Centrifugal membrane and density separation (CMS) is a novel technology proposed for treatment of waste water and industrial process streams. This cross flow filtration process combines the energy recovery inherent to centrifugal reverse osmosis (CRO) with the potential alleviation of membrane fouling and concentration polarization due to the favourable effects of centrifugal and Coriolis accelerations. This dissertation presents a computational study of CMS undertaken to understand the basic hydrodynamics and mass transfer of the processes and to provide insight for the design of CMS devices. Two distinct membrane models were developed, the porous wall model (PWM) and the source term model (STM), and incorporated into Computational Fluid Dynamics (CFD) codes which solve the full Navier-Stokes equations coupled to a scalar transport equation which accounts for dissolved species. These models are used to simulate two and three dimensional laminar flows in both non-rotating and rotating reverse osmosis membrane cartridges and to predict permeate fluxes. Plate and frame geometries are first examined and it is determined that CMS benefits most from channels with streamwise directions directed radially. It is also shown that the benefits of CMS can be attributed largely to the secondary flows and mixing associated with Coriolis acceleration, and the PWM and the STM are found to perform similarly in the case of reverse osmosis. Next, the STM is used to perform a parametric study of the flow and mass transfer in rectangular and square rotating channels. It is shown that while normal rotation is preferable to spanwise rotation, relatively small deviations from the spanwise orientation are adequate to achieve most of the normal rotation performance, and that differences between the two orientations are minimal in the case of square channels. Also, the flow characteristics are again shown to correlate well with the magnitude of the Coriolis acceleration. Flows in triangular and circular channels are also considered, and are shown to perform similarly to rectangular channels. These channel orientations have application in hollow fiber membrane modules and potentially in spiral wound membrane modules. Finally, the flow and mass transfer in channels with periodic streamwise obstacles are considered. Such obstacles are related to feed spacers used in spiral wound membrane elements and impact considerably on the flow characteristics and mass transfer performance. Flow obstacles are shown to increase mass transfer performance in all cases, with alternating surface mounted performing best. A preliminary investigation is undertaken into rotating flows with periodic obstacles, and the flow fields are shown to depend strongly on the blockage ratio and on the Rossby number. In most cases, it is found that mass transfer performance does not necessarily correlate with either wall shear stress or the local flow field. Several general conclusions regarding CMS can be drawn from this work. It is preferable to operate a CMS devices at low flow rates, which is contrary to conventional wisdom in membrane separation. Secondly, the mixing induced by channel rotation is both more effective and more efficient than the mixing induced by the feed spacers considered here. Finally, the magnitude of the Coriolis acceleration is the dominant parameter in determining CMS performance. This means that a CMS device can either operate at relatively low rotational speeds with flow in the radial direction, or at higher speeds but lower angles of inclination with respect to the rotational axis. / Graduate

