Chemical and Biomolecular Engineering - Theses
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ItemAssembly of polymer matrices enveloping cubic lyotropic liquid crystalline nanoparticles for drug delivery applications( 2012)Cubic lyotropic liquid crystalline nanoparticles (cubosomes™) exhibit great potential as drug delivery vehicles due to their nanoscale size, biocompatible constituents, and high loading potential for hydrophobic, hydrophilic, and amphiphilic agents. However, they also suffer from some limitations which have restricted their clinical effectiveness. For example, they release their cargo in a rapid, uncontrolled manner— a phenomenon known as burst release. In addition, the lipids which form reverse cubic phase typically do not contain surface functional groups for the immobilisation of targeting or stealth providing moieties. Polymeric capsules, in particular those made with the layer-by-layer technique, are able to modify the release properties of a loaded drug according to the number and nature of polymer layers. Many of the polymers employed also contain available functional groups for additional chemistry. However polymeric capsules can be difficult to efficiently load with therapeutic agents, particularly when the drugs are lipid soluble. Additionally, the removal of the capsule core template often requires conditions that can cause instability. This thesis examined the use of polymers to modulate the properties of cubosomes with the intention to aid stability, limit burst release, add potential functionality, and increase the payload. Different methods used to prepare stable, well dispersed amphiphilic cubosomes (high pressure homogenisation, extrusion, and ultrasonication) were analysed and compared. The effect of an additive to the aqueous environment (such as sodium chloride or phosphate buffered saline (PBS)) was also investigated. Certain additives to the amphiphile matrix such as the charged lipids cetyl trimethylammonium bromide (CTAB), dioctadecyl-dimethylammonium bromide (DODAB) or sodium dodecyl sulphate (SDS) were found to cause structural changes to both bulk and dispersed cubic phase but could be tolerated up to a certain quantity before complete destabilisation occurred. Integrating cubic nanoparticles and polymer matrices was first accomplished by coating silica microparticles. This resulted in a multilayered polymer coating representing an embedded layer of cubosomes surrounded by poly(allylamine hydrochloride) (PAH) and poly(styrene sulfonate) (PSS) polyelectrolytes. Upon removal of the silica core, stable polymer microcapsules containing embedded cubic nanoparticles were obtained. A diversity of molecular encapsulation matrices is offered through the capsule core, polyelectrolyte layers, and the embedded cubosomes of these sub-compartmentalised, nanostructured microcapsules. Individual cubic nanoparticles surrounded by polyelectrolyte multilayers were prepared next. The polymers were able to interact with the non-charged cubic lipid nanoparticles by utilising a polyelectrolyte modified with hydrophobic side chains (poly(methacrylic acid-co-oleyl methacrylate), PMAO) as an initial layer. Three bi-layers of poly(L-lysine) (PLL) and poly(methacrylic acid) (PMA) were then sequentially added. In order to separate accrued polymer aggregates from the coated lipid nanoparticles, a simple technique was developed whereby centrifugation separated the less dense cubosomes for collection. Modulation of the drug release properties and attenuation of the burst release from coated cubosome particles was demonstrated using two model drugs (fluorescein and perylene). The modified polymer PMAO was then utilised as an alternative stabiliser for lyotropic liquid crystalline nanoparticles. The charge-stabilised particles were tested against the most commonly utilised steric stabiliser Pluronic F127 for stability and drug release characteristics. Although PMAO-stabilised nanoparticles still exhibited burst release, improved particle stability was observed over time and over a range of temperatures, including storage under refrigeration. A lesser amount of PMAO stabiliser and less energy input were also required to disperse the bulk lipid into discrete, uniform nanoparticles compared to Pluronic F127. These studies demonstrate the viability of combining layer-by-layer polymer matrix technology with cubic lyotropic liquid crystalline nanoparticles to enhance the future of drug delivery.
