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No description available.

A dupla filtração pode ser considerada como uma das mais promissoras tecnologias para tratamento de água, estimando-se que grande parte das necessidades de tratamento poderiam ser satisfeitas com o uso desta tecnologia. Alguns aspectos ainda não devidamente esclarecidos até o presente sobre esta tecnologia estão relacionados ao tratamento de água com turbidez elevada. Com a montagem e operação de uma instalação piloto, constituída de dois sistemas de dupla filtração (sistema 1: filtro ascendente de areia grossa e filtro descendente de areia e sistema 2: filtro ascendente de pedregulho e filtro descendente de areia), foi realizada uma investigação experimental com águas de estudo preparadas com caulinita (água tipo I com turbidez em torno de 100 uT e água tipo II com turbidez em torno de 300 uT). A coagulação foi realizada com o sulfato de alumínio, sem o uso de alcalinizante ou de acidificante, para que resultasse potencial zeta próximo de zero. A operação de ambos os sistemas foi efetuada com e sem descargas de fundo intermediárias nos filtros ascendentes, e foram variadas as taxas de filtração em ambos os filtros (de 120 a 240 m&sup3/m&sup2.d nos filtros ascendentes e de 180 a 300 m&sup3/m&sup2.d nos filtros descendentes). Concluiu-se principalmente que os dois sistemas foram capazes de produzir água filtrada com turbidez consistentemente menor que 0,5 uT e que a produção efetiva de água depende da turbidez da água de estudo, das taxas de filtração, da execução das descargas de fundo intermediárias e da carga hidráulica disponível para retenção de sólidos. / Double filtration may be considered one of the most important technologies for water treatment. It has been estimated that most of water treatment can be efficiently achieved with the use of this technology, although some design and operational aspects related to the high turbidity of the influent water have not been fully studied until the present time. A pilot plant was built comprising two double filtration systems (system 1 with an upflow coarse sand filter followed by a downflow fine sand filter; system 2 with an upflow gravel filter followed by a downflow filter identical to that used in system 1). The experimental investigation was carried out using influent waters prepared with kaolin (water type I with turbidity of approximately 100 NTU and water type II with turbidity of approximately 300 NTU). Coagulation was accomplished by using aluminum sulfate (no acid or alkaline products) so that the zeta potential resulted approximately zero. The operation of both systems was carried out with and without intermediate down flushes during the runs. Filtration rates in the filters of both systems varied from 120 to 240 m&sup3/m&sup2.d in the upflow filters and from 180 to 300 m&sup3/m&sup2.d in downflow filters. It was mainly concluded that both systems resulted capable to produce filtered water with turbidity consistently lower than 0.5 NTU and that the net production was related to the influent water turbidity, filtration rates, execution of intermediate down flushes and the hydraulic head provided for solids retention in both filter of each double filtration system.

No description available.

