No description available.

No description available.

L’évaluation de l’exposition aux composés organiques volatils (COV) recourt couramment à l’analyse des métabolites urinaires en assumant qu’aucune interaction ne survient entre les composés. Or, des études antérieures ont démontré qu’une inhibition de type compétitive survient entre le toluène (TOL), l’éthylbenzène (EBZ) et le m-xylène (XYL). Le chloroforme, qui est également un solvant métabolisé par le CYP2E1, se retrouve souvent en présence des autres COV dans les échantillons de biosurveillance. La présente étude visait donc à évaluer si le chloroforme (CHL) peut lui aussi interagir avec ces COV et évaluer ces interactions au niveau de l’excrétion des biomarqueurs urinaires associés, soit l’o-crésol, l’acide mandélique et l’acide m-méthylhippurique pour TOL, EBZ et XYL respectivement. Afin d’obtenir des données humaines, cinq volontaires ont été exposés par inhalation à différentes combinaisons de COV (seuls et mélanges binaires ou quaternaires) où la concentration de chacun des composés était égale à 1/4 ou 1/8 de la valeur limite d’exposition (VLE) pour une durée de 6h. Des échantillons d’air exhalé, de sang et d’urine ont été récoltés. Ces données ont ensuite été comparées aux modèles pharmacocinétiques à base physiologique (PCBP) existants afin de les ajuster pour l’excrétion urinaire. Certaines différences ont été observées entre les expositions aux solvants seuls et les coexpositions, mais celles-ci semblent majoritairement attribuables aux remplacements de participants à travers les différentes expositions. Les valeurs de Vmax pour EBZ et CHL ont été optimisées afin de mieux prédire les niveaux sanguins de ces COV. À l’exception du modèle pour EBZ, tous les paramètres pour l’excrétion urinaire ont été obtenus à partir de la littérature. Les modèles adaptés dans cette étude ont permis de simuler adéquatement les données expérimentales. / Evaluation of volatile organic compounds (VOC) exposure commonly resorts to urinary metabolite analyses, assuming that no interaction occur between coexposed chemicals. However, previous studies have reported competitive inhibition between toluene (TOL), ethylbenzene (EBZ) and m-xylene (XYL). Chloroform, which is also metabolized by CYP2E1, is also often found in human biomonitoring samples along with the mentioned VOCs. The goal of the present study was to evaluate if chloroform (CHL) can interact with previous VOC and to evaluate those interactions at the urinary biomarker excretion level for corresponding metabolites, namely o-cresol, mandelic acid and m-methylhippuric acid for TOL, EBZ and XYL respectively. To obtain human data, five male volunteers were exposed by inhalation to different VOC combinations (single and binary or quaternary mixtures) where concentration of each chemical was equal to 1/4 or 1/8 of the threshold limit value (TLV) for 6h. Exhaled air blood and urine samples were collected. These data were then compared with existing physiologically based pharmacokinetic (PBPK) model predictions for adjustment for urinary excretion. Some differences were observed between single and mixed exposures but they may be mainly related to volunteer replacements throughout experiments. Vmax values for EBZ and CHL were optimized to better fit blood data. Except for EBZ model, all urinary excretion parameters were taken from the literature. Models adapted in the present study adequately simulated experimental data.

