In the present work, a super water-absorbent poly(acrylic acid) was synthetized by inverse suspension polymerization, using Span60 as the dispersant, toluene as the dispersing organic phase, trimethylolpropane triacrylate as the crosslinking agent, and sodium persulfate as the initiator. The synthesis was conducted in a small-scale glass reactor operated in semi-batch mode. The following reaction conditions were evaluated: effects of initiator concentration, temperature, percentage of multifunctional cross-linker agent and monomer concentration. Also, two important properties were determined, conversion and gel fraction. A kinetic model including a population balance was employed to simulate the process. The proposed model uses the numerical fractionation technique and is capable of predicting the pre-gel and post-gel properties, the effect of the crosslinking agent level on the polymer properties and the dynamic of gelation. The model was compared with the experimental results and showed a satisfactory representation of the system after parameter adjusting. / No presente trabalho, o poli (ácido acrílico) super-absorvente foi sintetizado por polimerização em suspensão inversa, usando Span 60 como o dispersante, tolueno como fase orgânica, trimetilolpropano triacrilato como agente de reticulação e persulfato de sódio como iniciador. A síntese foi conduzida num reator de vidro em escala de bancada, operado em modo semi-batelada-batelada. As seguintes condições da reação foram avaliadas: os efeitos da concentração de iniciador, a temperatura, a porcentagem de agente de reticulação multifuncional e a concentração de monómero. Além disso, foram determinadas propriedades importantes, como a conversão e a fração de gel. Da mesma forma, foi desenvolvido um modelo de balanço populacional para simular o processo em conjunto com a técnica de fracionamento numérico, que é capaz de prever as propriedades pré-gel e pós-gel, o efeito do nível do agente de reticulação no polímero e as propriedades da dinâmica de gelificação. O modelo foi comparado com os resultados experimentais e mostrou uma representação satisfatória do sistema após o ajuste dos parâmetros.

In recent years, electrochemical capacitors have emerged as devices with the potential to enable major advances in electrical energy storage. Electrochemical capacitors (ECs) are akin to conventional capacitors but employ higher surface-area electrodes and thinner dielectrics to achieve larger capacitances. This helps ECs to attain energy densities greater than those of conventional capacitors and power densities greater than those of batteries. Akin to conventional capacitors, ECs also have high cycle-lives and can be charged and discharged rapidly. But ECs are yet to match the energy densities of mid to high-end batteries and fuel cells. On the basis of mechanism involved in the charge-storage process, ECs are classified as electrical double-layer capacitors (EDLCs) or pseudocapacitors. Charge storage in EDLCs and pseudocapacitors is brought about by non-faradaic and faradaic processes, respectively. Faradaic process, such as an oxidation-reduction reaction, involves the transfer of charge between electrode and electrolyte. By contrast, a non-faradaic process does not use a chemical mechanism and charges are distributed on surfaces by physical processes that do not involve any chemical reaction. ECs employ both aqueous and non-aqueous electrolytes in either liquid or solid form, the latter providing the advantages of freedom from leakage of any liquid component, compactness, reliability and large operating potential-window. In the literature, polymer electrolytes are the most widely studied solid electrolytes. Complexation of functional-groups of certain polymers with cations results in the formation of polymer-cation complexes commonly referred to as solid-polymer electrolytes (SPEs). Mixing a polymer with an alkali metal salt dissolved in an organic solvent result in the formation of a polymer gel electrolyte. Organic solvents with low molecular-weights, such as ethylene carbonate and propylene carbonate, employed in polymer gel electrolytes are commonly referred to as plasticizers. When water is used as a plasticizer, the polymer electrolyte is called a polymer hydrogel electrolyte. Part I of the thesis is directed to studies pertaining to Polymer Hydrogel Electrolytes for Electrochemical Capacitors and comprises four sections. After a brief survey of literature on polymer hydrogel electrolytes employed in ECs in Section I.1, Section I.2 of Part I describes the studies on electrochemical capacitors employing cross-linked poly (vinyl alcohol) hydrogel membrane electrolytes with varying perchloric