias e da fração de gel foi feita através de balanços populacionais em termos de função geradora em conjunto com o método das características. Os modelos B e C consistiram de balanços de massa para espécies não poliméricas e método dos momentos para radicais ativos, radicais dormentes e polímero morto. A obtenção das massas moleculares médias e da fração de gel foi feita através do método do fracionamento numérico. Nestes dois modelos, foram consideradas as reações de ciclização através do método dos caminhos. Este método consiste num balanço de segmentos de cadeia que conectam grupos poliméricos. O número máximo de unidades monoméricas, considerado para estes segmentos foi 100 e o valor da constante cinética de ciclização do menor segmento ciclizável (3 unidades monoméricas) foi 450 s-1 para a temperatura de 90°C. O Modelo C leva em conta a redução da reatividade das ligações cruzadas em função do tamanho médio das cadeias em cada geração. Os resultados mostraram que, quando comparado com a FRP, a polimerização NMRP permite somente um controle limitado sobre o processo de reticulação, produzindo distribuições largas de tamanhos de cadeia. Micro e nanoestruturas foram identificadas em produtos obtidos por FRP e NMRP lineares e não lineares. Estas estruturas parecem ser consequência do processo de síntese (ex.: operação em temperatura de reação acima da temperatura de transição vítrea) e do tratamento dos produtos. Massa molecular média mássica e fração de gel foram afetadas consideravelmente pelas reações de ciclização em copolimerizações FRP, porém apresentaram pouca sensibilidade a estas reações em copolimerizações NMRP. A inclusão do mecanismo de ciclização, por si só (no Modelo B), não foi suficiente para produzir bons ajustes modelo/experimentos em termos de massa molecular média mássica (Mw) e fração de gel (Wg). No entanto, o Modelo C é capaz de fornecer boas previsões de Mw e Wg simultaneamente para os experimentos realizados a 90°C. O presente estudo mostrou uma análise na qual os modelos podem se complementar e fornecer subsídios para o desenvolvimento de um modelo unificado. / Homopolymerizations of styrene and copolymerizations of styrene-divinylbenzene were carried out in solution and aqueous suspension through conventional (FRP) and nitroxide-mediated (NMRP) techniques. The aim of the work was to reach a higher level of understanding in comparison to what is found in literature. In order to reach this goal, three mathematical models were assessed through validation using experimental data. The experiments were conducted in isothermal batch reactor. The main variables explored in this work were: reaction temperature, divinylbenzene initial concentration, initial dilution of monomers and polymerization techniques (FRP and NMRP). The mathematical models were named: Model A, Model B and Model C. The Model A consists of a balance of non-polymeric species and polymer groups. The average molecular weights and gel fraction were calculated through population balances in terms of generation function together with the method of characteristics. The models B and C were built using mass balance for non-polymeric species and the method of moments for active radicals, dormant radicals and dead polymer. The average molecular weights and gel fraction were calculated through the numerical fractionation technique. In these two models, cyclization reactions were considered through the method of paths. This method consists of a balance of chain segments which connect polymer groups. The maximum number of monomeric units considered for these segments was 100 and the value of the kinetic constant of cyclization for the smaller cyclizable path (3 monomeric units) was 450 s-1 at 90°C. The Model C takes into account the reduction of reactivity of the crosslink reactions in function of the average size of the chains in each generation. The results showed that, when compared with FRP, NMRP allows only a limited control over the crosslinking process, producing broad chain length distributions. Micro and nanostructures were identified in products obtained by linear and non-linear FRP and NMRP. These structures seem to be consequence of the synthesis process (e.g.: operation in reaction temperatures above the glass transition temperature) and of the products treatment. Weight average molecular weight and gel fraction were affected considerably by the cyclization reactions in FRP, however they presented few sensibility to these reactions in NMRP. The inclusion of the mechanism of cyclization, itself (in Model B), was not enough to obtain good model/experiments fittings in terms of weight average molecular weight (Mw) and weight fraction of gel (Wg). Although, the Model C is capable of providing good predictions of Mw and Wg simultaneously for the experiments carried out at 90°C. The present study showed an analysis in which the models can complement each other, providing subsidies for the development of a unified model.

