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By Olaf Kessler, Jan Kalich, Michael Reich, Julia Osten, Uwe Füssel

Modern automobile bodies consist of different materials, e.g. aluminium alloys and high strength steels. Mechanical joining, e.g. clinching, is very suitable for joining aluminium and steel sheet. But clinching needs a sufficient ductility, which is no longer supplied by high strength steels. Laser-assisted clinching has been shown, to be able to join aluminium and high strength steel sheet successfully. Thereby the steel sheets were heated locally for short times to increase their ductility. Due to the thermal contact between steel and aluminium sheet the aluminium alloys also achieve a local short-time heat treatment. This fact may cause a significant impact, as aluminium sheet in automobile bodies is often used in T4 (or similar) condition and later artificially aged during the paint bake cycle. Aluminium alloys 6016 and 6181 have been short-time heat treated with heating rates up to some 100 K/s. Precipitation and dissolution processes have been monitored in-situ by calorimetry. Mechanical properties have been investigated on as well as after short-time heat treatment by deformation dilatometry. The results show, that suitable short-time annealing parameters during laser-assisted clinching can increase ductility and at the same time act as retrogression for aluminium sheets, resulting in increased strength after aging.

Jan 1, 2015

By S. Banisi, A. Haji-Zadeh, A. R. Hasankhoei, M. Maleki-Moghaddam

At the concentration plant of the Gol-E-Gohar Iron Ore Company (Iran) three 9m × 2.05m AG (Autogenous) mills (fixed speed) are used in parallel in a dry operation. The test works conducted in a scale down mill with a diameter of 1m indicated that conventionally used "deflector" type liners did not provide efficient environment for grinding. In this research, to improve the grinding efficiency, a new design using low profile end liners incorporating radial ribs of proper height was investigated. In order to determine an appropriate liner design at different operating conditions, a 100cm×10.8cm model mill was used for experimentation. The special design of model mill made it possible to increase the radial ribs height in steps of 6mm up to 18.5mm. The transparent end of the mill enabled accurate trajectory determination by image analysis. The results indicated that the new lower height profile deflectors and 15.5mm-height (14.5cm in industrial scale) radial ribs improved the mill performance while avoiding excessive pressure drop across the mill and wear on the liner. The image analysis showed that the use of new liners increased the distribution of coarse particles across the mill cross section from 28% to 35%. A new liner design was proposed by decreasing the number of liners in each slice from 5 to 4 pieces. The thickness of the inner head liners reduced from 45cm to 30cm and the outer deflector liners replaced by radial ribs. The distance between the feed and discharge inner head liners increased from the original 115cm to 145cm which increased the effective length of the mill by 26%. The new design reduced the weight and volume of end liners by 9% and 23%, respectively. It was predicted that the new liners design increases the mill throughput by 10% and reduces the metal consumption by 20%.

Jan 1, 2016

By Ausenco Engineering Canada

"This paper demonstrates the selection of grinding circuit technology for a number of recent projects including discussion of the key drivers and the role of energy efficiency. Decreasing head grades combined with a strong and sustained increase in operating costs has forced miners to examine increased project size, increased equipment capacity and efficiency improvements in order to reduce their unit operating costs and improve overall project economics. Comminution energy consumption, safety and capital cost considerations play a critical role in the success of projects. This paper presents some key guidelines for a successful and cost effective comminution circuit design and includes a case study on three projects, outlining the issues and the drivers which led to the ultimate circuit selection and the critical role that energy efficiency played.INTRODUCTIONComminution circuits for minerals processing are selected based on their suitability and efficiency in reducing run-of-mine ore to the desired feed size for the downstream process. The input material (ore) properties and downstream process requirements are the key determinants and there are standard approaches for each circumstance.The minerals processing industry has been a fast adaptor of efficiency improvements based on increasing capacity of equipment (e.g. trucks, crushers, mills, pumps) but less successful in adapting radically new technologies that disrupt incumbent flowsheets or processes.The installed power of grinding mills has increased linearly over the past 25 years (Meka & Lane, 2010) and pumps and classification equipment have kept pace. The autogenous grinding (AG) and semiautogenous grinding (SAG) mills displaced stage crushing as a dominant method of coarse rock breakage in many applications causing crusher manufactures to increase the capacity of cone crushers to meet the competitive demand.Examples of new comminution technology in the 20th and 21st centuries are the development and adoption of cyclone classification in the 1940s (Newtech, 2016), AG milling in the late 1950s, vertical grinding mills in the 1980s, high pressure grinding rolls (HPGRs) also in the 1980s and ultrafine milling technology in the 1990s (Meka & Lane, 2010)."