acid dopant concentration. Acidic poly (vinyl alcohol) hydrogel membrane electrolytes (PHMEs) with different perchloric acid concentrations are prepared by cross-linking poly (vinyl alcohol) with glutaraldehyde in the presence of a protonic acid acting as a catalyst under ambient conditions. PHMEs are characterized by scanning electron microscopy and temperature-modulated differential scanning calorimetry in conjunction with relevant electrochemical techniques. An optimised electrochemical capacitor assembled employing PHME in conjunction with black pearl carbon (BPC) electrodes yields a maximum specific capacitance value of about 96 F g-1, phase angle value of about 79o and a discharge capacitance value of about 88 F g-1. Section I.3 of Part I describes the studies on cross-linked poly (vinyl alcohol)/ploy (acrylic acid) blend hydrogel electrolytes for electrochemical capacitors. Acidic poly (vinyl alcohol)/poly (acrylic acid) blend hydrogel electrolytes (BHEs) have been prepared by cross-linking poly (vinyl alcohol)/poly (acrylic acid) blend with glutaraldehyde in presence of perchloric acid. These acidic BHEs have been treated suitably to realize alkaline and neutral BHEs. Thermal characteristics and glass-transition behavior of BHEs have been followed by differential scanning calorimetry. Ionic conduction in acidic BHEs has been found to take place by Grötthus-type mechanism while polymer segmental motion mechanism is predominantly responsible for ion motion in alkaline and neutral BHEs. Ionic conductivity of BHEs has been found to range between 10-3 and 10-2 S cm-1 at 298 K. Electrochemical capacitors assembled with acidic PVA hydrogel electrolyte yield a maximum specific capacitance of about 60 and 1000 F g-1 with BPC and RuOx.xH2O/C electrodes, respectively. Section I.4 of Part I describes the studies on gelatin hydrogel electrolytes and their application to electrochemical capacitors. Gelatin hydrogel electrolytes (GHEs) with varying NaCl concentrations have been prepared by cross-linking an aqueous solution of gelatin with aqueous glutaraldehyde under ambient conditions, and characterized by scanning electron microscopy, temperature-modulated differential scanning calorimetry, cyclic voltammetry, electrochemical impedance spectroscopy and galvanostatic chronopotentiometry. Glass transition temperatures for GHEs range between 340 and 377 K depending on the dopant concentration. Ionic conductivity behavior of GHEs is studied with varying concentrations of gelatin, glutaraldehyde and NaCl, and conductivity values are found to vary between 10-3 and 10-1 S cm-1 under ambient conditions. GHEs have a potential window of about 1 V with BPC electrodes. The ionic conductivity of pristine and 0.25 N NaCl-doped GHEs follows Arrhenius behavior with activation energy values of 1.9×10-4 and 1.8×10-4 eV, respectively. Electrochemical capacitors employing GHEs in conjunction with black pearl carbon electrodes are assembled and studied. Optimal values for capacitance, phase angle, and relaxation time constant of about 81 F g-1, 75o, and 0.03 s are obtained for 3 M NaCl-doped GHE, respectively. EC with pristine GHE exhibits continuous cycle life for about 4.3 h as against 4.7 h for the electrochemical capacitor with 3 M NaCl-doped GHE. Unlike electrochemical capacitors, fuel cells do not store the charge internally but instead use a continuous supply of fuel from an external storage tank. Thus, fuel cells have the potential to solve the most challenging problem associated with the electrochemical capacitors, namely their limited energy-density. A fuel cell is an electrochemical power source with advantages of both the combustion engine and the battery. Like a combustion engine, a fuel cell will run as long as it is provided with fuel; and like a battery, fuel cells convert chemical energy directly to electrical energy. As an electrochemical power source, fuel cells are not subjected to the Carnot limitations of combustion (heat) engines. A fuel cell operates quietly and efficiently and, when hydrogen is used as a fuel, it generates only power and potable water. Thus, a fuel cell is a so called ‘zero-emission engine’. In the past, several fuel cell concepts have been tested in various laboratories but the systems that are being potentially considered for commercial developments are: (i) Alkaline Fuel Cells (AFCs), (ii) Phosphoric Acid Fuel Cells (PAFCs), (iii) Polymer Electrolyte Fuel Cells (PEFCs), (iv) Solid-Polymer-Electrolyte-Direct Methanol Fuel Cells (SPE-DMFCs), (v) Molten Carbonate Fuel Cells (MCFCs) and (vi) Solid Oxide Fuel Cells (SOFCs). Among the aforesaid systems, PEFCs that employ hydrogen as fuel are considered attractive power systems for