Nas últimas décadas, o interesse nas propriedades específcas dos organolantanídeos está aumentando muito, principalmente no uso como catalisadores em diversas reações orgânicas. Com o objetivo de contribuir para a aplicação de compostos organolantanídeos como catalisadores nessas reações, avaliou-se o desempenho de sistemas catalíticos a base de compostos organolantanídeos do tipo LnBrCp2(THF)2 e LnBrCp*2THF (Cp = ciclopentadienil , Cp* = pentametilciclopentadienil Ln = Pr e Yb) utilizando metilaluminoxano (MAO) como cocatalisador em reações de polimerização de etileno, propileno, metil metacrilato e estireno. Os compostos foram sintetizados pela reação entre os brometos de lantanídeos anidros e NaCp ou NaCp* em THF, na proporção molar 1:2,2 (Ln:Cp,Cp*) e caracterizados pela %Ln e %Br, termogravimetria, espectroscopia vibracional no infravermelho e RMN de 1H. Os sistemas estudados não foram ativos nas reações de polimerização de etileno, propileno ou metil metacrilato, mas produziram poliestireno com rendimento de até 8,0 % em 1,5 h na presença de tolueno e até 26,0 % em 1,5 h com PrBrCp*2THF/MAO a 90º C na ausência de solvente. Os polímeros formados são atáticos, indicando que a polimerização não é estereoespecífica, e possuem baixas massas molares. / In the last decades, the specific properties of organolanthanide compounds have attracted attention, specially in applications as catalysts in organic reactions. In an attempt to contribute to the application of these compounds in olefin polymerization reactions, we studied the catalytic systems based on LnBrCp2(THF)2 and LnBrCp*2THF (Cp = cyclopentadienyl , Cp* = pentamethylciclopentadienyl, Ln = Pr, Yb) and methylaluminoxane (MAO) as cocatalyst in polymerization of ethylene, propylene, methyl methacrylate and styrene. The organolanthanide compounds were obtained by the reaction of anydrous lanthanide tribromides and NaCp or NaCp* in THF, in the molar proportion of 1:2,2 (Ln:Cp, Cp*) and were characterized by %Ln, %Br, thermogravimetry, vibrational spectroscopy in the infrared region and 1H NMR. The catalytic systems were not active in ethylene, propylene, methyl methacrylate polymerizations, but were able to form polystyrene with yields up to 8.0 % in 1.5 h in toluene and 26% in 1.5 h in absence of solvent, using PrBrCp*2THF/MAO at 90º C. The polymers obtained are atactic, indicating no stereospecificity of the catalytic system, and have low molar masses.

Foram realizados experimentos de homopolimerização de estireno e copolimerização de estireno-divinilbenzeno em solução e suspensão aquosa pelos métodos convencional (FRP) e mediado por nitróxido (NMRP). Objetivou-se atingir um maior grau de entendimento sobre estes sistemas em relação ao que se tem na literatura. Para isto, três modelos matemáticos foram avaliados através de validação com os dados obtidos nos experimentos. Os experimentos foram conduzidos em reator de batelada isotérmico. As principais variáveis exploradas neste trabalho foram: temperatura de reação, concentração inicial de divinilbenzeno, diluição inicial da mistura de monômeros e técnicas de polimerização (FRP e NMRP). Os modelos matemáticos foram intitulados: Modelo A, Modelo B e Modelo C. O Modelo A consiste de um balanço de espécies não poliméricas e grupos poliméricos. A determinação das massas moleculares médias e da fração de gel foi feita através de balanços populacionais em termos de função geradora em conjunto com o método das características. Os modelos B e C consistiram de balanços de massa para espécies não poliméricas e método dos momentos para radicais ativos, radicais dormentes e polímero morto. A obtenção das massas moleculares médias e da fração de gel foi feita através do método do fracionamento numérico. Nestes dois modelos, foram consideradas as reações de ciclização através do método dos caminhos. Este método consiste num balanço de segmentos de cadeia que conectam grupos poliméricos. O número máximo de unidades monoméricas, considerado para estes segmentos foi 100 e o valor da constante cinética de ciclização do menor segmento ciclizável (3 unidades monoméricas) foi 450 s-1 para a temperatura de 90°C. O Modelo C leva em conta a redução da reatividade das ligações cruzadas em função do tamanho médio das cadeias em cada geração. Os resultados mostraram que, quando comparado com a FRP, a polimerização NMRP permite somente um controle limitado sobre o processo de reticulação, produzindo distribuições largas de tamanhos de cadeia. Micro e nanoestruturas foram identificadas em produtos obtidos por FRP e NMRP lineares e não lineares. Estas estruturas parecem ser consequência do processo de síntese (ex.: operação em temperatura de reação acima da temperatura de transição vítrea) e do tratamento dos produtos. Massa molecular média mássica e fração de gel foram afetadas consideravelmente pelas reações de ciclização em copolimerizações FRP, porém apresentaram pouca sensibilidade a estas reações em copolimerizações NMRP. A inclusão do mecanismo de ciclização, por si só (no Modelo B), não foi suficiente para produzir bons ajustes modelo/experimentos em termos de massa molecular média mássica (Mw) e fração de gel (Wg). No entanto, o Modelo C é capaz de fornecer boas previsões de Mw e Wg simultaneamente para os experimentos