Une des voies privilégiées pour réduire la teneur en soufre dans les essences commerciales est l'hydrodésulfuration sélective (HDS) des essences issues du procédé de FCC. Une essence étant composée d'un mélange de composés soufrés (1000 ppm) et d'oléfines (20-40%pds). Il est important de comprendre leur transformation de manière à améliorer l'HDS tout en minimisant l'hydrogénation (HYD) des oléfines. Par conséquent, la transformation de plusieurs molécules modèles soufrées (2-méthylthiophène, 3-méthylthiophène et le benzothiophène) et oléfiniques (hex-1-ène, 4-méthylpent-1-ène, 3,3-diméthylbut-1-ène et 2,3-diméthylbut-2-ène) a été étudiée dans les conditions opératoires d'HDS. Par une approche expérimentale couplée à de la modélisation cinétique, nous avons établi une échelle de réactivité entre les composés soufrés d'une part et les oléfines d'autre part. Le benzothiophène est le composé le plus réactif, mais aussi celui qui est le plus inhibiteur pour la transformation des autres composés soufrés. Concernant les oléfines, l'hex-1-ène est la plus réactive par rapport aux autres oléfines ramifiées. Lorsque ces composés sont en mélange, on constate des inhibitions mutuelles plus au moins conséquentes selon la structure des composés modèles. Ces effets qui résultent de compétitions à l'adsorption entre les molécules à la surface du catalyseur ont été modélisés et quantifiés (constantes cinétique et d'adsorption) à partir d'un modèle unique en considérant le formalisme de Langmuir-Hinshelwood. / A preferred route to reduce the sulfur content on the commercial gasoline is the selective hydrodesulfurization (HDS) process of FCC gasoline. A typical gasoline is composed by a mixture of sulfur (1000 ppm) and olefins (20-40%wt) compounds. Therefore, it is important to understand their transformation in order to improve the HDS and minimizing the olefin hydrogenation (HYD). Consequently, the transformation of various sulfur (2-methylthiophene, 3-methylthiophene and benzothiophene) and olefins (hex-1-ene, 4-methylpent-1-ene, 3,3-dimethylbut-1-ene and 2,3-dimethylbut-2-ene) has been studied under HDS operating conditions.By experimental and theoretical (kinetic modeling) approaches, a reactivity scale has been established between the sulfur compounds on one hand and olefins compounds on the other hand. The benzothiophene is the most reactive compound. However it is the most inhibitor compound for the transformation of others sulfur compounds. Regarding the olefins, the hex-1-ene is the most reactive compound among the others branched compounds. A mutual inhibition has been observed when those compounds are studied in mixture according with their structures. These effects result from competitive adsorption between the molecules on the catalyst surface. These results could be modeled and quantified (adsorption and kinetic constants) from a unique model considering the Langmuir-Hinshelwood formalism.

Ruthenium (Ru) has been theoretically considered a viable alkaline hydrogen evolution reaction electrocatalyst due to its fast water dissociation kinetics. However, its strong affinity to the adsorbed hydroxyl (OHad) blocks the active sites, resulting in unsatisfactory performance during the practical HER process. Here, we first reported a competitive adsorption strategy for the construction of SnO2 nanoparticles doped with Ru single-atoms supported on carbon (Ru SAs-SnO2/C) via atomic galvanic replacement. SnO2 was introduced to regulate the strong interaction between Ru and OHad by the competitive adsorption of OHad between Ru and SnO2, which alleviated the poisoning of Ru sites. As a consequence, the Ru SAs-SnO2/C exhibited a low overpotential at 10 mAcm􀀀2 (10 mV) and a low Tafel slope of 25 mVdec􀀀1. This approach provides a new avenue to modulate the adsorption strength of active sites and intermediates, which paves the way for the development of highly active electrocatalysts.

