The growing demand in portable and compact consumer devices and appliances has resulted in the need for the miniaturisation of electronic components. These miniaturised electronic components are sensitive and susceptible to damage by voltages as low as 20V. Electrically conductive styrenic thermoplastics are widely used in electronic packaging applications to protect these sensitive electronic components against electro-static discharge (ESD) during manufacturing, assembly, storage and shipping. Such ESD applications often require the optimal volume resistance range of ≥ 1.0x105 to < 1.0x108 Ω. The best known method to render styrenic thermoplastics conductive is by the incorporation of conductive fillers, such as carbon black but the main limitation is the difficulty in controlling the conductivity level due to the steep percolation curve. Thus the aim of this research is to develop electrically conductive styrenic thermoplastics by blending several styrenic resins with polymeric conductive additives to achieve optimal volume resistance range for ESD applications with the ease in controlling the conductivity level.

Les objectifs de cette thèse consistent à identifier les morphologies adoptées par des mélanges d’élastomères chargés en noir de carbone, à étudier l’influence de l’introduction de charges sur ces morphologies mais aussi de détecter la localisation de la charge dans ces mélanges. Dans une dernière partie, l’impact de ces différentes structures sur les défauts d’extrusion est abordé. Ces travaux concernent l’étude des coupages caoutchouc naturel / styrene-butadiene rubber (NR / SBR) et polybutadiène / styrene-butadiene rubber (BR / SBR) non vulcanisés. Dans un premier temps, les morphologies adoptées par ces mélanges non chargés ont été identifiées grâce à plusieurs protocoles expérimentaux. L’influence de l’introduction de noir de carbone ainsi que l’étude de la localisation de la charge dans ces mélanges ont constitué une seconde étape dans ces travaux. Aucune localisation préférentielle de la charge n’a été détectée pour ces mélanges. Un système ségrégé a donc été réalisé par la suite. Enfin, le comportement en extrusion de ces mélanges a été simulé par rhéométrie capillaire et des observations de défauts d’aspect ont été faites. La ségrégation du noir de carbone ne semble pas entraîner la création de défauts d’aspect, sauf dans le cas d’une localisation dans la matrice / The purpose of this project is to investigate the morphology of elastomeric blends filled with carbon black, the localization of the filler in these blends and the structure impact on their processing. This work concerns uncured natural rubber / styrene-butadiene rubber (NR / SBR) blends and butadiene rubber / styrene-butadiene rubber (BR / SBR) blends. Firstly, the morphology of these blends unfilled was described by different experimental procedures over the entire composition range. Secondly, the impact of the filler on the morphology and the localization of it on the blends were studied. No preferential localization was observed in our case. Another blend with a segregation was realized. And finally, the processing of these elastomeric blends was simulated by capillary rheology to detect the formation of flow instabilities. Few melt fractures were observed, except when the filler is localized in the matrix

A reciclagem de materiais poliméricos tem sido objeto de estudos a fim de poupar recursos naturais, principalmente de fontes não renováveis, com objetivo de minimizar os impactos causados ao meio ambiente. Nesse cenário, aparecem os materiais elastoméricos, como a borracha, principalmente na utilizada da fabricação de pneus, uma vez que a indústria pneumática consome aproximadamente 60% da produção de borracha. Como a destinação final de forma ambientalmente correta do pneu é uma exigência devidamente amparada por normas e leis nacionais e internacionais, o objetivo desse trabalho é desenvolver um estudo sobre a eficácia das irradiações das micro-ondas no processo de desvulcanização do pó de pneu. Para esse estudo as amostras de pó de pneu foram submetidas a irradiações de micro-ondas, e posteriormente incorporadas às matrizes poliméricas de NR (borracha natural) e SBR (borracha de butadieno-estireno), e caracterizadas para verificação de suas propriedades. Para caracterização das amostras foram utilizados os seguintes ensaios: Espectroscopia no Infravermelho (FTIR), Dureza, Resistência à Tração e Alongamento, Reometria, Índice de Inchamento, Análise Termogravimétrica (TGA) e Microscopia Eletrônica de Varredura (MEV). Verificou-se viabilidade técnica da incorporação do pó de pneu nas matrizes de NR e SBR, uma vez que alguns resultados mostraram que a adição do pó de pneu irradiado via micro-ondas não ocasionou perdas significativas nas propriedades mecânicas e térmicas dos compostos. / The recycling of polymeric materials has been studied in order to save natural resources, mainly from non-renewable sources, in order to minimize the impacts caused to the environment. In this scenario, there are elastomeric materials, such as rubber, mainly used in tire manufacturing, since the pneumatic industry consumes approximately 60% of rubber production. As the final destination of an environmentally correct tire is a requirement, duly supported by national and international laws and regulations, the objective of this