realizados a 90°C. O presente estudo mostrou uma análise na qual os modelos podem se complementar e fornecer subsídios para o desenvolvimento de um modelo unificado. / Homopolymerizations of styrene and copolymerizations of styrene-divinylbenzene were carried out in solution and aqueous suspension through conventional (FRP) and nitroxide-mediated (NMRP) techniques. The aim of the work was to reach a higher level of understanding in comparison to what is found in literature. In order to reach this goal, three mathematical models were assessed through validation using experimental data. The experiments were conducted in isothermal batch reactor. The main variables explored in this work were: reaction temperature, divinylbenzene initial concentration, initial dilution of monomers and polymerization techniques (FRP and NMRP). The mathematical models were named: Model A, Model B and Model C. The Model A consists of a balance of non-polymeric species and polymer groups. The average molecular weights and gel fraction were calculated through population balances in terms of generation function together with the method of characteristics. The models B and C were built using mass balance for non-polymeric species and the method of moments for active radicals, dormant radicals and dead polymer. The average molecular weights and gel fraction were calculated through the numerical fractionation technique. In these two models, cyclization reactions were considered through the method of paths. This method consists of a balance of chain segments which connect polymer groups. The maximum number of monomeric units considered for these segments was 100 and the value of the kinetic constant of cyclization for the smaller cyclizable path (3 monomeric units) was 450 s-1 at 90°C. The Model C takes into account the reduction of reactivity of the crosslink reactions in function of the average size of the chains in each generation. The results showed that, when compared with FRP, NMRP allows only a limited control over the crosslinking process, producing broad chain length distributions. Micro and nanostructures were identified in products obtained by linear and non-linear FRP and NMRP. These structures seem to be consequence of the synthesis process (e.g.: operation in reaction temperatures above the glass transition temperature) and of the products treatment. Weight average molecular weight and gel fraction were affected considerably by the cyclization reactions in FRP, however they presented few sensibility to these reactions in NMRP. The inclusion of the mechanism of cyclization, itself (in Model B), was not enough to obtain good model/experiments fittings in terms of weight average molecular weight (Mw) and weight fraction of gel (Wg). Although, the Model C is capable of providing good predictions of Mw and Wg simultaneously for the experiments carried out at 90°C. The present study showed an analysis in which the models can complement each other, providing subsidies for the development of a unified model.

Este trabalho trata do estudo teórico atomístico das conformações da molécula de estireno sobre a superfície de Si(100)(2xl):H. Estudamos a molécula fisissorvida e quimissorvida sobre esta superfície. Os cálculos foram realizados através de Dinâmica Molecular Clássica. Nós reparametrizamos o Universal Force Field (UFF) com base em cálculos ab initio para sistemas modelo, e comparação a dados experimentais. Nossos resultados indicam que no processo de fississorção a região de vale da superfície é preferencial, e ocorre formação de agregados de moléculas antes do contato com a superfície. Quando passamos à análise da quimissorção de uma molécula, a região de vale permanece sendo o sítio preferencial para a posição do grupo vinil. Para as conformações de linhas de estireno, a estrutura mais estável tem todas as moléculas dispostas sobre a região de vale (ordenamento tipo \"pilha-1r\"); identificamos também outra estrutura, quase degenerada em energia, na qual o grupo vinileno se dispõe em conformação tipo \"espinha de peixe\", alternando entre a região de vale e sobre o dímero. / In this work we present a theoretical study of ,the conformation of styrene molecules on the Si(100)(2xl):H surface. We studied the conformations for styrene molecules physisorbed and chemisorbed on this surface. The study was conducted by Classical Molecular Dynamics. We performed a re-parametrization of the Universal Force Field (UFF), based on ab initio calculations for model structures, and comparison to experimental data. Our results show that for the physisorbed situations, the styrene molecules preferentially interact with the surface valley. We also identified that the molecules aggregate in clusters before reaching the surface. The valley is again the region of lowest energy for the vinylene position, for chemisorption of a single styrene molecule on the monohydride surface. For systems where we have a styrene layer chemisorbed on the dimer row, the most stable structure has ali the molecules arranged on the valley region o f the surface ( 1r -stack); we find another structure, almost degenerate in energy, in which molecules arrange in a herringbone- like configuration, with the vinylene group alternating between the valley and dimer regions.