Une approche synthétique a été développée pour préparer les phtalocyanines dimériques de fer azote ponté substituées par les substituants alkylesulfoniles attracteurs d’électrons. Six nouvelles phtalocyanines avec des petits substituants (méthylesulfonile, éthylesulfonile et hexylesulfonile) et des gros substituants (t-butylesulfonile, adamantylesulfonile et cyclohexylesulfonile) ont été préparées et caractérisées par ionisation électrospray (ESI-MS), UV-vis, FT-IR et RPE. Deux complexes (avec substituants hexylesulfoniles et t-butylesulfoniles) ont été caractérisés par spectroscopie Mössbauer, spectroscopie photoélectronique de rayons X (XPS) et par spectroscopie d’absorption des rayons X (XANES, EXAFS, spectroscopie d’émission Kβ haute résolution). Il a été montré que l’état électronique de fer de ces complexes dépend de la taille de substituants. Les phtalocyanines de fer à l’azote ponté avec les gros substituants (t-butylesulfonile, adamantylesulfonile et cyclohexylesulfonile) sont cationiques (PcFeIVNFeIVPc)+N3-, tandis que les complexes avec les substituants plus gros (t-butylesulfonyles, adamantylesulfonyles et cyclohexylesulfonyles) sont non-chargés, formellement PcFeIIINFeIVPc. Les propriétés catalytiques des six complexes ont été étudiées en utilisant du butyle hydroperoxyde comme oxydant en oxydation de toluène, de p-xylène et des alcools. Ce travail montre l’efficacité des phtalocyanines dimériques de fer azote ponté substituées par les groupements alkylesulfoniles attracteurs d’électrons comme catalyseurs pour oxydation dans les conditions favorables pour les applications industrielles propres / The synthetic approach was developed for the preparation of N-bridged diiron phthalocyanines substituted by different electron-withdrawing alkylsulfonyl substituents. Six novel phthalocyanines bearing small (methylsulfonyl, ethylsulfonyl and hexylsulfonyl) and bulky (t-butylsulfonyl, adamantylsulfonyl and cyclohexylsulfonyl) substituents have been prepared and characterized by electrospray ionization mass spectrometry (ESI-MS), UV-Vis, FT-IR and EPR. Two complexes (with hexylsulfonyl and t-butylsulfonyl substituents) were characterized in addition by Mössbauer techniques, X-ray photoelectron spectroscopy (XPS) and Fe K-edge X-ray absorption spectroscopy (XANES, EXAFS, high resolution Kβ emission spectroscopy). It has been evidenced that the electronic state of iron in these complexes depends on the size of the substituents. While N-bridged diiron phthalocyanines having methylsulfonyl, ethylsulfonyl and hexylsulfonyl substituents are cationic (PcFeIVNFeIVPc)+N3- complexes, N-bridged diiron phthalocyanines with bulkier t-butylsulfonyl, adamantylsulfonyl and cyclohexylsulfonyl substituents are formally neutral PcFeIIINFeIVPc species. The catalytic properties of six N-bridged diiron phthalocyanines have been studied, using tert-butyl hydroperoxide (tBuOOH) as the oxidant in the oxidation of toluene, p-xylene as well as in the oxidation of various alcohols. This thesis demonstrates the efficiency of N-bridged diiron phthalocyanines substituted by electron-withdrawing alkylsulfonyl groups as oxidation catalysts, in conditions required by environmental and industrial preoccupations

Ce travail s'inscrit dans le cadre de la protection de l'environnement et s'intéresse spécifiquement à la dépollution d'effluents aqueux en vue de piéger d'une part les anions nitrate et/ou phosphate, responsables du phénomène d'eutrophisation, mais également le toluène, hydrocarbure couramment rencontré dans les effluents aqueux urbains et industriels ou les eaux naturelles. Le piégeage de ces polluants a été effectué sur des matériaux zéolithiques. Une grande partie des expérimentations utilise un matériau potentiellement efficace pour le piégeage des trois polluants cités plus haut, à savoir la SMZ ("Surfactant-Modified Zeolite"), classiquement préparée à partir d'une zéolithe naturelle, la clinoptilolite, et d'un tensioactif, le bromure d'hexadecyltriméthylammonium (HDTMA+). En piégeage d'ions nitrate, d'autres