quick start-up and ambient-temperature operations. Ironically, however, hydrogen as fuel is not available freely in the nature. Accordingly, it has to be generated from a readily available hydrogen carrying fuel such as natural gas, which needs to be reformed. But, such a process leads to generation of hydrogen with some content of carbon monoxide, which even at minuscule level is detrimental to the fuel cell performance. Pure hydrogen can be generated through water electrolysis but hydrogen thus generated needs to be stored as compressed / liquefied gas, which is cost-intensive. Therefore, certain hydrogen carrying organic fuels such as methanol, ethanol, propanol, ethylene glycol, and diethyl ether have been considered for fuelling PEFCs directly. Among these, methanol with a hydrogen content of about 13 wt. % (specific energy = 6.1 kWh kg-1) is the most attractive organic liquid. PEFCs using methanol directly as fuel are referred to as SPE-DMFCs. But SPE-DMFCs suffer from methanol crossover across the polymer electrolyte membrane, which affects the cathode performance and hence the cell performance during its operation. SPE-DMFCs also have inherent limitations of low open-circuit-potential and low electrochemical-activity. An obvious solution to the aforesaid problems is to explore other promising hydrogen carrying fuels such as sodium borohydride, which has a hydrogen content of about 11 wt. %. Such fuel cells are called direct borohydride fuel cells (DBFCs). Part II of the thesis includes studies on direct borohydride fuel cells and comprises three sections. After a brief introduction to DBFCs in section II.1, Section II.2 describes studies on an alkaline direct borohydride fuel cell with hydrogen peroxide as oxidant. A peak power density of about 150 mW cm-2 at a cell voltage of 540 mV could be achieved from the optimized DBFC operating at 70oC. Section II.3 describes studies on poly (vinyl alcohol) hydrogel membrane as electrolyte for direct borohydride fuel cells. This DBFC employs a poly (vinyl alcohol) hydrogel membrane as electrolyte, an AB5 Misch metal alloy as anode, and a gold-plated stainless steel mesh as cathode in conjunction with aqueous alkaline solution of sodium borohydride as fuel and aqueous acidified solution of hydrogen peroxide as oxidant. The performance of the PHME-based DBFC in respect of peak power outputs, ex-situ cross-over of oxidant, fuel, anolyte and catholyte across the membrane electrolytes, utilization efficiencies of fuel and oxidant as also cell performance durability under ambient conditions are compared with a similar DBFC employing a Nafion®-117 membrane electrolyte (NME). Peak power densities of about 30 and 40 mW cm-2 are observed for the DBFCs with PHME and NME, respectively. The PHME and NME-based DBFCs exhibit cell potentials of about 1.2 and 1.4 V, respectively, at a load current density of 10 mA cm-2 for 100 h. Publications of Nurul Alam Choudhury 1. Gelatin hydrogel electrolytes and their application to electrochemical supercapacitors, N. A. Choudhury, S. Sampath, and A. K. Shukla, J. Electrochem. Soc., 155 (2008) A74. 2. Cross-linked polymer hydrogel electrolytes for electrochemical capacitors, N. A. Choudhury, A. K. Shukla, S. Sampath, and S. Pitchumani, J. Electrochem. Soc., 153 (2006) A614. 3. Hydrogel-polymer electrolytes for electrochemical capacitors: an overview, N. A. Choudhury, S. Sampath, and A. K. Shukla, Energy and Environmental Science (In Press). 4. Cross-linked poly (vinyl alcohol) hydrogel membrane electrolytes with varying perchloric acid dopant concentration and their application to electrochemical capacitors, N. A. Choudhury, S. Sampath, and A. K. Shukla, J. Chem. Sc. (Submitted) 5. An alkaline direct borohydride fuel cell with hydrogen peroxide as oxidant, N. A. Choudhury, R. K. Raman, S. Sampath, and A. K. Shukla, J. Power Sources, 143 (2005) 1. 6. Poly (vinyl alcohol) hydrogel membrane as electrolyte for direct borohydride fuel cells, N. A. Choudhury, S. K. Prashant, S. Pitchumani, P. Sridhar, and A. K. Shukla, J. Chem. Sc. (Submitted). 7. A phenyl-sulfonic acid anchored carbon-supported platinum catalyst for polymer electrolyte fuel cell electrodes, G. Selvarani, A. K. Sahu, N. A. Choudhury, P. Sridhar, S. Pitchumani, and A. K. Shukla, Electrochim. Acta, 52 (2007) 4871. 8. A high-output voltage direct borohydride fuel cell, R. K. Raman, N. A. Choudhury, and A. K. Shukla, Electrochem. Solid-State Lett., 7 (2004) A 488. 9. Carbon-supported Pt-Fe alloy as a methanol-resistant oxygen-reduction catalyst for direct methanol fuel cells, A. K. Shukla, R. K. Raman, N. A. Choudhury, K. R. Priolkar, P. R. Sarode, S. Emura, and R. Kumashiro, J. Electroanal. Chem., 563 (2004) 181.