Nas últimas décadas, o interesse nas propriedades específcas dos organolantanídeos está aumentando muito, principalmente no uso como catalisadores em diversas reações orgânicas. Com o objetivo de contribuir para a aplicação de compostos organolantanídeos como catalisadores nessas reações, avaliou-se o desempenho de sistemas catalíticos a base de compostos organolantanídeos do tipo LnBrCp2(THF)2 e LnBrCp*2THF (Cp = ciclopentadienil , Cp* = pentametilciclopentadienil Ln = Pr e Yb) utilizando metilaluminoxano (MAO) como cocatalisador em reações de polimerização de etileno, propileno, metil metacrilato e estireno. Os compostos foram sintetizados pela reação entre os brometos de lantanídeos anidros e NaCp ou NaCp* em THF, na proporção molar 1:2,2 (Ln:Cp,Cp*) e caracterizados pela %Ln e %Br, termogravimetria, espectroscopia vibracional no infravermelho e RMN de 1H. Os sistemas estudados não foram ativos nas reações de polimerização de etileno, propileno ou metil metacrilato, mas produziram poliestireno com rendimento de até 8,0 % em 1,5 h na presença de tolueno e até 26,0 % em 1,5 h com PrBrCp*2THF/MAO a 90º C na ausência de solvente. Os polímeros formados são atáticos, indicando que a polimerização não é estereoespecífica, e possuem baixas massas molares. / In the last decades, the specific properties of organolanthanide compounds have attracted attention, specially in applications as catalysts in organic reactions. In an attempt to contribute to the application of these compounds in olefin polymerization reactions, we studied the catalytic systems based on LnBrCp2(THF)2 and LnBrCp*2THF (Cp = cyclopentadienyl , Cp* = pentamethylciclopentadienyl, Ln = Pr, Yb) and methylaluminoxane (MAO) as cocatalyst in polymerization of ethylene, propylene, methyl methacrylate and styrene. The organolanthanide compounds were obtained by the reaction of anydrous lanthanide tribromides and NaCp or NaCp* in THF, in the molar proportion of 1:2,2 (Ln:Cp, Cp*) and were characterized by %Ln, %Br, thermogravimetry, vibrational spectroscopy in the infrared region and 1H NMR. The catalytic systems were not active in ethylene, propylene, methyl methacrylate polymerizations, but were able to form polystyrene with yields up to 8.0 % in 1.5 h in toluene and 26% in 1.5 h in absence of solvent, using PrBrCp*2THF/MAO at 90º C. The polymers obtained are atactic, indicating no stereospecificity of the catalytic system, and have low molar masses.