Jan 1, 2016

By S. J. Cook

The subject of capital and the Canadian mining industry is so broad as to be impossible of comprehensive treatment in brief form. The purpose of the present paper therefore will be only to outline in a meagre and somewhat sketchy way the nature and extent of the mineral industry in Canada and to point out those features which are likely to be of general public interest. Canada's mineral industry has a long and creditable production record. The? value of the output per capita rose from $2.23 in 1886 to a maximum of $26.40 in 1920 and the value of the products from ten million dollars in the former year to almost two hundred and twenty-eight million dollars in 1920. Compared with other primary industries and on the basis of the value of production, mining held third place in Canada in 1920, the premier position going to agriculture and the value of forestry production placing that industry second in the list. In the mineral industry, between six and seven thousand properties are operated annually giving employment to up- wards of sixty thousand employees to whom about seventy-five million dollars is paid in salaries and wages. During 1923, seventeen mineral products reached a production value of one million dollars or over in Canada and in order of the values assigned these were: coal, gold, nickel, cement, cop-per, silver, clay products, lead, asbestos, natural gas, stone, zinc, lime, cobalt, sand and gravel, gypsum and salt.

Jan 1, 1924

By Clifford S. Gibson

THESE troubled times suggest three reasons for maximum effort to control silicosis: (1) To keep to a minimum the ever-increasing burden occasioned by past deficiencies in this respect. (2) To effect the greatest production with maximum efficiency, which means at the least cost. (3) To preserve man-power in every way. Good control of the silicosis problem aids these aims. Inadequate control hampers all three. Insofar as our knowledge goes, silicosis in Ontario mines is caused by the inhalation of finely particulate quartz. It follows, therefore, that removal of dust containing this mineral automatically erases the cause. The achievement of this ideal is the aim of the mine operator. His best tool to this end is ventilation. This paper discusses mine ventilation from the viewpoint of dust control and it is hoped that in so doing there may result a better understanding of the part played by air in silicosis prevention. No attempt will be made to treat the subject fully. Instead, there will be presented certain salient aspects culled from field observations, the data in all cases referring to gold mines, unless mention to the contrary is made.

Jan 1, 1942

By H. R. Huffman

"This paper reviews the history of iron powder production, and outlines the varions production methods. The uses of iron powder and the reasons for its use are also covered. The paper concludes with a look at future trends in powder metallurgy.INTRODUCTION TO POWDERSTHE IRON POWDER INDUSTRY is enjoying a very rapid growth. The annual consumption of iron powder is now at the 100,000-ton level, twenty times higher than it was at the end of World War II, and the yearly in-crease bas been almost consistent at 20 per cent. This is expected to increase, bringing the tonnage to 200,-000, or even (according to some experts) to 270,000, in 1970. In any event, powder metallurgy is expanding at high speed and making an important impact on the production of iron and steel products. Some indication of the faith in the future market may be indicated by the commencement of three new powder production plants in Canada with a total capacity of 136,000 tons annually."

