942 resultados para SOLID-LIQUID EQUILIBRIUM


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We reported the first application of in situ shell-isolated nanoparticle enhanced Raman spectroscopy (SHINERS) to an interfacial redox reaction under electrochemical conditions. We construct gap-mode sandwich structures composed of a thiol-terminated HS-6V6H viologen adlayer immobilized on a single crystal Au(111)-(1x1) electrode and covered by Au(60 nm)@SlO(2) core shell nanoparticles acting as plasmonic antennas. We observed high-quality, potential-dependent Raman spectra of the three viologen species V(2+),V(+center dot) and V(0) on a well-defined Au(111) substrate surface and could map their potential-dependent evolution. Comparison with experiments on powder samples revealed an enhancement factor of the nonresonant Raman modes of similar to 3 x 10(5), and up to 9 x 10(7) for the resonance modes. The study illustrates the unique capability of SHINERS and its potential in the entire field of electrochemical surface science to explore structures and reaction pathways on well-defined substrate surfaces, such as single crystals, for molecular, (electro-)- catalytic, bioelectrochemical systems up to fundamental double layer studies at electrified solid/liquid interfaces.

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Biological homochirality on earth and its tremendous consequences for pharmaceutical science and technology has led to an ever increasing interest in the selective production, the resolution and the detection of enantiomers of a chiral compound. Chiral surfaces and interfaces that can distinguish between enantiomers play a key role in this respect as enantioselective catalysts as well as for separation purposes. Despite the impressive progress in these areas in the last decade, molecular-level understanding of the interactions that are at the origin of enantiodiscrimination are lagging behind due to the lack of powerful experimental techniques to spot these interactions selectively with high sensitivity. In this article, techniques based on infrared spectroscopy are highlighted that are able to selectively target the chiral properties of interfaces. In particular, these methods are the combination of Attenuated Total Reflection InfraRed (ATR-IR) with Modulation Excitation Spectroscopy (MES) to probe enantiodiscriminating interactions at chiral solid-liquid interfaces and Vibrational Circular Dichroism (VCD), which is used to probe the structure of chirally-modified metal nanoparticles. The former technique aims at suppressing signals arising from non-selective interactions, which may completely hide the signals of interest due to enantiodiscriminating interactions. Recently, this method was successfully applied to investigate enantiodiscrimination at self-assembled monolayers of chiral thiols on gold surfaces. The nanometer size analogues of the latter--gold nanoparticles protected by a monolayer of a chiral thiol--are amenable to VCD spectroscopy. It is shown that this technique yields detailed structural information on the adsorption mode and the conformation of the adsorbed thiol. This may also turn out to be useful to clarify how chirality can be bestowed onto the metal core itself and the nature of the chirality of the latter, which is manifested in the metal-based circular dichroism activity of these nanoparticles.

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We have studied Au(55 nm)@SiO2 nanoparticles (NPs) on two low-index phases of gold and platinum single crystal electrodes in ClO4– and SO42– ion-containing electrolytes by both electrochemical methods and in-situ shell-isolated nanoparticle enhanced Raman spectroscopy (SHINERS). We showed the blocking of the electrode with surfactants originating from the synthesis of as-prepared SHINERS NPs. We introduce an efficient procedure to overcome this problem, which provides a fundamental platform for the application of SHINERS in surface electrochemistry and beyond. Our method is based on a hydrogen evolution treatment of the SHINERS-NP-modified single-crystal surfaces. The reliability of our preparation strategy is demonstrated in electrochemical SHINERS experiments on the potential-controlled adsorption and phase formation of pyridine on Au(hkl) and Pt(hkl). We obtained high-quality Raman spectra on these well-defined and structurally carefully characterized single-crystal surfaces. The analysis of the characteristic A1 vibrational modes revealed perfect agreement with the interpretation of single-crystal voltammetric and chronoamperometric experiments. Our study demonstrates that the SHINERS protocol developed in this work qualifies this Raman method as a pioneering approach with unique opportunities for in situ structure and reactivity studies at well-defined electrochemical solid/liquid interfaces.

