Les sources secondaires de métaux précieux, tels que les déchets électroniques, ont récemment attiré l’attention générale suite à la sensibilisation sur l’épuissement des ressources naturelles et sur l’industrie du recyclage sur l’emploi et la croissance économique. Developper des technologies de recyclage qui permettent l’extraction de palladium (Pd) et d’or (Au) en très faibles concentrations (10-100 ppm) dans les effluents électroniques s’avère aujourd’hui économiqueemnt viable.Dans ce contexte, notre étude aborde l’utilisation de nanoparticules de ZrO2 modifiées avec des ligands complexants en surface pour capturer efficacement et sélectivement des ions Pd(II) et Au(III) dan les effluents électroniques. Les avantages de l’utilisation de acide thioctique commercial (TOA) par rapport aux acides dialkyldiglycoamide ou (N, N)-dialkylcarbamoylméthylphosphoniques en termes de capacité d’adsorption et de sélectivité ont été démontrés. Des expériences d’adsorption en mode batch combinées à la méthode ICP-OES ont été réalisées et nos résultats ont montré des capacités d’adsorption envers le Pd et l’Au de 6.3 mg/g et de 43 mg/g, respectivement. Les processus d’adsorption suivaient le modèle de Langmuir et les cinétiques chimiques d’adsorption étaient mieux adaptés à l’équation du pseudo-second ordre. Les conditions d’optimisation pour la mise en place du stripping sélectif à l’aide de solutions acidifiées de thiourée ont également été étudiées. En particulier, afin d’améliorer la réutilisation de ce matériau hybride, des processus de modification des surface en deux étapes ont été développés par fonctionnalisation de la surface de nano-ZrO2 avec de l’acide alendronique et par une réaction de couplage peptidique avec du TOA.De plus, les procédés de greffage de nano-ZrO2 sur un textile en polypropylène modifié avec les groupements carboxylique ont été étudiés via des méthodes traditionnelles de revêtement par immersion (dip-coating) et de revêtement couche par couche (LbL). Cette dernière s’est avérée être une méthode prometteuse en termes de flexibilité, de facilité de manipulation et de respect de l’environnment. Les nanocomposites obtenus ont démontré d’excellentes propriétés d’adsorption de Pd et d’Au / Secondary sources of precious metals, such as e-waste, have been recently gaining more attention thanks to raising awareness of natural resources depletion and sound impact of recycling industry on employment and economic growth. Recycling technologies have now to be developed, enabling extraction of very small concentration (10-100 ppm) of precious metals, such as palladium (Pd) and gold (Au), from effluents of recycling factories economically viable.In this context, our study addresses the use of thioctic surface-modified zirconia nanoparticles to capture efficiently and selectively Pd(II) and Au(III) ions from industrial electronic wastewater. The advantages of using the commercial thioctic acid (TOA) over dialkyldiglycoamide or (N,N)-dialkylcarbamoylmethylphosphonic acids ones in terms of adsorption capacity and selectivity were demonstrated. Batch-mode adsorption experiments combined with ICP-OES method were conducted and our findings have displayed adsorption capacities toward Pd and Au of 6.3 mg/g and 43.3 mg/g, respectively. The adsorption processes were found to follow the Langmuir model and adsorption rates were best-fitted to pseudo-second order equation. The optimization conditions for selective stripping set-up using acidified solutions of thiourea were also investigated. Particularly, in order to improve the reusability of this hybrid nanomaterial, two-step surface modification processes were developed through alendronic acid-surface functionalization of nano-ZrO2 and amide coupling reaction with TOA.Furthermore, the grafting processes of nano-ZrO2 onto carboxylic-modified polypropylene textile were studied via traditional dip-coating and layer-by-layer coating methods. It has been realized that layer-by-layer coating method is a promising method in terms of its flexibility, ease of handling, and environmental friendliness

This project was specifically aimed at using increased acceleration separation, as a method to optimize the recovery of gold in an ore body mainly consisting of hematite. The specific gravity of gold is much higher in comparison to the carrying material, making it possible to separate gold from other materials such as silica, base metals and their oxides, usually associated with gravitation–gold–recovery processes. The ore body investigated in this project originated from a mined gold reef containing a large proportion of gold locked inside the gold pyrite complexes. In the mine's processing plant a gold pyrite concentrate was produced by means of a flotation process. The roasting process that followed, oxidized the pyrite to iron oxide (hematite) and sulphur dioxide. The gold particles which were locked up inside the pyrite gold complex were exposed or liberated, allowing the chemicals to penetrate the complex and dissolve the gold. After the cyanide gold extraction process, the material was pumped on to a mine reserve dump, referred to as tailings or tailings reserve dump. The tailings usually contain iron oxides, free gold, gold associated with iron oxides and gold associated with silica, and free silica, commonly referred to as calcine. The gold content on the calcine dump was significantly lower than the flotation concentrate before the extraction of the gold and it was no longer viable for the mine to process the tailings further. As the volume of the mine reserve dump increased over the years, it became viable to recover the gold in a high volume low grade plant. Several attempts were made to recover the gold in this dump, but due to the high cost of processing and milling the material, it was not done. The norm in the mining industry is that it is impossible to concentrate the gold by means of gravity separation techniques