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ItemDrinking water treatment sludge production and dewaterabilityф(D. I. Verrelli, 2008)The provision of clean drinking water typically involves treatment processes to remove contaminants. The conventional process involves coagulation with hydrolysing metal salts, typically of aluminium (‘alum’) or trivalent iron (‘ferric’). Along with the product water this also produces a waste by-product, or sludge. The fact of increasing sludge production — due to higher levels of treatment and greater volume of water supply — conflicts with modern demands for environmental best practice, leading to higher financial costs. A further issue is the significant quantity of water that is held up in the sludge, and wasted. One means of dealing with these problems is to dewater the sludge further. This reduces the volume of waste to be disposed of. The consistency is also improved (e.g. for the purpose of landfilling). And a significant amount of water can be recovered. The efficiency, and efficacy, of this process depends on the dewaterability of the sludge.In fact, good dewaterability is vital to the operation of conventional drinking water treatment plants (WTP’s). The usual process of separating the particulates, formed from a blend of contaminants and coagulated precipitate, relies on ‘clarification’ and ‘thickening’, which are essentially settling operations of solid–liquid separation.WTP operators — and researchers — do attempt to measure sludge dewaterability, but usually rely on empirical characterisation techniques that do not tell the full story and can even mislead. Understanding of the physical and chemical nature of the sludge is also surprisingly rudimentary, considering the long history of these processes. The present work begins by reviewing the current state of knowledge on raw water and sludge composition, with special focus on solid aluminium and iron phases and on fractal aggregate structure. Next the theory of dewatering is examined, with the adopted phenomenological theory contrasted with empirical techniques and other theories.The foundation for subsequent analyses is laid by experimental work which establishes the solid phase density of WTP sludges. Additionally, alum sludges are found to contain pseudoböhmite, while 2-line ferrihydrite and goethite are identified in ferric sludges. A key hypothesis is that dewaterability is partly determined by the treatment conditions. To investigate this, numerous WTP sludges were studied that had been generated under diverse conditions: some plant samples were obtained, and the remainder were generated in the laboratory (results were consistent). Dewaterability was characterised for each sludge in concentration ranges relevant to settling, centrifugation and filtration using models developed by LANDMAN and WHITE inter alia; it is expressed in terms of both equilibrium and kinetic parameters, py(φ) and R(φ) respectively.This work confirmed that dewaterability is significantly influenced by treatment conditions.The strongest correlations were observed when varying coagulation pH and coagulant dose. At high doses precipitated coagulant controls the sludge behaviour, and dewaterability is poor. Dewaterability deteriorates as pH is increased for high-dose alum sludges; other sludges are less sensitive to pH. These findings can be linked to the faster coagulation dynamics prevailing at high coagulant and alkali dose.Alum and ferric sludges in general had comparable dewaterabilities, and the characteristics of a magnesium sludge were similar too.Small effects on dewaterability were observed in response to variations in raw water organic content and shearing. Polymer flocculation and conditioning appeared mainly to affect dewaterability at low sludge concentrations. Ageing did not produce clear changes in dewaterability.Dense, compact particles are known to dewater better than ‘fluffy’ aggregates or flocs usually encountered in drinking water treatment. This explains the superior dewaterability of a sludge containing powdered activated carbon (PAC). Even greater improvements were observed following a cycle of sludge freezing and thawing for a wide range of WTP sludges. Further aspects considered in the present work include deviations from simplifying assumptions that are usually made. Specifically: investigation of long-time dewatering behaviour, wall effects, non-isotropic stresses, and reversibility of dewatering (or ‘elasticity’).Several other results and conclusions, of both theoretical and experimental nature, are presented on topics of subsidiary or peripheral interest that are nonetheless important for establishing a reliable basis for research in this area. This work has proposed links between industrial drinking water coagulation conditions, sludge dewaterability from settling to filtration, and the microstructure of the aggregates making up that sludge. This information can be used when considering the operation or design of a WTP in order to optimise sludge dewaterability, within the constraints of producing drinking water of acceptable quality.