<p>Spray drying is a method with a high potential in the preparation of protein particles suitable for pulmonary delivery. However, surface induced denaturation of bio-molecules during atomization and subsequent drying can be substantial and it is therefore important to develop new formulation concept for concurrent encapsulation and stabilization of proteins during spray drying. Hence, with an overall objective to increase the knowledge of the formation of particulate systems for systemic administration of proteins by spray drying, the first part of this thesis, systematically investigated the particle formation by droplet size and particle size measurements. It was described how specific properties, such as the solubility and the crystallization propensity of the solute, can affect the product, e.g. the particle size, internal structures, and possibly particle density. A new method using atomic force microscopy (AFM) for the assessment of the effective particle density of individual spray-dried particles was demonstrated. In the second part, two different formulation concepts for encapsulation of protein during spray drying were developed. Both systems used non-ionic polymers for competitive adsorption and displacement of protein from the air/water interface during spray drying. The aqueous two-phase system (ATPS) of polyvinyl alcohol (PVA) and dextran, and the surface-active polymers, hydroxypropyl methylcellulose (HPMC) and triblock co-polymer (poloxamer 188) used for in situ coating, proved efficient in encapsulation of a model protein, bovine serum albumin (BSA). Inclusion of polymeric materials in a carbohydrate matrix also influenced several particle properties, such as the particle shape and the surface morphology, and was caused by changes in the chemical composition of the particle surface and possibly the surface rheology. In addition, powder performance of pharmaceutical relevance, such as dissolution and flowability, were affected.</p>

Spray drying is a method with a high potential in the preparation of protein particles suitable for pulmonary delivery. However, surface induced denaturation of bio-molecules during atomization and subsequent drying can be substantial and it is therefore important to develop new formulation concept for concurrent encapsulation and stabilization of proteins during spray drying. Hence, with an overall objective to increase the knowledge of the formation of particulate systems for systemic administration of proteins by spray drying, the first part of this thesis, systematically investigated the particle formation by droplet size and particle size measurements. It was described how specific properties, such as the solubility and the crystallization propensity of the solute, can affect the product, e.g. the particle size, internal structures, and possibly particle density. A new method using atomic force microscopy (AFM) for the assessment of the effective particle density of individual spray-dried particles was demonstrated. In the second part, two different formulation concepts for encapsulation of protein during spray drying were developed. Both systems used non-ionic polymers for competitive adsorption and displacement of protein from the air/water interface during spray drying. The aqueous two-phase system (ATPS) of polyvinyl alcohol (PVA) and dextran, and the surface-active polymers, hydroxypropyl methylcellulose (HPMC) and triblock co-polymer (poloxamer 188) used for in situ coating, proved efficient in encapsulation of a model protein, bovine serum albumin (BSA). Inclusion of polymeric materials in a carbohydrate matrix also influenced several particle properties, such as the particle shape and the surface morphology, and was caused by changes in the chemical composition of the particle surface and possibly the surface rheology. In addition, powder performance of pharmaceutical relevance, such as dissolution and flowability, were affected.

This thesis concerns the development and validation of methods for the industrially important area of adsorption isotherm parameter estimation in preparative, nonlinear high performance liquid chromatography (HPLC). Preparative chromatography is a powerful separation method to get pure compounds from more or less complex liquid mixtures, e.g., mixtures of mirror-image molecules. Computer simulations can be used to optimize preparative chromatography, but then competitive adsorption isotherm parameters are usually required. Here two methods to estimate adsorption isotherm parameters are treated: (i) the perturbation peak (PP) method and (ii) the inverse method (IM). A new theory for the PP method was derived and led to a new injection technique which was validated experimentally. This injection technique solved the severe problem with vanishing peaks and enabled us to use the PP method to estimate binary competitive adsorption isotherms valid over a broad concentration range. Also, the injection technique made it possible to estimate competitive adsorption isotherms for a quaternary mixture for the first time. Finally, an interesting perturbation peak phenomenon, known as the “Helfferich Paradox”, was experimentally verified for the first time. The IM is a relatively new method to determine adsorption isotherm parameters. It has the advantage of requiring very small samples, but also requires an advanced computer algorithm. An improved implementation of this computer algorithm was developed and tested experimentally. Also, a variant of the IM called “the inverse method on plateaus” was tested experimentally and the estimated adsorption isotherm parameters were shown to be valid over a broader concentration range than those estimated with the standard IM.

