Ce travail porte sur le processus de fabrication de microballons en mousse basse densité et le contrôle fin de leur forme (diamètre, épaisseur, densité, sphéricité, non-concentricité). Durant cette thèse nous nous sommes concentrés sur le critère de non-concentricité qui doit être inférieure à 1%. Les microballons sont synthétisés en utilisant un procédé de microencapsulation conduisant à une émulsion double, suivie d'une polymérisation thermique à 60°C. Selon la littérature, trois paramètres majeurs, la densité des trois phases, les déformations du microballon pendant le procédé et la cinétique de polymérisation ont une influence directe sur la non-concentricité des microballons. Les résultats obtenus ont montré que lorsque l'écart de densité entre la phase aqueuse interne et la phase organique augmente, la non-concentricité des microballons TMPTMA s'améliore. Un écart de densité de 0,078 g.cm-3 à 60°C conduit à une non-concentricité moyenne de 2,4% avec un rendement en microballons de 58%. Il a également été montré que la synthèse peut être considérée comme reproductible. Pour une même phase aqueuse interne, les résultats de non-concentricité sont équivalents en utilisant soit un tube droit, un tube à étranglement ou un serpentin court. Le temps requis pour fixer la forme des microballons est d'au moins 20 minutes avec la polymérisation thermique. Ainsi, il semble que le temps passé par les microballons à l'intérieur des bouteilles de réception permet le centrage de la phase aqueuse interne à l'intérieur de la phase organique, quel que soit le processus de circulation précédemment utilisé. Afin d'obtenir des vitesses de polymérisation plus élevées et d'éviter les phénomènes de déstabilisation, nous avons alors concentré notre étude sur la photopolymérisation. Lorsque la synthèse est effectuée en utilisant une lampe UV avec une intensité lumineuse efficace, les microballons ont une épaisseur légèrement supérieure à celle des microballons synthétisés par voie thermique. Par ailleurs, un rendement plus élevé, environ 80%, est obtenu avec la polymérisation UV. Toutefois, la non-concentricité moyenne des microballons synthétisés est environ de 20%, ce qui est vraiment élevé par rapport à la non-concentricité moyenne de 2,4% obtenue par polymérisation thermique. Il serait intéressant d'exposer les microballons à la lumière UV, à différents moments après la collecte afin d'étudier l'influence du temps d'agitation sur la non-concentricité des microballons. / This work deals with the fabrication process of low density foam shells and the sharp control of their shape (diameter, thickness, density, sphericity, non-concentricity). During this PhD we focused on the non-concentricity criterion which has to be lower than 1%. The shells are synthesized using a microencapsulation process leading to a double emulsion and followed by a thermal polymerization at 60°C. According to the literature, three major parameters, the density of the three phases, the deformations of the shells along the process and the kinetics of the polymerization have a direct influence on the shells non-concentricity. The results obtained showed that when the density gap between the internal water phase and the organic phase increases, the TMPTMA shells non-concentricity improves. A density gap of 0.078 g.cm-3 at 60°C, leads to an average non-concentricity of 2.4% with a yield of shells of 58%. It was also shown that the synthesis process can be considered as reproducible. While using the same internal water phase, equivalent non-concentricity results are obtained using either a straight tube, a tube with areas of constriction or a short wound tube. The time required to fix the shell’s shape is at least 20 minutes with thermal polymerization. So, it seems that the time spent by the shells inside the rotating flask allows the centering of the internal water phase inside the organic phase, whatever the circulation process used. In order to get higher polymerization rates and to avoid destabilization phenomena, we then focused our study on photopolymerization. When the synthesis is performed using a UV lamp with an efficient light intensity, the shells have a slightly higher thickness than the shells synthesized by thermal polymerization. Moreover, a really higher yield, around 80%, is achieved with UV polymerization. However, the average non-concentricity of the shells synthesized lays around 20%, which is really high compared to the 2.4% average non-concentricity obtained with thermal polymerization. It would be interesting to expose the shells to UV light at different times after collection in order to study the influence of the agitation time on the shells non-concentricity.