Inúmeras mudanças têm sido observadas no âmbito da conjugalidade, desde a variedade de arranjos conjugais, até as diferentes concepções sobre o casamento e a família e os sentidos do estabelecimento desses vínculos, configurando a relação conjugal cada vez mais como passível de rompimento. Nesse contexto, dados estatísticos (IBGE, 2008) tem apontado para um número crescente de separações, além de uma progressão na quantidade de pessoas que, após esse processo, optam por se envolver em uma segunda relação conjugal. Diante da escassez de pesquisas voltadas para o estudo do recasamento, e especialmente às questões específicas dessa nova relação conjugal, o presente trabalho pretende colocar em discussão esse processo e as possíveis mudanças decorrentes do mesmo. Inicialmente, são abordados a separação e o recasamento como disparadores de mudanças sócio-culturais (ao mesmo tempo em que são engendrados por elas), além do movimento durante o qual o amor passa a estar atrelado ao casamento, até o momento em que se configura como razão para o estabelecimento desse vínculo. A partir do referencial teórico da Esquizoanálise e assumindo como norteador o método cartográfico, foram realizadas oito entrevistas com mulheres atualmente casadas, ao menos, pela segunda vez. Após esses encontros, foi possível a identificação de experiências extremamente singulares. São apresentadas as vivências dessas mulheres no período após a separação, no que se refere ao desejo por se casar pela segunda vez, aos relacionamentos estabelecidos entre os dois casamentos, às expectativas para o segundo casamento, entre outros aspectos. São também apontadas as especificidades dessa nova relação conjugal, estabelecida após uma separação, abordando as dimensões da administração da vida cotidiana, da vida financeira, bem como a vida sexual e reprodutiva. Após esta pesquisa, foi possível identificar o recasamento como um tema relevante para o desenvolvimento de diversos outros estudos, tendo em vista a diversidade de fatores envolvidos nesse processo, em face às constantes mudanças nas concepções sobre conjugalidade e separação e a escassez de trabalhos sobre o assunto. / A lot of changes have been noticed in the marital scope, from the variety of conjugal arrangements, until the different conceptions about marriage, family and the meanings of these links establishment, configuring the conjugal relation as more possible to be broken up each time. In this context, statistical data (IBGE, 2008) pointed to an increasing number of separations, beyond a progression in the number of people that, after this process, choose to get into another conjugal relation. Considering the researches scarcity about remarriage, and specially, about specific issues of this new conjugal relation, the present work intends to discuss this process and the possible changes that it can lead. Initially, the separation and the remarriage are approached as a trigger for social and cultural changes (at the same time that they are produced by them), beyond the movement during which love becomes connected to marriage, until the moment that it is configured as a reason to this bond establishment. Based on the Schizoanalysis theoretical reference, and adopting the cartographic method as a guiding, eight interviews have been carried out with women that are presently married, at least, for the second time. After these meetings, it was possible to identify extremely special experiences. Their experiences after the separation period are presented here. They refer to the desire of getting married for the second time, the relationships that they had between both marriages, the expectations for the second marriage, among other issues. The specificities of this new conjugal relation are also indicated, established after the separation, dealing with the dimensions of managing the daily routine, the financial situation and the sexual and reproductive lives. After this research, it was possible to identify the remarriage as an important subject to the development of many other studies, considering the diversity of the factors involved in this process, in face of the constant changes in the conjugality and separation conceptions and the scarcity of works about this subject

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Thesis (MTech (Chemical Engineering))--Cape Peninsula University of Technology, Cape Town, 2006 / During recent years, the use of liquid membranes has gained general interest in the treatment of effiuents where solute concentrations are low and large volumes of solutions should be processed, and, if possible, without generating any secondary waste. Liquid membrane processes have been proposed as a clean technology, owing to their characteristics, i.e. high specificity, low energy and utilization. Two liquid membrane processes have been used in metal recovery, which are the liquid surfactant membrane (LSM), which corresponds to double water-in-oil emulsion and solid . supported liquid membranes (SLM), which are made by dispersing or impregnating the extractant within the pores of in.ert solid support. Previously, the recovery of eu (IT) in a SLM system was conducted by other membrane models such as hollow fibre, spiral and flat sheet. Only a small measure of success on scale-up and industrialization of these models has been attained. One of the disadvantages of the hollow fibre system was the small lumen size through which the feed needed to pass. Pores became clogged by suspended particles because the pressure drop over the small diameter augments lower flow rates and therefore, pre-filtering is necessary (Rathore, et al., 2001). In this study the behaviour of a tubular SLM reactor with an inner diameter of the lumen approximately fifty times bigger than that of the hollow fibre are used in order to solve the problem of clogging. This tubular reactor was incorporated in to a bench scale plant and proved successful in copper extraction. By observing transient data, mass transport coefficients were determined and compared to published values.

Thesis (Masters Diploma (Technology)--Cape Technikon, Cape Town,1993 / Various experimental and established membranes were tested on industrial effluents. Ultrafiltration, reverse osmosis and nanofiltration membranes were used in various applications. Research was done on aspects such as the cleaning of fouled membranes, production quality control and process development. Polyvinyl alcohol ultra-thin-film reverse osmosis membranes were manufactured for the desalination of brackish water to a potable standard. The membranes were manufactured in the tubular configuration. Experimental ultrafiltration, reverse osmosis and nanofiltration membranes were tested on cooling water blowdown on a laboratory-scale. On-site testing was done directly on the effluent at a later stage. A s!udy was also conducted to determine the effect of gel-polarization on membrane performance. The gel-layer model was used to predict the limiting flux of specific membranes. Membrane processes were also applied in the fractionation of wine-lees to provide usable by-products such as yeast cells and potassium bitartrate. Ultrafiltration membranes operated in diafiltration mode were used to "wash" the slurry at different solid concentrations. The bitartrate-rich permeate collected from ultrafiltration was then concentrated using reverse osmosis and nanofiltration to allow subsequent precipitation of the product.