The most important advantages of Multilevel Inverters are the absence of a coupling transformer for medium voltage applications and low harmonic current content. In this way, relocatable and economical STATCOM systems can be realized. Complex control algorithms and the isolation problems of measurement devices and power supplies are the main challenging parts of this type of application. In this study, the design, realization, and the performance of a Voltage Source Type Cascaded Multilevel Converter Based STATCOM will be investigated in terms of digital computation, control hardware and the semiconductors devices commercially available in the market. This research work is fully supported by the Public Research Grant Committee (KAMAG) of TUBiTAK within the scope of National Power Quality Project of Turkey with the project No: 105G129.

The esterification of lactic acid with ethanol over Lewatit S 100, strong cation ion exchange resin catalyst, was studied in counter current vapor-liquid contactor type differential reactor by feeding ethanol and lactic acid solution as vapor and liquid phases, respectively. The ethanol vapor phase was diluted by dry air and the water removal was achieved by the mass transfer of water from liquid to vapor phase. Effect of ethanol to lactic acid feed molar ratio and vapor flow rate on fractional conversion and water removal efficiency were tested at 40-70&deg / C of column temperature range. It was observed that Lewatit S 100 was adequate catalyst for esterification of lactic acid with ethanol. Increase in ethanol to lactic acid feed molar ratio enhanced both lactic acid conversion and water removal by upper product stream. However, lactic acid conversion was suppressed by the increase of inlet vapor flow rate because of the decrease in ethanol concentration in gas phase which affected both esterification reaction rate and mass transfer rate. The reaction temperature is the other important parameter that affects the mass transfer of ethanol from vapor to liquid phase. Although reaction rate and equilibrium conversion values were promoted by temperature, the lower solubility of ethanol in liquid phase limited the fractional conversion while promoted the water mass transfer from liquid to vapor phase. The optimized vapor phase velocity and temperature can yield higher conversions than the equilibrium conversion at the same temperature and initial composition. Therefore, low pressure organic acids such as lactic acid can be successfully esterified by using counter current V-L contactor type reactors and by using integrated reaction and separation units.

In this thesis, numerical simulation of one dimensional detonation tube problem is solved with finite rate chemistry. For the numerical simulation, Euler equations have been used. Since detonation tube phenomena occurs in high speed flows, viscosity eects and gravity forces are negligible. In this thesis, Godunov type methods have been studied and afterwards high resolution method is used for the numerical solution of the detonation tube problem. To solve the chemistry aspect of the problem ZND theory have been used. For the numerical solution, a FORTRAN code is written and the numerical solution of the problems compared with the exact ZND solutions.