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No. of bitstreams: 2 Dissertação - Débora Cristina Aguiar Chaves Paiva - 2017.pdf: 5630280 bytes, checksum: 8935fe44bd6a04a467ea7bb4c6de8f68 (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) Previous issue date: 2017-09-21 / The present work had as objective to investigate the performance of a fixed bed aerobic reactor with biomass adhered in the treatment of waters contaminated with glyphosate and different concentrations of phosphorus. The effect of different phosphorus concentrations on the adsorption kinetics of glyphosate in a support medium was evaluated by means of the determination of the exhaust curve in a system composed of an adsorption column filled with expanded clay. The glyphosate solution used was commercial product based on Glyphosate Di-ammonium salt 445 g.L-1 (370 g.L-1 equivalent acid) and ultra purified water, with final glyphosate concentration of 8 mg.L-1. Concentrations of 0.8 mg.L-1 were used in the adsorbent assays; 8 mg.L-1; and 16 mg.L-1, and the pH values adopted were: 4; 7 and 10. The results obtained demonstrate the influence of both pH and phosphate ions on the adsorption of glyphosate in expanded clay, where the adsorption kinetics showed the influence of both parameters, in general, on higher concentrations of phosphate ions. The effect of different concentrations of phosphorus on glyphosate biodegradation kinetics was evaluated by means of temporal profiles of the glyphosate and phosphorus concentration decay in the same system used in the adsorption tests with aerobic sludge inoculation in the expanded clay. The glyphosate solution was the same as that used in the 15 mg.L-1 adsorption assays, evaluating the degradation in the presence of concentrations of 2.15 mg.L- 1; 5.37 mg.L-1; 10.75 mg.L-1; 16.12 mg.L-1; 21.5 mg.L-1; 43 mg.L-1 phosphorus. The results demonstrate the influence of phosphate ions on the degradation kinetics of glyphosate in expanded clay. It is possible to observe that glyphosate treatment efficiency increased as phosphorus concentrations increased, indicating that kinetics of degradation was directly associated to kinetics adsorptive. The data were analyzed by means of multiple regression, which was able to verify with 95% confidence the effect of the phosphorus (p <0.05) on the degradation process. / O presente trabalho teve como objetivo investigar o desempenho de um reator aeróbio de leito fixo com biomassa aderida no tratamento de águas contaminadas com glifosato e diferentes concentrações de fósforo. Avaliou-se inicialmente o efeito de diferentes concentrações de fósforo na cinética de adsorção do glifosato em meio suporte por meio da determinação da curva de exaustão em sistema composto por coluna de adsorção preenchidacom argila expandida. A solução de glifosato utilizada foi composta por produto comercial a base de sal de Di-amônio de Glifosato 445 g.L-1 (370 g.L-1 equivalente ácido) e água ultra purificada, com concentração final de glifosato de 8 mg.L-1. Nos ensaios adsortivos foram utilizadas concentrações de 0,8 mg.L-1; 8 mg.L-1; e 16 mg.L-1, e os valores de pH adotados foram: 4; 7 e 10. Os resultados obtidos demonstram a influência tanto do pH quanto dos íons fosfato na adsorção do glifosato em argila expandida, onde a cinética de adsorção demonstrou a influência de ambos os parâmetros, em geral, em concentrações mais elevadas de íons fosfato. Posteriormente avaliou-se o efeito de diferentes concentrações de fósforo na cinética de biodegradação do glifosato por meio da realização de perfis temporais do decaimento da concentração de glifosato e fósforo no mesmo sistema utilizado nos ensaios de adsorção com inoculação de lodo aeróbio na argila expandida. A solução de glifosato foi a mesma utilizada nos ensaios adsortivos na concentração de 15 mg.L-1, avaliando a degradação na presença das concentrações de 2,15 mg.L-1; 5,37 mg.L-1; 10,75 mg.L-1; 16,12 mg.L-1; 21,5 mg.L-1; 43 mg.L-1 de fósforo. Os resultados demonstram a influência dos íons fosfato na cinética de degradação do glifosato em argila expandida, sendo possível observar a eficiência de tratamento do glifosato foi crescente à medida que se aumentou as concentrações de fósforo, indicando que a cinética de degradação esteve diretamente associada à cinética adsortiva. Os dados foram analisados por meio de regressão múltipla, a qual foi possível verificar com 95% de confiança o efeito do fósforo (p<0,05) sobre o processo de degradação.