SMZ, réalisées à partir de zéolithes synthétiques (LTA, FAU) et diverses espèces organiques tensioactives ou non se montrent moins performantes que la SMZ classique, à l'exception d'un nouveau matériau préparé à partir de nanofeuillets de zéolithe MFI et modifié avec l'ion HDTMA+ (SMZN). Pour le piégeage des ions phosphate, les performances de la SMZ classique ont été comparées à celles de plusieurs zéolithes calciques. Enfin, le piégeage de toluène a été expérimenté sur quatre matériaux, la SMZ classique, un charbon actif et deux zéolithes hydrophobes, la silicalite-1 et la zéolithe bêta. Les expérimentations de piégeage ont été réalisées en système fermé ou en système ouvert. L'influence de la concentration initiale en polluants, du rapport liquide/solide, du débit de filtration, de la présence de compétiteurs et du temps de contact a été examinée. / This work concerns the environmental protection, specifically the treatment of aqueous effluents. Effluents containing nitrate and/or phosphate anions, responsible for the eutrophication phenomenon, and also toluene, which is commonly found in urban and industrial flows and natural waters, were specifically studied. The removal of these pollutants was performed on zeolitic materials. A large part of the experiments use a material potentially efficient to remove the three pollutants mentioned above, namely the SMZ ("Surfactant-Modified Zeolite"), conventionally prepared from a natural zeolite, clinoptilolite, and a surfactant, hexadecyltrimethylammonium bromide (HDTMA+). For nitrate removal, other SMZ, prepared from synthetic zeolites (LTA, FAU) and various organic species (surfactant or not) were less efficient than conventional SMZ except a new material prepared from zeolite MFI nanosheets and modified with HDTMA+ ion. The efficiency of the conventional SMZ for the phosphate ions uptake was compared with those of several calcic zeolites. Finally, removal of toluene was performed on four materials, conventional SMZ, an activated carbon and two hydrophobic zeolites, namely silicalite-1 and beta zeolite. Uptake experiments were conducted in batch-wise and fixed-bed column systems, the second representing a more realistic simulation of dynamic field condition The influence of the initial pollutant concentration, the liquid/solid ratio, the filtration rate, the presence of competitive species and the contact time was examined.

L’obtention de nanoparticules d’or nécessite le contrôle de nombreux paramètres et la compréhension du mode d’interaction entre l’or et le support. Pour cela, le choix du support est très important. Le premier volet de la thèse concerne la préparation contrôlée des catalyseurs à base d’or supporté sur les oxydes mésoporeux réductibles TiO₂, CeO₂ et Fe₂O₃ synthétisés via deux stratégies Soft et hard template en utilisant respectivement comme agents structurants le tribloc copolymère (Pluronic 123) et la silice mésoporeuse SBA-15. Les différentes techniques de caractérisation mettent bien en évidence que le taux de dépôt de l’or dépend de la concentration initiale de HAuCl₄, de la méthode de préparation (DPU, DP NaOH), de la teneur en or visée et de la nature du support ; Ces résultats sont à relier à la spéciation des espèces or en solution en fonction du pH final de la solution. Les taux de dépôt de l’or sont plus importants sur CeO₂ et ceci quelle que soit la teneur en or visée dans ce travail. Une dispersion très élevée est obtenue (la taille moyenne des particules d’or est de 2nm) sur les catalyseurs à 1% et 2%Au/CeO₂ préparés par la méthode DPU et calcinés à 400°C. Le deuxième volet de cette étude concerne l’oxydation en phase gaz d’une molécule organique modèle le toluène et l’oxydation en phase liquide d’une molécule organique modèle le phénol par des réactions de type Fenton et photo Fenton. Dans l’oxydation du toluène en phase gazeuse, les catalyseurs à base d’or supportés sur oxydes mésoporeux sont totalement sélectifs en CO₂ et H₂O. Les performances catalytiques dépendent des conditions de synthèse des catalyseurs