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Employing a scanning tunneling microscopy based beak junction technique and mechanically controlled break junction experiments, we investigated tolane (diphenylacetylene)-type single molecular junctions having four different anchoring groups (SH, pyridyl (PY), NH2, and CN) at a solid/liquid interface. The combination of current–distance and current–voltage measurements and their quantitative statistical analysis revealed the following sequence for junction formation probability and stability: PY > SH > NH2 > CN. For all single molecular junctions investigated, we observed the evolution through multiple junction configurations, with a particularly well-defined binding geometry for PY. The comparison of density functional theory type model calculations and molecular dynamics simulations with the experimental results revealed structure and mechanistic details of the evolution of the different types of (single) molecular junctions upon stretching quantitatively.

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The Effingen Member is a low-permeability rock unit of Oxfordian age (ca. 160 Ma) that occurs across northern Switzerland. It comprises sandy calcareous marls and (argillaceous) limestones. This report describes the hydrogeochemistry, mineralogy and supporting physical properties of the Effingen Member in three boreholes in the Jura-Südfuss area: Oftringen, Gösgen and Küttigen, where it is 220–240 m thick. The top of the Effingen Member is at 420, 66 and 32 m depths at the three sites. Core materials are available from Oftringen and Gösgen, whereas information from Küttigen is limited to cuttings, in-situ hydrogeological testing and geophysical logging. Hydrogeological boundaries of the Effingen Member vary between locations. Ground-water flows were identified during drilling at the top (Geissberg Member), but not at the base, of the Effingen Member at Oftringen, at the base (Hauptrogenstein Formation) of the Effingen Member at Gösgen, and in a limestone layer (Gerstenhübel unit) within the Effingen Member at Küttigen. The marls and limestones of the Effingen Member have carbonate contents of 46–91 wt.-% and clay-mineral contents of 5–37 wt.-%. Pyrite contents are up to 1.6 wt.-%, but no sulphate minerals were detected by routine analyses. Clay minerals are predominantly mixed-layer illite-smectite, illite and kaolinite, with sporadic traces of chlorite and smectite. Veins filled with calcite ± celestite occur through the Effingen Member at Oftringen but not at Gösgen or Küttigen. They formed at 50–70 ºC from externally derived fluids, probably of Miocene age. Water contents are 0.7–4.2 wt.-%, corresponding to a water-loss porosity range of 1.9–10.8 vol.-%. Specific surface areas, measured by the BET method, are 2–30 m2/g, correlating with clay-mineral contents. Water activity has been measured and yielded surprisingly low values down to 0.8. These cannot be explained by pore-water salinity alone and include other effects, such as changes in the fabric due to stress release or partial saturation. Observed variations in measurements are not fully understood. Cation exchange capacity (CEC) and exchangeable cation populations have been studied by the Ni-en method. CEC, derived from the consumption of the index cation Ni, is 9–99 meq/kgrock at a solid:liquid ratio of 1, correlating with the clay-mineral content. Cation concentrations in Ni-en extract solutions are in the order Na+≥Ca2+>Mg2+>K+>Sr2+. However, the analytical results from the Ni-en extractions have additional contributions from cations originating from pore water and from mineral dissolution reactions that occurred during extraction, and it was not possible to reliably quantify these contributions. Therefore, in-situ cation populations and selectivity coefficients could not be derived. A suite of methods have been used for characterising the chemical compositions of pore waters in the Effingen Member. Advective displacement was used on one sample from each Oftringen and Gösgen and is the only method that produces results that approach complete hydrochemical compositions. Aqueous extraction was used on core samples from these two boreholes and gives data only for Cl- and, in some cases, Br-. Out-diffusion was used on core samples from Oftringen and similarly gives data for Cl- and Br- only. For both aqueous extraction and out-diffusion, reaction of the experimental water with rock affected concentrations of cations, SO42 and alkalinity in experimental solutions. Another method, centrifugation, failed to extract pore water. Stable isotope ratios (δ18O and δ2H) of pore waters in core samples from Oftringen were analysed by the diffusive exchange method and helium contents of pore water in Oftringen samples were extracted for mass spectrometric analysis by quantitative outgassing of preserved core samples. Several lines of evidence indicate that drillcore samples might not have been fully saturated when opened and subsampled in the laboratory. These include comparisons of water-loss porosities with physical porosities, water-activity measurements, and high contents of dissolved gas as inferred from ground-water samples. There is no clear proof of partial saturation and it is unclear whether this might represent in-situ conditions or is due to exsolution of gas due to the pressure release since drilling. Partial saturation would have no impact on the recalculation of pore-water compositions from aqueous extraction experiments using water-loss porosity data. The largest uncertainty in the pore-water Cl- concentrations recalculated from aqueous extraction and out-diffusion experiments is the magnitude of the anion-accessible fraction of