In the present era where MEMS (Micro Electro-Mechanical Systems) technology is in¬evitable from the perspective of applications in non-silicon based micro-devices (such as biosensors, microfluidics, microvalves etc.), it is imperative to develop different micro¬fabrication technologies which are simple in operation, have low operational cost and high versatility in terms of incorporating different materials. The microfabrication tech¬nologies (e.g: bulk micromachining, surface micromachining, X-ray LIGA (lithoqraphie galvanoformung abformung) etc.), which exist commercially are mostly limited to sili¬con based technologies. They are either constrained in fabricating complex geometry in micro dimension or have high operational cost. Microstereolithography (MSL) is one such rapid prototyping technique, which can satisfy the above requirements to a larger extent. MSL h8B evolved in the l8Bt decade from conventional stereolithographic (SLA) technique, which involves the free-form microfabrication of a UV sensitive liquid resin layer by layer photo-polymerization process, when it is exposed to UV irradiation accord¬ing to the predefined CAD (Computer Aided Design). However, this technique is not limited to polymer microfabrication and it h8B an immense potential to fabricate com¬plex 3D structures of ceramics in micro dimension. In this thesis, the primary focus is on developing an in house built scanning b8Bed MSL system indigenously and to explore the possibility of micro fabrication of different materials (from polymer to ceramics involving different routes. In addition, polymer micro cantilever h8B been fabricated using this technique and its application to surface stress me8Burement h8B been demonstrated. The thesis comprises of eight chapters. The following section describes the summary of the individual chapters. Chapter 1 describes the introduction and background literature of this technol¬ogy. A brief review on MSL technology developed by various research groups and their achievements h8B been listed. Since photopolymerizable resin is the primary material to fabricate micro dimensional structures, the rate of photopolymerization is an impor¬tant phenomena which requires an attention before choosing the photopolymerizable resin. Further, this chapter also describes the photoinitiation principles and the type of photo initiators (PI) which help to photopolymerize the resin in order to fabricate micro dimensional polymer structures. In addition, this chapter also gives a glimpse of applications of this technology in fabrication of micro cantilever b8Bed sensors. The later part of the chapter focused on the microfabrication of ceramic from colloidal and met¬alorganic routes in brief. In Chapter 2, the design of the in house built MSL system and its working princi¬ples including various optical issues have been addressed. Several research groups have attempted to optimize photopolymerization parameters to incre8Be the throughput of the scanning b8Bed MSL systems through modified beam scanning techniques. Efforts in reducing the curing line width in order to get low feature size have been implemented through high numerical aperture (NA) optical setups. However, the intensity contour symmetry and the depth of field of focus have led to grossly non-vertical and non-uniform curing profiles. The focus of the work h8B been to exploit the rich potential of photoreactor scanning system in achieving desired fabrication modalities (minimum curing width, uniform depth profile, and vertical curing profile) even with a reduced NA optical setup and a single movable stage. The present study tries to manipulate to its advantage the effect of optimized lower photoinitiator (PI) concentration ([c]) in reduc¬ing the minimum curing width to 10-15 jJm, even with the higher spot size (21.4 jJm) rv through a judiciously chosen gmonomer UPIi' system. In this chapter, two different cl8BS of multifunctional acrylates (1,6 Hexane diol diacrylate (HDDA) and Trimethylol propanetriacrylate (TMPTA)) and one monofunctional methacrylate (methyl mathacry¬late (MMA)) have been chosen to explore their fabricability in micro dimensions using this MSL technology, by varying the various operational parameters including the type and the concentration of the PI. Chapter 3 deals with the application of this technology in micro cantilever based sensors. Microcantilever based sensors have been explored for several decades for their application in bio-molecular or explosive detection, chemical sensing etc. Due to the adsorption of molecular species on the cantilever surface, differential surface stress gen¬erates between the top and bottom surface of the cantilever. Depending on the type of stress (tensile or compressive) generated, the cantilever bends accordingly. The, novel diffraction based deflection method has been proposed in order to measure the deflection profile accurately for low dimensional structures. To prove this method, a dual mi¬crocantilever structure with sufficiently low gap (100 f.lm) has been fabricated using the developed MSL set up, such that diffraction occurs during transillumination by spherical wavefronts. Among the two micro cantilevers one was fabricated bent with a specific di¬mension with respect to the other. The cantilever material was chosen as poly HDDA for its low elastic modulus in order to achieve high sensitivity. From the obtained diffraction pattern, the bent profile of the each cross section of one cantilever corresponding to the other has been measured. This proposition will enable to measure surface stress at each cross section of the cantilever depending on the adsorbed analyte