work is to develop a study on the efficiency of microwave irradiation in the process of tire powder devulcanization. For this study the tire powder samples were subjected to microwave irradiation, and later incorporated into the polymer matrices of NR (natural rubber) and SBR (butadiene-styrene rubber), and characterized for verification of their properties. For characterization of the samples the following tests were used: Infrared Spectroscopy (FTIR), Hardness, Tensile Strength and Stretching, Rheometry, Swell Index, Thermogravimetric Analysis (TGA) and Scanning Electron Microscopy (MEV). It was verified the technical feasibility of the incorporation of the tire powder in the NR and SBR matrices, since some results showed that the addition of the tire powder irradiated by microwave did not cause significant losses in the mechanical and thermal properties of the compounds.

O propósito deste trabalho foi o desenvolvimento de um procedimento simulador de processo reproduzindo a etapa de destilação extrativa de uma unidade de extração de butadieno a partir de uma corrente de hidrocarbonetos na faixa de quatro átomos de carbono, através da adição do solvente n-metil-2- pirrolidona (NMP). Os resultados obtidos foram comparados e validados com dados de processo obtidos por uma unidade industrial de extração de butadieno. O aprofundamento nos conceitos do processo de separação através de uma ferramenta em simulador de processo capaz de predizer condições de operação permitiu avaliações de aumento de capacidade. A capacidade dos elementos internos dos equipamentos envolvidos na separação pode ser avaliada e a identificação do ponto inicial de engargalamento da unidade foi possível. O procedimento proposto também permite reduzir incertezas para identificação de novos pontos de engargalamento a partir de uma nova configuração dos elementos internos identificados como ineficientes com a elevação de carga processada. / The purpose of this study was the development of a model using a commercial process simulator software in order to reproduce the extractive distillation step of a butadiene extraction unit from a hydrocarbon stream by the addition of the solvent n- methyl-2-pyrrolidone (NMP). The results obtained from the simulations were compared with process data from an operational butadiene extraction unit. The knowledge of the separation process due the model should predict operating conditions allowing revamps on the actual asset. The internals capacity for the equipment involved in the separation could be evaluated and units bottlenecks points should be identified.

O uso de asfaltos modificados com polímeros tem crescido significativamente nas últimas décadas em função do aumento da densidade de tráfego, da carga por eixo nos veículos e da pressão dos pneus. Estes ligantes proporcionam o aumento a vida útil e a redução do custo de manutenção das rodovias. Os polímeros mais utilizados na modificação de asfalto são os copolímeros em bloco de estireno-butadienoestireno. Esta tese avaliou os efeitos de diferentes agentes compatibilizantes (óleos) e agentes de ligação no comportamento reológico de misturas asfálticas modificadas com copolímeros de estireno-butadieno-estireno, bem como a influência da sua estrutura, se linear ou radial. Para isto foram realizados análises convencionais e testes em reômetro de cisalhamento dinâmico. Os dados obtidos permitiram evidenciar a eficácia do óleo de xisto como agente compatibilizante, proporcionando excelente dispersão do polímero na matriz asfáltica e estabilidade a estocagem a altas temperaturas. Este óleo apresenta-se como uma opção tecnicamente viável para o óleo aromático atualmente em uso no mercado. Foi também verificado que o uso de enxofre como agente de ligação tem um efeito altamente positivo nas propriedades do ligante modificado, com significativa redução da tan ō, da deformação após aplicação de cargas cíclicas e elevação do módulo complexo, o que contribui para obtenção de pavimentos com maior resistência a deformação e ao trincamento por fadiga. / The use of polymer modified asphalts has grown significantly in the last decades due to the increase in traffic density, axle loading in vehicles and tyre pressure. These binders favor the increase of pavement life and the reduction of its maintenancement costs. The most used polymer for asphalt modification is styrene-butadiene-styrene blocked copolymers. This thesis evaluated the effects of different compatibilizers and crosslinkers on rheological behavior of styrene-butadiene-styrene copolymer modified asphalt binders, as well as the influence of its structure, linear or radial. Binder’s characteristics were determined by conventional analysis and tests in dinamic shear rheometer. Data obtained provided evidence of the positive effect of sulfur as crosslinker in modified binders properties, with high tan ō reduction, complex modulus increase and deformation reduction after application of cyclic loads, characteristics that turn possible the existence of pavements with greater rutting and fatigue resistance. It was also verified the shale oil efficacy as a compatibilizer agent, providing an excellent polymer dispersion inside asphalt matrix and a stable storage binder at high temperatures. This oil can be considered as a technical available option to aromatic oil presently in use at pavement industry.