Jan 1, 1969

By J. E. Dutrizac

"The end of an era in zinc metallurgy took place on July 31, 1976 when the horizontal retort furnaces of the National Zinc Company in Bartlesville, Oklahoma were permanently shut down (1) . For more than a century, horizontal retorting had been the most common method of producing zinc in the United States; it was a thriving industry in many parts of that country, especially in the natural gas belts of Oklahoma and Texas. With the Bartlesville closure, yet another metallurgical process has become an object of historical interest for North American metallurgists. Although shrouded in controversy, the origins of zinc metallurgy seem to date back at least 2000 years. Pyrometallurgical methods with carbon reductants are capable of producing zinc from oxidic zinc ores, but only above the boiling point of the metal. Although slow cooling results in re-oxidation of the zinc vapour by air or carbon monoxide, quenching yields liquid zinc; some form of rapid cooling, either accidental or intentional, was likely used by ancient metallurgists to liquify the metal. Zinc metal found in Athenian objects of the Roman era was likely of accidental origin. The Romans employed brass extensively for coins and ornaments(2) , and this was intentionally produced by the calamine process whereby oxidic zinc ores were added to molten copper under strongly reducing conditions. Zinc appears to have been known in China and India as early as 1000-1300 A.D., and was probably smelted commercially in those countries from the 14th century. Although the early metallurgical procedures were probably inefficient, they were able to produce zinc metal in significant amounts. The large heaps of zinc residues with clay retorts bear testimony to an early smelting industry of impressive magnitude. It is estimated that the heaps at Zawar, India alone represent the extraction of 100 000 tons of metallic zinc(2) In the 1730s the smelting of oxidic zinc ores was developed in England using a vertical retort method. In 1788 a British patent was granted for making zinc from zinc blends (ZnS) by roasting the ore in a coalfired reverberatory furnace, mixing the calcine with charcoal and smelting the mixture with suitable zinc condensation. The English process was very energy intensive, however, and early in the 19th century the Belgians developed a horizontal retort process for the reductiondistillation of zinc that was more fuel efficient. This technique was gradually developed into what came to be known as the Belgian process, the forerunner of the ""modern"" horizontal retort furnace."

Jan 1, 1999

By Marcel Labbé

La largeur de l?armature peut être modifiée selon les besoins du client entre 48 " et 64" de largeur totale, donc 2 sections de 24" à 32". Ceci permet à l?opérateur d?effectuer le démantèlement de l?équipement pour le déplacement dans les endroits restreints. Le déménagement d?un niveau à un sous-niveau devrait se faire dans un quart de travail de 8 heures. L?option de largeur permet au client de choisir un équipement adapté à son environnement de travail (1). La largeur de la table de forage peut être modifiée selon les besoins du client entre 48" et 96". Cette particularité permet une meilleure stabilité, et plus de précision dans le forage (2). Il y a 4 pattes hydrauliques à chaque coin pour la stabilisation lors de forage (3). La table de forage a 360° d?angle de forage sur 3 côtés du transporteur. La table peut sortir de chaque côté du transporteur de 40 ½" à partir du centre du transporteur pour faciliter la mise en place de la foreuse dans les endroits difficiles d?accès. La plage de forage est considérablement agrandie. Cette caractéristique qui fonctionne hydraulique, permet à l?opérateur de forer sans être obligé de changer la position du transporteur pour des changements de trous. Tous les types de foreuse peuvent être installés sur cette table de forage (4). Sa petite dimension lui permet d?accéder, par des monteries de 30" de diamètre, à des sites de travail de 2,5 mètres de hauteur et largeur. C?est un équipement adapté aux gisements filoniens. Ce genre de gisement est de moins en moins rentable pour les compagnies minières. La mécanisation des ces gisements va permettre de les rentabilisés en augmentant la productivité et la santé du travailleur, en réduisant la dilution (5). Les manettes de contrôle de la foreuse, les mouvements de la table de forage ainsi que le déplacement du transporteur ont été installés selon les recommandations d?un ergonome. Des recherches ont été effectuées par ce spécialiste sur les cas d?accident survenus avec l?utilisation de ce genre d?équipement. Il a déterminé les positions le plus confortable que l?opérateur doit prendre pour éviter les douleurs prolongées (6). Le système de roulement est composé de 4 roues pleines installées sur 4 planétaires de 9000 à 15000 livres de capacité munis chacun d?un moteur hydraulique. Des freins ont été installés sur les planétaires pour assurer la sécurité de l?opérateur et faciliter le positionnement du transporteur lors du forage. Des roues rétractables peuvent être installées pour faciliter l?accès sur rail (7). Ce transporteur peut être alimenté par une puissance électrique plutôt que par une puissance pneumatique. Cette puissance électrique est fournie par un Power Pack qui transforme l?énergie en puissance hydraulique. Ce type d?alimentation est employé lors du forage de développement, mais il peut aussi être utilisé pour le forage long trou. Cet avantage permet au client qui a un problème de pression d?air d?utiliser l?électricité. Par contre si vous utilisez l?électricité mais que dans un secteur isolé le gros courant électrique n?est pas accessible vous pouvez utiliser votre équipement en utilisant la puissance pneumatique. Le changement d?alimentation énergétique se fait facilement (8). Cet équipement est construit pour effectuer 4 types d?activités : forage de développement de niveau et sousniveau avec l?installation d?un bras porteur, forage et pose de câbles d?encrage pour soutènement de terrain, forage de production long trou et forage de monterie ascendante et descendante. L?avantage est que vous investissez dans un seul équipement au lieu de 2 ou 3. Cet avantage vous fait économiser dans votre budget d?équipement. En plus cet équipement est construit pour de dure travaux et ne contient aucun système électronique (9).