et de la nature de l’oxyde utilisé ; le catalyseur 1%Au/CeO₂ est très actif et très stable au cours de quatre cycles successifs et au cours du temps. L’oxydation en phase liquide d’une molécule organique modèle le phénol par des réactions de type Fenton et photo Fenton a été effectuée sur les catalyseurs FeSBA-15 synthétisés via différentes stratégies : introduction du fer par voie postsynthétique et par voie hydrothermale en milieu faiblement et fortement acide respectivement à pH=6 et pH=3. Les performances catalytiques dépendent du rapport Si/Fe et de la taille des particules des espèces de fer, la taille des particules étant directement liée à la stratégie de synthèse des catalyseurs. Le catalyseur FeSBA-15(Si/Fe=60) synthétisé à pH=6 est un candidat potentiel dans la dégradation de polluants organiques par procédé Fenton et photo-Fenton en milieu neutre. / Well dispersed gold nanoparticles are the key to obtain an active gold catalyst. Obtaining gold nanoparticles requires control of many parameters and understanding of the interaction mode between gold and the support. For this reason the choice of the support is very important. The first part of this thesis concerns the controlled preparation of gold catalysts supported on reducible mesoporous oxides TiO₂, CeO₂ and Fe₂O₃ synthesized via two strategies Soft and Hard template using respectively. triblock copolymer (Pluronic 123) and mesoporous silica SBA-15 as template. This study clearly shows that the gold loading depends on the initial concentration of HAuCl₄, the method of preparation (DPU DP NaOH), theoretical gold content and the nature of the support. These results are to relate to the gold speciation which is a function of pH of the solution. The gold loading is higher on CeO₂ than on TiO₂ and Fe₂O₃ whatever the theoretical gold content. Very high gold dispersion is obtained (the gold particle size is 2 nm) on 1wt% and 2wt% Au/CeO₂ prepared by DPU and calcined at 400°C. The second part of this study concerns the toluene oxidation in the gas phase on Au/mesoporous oxide catalysts and the Fenton and photo-Fenton degradation of phenolic aqueous solutions by H₂O₂ on FeSBA-15 catalysts prepared following different synthesis routes, direct synthesis by adjusting pH at 3 and 6 and with post synthesis procedure. In the toluene oxidation in the gas phase Au/mesoporous oxide catalysts are totally selective for CO₂ and H₂O. The catalytic performances depend on the synthesis conditions of catalysts and the support; the 1wt% Au/CeO₂ catalyst is very active and exhibits a long-term stability. In the Fenton and photo-Fenton degradation of phenolic aqueous solutions the catalytic performances depend on the Si/Fe ratio and the particle size of the iron species, the particle size being directly related to the synthesis strategy of the catalysts. The catalyst FeSBA-15 (Si/Fe = 60) synthesized at pH = 6 is a potential candidate in the degradation of organic pollutants by Fenton and photo-Fenton process in neutral medium. / م لخصمسقني لمعلا يف هذه ةحورطألا ىلإ نيئزج:OiT 2ب وا سطة OeC 2و , Fe2O ي خ تص الاول ال ق سم ب تح ض يرمح فزات من ال ذهبن وع من م يزوب ري ة ب مواد مدعم 3ان واع مخ ت لف ال تح ض ير. ت شخ يص ف ي ال م س ت عم لة ال ت ق ن يات مخ ت لفت ب ين ال مح ضرة ل مح فزات انال دعم ط ب ي عة ك ذا و ال مح فز ت ح ض ير وطري قة HAuCl ت ر سب معدل ي ت ع لق ل ذه با ت رك يز ع لى 4ي ع ضو جزيء و سطغازي enèuloT أك سدة ف ي ال مواد هذه ب تط ب يق ي ت ع لق ال ثان ي ال ق سم ف يال مح فز ت ح ض ير Ò طرق ك ذا و ل ت فاعل هذا ع لى ال مؤث رة ل عوامل ب درا سة ق م نا سال فا ال مذك ورة ل لمح فزات ال ف عال ية ع لان واع مخ ت لف ب وا سطة FeSBA- ي ع ضو جزيء lonehP ت فاعل ب وا سطة notneF سائ ل و سط ف ي وعمن 51 ن مح فزات ع لىوHp ال و سط Si/Fe قلعتي ةبسنب FeSBA- ريضحتلا.ادأء 1515FeSBA-15, Fenton, Phenol, Toluène, TiO و 2 CeO2, Fe2O3, SBA- ال ك لمات ال م ف تاح ية ׃م يزوب وري ة ,