O óleo extensor normalmente empregado em copolímeros à base de butadieno e estireno ( borracha SBR) da série 1712 é o extrato aromático (DAE). Nesta Dissertação, esse óleo foi substituído por óleos com baixos teores de policíclicos aromáticos em formulações de SBR. Esta substituição se deu em atendimento a Regulamentação REACH (EC No1907/2006 do Parlamento Europeu e do Conselho de 18 de Dezembro de 2006, Anexo XVII) que determina que a soma de hidrocarbonetos policíclicos aromáticos individuais (PAHs) deve ser abaixo de 10 mg/kg e o teor de benzo(a)pireno (BaP) não deve exceder 1 mg/kg. Os óleos empregados foram o extrato aromático residual tratado (TRAE) e dois óleos naftênicos de fornecedores diferentes (HN1 e HN2). As composições de SBR estendidas em DAE, TRAE, HN1 e HN2 tiveram suas propriedades térmicas avaliadas por análise termogravimétrica (TG) e calorimetria diferencial de varredura (DSC). As propriedades físicas foram determinadas por ensaios de tração, dureza, resistência à abrasão e resiliência. Foram ainda avaliadas as propriedades reométricas e reológicas, por viscosidade e relaxação Mooney, respectivamente. Ao final os resultados demonstraram que é possível a substituição do óleo extensor por quaisquer dos óleos testados sem prejuízos nas propriedades estudadas / The extender oil usually employed in compositions of rubbers based on sytrene and butadiene (SBR) 1712 is the aromatic extract DAE. In this Dissertation, this oil was substituted by oils with low levels of polycyclic aromatic hydrocarbons: the treated residual aromatic extract (TRAE) and two naphthenic oils from different suppliers (HN1 and HN2). This substitution was performed in response to REACH Regulation (EC No1907/2006 European Parliament and the Council of 18 December 2006, Annex XVII) which state that the sum of individual polycyclic aromatic hydrocarbons (PAHs) should be below 10 mg / kg and the levels of benzo (a) pyrene (BaP) should not exceed 1 mg / kg. SBR compositions extended with DAE, TRAE, HN1 and HN2 were characterized in terms of thermal properties by thermogravimetry (TG) and differential scanning calorimetry (DSC), rheometric properties, physical properties (tension tests, hardness, abrasion resistance and resilience) and rheological (viscosity and Mooney relaxation). The final results showed that it is possible to replace the extender oil DAE for any of the tested oils without loss in the studied properties

This study investigates the rate kinetics for BD and PGMEA oxidation by UV/O3 process. The reactor constructs of a 100 cm x 20 cm x 85 cm (L x W x H) stainless steel chamber, in which four vertical steel plates (20 cm x 65 cm, W x H) were inserted to establish a plug flow path for the flowing gas. The reactor has a total effective volume of 170 L. Each of the five compartments of the reactor is equipped with an individual UV irradiation system with a 3.0-cm x 15-cm (ID x L) quartz sheath that housed an UV lamp, and two electric UV power inputs of 0.147 or 0.294 W/L were obtained. The gas flows perpendicularly to the UV lamps in the reactor. The influent tested VOC concentration was adjusted to about 50 ppm, and the gas flows were controlled at the individual flow rate of 60 and 120 L/min. The effects