Cette thèse rapporte le greffage chimique de brosses de polymères neutres de poly(acrylate de tert-butyle) (PtBA) et de brosses chargées d’acide polyacrylique (PAA) sur des substrats de mica afin d’étudier leur conformation en fonction de la densité de greffage, du pH et de la force ionique. Le greffage est réalisé par polymérisation contrôlée par transfert d’atome (ATRP) initiée depuis la surface de mica afin de contrôler la croissance du polymère et sa densité de greffage. L’étude de la conformation des brosses de PtBA et de PAA a été menée avec la technique AFM en mesurant les épaisseurs des films à sec et gonflés sous différentes conditions de solvant, de pH et de force ionique. Une monocouche d’amorceurs est tout d’abord greffée sur du mica porteur de groupes hydroxyles créés par plasma (Ar/H2O). Cette couche a été caractérisée par des mesures d’angle de contact et par la technique TOF-SIMS. L’amorceur greffé a ensuite permis d’initier l’ATRP directement depuis la surface pour former des brosses neutres de PtBA liés de façon covalente au mica. La croissance linéaire de l’épaisseur du film avec la masse molaire du polymère en solution et le taux de conversion montre que la polymérisation est contrôlée. De plus, la ré-initiation des chaînes greffées atteste du caractère vivant de la polymérisation. L’hydrolyse des brosses de PtBA, confirmée par des mesures d’angle de contact, d’épaisseur et par FT-IR, conduit à des brosses de PAA. Les différentes couches greffées sont stables à l’air, en milieu organique et en milieu aqueux et leur gonflement est réversible. Le degreffage de la couche de PAA est observé suite à une longue exposition à pH basique. Cette étude représente le premier exemple de brosses greffées chimiquement sur du mica par polymérisation initiée depuis la surface. La variation des paramètres de la réaction de greffage de l’amorceur, tels que la concentration et la durée de réaction, a permis de contrôler le taux de recouvrement de l’amorceur et la densité de greffage du polymère. Une grande gamme de taux de recouvrement de l’amorceur est accessible et se traduit par un intervalle de densités de greffage allant de faibles à élevées (e.g. 0,04 chaîne/nm2 à 0,5 chaîne/nm2). L’étude de la conformation des chaînes de PtBA dans le DMF montre que cet intervalle de densités recouvre le régime crêpe au régime brosse. Le gonflement de brosses de PAA et la variation de la hauteur de la brosse L ont été étudiés en fonction de la densité de greffage, du pH et du sel ajouté cs (NaCl). Une transition brusque de collapsée à étirée est observée avec l’augmentation du pH, indépendamment de la densité de greffage. A pH neutre, les brosses sont collapsées et se comportent comme des brosses neutres en mauvais solvant. A pH basique, les brosses sont gonflées et chargées et se trouvent dans un régime de Pincus caractéristique des polyélectrolytes forts. En présence de sel, les charges sont partiellement écrantées et les répulsions électrostatiques dominent toujours dans la brosse. Cette étude contribue à une meilleure compréhension du comportement complexe des brosses de polyélectrolytes faibles et apporte un soutien expérimental à la théorie sur le comportement de ces brosses. / Neutral polymer brushes of poly(tert-butyl acrylate) (PtBA) and polyelectrolyte brushes of poly(acrylic acid) (PAA) were chemically grafted on mica in order to study their conformation as a function of grafting density, pH and ionic strength. The brushes were prepared via surface-initiated atom-transfer radical polymerization (SI-ATRP). This approach allows the control of the polymer growth and of the polymer grafting density. The study of brush conformation was investigated by measuring the dry and the swollen film thicknesses by Atomic Force microscopy (AFM) under various environmental conditions. Mica substrates were activated by a plasma method leading to OH-functionalized surfaces to which a radical initiator was covalently bound using standard siloxane protocols. The initiator grafting on the mica substrate was confirmed by water contact angle measurements and time-of-flight secondary ion mass spectrometry (TOF-SIMS). The covalently immobilized initiator successfully underwent SI-ATRP with tert-butyl acrylate, yielding end-grafted PtBA brushes that are covalently linked to mica. A linear relationship of the polymer thickness with respect to the molecular weight of the free polymer and with respect to the monomer conversion is obtained confirming that SI-ATRP is well controlled. The PtBA brushes were then hydrolyzed to PAA as confirmed by water contact angle measurements, polymer thickness measurements and FT-IR. The grafted layers show a good stability in air, organic solvent and aqueous solution and a reversible swelling. Film cleavage is observed for long exposure time in basic solution. This study represents the first example of chemically grafted brushes on mica via SI-ATRP. The polymer grafting density of poly(tert-butyl acrylate) was controlled by tuning the initiator surface coverage. By adjusting parameters such as the immobilization reaction time and concentration of the initiator, a wide range of initiator surface coverages and hence polymer densities on mica were possible ranging from 0.04 chain/nm2 to 0.5 chain/nm2). The swelling behavior of PAA brushes was investigated as a function of the polymer grafting density, pH and ionic strength cs (NaCl). A sharp transition from collapsed to stretched conformation was found with increasing pH. At neutral pH, the brushes are collapsed and behave like neutral brushes in poor solvent. At high pH, the brushes are swollen and charged and belong to the Pincus regime. In the presence of salt, the Coulombic repulsions are screened. The observed behavior of PAA brushes resembles the one of strong polyelectrolyte brushes. This study contributes to a better understanding of the complex behaviour of weak polyelectrolyte brushes and brings experimental support to theoretical studies.

