No description available.

Protein nanofibres, commonly known as amyloid fibrils, are emerging as potential biological nanomaterials in a number of applications. Protein nanofibres are a highly ordered insoluble form of protein, which results when a normally soluble protein aggregates via a self-association process. However, researchers are currently faced with several challenges such as finding a cheap source of proteins that can be obtained without expensive purification and optimizing a scalable method of the manufacturing of protein nanofibres. This thesis has identified crude mixtures of fish lens crystallins as a cheap protein source and has optimized methods for large scale production of protein nanofibres of varying morphologies. Results show that by varying the conditions of fibre formation, individual protein fibres can be used as building blocks to form higher order structures. This ability to control the morphology and form higher ordered structures is a crucial step in bottom up assembly of bionanomaterials and opens possibilities for applications of protein nanofibres. The method of formation of protein nanofibres was optimized on a bench scale (1.5 mL Eppendorf tubes) and successfully scaled-up to 1 L volume. For larger scale-up volume (i.e. greater than 10 ml), internal surface area was important for the formation of protein nanofibres. The crude crystallin mixture prepared at 10 mg/mL was heated at 80oC in the presence of 10% v/v TFE at pH 3.8 for 24 hours and stored for an additional of 24 hours at room temperature for storage process. Aggregation and precipitation of proteins were observed as the protein solution was added to the pre-heated TFE. The resulting protein nanofibres were characterised using ThT dye binding, TEM and SEM. The TEM images show a network of long and criss-crossing protein nanofibres with individual fibres of approximately 10 to 20 nm in diameter and 0.5 to 1 μm long. These protein nanofibres were prepared in 1 mL centrifuge tubes and were left on the laboratory bench at room temperature. After 5 months, fresh TEM grids of the sample were prepared and visualized using TEM. Interestingly, TEM images show that a number of individual fibres had self-assembled in an intertwining fashion to form large bundles and higher order structures containing bundles of nanofibres up to 200 nm thick.

The successful production of a wide range of polymer latex products relies on the ability to control the rates of particle nucleation, growth and coagulation in order to maintain control over the particle size distribution (PSD). The development of advanced population balance models (PBMs) has simplified this task at the laboratory scale, but commercialization remains challenging as it is difficult to maintain control over the composition (i.e. spatial distributions of reactant concentration) of larger reactors. The objective of this thesis is to develop and test a combined Computational Fluid Dynamics (CFD) -PBM hybrid modeling framework. This hybrid modeling framework can be used to study the impact of changes in process scale on product quality, as measured by the PSD. The modeling framework developed herein differs from previously-published frameworks in that it uses information computed from species tracking simulations to divide the reactor into a series of interconnected zones, thereby ensuring the reactor is zoned based on a mixing metric. Subsequently, an emulsion polymerization model is solved on this relatively course grid in order to determine the time evolution of the PSD. Examination of shear rate profiles generated using CFD simulation (at varying reactor scales) suggests that, dependent on conditions, mechanically-induced coagulation cannot be neglected at either the laboratory or the commercial scale. However, the coagulation models that are formulated to measure the contributions of both types of coagulation simultaneously are either computationally expensive or inaccurate. For this reason the decision was made to utilize a DLVO-coagulation model in the framework. The second part of the thesis focused on modeling the controlled coagulation of high solids content latexes. POLY3D, a CFD code designed to model the flow of non-Newtonian fluids, was modified to communicate directly with a multi-compartment PBM. The hybrid framework was shown to be well-suited for modeling the controlled coagulation of high solid content latexes in the laminar regime. It was found that changing the size of the reactor affected the latex PSD obtained at the end of the process. In the third part of the thesis, the framework was adapted to work with Fluent, a commercial CFD code, in order to investigate the scale-up of a styrene emulsion polymerization reaction under isothermal conditions. The simulation results indicated that the ability to maintain good control of the PSD was inversely related to the reactor blend time. While the framework must be adapted further in order to model a wider range of polymerization processes, the value of the framework, in obtaining information that would otherwise be unavailable, was demonstrated. / Thesis (Ph.D, Chemical Engineering) -- Queen's University, 2012-05-01 07:09:08.362