molecule adsorption. In Chapter 4, an effort has been made to improve the thermal, thermo mechanical and mechanical properties of the cantilever material (poly HDDA). The sensitivity of a micro cantilever depends precisely on fabrication and material aspects. The former de¬pends on the aspect ratio of the structure and can be controlled by fabrication parameters whereas the latter is inherently limited by the choice of the material. The properties of the material which impact the applicability are elastic modulus, Poisson's ratio, thermal expansion and thermal stability. Hence, these properties are studied for poly HDDA. However, the properties are not completely satisfactory for only poly HDDA (PHDDA) since, PHDDA will fail for high surface stress measurement (>275 mN/m). Hence, it h8B been copolymerized with MMA with an intention to improve the above mentioned properties and to determine the best composition for the micro cantilever application. It is observed by Finite Element Analysis (FEM) that Phpm5050 (HDDA:MMA(50:50)) composition shows optimum sensitivity when reliability is concerned for me8Buring high surface stress (275 mN/m). Chapter 5 bridges Chapter 2 and Chapter 6. Chapter 2 highlights the polymer mi¬crofabrication where8B, Chapter 6 deals with the microfabrication of ceramics. In order to fabricate ceramic micro objects by MSL, ceramic particles need to be blended with a photopolymerizable monomer followed by l8Ber induced photopolymerization . Under l8Ber irradiation, the monomer gets cured and traps the ceramic particles. Thus near net shape of green ceramic structures are 0 btained. After achieving the near net shape, it is important to remove the polymer, which acts 8B the binder for the green ceramic body. This debinding should be diffusion controlled so 8B to achieve defect free micro ceramics. Here two multifunctional monomers (HDDA and TMPTA) have been chosen 8B a b8Be monomer for fabricating ceramics. Therefore it is essential to understand the debinding mechanism of these polymers. However, (HDDA) h8B high shrinkage upon polymeriza¬tion with low rate of polymerization kinetics and low viscosity where8B the properties of (TMPTA) are exactly opposite. Hence, in order to optimize these properties, copoly¬merization of HDDA and TMPTA h8B been carried out for different compositions and their thermal properties have been investigated to understand the degradation mech¬anism. This chapter deals with the mechanism of thermal degradation by model free kinetic methods with an intention to determine the optimum composition of HDDA and TMPTA copolymer, to used 8B the b8Be monomer material for ceramic microfabrication. Besides, the debinding strategy is also discussed b8Bed on the degradation profile of the optimum composition. TH20S0(TMPTA: HDDA(20:S0)) is found to be the ideal com¬position to fabricate ceramic micro-component by MSL since its degradation is diffusion controlled in N 2 atmosphere. Chapter 6 describes the methodology of microfabrication of ceramics by the de-veloped MSL technique. A colloidal approach has been adopted to fabricate ceramics in micro-dimensions. Two different ceramics have been chosen, which have potential applications in structural (alumina) and functional (Lead Iron Niobate (PFN))aspects. Before fabricating ceramic micro-objects, ceramic particles need to be blended in the monomer suspension in the presence of dispersant at an optimum solids loading. Opti¬mization of solids loading is important in view of low dimensional shrinkage after sin¬tering. However, lower loading leads to higher shrinkage whereas higher loading would increase the viscosity of the suspension and make the suspension inconvenient to deal with. Hence, rheological studies have been carried out to optimize the solids loading and dispersant concentration. 40 vol% alumina and 35 vol% PFN are found to be the highest achievable solids loading for the chosen monomer (TH2080) composition. This chapter also describes the limitation involved in ceramic microfabrication depending on their scattering factors during laser irradiation. The chapter demonstrates the fabrica¬tion methodology of several complex ceramic(alumina and PFN) micro-objects by the in house built MSL instrument. Chapter 7 investigates the possibility of microfabrication of ceramics from metalor¬ganic precursor. In this route, titanium metal-organic (Ti-n butoxide) precursor has been chosen which is stabilized by the addition of chelating monomer (2-( methacryloyloxy) ethyl acetoacetate). Following this, the crosslinker and photoinitiators have been added to form Ti photoresist which is coated on top of the bare silicon substrate by spin coating to achieve specific thickness. The coated silicon wafer by the above photoresist has been patterned by selectively exposure in the MSL setup. The cured patterns are washed and heat treated at high temperature in order to 0 btain the net shape of the Ti02 pattern of polycrystalline rutile phase. It is observed this route is advantageous in terms of reduc¬ing curing dimension (curing width 14 f.lm) than the colloidal route (curing width more than 80 f.lm ) of fabrication of ceramics where the scattering factor greatly influences the dimensions of the feature size. The key findings and future aspects are summarized in the Chapter 8. The work reported in this thesis has been carried out by the candidate as part of the Ph.D. programme. He hopes that this would constitute a worthwhile contribution towards developing an MSL technique and its aspects in micro fabrication of polymer and ceramic structures of any complex shape and its possible applications in microdevices.

