In the present study, the dissolution mechanism and rate of lime, limestone and dolomite in converter slag was studied. Lime dissolution in stagnant slag was studied first and dissolution of lime, limestone and dolomite under forced convection were carried out by new experimental setup. Dissolution of different CaO samples into stagnant converter slags was carried out in a closed tube furnace at 1873K. In the case of CaO-‘FeO’-SiO2 slag, the dissolution of CaO rod in the stagnant slag was retarded after the initial period (2 minutes). A dense layer of 2CaO∙SiO2 was found to be responsible for the total stop of the dissolution. It could be concluded that constant removal of the 2CaO∙SiO2 layer would be of essence to obtain high dissolution rate of lime. In this connection, it was found necessary to study the dissolution of lime in moving slag. In order to obtain reliable information of lime dissolution under forced convection, the commonly used rotating rod method was examined. Both CFD calculation and cold model experiments showed evidently that the mass transfer due to radial velocity introduced by forced convection was zero if the rod was centrally placed in a cylindrical container. A new experimental design was therefore developed. A cube was placed in the crucible and stirred by Mo rod along with slag. The whole system could be quenched in order to maintain the state of the system at high temperature. A linear relationship between normalized length and time was obtained for lime dissolution. Different lime samples showed big difference in dissolution rate. It was found that the main mechanism of CaO dissolution in slag was due to the removal of 2CaO∙SiO2 layer. Decomposition and dissolution of limestone and dolomite in slag at 1873 K were studied. The decomposition was carried out both in argon and in slag under argon atmosphere. The decomposition process was simulated using Comsol. The results showed evidently that the decomposition of limestone and dolomite was controlled mostly by heat transfer. It was also found that the decomposition of limestone product: CaO had very dense structure, no matter the sample was decomposed in slag or in argon. The slow decomposition and the dense CaO layer would greatly hinder the dissolution of lime in the slag. The present results clearly indicate that addition of limestone instead of lime would not be beneficial in converter process. Discontinuous 2CaO∙SiO2 layer along with MgO∙Fe2O3 particles was found on the surface of the dolomite sample. Some 2CaO∙SiO2 islands were found in the vicinity of the sample in the slag, which revealed therefore that the dissolution was dominated by the peeling-off of the layer of 2CaO∙SiO2-MgO∙Fe2O3 mixture. 2CaO∙SiO2, (Mg, Fe)Oss along with super cooled liquid phases were found inside dolomite sample close to the surface. 2CaO∙SiO2 phase was replaced gradually by 3CaO∙SiO2 towards the centre of the decomposed sample. / <p>QC 20120829</p>

Afin de mieux comprendre la cohesion entre les bioverres et le tissu osseux, on a realise des essais de dissolution a ph non controle, dans le tampon tris-hydroxymethyl aminomethane et a ph stabilise, sur des verres du systeme sio::(2)-na::(2)o-cao-p::(2)o::(5) sous forme de poudres ou d'esquilles