Grâce aux développements des méthodes de synthèse et de caractérisation, les nanomatériaux constituent un champ d'investigation de plus en plus actif et attractif. Cette thèse s'attache à étudier un procédé de synthèse de nanoparticules d’oxyde de zinc par voie polyol. Ce procédé a l’avantage de fournir une large variété morphologique de particules présentant une bonne qualité cristalline. Dans cette thèse, nous montrons qu’en variant les paramètres de synthèse nous pouvons moduler la taille, la distribution de taille et la morphologie des nanoparticules pour les obtenir en forme de nanosphères aussi fines que 6 nm ou des nanofils aussi longs que600 nm. Notre étude systémique a porté sur un ensemble de paramètres qui contrôlent la réaction d’hydrolyse forcée incluant la stoechiométrie, la température, la nature du polyol mais également l’agitation, l’injection des réactifs et l’activation par ultra sons du milieu. Nous montrons que la forme des nanoparticules est déterminée par la compétition entre les réactions de croissance de différentes faces du cristal d’oxyde de zinc. Notre étude a permis aussi de comparer différents dispositifs de mélange comme le réacteur du laboratoire, le T de mélange et les jets libres. Par ailleurs, pour produire en masse ces nano objets nous avons développé une stratégie originale pour comprendre l’effet du mélange sur la taille des nanoparticules. Notre approche s’appuie sur la résolution numérique des équations de Navier-Stokes et la corrélation entre les profils d’énergie turbulente dissipée et la taille des nanoparticules mesurée expérimentalement. L’application au cas spécifique de l’oxyde de zinc nous a permis de produire jusqu’à ~50 g de nanoparticules par Batch. Ces nanoparticules ont par la suite été incorporées comme matériau semi conducteur dans des cellules photovoltaïques à colorant préparées à l’École Nationale Supérieure de Chimie de Paris. En effet, la richesse morphologique de ZnO obtenu par voie polyol laisse présager une bonne adsorption du colorant à sa surface. Nos résultats montrent que les rendements de photoconversion dépendent aussi bien de la morphologie que de la taille. Les meilleures cellules élaborées dans cette thèse ont un rendement qui avoisine 5.3 %. / Thanks to developments in synthesis methods and characterization techniques, nanomaterials research field is increasingly active and attractive. This thesis aims to investigate the polyol process for zinc oxide nanoparticles synthesis. Indeed, this method has the advantage of providing a wide variety of particle morphology with a good crystalline quality. In this thesis, we show that by varying the synthesis conditions we can adjust the size, the size distribution and the morphology of nanoparticles to obtain either shaped nanospheres as small as 6 nm or nanowires as long as 600 nm. Our systemic study focused on a set of parameters that control the forced hydrolysis reaction including stoichiometry, temperature, nature of the polyol but also mixing, injection of reagents and ultrasound activation. We show that the shape of the nanoparticles is determined by the competition between growth rates of different zinc oxide crystal facets. Our study also compared different mixing devices such as laboratory reactor, T- mixer and impinging jets. More over, to mass produce zinc oxide nanoparticles, we developed an original strategy to understand the effect of mixing on nanoparticle size. In our approach, we correlate the turbulent energy dissipated as obtained from Computation Fluid Dynamics with theme asured nanoparticle size. The application to the specific case of zinc oxide has allowed us to produce sample aliquots of ~50 g per Batch. These nanoparticles were subsequently incorporated into dye-sensitized solar cells as semi conducting material at the École Nationale Supérieure de Chimie de Paris. Indeed, the morphological richness of the zinc oxide produced via polyol process suggests good adsorption of the dye on their surfaces. Our results show that the photoconversion efficiencies depend both on the morphology and the size. Our best photoconversion efficiency approaches 5.3%.