Photo-initiated reactions involve the use of ultraviolet (UV) or visible light radiation to effect chemical transformations. Some of the advantages of photo-initiated reactions over thermal or high pressure reactions include mild reaction conditions like ambient temperature and pressure, good control over the reaction by the simple switching on/off the light source, and faster reaction kinetics. Usually, semiconductor photocatalysts or oxidizing agents are used to enhance the rate of photo reactions. “Photocatalysis” involves the generation of valence band holes and conduction band electrons by the band gap excitation of a semiconductor photocatalyst. These charge carriers produce reactive hydroxyl and superoxide radicals, which mediate oxidation and reduction reactions. However, the oxidizing agents are decomposed by the incident radiation to generate reactive radicals, which accelerate the photo reaction. Today, photocatalysis and photo-oxidative reactions are widely being practiced for environmental pollution abatement, synthesis of fine chemicals, synthesis of polymers, generation of hydrogen as a clean energy carrier, and in anti-fogging and self-cleaning surface treatments. The present investigation focuses on elucidating the mechanism and kinetics of environmentally and synthetically relevant photo-initiated reactions for a better understanding of the fundamental aspects of the photo processes. The different photo-initiated reactions studied in this dissertation can be grouped under the broad categories of (i) photocatalytic degradation of organic compounds like dyes and phenols, and reduction of metal ions, (ii) photocatalytic degradation of polymers, (iii) selective photocatalytic oxidation of cyclohexane, (iv) sonophotocatalytic degradation of dyes, (v) photopolymerization, and (vi) sonophotooxidative degradation of polymers. Nano-sized TiO2, synthesized by solution combustion technique (henceforth denoted as CS TiO2), was used as the photocatalyst for most of the above reactions, except for the last two polymer reactions, where organic initiators were used. Invariably, the photocatalytic activity of CS TiO2 was compared with the commercially available Degussa P-25 TiO2 (DP25). Based on the experimental results, detailed mechanisms were proposed for the different reactions, kinetic models were derived, and the rate coefficients signifying the importance of the underlying reaction steps were evaluated. Pd2+ substituted and Pd0 impregnated TiO2 were synthesized by solution combustion and reduction techniques, respectively, and characterized by powder XRD, XPS, TEM, BET surface area, UV/visible, TGA, FT-IR and photoluminescence measurements. While the above catalysts are known to be more active compared to CS TiO2 for the gas phase NO reduction and NO decomposition reactions, it was found in this study, that these catalysts exhibit lower activity for the degradation of organic compounds like dyes, phenol and 4-chlorophenol, in the aqueous phase. The decrease in activity was correlated with a reduction in surface area and photoluminescence intensity of these catalysts, compared to CS TiO2. Ag+ substituted (Ag sub) and Ag0 impregnated (Ag imp) nano-TiO2 were synthesized by solution combustion and reduction techniques, respectively, and characterized by the above standard measurements. These catalysts were used for the photodegradation of dyes, and the selective photooxidation of cyclohexane to cyclohexanone. For the photocatalytic degradation of dyes, unsubstituted CS TiO2 exhibited the highest activity, followed by 1% Ag imp and 1% Ag sub. However, for the photooxidation of cyclohexane, the total conversion of cyclohexane and the selectivity of cyclohexanone followed the order: 1% Ag sub > DP-25 > CS TiO2 > 1% Ag imp. The kinetics of photodegradation of the dyes and the photooxidation of cyclohexane was modeled using Langmuir-Hinshelwood rate equation, and a free radical mechanism, respectively. This study proves that the photoactivity of a catalyst is not solely determined by a single physical property, but rather by a number of variables including the surface area, band gap, surface hydroxyl content, oxide ion vacancy and surface charge of the catalyst. The photocatalytic degradation of five anionic, eight cationic and three solvent dyes, containing different functional groups, was evaluated. The degradation of the dyes was quantified using the initial rate of decolorization and overall percent mineralization. The decolorization of the anionic dyes with CS TiO2 followed the order: Indigo Carmine > Eosin Y > Amido Black 10B > Alizarin Cyanine Green > Orange G. The decolorization of the cationic dyes with DP-25 followed the order: Malachite Green > Pyronin Y > Rhodamine 6G > Azure B > Nile Blue Sulfate > Auramine O ≈ Acriflavine ≈ Safranin O. CS TiO2 exhibited higher rates of decolorization and mineralization for all the anionic dyes, while DP-25 was better in terms of decolorization for most of the cationic dyes. The solvent dyes exhibited adsorption dependent decolorization. The observed results were rationalized based on the molecular structure and degradation pathway of the dyes. The simultaneous photocatalytic degradation of phenolic compounds like phenol and 4-nitrophenol, and the reduction of metal ions like copper (Cu2+) and chromium (Cr6+) were studied. It was found that the presence of phenol accelerated the reduction of Cu2+ to Cu+, and the presence of phenol and 4-nitrophenol accelerated the adsorption of Cr6+ onto CS TiO2. A detailed dual-cycle, multi-step reaction mechanism was proposed for the simultaneous degradation and reduction, and a model was developed using the network reduction technique. The kinetic rate constants in the model were evaluated for the systems studied. The simultaneous UV and ultrasound (US) degradation of anionic dyes was carried out in presence of CS TiO2. The rates of degradation and mineralization of the dyes were higher for the sonophotocatalytic process compared to the individual photo-and sonocatalytic processes. The effect of dissolved gases and US intensity on the sonophotocatalytic degradation of the dyes was evaluated. A dual-pathway network mechanism of sonophotocatalytic degradation was proposed for the first time, and the rate equations were modeled using the network reduction technique. The kinetic rate coefficients of the individual steps were evaluated for all the systems by fitting the model with the experimental data. Eosin Y and Fluorescein dye sensitized visible light degradation of phenol, 4chlorophenol, 2,4-dichlorophenol and 2,4,6-trichlorophenol was studied. A detailed mechanism of sensitized degradation was proposed, and a mechanistic model for