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This work reports an investigation of colloidal suspensions during sedimentation in what is known as the intermediate concentration range; one notoriously difficult to study. Two materials were examined: titanium dioxide P25 nanoparticles and magnesium hydroxide. The characterisation of these materials highlighted their high tendency to form aggregates under certain conditions. By the use of laser diffraction, measurements of the cluster size were conducted at under various conditions of shear. The use of sonication energy suggested the identification and classification of two classes of clusters related to their strength: high strength , and low strength clusters. A mathematical model which considered cluster formation and the occurrence of breakage predicted the aggregation and disaggregation kinetics. The approach was based on cluster-cluster interactions rather than particle-particle interactions. The results obtained by particle size analysis were compared with the size obtained using permeability analysis and settling velocity. In both cases the calculated sizes were comparable with the data obtained from size analysis; however, for magnesium hydroxide the predicted cluster size was a little higher and this may be due to the formation of channels giving faster settling. For the titanium dioxide it was noticeable that different mixing strategies exhibited different cluster size, network formation and settling behaviour. Finally, a novel modelling approach based on the presence of clusters rather than particles is presented. It is a combined model which considers the settling curve divided into two zones: a zone below the gel point modelled by a Kynch type approach and a zone above the gel point modelled by consolidation theory. This combined approach was only applicable to the settling data of titanium dioxide, where the settling data encompassed the gel point and the gel point could be identified by consideration of the Richardson and Zaki plots. For magnesium hydroxide, only the consolidation model was needed as all the initial settling concentrations were above the gel point.

The permeability of lipid bilayer membranes to glucose and carboxyfluorescein has been studied in model membranes. Using an enzyme assay, the permeability of glucose was monitored spectrometrically with both large and giant unilamellar vesicles (LUVs and GUVs). The permeability of carboxyfluorescein was studied by entrapping the dye and monitoring its leakage over time from a single GUV. Permeability study using GUVs may provide new information that cannot be obtained from LUVs.The stability of lipid membranes was enhanced by incorporating polymer scaffold. LUVs were prepared with hydrophobic monomers partitioned and then polymerized inside the hydrophobic interior of the lipid bilayers. The sizes of the formed polymers were characterized using gel permeation chromatography and mass spectrometry. This study suggests that large molecular weight polymers were formed inside the lipid bilayers and that the stability of the membranes is related to the size of the polymers.

The skin, by weight, is the largest organ of the body. Human skin serves to provide several important functions that may be classified. in a general context, as protective, maintaining homeostasis and sensing. The outermost layer of the skin, the stratum corneum, has an essential role as a barrier against the transport of water and of chemical and biological agents. In this study acyclovir (ACV), an antiviral used for treating the varicella zoster virus, was used. It is sensible to say that a hydrophilic drug like acyclovir needs a delivery vehicle or penetration enhancer to permeate the skin with more ease. In an attempt to enhance the permeation of acyclovir, it was formulated in a delivery vehicle with the same formulation as for a micro-emulsion. Increasing percentages of the surfactant, Brij 97, were incorporated in the formulation to determine which of the four formulations is indeed a micro-emulsion. A gelating agent. carrageenan, was used to make the emulsion transdermally more applicable; the influence of this component on the transdermal delivery of acyclovir was also determined. Therefore the aim of this study was to determine: -The effect of a drug delivery vehicle on the transdermal delivery of acyclovir; -The specific formulation of a micro-emulsion and -The influence of a gelating agent on the transdermal delivery of acyclovir. Diffusion studies were performed in vertically mounted glass Franz diffusion cells. The epidermis of female abdominal skin, obtained after abdomeoplasty, was heat separated from the dermis. One millilitre of emulsion (0.1%: 1mg/ml ACV) was added to the skin sample in the donor side of the diffusion cell. The control solution had an equivalent amount of active in water and was added to the donor compartment in a separate experiment. The receptor phase was PBS (phosphate buffered solution). The entire receptor phase of the cells was removed every second hour and was replaced with fresh receptor phase at 37°C. The amount of acyclovir in the receptor phase was determined by HPLC analysis. The cumulative amounts of the active that permeated the skin over the 24 hour period were plotted with the slope of the graphs representing the flux in ng/cm²/h. The average flux values of the experimental cells and control cells were compared. Results of the diffusion studies without carrageenan showed that increasing the concentration of the surfactant increased the diffusion of acyclovir. Permeation studies with carrageenan had a totally different outcome. The enhancement ratio of the experimental cells was much lower than that of the control cells. However the experimental cells showed a small increase as the concentration of the surfactant increased. From VanKel dissolution studies it could be seen that release of acyclovir from the emulsion was not a problem and that the active was available for absorption. Confocal studies were done to determine whether there were any vesicles in the emulsions. Vesicles were expected in the 25% Brij 97 emulsion because it was the same formulation as a micro-emulsion, but vesicles could only be found in the 4% and 8% Brij 97 emulsion. A previous study with acyclovir and three different delivery vehicles gave enhancement ratios between 0.32 to 2.92. Values obtained in this study of the 4% and 8% Brij 97 emulsion without carrageenan were more or less the same but the 15% and 25% Brij 97 emulsion had a much higher enhancement ratio. For the emulsions with carrageenan not one exceeded an enhancement ratio of 0.57. More studies still have to be done on micro-emulsions to determine which specific concentration of surfactant forms a micro-emulsion. The active itself and its physicochemical properties also play an important role in the diffusion studies with the specific delivery vehicle and further research has to be done with different model drugs. / Thesis (M.Sc. (Pharmaceutics))--North-West University, Potchefstroom Campus, 2006.