The self-assembly of polystyrene-stabilized cadmium sulfide nanoparticles (PS-CdS) with amphiphilic stabilizing chains of polystyrene-block-poly(acrylic acid) (PS-b-PAA) into colloidal quantum dot compound micelles (QDCMs) is studied on two-phase gas-liquid segmented microfluidic reactors. The resulting particle sizes are found to arise from the interplay of shear-induced coalescence and particle breakup, depending on a combination of chemical and flow conditions. Variation of water content, gas-to-liquid ratio, and total flow rate, enable control of QDCM sizes in the range of 140 – 40 nm. The flow-variable shear effect on similar microfluidic reactors is then applied to direct the solution self-assembly of a PS-b-PAA block copolymer into various micelle morphologies. The difference between off-chip and on-chip morphologies under identical chemical conditions is explained by a mechanism of shear-induced coalescence enabled by strong and localized on-chip shear fields, followed by intraparticle chain rearrangements to minimize local free energies. Time-dependent studies of these nanostructures reveal that on-chip kinetic structures will relax to global equilibrium given sufficient time off-chip. Further investigations into the effect of chemical variables on on-chip shear-induced morphologies reveal a combination of thermodynamic and kinetic effects, opening avenues for morphology control via combined chemical (bottom-up) and shear (top-down) forces. An equilibrium phase diagram of off-chip micelle morphologies is constructed and used in conjunction with kinetic considerations to rationalize on-chip mechanisms and morphologies, including cylinders and vesicles, under different chemical conditions. Finally, we extend our strategy of two-phase microfluidic self-assembly of PS-b-PAA to the loading of fluorescent hydrophobic probes (pyrene and naphthalene) with different affinities for the PS core. The on-chip loading approach provides a fast alternate to the slow off-chip method, with implications for the potential development for point-of-care devices for drug loading. On-chip loading results indicate that loading efficiencies are dependent on water content and, to a lesser extent, on flow rate; the results also suggest that the on-chip morphologies of the PS-b-PAA micelles are an important factor in the loading efficiencies. / Graduate

No description available.

In the present work, a super water-absorbent poly(acrylic acid) was synthetized by inverse suspension polymerization, using Span60 as the dispersant, toluene as the dispersing organic phase, trimethylolpropane triacrylate as the crosslinking agent, and sodium persulfate as the initiator. The synthesis was conducted in a small-scale glass reactor operated in semi-batch mode. The following reaction conditions were evaluated: effects of initiator concentration, temperature, percentage of multifunctional cross-linker agent and monomer concentration. Also, two important properties were determined, conversion and gel fraction. A kinetic model including a population balance was employed to simulate the process. The proposed model uses the numerical fractionation technique and is capable of predicting the pre-gel and post-gel properties, the effect of the crosslinking agent level on the polymer properties and the dynamic of gelation. The model was compared with the experimental results and showed a satisfactory representation of the system after parameter adjusting. / No presente trabalho, o poli (ácido acrílico) super-absorvente foi sintetizado por polimerização em suspensão inversa, usando Span 60 como o dispersante, tolueno como fase orgânica, trimetilolpropano triacrilato como agente de reticulação e persulfato de sódio como iniciador. A síntese foi conduzida num reator de vidro em escala de bancada, operado em modo semi-batelada-batelada. As seguintes condições da reação foram avaliadas: os efeitos da concentração de iniciador, a temperatura, a porcentagem de agente de reticulação multifuncional e a concentração de monómero. Além disso, foram determinadas propriedades importantes, como a conversão e a fração de gel. Da mesma forma, foi desenvolvido um modelo de balanço populacional para simular o processo em conjunto com a técnica de fracionamento numérico, que é capaz de prever as propriedades pré-gel e pós-gel, o efeito do nível do agente de reticulação no polímero e as propriedades da dinâmica de gelificação. O modelo foi comparado com os resultados experimentais e mostrou uma representação satisfatória do sistema após o ajuste dos parâmetros.