water-loss porosity. General experience of clay-mineral rich formations suggests that the anion-accessible porosity fraction is very often about 0.5 and generally in a range of 0.3 to 0.6 and tends to be inversely correlated with clay-mineral contents. Comparisons of the Cl- concentration in pore water obtained by advective displacement with that recalculated from aqueous extraction of an adjacent core sample suggests a fraction of 0.27 for an Oftringen sample, whereas the same procedure for a Gösgen sample suggests a value of 0.64. The former value for anion-accessible porosity fraction is presumed to be unrepresentative given the local mineralogical heterogeneity at that depth. Through-diffusion experiments with HTO and 36Cl- suggest that the anion-accessible porosity fraction in the Effingen Member at Oftringen and Gösgen is around 0.5. This value is proposed as a typical average for rocks of the Effingen Member, bearing in mind that it varies on a local scale in response to the heterogeneity of lithology and pore-space architecture. The substantial uncertainties associated with the approaches to estimating anion-accessible porosity propagate into the calculated values of in-situ pore-water Cl- concentrations. On the basis of aqueous extraction experiments, and using an anion-accessible porosity fraction of 0.5, Cl- concentrations in the Effingen Member at Oftringen reach a maximum of about 14 g/L in the centre. Cl- decreases upwards and downwards from that, forming a curved depth profile. Cl- contents in the Effingen Member at Gösgen increase with depth from about 3.5 g/L to about 14 g/L at the base of the cored profile (which corresponds to the centre of the formation). Out-diffusion experiments were carried out on four samples from Oftringen, distributed through the Effingen Member. Recalculated Cl- concentrations are similar to those from aqueous extraction for 3 out of the 4 samples, and somewhat lower for one sample. Concentrations of other components, i.e. Na+, K+, Ca2+, Mg2+, Sr2+, SO42- and HCO3- cannot be obtained from the aqueous extraction and out-diffusion experimental data because of mineral dissolution and cation exchange reactions during the experiments. Pore-water pH also is not constrained by those extraction experiments. The only experimental approach to obtain complete pore-water compositions for samples from Oftringen and Gösgen is advective displacement of pore water. The sample from Oftringen used for this experiment is from 445 m depth in the upper part of the Effingen Member and gave eluate with 16.5 g/L Cl- whereas aqueous extraction from a nearby sample indicated about 9 g/L Cl-. The sample from Gösgen used for advective displacement is from 123 m depth in the centre of the Effingen Member sequence and gave eluate with about 9 g/L Cl- whereas aqueous extraction gave 11.5 g/L Cl-. In both cases the pore waters have Na-(Ca)-Cl compositions and SO42- concentrations of about 1.1 g/L. The Gösgen sample has a Br/Cl ratio similar to that of sea water, whereas this ratio is lower for the Oftringen sample. Taking account of uncertainties in the applied experimental approaches, it is reasonable to place an upper limit of ca. 20 g/L on Cl- concentration for pore water in the Effingen Member in this area. There are major discrepancies between pore-water SO42- concentrations inferred from aqueous extraction or out-diffusion experiments and those obtained from advective displacement in both the Oftringen and Gösgen cases. A general conclusion is that all or at least part of the discrepancies are attributable to perturbation of the sulphur system and enhancement of SO42- by sulphate mineral dissolution and possibly minor pyrite oxidation during aqueous extraction and out-diffusion. Therefore, data for SO42- calculated from those pore-water sampling methods are considered not to be representative of in-situ conditions. A reference pore-water composition was defined for the Effingen Member in the Jura Südfuss area. It represents the probable upper limits of Cl- contents and corresponding anion and cation concentrations that are reasonably constrained by experimental data. Except for Cl- and possibly Na+ concentrations, this composition is poorly constrained especially with respect to SO42- and Ca2+ concentrations, and pH and alkalinity. Stable isotope compositions, δ18O and δ2H, of pore waters in the Effingen Member at Oftringen plot to the right of the meteoric water line, suggesting that 18O has been enriched by water-rock exchange, which indicates that the pore waters have a long residence time. A long residence time of pore water is supported by the level of dissolved 4He that has accumulated in pore water of the Effingen Member at Oftringen. This is comparable with, or slightly higher than, the amounts of 4He in the Opalinus Clay at Benken. Ground waters were sampled from flowing zones intersected by boreholes at the three locations. The general interpretation is that pore waters and ground-water solutes may have similar origins in Mesozoic and Cenozoic brackish-marine formations waters, but ground-water solutes have been diluted rather more than pore waters by ingress of Tertiary and Quaternary meteoric waters. The available hydrochemical data for pore waters from the Effingen Member at these three locations in the Jura-Südfuss area suggest that the geochemical system evolved slowly over geological periods of time, in which diffusion was an important mechanism of solute transport. The irregularity of Cl- and δ18O profiles and spatial variability of advective ground-water flows in the Malm-Dogger system suggests that palaeohydrogeological and hydrochemical responses to changing tectonic and surface environmental conditions were complex.