Nanoporous molecular sieve materials like metal organic frameworks (MOFs) and metal oxide nanotubes (AlSiNTs) have found a wide range of technological applications in catalysis, separations, and ion exchange due to their salient features over other contemporary sensing materials. As a result, these materials can function as a chemical recognition layer that relies on analyte adsorption and they have shown to selectively adsorb specific gas molecules from mixtures. The characterization of gas adsorption in these materials is performed predominantly by commercial gravimetric equipment, whose capital and operating costs are generally high and require relatively large amounts of sample. Thus, it is desirable to obtain a reliable measure of the gas transport properties of these materials over a substantial range of pressure and temperature by non-gravimetric methods. The objective of this thesis is to investigate the adsorption and diffusion characteristics of recently-identified nanoporous materials through the development and use of a high-pressure/high-temperature quartz crystal microbalance (QCM) device. In this regard, this thesis is divided into four main objectives, viz. (1) Design and development of high temperature/ high pressure QCM device, (2) Measurement and analysis of adsorption characteristics in nanoporous materials, (3) Diffusion measurement and analysis in polymer thin films and (4) Diffusion measurement and analysis in MOF crystals. The results obtained in Objectives 2-4 will allow us to make important recommendations regarding the use of specific nanoporous materials in molecular separation applications and also lead to significant understanding of gas uptake thermodynamics in nanoporous materials via the application of analytical models to the experimental data.

