Increasing environmental awareness over the past decade as well as stringent environmental laws forced all factories to invest in water treatment processes for effluent treatment before discharge or re-use. Most of these effluent treatment processes utilize membranes as the physical. barrier for separation. The membranes used in water applications are expensive and alternative materials and production techniques will increase the viability of membrane separation processes. Experiments conducted on irradiated polyethylene showed that some of its properties were enhanced while others deteriorated. However, the enhanced properties make the polyethylene, in particular ultra-high molecular weight polyethylene, an ideal membrane material. The manufactured membranes were tested in extraction experiments, and satisfactory results were obtained. Permeation studies on the membranes compared favourably with similar studies done on commercially available membranes. An extraction rate of 1.08 g/(m2h) nickel was achieved. A preliminary cost evaluation showed that these membranes can be manufactured at a low cost (R13.45/m2). and can be applied as supported liquid membranes. Future research should focus on methods to decrease the brittleness and stiffness of the membranes. / Thesis (MIng)--PU for CHE, 1999

Increasing environmental awareness over the past decade as well as stringent environmental laws forced all factories to invest in water treatment processes for effluent treatment before discharge or re-use. Most of these effluent treatment processes utilize membranes as the physical. barrier for separation. The membranes used in water applications are expensive and alternative materials and production techniques will increase the viability of membrane separation processes. Experiments conducted on irradiated polyethylene showed that some of its properties were enhanced while others deteriorated. However, the enhanced properties make the polyethylene, in particular ultra-high molecular weight polyethylene, an ideal membrane material. The manufactured membranes were tested in extraction experiments, and satisfactory results were obtained. Permeation studies on the membranes compared favourably with similar studies done on commercially available membranes. An extraction rate of 1.08 g/(m2h) nickel was achieved. A preliminary cost evaluation showed that these membranes can be manufactured at a low cost (R13.45/m2). and can be applied as supported liquid membranes. Future research should focus on methods to decrease the brittleness and stiffness of the membranes. / Thesis (MIng)--PU for CHE, 1999

A sampler has been fabricated to facilitate the in-situ speciation of Cr. Teflon® was selected as the material for the samplers because of its inert chemical nature. The design of the sampler is based on the Supported Liquid Membrane (SLM) extraction technique, which utilizes charged organic carrier molecules loaded onto a polymeric (Teflon®) support membrane and the principles of electrostatics to selectively transport Cr ions through an ion-pairing mechanism. Cr ions in the feed solution that have an opposite charge from the carrier molecule form an ion-pair with the carrier and are transported through the membrane and deposited into a second aqueous phase referred to as the acceptor phase. A counter-ion from the acceptor phase is exchanged for the Cr ion to complete the extraction process. Since the acceptor phase is contained in a Teflon® bottle, the SLM sampler is capable of speciation and storage of Cr ions, which is a major advantage over current speciation techniques. A food coloring test was used to check the samplers for leaks. A plastic barrier was used in place of the polymeric membrane and the acceptor phase bottle was filled with DI water. The sampler was submerged in a beaker containing food coloring and DI water. The bottle contents were checked for the presence of food coloring using UV-vis spectroscopy. The sampler was determined to be leak-free if the bottle did not contain food coloring. All systems prepared were validated upon the initial test and required no further manipulation to ensure structural soundness. The SLM extraction technique involves two liquid-liquid extractions (LLEs). Before the samplers could be evaluated for their performance and stability in Cr speciation applications, liquid-liquid extraction studies were conducted on both systems (Cr (III) and Cr (VI)) to determine the optimal operating parameters (carrier concentration, decanol concentration, and acceptor phase concentration) of the SLM system. The selectivity of each system was also evaluated to validate proper SLM function. The performance of the samplers was evaluated in a series of tank studies that focused on the uptake of Cr into the acceptor phase as well as the depletion of Cr ion from this phase. The goal of the performance studies was to determine the mechanical and chemical stability of the SLM samplers. As part of the validation process, selectivity studies and studies without the carrier molecule were conducted to ensure that the systems were functioning according to SLM theory. Tank studies that simulated natural sampling condition were also conducted. The results of the tests conducted in the laboratory indicate that the SLM samplers are a stable, reliable, and viable method for Cr speciation. Future directions of this project will include the incorporation of the SLM sampler into the existing Multi-layer Sampler (MLS) technology as well as the analysis of the stability and performance of the incorporated systems in the ""in-situ speciation application. / Ph. D.

This report details the development and validation of a model for the simulation of supported liquid membrane processes, as applied to the extraction of lanthanides. Supported liquid membranes are systems where two phases, usually aqueous, are separated by a third phase, typically organic, which acts as a membrane, in order to separate solutes from one phase to the other. The model employs an analytical solution to the diffusion equation for the organic phase and linear approximations of the resistances to mass transfer in the aqueous phase boundary layers. The goal of this model is to underline the importance of taking these boundary layer resistances into account. / Detta arbete introducerar, deriverar och evaluerar en matematisk modell för simulering av vätskemembranprocesser, tillämpat på vätskeextraktion av lantanider. Immobiliserade vätskemembran betecknar system där två faser oftast vatten, separeras av en tredje organisk fas som agerar membran för att separera och transportera lösta komponenter från den ena vattenfasen till den andra. Modellen utnyttjar sig av en analytisk lösning till diffusionsekvationen för den organiska fasen och linjära approximationer för motstånden mot masstransport i de båda vattenfasernas gränsskikt. Målet med modellen är att understryka vikten av att inkludera dessa gränsskikt i beräkningarna.

El presente trabajo de Tesis tiene como finalidad analizar el potencial de los líquidos iónicos como medios de reacción y separación en reacciones de transesterificación enzimáticas. Los ILs inmiscibles con agua han resultado medios muy adecuados para llevar a cabo la síntesis de ésteres catalizada por la lipasa B de Candida antarctica (CALB), incrementando la actividad y selectividad enzimática con respecto a los valores obtenidos en disolventes orgánicos convencionales como n-hexano. El uso de líquidos iónicos miscibles con agua ha dado lugar a menores valores de actividad enzimática que n-hexano, aunque la selectividad en estos medios es mucho mayor. Los ILs se han revelado también como prometedores disolventes en su empleo en procesos de separación, más concretamente como fase líquida en membranas líquidas soportadas (SLMs). Se han desarrollado SLMs basadas en ILs altamente estables que permiten llevar a cabo la separación selectiva de sustratos y productos de reacciones de transesterificación. / The main objective of this thesis is to analyze the potential use of ionic liquids as reaction and separation media in lipase-catalysed transesterification reactions. The use of ionic liquids in biocatalytic processes has been shown to be an environmentally attractive alternative to classical organic solvents. Water-immiscible ionic liquids appeared as suitable media for the transesterification reactions catalysed by Candida antarctica lipase B (CALB), increasing the activity and selectivity with respect to the values obtained with a classical organic solvent, n-hexane. The use of water-miscible ionic liquids led to lower activities than obtained in n-hexane, although the selectivity values were much higher in these media. Ionic liquids have also been shown to be promising solvents for the use in separation processes, more specifically as liquid phase in supported liquid membranes (SLMs). Highly stable SLMs based on ionic liquids have been succesfully used for the selective separation of different organic compounds which are substrates and products of transesterification reactions.