the rate of degradation of the phenolic compound was derived by using the pyramidal network reduction technique to evaluate the rate coefficients. An important conclusion of this study indicates that at low initial dye concentrations, the rate of degradation of the phenolic compound is first order in the concentration of the dye, while at high initial dye concentrations, the rate is first order in the concentration of the phenolic compound. The different phenolic and dye intermediates that were formed during degradation were identified by mass spectrometry, and a most probable pathway of degradation was proposed. The solution photopolymerization of methyl-, ethyl-, butyl-and hexylmethacrylates in presence of benzoyl peroxide as the initiator was studied. The effect of initiator and monomer concentrations on the time evolution of polymer concentration, number average molecular weight (Mn) and polydispersity (PDI) was examined. The reversible chain addition and β-scission, and primary radical termination steps were included in the mechanism along with the classical initiation, propagation and termination steps. The rate equations were derived using continuous distribution kinetics and solved numerically to fit the experimental data. The model predicted the instantaneous increase of Mn and PDI of the polymers to steady state values. The rate coefficients exhibited a linear increase with the size of the alkyl chain of the alkyl methacrylates. Poly(acrylamide-co-acrylic acid) copolymers of different compositions were synthesized and characterized. The copolymers were statistical with a relatively high percentage of acrylamide units, as determined by 13C-NMR. The aqueous phase photolytic and photocatalytic degradation of the copolymers and the homopolymers was conducted. The degradation was modeled using continuous distribution kinetics. The degradation followed a two step mechanism, wherein the rapid first step comprised of the scission of weak acrylic acid units along the chain, which was followed by the breakage of the relatively strong acrylamide units. The rate constants for the weak and strong links followed a linear trend with the percentage of acrylic acid and acrylamide in the copolymer, respectively. The photocatalytic degradation of the copolymers of methyl methacrylate with butyl methacrylate (MMA-BMA), ethyl acrylate (MMA-EA) and methacrylic acid (MMA-MAA) was carried out in toluene. The copolymers and the corresponding homopolymers degraded randomly along the chain. The degradation rate coefficient was determined using continuous distribution kinetics. The time evolution of the hydroxyl and hydroperoxide stretching vibration in the FT-IR spectra of the copolymers indicated that the degradation rate follows the order: MMA-MAA > MMA-EA > MMA-BMA. The photodegradation rate coefficients were compared with the activation energy of pyrolytic degradation. The observed contrast in the order of thermal stability compared to the photostability of these copolymers was attributed to the two different mechanisms governing the scission of the polymers and the evolution of the products. The mechano-chemical degradation of poly(methyl methacrylate), poly(ethyl methacrylate) and poly(n-butyl methacrylate) using US and UV radiation, in presence of benzoin as the photoinitiator, was carried out. A degradation mechanism that included the decomposition of the initiator, generation of polymer radicals by hydrogen abstraction of the initiator radicals, and reversible chain transfer between the stable polymer and the polymer radicals, was proposed. The mechanism assumed mid-point chain scission due to US and random chain scission due to UV radiation. The steady state evolution of PDI was successfully predicted by the continuous distribution kinetics model. The rate coefficients of polymer scission due to US and UV radiation exhibited a linear increase and decrease with the size of the alkyl group of the poly(alkyl methacrylate)s, respectively.

Polymer brush patterns were prepared by a combination of electron beam induced damage in self-assembled monolayers (SAMs), creating a stable carbonaceous deposit, and consecutive self-initiated photografting and photopolymerization (SIPGP). This newly applied technique, reactive writing (RW), is investigated with 1H,1H,2H,2H-perfluorooctyltriethoxysilane SAM (PF-SAM) on silicon oxide, which, when modified by RW, can be selectively functionalized by SIPGP. With the monomer N,N-dimethylaminoethyl methacrylate (DMAEMA), we demonstrate the straightforward formation of polymer brush gradients and single polymer lines of sub-100 nm lateral dimensions, with high contrast to the PF-SAM background. The lithography parameters acceleration voltage, irradiation dose, beam current and dwell time were systematically varied to identify the optimal conditions for the maximum conversion of the SAM into a carbonaceous deposit. The results of this approach were compared to patterns prepared by carbon templating (CT) under analogous conditions, revealing a dwell time dependency, which differs from earlier reports. This new technique expands the range of CT by giving the opportunity to not only vary the chemistry of the created polymer patterns with monomer choice but also vary the chemistry of the surrounding substrate.

Aim of magister´s thesis was to study reaction kinetics of dental materials. Thesis was focused on dimethacrylate dental polymers, which are for example used for dental restoration, tooth repair and creating now teeth. First part of the thesis concentrates on influence of molar ratio on reation kinetics by addition of other monomer to polymer resin. Second part concentrates on influence of addition of additive silica on reaction kinetics of polymerization. Essential variables know as a polymerization ratio, conversion, gel point, glass transition temperature and storage modulus were studied. Firstly, polymerization ratio and conversion were observed by differential scanning calorimetry (DSC). Secondly rheology was observed by photoreometr. Finally, glass transition temperature and storage modulus were observed by dynamic mechanical analysis (DMA). Behaviour changes caused by addion of monomer or filler point out decrease of polymeration ratio and converstion. Same behaviour was observed by short exposure. In order to established network formation, values of gel point increased by higher concentration of monomer or filler. Glass transition temperature and storage modulus measured by DMA were evaluated. Those valuables had variable tendency due to monomer acting like filler at higher concentration. Also contradictory impact of different material conversion and filler concetration was discussed.