Induced pluripotent stem cells (iPSCs) have been recognised as a virtually unlimited source of stem cells that can be generated in a patient-specific manner. Due to these cells’ potential to give rise to all differentiated cell types of the human body, they have been widely used to derive differentiated cells for drug screening and disease modelling purposes. iPSCs also garner much interest as they can potentially serve as a source for cell replacement therapy. Towards the realisation of these biomedical applications, this thesis aims to address challenges that are associated with scale-up, safety and biofabrication. Firstly, the manufacture of a high number of human iPSCs (hiPSCs) will require standardised procedures for scale-up and the development of a flexible bioprocessing method, since standard adherent hiPSC culture exhibits limited scalability and is labour-intensive. While the quantity of cells that are required for cell therapy depends largely on the tissue and defect that these replacing cells are meant to correct, an estimate of 1 × 10^9 has been suggested to be sufficient for several indications, including myocardial infarction and islet replacement for diabetes. Here, the development of an integrated, microcarrier-free workflow to transition standard adherent hiPSC culture (6-well plates) to scalable stirred suspension culture in bioreactors (1 L working volume, 2.4 L maximum working volume) is presented. The two-phase bioprocess lasts 14 days and generates hiPSC aggregates measuring 198 ± 58 μm in diameter on the harvesting day, yielding close to 2 × 10^9 cells. hiPSCs can be maintained in stirred suspension for at least 7 weeks with weekly passaging, while exhibiting pluripotency-associated markers TRA-1-60, TRA-1-81, SSEA-4, OCT4, and SOX2. These cells retain their ability to differentiate into cells of all the three germ layers in vitro, exemplified by cells positive for AFP, SMA, or TUBB3. Additionally, they maintain a stable karyotype and continue to respond to specification cues, demonstrated by directed differentiation into beating cardiomyocyte-like cells. Therefore, the aim of manufacturing high hiPSC quantities was met using a state-of-the-art scalable suspension bioreactor platform. Secondly, multipotent stem cells such as induced neural stem cells (iNSCs) may represent a safer source of renewable cells compared to pluripotent stem cells. However, pre-conditioning of stem cells prior to transplantation is a delicate issue to ensure not only proper function in the host but also safety. Here, iNSCs which are normally maintained in the presence of factors such as hLIF, CHIR99021, and SB431542 were cultured in basal medium for distinct periods of time. This wash-out procedure results in lower proliferation while maintaining key neural stem cell marker PAX6, suggesting a transient pre-differentiated state. Such pre-treatment may aid transplantation studies to suppress tumourigenesis through transplanted cells, an approach that is being evaluated using a mouse model of experimental focal demyelination and autoimmune encephalomyelitis. Thirdly, biomedical applications of stem cells can benefit from recent advancements in biofabrication, where cells can be arranged in customisable topographical layouts. Employing a 3DDiscovery bioprinter, a bioink consisting of hiPSCs in gelatin-alginate was extruded into disc-shaped moulds or printed in a cross-hatch infill pattern and cross-linked with calcium ions. In both discs and printed patterns, hiPSCs recovered from these bioprints showed viability of around 70% even after 4 days of culture when loaded into gelatin-alginate solution in aggregate form. They maintained pluripotency-associated markers TRA-1-60 and SSEA-4 and continued to proliferate after re-plating. As further proof-of-principle, printed hiPSC 3D constructs were subjected to targeted neuronal differentiation, developing typical neurite outgrowth and resulting in a widespread network of cells throughout and within the topology of the printed matrix. Staining against TUBB3 confirmed neuronal identity of the differentiated cellular progeny. In conclusion, these data demonstrate that hiPSCs not only survive the 3D-printing process but were able to differentiate along the printed topology in cellular networks. / Induzierte pluripotente Stammzellen (iPSZ) stellen eine praktisch unbegrenzte Stammzellquelle dar, welche patientenspezifisch erzeugt werden kann. Da diese Zellen das Potenzial haben, alle differenzierten Zelltypen des menschlichen Körpers hervorzubringen, werden sie für die Herstellung differenzierter Zellen für Arzneimitteltests und für die Krankheitsmodellierung verwendet. Sie erfahren auch großes Interesse, weil sie als Zellquelle in der Zellersatztherapie Anwendung finden könnten. Die vorliegende Dissertation beschäftigt sich mit drei zentralen Herausforderungen, die im Rahmen der biomedizinischen Anwendung von iPSZ auftreten. Die Herstellung einer großen Zahl von humanen iPSZ (hiPSZ) erfordert die Entwicklung standardisierter Verfahren für die Skalierung, welche durch die Entwicklung einer flexiblen Bioprozessmethode realisiert werden kann. Bisher wird die Skalierbarkeit durch eine standardmäßig adhärente Zellkultur und den damit verbundenen hohen Arbeitsaufwand begrenzt. Die Menge an Zellen, die für die Zelltherapie benötigt wird, hängt stark vom Gewebetyp ab, welcher von den ersetzenden Zellen korrigiert werden soll. Berechnungen legen nahe, dass eine Anzahl 1 × 10^9 Zellen für eine Vielzahl von Indikationen ausreicht – einschließlich Myokardinfarkt und Inselzelltransplantation für Diabetes. Im Rahmen dieser Arbeit wurde ein integrierter Arbeitsablauf zur skalierbaren Zellsuspensionskultur von hiPSZ ohne Verwendung von microcarrier entwickelt, um die standardmäßig adhärente Kultur (6-Well-Platten) in Bioreaktoren (1 L Arbeitsvolumen, 2,4 L maximales Arbeitsvolumen) zu überführen. Der zweiphasige Produktionsprozess dauert 14 Tage und erzeugt hiPSZ-Aggregate mit einem finalen Durchmesser von 198 ± 58 μm, der annähernd 2 × 10^9 Zellen beinhaltet. hiPSZ können mindestens 7 Wochen lang in einer gerührten Zellsuspension bei wöchentlichem Passagieren gehalten werden, wobei sie Pluripotenz-assoziierte Marker wie TRA-1-60, TRA-1-81, SSEA-4, OCT4 und SOX2 beibehalten. Die Zellen behalten weiterhin ihre Fähigkeit, sich in vitro in Zellen mit AFP-, SMA- oder TUBB3-Immunoreaktivität und damit in Zellen aller drei Keimblätter zu differenzieren. Darüber hinaus halten sie einen stabilen Karyotyp aufrecht und reagieren auf gezielt eingesetzte externe Differenzierungsstimuli, wie durch eine gezielte Differenzierung in schlagende Kardiomyozyten-ähnliche Zellen demonstriert werden konnte. Somit wurde das Ziel, eine großen Anzahl hiPSCs herzustellen, mit einer hochmodernen, skalierbaren Suspensionsbioreaktorplattform erreicht. Multipotente Stammzellen wie induzierte neurale Stammzellen (iNSZ) gelten verglichen mit iPSZ als sicherere Zellquelle für Ersatztherapien. Die Vorkonditionierung von Stammzellen vor der Transplantation ist jedoch ein heikles Thema, da sowohl die einwandfreie Funktion im Wirtsgewebe als auch Sicherheit gewährleistet werden müssen. Im Rahmen dieser Arbeit wurden iNSZ, die normalerweise im Kulturmedium mit Faktoren wie hLIF, CHIR99021 und SB431542 gehalten werden, für eine definierte Zeitspanne in basalem Medium kultiviert. Die Vorbehandlung führt zu einer geringeren Proliferation, jedoch unter Erhalt der Expression des wichtigen neuralen Stammzellmarkers PAX6, was auf einen transienten vordifferenzierten Zustand hindeutet. Eine solche Vorbehandlung könnte bei zukünftigen Transplantationsstudien angewandt werden, um die Tumorentstehung durch transplantierte Zellen zu unterdrücken. Dieser Ansatz wird in Zukunft mit einem Mausmodell der experimentellen fokalen Demyelinisierung und der autoimmunen Enzephalomyelitis untersucht. Schließlich kann die Zellersatztherapie von den jüngsten Fortschritten in der Biofabrikation profitieren, bei der die Zellen durch das Drucken in anpassbare topographische Profile angeordnet werden können. Mit einem 3DDiscovery Biodrucker wurde eine Biotinte bestehend aus Gelatine-Alginat und hiPSZ in scheibenförmig extrudiert oder in einem Kreuzschraffurmuster gedruckt und mittels Kalziumionen-Zugabe vernetzt. Gedruckte hiPSZ zeigten auch nach 4 Tagen Kultivierung eine Lebensfähigkeit von etwa 70 % und weiterhin das Auftreten der Pluripotenz-assoziierten Marker TRA-1-60 und SSEA-4. Zudem konnten sie sich anschließend mit standardmäßig adhärenter Zellkultur weiter vermehren. Zudem konnte gezeigt werden, dass die gedruckten Konstrukte einer gezielten neuronalen Differenzierung unterzogen werden können, die zu einem typischen Neuritenauswuchs und zu einer weitreichenden interzellulären Vernetzung durch und innerhalb der Topologie der gedruckten Matrix führte. Die Färbung gegen TUBB3 bestätigte die neuronale Identität der differenzierten Zellen. Zusammenfassend zeigen diese Daten, dass bei Verwendung des in dieser Studie erarbeiteten Protokolls hiPSZ nicht nur den 3D-Druckprozess überleben, sondern auch entlang der gedruckten 3D Topologie in Netzwerke Neurone differenzieren können.