Les émissions de composés organiques volatiles (COV) dans l'atmosphère sont réglementées à caus de leur impact sur la santé. L'oxydation catalytique est une des techniques prometteuses pour limiter ces émissions. L'objectif de ce travail était de mettre au point des catalyseurs actifs, sélectifs en dioxyde de carbone et stables pour la destruction de COV. Afin de trouver une alternative à l'utilisation de catalyseurs à base de métaux nobles, ce travail de recherche a été orienté sur la synthèse de matériaux à base d'oxydes de métaux de transition. Les différents oxydes mixtes ont été caractérisés par différentes techniques physico-chimiques dont la Diffraction des Rayons X (DRX), les Analyses Thermiques (ATD/ATG), la Réduction en Température Programmée (H₂-RTP), la Microscopie Électronique à Transmission (MET), la Spectrométrie de Photoélectrons induits par rayons X (SPX),... Dans un premier temps, une étude sur la préparation d'oxydes mixtes issus de précurseurs de type hydrotalcite a été menée, concernant le remplacement du cation bivalent. Cette étude a montré que l'oxyde mixte contenant du cobalt et de l'aluminium présentait une activité catalytique intéressante pour l'oxydation du toluène ainsi que du monoxyde de carbone. Afin d'améliorer cet oxyde mixte, une étude sur l'influence des méthodes non conventionnelles de préparations du précurseur hydrotalcite a été effectuée. Les micro-ondes ainsi que les ultrasons ont été utilisés lors de cette synthèse et les différents oxydes mixtes ont été testés dans les réactions du toluène et du CO. Lors de cette application, un effet bénéfique de l'utilisation des micro-ondes lors de la synthèse a été observé. Dans un troisième temps, une étude de l'incorporation de cérium dans la structure hydrotalcite a été menée. Un oxyde mixte du type CoAlCe a montré une activité catalytique intéressante pour l'oxydation totale du toluène. De plus, une relation entre la réductabilité et l'activité catalytique a pu être mise en évidence. Une comparaison entre les meilleurs catalyseurs de cette étude et des catalyseurs à base de métaux nobles commerciaux a été abordée. L'étude cinétique de l'oxydation totale du toluène a montré, que dans le cas des oxydes mixtes CoAlCe et CoAl, un mécanisme du type Mars Van Krevelen décrirait le mieux la réaction. Enfin, les quatre meilleurs oxydes mixtes ont été testés dans la réaction d'oxydation du toluène en présence de monoxyde de carbone. Un effet bénéfique de celui-ci sur la réactivité vis-à-vis du toluène a été observé. / Catalytic oxidation is one of the promising technologies to reduce VOC emissions. The objective of this work was to develop active, selective and stable catalyst for the destruction of VOC. In order to find an alternative to the use of noble metals based catalysts, this research has been focused on the synthesis of materials based on transition metal oxides. The various mixed oxides were characterized by different physico-chemical techniques including XRD, Thermal Analysis, H2-TPR, TEM, XPS...Initially, a study on the preparation of mixed oxides derived from hydrotalcite-like precursors was conducted. Thus, it was shown that the mixed oxide containing cobalt and aluminum exhibited interesting for catalytic activity for the toluene aznd carbon monoxide total oxidation. To improve this mixed oxide, a study of the influence of non-conventional methods for the preparation of the precursor was performed. The microwave and ultrasound have been used in these syntheses. The various mixed oxides thus prepared were tested in the oxidation reactions of CO and toluene. In this application, a beneficial effectvof the use of microwaves in the synthesis was observed. Thirdly, a study of the incorporation of cerium in the hydrotalcite structure was conducted. Mixed oxides of CoAlCe show interest for the total oxidation of toluene catalytic activity. Moreover, a relationship between the reductibility and the catalytic activity has been demonstrated. A comparison of the best catalysts of this study and catalysts of noble metals business was discussed. The kinetic study of the complete oxidation of toluene showed that in the case of mixed oxides CoAlCe and CoAl, a mechanism of March Van Krevelen type described the reaction.