The thesis presents work regarding amphiphilic molecules associated in aqueous solution or at the liquid/solid interface. Two main topics are included: the temperature-dependent behavior of micelles and the adsorption of dispersants on carbon nanotube (CNT) surfaces. Various NMR methods were used to analyze those systems, such as chemical shift detection, spectral intensity measurements, spin relaxation and, in particular, self-diffusion experiments. Besides this, small angle X-ray scattering (SAXS) was also applied for structural characterization.   A particular form of phase transition, core freezing, was detected as a function of temperature in micelles composed by a single sort of Brij-type surfactants. In mixed micelles, that phase transition still occurs accompanied by a reversible segregation of different surfactants into distinct aggregates. Adding a hydrophobic solubilizate shifts the core freezing point to a lower temperature. Upon lowering the temperature to the core freezing point, the solubilizate is released. The temperature course of the release curves with different initial solubilizate loadings is rationalized in terms of a temperature-dependent loading capacity.   The behavior of amphiphilic dispersant molecules in aqueous dispersions of carbon nanotubes (CNTs) has been investigated with a Pluronic-type block copolymer as frequent model dispersant. Detailed dispersion curves were recorded and the distribution of the dispersant among different available environments was analyzed. The amount of dispersed CNT was shown to be defined by a complex interplay of several factors during the dispersion process such as dispersant concentration, sonication time, centrifugation and CNT loading. In the dispersion process, high amphiphilic concentration is required because the pristine CNT surfaces made available by sonication must be rapidly covered by dispersants to avoid their re-attachment. In the prepared dispersions, the competitive adsorption of possible dispersants was investigated that provided information about the relative strength of the interaction of those with the nanotube surfaces. Anionic surfactants were found to have a strong tendency to replace Pluronics, which indicates a strong binding of those surfactants.   CNTs were dispersed in an epoxy resin to prepare nanotube-polymer composites. The molecular mobility of epoxy was investigated and the results demonstrated the presence of loosely associated CNT aggregates within which the molecular transport of epoxy is slow because of strong attractive intermolecular interactions between epoxy and the CNT surface. The rheological behavior is dominated by aggregate-aggregate jamming. / <p>QC 20180103</p>

No description available.

The diploma thesis is aimed at adsorption processes during the removal of pesticides onto granular activated carbon (GAC) in the process of drinking water treatment. Adsorption onto GAC represents an efficient method for pesticides removal. High adsorption efficiency can be significantly reduced due to the occurrence of natural organic matter (NOM) in raw water, which involves AOM (Algal Organic Matter) produced by phytoplankton. Analogous to NOM, AOM probably affects adsorption of pesticides by two different mechanisms - a direct site competition and pore blockage effect, in dependence on the different molecular weight of particular AOM fractions. Equilibrium batch and kinetic adsorption experiments were performed using two types of GAC (Norit 1240 and Filtrasorb 400) and two pesticides (terbuthylazine and alachlor). In order to examine the effect of AOM on adsorption of pesticides, raw GAC and GAC preloaded by AOM were used. The effect of pH on the competitive adsorption of AOM was also evaluated. A solid phase extraction (SPE) method and gas chromatography with electron capture detection (GC-ECD) were used to determine pesticides in water samples. AOM was characterized using fractionation onto sorptive resins. The representation of apparent molecular weights of AOM proteins was determined by...