May 1, 2001

By Gordon S. Farnham

THIS paper summarizes the results of investigations carried out at Sydney Mines, N.S., and at Ottawa, following the disaster at Princess colliery, December 6th, 1938. The Honourable Minister of Mines for Nova Scotia appointed A. E. Cameron special investigator to enquire into and report upon the cause of the rope failure. Public hearings were held in Sydney Mines and evidence taken from many witnesses. The site of the accident was examined in detail and investigations made of the rope layout and colliery practice. At the request of the special investigator, the Department of Mines and Resources, Ottawa, kindly undertook technical and scientific examination of the broken ends of the rope. These investigations were carried out in the Metallurgical Laboratories of the Department of Mines and Resources, under the supervision of G. S. Farnham, Metallurgist for the Department. Valuable assistance in interpretation of many features of the investigation was received from other sources. Acknowledgment is due to Messrs. Stuewe, McCall, and Gordon, and other members of the staff of the Dominion Steel & Coal Corporation; to Messrs. Morrison and Scott, and other members of District 26, United Mine Workers of America; and to Messrs. Timm, Parsons, Haycock, Haanell, and other members of the staff of the Department of Mines and Resources, Ottawa, for helpful ad vice and technical assistance in assembly of information, and preparation of material and interpretation of evidence obtained.

Jan 1, 1939

By W. Curlook, V. G. Papangelakis, M. Baghalha

A pressure acid leaching process has been developed for the extraction of metal values, nickel, copper, cobalt and zinc, from base metal smelter slags. The basic concept contemplates cooling the smelter slags through solidification sufficiently slowly to induce a good measure of crystallization; and subsequently, after fine grinding, to pressure leach such slags at around 250°C while applying oxygen overpressure, utilizing smelter byproduct sulphuric acid. High levels of extraction of the slags' metal values are thereby achieved. It has been shown that if the same slags are quenched thereby producing an amorphous structure, the resulting metal extractions are very low. The process is applicable to smelting furnace throwaway/discard/dump slags, as well as to in-process converter slags. By extracting the bulk of the residual base metal values in the throwaway/discard/dump slags, the resulting leached residues are rendered virtually benign vis-à-vis the external environment.

Jan 1, 2004

By J. W. Baker

"The Kerr-Addison mine is on the northeast shore of Larder Lake in the township of McGarry, District of Timiskaming, Ontario. It lies just south of the highway leading to the town of Kirkland Lake, 25 miles to the west.The property was first staked in the summer of 1906, by a party of prospectors led by a Dr. Reddick of Ottawa. Subsequent assessment work resulted in the erection of a 20-stamp mill in 1908. Gold from this mill was used in the first gold coins to be minted in Canada. The operation did not prove successful, however, and mining was suspended. In 1914 a consider-able amount of underground development was undertaken by the Associated Goldfields Co., without success.In 1936 Kerr-Addison Gold Mines Co. carried out large-scale sampling from four adits driven into the hillside at the mine. Results were not satisfactory, but it was decided to drill one last deep diamond drill hole from surface. The hole cut a wide section of gold ore. With this encouragement, further development outlined a large tonnage of ore, and a 500-ton mill was put into production in May, 1938. In 1939, its first full year, the mine produced 54,480 ounces of gold and 2,732 ounces of silver. By 1955 the mill had been expanded to a rate of 4,549 tons daily, and in this year 427,193 ounces of gold and 23,490 ounces of silver were produced.From 1938 to the end of 1955 the total production, from 17,473,797 tons milled, has been 3,607,462.74 ounces of gold (0.2064 ounces per ton), and 182,278.56 ounces of silver, with a total value of $131,073,037."