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Photopolymerized hydrogels are commonly used for a broad range of biomedical applications. As long as the polymer volume is accessible, gels can easily be hardened using light illumination. However, in clinics, especially for minimally invasive surgery, it becomes highly challenging to control photopolymerization. The ratios between polymerization- volume and radiating-surface-area are several orders of magnitude higher than for ex-vivo settings. Also tissue scattering occurs and influences the reaction. We developed a Monte Carlo model for photopolymerization, which takes into account the solid/liquid phase changes, moving solid/liquid-boundaries and refraction on these boundaries as well as tissue scattering in arbitrarily designable tissue cavities. The model provides a tool to tailor both the light probe and the scattering/absorption properties of the photopolymer for applications such as medical implants or tissue replacements. Based on the simulations, we have previously shown that by adding scattering additives to the liquid monomer, the photopolymerized volume was considerably increased. In this study, we have used bovine intervertebral disc cavities, as a model for spinal degeneration, to study photopolymerization in-vitro. The cavity is created by enzyme digestion. Using a custom designed probe, hydrogels were injected and photopolymerized. Magnetic resonance imaging (MRI) and visual inspection tools were employed to investigate the successful photopolymerization outcomes. The results provide insights for the development of novel endoscopic light-scattering polymerization probes paving the way for a new generation of implantable hydrogels.

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The understanding of the charge transport through single molecule junctions is a prerequisite for the design and building of electronic circuits based on single molecule junctions. However, reliable and robust formation of such junctions is a challenging task to achieve. In this topical review, we present a systematic investigation of the anchoring group effect on single molecule junction conductance by employing two complementary techniques, namely scanning tunneling microscopy break junction (STM-BJ) and mechanically controllable break junction (MCBJ) techniques, based on the studies published in the literature and important results from our own work. We compared conductance studies for conventional anchoring groups described earlier with the molecular junctions formed through π-interactions with the electrode surface (Au, Pt, Ag) and we also summarized recent developments in the formation of highly conducting covalent Au–C σ-bonds using oligophenyleneethynylene (OPE) and an alkane molecular backbone. Specifically, we focus on the electron transport properties of diaryloligoyne, oligophenyleneethynylene (OPE) and/or alkane molecular junctions composed of several traditional anchoring groups, (dihydrobenzo[b]thiophene (BT), 5-benzothienyl analogue (BTh), thiol (SH), pyridyl (PY), amine (NH2), cyano (CN), methyl sulphide (SMe), nitro (NO2)) and other anchoring groups at the solid/liquid interface. The qualitative and quantitative comparison of the results obtained with different anchoring groups reveals structural and mechanistic details of the different types of single molecular junctions. The results reported in this prospective may serve as a guideline for the design and synthesis of molecular systems to be used in molecule-based electronic devices.