where the average particle sizes are smaller than 50 um in diameter and upgrading with inexpensive gravity separation techniques was ruled out by the mine, because the average particle sizes were too small. The dump investigated in this project differed from other reserve dumps in that the main phase of material in this dump was hematite and not silica. A suspension of this material would have different fall–out properties than other mine reserve dumps, because of the hematite's high specific gravity compared to silica. This property of the material birthed the idea that the material will respond positively to high acceleration separation, although the particle sizes were too small for effective upgrading according to the norm in the mining industry. Using acceleration concentration as a first stage in the gold recovery process the production cost per gram of gold produced could be reduced significantly. Firstly, the volume of concentrated material to be treated in the chemical extraction process was reduced ninety percent and secondly, the gold concentration was increased significantly. If the gold could be concentrated to more than twenty grams of gold per ton, it could be extracted economically with an aggressive chemical processes. This was not possible with low grade material contained in the dump. The theoretical principle, on which this project was based, was to make use of high acceleration separation to establish separation between the particles associated with the gold, and the particles not associated with gold. Applying a high gravitational force would have an influence on the velocity by which the particles would fall–out in a suspension. As the acceleration force increased the fall–out velocity would also be increased and the particles with higher specific gravity would be affected more. A factor that was equally important was the particle size and weight distribution. A large hematite particle would compete with a small gold particle due to the similarity in weight. This could cause loss in small gold particles or retention of hematite particles with no gold content. Very little scientific information was available on the material investigated and in order to assemble a concentration plant setup, the head grade and particle size distribution for both the dump and bulk sample were determined accurately. Thereafter, chemical analyses and mineralogical examination were done on a representative sample of the bulk sample, determining the chemical composition of the material. The results obtained thereof were evaluated and used to configure a pilot plant. A large bulk sample was processed in the pilot plant and from the analytical results the efficiency could be evaluated. The results at optimum acceleration forces applied, resulted in a recovery of 5% of the mass, with a gold concentrate of 90 g/t Au, which represented 58% recovery of the gold. The hematite with high specific gravity as main phase positively influenced the high acceleration separation process. It proved that if the specific gravity of particles in a suspension were increased, high acceleration separation could be applied effectively to separate much smaller particle sizes. / Thesis (M.Sc. Engineering Sciences (Chemical and Minerals Engineering))--North-West University, Potchefstroom Campus, 2012.

This project was specifically aimed at using increased acceleration separation, as a method to optimize the recovery of gold in an ore body mainly consisting of hematite. The specific gravity of gold is much higher in comparison to the carrying material, making it possible to separate gold from other materials such as silica, base metals and their oxides, usually associated with gravitation–gold–recovery processes. The ore body investigated in this project originated from a mined gold reef containing a large proportion of gold locked inside the gold pyrite complexes. In the mine's processing plant a gold pyrite concentrate was produced by means of a flotation process. The roasting process that followed, oxidized the pyrite to iron oxide (hematite) and sulphur dioxide. The gold particles which were locked up inside the pyrite gold complex were exposed or liberated, allowing the chemicals to penetrate the complex and dissolve the gold. After the cyanide gold extraction process, the material was pumped on to a mine reserve dump, referred to as tailings or tailings reserve dump. The tailings usually contain iron oxides, free gold, gold associated with iron oxides and gold associated with silica, and free silica, commonly referred to as calcine. The gold content on the calcine dump was significantly lower than the flotation concentrate before the extraction of the gold and it was no longer viable for the mine to process the tailings further. As the volume of the mine reserve dump increased over the years, it became viable to recover the gold in a high volume low grade plant. Several attempts were made to recover the gold in this dump, but due to the high cost of processing and milling the material, it was not done. The norm in the mining industry is that it is impossible to concentrate the gold by means of gravity separation techniques where the average particle sizes are smaller than 50 um in diameter and upgrading with inexpensive gravity separation techniques was ruled out by the mine, because the average particle sizes were too small. The dump investigated in this project differed from other reserve dumps in that the main phase of material in this dump was hematite and not silica. A suspension of this material would have different fall–out properties than other mine reserve dumps, because of the hematite's high specific gravity compared to silica. This property of the material birthed the idea that the material will respond positively to high acceleration separation, although the particle sizes were too small for effective upgrading according to the norm in the mining industry. Using