Hydrogen economy is capitalizing the decarbonization of transport and industrial sectors. Ammonia is an attractive intermediate to store and transport hydrogen, due to its low production cost, well developed storage and transportation infrastruc- ture, high hydrogen density in its liquified form (for transportation) and the potential production from renewable energy sources. Although there have been significant ad- vancements in catalyst development for ammonia decomposition, the potential of this technology cannot be fully exploited until significant process development is made. In this sense, catalytic membrane reactors show promising features and performances. In this work, ammonia decomposition has been studied using the following ap- proach: (1) Catalytic Packed Bed Reactor (CPBR) and kinetic modeling, (2) Cat- alytic Packed Bed Membrane Reactor (CPBMR) modeling and (3) CPBMR scale-up. Stage (1) was performed using Ru-K/CaO and Co-Ce catalysts over a wide range of experimental conditions (including pressures up to 16 bar). Stage (2) includes 1-D and 2-D models that were further validated experimentally, also using different software to tackle the stage (3), which aims to give the optimized geometry and properties of a CPBMR for a production of 5 N m3 h−1 of high purity H2 . The results presented in this Thesis enabled to: (1) obtain a reliable kinetic model capable of describing the ammonia decomposition under a wide range of operating conditions, using Ru-K/CaO and Co-Ce catalysts. (2) identify a range of operat- ing conditions where the CPBMR performs better than the CPBR in terms of NH3 conversion, H2 recovery and H2 purity. This range includes: reaction temperature between 250◦C and 500◦C; reaction pressures between 1 and 16 bar; space times be- tween 1 and 15 gcat h mol−1 and H2 permeate pressure higher than the atmospheric pressure (up to 5 bar). (3) scale-up the CPBMR for ammonia decomposition at a pilot scale, encountering that a pilot plant for a production of 5 N m3 h−1 of pure H2 ( >99.99%) could be obtained with a relatively small multitubular arraignment, that might be even smaller than the needed for the same product using other technology.