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El propósito de este trabajo es obtener un antioxidante natural a partir de las semillas de uva (Vitis vinifera L.), para emplear en alimentos. Para ello se compararon distintos solventes para la extracción de fenoles de las semillas de la uva, de modo de obtener el extracto más concentrado en compuestos activos con la mínima degradación de su poder antioxidante durante el proceso de obtención. La concentración de fenoles totales de los extractos se determinó por el método Folin Ciocalteu. El poder reductor de los extractos se midió empleando el método de Oyaizu. Una vez seleccionado el solvente más adecuado para la extracción, se analizó la cinética de extracción, optimizando el tiempo de tratamiento. El extracto fue concentrado al vacío, y se veríficó la conservación del poder reductor en el extracto concentrado, por el método de Oyaizu. El extracto de semillas concentrado y sin concentrar se empleó en un sistema real sujeto a oxidación, tal como el jugo de manzanas. El grado de oxidación del jugo se midió por el método de Özoglu. El extracto concentrado fue deshidratado por secado en lecho de espuma y por liofilizado. En ambos casos se verificó el efecto del tratamiento de secado sobre el poder reductor. Finalmente, se evaluó la actividad antioxidante del extracto líquido concentrado de semillas de vid, respecto de otros antioxidantes comerciales como ácido ascórbico y dióxido de azufre. El sustrato oxidable fue el jugo de manzanas, y el grado de oxidación se midió por el método de Özoglu. El análisis estadístico de los datos se realizó mediante el análisis de la varianza; cuando no fue posible emplear el mencionado análisis, debido a que no se verificaban los supuestos básicos para su aplicación, se empleó la prueba de Kruskal –Wallis. En todos los casos, se utilizó el programa Statgraphics plus ®4.0. Para obtener un extracto antioxidante a partir de semillas de vid se utilizó una ex-tracción con agua a 90ºC, durante 4 horas. La relación sólido- líquido empleada fue de 1g de semillas enteras por 10 ml de solvente. El extracto obtenido presentaba una concentración de 12,587 mg de fenoles totales por gramo de semillas de uva extractadas y un poder reductor de 1,290 unidades. Como consecuencia del análisis de la cinética de extracción, el tiempo de tratamiento se redujo de 4 horas a 3 horas. La concentración del extracto se realizó al vacío a 60ºC, verificándose un aumen-to del poder reductor en el extracto concentrado, comprobado sobre jugo de manzanas. Comparando el extracto concentrado y el extracto sin concentrar se observa que la concentración de fenoles totales aumentó 29,57 veces, mientras que el poder reductor aumentó 37,39 veces. El deshidratado del extracto por medio del lecho de espuma permitió conservar el poder reductor del mismo, no ocurrió lo mismo en el deshidratado por liofilizado, donde se produjo un deterioro del poder reductor. Para un mismo contenido de fenoles totales agregado al jugo de manzanas, el ex-tracto líquido sin concentrar produjo un 28,4% de inhibición de la oxidación, mientras que el de extracto líquido concentrado produjo un 51,5 % de inhibición de la oxidación del jugo de manzanas. El extracto de semillas de vid, aplicado como antioxidante en jugo de manzanas, inhibió el desarrollo de la oxidación en un 31,51%, considerando 24 horas el tiempo de tratamiento. Este desempeño supera al ácido ascórbico, que en iguales condiciones, inhibió el desarrollo de la oxidación en un 2,6%. Pero en las condiciones de tra-bajo, el dióxido de azufre resulta mejor antioxidante que ambos, ya que logró inhibir el desarrollo de la oxidación en un 97,40 %.