Matrix acidizing is used in carbonate formations to create wormholes that connect the formation to the wellbore. Hydrochloric acid, organic acids, or mixtures of these acids are typically used in matrix acidizing treatments of carbonate reservoirs. However, the use of these acids in deep wells has some major drawbacks including high and uncontrolled reaction rate and corrosion to well tubulars, especially those made of chrome-based tubulars (Cr-13 and duplex steel), and these problems become severe at high temperatures. Hydrochloric acid (HCl) and its based fluids have a major drawback in stimulating shallow (low fracture gradient) formations as they may cause face dissolution (formation surface washout) if injected at low rates. The objective of stimulation of sandstone reservoirs is to remove the damage caused to the production zone during drilling or completion operations. Many problems may occur during sandstone acidizing with Hydrochloric/Hydrofluoric acids (HCl/HF) mud acid. Among those problems: decomposition of clays in HCl acids, precipitation of fluosilicates, the presence of carbonate can cause the precipitation of calcium fluorides, silica-gel filming, colloidal silica-gel precipitation, and mixing between various stages of the treatment. To overcome problems associated with strong acids, chelating agents were introduced and used in the field. However, major concerns with most of these chemicals are their limited dissolving power and negative environmental impact. Glutamic acid diacetic acid (GLDA) a newly developed environmentally friendly chelate was examined as stand-alone stimulation fluid in deep oil and gas wells. In this study we used GLDA to stimulate carbonate cores (calcite and dolomite). GLDA was also used to stimulate and remove the damage from different sandstone cores containing different compositions of clay minerals. Carbonate cores (calcite and dolomite) of 6 and 20 in. length and 1.5 in. diameter were used in the coreflood experiments. Coreflood experiments were run at temperatures ranging from 180 to 300oF. Ethylene diamine tetra acetic acid (EDTA), hydroxyl ethylethylene diaminetriacetic acid (HEDTA), and GLDA were used to stimulate and remove the damage from different sandstone cores at high temperatures. X-ray Computed Topography (CT) scans were used to determine the effectiveness of these fluids in stimulation calcite and dolomite cores and removing the damage from sandstone cores. The sandstone cores used in this study contain from 1 to 18 wt percent illite (swellable and migratable clay mineral). GLDA was found to be highly effective in creating wormholes over a wide range of pH (1.7-13) in calcite cores. Increasing temperature enhanced the reaction rate, more calcite was dissolved, and larger wormholes were formed for different pH with smaller volumes of GLDA solutions. GLDA has a prolonged activity and leads to a decreased surface spending resulting in face dissolution and therefore acts deeper in the formation. In addition, GLDA was very effective in creating wormholes in the dolomite core as it is a good chelate for magnesium. Coreflood experiments showed that at high pH values (pH =11) GLDA, HEDTA, and EDTA were almost the same in increasing the permeability of both Berea and Bandera sandstone cores. GLDA, HEDTA, and EDTA were compatible with Bandera sandstone cores which contains 10 wt percent Illite. The weight loss from the core was highest in case of HEDTA and lowest in case of GLDA at pH 11. At low pH values (pH =4) 0.6M GLDA performed better than 0.6M HEDTA in the coreflood experiments. The permeability ratio (final/initial) for Bandera sandstone cores was 2 in the case of GLDA and 1.2 in the case of HEDTA at pH of 4 and 300oF. At high pH HEDTA was the best chelating agent to stimulate different sandstone cores, and at low pH GLDA was the best one. For Berea sandstone cores EDTA at high pH of 11 was the best in increasing the permeability of the core at 300oF. The low pH GLDA based fluid has been especially designed for high temperature oil well stimulation in carbonate and sandstone rock. Extensive studies have proved that GLDA effectively created wormholes in carbonate cores, is gentle to most types of casing including Cr-based tubular, has a high thermal stability and gives no unwanted interactions with carbonate or sandstone formations. These unique properties ensure that it can be safely used under extreme conditions for which the current technologies do not give optimal results. Furthermore, this stimulation fluid contributes to a sustainable future as it based on readily biodegradable GLDA that is made from natural and renewable raw material.

A novel approach to geologic CO₂ sequestration is the surface dissolution method. This method involves lifting native brine from an aquifer, dissolution of CO₂ into the brine using pressurized mixing and injection of the CO₂ saturated brine back into the aquifer. This approach has several advantages over the conventional approach, including minimization of the risk of buoyancy driven leakage and dramatic reduction in the extent of pressure elevation in the storage structure. The mass transfer coefficient for the CO₂/brine two-phase system and associated transport calculations allow efficient design of the surface equipment required to dissolve CO₂ under pressure. This data was not previously available in the literature. Original experimental data on the rate of dissolution of CO₂ into Na-Ca-Cl brines across a range of temperatures and wet CO₂ densities are presented. From this data, the intrinsic mass transfer coefficient between CO₂-rich and aqueous phases has been calculated. The statistically significant variation in the mass transfer coefficient was evaluated and compared with the variation caused by the experimental method. An empirical correlation was developed that demonstrates that the mass transfer coefficient is a function of the NaCl salinity, temperature and wet CO₂ density. For the conditions tested, the value of the coefficient is in the range of 0.015 to 0.056 cm/s. Greater temperature and smaller NaCl salinity increases the mass transfer coefficient. There is an interaction effect between temperature and wet CO₂ density, which increases or decreases the mass transfer coefficient depending on the value of each. CaCl₂ salinity does not have a statistically significant effect on the mass transfer coefficient. The transport calculations demonstrate that wellhead co-injection of CO₂ and brine is feasible, providing the same technical outcome at lower cost. For example, assuming a 2000 ft deep well and typical aquifer injection conditions, complete dissolution of the bulk COv phase can be achieved at 670 ft for bubbles of 0.16 cm initial radius. Using a horizontal pipe or mixing tank was also shown to be feasible. Gas entrainment was shown to provide a marked reduction in size of mixing apparatus required. / text

No description available.