No description available.

Yes / Mechanochemical synthesis has the potential to change the way in which chemistry is conducted, particularly with regard to removing or dramatically reducing the need for solvents. Recently, it has been demonstrated that mechanochemistry can be carried out continuously and on large scale through the use of twin-screw extrusion (TSE). TSE has successfully been applied to the synthesis of cocrystals, metal organic frameworks (MOFs), deep eutectic solvents (DESs), metal complexes, and organic condensation reactions. However, while TSE provides a route for mechanochemical synthesis to be developed into a continuous, high-volume manufacturing process, little is currently understood about how to best optimize the various process parameters involved. Herein, we investigate the use of a batch mixer that has been previously used in polymer processing, to optimize mechanochemical reactions performed by extrusion. In particular, reactions between 8-hydroxyquinoline (Hq) and metal acetate salts of zinc or aluminum to give quinolinate complexes Znq2·AcOH and Alq3·AcOH, which are of interest for organic light-emitting diode (OLED) applications, have been investigated. The manner in which the progress of the reaction correlates with the machine torque, temperature, and specific mechanical energy (SME) imparted by the batch mixer has been elucidated. Significantly, this knowledge enabled optimization of the mechanochemical reactions by TSE through the key parameters of screw speed, feed rate, temperature, and particle size. / EPSRC (EP/L019655/1).

No description available.

La demande sociétale en protéines végétales a augmenté d’environ 50% durant la dernière décennie. Les nouvelles tendances alimentaires et l’intérêt pour leurs propriétés font de ces protéines une alternative intéressante dans de nombreux secteurs industriels à moyenne et haute valeur ajoutée. L'objet de cette thèse est de progresser dans l'étude d’un procédé simple et robuste permettant la mise au point d'une éco-filière de production de protéine. L’objectif est d’étudier l’extraction et le procédé de purification de la protéine, à partir des plantes sélectionnées, afin de garantir la conservation de ses propriétés technologiques moussantes, émulsifiantes et gélifiantes. / Social requirements for vegetal proteins increased almost by 50% in last decade. New food trends and their interesting functional properties make these proteins a preferential choice for industrial sectors of middle and high added-value. The aim of this PhD Thesis is to contribute to the analysis of a simple and robust process able to favour an eco-industry for protein production. The objective is to study the extraction and the purification of the protein, from selected green-plants, in order to guarantee techno-functional properties such as foaming, emulsifying and gelling powers