Groundwater contamination by petroleum hydrocarbons has become one of the serious environmental problems in many countries. The sources of petroleum-hydrocarbon contaminants may be released from above ground and underground storage tanks, and pipelines. Petroleum hydrocarbons are mainly composed of benzene, toluene, ethyl- benzene, and xylems (BTEX), and other constituents such as methyl-tert-butyl ether (MTBE), naphthalene, 1,3,5-trimethylbenzene (1,3,5-TMB), and 1,2,4-trimethylbenzene (1,2,4-TMB). It is generally recognized that petroleum hydrocarbons have high risks to environmental receptors when hydrocarbon releases occur. Various biological, physical, and chemical remediation technologies (e.g. pump and treat, air sparging, enhanced bioremediation, and chemical oxidation) can be used to remediate petroleum-hydrocarbon contaminated groundwater. However, many of these techniques are typically costly or have limited applications. Permeable reactive barriers (PRBs) are a promising technology for the passive and in situ treatment of contaminated groundwater. A PRB can be defined as ¡§an emplacement of reactive materials in the subsurface designed to intercept a contaminant plume, provide a preferential flow path through the reactive media, and transform the contaminant(s) into environmentally acceptable forms to attain remediation concentration goals at points of compliance.¡¨ The oxygen release materials can be emplaced in the PRBs to passive increase dissolved oxygen (DO) in the subsurface to enhance the intrinsic biodegradation of dissolved hydrocarbons. In the first part of this study, guidelines for PRBs installation have been developed for the remediation of petroleum hydrocarbons, heavy metals, and organic solvents contaminated groundwater. PRB is a cost-effective approach for the remediation of contaminated aquifers. As contaminated groundwater moves through a permeable reactive barrier, the contaminants are scavenged or degraded, and uncontaminated groundwater emerges from the downgradient side of the reactive zone. The permeable reactive barrier concept has several advantages over other remediation technologies currently in use (e.g., pump and treat, air sparging), including absence of mechanical facilities and the electric power, no groundwater extraction and reinjection, treatment in situ, and cost-effective. The first part of this study presents the designs, applications, and case studies of PRB systems on groundwater remediation. In the second part of this study, oxygen release materials have been constructed and evaluated for the appropriate components in batch experiments. Microbial degradation of petroleum hydrocarbons in groundwater can occur naturally. Since the petroleum-hydrocarbons are generally degraded faster under aerobic conditions, aerobic bioremediation can be applied to enhance the biodegradation of petroleum-hydrocarbons within of the plume if oxygen can be provided to the subsurface economically. Batch experiments were conducted to design and identify the components of the oxygen-releasing materials. Cement and gypsum were used as a binder in this mixtures experments. (1) using cement as the binding material The mixtures of the oxygen release material were prepared by blending cement, peat, sand, ethylene-vinyl acetate copolymer(EVA), calcium peroxide (CaO2), and water together at a ratio of 1.0¡G0.18¡G0.20¡G0.10¡G1.12¡G1.74 by weight. Cement was used as a binder and regular medium filter sand was used to increase the permeability of the mixture. Calcium peroxide releases oxygen upon contact water. The designed material with a density of 1.9 g/cm3 was made of 3.5 cm cube for the batch experiment. Results show that the oxygen release rate of the material is 0.046 mg O2/day/g rock. The oxygen release material was able to remain active in oxygen release for more than three months. (2) using gypsum as the binding material The mixtures of the oxygen release material were prepared by blending gypsum, CaO2, sand, and water together at a ratio of 1¡G0.5¡G0.14¡G0.75 by weight. Gypsum was used as a binder and regular medium filter sand was used to increase the permeability of the mixture. Calcium peroxide releases oxygen upon contact water. The designed material with a density of 1.1 g/cm3 was made of 3.5 cm cube for the batch experiment. Results show that the oxygen release rate of the material is 0.031 mg/day/g. The oxygen release material was able to remain active in oxygen release for more than three months. In the third part of this study, immobilization technology was applied to produce the low permeability wrapping film for the construction of oxygen-releasing granular materials. The mixtures of the oxygen release material were prepared by blending alginate, CaO2, and sand together at a ratio of 8.3¡G1.0¡G1 by weight. The low permeability wrapping film of the oxygen release material was able to remain active in oxygen release for two months. In the fourth part of this study, a laboratory-scale column experiment was conducted to evaluate the feasibility of this proposed system on the bioremediation of petroleum-hydrocarbon contaminated groundwater. This system was performed using a series of continuous-flow glass columns including four consecutive soil columns. Simulated petroleum-hydrocarbons contaminated groundwater with a flow rate of 0.263 m/day was pumped into this system. In the column experiment, the samples of column influent and specified sampling ports were collected and analyzed for pH, DO, BTEX, MTBE, and microbial populations. Results show that up to 99% of BTEX removal was observed in this passive system. Results from this study would be useful in designing an efficient and cost-effective passive oxygen-releasing and bioremediation system to remediate petroleum- hydrocarbon contaminated aquifer.

Angiotensin II (Ang II) exerts diverse physiological actions in both peripheral and central nervous system. It has been demonstrated to implicate in central mechanisms leading to hypertension in the nucleus tractus solitarii (NTS) of rats, and mediated by the type-1 receptors (AT1R). Our previous studies already suggested that inhibition of NO synthesis in the NTS causes sustained hypertension. It was reported that the activity of Ang II was higher in the NTS of spontaneously hypertensive rat (SHR) and AT1R are colocalized in the neurons of the NTS, providing the local reactive oxygen species (ROS) production by Ang II. However, the signaling mechanisms of Ang II that induce hypertension remain uncertain. In the present study, we investigated the possible signal pathways involved in the cardiovascular regulation of Ang II in the NTS. Male SHR was treated with AT1R blocker, losartan (30 mg/kg/day) or superoxide dismutase (SOD) mimetic, tempol (1 mM/kg/day) for two weeks, systolic blood pressure was decreased significantly in losartan- or tempol-treated SHR. The NTS was excised for dihydroethidium (DHE) staining, NO analysis, immunoblotting and immunohistochemistry. Our results demonstrated that DHE staining revealed of ROS was much more in the NTS of SHR than in the NTS of wistar-Kyoto (WKY) rat. The ROS in the NTS of SHR was reduced by losartan. The NO content in the NTS of SHR was lower than WKY, while losartan and tempol could increase NO in the NTS of SHR. Immunoblotting and immunohistochemistry studies demonstrated that Ang II-induced hypertension inhibited neuronal NO synthase (nNOS), ERK and RSK phosphorylation levels in the NTS of SHR. These results suggest that Ang II induces ROS production in the NTS of SHR. In addition, the cardiovascular modulatory effects of Ang II in the NTS are accomplished by downregulation of ERK1/2-RSK phosphorylation levels and then nNOS level.