Photopolymerization is a technique used to create surface structures or microobjects from a photoresist. This process is started by illuminating the sample with a light of proper wavelength absorbed by the resist. After exposure, the sample is processed according to the type of the photoresist – be it heating, treating with developer or just washing the unaffected monomer with some reagent. Focused femtosecond laser beam with double wavelength can be used in the process. Short pulse length with high photon density starts two-photon absorption localized in the vicinity of focal point. The method resolution is thus increased and details with 1/10 micrometer size can be created. Moreover, very short laser pulse decreases the heat affected zone and the risk of thermal initiation is minimized. Manufacturing of larger structures composed of tiny details with two-photon photopolymerization is time-demanding process. Therefore, we have complemented the optical setup with spatial light modulator (SLM), which splits the incoming laser beam into several beams with holograms dynamically generated by a computer. Polymerization can be thus performed by multiple foci simultaneously which can be used to create separated microparticles or periodical surface structures. Additional speed improvement of the process can be substitution of static configuration, requiring sample replacement after each exposition, with continuous setup using microfluidic channel steadily supplied with photoresist transported to the active region of the sample.

Plant derived oils bear intrinsic double-bond functionality that can be utilized directly for the thiol–ene reaction. Although terminal unsaturations are far more reactive than internal ones, studies on the reversible addition of thiyl radicals to 1,2-disubstituted alkenes show that this is an important reaction. To investigate the thiol–ene coupling reaction involving these enes, stoichiometric mixtures of a trifunctional propionate thiol with monounsaturated fatty acid methyl esters (methyl oleate or methyl elaidate) supplemented with 2.0 wt.% Irgacure 184 were subjected to 365-nm UV-irradiation and the chemical changes monitored. Continuous (RT– FTIR) and discontinuous (NMR and FT–Raman) techniques were used to follow the progress of the reaction and reveal details of the products formed. Experimental results supported by numerical kinetic simulations of the system confirm the reaction mechanism showing a very fast cis/trans-isomerization of the alkene monomers (<1.0 min) when compared to the total disappearance of double-bonds, indicating that the rate-limiting step controlling the overall reaction is the hydrogen transfer from the thiol involved in the formation of final product. The loss of total unsaturations equals thiol consumption throughout the entire reaction; although product formation is strongly favoured directly from the trans-ene. This indicates that initial cis/trans-isomer structures affect the kinetics. High thiol–ene conversions could be easily obtained at reasonable rates without major influence of side-reactions demonstrating the suitability of this reaction for network forming purposes from 1,2-disubstituted alkenes. To further illustrate the validity of this concept in the formation of cross-linked thiol–ene films a series of globalide/caprolactone based copolyesters differing in degree of unsaturations along the backbone were photopolymerized in the melt with the same trithiol giving amorphous elastomeric materials with different thermal and viscoelastic properties. High thiol–ene conversions (>80%) were easily attained for all cases at reasonable reaction rates, while maintaining the cure behaviour and independent of functionality. Parallel chain-growth ene homopolymerization was considered negligible when compared with the main coupling route. However, the comonomer feed ratio had impact on the thermoset properties with high ene-density copolymers giving networks with higher glass transition temperature values (Tg) and a narrower distribution of cross-links than films with lower ene composition. The thiol–ene systems evaluated in this study serve as model example for the sustainable use of naturally-occurring 1,2-disubstituted alkenes at making semi-synthetic polymeric materials in high conversions with a range of properties in an environment-friendly way. / Vegetabiliska oljor som innehåller dubbelbindningar kan användas direkt för thiolene reaktioner. Trots att terminala dubbelbindningar är mycket mer reaktiva än interna visar dessa studier att den reversibla additionen av thiyl radikaler till 1,2-disubstituerade alkener är en viktig reaktion. För att undersöka tiol–ene reaktionerna, som ivolverar dessa alkener förbereddes stökiometriska blandningar av en trifunktionell propionat tiol och enkelomättade fettsyrametylestrar (metyloleat eller metyl elaidat) samt 2.0 vikt.% Irgacure 184. Dessa blandningar utsattes för 365-nm UV strålning och de kemiska förändringarna studerades. De kemiska förändringarna analyserades med olika kemiska analysmetoder; realtid RT–FTIR, NMR och FT–Raman. Dessa användes för att analysera de kemiska reaktionerna i realtid och följa bildandet av produkterna. Reaktionsmekanismen bekräftades med hjälp av experimentella data och beräkningar av numeriska och kinetiska simuleringar för systemet. Resultaten visar en mycket snabb cis/trans-isomerisering av alkenmonomeren (<1.0 min) jämfört med den totala förbrukningen av dubbelbindningarna, vilket indikerar att det hastighetsbegränsande steget kontrolleras av väteförflyttningen från tiolen till slutprodukten. Förbrukningen av den totala omättade kolkedjan är lika med tiolförbrukningen under hela reaktionen, även om bildandet av produkten gynnas från trans-enen. Detta indikerar att den första cis/trans-isomerstrukturen påverkar kinetiken. Höga tiol-ene utbyten kan enkelt erhållas relativt snabbt utan inverkan av sidoreaktioner. Detta innebär att denna reaktion kan användas som nätverksbildande reaktion för flerfunktionella 1,2-disubstituted alkenmonomerer. Vidare användes fotopolymerisation i smälta på en serie globalid/kaprolaktonbaserade sampolyestrar med varierad grad av omättnad med samma tritiol vilket resulterade i bildandet av amorfa elastomeriska material med olika termiska och viskoelastiska egenskaper. Hög omsättning (>80%) uppnåddes relativt enkelt för samtliga blandningar oberoende av den initiala funktionaliteten. Homopolymerisation av alkenen var försumbar i jämförelse med den tiol–en-reaktionen. Mängden alkengrupper har inverkan på härdplastsegenskaperna där en hög andel alken ger en nätstruktur med högre glastransitionstemperatur (Tg). Tiol–ene reaktionen utvärderades i modellsystem baserade på naturlig förekommande 1,2-disubstituterade alkener för att demonstrera konceptet med tiol-förnätade halvsyntetiska material. / QC 20110915