La présence de leucocytes dans les dérivés sanguins à transfuser a été soulignée et rendue responsable de différentes complications graves chez les patients receveurs,et notamment chez certaines catégories de patients plus sensibles tels les immunodéprimés, les nouveau-nés, les candidats aux greffes, et les personnes transfusées à répétition. Le but de ce projet est l'aménagement de membranes de filtration du sang permettant une rétention cellulaire sélective par greffage covalent de ligands spécifiquement reconnus par les intégrines α4β1, α4β7, et β2 exprimées chez les leucocytes Nous avons envisagé l'amélioration des propriétés filtrantes de deux membranes commerciales, de PVDF et de PBT, en y fixant de manière covalente des ligands d'intégrines de leucocytes. Nous avons réalisé la synthèse de divers dérivés des tripeptides LDV et LLG ainsi que d'un composé peptidomimétique. Ces molécules ont été greffées de manière covalente aux membranes, par le biais de bras d'espacement de type polyéthylène glycol, permettant d'exposer les signaux biologiques de façon optimale vis-à-vis de la reconnaissance cellulaire. Nous avons caractérisé les membranes de PVDF et de PBT par SEM (Scanning electron microscopy : étude structurale, compatibilité des solvants, contrôle d'intégrité après traitements), par XPS (X-Ray photoelectron spectroscopy : étude sur les membranes natives, greffages de sondes chlorées ou fluorées) ainsi que par LSC (Liquid scintillation counting : mesures de réactivité de surface vis-à-vis de la lysine tritiée,tests d'activation, mise au point des modes opératoires).Les fonctions accessibles au greffage sont de type acides carboxyliques et alcools pour les membranes de PBT et de type alcools pour celles de PVDF. Diverses méthodes de greffage ont été testées sur ces deux matériaux. La méthode retenue pour le PBT consiste en l'utilisation d'un clip moléculaire muni d'une fonction azoture et d'un ester activé sous forme de N-hydroxysuccinimide, mis au point au laboratoire, greffé par activation photochimique. D'autre part, c'est une activation des fonctions alcools présentes sur le PVDF par le fluorure de cyanuryle qui a retenu notre attention. Ces deux méthodes ont été appliquées à la fixation des ligands d'intérêt synthétisés par nos soins. Les membranes dérivatisées ont finalement été analysées en XPS pour s'assurer de la présence des ligands et utilisées dans des tests de filtration de buffy coat. La qualité de la filtration obtenue a pu être évaluée en cytométrie de flux. Les résultats obtenus sont intéressants puisqu'une nette amélioration de la qualité de la rétention leucocytaire a pu être observée (facteur 100).

Thesis (M.S.)--Ohio State University, 1983. / Includes bibliographical references (leaves 91-93). Available online via OhioLINK's ETD Center

The main objective of the present work is the removal of inclusions from silicon scrap and metallurgical grade silicon. To reach this goal, two various routes are investigated. First, settling of SiC particles from molten silicon followed by directional solidification is reported in this thesis. Then, removal of SiC and Si3N4 inclusions in silicon scrap by filtration with foam filters and wettabilities of silicon on graphite materials are studied. To supply the increasing needs of the photovoltaic industry it is necessary to produce a low cost silicon feedstock. One of the many routes established from the industry is the Solsilc project. This project aims to produce solar-grade silicon by carbothermal reduction of silicon, based on the use of very pure raw materials. The high carbon content of about 700 mass ppm of the silicon in the form of SiC particles, needs to be removed before the Solsilc silicon could be used as a feedstock to PV industry. Settling of SiC particles in molten silicon was investigated. This part of the work was in cooperation with SINTEF Materials & Chemistry. Two experiments were conducted and the cast silicon ingots were analyzed by light microscopy and LECO carbon analyzer. The results showed that the number of inclusions in the middle of the ingots was less than in the bottom and top. The removal efficiency was above 96% in the middle part of an ingot and the total carbon content measured by LECO was < 25 mass ppm. The difference in density between the particles and the melt gives the SiC particles a relatively high settling velocity leading to a high removal efficiency. Pushing and engulfment of SiC particles by solidification front was also studied. Directional solidification of silicon that followed settling pushes the particles to the top of the ingot. The presence of SiC particles in the middle of the ingot is explained by engulfment. Top-cut silicon scrap represents a considerable loss of the PV silicon. Removal of inclusions from the silicon scrap would make it possible to recycle it to feedstock in the PV cell production. This was carried out by filtration with ceramic foam filters. Carbon and SiC foam filters with various pore sizes were employed in the filtration experiments. They were provided by Eger-Sørensen, a Norwegian company and Foseco AB in Sweden. The top-cut silicon scrap came from REC-Scan Wafer. Characterization of inclusions in silicon scrap before and after filtration experiments took place. Two techniques were developed and used in this work. First, extraction of inclusions by acid dissolution of the silicon was carried out. The SiC and Si3N4 particles collected afterwards were analyzed and counted by automated light microscopy. In the second technique, silicon samples were ground and polished with diamond paste. Microscopic analysis consisted of measuring the surface area of the inclusions found in the silicon samples. Results show that inclusions in top-cut solar cell silicon scrap are needle-like Si3N4 particles and round SiC inclusions. The removal efficiency for a 30 ppi SiC filter is more than 99%. The inclusions remaining after filtration are mainly SiC particles smaller than 10 µm. The experiments show that the filtration efficiency increases with decreasing filter pore size. Some filter cakes that mainly consist of large Si3N4 inclusions are found on the top surface of the filter. Deep bed filtration is the mechanism responsible for the removal of small particles. After taking into consideration various models for the foam filters the main conclusion is that interception seems to be the main removal mechanism of inclusions in silicon. Settling appears to play a minor role for our system. A new model named branch model explains better the experimental results. Due to the low wetting angle between molten metal and the filter material, capillary forces drive the melt through the filter. Therefore, the melt velocity through the filter is high. This justifies the usage of potential flow in the branch model.   It is shown that molten silicon may be contaminated in contact with the refractories. Since purity for solar cell silicon is crucial, contamination must be minimized. Graphite crucibles may be a source of relatively high levels of Al, Fe, and P. In the filtration process, wettability of the molten silicon with the filter material is very important. Thus, spreading and infiltration of molten silicon into the graphite substrates were also investigated in this thesis. Five different graphites were provided by Svenska Tanso AB. They are in use as refractories in the PV industry and vary from each other in porosity, density, and average pore size. The sessile drop technique is employed to study the wetting behavior of molten silicon on the graphite materials. The measured contact angles show that molten silicon does not initially wet carbon materials. However, due to the chemical reaction between Si and C, a SiC layer is formed in the interface between molten silicon and the graphite. Formation of this layer lowers the contact angles finally reaching equilibrium wetting angles of molten silicon with SiC materials. Spreading of molten silicon is affected not only by the reaction formed SiC layer, but also by the surface finish. The final contact angles, also called equilibrium contact angles, decrease with increasing surface roughness of the graphites. Infiltration of silicon into graphites is mainly related to the average pore size of graphite materials. Materials with large pores are penetrated deeper by the liquid silicon. Zero contact angles of the silicon with graphites are found in materials with both high surface roughness and large average pore size. These results indicate that graphites for use in the PV industry should have a small average pore size. The surface of the graphite in direct contact with silicon should be smooth (low roughness).