As a low cost natural polymer, starch is widely used in paper, food, adhesive, and many other industries. In order to improve the performance of starch, crosslinking is often conducted either in the processes of starch modification or during the application processes. Many crosslinkers have been developed in the past for crosslinking starch. Ammonium zirconium carbonate (AZC) is one of the common crosslinkers for crosslinking starch in aqueous solutions, having been widely used as a starch crosslinking agent in paper surface coating for more than 20 years. However, the mechanisms of starch crosslinking with AZC have not been well studied. In order to optimize the crosslinking chemistry of starch and find new paths for the utilization of starch in papermaking, a better understanding of the starch crosslinking mechanism is necessary. This thesis focuses on the fundamental study of starch crosslinking in an aqueous solution and its applications in fiber surface grafting, filler modification, and starch nanoparticle formation. Particularly, the thesis contains three major parts: (1) Mechanism study of starch crosslinking induced by AZC: In this thesis, the crosslinking (or gelation) kinetics of starch/AZC blends were investigated by using rheological measurements. The evolution of viscoelastic properties of AZC solutions and the AZC-starch blends was characterized. It was found that for both AZC self-crosslinking and AZC-starch co-crosslinking, the initial bond formation rate and the gel strength had a strong power law relationship with the concentrations of both AZC and starch. It is suggested that the development of the crosslinking network is highly dependent on the AZC concentration, while the starch concentration effect is less significant. It was determined that the activation energy of AZC self-crosslinking was approximately 145-151 kJ/mol, while the activation energy of AZC-starch co-crosslinking was 139 kJ/mol. (2) Fiber and filler modifications with starch and crosslinkers: Besides reacting with starch, AZC can react with cellulose which also contains hydroxyl groups. Theoretically, it is possible to use AZC as a crosslinker / coupling agent to graft starch onto cellulose fibers. It is believed that the grafted starch on fiber surfaces can improve the fiber bonding capability. In this thesis, a facile method to graft starch onto cellulose fiber surfaces through the hydrogen bond formation among cellulose, starch and AZC was developed. Compared with the paper sheets made of fibers with an industry refining level (420 ml CSF), the paper sheets made of fibers with a much lower refining degree but with grafted starch showed higher paper strengths, including the tensile strength, stiffness and z direction tensile; meanwhile, a faster drainage rate during web formation could also be achieved. Not only can the fiber-fiber bonding be improved by grafting starch onto fiber surfaces, but the filler-fiber bonding can also be improved if starch can be effectively coated on the filler surface. This concept has been supported by the early studies. In this thesis, the effects of the crosslinking of starch in the filler modification for the papermaking application were also studied. (3) Mechanism of starch nanoparticle formation during extrusion with crosslinkers: It was reported that starch crosslinking could facilitate the reduction of starch particle size during reactive extrusion. However, the mechanism of the particle size reduction by starch crosslinking was not illustrated. The reason that the crosslinking can cause the particle size reduction of starch during extrusion is fundamentally interesting. In this thesis, the mechanism of starch particle size reduction during extrusion with and without crosslinkers was investigated by identifying the contributions of thermal and mechanical effects. The effects of extrusion conditions, including temperature, screw speed, torque, starch water content and crosslinker addition, on the particle size were studied. It was found that the addition of crosslinkers could significantly increase the shear force (torque), and consequently facilitate the reduction of the particle size. The results indicate that for extrusion without a crosslinker, the starch particle size decreased with the increase of temperature. At 100 degree Celsius, the starch particles with a size of 300 nm could be obtained. With the addition of appropriate crosslinkers (glyoxal), the starch particle size could be reduced to around 160 nm, even at a lower extrusion temperature of 75 degree Celsius .

Ultrasound contrast agents (UCA) have tremendous potential for in vivo molecular imaging because of their high sensitivity and great spatial resolution of ultrasound imaging. However, the diagnostic potential of UCAs has been difficult to exploit because current contrast agents are based on pre-formed microbubbles, which can only detect cell surface receptors. In this work, we demonstrated that chemical reactions that generate gas forming molecules can be used to perform molecular imaging by ultrasound in vivo. This new approach for generating ultrasound contrast agents was demonstrated by imaging reactive oxygen species (ROS) in vivo with allylhydrazine, a compound that is converted into nitrogen and propylene gas after reacting with radical oxidants. We demonstrated that allylhydrazine encapsulated within liposomes (termed APLs) can detect a 10 uM concentration of radical oxidants by ultrasound, and can image oxidative stress in mice, induced by lipopolysaccharide (LPS), using a clinical ultrasound machine. We showed that a 1-2% increase in gas concentration above saturation can be detected acoustically and suggest that numerous biological targets can be imaged via appropriately designed gas forming reactions. This work was the first demonstration of in vivo imaging of ROS using ultrasound, and this work presented a new strategy to generate gas bubbles from reactions involving radical oxidants. We anticipate numerous applications of chemically generated microbubbles, given the excellent spatial resolution of ultrasound imaging, its widespread clinical use and its high sensitivity to detect gas bubbles.