The skin, by weight, is the largest organ of the body. Human skin serves to provide several important functions that may be classified. in a general context, as protective, maintaining homeostasis and sensing. The outermost layer of the skin, the stratum corneum, has an essential role as a barrier against the transport of water and of chemical and biological agents. In this study acyclovir (ACV), an antiviral used for treating the varicella zoster virus, was used. It is sensible to say that a hydrophilic drug like acyclovir needs a delivery vehicle or penetration enhancer to permeate the skin with more ease. In an attempt to enhance the permeation of acyclovir, it was formulated in a delivery vehicle with the same formulation as for a micro-emulsion. Increasing percentages of the surfactant, Brij 97, were incorporated in the formulation to determine which of the four formulations is indeed a micro-emulsion. A gelating agent. carrageenan, was used to make the emulsion transdermally more applicable; the influence of this component on the transdermal delivery of acyclovir was also determined. Therefore the aim of this study was to determine: -The effect of a drug delivery vehicle on the transdermal delivery of acyclovir; -The specific formulation of a micro-emulsion and -The influence of a gelating agent on the transdermal delivery of acyclovir. Diffusion studies were performed in vertically mounted glass Franz diffusion cells. The epidermis of female abdominal skin, obtained after abdomeoplasty, was heat separated from the dermis. One millilitre of emulsion (0.1%: 1mg/ml ACV) was added to the skin sample in the donor side of the diffusion cell. The control solution had an equivalent amount of active in water and was added to the donor compartment in a separate experiment. The receptor phase was PBS (phosphate buffered solution). The entire receptor phase of the cells was removed every second hour and was replaced with fresh receptor phase at 37°C. The amount of acyclovir in the receptor phase was determined by HPLC analysis. The cumulative amounts of the active that permeated the skin over the 24 hour period were plotted with the slope of the graphs representing the flux in ng/cm²/h. The average flux values of the experimental cells and control cells were compared. Results of the diffusion studies without carrageenan showed that increasing the concentration of the surfactant increased the diffusion of acyclovir. Permeation studies with carrageenan had a totally different outcome. The enhancement ratio of the experimental cells was much lower than that of the control cells. However the experimental cells showed a small increase as the concentration of the surfactant increased. From VanKel dissolution studies it could be seen that release of acyclovir from the emulsion was not a problem and that the active was available for absorption. Confocal studies were done to determine whether there were any vesicles in the emulsions. Vesicles were expected in the 25% Brij 97 emulsion because it was the same formulation as a micro-emulsion, but vesicles could only be found in the 4% and 8% Brij 97 emulsion. A previous study with acyclovir and three different delivery vehicles gave enhancement ratios between 0.32 to 2.92. Values obtained in this study of the 4% and 8% Brij 97 emulsion without carrageenan were more or less the same but the 15% and 25% Brij 97 emulsion had a much higher enhancement ratio. For the emulsions with carrageenan not one exceeded an enhancement ratio of 0.57. More studies still have to be done on micro-emulsions to determine which specific concentration of surfactant forms a micro-emulsion. The active itself and its physicochemical properties also play an important role in the diffusion studies with the specific delivery vehicle and further research has to be done with different model drugs. / Thesis (M.Sc. (Pharmaceutics))--North-West University, Potchefstroom Campus, 2006.

Zeolite membranes are considered to be a promising alternative to polymeric membranes and they have the potential to separate gases under harsh conditions. Silicalite-1 membranes in particular are easy to prepare and suitable for several industrial applications. In this research project, silicalite-1/ceramic composite membranes were prepared using the pore plugging hydrothermal synthesis method and supports with zirconium oxide and/or titanium oxide as active layers. The effect of the support’s pore size on the morphology and permeation performance of the prepared membranes was investigated using five supports with different active layer pore sizes in the range of 0.14 – 1.4 m. The prepared membranes were characterized by X-ray diffraction (XRD), scanning electron microscope (SEM), electron diffraction spectrometer (EDS), single gas and binary gas mixtures permeation tests. The results confirmed the presence of a typical silicalite-1 zeolite structure with a high internal crystalline order grown inside the pores of the active layer of the supports, with a dense film covering most of the supports active layers. Silicalite-1 crystals in the prepared membranes were preferably oriented with either a- or b-axes perpendicular to the support surface. Single gas permeation results illustrated that the observed permeances were not directly related to the kinetic diameter of permeants. Instead, the transport of the studied gases through the prepared membranes occurred by adsorption followed by surface diffusion mechanism. Binary gas tests performed with CO2 and N2 mixtures showed that the prepared membranes were selective and very permeable with CO2/N2 permselectivities up to 30 and a CO2 permeances in the order of 10-6 mol m-2 Pa-1 s-1. A model was developed, based on Maxwell−Stefan equations and Extended Langmuir adsorption isotherm, to describe the transport of binary CO2 and N2 mixtures through the prepared silicalite-1 membranes. The model results showed that the exchange diffusivities (D12 and D21) were less dependent on the feed pressure and feed composition compared to the permeances and the permselectivities. Hence, they are more appropriate to characterize the intrinsic transport properties of the prepared silicalite-1 membranes.