Finding economical and environmentally friendly processes to recover heavy metals (HMs) from spent batteries is a research priority to move toward sustainability. Adsorption seems an acceptable procedure to replace the current separation/purification stage of hydrometallurgical techniques. Chitosan is an efficient adsorbent for HM uptake from aqueous solutions. Nevertheless, in practice, chitosan modification is unavoidable to improve its physicochemical properties. Sodium tripolyphosphate is an environmentally benign crosslinker that can be used for chitosan modification. In addition, ion-imprinting technique could potentially enhance the adsorption efficiency and selectivity of crosslinked chitosan. Considering the above, the primary purposes of this research were: investigating the adsorption efficiency of chitosan for heavy metals uptake from synthetic solutions; modifying chitosan by crosslinking alone and combined with ion-imprinting techniques to improve the physicochemical properties as well as adsorption capacity and selectivity of chitosan; evaluating and comparing the adsorption efficiency of modified chitosan beads for the adsorption of Cd(II), Ni(II) and Co(II) in single and multicomponent batch adsorption systems. Chitosan and sodium tripolyphosphate crosslinked chitosan beads were prepared to remove Cd(II) from aqueous solution in the first phase. FTIR and XRD of the synthesized beads showed partial consumption of chitosan amine groups and a decrease in crystallinity of chitosan structure over crosslinking reaction. The isotherm and thermodynamic studies showed that Langmuir isotherm was the best fit to the experimental data of Cd(II) adsorption on crosslinked chitosan and all the adsorption reactions were endothermic and spontaneous. A reduced quadratic model, constructed by the Response Surface Methodology (RSM), indicated that the Cd(II) adsorption uptake of 99.87 (mg/g) was achieved at 55 °C and 2.92 % (w/v) crosslinking degree. Then, chitosan and crosslinked chitosan beads by sodium tripolyphosphate were used for Ni(II) adsorption from aqueous media in the second phase. The BET characterization showed that increasing the crosslinking degree reduced the chitosan beads' surface area and their total pore volume. The Langmuir model described the experimental results best and showed that the maximum adsorption capacity of chitosan (80.00 mg/g) decreased after crosslinking (52.36 mg/g). In addition, a reduced quadratic model with a correlation coefficient of 0.96 was established to correlate the adsorption uptake of Ni(II) with pH and crosslinking degree. In the third phase, the adsorption of Ni(II) and Cd(II) ions from single and binary metal ions solutions onto chitosan and crosslinked chitosan beads was studied. The extended Freundlich model fitted the adsorption equilibrium data in the binary system, implying the existence of preference in the order of Ni(II) > Cd(II). Desorption studies with a mixture of NaCl and H2SO4 were also conducted during this phase, demonstrating a desorption efficiency of greater than 85 %. In the fourth phase, the removal of cadmium from aqueous solution was examined using a novel Cd(II)-imprinted crosslinked chitosan. SEM, FTIR, TGA, and BET characterizations revealed that the ion-imprinted chitosan beads had better physicochemical properties than chitosan beads and superior potential adsorption properties than non-imprinted crosslinked chitosan beads. The isotherm and thermodynamic studies revealed that the Langmuir isotherm fitted the Cd(II) experimental data the best, and the adsorption reactions were spontaneous and endothermic. The kinetics data were also best fitted by the pseudo-second-order equation. Finally, the ion-imprinted crosslinked chitosan beads were employed for the selective adsorption of Cd(II) in a competitive adsorption system of Cd(II)-Ni(II)-Co(II) in phase five. The characterization of the prepared adsorbents was performed using XRD and BET, showing a higher surface area of ion-imprinted crosslinked chitosan than non-imprinted crosslinked chitosan beads. The Extended Langmuir model fitted the experimental results obtained from the multi-component system, indicating that ion-imprinted crosslinked chitosan had a higher total metal uptake with better selectivity toward Cd(II) uptake compared to non-imprinted crosslinked chitosan. Studying the adsorption mechanism in a ternary system showed that the adsorption was governed by chemical binding and ion exchange mechanisms in the ternary system. In conclusion, crosslinking by sodium tripolyphosphate improved chitosan physiochemical properties; however, it resulted in a decrease in HM adsorption uptake. The RSM was used to assess the effect of pH, temperature, and crosslinking degree and optimize the adsorption uptake of chitosan. Also, ion-imprinting was effective in enhancing the adsorption capacity and selectivity of crosslinked chitosan for the ion used as a template (Cd(II)) in preparing ion-imprinted crosslinked chitosan.