<p>This work describes how a fatty acid methyl ester (FAME) derived from a vegetable oil can be introduced as reactive diluent in a solvent-borne thermally cured coil-coating system. The evaluated reactive diluent, rape seed methyl ester (RME), has been evaluated both in a fully formulated clear coat system and via model studies.</p><p>A reactive diluent is a compound that acts as a solvent in the liquid paint, lowering the viscosity, and chemically reacts into the final film during cure. Introduction of a reactive diluent derived from vegetable oil give a more environmental compliant coating since a renewable material is incorporated in the coating and the amount of traditional solvent can be decreased. These positive environmental factors have increased the industrial interest.</p><p>The fully formulated clear coat studies describes how addition of reactive diluent affects rheological properties of the wet paint, film formation, incorporation, and final film properties in a hydroxyl-functional polyester/melamine coil-coating system. The coating were cured under industrial coil-coating cure conditions and analyzed with Raman, carbon-14 dating, extraction, dynamic mechanical analysis, and visually observed. Viscosity measurement of the wet paint show that RME works as a diluent. RME increase the mobility in the system enhancing the film formation process and occurrence of defect-free films. The incorporation of RME could not be confirmed by Raman analysis. However, carbon-14 dating did indicate the presence of RME that could not be extracted from the films. The appearance and mechanical properties of the films were also significantly affected by addition of RME. Dynamic mechanical analysis of the free standing films showed that the final film properties were affected by oven temperature, choice of co-solvent, and flash-off period.</p><p>Model studies were performed to further clarify how RME chemically can react through transesterification with the hydroxyl-groups of the polyester. RME and its two main components methyl oleate and methyl linoleate were reacted with primary alcohols with and without tertiary hydrogen both under low temperature (110, 130, 150, 170°C) and industrial cure conditions. The transesterification reaction was monitored with 1H-NMR and real time IR. Evaporation and side reactions, e.g. oxidation, are competing factors with the transesterification reaction. The fatty acid structure affects the conversion as a higher amount of unsaturations triggers higher degree of oxidation. The study also showed that reaction time and temperature affects the transesterification conversion, degree of side reactions, and catalyst choice.</p>

La notion de système réactif désigne des systèmes qui maintiennent une<br />interaction permanente avec un environnement donné. La famille des<br />langages synchrones regroupe un des langages de programmation<br />dédiés à la conception de tels systèmes. De manière générale, ces langages<br />permettent de décrire le comportement de composants parallèles qui<br />s'exécutent de manière synchrone, relativement à une horloge logique sur<br />laquelle repose un mécanisme de diffusion instantanée de l'information.<br />La conception de ces langages permet un ordonnancement statique des composants<br />parallèles et une compilation des programmes vers du code séquentiel, des<br />automates à états finis ou des circuits. En contrepartie, les contraintes<br />imposées sur ces langages limitent leur utilisation à des domaines très<br />spécifiques. La programmation réactive désigne un paradigme de programmation<br />qui repose sur une relaxation de ces contraintes. Ce paradigme de<br />programmation, inspiré plus particulièrement par le langage Esterel, propose<br />un type de programmation concurrente plus général ayant pour objectif la<br />réalisation, par exemple, de controleurs "event driven", d'interfaces graphiques<br />, de simulations physiques, de service web et de jeux multi-joueurs.<br />Ce document porte sur la notion de logiciel sur dans le cadre de la<br />programmation réactive.<br />Dans la première partie, nous nous intéressons à la question du<br />controle statique des ressources nécessaires à l'exécution d'un programme<br />pour une algèbre de processus synchrone inspirée par le paradigme réactif.<br />Dans la seconde partie, nous nous intéressons à la question de<br />l'utilisation de la programmation réactive pour le développement<br />d'applications adaptées aux architectures multicores.<br />Plus précisèment, nous nous reposerons sur une analyse statique<br />des programmes permettant d'étendre dans un cadre plus générale<br />(vrai concurrence) les avantages d'une approche purement coopérative<br />de l'ordonnancement des threads choisie par plusieurs implémentations<br />de langages basés sur le paradigme réactif.

Thesis (Ph.D.)--Virginia Commonwealth University, 2009. / Prepared for: Dept. of Physiology. Title from resource description page. Includes bibliographical references.