A glicerina é um composto de grande utilidade em muitas áreas de aplicação. Atualmente, a maior fonte de glicerina é como subproduto da produção do biodiesel. Em 2010 o Brasil foi o segundo maior produtor de biodiesel no mundo com 2,4 milhões de m3. Estima-se que 10% da produção de biodiesel é glicerina bruta e destes 10%, aproximadamente entre 30% e 60% correspondem à glicerol. As impurezas são formadas por água, sais orgânicos e inorgânicos, ésteres e álcoois, e traços de glicerídeos. Como as aplicações mais nobres da glicerina requerem uma glicerina isenta de impurezas, novas rotas de purificação da glicerina bruta vem sendo estudadas. Neste sentido, o Laboratório de Separações Térmicas e Mecânicas da EPUSP propôs uma nova rota de purificação em 2008, na qual a ultima etapa é a desidratação de uma solução glicerol-água por meio de destilação trifásica usando tolueno como arrastador. O objetivo do presente trabalho foi estudar o comportamento deste tipo de destilação em uma coluna modulada com três pratos perfurados. Nesta coluna avaliou-se o layout de pratos e as melhores condições de operação. Os resultados, obtidos com este estudo, constituem uma contribuição importante para o projeto básico de coluna de destilação trifásica. As séries experimentais foram planejadas sequencialmente empregando-se planejamento estatístico de experimentos (DOE). Como variáveis de processo foram estudadas a vazão de vapor do tolueno (kg/h), vazão de alimentação de glicerina (kg/h) e concentração de glicerol na alimentação (% em massa). Como variáveis geométricas foram estudadas a área livre do prato () e a altura de vertedouro (Hw). O desempenho da coluna foi avaliado mediante o incremento da concentração de glicerol (em relação à concentração de glicerol na alimentação) e a concentração de glicerol no fundo da coluna (estas duas variáveis de resposta são dependentes entre si). A influência das variáveis de processo e geométricas nas respostas estudadas permitiram a construção de modelos estatísticos, e o melhor deles foi comparado com os modelos de não equilíbrio (NEQ) e de equilíbrio (EQ) obtidos por simulação no programa ASPEN PLUS. O modelo de não equilíbrio está baseado nas equações de Maxwell-Stefan, que utiliza a abordagem de Eckert e Vanek (2001) e a correlação de Chen-Chuang (1993), para estimar os coeficientes binários de transporte de massa. O modelo de equilíbrio utiliza as equações MESH (Material balance, Equilibrium, mole fraction Summation, and Heat balance). Conclusivamente, pode-se afirmar que as variáveis operacionais exercem maior influência do que as variáveis geométricas na desidratação da glicerina. As melhores condições foram: a vazão de vapor de tolueno de 23,5 kg/h, vazão de alimentação de glicerina de 2,2 kg/h e concentração de glicerol na alimentação de 50 % glicerol em massa, usando o layout L5 com área livre de 0,04 e altura de vertedouro de 70 mm. Os valores preditos pelo modelo estatístico (obtido com dados experimentais) e pelo modelo de NEQ representaram o comportamento da desidratação da glicerina por destilação trifásica à pressão atmosférica usando tolueno como arrastador, na coluna de pratos perfurados estudada. O modelo de EQ superestimou os valores reais. / Glycerine is a material of outstanding utility with many areas of application. Currently, the largest source of glycerine is as a by-product of biodiesel production. In 2010, Brazil was the second largest biodiesel productor in the world with 2.4 million m3. It is estimated that 10% of biodiesel is raw glycerine, and of this 10%, approximately between 30% and 60% corresponds to glycerol. The impurities are formed by water, organic and inorganic salts, esters and alcohols, and traces of glycerides. Although many attempts have been made to use raw glycerine, it is still necessary to purify it for of the most applications; hence new routes of glycerine purification have been studied. In this way, the Laboratory of Thermal and Mechanical Separations of EPUSP have proposed a new route of purification in 2008, where the last step is the dehydration of glycerol-water solution by three-phase distillation using toluene as entrainer. The aim of the present work was to study the behavior of the three-phase distillation using a modulated column with three sieve trays. In this column, the tray layout and the best operating conditions were evaluated. The results achieved in this study are an important contribution to the basic design of three-phase distillation column. Experimental series were designed sequentially employing a statistical design of experiments (DOE). The process variables studied were the vapor flow rate of toluene (kg/h), feed flow rate of glycerine (kg/h) and the feed glycerol concentration (% wt.). The geometric variables studied were the fractional hole area () and the weir height (Hw). The column performance was evaluated by the increment of glycerol concentration (in relation to the feed glycerol concentration) and the bottom glycerol concentration (these two variables are mutually dependent responses). The influence of process and geometric variables allowed the empirical models building, in which the best model was compared with the non-equilibrium (NEQ) and equilibrium (EQ) models obtained by the simulator ASPEN PLUS. The non-equilibrium model is based on Stefan-Maxwell equations, which uses the approach of Eckert and Vanek\'s (2001) and the Chen-Chuang correlation (1993), to estimate the binary coefficients of mass transport. The equilibrium model is based on the MESH equations (Material balance, Equilibrium, mole fraction Summation, and Heat balance). Finally, it can be stated that the operating variables have more influence than the geometric variables in the glycerine dehydration. The best conditions were: vapor flow rate of toluene of 23.5 kg/h, feed flow rate of glycerine of 2.2 kg/h and feed glycerol concentration of 50% wt., using the fractional hole area of L5 of 0.04 and weir height of 70 mm. The predicted values obtained by the statistical model and by the non-equilibrium model represented the behavior of the glycerine dehydration by three-phase distillation at atmospheric pressure using toluene as entrainer in the sieve tray column studied. The equilibrium model (EQ) overpredicted the real values.