Jan 1, 1949

By Z. D. Hora

The major fluorite producer in British Columbia was the Rock Candy Mine, inactive since 1942. Other deposits of economic interest include the Rexspar deposit, in which fluorite is associated with uranium and rare earth mineralization, and the Eaglet and Liard River occurrences. THE former Rock Candy fluorite mine, located 26 km north of Grand Forks, is the only major past producer of fluorite in British Columbia. The deposit was in production from 1918 to 1929 and again in 1942; total output was about 36,000 tonnes with average grade between 22 and 32 per cent CaF2. The fluorite body occupies a steeply-dipping vein structure, approximately 175 m long and up to 12 m wide, in porphyritic syenite. The chief vein-filling minerals are quartz and fluorite with local small len ses of barite. Fluorite content decreases with depth and the deposit becomes silicified. The Rexspar (or Birch Island) fluorite deposit is located 130 km north of Kamloops. The deposit is complex with rare earth elements and high uranium values, but !1uorite mineralization forms an independent zone adjacent to the uranium orebodies. Fluorite is present as fine-grained impregnations and as breccia cement in strongly schistose or brecciated alkali feld spar porphyry. Reported reserves are 1,088,000 tonnes of 22 per cent CaF2 or 450,000 tonnes of 29 per cent CaF2. 268 Another potential deposit of fluorite is Eaglet, situated on the north side of Quesnel Lake. Fluorite occurs as a stock work with scattered veins and irregular lenses up to 20 centimetres wide and as impregnations in altered Proterozoic Kaza Group feld spathic gneiss over an area of 1,500 metres by 500 metres. To date (1983) approximately $2 million have been spent on the exploration of this property and reserves of 18.8 mimon tonnes grading 11.59 per cent CaF2 have been outlined . A group of significant occurrences is known from north of Liard River Hot Springs Park , where fluorite occurs in small zones up to 17 m thick along the interface between Middle Devonian Dunedin Formation limestone and Middle Devonian to Mississippian Besa River Formation argillite. Fluorite, associated with witherite, barytocalcite and barite, is present as replacement bodies, breccia fillings and minor veins.

Jan 1, 1984

By Imre Gombköto, Barnabás Csoke

"Raw material management means not only mining and processing of primary raw materials like ores, but means also collecting and processing secondary sources of raw materials. Recycling is one of the most developing field of raw material management in Europe, and its solutions are derived from mineral processing roots and principals. Complexity and challenges of the field of recycling results innovative solutions of material processing- Since European Union identified 20 raw materials as critical (CRM) due to lack of primary sources within the border of the EU, recycling become more recognised as source of different raw materials. WEEE is the waste streams contains many of the critical elements and along them at least 15 different species of plastics of which recycling is delayed by a lack of effective separation technique. Most paper deals with separation methods based on different specific gravity, triboelectric charge or surface properties of plastic species. Plastics however have differences of thermal properties and thermoplastics, duroplasts and elastomers can be recognised. The experiments described in the paper aimed to determine thermo adhesive behaviour of plastic species often identified in WEEE streams for separation purposes. According to the results, some plastic types as PS, PP. PC or PVC and PET pairs are possible to easily separate from each other, however different additives are changing thermo adhesive properties of most of the plastics that makes industrial process difficult to develop. Along thermo adhesive behaviour, combination of physical interaction can be used to enhance separation selectivity.INTRODUCTIONPlastics has a relatively long term of history as a light, multi-functional material in construction, packaging, automotive industry and electric and electronic products. There are a numerous types of plastic species can be used for various applications therefore they amount are growing from year to year. This quantity however become part of the waste stream and while metal recycling has been done for decades due to its economic value - cheap plastic parts are less desirable as secondary products. In 2013 an annual 5% of plastic production growth has been estimated with a base data of 265 million tonnes at 2010 (Guiqing & Zhenming, 2013). Since landfill requirements are increasing while—especially in Europe where actual regulations are trying to deflect waste from landfills - landfill capacities are decreasing, costs are become more and more expensive, Applications like energy production based on plastics as a fuel or recycling are some of the options can be applied. Direct incineration of plastics are applied at many plants - in most cases where waste consist of dangerous substances are incinerated because plastics high calorific value helps correct average mixture composition enable operators reaching high enough temperature for combined power and heat generation while most of substances—like PAH, PCB or dioxins—are destroyed. Another path is using low temperature reductive cracking due to pyrolysis process, however the chance having higher concentrate of carcinogen substances in the products are higher since it applies around 400°C during the process."