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Some floating-liquid-zone experiments performed under reduced-gravity conditions are reviewed. Several types of instabilities are discussed, together with the relevant parameters controlling them. It is shown that the bounding values of these parameters could be increased, by orders of magnitude in several instances, by selecting appropriate liquids. Two of the many problems that a Fluid-Physics Module, devised to perform experiments on floating zones in a space laboratory, would involve are discussed: namely (i) procedures for disturbing the zoneunder controlled conditions, and (ii) visualisation of the inner flow pattern. Several topics connected with the nonisothermal nature and the phase-changes of floating zones are presented. In particular, a mode of propagation through the liquid zone for disturbances which could appear in the melting solid/liquid interface is suggested. Although most research on floating liquid zones is aimed at improving the crystal-growth process, some additional applications are suggested.

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Granular materials, such as sand, gravel, powders, and pharmaceutical pills, are large aggregates of macroscopic, individually solid particles, or “grains.” Far from being simple materials with simple properties, they display an astounding range of complex behavior that defies their categorization as solid, liquid, or gas. Just consider how sand can stream through the orifice of an hourglass yet support one's weight on the beach; how it can form patterns strikingly similar to a liquid when vibrated, yet respond to stirring by “unmixing” of large and small grains. Despite much effort, there still is no comprehensive understanding of other forms of matter, like ordinary fluids or solids. In what way, therefore, is granular matter special, and what makes it so difficult to understand? An emerging interdisciplinary approach to answering these questions focuses directly on the material's discontinuous granular nature.

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O principal resíduo da indústria de café solúvel é a borra de café, gerada após a extração de sólidos solúveis com água, sendo usualmente queimada em caldeiras para geração de energia para a própria indústria. Entretanto, este co-produto pode conter de 15 a 20 % de óleo, componente de grande interesse na indústria alimentícia. Em paralelo, na indústria de produção de óleos vegetais o solvente frequentemente utilizado é o hexano. Contudo, por este ser um derivado de combustíveis fósseis, alternativas para sua substituição por solventes mais amigáveis ao meio ambiente, que podem ser obtidos por via biotecnológica, estão sendo estudadas. Deste modo, o objetivo principal desta dissertação de mestrado foi a viabilização técnica do emprego de solventes alcoólicos no processo de extração de óleo de borra de café proveniente da indústria de processamento de café solúvel. Foram realizadas extrações sólido-líquido em um estágio para estudar a influência das variáveis de processo temperatura (60 a 90 °C), tipo de solvente (etanol, ET ou isopropanol, IPA) e a hidratação do solvente (absoluto ou azeotrópico) nas características das fases extrato e rafinado, em termos de rendimento de extração de óleo, de ácidos clorogênicos (ACG), de carboidratos totais, teor de proteínas e índice de solubilidade de nitrogênio (ISN) da fase rafinado. Pré-tratamento enzimático ao processo de extração também foi realizado para investigar a sua atuação sobre o rendimento de extração de óleo e ACG, além do ISN das fases rafinado obtidas na temperatura de 70 °C. De forma geral, pode-se inferir que a temperatura favorece a extração de compostos lipídicos, mas a hidratação do solvente prejudica a extração destes compostos pelo aumento da polaridade do solvente. Do mesmo modo, como o ET é mais polar que o IPA, o primeiro solvente proporcionou a obtenção de menores rendimentos de extração de óleo. A temperatura de processo também influenciou a extração de ACG, a qual foi beneficiada a temperaturas mais baixas pelo aumento da polaridade dos solventes utilizados. De tal forma, que a 60 °C, nos experimentos utilizando etanol azeotrópico obteve-se os menores rendimentos de extração de óleo, porém maior rendimento de extração de ACG. O pré-tratamento enzimático apresentou diferenças significativas nas características das fases extrato e rafinado. No entanto, somente os experimentos com etanol absoluto resultaram em rendimentos de extração de óleo economicamente viáveis. De fato, será relevante um estudo mais aprofundado das variáveis de pré-tratamento enzimático para obter resultados mais expressivos em relação à extração de compostos lipídicos. Diante dos dados experimentais obtidos, conclui-se que é tecnicamente viável o emprego de solventes alcoólicos no processo de extração de óleo de borra de café. Entretanto, nota-se que as condições de processo devem ser avaliadas minuciosamente com o objetivo de se obter altos rendimentos de extração de óleo com maior teor de ACG.