Doctor of Philosophy / The kinetics of electrosterically stabilized emulsion systems was studied. The aim of this was to understand the impact that steric and electrosteric stabilizers have on the kinetics of particle growth and particle formation in the area of emulsion polymerization. The well-established mechanisms that govern these processes for emulsions stabilized by conventional low molecular weight surfactants were used as a reference point for comparative purposes. Model latexes were synthesized that comprised of a poly(styrene) core stabilized by a corona of poly(acrylic acid). The advent of successful controlled radical polymerization techniques in heterogeneous media (via RAFT polymerization) allowed for latexes to be synthesized under molecular weight control. For the first time, the degree of polymerization of the stabilizing block on the particle surface was able to be controlled and verified experimentally using mass spectrometry techniques. Three latexes were made with different average degrees of polymerization of the stabilizing block; five, ten and twenty monomer units respectively. A methodology was developed to remove the RAFT functionality from the polymer chains present in the emulsion while retaining the desired particle morphology. Oxidation with tertbutylhydroperoxide (TBHP) was proven to be successful at eliminating the living character provided by the thiocarbonyl end-group. Extensive dialysis and cleaning of the latex was performed to ensure no residual TBHP or reaction by-products remained. Latexes with poly(styrene) cores were chosen for this work as poly(n-butyl acrylate) latexes were shown to be influenced by chain transfer to polymer, providing an additional kinetic complication. The three electrosterically stabilized emulsions were used as seed latexes in carefully designed kinetic experiments to measure the rate of polymerization as a function of time. Two independent techniques (chemically initiated dilatometry and γ-relaxation dilatometry) were used to measure the rate coefficients of radical entry (ρ) and exit (k) in these systems – the two parameters that essentially govern the rate of particle growth. The latexes were chosen such that they satisfied ‘zero-one’ conditions (i.e. that any given latex particle contains at most one growing radical at any given time) in order to simplify data analysis. Three different chemical initiators were used, each yielding a radical with a different electric charge. Results from γ-relaxation experiments demonstrated that the three electrosterically stabilized latexes gave very long relaxation times when removed from the radiation source, ultimately yielding very small k values. These values were up to a factor of 10 smaller than that predicted by the ‘transfer-diffusion’ model for exit for particles of that size. This reduction was attributed to a ‘restricted diffusion’ effect, where the exiting monomeric radical has to diffuse through a dense layer of polymer on the particle surface, where its mobility will be restricted. Modification of the Smoluchowski equation for diffusion-controlled adsorption/desorption to account for this postulate led to the development of a model that gave excellent semi-quantitative agreement with experiment. Chemically initiated dilatometric experiments (using three different types of initiator) gave the unusual result of very low reaction rates and low steady-state values of 'nbar', the average number of radicals per particle. Using the standard kinetic equations for styrene-based systems (where it is assumed that an exited monomeric radical undergoes re-entry), this led to the calculation of impossibly small values of the entry rate coefficient ρ (far below any background or ‘thermal’polymerization rate). However upon removing the assumption of re-entry and assuming that exited radicals undergo termination, the obtained values of ρ were in almost perfect agreement with the values predicted from the ‘control by aqueous phase growth’ entry mechanism. This unexpected result was attributed to chemical reaction with the poly(acrylic acid) stabilizers through chain transfer to polymer (via hydrogen-atom abstraction). This postulate was verified by separate experiments that demonstrated that poly(acrylic acid) could act as a reasonably efficient chain transfer agent for styrene polymerization. The addition of poly(acrylic acid) to the aqueous phase of a conventionally stabilized emulsion also led to the rate reduction seen previously. NMR experiments demonstrated the existence of poly(acrylic acid-graft-styrene), which could only be formed through termination of a poly(styrene) chain with a poly(acrylic acid) chain bearing a mid-chain radical (as the product of a chain transfer reaction). These additional terms of transfer and termination were included in the governing kinetic equations of emulsion systems (the Smith-Ewart equations) to develop a model to account for the behaviour of electrosterically stabilized latexes. The ultimate fate of an exiting radical was now shown to be a competition between fates; successful desorption into the aqueous phase, or chemical reaction (through transfer or termination) within the hairy layer. These additional terms were shown to significantly reduce the theoretical value of nbar, and were in excellent agreement with experiment. For small electrosterically stabilized particles with a densely packed ‘hairy layer,’ it was seen that transfer/termination is the dominant loss mechanism as opposed to desorption. The developed model showed that as the particle size was increased, the dominant loss mechanism once again became successful desorption into the aqueous phase. The model was shown to give excellent agreement with experimental data from ‘uncontrolled’ emulsion systems. To explain the highly unusual secondary nucleation behaviour seen in systems such as these, it was postulated that beta-scission of a poly(acrylic acid) chain bearing a mid-chain radical is an important mechanistic step in the nucleation mechanisms of these systems. Modelling (both steady-state and time-dependent) gave good agreement with experiment with a minimal number of adjustable parameters. Theory (and supporting experimental evidence) demonstrated that this nucleation mechanism is only significant at high particle numbers; under other conditions the well-known ‘homogeneous nucleation’ mechanism is once again dominant.