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Ceria (cerium oxide) nanomaterials, or nanoceria, have commercial catalysis and energy storage applications. The cerium atoms on the surface of nanoceria can store or release oxygen, cycling between Ce3+ and Ce4+, and can therefore act as a therapeutic to relieve oxidative stress within living systems. Nanoceria dissolution is present in acidic environments in vivo. In order to accurately define the fate of nanoceria in vivo, nanoceria dissolution or stabilization is observed in vitro using acidic aqueous environments. Nanoceria stabilization is a known problem even during its synthesis; in fact, a carboxylic acid, citric acid, is used in many synthesis protocols. Citric acid adsorbs onto nanoceria surfaces, capping particle formation and creating stable dispersions with extended shelf lives. Nanoceria was shown to agglomerate in the presence of some carboxylic acids over a time scale of up to 30 weeks, and degraded in others, at pH 4.5 (representing that of phagolysosomes). Sixteen carboxylic acids were tested: citric, glutaric, tricarballylic, α-hydroxybutyric, β-hydroxybutyric, adipic, malic, acetic, pimelic, succinic, lactic, tartronic, isocitric, tartaric, dihydroxymalonic, and glyceric acid. Each acid was introduced as 0.11 M, into pH 4.5 iso-osmotic solutions. Controls such as ammonium nitrate, sodium nitrate, and water were also tested to assess their effects on nanoceria dissolution and stabilization. To further test stability, nanoceria suspensions were subject to light and dark milieu, simulating plant environments and biological systems, respectively. Light induced nanoceria agglomeration in some, but not all ligands, and is likely to be a result of UV irradiation. Light initiates free radicals generated from the ceria nanoparticles. Some of the ligands completely dissolved the nanoceria when exposed to light. Citric and malic acids form coordination complexes with cerium on the surface of the ceria nanoparticle that can inhibit agglomeration. This approach identifies key functional groups required to prevent nanoceria agglomeration. The impact of each ligand on nanoceria was analyzed and will ultimately describe the fate of nanoceria in vivo. In addition, simulated biological fluid (SBF) exposure can change nanoceria’s surface properties and biological activity. The citrate-coated nanoceria physicochemical properties such as size, morphology, crystallinity, surface elemental composition, and charge were determined before and after exposure to simulated lung, gastric, and intestinal fluids. SBF exposure resulted in either loss or overcoating of nanoceria’s surface citrate by some of the SBF components, greater nanoceria agglomeration, and small changes in the zeta potential. Nanocomposites are comprised of a polymer matrix embedded with nanoparticles. These nanoparticles can alter material and optical properties of the polymer. SR-399 (dipentaerythritol pentaacrylate) is a fast cure, low skin irritant monomer that contains five carbon-carbon double bonds (C=C). It is a hard, flexible polymer, and also resistant to abrasion. It can be used as a sealant, binder, coating, and as a paint additive. In this case, metal oxide nanoparticles were added to the monomer prior to polymerization. Titania nanoparticles are known to absorb UV light due to their photocatalytic nature. Titania nanoparticles were chosen due to their high stability, non-toxicity, and are relatively quick, easy, and inexpensive to manufacture. Channels in thin monomer films were created using a ferrofluid manipulated by magnetic fields. The mechanical properties of a microfluidic device by rapid photopolymerization is dependent on the crosslinking gradient observed throughout the depth of the film. Quantitative information regarding the degree of polymerization of thin film polymers polymerized by free radical polymerization through the application of UV light is crucial to estimate material properties. In general, less cure leads to more flexibility, and more cure leads to brittleness. The objective was to quantify the degree of polymerization to approximate the C=C concentration and directly relate it to the mechanical properties of the polymer. Polymerization of C=C groups was conducted using a photoinitiator and an UV light source from one surface of a thin film of a multifunctional monomer. The C=C fraction in the film was found to vary with film depth and UV light intensity. The extents of conversion and crosslinking estimates were compared to local mechanical moduli and optical properties. A mathematical model linking the mechanical properties to the degree of polymerization, C=C composition, as a function of film depth and light intensity was then developed. For a given amount of light energy, one can predict the hardness and modulus of elasticity. The correlation between the photopolymerization and the mechanical properties can be used to optimize the mechanical properties of thin films within the manufacturing and energy constraints, and should be scalable to other multifunctional monomer systems.