of moisture content (relative humidity, RH), ozone dosage (initial molar ratio of ozone to the tested VOC, m) and UV volumetric electric power input on the removal of the tested VOCs are investigated in the study. Also, kinetic models of the tested VOCs by photolysis, ozonation and UV/O3 have been developed and confirmed with reference to the experimental data. According to the kinetic models, both photolysis rate and oxidation rate by UV/O3 are following the first order behavior with respect to the tested VOC concentrations which are low. The result reveals the absorbance for the reactions is weak absorbance under UV irradiation. The reaction rates are proportional to the UV electric power inputs in UV-initiated reactions. And the parameter, £i, which represents the ratio of OH radical consumption rate by the tested VOC to the total OH radical consumption rate, can be obtained by simulating the performance of experimental data of OH reactions. The experimental results reveal that for BD oxidation with a gas space time of 85 sec and RH = 40 ¡V 99%, BD photolysis did not occur at wavelength of 185 nm with UV electric power inputs of 0.147 and 0.294 W/L. The ozonation efficiency of BD reached 90% at m = 3.5, and RH had no influence on the removal efficiency of BD. The removal efficiencies by UV/O3 process reached 90% with m = 2.2 and 1.6 for UV power inputs of 0.147 and 0.294 W/L, respectively. The addition of ozone apparently encouraged BD removal efficiency by UV/O3 process. And the enhancement of ozone dosage (m = 0.5 ¡V 4.4) would promote the decomposition of BD more effectively than the enhancements of UV power input (from 0.147 to 0.294 W L-1) and RH (from 40 to 99%). For PGMEA photolysis in a batch reactor with volume of 1.188 L, the photolysis occurred at wavelength of 185 nm under UV irradiation. And the photolysis rate follows the first order behavior with respect to the concentration of PGMEA. But PGMEA photolysis did not occurred at UV wavelength of 254 nm. PGMEA ozonation was performed in the same batch reactor; and the removal efficiency of only 50% at m = 3.96 would take 35 min. So, PGMEA ozonation in the plug flow reactor did not be observed at the conditions of the gas space time of 85 sec and RH = 15 ¡V 99%. Besides, the photolysis of PGMEA was carried out at the above conditions. The removal efficiency of PGMEA by UV/O3 could reach 90% at the conditions of the gas space time of 170 sec, UV volumetric electric power input of 0.294 W/L and m = 2.9. And the enhancement of UV power input (from 0.147 to 0.294 W L-1) would promote the decomposition of PGMEA more effectively than the addition of ozone dosage (m = 1.05 ¡V 15.63) and RH = 15 ¡V 99%.

Μελετήθηκε το φαινόμενο της ηλεκτροχημικής ενίσχυσης για τις αντιδράσεις της εκλεκτικής υδρογόνωσης του ακετυλενίου προς αιθυλένιο σε καταλύτη Pd εναποτεθειμένο σε β\"-Al2O3 και της οξείδωσης του βουταδιενίου προς προϊόντα εκλεκτικής οξείδωσης σε καταλύτη Ag0.73V2O5.365 εναποτεθειμένο σε YSZ. Το φαινόμενο της ηλεκτροχημικής ενίσχυσης (Electrochemical Promotion) αφορά την τροποποίηση της ενεργότητας καταλυτών που είναι εναποτεθειμένοι πάνω σε στερεούς ηλεκτρολύτες κατά την επιβολή δυναμικού στη διεπιφάνεια καταλύτη | στερεού ηλεκτρολύτη. Στην