Die Toluol-Dioxygenase von Pseudomonas putida F1 ist eine Rieske-Dioxygenase und besteht aus Reduktase-, Ferredoxin- und Oxygenase-Komponente. Sie katalysiert den ersten Schritt im aeroben Abbau von Toluol. Ein effizienter Elektronentransfer zur terminalen Oxygenase-Komponente - an der die Sauerstoffaktivierung und Umwandlung von Toluol zum cis-Toluol-Dihydrodiol stattfindet - setzt eine reibungslose Interaktion aller Komponenten voraus. Die Ergebnisse der Stopped-flow-Messungen in der reduktiven Halbreaktion zeigen, dass NADH die Reduktase mittels Hydridtransfer reduziert, wodurch ein stabiler Ladungstransfer-Komplex zwischen NAD+ und FADH- entsteht. In der oxidativen Halbreaktion wird dieser dann durch einen Elektronenakzeptor über das blaue Semichinon zum Chinon oxidiert. Dabei zeigt sich, dass der Ladungstransfer-Komplex die Reaktion der Reduktase mit Sauerstoff unterdrückt. Eine Erklärung hierfür liefert die Kristallstruktur des Ladungstransfer-Komplexes. Die Reaktion mit Sauerstoff wird dadurch unterdrückt, dass das NAD+ koplanar mit dem Isoalloxazinring ist und den reaktiven N5-C4a Teil des FADs schützt und zudem den Isoalloxazinring in eine planare, weniger sauerstoffempfindliche Konformation zwängt. Durch die Bildung des Reduktase-Ferredoxin-Komplexes wird ein effizienter Elektronentransfer folgendermaßen ermöglicht: a) das Ferredoxin bindet an die Reduktase aufgrund elektrostatischer Anziehung entgegengesetzter Oberflächenladungen beider Proteine, b) die hydrophobe Region, die die beiden Redoxzentren umgibt, fungiert als Ein- und Ausgang für Elektronen und c) die geringe Entfernung von 11.7 Å zwischen beiden Kofaktoren erlaubt einen schnellen Elektronentransfer. Die Ergebnisse dieser Arbeit zeigen, dass der Elektronentransfer zwischen Reduktase und Ferredoxin durch die Bildung eines stabilen Ladungstransfer- und Reduktase- Ferredoxin-Komplexes beeinflusst wird und dadurch das Problem einer ungewollten Reaktion mit Sauerstoff umgangen wird. / The toluene dioxygenase from Pseudomonas putida F1 is a three-component Rieske non-heme iron dioxygenase comprising of a reductase, ferredoxin and an oxygenase component. It catalyzes the initial step in the aerobic degradation of toluene to cis-toluene dihydrodiol. A smooth interaction between all three components needs to be ensured to efficiently transfer the electrons derived from NADH oxidation to the terminal oxygenase component where molecular oxygen is activated and used for the hydroxylation of toluene. The results of the kinetic studies of the reductive half reaction of reductase reveal that NADH reduces the reductase, resulting in the formation of a stable charge transfer complex between NAD+ and FADH-. Oxidation of the charge transfer complex by an electron acceptor proceeds via the neutral semiquinone to the quinone state of FAD. It is shown that the charge transfer complex suppresses the reaction of the reductase with dioxygen. An explanation for this change in reactivity can be deduced from the structure of the charge transfer complex. Its slower reaction with dioxygen results from NAD+ lying coplanar with the FAD shielding its reactive N5-C4a locus and the forced planarity of the isoalloxazine ring. The formation of the reductase-ferredoxin complex allows efficient electron transfer from reductase to ferredoxin because a) the oppositely charged interacting surfaces of both proteins facilitate the pre-orientation of the ferredoxin on the reductase, b) a hydrophobic region surrounding the two redox centers in the complex acts as an exit/entrance port for electrons and c) the short edge-to-edge distance between both cofactors of 11.7 Å guarantees a fast electron transfer. The results demonstrate that the electron transfer between reductase and ferredoxin is governed by the formation of a stable charge transfer and of a reductase-ferredoxin complex with which the problem of an unwanted side reaction with dioxygen is obviated.