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Este trabalho apresenta um estudo da solidificação de metais puros utilizando o modelo de campo de fases. O modelo é utilizado para simular a solidificação com o intuito de obter a morfologia da interface sólido-líquido sob diversas condições de transferência de calor. Foram realizados testes de validação comparando as morfologias da interface sólido-líquido obtida com as morfologias apresentadas em trabalhos anteriores para os casos bi e tridimensionais. O modelo do campo de fases adotado consiste principalmente de duas equações diferenciais: uma para calcular a variável de campo de fases e outra para calcular o campo de temperaturas. As equações foram solucionadas numericamente para um oitavo do domínio devido a simetria do problema. Os cálculos do modelo indicam que um sólido esférico com um raio inicial menor que o raio crítico de nucleação refunde. Entretanto uma esfera de raio maior cresce. Quando o sólido inicial cresce em uma malha numérica relativamente grosseira, a forma do sólido desvia da forma esférica devido perturbações na interface sólido-líquido. Quando a malha é refinada, as perturbações não são detectadas; contudo, quando introduzidas artificialmente as perturbações crescem e distorcem o formato esférico.

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Os equipamentos elétricos e eletrônicos (EEE) possuem uma grande importância na sociedade contemporânea, e estão presentes no cotidiano das pessoas de forma ubíqua. Com o aumento no consumo de EEE juntamente com a obsolescência precoce, surge um novo tipo de resíduo, chamado de Resíduos de Equipamentos Elétricos e Eletrônicos (REEE). Os REEE não devem ser descartados em aterros, pelo risco de contaminação e pelo desperdício de material. Assim, a reciclagem se faz necessária. As placas de circuito impresso (PCI) estão presentes na grande maioria do REEE e contem a maior variedade de metais, incluindo metais valiosos como Au, Ag, Pt e Cu. A complexidade torna a reciclagem destas placas muito difícil. Rotas hidrometalúrgicas tem surgido como uma alternativa mais limpa para o tratamento de PCI, em detrimento aos processos pirometalúrgicos. Nas rotas hidrometalúrgicas, os metais são extraídos pela lixiviação realizada por ácidos ou bases. O efeito ultrassônico tem sido empregado na síntese de novas substâncias e também em alguns casos no tratamento de resíduos. O processo central no uso de ultrassom é a cavitação acústica, capaz de produzir microbolhas na solução com temperatura da ordem de 5000 K e pressão de 500 atm localmente. Além disto, a implosão das bolhas de cavitação em meio heterogêneo causa um jato de solução na superfície, que pode alcançar velocidade de 100 m.s-1. Assim, esta tese tem como objetivo a investigação do efeito do ultrassom sobre PCI obsoletas. Dois efeitos foram investigados: o efeito da cominuição das PCI promovido pela cavitação e a influência da cavitação na lixiviação com ácido sulfúrico de Fe, Al e Ni. Os parâmetros investigados na cominuição foram: tipo de placa, granulometria da placa moída e potência de ultrassom. Os parâmetros de lixiviação avaliados foram: razão sólido-líquido (S/L), concentração de ácido e potência de ultrassom. Também foram realizados ensaios de lixiviação sonicados com meio oxidante. Foi feita a análise cinética para se determinar qual é o controle da reação de lixiviação.