acceleration concentration as a first stage in the gold recovery process the production cost per gram of gold produced could be reduced significantly. Firstly, the volume of concentrated material to be treated in the chemical extraction process was reduced ninety percent and secondly, the gold concentration was increased significantly. If the gold could be concentrated to more than twenty grams of gold per ton, it could be extracted economically with an aggressive chemical processes. This was not possible with low grade material contained in the dump. The theoretical principle, on which this project was based, was to make use of high acceleration separation to establish separation between the particles associated with the gold, and the particles not associated with gold. Applying a high gravitational force would have an influence on the velocity by which the particles would fall–out in a suspension. As the acceleration force increased the fall–out velocity would also be increased and the particles with higher specific gravity would be affected more. A factor that was equally important was the particle size and weight distribution. A large hematite particle would compete with a small gold particle due to the similarity in weight. This could cause loss in small gold particles or retention of hematite particles with no gold content. Very little scientific information was available on the material investigated and in order to assemble a concentration plant setup, the head grade and particle size distribution for both the dump and bulk sample were determined accurately. Thereafter, chemical analyses and mineralogical examination were done on a representative sample of the bulk sample, determining the chemical composition of the material. The results obtained thereof were evaluated and used to configure a pilot plant. A large bulk sample was processed in the pilot plant and from the analytical results the efficiency could be evaluated. The results at optimum acceleration forces applied, resulted in a recovery of 5% of the mass, with a gold concentrate of 90 g/t Au, which represented 58% recovery of the gold. The hematite with high specific gravity as main phase positively influenced the high acceleration separation process. It proved that if the specific gravity of particles in a suspension were increased, high acceleration separation could be applied effectively to separate much smaller particle sizes. / Thesis (M.Sc. Engineering Sciences (Chemical and Minerals Engineering))--North-West University, Potchefstroom Campus, 2012.

M. Tech. (Department of Metallurgical Engineering, Faculty of Engineering and Technology), Vaal University of Technology. / Dust generated during comminution of end of life printed circuit boards (PCB), typically having d80 of 212 μm, contains copper and gold up to 6.32 % and 635 g/ton, respectively. The dust particles being highly diverse in material makeup, an hydrometallurgical processing scheme able to selectively recover target values was studied. Use of mineral acids will result in multiple metal dissolution which will complicate subsequent solution treatments. Detailed characterization of the dust was first carried out, and leaching scheme were thereafter investigated to selectively recover gold and copper from the dust, in three leaching stages. Different conditions of ammonia and thiourea leaching were investigated to optimize agitation speed, reagents concentration, temperature and leaching time. The leaching kinetics of these elements from the dust under different prevailing leaching conditions were studied. Elemental composition of the dust size fractions indicates metal contents generally increase with decreasing dust particle size, down to – 53 μm size, which contains up to 635 g/ton Au, 25.43 % Fe, and 1.40 % Cu, compared to 51 g/ton Au, 3.07 % Fe and 6.32 % Cu in the 150–212 μm fraction. Thermodynamically, under oxidative ammonia leaching, zinc and copper ammine complex is feasible, yet zinc recovery is low. For 75 – 106 μm dust size, 2 M NH4OH, 17.5 M H2O2, 1 atm. pressure and 400 rpm in Parr reactor, Cu and Zn recoveries were 92 % and 50 %, while the activation energies evaluated within 283 – 313 K gave 47.39 kJ/mol and 33.12 kJ/mol. The kinetic analysis for copper leaching gave best correlation coefficient (R2) of 0.9804 when fitted into the chemical control model, and the rate constant was 4.4 x 10-3 at 313 K. The presence of base metals frustrates direct gold recovery from the dust using thiourea with sulphuric acid and hydrogen peroxide. Therefore, the residue obtained from the first stage copper leach was acid washed to remove iron and other residual base metal contents with 5 M H2SO4, at 333 K, 400 rpm for 2 hours. Recovery analysis shows that about 75-98 % Fe, 54-65 % Zn and 96-98 % Ni were recovered under this condition while Cu was less than 7 % at all PSDs; copper having been selectively removed at the first stage. Using 75 – 106 μm dust fraction, gold recovery was optimum when the acid wash residue was leached with 0.5 M thiourea (SC(NH2)2), 0.5 M sulphuric acid (H2SO4), 0.1 M hydrogen peroxide (H2O2) under 1 atm. pressure, 298 K and 400 rpm for 4 hours. The recovery was 98 % Au. Using this optimum for other size fractions, over 98 % gold was recovered from 150–212 μm, 106 – 150 μm and 75 – 106 μm dust while 71 % and 68 % Au were recovered from 53 – 75 μm and – 53 μm respectively. The lower recovery at the finest sizes can be due to the quantity of the gold contents deported in this particle size, which will require higher reagent dosage. The kinetic analysis gave best correlation coefficient (R2) of 0.99 when fitted to the chemical control leaching model. From this data, a process flowsheet was proposed to give separate streams rich in copper and gold values from the processed dust, with detailed processing parameters. This is considered a readily scalable process solution for retrieving gold and copper from PCB dust.