O tolueno e o xileno são substâncias presentes, ao lado de outras, em vários produtos, entre eles as tintas, tíneres e colas, provocando exposição combinada dos trabalhadores a diversas substâncias químicas. Assim, foi objetivo deste trabalho desenvolver um método simples, rápido e confiável de cromatografia em fase gasosa que permitisse análise simultânea do ácido hipúrico (AH) e ácido metil-hipúrico (AMH) em urina, bioindicadores de dose interna utilizados na monitorização da exposição ocupacional ao tolueno e xileno respectivamente. Após extração líquido-líquido e derivação com trimetilfenilamôneo, foi realizada análise cromatográfica em coluna capilar 100% polidimetilsiloxano, usando-se o ácido heptadecanóico como padrão interno. Foram avaliados 69 trabalhadores que manipulavam tintas em atividades de repintura de veículos e 31 trabalhadores não-expostos (controle). O método mostrou-se linear entre 0,1 (limite de quantificação) e 5,0 g/L para o AH e 0,2 (limite de quantificação) e 5 g/L para o AMH. A recuperação média foi de 81 % e a inexatidão de aproximadamente - 8,0% (bias) para ambos os analitos. Os coeficientes de variação médios para as concentrações de 0,5; 2,0 e 4,0 g/L foram, para a precisão intra-ensaio, de 3,5% para o AH e de 3,7% para o AMH, e para a interensaio, de 10,5% para o AH e de 10,7% para o AMH. Os analitos permaneceram estáveis em até 3 ciclos de congelamento/descongelamento das amostras de urina. O valor médio obtido nas amostras de trabalhadores expostos foi de 0,55 g/g de creatinina (mediana = 0,36 g/g de creatinina). Apesar de diferença estatisticamente significativa (teste t Student, p ≤ 0,05) ter sido observada entre os valores médios de AH nos trabalhadores expostos e nos do grupo controle, esta diferença não foi detectada quando analisou-se as medianas. O hábito de fumar e de ingerir bebidas alcoólicas também não mostrou alterar significativamente a excreção dos bioindicadores no grupo avaliado. / Toluene and the xylene, among others substances, are solvents used in several products, such as inks, thiners and glues, and are responsible for mixed exposure in workers. Thus, the aim of this work was to develop a simple, fast and reliable gas chromatographic method to allow the simultaneous detection and quantitation of hippuric acid (HA) and methylhippuric acid (MHA) in urine, which are internai dose bioindicators in the monitoring of occupational exposure to toluene and the xylene, respectively. After liquid-liquid extraction and derivation with trimethylphenylammonium, the chromatographic analysis was accomplished using capillary column 100% methylsiloxane, and heptadecanoic acid as internai standard. 69 workers exposed to inks in activities such as vehicles painting and 31 nonexposed workers were evaluated. The method showed linearity range between 0,1 (quantitation limit) and 5,0 g/L for HA and 0,2 (quantitation limit) and 5 g/L for MHA. The recovery was 81 % and the inaccuracy of approximately - 8,0% (bias) for both analytes. The mean variation . coefficients for the concentrations of 0,5; 2,0 and 4,0 g/L were, for the intraassay precision, of 3,5% for HA and of 3,7% for MHA, and for the inter assay, 10,5% for HA and 10,7% for MHA. The analytes were stable for 3 freezing cycles of the urine samples. The medium value obtained in the exposed workers\' samples was of 0,55 creatinina g/g (medium = 0,36 creatinina g/g). In spite of the observed statistical significant differences (test t Student, p ≤ 0,05) among the medium values of HA in the exposed workers and the control groups, this difference was not detected when it was analyzed the respective median values. Smoking and drinking alcoholic beverages habits did not significantly alter the excretion of these bioindicators in the studied group.