Ces travaux décrivent la synthèse de nanoparticules stabilisées par des polyélectrolytes d’originesynthétique (poly(acide (méth)acrylique)) ou naturelle (alginate) par polymérisation radicalairecontrôlée (PRC) de type RAFT en émulsion. Ce procédé est basé sur l’utilisation d’un polymèrehydrophile obtenu par RAFT (macroRAFT) qui est réactivé dans l’eau pour la polymérisation d’unmonomère hydrophobe. Des copolymères à blocs amphiphiles sont ainsi générés et s’auto-assemblent in situ pour former des nanoparticules. Dans un premier temps, nous avons cherché à conduire l’ensemble du procédé en milieu aqueux. Des études ont ainsi été menées sur la polymérisation RAFTdans l’eau de l’acide acrylique et de l’acide méthacrylique. Des homopolymères bien définis ont été obtenus sur une large gamme de conditions, puis ont été utilisés comme macroRAFTs pour la polymérisation en émulsion de monomères hydrophobes. Des nanoparticules stables constituées de copolymères à blocs amphiphiles bien définis ont été produites. Il a été montré que le contrôle de la polymérisation et la nucléation dépendaient fortement du pH, mais qu’une bonne stabilité colloïdale était néanmoins observée dans tous les cas. Ce procédé "one-pot " a ensuite été extrapolé à la synthèse de particules stabilisées par des copolymères hydrophiles de N-acryloylmorpholine (NAM) et de macromonomères d’alginate. Des nano-objets aux morphologies variées ont été obtenus. Afin de mieux appréhender la formation de ces morphologies, un système modèle employant un copolymère hydrophile de NAM et de macromonomère de polyNAM obtenu par polymérisation RAFT a été étudiépour la polymérisation en émulsion du styrène. / This work describes the synthesis of nanoparticles stabilized by polyelectrolytes from synthetic(poly((meth)acrylic acid)) or natural (alginate) source by controlled free radical polymerization (CRP),namely RAFT, in emulsion. This process is based on the use of a hydrophilic polymer prepared by RAFT (i.e. macroRAFT) which is reactivated in water for the polymerization of a hydrophobic monomer. The formation of amphiphilic block copolymers which self-assemble in situ leads to the formation of nanoparticles. Firstly, we tried to perform the whole process in water. The RAFT polymerization of acrylic acid and methacrylic acid was studied in this context. Well-defined homopolymers were obtained under a large range of conditions, and further used as macroRAFTs in emulsion polymerization of hydrophobic monomers. Stable nanoparticles composed of well-defined amphiphilic block copolymers were produced. It was shown that the control of the polymerization and the nucleation were strongly dependent on the pH. Nevertheless, a good colloidal stability wasobserved in all cases. This “one-pot” process was then extrapolated to the synthesis of particles stabilized by hydrophilic copolymers of N-acryloylmorpholine (NAM) and alginate macromonomer. Nano-objects with various morphologies were obtained. In order to better understand the formation of these morphologies, a model system using a hydrophilic copolymer of NAM and a polyNAM macromonomer obtained by RAFT polymerization was studied in styrene emulsion polymerization.

L’objectif de ce travail a été d’introduire des groupements fonctionnels au sein de chaînes polymère silicone pour former des assemblages supramoléculaires, dans le but de former de nouveaux matériaux. Tout d’abord, une étude approfondie de la bibliographie a permis de cerner les avantages et limitations de la réaction d’aza-Michael appliquée aux silicones. Cette étude a aussi permis d’acquérir de solides connaissances générales sur la réaction d’aza-Michael appliquée à des composés organiques aminé et de soulever des points peu ou pas traités tels que la sélectivité et la réversibilité de la réaction. Afin de comprendre et contrôler cette réaction, une étude modèle impliquant un PDMS aminé simple et l’acrylate de butyle a été réalisée. Plusieurs paramètres tels que la présence de solvants polaires protiques, de catalyseurs, ou une température élevée permettent de promouvoir la réaction. Des données cinétiques ont également mis en relief la possibilité de contrôler la sélectivité de la réaction sur un groupement amine primaire (mono- ou di-addition). Un composé 100% mono-adduit et un composé 100% di-adduit ont ainsi été synthétisé en choisissant soigneusement les