The widespread usage of products containing volatile organic compounds (VOC) has lead to a general human exposure to these chemicals in work places or homes being suspected to contribute to the growing incidence of environmental diseases. Since the causal molecular mechanisms for the development of these disorders are not completely understood, the overall objective of this thesis was to investigate VOC-mediated molecular effects on human lung cells in vitro at VOC concentrations comparable to exposure scenarios below current occupational limits. Although differential expression of single proteins in response to VOCs has been reported, effects on complex protein networks (proteome) have not been investigated. However, this information is indispensable when trying to ascertain a mechanism for VOC action on the cellular level and establishing preventive strategies. For this study, the alveolar epithelial cell line A549 has been used. This cell line, cultured in a two-phase (air/liquid) model allows the most direct exposure and had been successfully applied for the analysis of inflammatory effects in response to VOCs. Mass spectrometric identification of 266 protein spots provided the first proteomic map of A549 cell line to this extent that may foster future work with this frequently used cellular model. The distribution of three typical air contaminants, monochlorobenzene (CB), styrene and 1,2 dichlorobenzene (1,2-DCB), between gas and liquid phase of the exposure model has been analyzed by gas chromatography. The obtained VOC partitioning was in agreement with available literature data. Subsequently the adapted in vitro system has been successfully employed to characterize the effects of the aromatic compound styrene on the proteome of A549 cells (Chapter 4). Initially, the cell toxicity has been assessed in order to ensure that most of the concentrations used in the following proteomic approach were not cytotoxic. Significant changes in abundance and phosphorylation in the total soluble protein fraction of A549 cells have been detected following styrene exposure. All proteins have been identified using mass spectrometry and the main cellular functions have been assigned. Validation experiments on protein and transcript level confirmed the results of the 2-DE experiments. From the results, two main cellular pathways have been identified that were induced by styrene: the cellular oxidative stress response combined with moderate pro-apoptotic signaling. Measurement of cellular reactive oxygen species (ROS) as well as the styrene-mediated induction of oxidative stress marker proteins confirmed the hypothesis of oxidative stress as the main molecular response mechanism. Finally, adducts of cellular proteins with the reactive styrene metabolite styrene 7,8 oxide (SO) have been identified. Especially the SO-adducts observed at both the reactive centers of thioredoxin reductase 1, which is a key element in the control of the cellular redox state, may be involved in styrene-induced ROS formation and apoptosis. A similar proteomic approach has been carried out with the halobenzenes CB and 1,2-DCB (Chapter 5). In accordance with previous findings, cell toxicity assessment showed enhanced toxicity compared to the one caused by styrene. Significant changes in abundance and phosphorylation of total soluble proteins of A549 cells have been detected following exposure to subtoxic concentrations of CB and 1,2-DCB. All proteins have been identified using mass spectrometry and the main cellular functions have been assigned. As for the styrene experiment, the results indicated two main pathways to be affected in the presence of chlorinated benzenes, cell death signaling and oxidative stress response. The strong induction of pro-apoptotic signaling has been confirmed for both treatments by detection of the cleavage of caspase 3. Likewise, the induction of redox-sensitive protein species could be correlated to an increased cellular level of ROS observed following CB treatment. Finally, common mechanisms in the cellular response to aromatic VOCs have been investigated (Chapter 6). A similar number (4.6-6.9%) of all quantified protein spots showed differential expression (p<0.05) following cell exposure to styrene, CB or 1,2-DCB. However, not more than three protein spots showed significant regulation in the same direction for all three volatile compounds: voltage-dependent anion-selective channel protein 2, peroxiredoxin 1 and elongation factor 2. However, all of these