Collector well designs are necessary to maximize groundwater uptake and riverbank filtration without negatively impacting an aquifer. Unfortunately, there is a lack of information and research regarding the implementation of collector well design parameters. In the past, collector well installation was too costly, but recent advances in well technology have made collector wells more cost effective. This research will contribute a set of guidelines to optimize riverbank filtration and groundwater remediation. This study models the hydrodynamics surrounding collector well configurations in riverbank filtration and groundwater remediation. Visual Modflow® was utilized to run a variety of numerical models to test four areas: flux along the laterals of a collector well, collector well interactions with a river, collector well yield, and collector well remediation capability. The two design parameters investigated were lateral length (25 m, 50 m, and 100 m) and number of laterals (3 and 4). The lateral flux tests confirm flux increases towards the terminal end of each lateral and pumping rate is the controlling factor in flux amount obtained along the laterals. The analysis of the flux-river interaction shows the main factor in determining flux amount is the initial river geometry, followed by the pumping rate, regional background flow, and collector well design, respectively. The models suggest that the 4-lateral collector well design is more effective than the 3-lateral design and in addition, 100 meter length laterals provide the highest amount of yield with the least amount of drawdown. The remediation tests investigate the application of vertical well equations to evaluate collector well designs in two areas: minimum pumping rate to capture line source of particles and first arrival time of particles. The remediation models show 100 meter length laterals provide both the lowest pumping rate and the highest residence time with the surrounding aquifer for maximum remediation. Ultimately, these models provide basic design guidelines and explain which designs are most effective, depending on the collector well purpose.

Reproduction de : Thèse d'exercice : Médecine. Néphrologie : Nantes : 2008. / Bibliogr.