paramètres expérimentaux. La réaction d’aza-Michael a ensuité été appliquée à un accepteur de Michael moins réactif, l’acide acrylique. Ce composé a la particularité de réagir instantanément et exothermiquement avec les amines par réaction acido-basique. Un déplacement de l’équilibre chimique de la réaction acido-basique vers la formation d’adduits de Michael a été rendu possible, générant ainsi des groupements zwitterioniques. Une étude approfondie de la réaction avec des amines organiques et des oligomères/polymères siliciés et aminés a été réalisée afin de déterminer la structure exacte des groupements fonctionnels obtenus et d’évaluer les propriétés visco-élastiques de tels produits. La dernière partie de ce projet a été focalisée sur l’étude et la caractérisation de ces matériaux silicones supramoléculaires s’échelonnant du liquide visco-élastique à l’élastomère silicone thermoplastique. / This PhD thesis was focused on the incorporation of functional groups onto the siloxane polymer backbone such that supramolecular assemblies are formed, in order to prepare new supramolecular silicone materials. First, an in-depth review of the aza-Michael reaction applied to silicon-containing compounds was realized, highlighting the whole potential of this addition reaction. The aza-Michael reaction applied to organic amines was thoroughly analyzed in order to emphasize some open issues such as selectivity or retro-aza-Michael reaction. In order to understand and master the aza-Michael reaction, a model reaction involving a bis-(3-aminopropyl)-terminated PDMS and butylacrylate was then fully investigated. Operating parameters such as protic polar solvents, catalysts or temperature allow promoting the reaction rate. Kinetic data showed that the selectivity towards the main formation of mono- or di-adduct can be controlled by carefully selecting the solvent nature and content. The syntheses of 100% mono- and 100% di-adduct compounds was succesfully achieved. The aza-Michael reaction was then applied to a less reactive Michael acceptor, i.e. acrylic acid. This unsaturated organic acid reacts instantaneously with amines by acid-base reaction leading to the formation of ionic pairs. This acid-base equilibrium is then shifted in the forward direction allowing the synthesis of zwitterionic groups by aza-Michael. The aza-Michael reaction of this peculiar Michael acceptor was thoroughly investigated both with simple organic amines and aminosilicone oligomers and polymers in order to elucidate the structures and to evaluate the rheological properties. Finally, supramolecular silicone materials bearing zwitterionic-like groups were prepared leading to supramolecular materials with properties ranging from visco-elastic liquids to thermoplastic silicone elastomers.

Motivation dieser Arbeit ist die Weiterentwicklung des etablierten Prozesses der Sprühtrocknung, der Trocknung einer Flüssigkeit zu Partikeln mit definierter Form und Größe. Ist die zerstäubte Flüssigkeit eine reagierende Polymer- oder Monomerlösung wird der neuartige Prozess als Sprühpolymerisation bezeichnet. Da die Verweilzeiten in einem Sprühtrockner gering sind, wird die hochreaktive radikalische Kettenpolymerisation von Acrylsäure und Acrylaten im Lösungsmittel Wasser untersucht. Im Fokus der Arbeit ist die Methode der Rheokinetik. Diese Methode wertet die rheologische Veränderung der reagierenden Lösung aus, sodass in dieser Arbeit die Ergebnisse der Rheokinetik zur Prozessgestaltung diskutiert werden. Die Messungen zur Rheokinetik verschiedener Acrylatelösungen zeigen im Vergleich zur Acrylsäure geringere Viskositätsanstiege, die sich durch die geringe Reaktionsgeschwindigkeit in der pH-neutralen Lösung der Acrylate erklären lässt. Die Theorie zur Rheokinetik lässt sich nur auf die Acrylsäure anwenden, da diese überwiegend neutrale Polymerlösungen bildet und die Viskositätsfunktion über die Zeit mit einer Potenzfunktion beschrieben werden kann. Das Ergebnis ist ein empirisches Modell, was die Induktionszeit und den Viskositätsanstieg, der mit dem Umsatz der Reaktion korreliert, über die Zeit beschreibt. Die numerische Modellierung, die die Polymerisation und Trocknung des Einzeltropfens beschreibt, zeigt abschließend, dass eine Konditionierung des Trocknungsgases sowie eine Vorreaktion vor der Sprühpolymerisation anzustreben sind, damit der Prozess in einem konventionellen