Azithromycin, an azalide and member of the macrolide group, is a broad spectrum antimicrobial, representing one of the bestselling antimicrobials worldwide. It is derived from erythromycin and exhibits improved acidic stability as a result of its structural modifications. The stable solid form of azithromycin is its dihydrate, although it also naturally occurs in its metastable forms, i.e. the monohydrate and anhydrate. Because azithromycin is poorly soluble in water, its absorption from the gastro-intestinal tract is negatively influenced, which ultimately affects its bioavailability following oral administration (37 %). Polymorphic (monohydrates and dihydrates) and anhydrous forms of azithromycin were screened and investigated. One anhydrous form also proved to be amorphous, which shifted the focus of this study from polymorphism to amorphism. An amorphous glassy azithromycin was subsequently prepared and fully characterised to present its solid state profile. The stability of this amorphous glassy form was established at a high temperature and relative humidity over a period of four weeks. Exposure to increased relative humidity (up to 95 %) and increased water content (up to 50 %) also served as stability indicating tests. Its solubility in various aqueous media was determined. A solid dosage form (tablet), containing the azithromycin glass, was prepared, whereafter these tablets were subjected to dissolution studies in different aqueous media. The stability of azithromycin glass in tablet form was determined over a period of three months. The permeability of azithromycin glass across excised pig intestinal tissue was further established at various pH values. This amorphous glassy form of azithromycin (AZM-G) proved to be very stable at high temperature and relative humidity, whilst also remaining stable after prolonged exposure to 95 % of relative humidity, as it only adsorbed moisture onto its surface. Water content (up to 50 %) had no plasticising effect on azithromycin glass. It demonstrated a significantly higher water solubility (339 % improvement) in comparison with the commercially available azithromycin dihydrate and was it also 39 % more soluble in phosphate buffer (pH 6.8) than its dihydrate counterpart. The prepared azithromycin glass tablets showed a promising dissolution profile in water, due to the improved water solubility of this glass form. The transport of azithromycin glass at higher pH values (6.8 and 7.2) across the membrane proved to be significantly higher than that of azithromycin dihydrate, thus also illustrating its pH dependence for its transport across pig intestinal tissue. The improved water solubility of the azithromycin glass, together with its faster dissolution rate, its superior stability and its increased permeability, may ultimately result in a higher azithromycin bioavailability following oral administration. These research outcomes hence give rise to the need for investigating the effect of administering lower dosages of azithromycin and to determine whether the same antimicrobial efficacy would possibly be achieved, due to maintaining the same tissue concentration levels at these lower dosages. / Thesis (PhD (Pharmaceutics))--North-West University, Potchefstroom Campus, 2013