παρούσα διατριβή μελετήθηκαν αντιδράσεις βιομηχανικού ενδιαφέροντος σε συνθήκες παρόμοιες με αυτές της βιομηχανικής πρακτικής. Υδρογόνωση Ακετυλενίου: Βρέθηκε ότι η αύξηση της κάλυψης της καταλυτικής επιφάνειας με ιόντα Na+ έχει σαν αποτέλεσμα την σημαντική αύξηση της εκλεκτικότητας προς αιθυλένιο. Το φαινόμενο είναι πλήρως αντιστρεπτό δηλαδή η απομάκρυνση των ιόντων Na+ από την καταλυτική επιφάνειας έχει σαν συνέπεια την επιστροφή των καταλυτικών ρυθμών στους αρχικούς που αντιστοιχούν σε επιφάνεια καθαρή από ιόντα Na+. Ο ηλεκτροχημικά ενισχυμένος καταλύτης της παρούσας βρέθηκε ότι είναι πιο εκλεκτικός (κατά 1.5%) σε σχέση με τον βιομηχανικό καταλύτη για υψηλή μετατροπή ακετυλενίου Εκλεκτική οξείδωση βουταδιενίου: Βρέθηκε ότι είναι δυνατή η ηλεκτροχημική ενίσχυση της οξείδωσης τόσο του αιθυλενίου, η οποία εξετάστηκε ως αντίδραση “μοντέλο”, όσο και του βουταδιενίου με χρήση ενός μη αγώγιμου οξειδοαναγωγικού καταλύτη όπως αυτού της παρούσας μελέτης. Η επιβολή θετικών δυναμικών δηλαδή η μεταφορά ιόντων οξυγόνου στην καταλυτική επιφάνεια έχει σαν αποτέλεσμα της αύξηση των καταλυτικών ρυθμών για τα περισσότερα προϊόντα εκλεκτικής οξείδωσης ενώ μικρότερες αυξήσεις παρατηρούνται κατά την επιβολή αρνητικών δυναμικών. Βρέθηκε επίσης ότι η οξειδωτική κατάσταση του καταλύτη επηρεάζει σημαντικά τόσο την κατανομή των προϊόντων όσο και το μέγεθος της ηλεκτροχημικής ενίσχυσης. / The phenomenon of Electrochemical Promotion was studied for two catalytic reactions of industrial importance: for the hydrogenation of acetylene on Pd catalytic films deposited on β\"-Al2O3 solid electrolyte and for the selective oxidation of butadiene on Ag0.73V2O5.365, industrial catalyst, deposited on YSZ solid electrolyte. The Electrochemical Promotion concerns the modification of catalytic activity and selectivity of conductive catalysts deposited on solid electrolytes by applying electrical currents or potential between the catalyst and the counter electrode also deposited on the solid electrolyte. Acetylene Hydrogenation: It was found that the selectivity to C2H4 is significantly enhanced upon increasing the coverage of catalytic surface with electrochemically supplied sodium ions. The phenomenon is reversible that is the electrochemical removing of sodium ions from the catalytic surface results to the return of catalytic activity and selectivity at the initial values corresponding to the unpromoted catalyst. The electrochemical promoted catalyst appears to be more selective (by 1.5%) than the industrial catalyst in the high acetylene conversion region Selective Oxidation of Butadiene: It was found that both ethylene oxidation, which is studied as “model” reaction and selective oxidation of butadiene can be enhanced electrochemically on a non conductive redox catalyst. It was found that the oxygen species, which are carried electrochemically from YSZ solid electrolyte to the catalytic surface, by applying positive potential or current, enhance the catalytic rates for all partial oxidation products. Minor increases to the catalytic rates observed by applying negative potential or current. It was also found that the oxidation state of catalyst affects significantly both the reaction rates and the magnitude of electrochemical promotion.