proteins are important molecular targets in stress- and cell death-related signaling pathways. / Die vermehrte Verwendung von Produkten, welche flüchtige organische Substanzen (VOC - volatile organic compound) enthalten, hat eine generelle Exposition der Bevölkerung mit diesen Substanzen an Arbeitsplätzen aber auch in Wohnräumen bedingt. VOCs stehen im Verdacht, zur zunehmenden Inzidenz umweltbedingter Erkrankungen beizutragen. Da die molekularen Ursachen dieser Erkrankungen bisher noch unverstanden sind, war es ein übergeordnetes Ziel dieser Arbeit, VOC-vermittelte molekulare Effekte in menschlichen Lungenepithelzellen anhand eines in vitro Modells zu untersuchen. Dabei sollten vor allem Konzentrationen unterhalb der gültigen Arbeitsplatzgrenzwerte untersucht werden. Obwohl Effekte auf einzelne Proteine bekannt sind, wurden bisher keine Effekte der VOC-Exposition auf das komplexe Netzwerk der zellulären Proteine (Proteom) untersucht. Dieses Wissen ist essentiell, um induzierte zelluläre Mechanismen zu verstehen und Strategien zu deren Vermeidung zu entwickeln. Für die hier durchgeführten Untersuchungen wurde die Lungenepithelzelllinie A549 in einem Zweiphasenexpositionsmodell eingesetzt. Dieses ermöglichte eine möglichst direkte zelluläre Exposition und wurde bereits erfolgreich verwendet, um durch VOC hervorgerufene Entzündungseffekte zu identifizieren. Die massen-spektrometrische Identifikation von 266 Proteinflecken lieferte die erste umfassende Proteomkarte der A549 Zelllinie, welche nachfolgende Untersuchungen mit diesem häufig verwendeten Zelltyp erleichtern wird. Zusätzlich wurde die Verteilung der drei gängigen Luftkontaminanten Chlorbenzol (CB), Styrol and 1,2-Dichlorobenzol (1,2-DCB) zwischen den beiden Phasen (gas/flüssig) des Expositionsmodells gaschromatographisch bestimmt. Die Verteilung entsprach den verfügbaren Literaturdaten. Anschließend wurde das modifizierte Expositionsmodell erfolgreich eingesetzt, um styrol-vermittelte Effekte auf das Proteom der A549 Zellen zu charakterisieren (Kapitel 4). Zu Beginn erfolgte die Erfassung der Zelltoxizität der Substanz, um sicher zu stellen, daß der überwiegende Teil der späteren Expositionsexperimente mit subtoxischen Konzentrationen durchgeführt wird. Es konnte eine signifikant veränderte Expression und Phosphorylierung der löslichen Proteinfraktion der A549 Zellen als Reaktion auf die Styrolexposition festgestellt werden. Die regulierten Proteine wurden massenspektrometrisch identifiziert und ihre wichtigsten Funktionen wurden zugewiesen. Validierungsexperimente auf Protein- und auf Transkriptebene bestätigten die 2-DE Ergebnisse. Insgesamt konnte die zelluläre Reaktion durch die styrol-vermittelte Induktion zweier zentraler Mechanismen erklärt werden: oxidativer zellulärer Stress und beginnende Apoptose. Folgeexperimente wie die Messung der Menge der zellulären reaktiven Sauerstoffspezies (ROS) und die Induktion von redox-sensitiven Markerproteinen konnte die Hypothese eines styrol-induzierten oxidativen Milieus bestätigen. Schließlich wurden Proteinaddukte des reaktiven Styrolmetaboliten Styrol 7,8 epoxide (SO) identifiziert. Besonders die SO-Addukte, welche and den beiden aktiven Zentren der Thioredoxin Reduktase 1 gefunden wurden könnten eine wichtige Rolle bei der styrol-induzierten ROS-Bildung sowie der beginnenden Apoptose spielen. In Analogie zum Styrolexperiment wurden die Effekte der halogenierten Benzole CB und 1,2-DCB untersucht (Kapitel 5). Es konnten ebenfalls sämtliche Proteine identifiziert und die wichtigsten zellulären Funktionen zugewiesen werden. Diese Substanzen modulierten ebenfalls apoptotische Signalwege und die zelluläre Antwort auf oxidativen Streß. Der beobachtete starke pro-apoptotische Effekt konnte für beide Substanzen mit der Spaltung der Caspase 3 nachgewiesen werden. Weiterhin konnte für CB die Induktion redox-sensitiver Proteinspezies mit einem beobachteten höherem Gehalt an ROS erklärt werden. Schließlich wurden ähnliche Mechanismen der zellulären Antwort auf die Exposition mit den drei untersuchten aromatischen VOCs diskutiert (Kapitel 6). Alle getesteten VOCs verursachten eine vergleichbare differentielle Expression (p<0,05) von 4,6-6,9% aller quantifizierten Proteinspezies. Nur drei Proteinspots wurden dabei gemeinsam für alle VOCs reguliert: voltage-dependent anion-selective channel protein 2, peroxiredoxin 1 and elongation factor 2. Allerdings gehören diese drei Proteine zu wichtigen zellulären Zielstrukturen der Signalwege für Stressantwort und Zelltod.