Ultrasound directed self-assembly (DSA) utilizes the acoustic radiation force associated with a standing ultrasound wave field to organize particles dispersed in a fluid medium into specific patterns. The ability to tailor the organization and packing density of spherical particles using ultrasound DSA in a viscous fluid medium is crucial in the context of (additive) manufacturing of engineered materials with tailored properties. However, the fundamental physics of the ultrasound DSA process in a viscous fluid medium, and the relationship between the ultrasound DSA process parameters and the specific patterns of particles that result from it, are not well-understood. Researchers have theoretically described the acoustic radiation force and the acoustic interaction force that act on spherical particles in a standing ultrasound wave field in both inviscid and viscous media. In addition, they have solved the forward and inverse ultrasound DSA problem in an inviscid medium, in which they relate the patterns of particles and the ultrasound DSA operating parameters. However, no theoretical model exists that allows simulating the steady-state and transient local particle packing density in a viscous medium during ultrasound DSA. Thus, in this dissertation, we (i) theoretically derive and experimentally validate a model to determine the steady-state locations where spherical particles assemble during ultrasound DSA as a function of medium viscosity and particle volume fraction. (ii) We also theoretically derive and experimentally validate a model to quantify the steady-state and transient local packing density of spherical particles within the pattern features that result from ultrasound DSA. Using these models, we quantify and predict the locations where spherical particles assemble during ultrasound DSA in a viscous medium, considering the effects of medium viscosity and particle volume fraction. We demonstrate that the deviation between locations where particles assemble in viscous and inviscid media first increases and then decreases with increasing particle volume fraction and medium viscosity, which we explain by means of the sound propagation velocity of the mixture. In addition, we quantify and predict the steady-state and transient local packing density of spherical particles within the pattern features, using ultrasound DSA in combination with vat photopolymerization (VP). We show that the steady-state local particle packing density increases with increasing particle volume fraction and increases with decreasing particle size. We also show that the transient local particle packing density increases with increasing particle volume fraction, decreasing particle size, and decreasing fluid medium viscosity. Increasing particle size and decreasing fluid medium viscosity decreases the time to reach steady-state. Finally, we implement single and multiple scattering in the calculation of the acoustic radiation force for spherical particles in a viscous medium and quantify their relative contributions to the calculation of the acoustic radiation force as a function of ultrasound DSA operating parameters and material properties. We demonstrate that the deviation between considering single and multiple scattering may reach up to 100%, depending on the ultrasound DSA process parameters and material properties. Also, increasing the particle volume fraction increases the need to account for multiple scattering. Quantifying and predicting the local packing density of spherical particles during ultrasound DSA in a viscous medium, as a function of ultrasound DSA process parameters is crucial towards using ultrasound DSA in engineering applications, in particular (additive) manufacturing of engineered polymer matrix composite materials with tailored properties whose properties depend on the spatial organization and packing density of particles in the matrix material. / Doctor of Philosophy / Ultrasound directed self-assembly (DSA) is a technique that uses ultrasound waves to arrange small particles submerged in a fluid into specific patterns. When combined with other manufacturing techniques, ultrasound DSA can be used to fabricate composite materials that derive their properties from the spatial organization of particles in a matrix material. However, ultrasound DSA in viscous fluids is not well-understood. Researchers have studied the forces associated with ultrasound waves that move small spherical particles in an inviscid fluid medium (fluids that experience little to no internal resistance to flow), and they have demonstrated intricate control of the patterns of particles that form using ultrasound DSA. However, that knowledge is not currently available for ultrasound DSA in viscous media. In this dissertation, we develop and evaluate theoretical models to understand ultrasound DSA of small spherical particles in a viscous fluid medium. We simulate where particles organize and how densely they pack together. We also determine the difference of the time-dependent motion of particles in a viscous fluid compared to that in an inviscid fluid medium and relate the difference to the number of particles submerged in the fluid and the viscosity of the fluid. Additionally, we examine the effect of particle size and fluid viscosity on the speed by which the particles reach their final location. We also study how ultrasound waves interact with multiple small particles in a viscous fluid, focusing on the forces that move these particles. We explore two models that account for single and multiple ultrasound wave scattering. Scattering is the process by which ultrasound waves deflect in different directions when they encounter a particle. The results show that the difference between single and multiple scattering models can be significant, depending on the ultrasound DSA process parameters and the properties of the fluid and particles. In general, the importance of accounting for multiple scattering increases with the number of particles submerged in the fluid. Understanding particle packing density when using ultrasound DSA in a viscous fluid is essential in many engineering applications, in particular manufacturing of composite materials that derive their properties from the spatial arrangement of particles in a matrix material.