En aquesta tesi, proposem la fabricació y la caracterització d’un microconcentrador de gasos, per ser acoblat amb un microsistema de detecció, per millorar el seu límit de detecció davant els gasos tòxics. Aquest estudi s’aplica especialment al benzè, que es un compost d’alta cancerigenitat. El preconcentrador proposat esta basat en estructura plana, que, es una opció de fabricació més simple y permet una millor aïllament tèrmic amb el resta d’unitats del microsistema, qu’els estructures 3D proposats a la literatura. No obstant, els factors de concentració obtinguts amb l’estructura plana queden generalment més baixos, per causa de la menor quantitat de material absorbent que pot acollir. En aquesta tesis, es va superar aquest problema mitjançant l’utilització del carboní actiu, un adsorbent d’alta capacitat d’adsorció, així com l’optimització de les condicions de funcionament del dispositiu. Finalment, acoblant el microconcentrador amb un micro-cromatògraf, vam aconseguir una detecció sensible y selectiva del benzè en barreja amb altres volàtils a l’aire. / The present thesis focuses on the fabrication and characterization of a gas microconcentrator for to be coupled with a detection microsystem, in order to lower its detection limit towards toxic gases and vapours in contaminated areas. This study was more especially applied to the preconcentration of benzene, a cancerigenic compound at low ppb level. A preconcentrator based on a planar structure was proposed regarding its simpler fabrication, better thermal insulation and lower power consumption, compared to the 3D structures proposed conventionally in literature. In order to obtain higher concentration factors with such structure, its small size was compensated by using a high adsorption capacity adsorbent such as activated carbon as well as the optimization of the preconcentration conditions of the device. Finally, the microconcentrator was validated as injection unit when coupled with a microchromatographic system, where a sensitive and selective analysis of benzene in mixture with other VOCs was achieved.

A construção de um analisador virtual é sustentada basicamente por três pilares: o modelo, as variáveis que integram o modelo e a estratégia de correção/atualização do modelo. Os modelos matemáticos são classificados quanto ao nível de conhecimento do processo contido nele, indo de modelos complexos baseados em relações fundamentais e leis físico-químicas, denominados white-box, até modelos obtidos através de técnicas de análise multivariável, como técnicas de regressão multiváriavel e redes neurais, referenciados como black box. O presente trabalho objetiva uma análise de dois dos pilares: os modelos, focando em modelos obtidos através das técnicas de redução de dimensionalidade do tipo PLS, e metodologias de seleção de variáveis para a construção dessa classe de modelos. Primeiramente é realizada uma revisão das principais variantes lineares e não lineares da metodologia PLS, compreendendo desde o seu desenvolvimento até a sua combinação com redes neurais. Posteriormente são apresentadas algumas das técnicas popularmente utilizadas para a seleção de variáveis em modelos do tipo black-box, técnicas de validação cruzada e técnicas de seleção de dados para calibração e validação de modelos. São propostas novas abordagens para os procedimentos de seleção de variáveis, originadas da combinação das técnicas de seleção de dados com duas metodologias de seleção de variáveis. Os resultados produzidos por essas novas abordagens são comparados com o método clássico através de casos lineares e não lineares. A viabilidade das técnicas analisadas e desenvolvidas é verificada através da aplicação das mesmas no desenvolvimento de um analisador virtual para uma coluna de destilação simulada através do simulador dinâmico Aspen Dynamics®. Por fim são apresentadas as etapas e desafios da implementação de um analisador virtual baseados em técnicas PLS em uma Torre Depropanizadora de uma central de matérias primas de um pólo petroquímico. / The construction of a virtual analyzer is sustained basically by three pillars: the model, the variables that integrate the model and the updating strategy of the model. The mathematical models are classified with relationship at the level of the process knowledge within it, going from complex models, based on fundamental relationships and physical-chemistries laws, called white-box, until models obtained through multivariable analysis techniques, as multiple linear regression and neural networks, also called as black box. The focus of the present work is the analysis of two of the pillars: the models, specially the ones obtained by dimension reduction techniques, like PLS, and methodologies used in the development of this class of models. Initially, a revision of the main linear and non linear variants of the PLS methodology is done, embracing since its development to its combination with neural networks. Later on, some popularly variables selection techniques for black-box models are explained, as well as some cross validation techniques and strategies for data selection for calibration and validation of models. New approaches for variables selection procedures are proposed, originated by the combination of data selection strategies and two variables selection techniques. The results produced by those new approaches are compared with the classic method through linear and non linear case studies. The viability of the analyzed and developed techniques is verified through the application of the same ones in the development of a virtual analyzer for a distillation column, simulated by the dynamic simulator Aspen Dynamics®. The steps and challenges faced in the implementation of a virtual analyzer based on PLS technical for a Depropanizer Unit are finally presented.