Palladium-catalyzed reactions have found widespread use in contemporary organic chemistry due to their impressive range of functional group tolerance and high chemo- and regioselectivity. The pioneering contributions to the development of the Pd-catalyzed C-C bond forming cross-coupling reaction were rewarded with the Nobel Prize in Chemistry in 2010. Today, this is a rapidly growing field, and the development of novel methods, as well as the theoretical understanding of the various processes involved are of immense importance for continued progress in this field. The aim of the work presented in this thesis was to develop novel palladium(0)- and palladium(II)-catalyzed reactions. The work involved in achieving this aim led to the development of a Mo(CO)6-mediated carbonylative Stille cross coupling reaction for the preparation of various deoxybenzoins. The protocol utilized convenient gas-free conditions to facilitate the carbonylative coupling of benzyl bromides and chlorides with aryl and heteroaryl stannanes. Mo(CO)6-assisted conditions were then used in the development of a general protocol suitable for the aminocarbonylation of aryl triflates. Both electron-poor and electron-rich triflates were coupled with primary, secondary and aryl amines. In addition, DMAP was found to be a beneficial additive when using sterically hindered or poorly nucleophilic amines. An efficient and convenient method for the synthesis of styrenes from arylboranes was developed, employing the relatively inexpensive vinyl acetate as the ethene source under Pd(II)-catalyzed conditions. The reaction mechanism was studied using ESI-MS, and a plausible catalytic cycle was proposed. A method for the oxidative Heck reaction employing aryltrifluoroborates and aryl MIDA boronates was also developed. Electron-rich and electron-poor olefins were regioselectively arylated under microwave-assisted conditions. Various arylboron species were identified in an ongoing reaction using ESI-MS.    Further investigations led to the development of a direct method for the synthesis of arylamidines from aryltrifluoroborates and cyanamides. Under Pd(II)-catalyzed conditions it was possible to insert the aryl into primary, secondary and tertiary cyanamides. Finally, a desulfitative method for the synthesis of aryl ketones was developed. A variety of aryl sulfinates were effectively inserted into alkyl- and aryl nitriles. The mechanism was further investigated using ESI-MS and a plausible catalytic cycle was proposed.

This thesis is based on three inter-related studies: the first part deals with the microbial consortium, the identification of microbes and their volatiles, the second part deals with the study of bio-chemical control methods of two conifer pests; the pine weevil Hylobius abietis (L.) and the root rot fungi Heterobasidion spp., and the third part describes the production of styrene by a fungus using forest waste.The large pine weevil (Hylobius abietis L.) is an economically important pest insect of conifers in reforestation areas of Europe and Asia. The female weevils protect their eggs from feeding conspecifics by adding frass (mixture of weevil feces and chewed bark) along with the eggs. In order to understand the mechanism behind frass deposition at the egg laying site and to find repellents/antifeedants for pine weevils, microbes were isolated from the aseptically collected pine weevil frass. Microbial produced volatile organic compounds (VOCs) were collected by solid phase micro extraction and analyzed by GC-MS after cultivating them on weevil frass broth. The major VOCs were tested against pine weevils using a multi-choice olfactometer. Ewingella sp., Mucor racemosus, Penicillium solitum, P. expansum, Ophiostoma piceae, O. pluriannulatum, Debaryomyces hansenii and Candida sequanensis were identified as abundant microbes. Styrene, 6-protoilludene, 1-octene-3-ol, 3-methylanisole, methyl salicylate, 2-methoxyphenol and 2-methoxy-4-vinylphenol were the VOCs of persistently isolated microbes. In behavioral bioassay, methyl salicylate, 3-methylanisole and styrene significantly reduced the attraction of pine weevils to their host plant volatiles. Heterobasidion spp. are severe pathogenic fungi of conifers that cause root and butt rot in plants. Bacterial isolates were tested for the antagonistic activity against fungi on potato dextrose agar. Bacillus subtilis strains significantly inhibited the growth of H. annosum and H. parviporum. Styrene is an industrial chemical used for making polymeric products, currently produced from fossil fuel. A strain of Penicillium expansum isolated from pine weevil frass was investigated for the production of styrene using forest waste. Grated pine stem bark and mature oak bark supplemented with yeast extract produced greater amounts of styrene compared to potato dextrose broth. / <p>QC 20130507</p>