Sprühtrockner erfolgreich wird.:1 Einleitung 2 Stand der Technik 2.1 Sprühpolymerisationsverfahren 2.1.1 Trocknung am Einzeltropfen 2.2 Rheologische Eigenschaften von Flüssigkeiten im Viskosimeter und Rheometer 2.2.1 Messmethoden der Scherviskosität 2.3 Charakterisierung der Monomere 2.4 Polymerisation von Acrylsäure bzw. Acrylaten 2.4.1 Radikalische Lösungspolymerisation 2.4.2 Überblick über die Reaktionskinetik der radikalischen Polymerisation 2.4.3 Weitere Reaktionstypen bei der radikalischen Polymerisation 2.4.4 Einfluss des Lösungsmittels auf die radikalische Polymerisation 2.4.5 Einflüsse auf die Terminierung bei der radikalischen Polymerisation 2.4.6 Übersicht zur Messung der Kinetik bei Polymerisationen 2.4.7 Momentenmethode zur Berechnung der Polymerisation 2.5 Charakterisierung der Polymere 2.5.1 Polymere im Lösungsmittel 2.5.2 Skalierungstheorie nach de Gennes von Polymeren in Lösungsmitteln 2.5.3 Messmethoden der molaren Masse von Polymeren in Lösungsmitteln 2.5.4 Viskosität von Polymerlösungen 2.5.5 Intrinsische Viskosität von Polymerlösungen 2.6 Rheokinetik 3 Experimentelle Methoden 3.1 Material – Monomere und Polymere 3.1.1 Neutralisation von Acrylsäure zur Herstellung der Acrylate 3.1.2 Stoffwerte von Acrylsäure und Wassermischungen 3.1.3 Versuchsvorbereitung und Versuchsplan 3.2 Messmethodik der Rheokinetik 3.2.1 Versuchsdurchführung 3.2.2 Berücksichtigung der Verdunstung aus dem Probevolumen 3.2.3 Bestimmung von Umsatz und Polymerisationsgrad 4 Ergebnisse zur Rheokinetik 4.1 Rheokinetik am wässrigen System mit Acrylsäure bzw. Acrylaten 4.1.1 Erläuterung zur Auswertungsprozedur an verschiedenen Rohdaten von Acrylsäure und Acrylaten 4.1.2 Ergebnisdiskussion zur Rheokinetik bei wässrigen Acrylsäure- bzw. Acrylatlösungen 4.2 Rheokinetik mit Modellbildung zur Polymerisation wässriger Acrylsäure Lösungen 4.2.1 Empirisches Modell zur Funktion η(t) 4.2.2 Modellierung der Rheokinetik 4.2.3 Bewertung der Rheokinetik durch Messungen von Umsatz und Viskosität im Rheometer 5 Numerische Modellierung von Reaktion und Trocknung 5.1 Numerische Modellierung der Reaktion im Rheometer 5.1.1 Ergebnisse der Momentenmethode für die Reaktion im Rheometer 5.2 Numerische Modellierung zur Reaktion im Sprühtrockner 5.2.1 Ergebnisse der Modellierung am Tropfen 6 Zusammenfassung und Ausblick 6.1 Ergebnisse zur Rheokinetik 6.2 Numerische Modellierung 6.3 Ausblick

Στην εργασία αυτή μελετήθηκε o ρυθμός ροής υδατικών διαλυμάτων, σε διάφορα pH περιβάλλοντος, διαμέσου ενός νανοπορώδους υλικού τροποποιημένου με πολυμερικές ψήκτρες. Ειδικότερα, ερευνήθηκε το σύστημα του σύνθετου υλικού πορώδους ανοδικής αλουμίνας με πολυμερικές ψήκτρες του γραμμικού δισυσταδικού συμπολυμερούς πολύ(Ισοπρένιου)–b–πολυ(Ακρυλικού Οξέους) (ΙΑΟ). Η προσρόφηση καθώς και η κινητική προσρόφησης του IAO στο νανοπορώδες υλικό διερευνήθηκε κυρίως μέσω τεχνικών δονητικής φασματοσκοπίας. Πιο συγκεκριμένα με τεχνικές υπερύθρου μετασχηματισμού κατά Φουριέ (Fourier Transform Infrared Spectroscopy ή FT-IR), εγγύ υπερύθρου (N-IR) και Αποσβεννύμενη Ολική Ανάκλαση στο μέσο υπέρυθρο (ATR-IR). Ακόμη, με σκοπό την ποσοτικοποίηση της προσροφημένης ποσότητας του ΙΑΟ εφαρμόστηκε η τεχνική της θερμοσταθμικής ανάλυσης (TGA). Τέλος, για την απόκτηση μιας λεπτομερούς εικόνας σχετικά με τη δομή του σύνθετου νανο-πορώδους υλικού τα δείγματα χαρακτηρίστηκαν και με ηλεκτρονική μικροσκοπία (SEM/EDS). / In the present study the flow rate of aqueous solutions of different pH values through a nanoporous material functionalized with polymeric brushes was investigated using spectroscopic and thermogravimetric methods. In particular, the system under study was a composite material of porous anodic alumina with polymeric brushes of the diblock copolymer poly(Isoprene)–b–poly(Acrylic Acid) (IAO). The adsorption and adsorption kinetics of the IAO onto nanoporous alumina were explored mainly through techniques of vibrational spectroscopy. More specifically Fourier Transformed Infrared Spectroscopy (FT-IR), Near Infrared (N-IR) and Attenuated Total Reflectance (ATR-IR) were employed for this purpose. Moreover, for the quantification of the adsorbed amount of IAO, thermogravimetric analysis was applied (TGA). Finally, to obtain a comprehensive picture of the structure of the nanoporous composite materials used in this study, samples were additionally characterized by electron microscopy (SEM/EDS).