Azithromycin, an azalide and member of the macrolide group, is a broad spectrum antimicrobial, representing one of the bestselling antimicrobials worldwide. It is derived from erythromycin and exhibits improved acidic stability as a result of its structural modifications. The stable solid form of azithromycin is its dihydrate, although it also naturally occurs in its metastable forms, i.e. the monohydrate and anhydrate. Because azithromycin is poorly soluble in water, its absorption from the gastro-intestinal tract is negatively influenced, which ultimately affects its bioavailability following oral administration (37 %). Polymorphic (monohydrates and dihydrates) and anhydrous forms of azithromycin were screened and investigated. One anhydrous form also proved to be amorphous, which shifted the focus of this study from polymorphism to amorphism. An amorphous glassy azithromycin was subsequently prepared and fully characterised to present its solid state profile. The stability of this amorphous glassy form was established at a high temperature and relative humidity over a period of four weeks. Exposure to increased relative humidity (up to 95 %) and increased water content (up to 50 %) also served as stability indicating tests. Its solubility in various aqueous media was determined. A solid dosage form (tablet), containing the azithromycin glass, was prepared, whereafter these tablets were subjected to dissolution studies in different aqueous media. The stability of azithromycin glass in tablet form was determined over a period of three months. The permeability of azithromycin glass across excised pig intestinal tissue was further established at various pH values. This amorphous glassy form of azithromycin (AZM-G) proved to be very stable at high temperature and relative humidity, whilst also remaining stable after prolonged exposure to 95 % of relative humidity, as it only adsorbed moisture onto its surface. Water content (up to 50 %) had no plasticising effect on azithromycin glass. It demonstrated a significantly higher water solubility (339 % improvement) in comparison with the commercially available azithromycin dihydrate and was it also 39 % more soluble in phosphate buffer (pH 6.8) than its dihydrate counterpart. The prepared azithromycin glass tablets showed a promising dissolution profile in water, due to the improved water solubility of this glass form. The transport of azithromycin glass at higher pH values (6.8 and 7.2) across the membrane proved to be significantly higher than that of azithromycin dihydrate, thus also illustrating its pH dependence for its transport across pig intestinal tissue. The improved water solubility of the azithromycin glass, together with its faster dissolution rate, its superior stability and its increased permeability, may ultimately result in a higher azithromycin bioavailability following oral administration. These research outcomes hence give rise to the need for investigating the effect of administering lower dosages of azithromycin and to determine whether the same antimicrobial efficacy would possibly be achieved, due to maintaining the same tissue concentration levels at these lower dosages. / Thesis (PhD (Pharmaceutics))--North-West University, Potchefstroom Campus, 2013

In some diseases it is preferable that the drugs used in their treatment are released in the colon. The colon is also suitable for systemic delivery of a variety of drugs. A variety of systems have been developed for the purpose of achieving colonic targeting. These approaches are either drug-specific (prodrugs) or formulation specific (coated or matrix preparations) and depends on the pH, transit time and pressure or bacteria in the colon. Different polymers, like chitosan, have been evaluated for their susceptibility to degradation by these bacterial enzymes. Chitosan is considered a good candidate for bacterial degradation and is widely available at low cost and has favourable biological properties. To investigate the influence of formulation factors on the properties of chitosan minitablets, it was necessary to ensure that the chitosan had satisfactory powder flow characteristics to ensure uniform compression in the tablet press and to prevent unacceptable variation in the tablet properties such as weight, thickness, disintegration and strength. Moisture content of the powder, particle size and the inclusion of glidants had an effect on the flowability and it could be improved from a composite flow index value of 32.7 to a value of 58.8. The compressibility of chitosan is very poor and different factors that might influence it, was investigated. Compression forces of between 15 and 20 bar resulted in tablets with acceptable physical characteristics. An increase in moisture content, using the powder fraction > 212 ym as well as a decrease in powder weight resulted in tablets with a higher tensile strength. Lower compression forces resulted in tablets that are extremely porous. This suggests that the chitosan can only be compressed at high compression forces which are difficult to obtain using a standard tablet press. The standard tablet press was therefore modified to fill more powder in the die and generate higher compression forces. Minitablets were compressed and the dissolution of isoniazide from these tablets was investigated. Varying the punch depth or the compaction of the powder did not result in the desired slower release of the drug as a result. The porosity of the tablets compressed at all the punch depth settings and compaction percentages was probably too high to have an effect on the wettablity of the tablets and as a result on the dissolution of the isoniazide from the tablets. The inclusion of excipients such as citric acid (an organic acid which would lower the pH in the tablet, allowing the chitosan to form a gel) and pectin (which would form an insoluble complex with the chitosan) into the formulation delayed the dissolution of the isoniazide from the minitablets. Coating of the minitablets with an enteric coating (Eudragit S ®) initially delayed the dissolution of the isoniazide and would protect the tablets from the harsh environment of the stomach so that the tablets will reach the colon and release the drug. / Thesis (Ph.D. (Pharmaceutics))--North-West University, Potchefstroom Campus, 2007

No description available.

No description available.