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Ao longo dos últimos anos, o crescimento ao acesso a esse tipo de tecnologia pelos consumidores brasileiros tem intensificado o aumento no interesse ambiental e econômico dos LCDs. Os displays de cristal líquido são utilizados em televisores, calculadoras, telefones celulares, computadores (portáteis e tablets), vídeo games entre outros equipamentos eletrônicos. O avanço tecnológico neste campo tem tornado estes aparelhos obsoletos cada vez mais rápido, aumentando o volume de resíduos de LCDs a ser dispostos em aterros o que contribui para a redução da sua vida útil. Neste contexto, os LCDs provenientes de televisores de LED LCD tem se tornado uma fonte importante de resíduos de equipamentos eletroeletrônicos (REEE). Assim, torna-se essencial o desenvolvimento de métodos e processos para tratamento e reciclagem de LCDs. Deste modo, o objetivo do presente trabalho é a caracterização física e química de telas de cristal líquido provenientes de displays de televisores de LED LCDs e o estudo de uma rota hidrometalúrgica para recuperação de índio. Para tanto se utilizou técnicas de tratamento de minérios e análises físicas e químicas (separação granulométrica, perda ao fogo, visualização em lupa binocular, TGA, FRX, FT-IR) para caracterização do material e quantificação do índio antes e, após, a rota hidrometalúrgica que, por sua vez, foi realizada em reatores de bancada utilizando três agentes lixiviantes (ácido nítrico, sulfúrico e clorídrico), três temperaturas (25ºC, 40ºC e 60ºC) e quatro tempos (0,5h; 1h; 2h e 4h). Encontrou-se que a tela de cristal líquido representa cerca de 20% da massa total do display de televisores de LCD e que é composta por aproximadamente 11% em massa de polímeros e 90% de vidro + cristal líquido. Verificou-se também que há seis camadas poliméricas nas telas de cristal líquido, onde: um conjunto com 3 polímeros compõe o analisador e o polarizador, sendo que o polímero da primeira e da terceira camada de cada conjunto é triacetato de celulose e corresponde a 64% da massa de polímeros das telas. Já o polímero da segunda camada é polivinilalcool e representa 36% da massa de polímeros. Os melhores resultados obtidos nos processos de lixiviação foram com o ácido sulfúrico, nas condições de 60°C por 4h, relação sólido-líquido 1/5. Nessas condições, foi extraído em torno de 61% do índio contido tela de LCD.

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Alkaline hydroxides, especially sodium and potassium hydroxides, are multi-million-ton per annum commodities and strong chemical bases that have large scale applications. Some of them are related with their consequent ability to degrade most materials, depending on the temperature used. As an example, these chemicals are involved in the manufacture of pulp and paper, textiles, biodiesels, soaps and detergents, acid gases removal (e.g., SO2) and others, as well as in many organic synthesis processes. Sodium and potassium hydroxides are strong and corrosive bases, but they are also very stable chemicals that can melt without decomposition, NaOH at 318ºC, and KOH at 360ºC. Hence, they can react with most materials, even with relatively inert ones such as carbon materials. Thus, at temperatures higher than 360ºC these melted hydroxides easily react with most types of carbon-containing raw materials (coals, lignocellulosic materials, pitches, etc.), as well as with most pure carbon materials (carbon fibers, carbon nanofibers and carbon nanotubes). This reaction occurs via a solid-liquid redox reaction in which both hydroxides (NaOH or KOH) are converted to the following main products: hydrogen, alkaline metals and alkaline carbonates, as a result of the carbon precursor oxidation. By controlling this reaction, and after a suitable washing process, good quality activated carbons (ACs), a classical type of porous materials, can be prepared. Such carbon activation by hydroxides, known since long time ago, continues to be under research due to the unique properties of the resulting activated carbons. They have promising high porosity developments and interesting pore size distributions. These two properties are important for new applications such as gas storage (e.g., natural gas or hydrogen), capture, storage and transport of carbon dioxide, electricity storage demands (EDLC-supercapacitors-) or pollution control. Because these applications require new and superior quality activated carbons, there is no doubt that among the different existing activating processes, the one based on the chemical reaction between the carbon precursor and the alkaline hydroxide (NaOH or KOH) gives the best activation results. The present article covers different aspects of the activation by hydroxides, including the characteristics of the resulting activated carbons and their performance in some environment-related applications. The following topics are discussed: i) variables of the preparation method, such as the nature of the hydroxide, the type of carbon precursor, the hydroxide/carbon precursor ratio, the mixing procedure of carbon precursor and hydroxide (impregnation of the precursor with a hydroxide solution or mixing both, hydroxide and carbon precursor, as solids), or the temperature and time of the reaction are discussed, analyzing their effect on the resulting porosity; ii) analysis of the main reactions occurring during the activation process, iii) comparative analysis of the porosity development obtained from different activation processes (e.g., CO2, steam, phosphoric acid and hydroxides activation); and iv) performance of the prepared activated carbon materials on a few applications, such as VOC removal, electricity and gas storages.