Characterization of semi-permeable films promotes the systematic selection of membranes and process design. When acquiring the diffusive and sorption properties of gas transport in non-porous membranes, the time lag method is considered the conventional method of characterization. The time lag method involves monitoring the transient accumulation of species due to permeation on a fixed volume present in a downstream reservoir. In the thesis at hand, an alternative approach to the time lag technique is proposed, termed as the short cut method. The short cut method appoints the use of a two reservoir system, where the species decay in the upstream face of the membrane is monitored, in combination with the accumulation on the downstream end. The early and short time determination of membrane properties is done by monitoring the inflow and outflow flux profiles, including their respective analytical formulas. The newly proposed method was revealed to have estimated the properties at 1/10 the required time it takes for the classical time lag method, which also includes a better abidance to the required boundary conditions. A novel design of the upstream reservoir, consisting of a reference and working volume, is revealed, which includes instructional use, and the mechanics involved with its operation. Transient pressure decay profiles are successfully obtained when the reference and working volumes consisted of only tubing. However when tanks were included in the volumes, large errors in the decay were observed, in particular due to a non-instantaneous equilibration of the pressure during the start up. This hypothesis was further re-enforced by examining different upstream tank-based configurations. iii In the end, a validated numerical model was constructed for the purpose of simulating the two reservoir gas permeation system. A modified form of the finite differences scheme is utilized, in order to account for a concentration-dependent diffusivity of penetrants within the membrane. Permeation behavior in a composite membrane system was disclosed, which provided a new perspective in analyzing the errors associated with the practical aspect of the system.

Killer yeasts secrete polypeptide toxins which kill sensitive cells of their own species and frequently those of other species and genera of yeasts. These protein compounds are designated as killer toxins. Also killer toxins of certain yeast strains have potential growth inhibitory activity on gram-positive pathogenic bacteria and plant pathogenic fungi. The yeasts are immune to their own killer protein. The killer phenomenon can be utilized for the protection of fermentation process against contaminating yeasts and for biological control of undesirable yeasts in the preservation of foods. The killer trait can also be used to produce large amount of foreign proteins in yeast. In the medical field , it is thought that their anti-microbial and anti-mycotic activity could be exploited in a therapeutic strategy. Yeast killer toxins are classified into 11 types according to their killing spectra and immunity-specificities such as K1, K2, etc. Altough there is considerable amount of published information concerning the applications of yeast killer toxins , among the 11 types , only K1 , K2 and K6 have been characterized. In this study , it was aimed to purify and characterize the K4 type yeast killer toxin secreted by the Hansenula anomala NCYC 432. Gel permeation chromatography was performed to isolate the killer toxin by using a HPLC system. The toxin was shown to be a glycoprotein having a molecular mass of between 49.08 kDa and 47.25 kDa and isoelectric point of between 3.77 and 3.41.

The effect of seeding on the properties of alumina supported MFI membranes was investigated in this study. Membranes were synthesized from clear solutions with a molar batch composition of TPAOH:9.80SiO2:0.025NaOH:0.019Al2O3: 602.27H2O:39.16C2H5OH on bare and seeded alumina supports at 130oC in autoclaves. The amount of seed on the support surface was changed between 0.6 mg/cm2 and 6.9 mg/cm2 by vacuum seeding method, which provided uniform and closely packed seed layers. Membranes were characterized by XRD and SEM, and by measuring single gas permeances of N2, SF6, n-C4H10 and i-C4H10. The quality of membranes was evaluated on the basis of N2/SF6 ideal selectivity. Membranes, which showed N2/SF6 ideal selectivity higher than 40, were considered to be good quality, comprising few defects. Good quality membranes were also used to separate butane isomers. Membranes synthesized on seeded supports had compact and uniform MFI layer if the seed amount is less than 1.0 mg/cm2 on the support surface. Membranes that were synthesized on the supports coated with higher amount of seed crystals showed an asymmetric structure with a dense and uniform MFI layer at the top, the support at the bottom and a seed layer between. Half of the membranes synthesized on seeded supports had N2/SF6 ideal selectivity higher than 40. These membranes exhibited n-C4H10/i-C4H10 separation selectivities between 5 and 27 and 8 and 21 at room temperature and at 200oC, respectively. High ideal and separation selectivities showed that membranes did not include non-zeolitic pores. Membranes synthesized on bare support had non-uniform MFI layer. Those membranes showed N2/SF6 ideal selectivities below Knudsen selectivity, indicating the existence of large non-zeolitic pores in the MFI layer.