Jan 1, 2016

By M. Krasowska, K. Malysa, M. Krzan

The paper presents fascinating, in our opinion, observations on mechanism and course of processes occurring during bubble collision with hydrophobic and hydrophilic solid surface. Hydrophobicity of particle surface is a necessary condition for the particle attachment to bubble. We have observed that even in the case of such hydrophobic solid surface as Teflon, the bubble attachment didn't occur at first collision. In distilled water the bubble bounced a few times without attachment. Influence of a-terpineol and n¬pentanol on bubble local and terminal velocity and the phenomena occurring during bubble collisions with hydrophobic and hydrophilic solid surfaces was studied. Bubble collisions with the solid surfaces were monitored and recorded using the high-speed (1182 frames per second) camera. It was found that in distilled water the velocity variations of the "approach-bounce" cycles were identical for Teflon and glass. Four distinct "approach-bounce" cycles were detected both at Teflon and glass surfaces. Moreover, the amplitude and frequency of the velocity variations were identical on collisions with the hydrophobic (polished) and hydrophilic surface. There was no immediate three phase contact formation, with the hydrophobic Teflon surface, what we found really astonishing. Roughness of Teflon surface seems to be important parameter, which affects probability of the bubble attachment as a result of a presence of micro-and/or nano-bubbles at the surface. It was detected that the presence of the micro-bubble affected attachment of the colliding bubble even in distilled water. Presence of a small amount of a-terpineol or n-pentanol affects dramatically the bubble velocity, but their role in mechanism of the bubble attachment needs further study.

Jan 1, 2004

By S. k. Kim, H. B. Trinh, R. R. Srivastava

"Spent auto-catalyst is a promising secondary resource of platinum group metals (PGMs), which are being extensively used in automobiles catalytic converters to control the hazardous gaseous emissions (CO, NOx and hydrocarbons). Several pyro or hydrometallurgical routes has been employed to recover PGMs from such spent materials but there is no proper process for recovering the other constituents metals. Therefore, it causes the loss of other major constituents like, Al and Mg along with rare earth metal Ce. In the present study, we investigate the dissolution of Al and Mg using sodium hydroxide (NaOH) roasting followed by a sulfuric acid (H2SO4) leaching; thereby concentrating the PGMs and Ce in leached residues. The effect of roasting temperature, time and amount of NaOH were varied. Subsequently, the dissolution behavior of metals in H2SO4 as a function of acid concentration was investigated from the roasted samples. At an optimal condition for roasting at 600°C with 1:1 NaOH-to-catalyst ratio and 60 min duration, the maximum of Al and Mg were dissolved in 1 M H2SO4 solution at ambient temperature (~25°C). Thus obtained leached residues containing enriched PGMs and Ce content can be treated separately for the recovery of these high-value metals.INTRODUCTION Spent auto-catalyst has been considered as a potential resource for recovering the platinum group metals (PGMs) (Jha et al., 2013). The commonly used auto-catalyst is made of cordierite (2MgO.2Al2O3.5SiO2) in which the chloro complexes of PGMs are impregnated onto the surfaces of porous washcoat of alumina substrate (Aberasturi et al., 2011). The average concentration of PGMs in ore are 2-4 g/ton for Pt, 7-2 g/ton for Pd and 0.2-0.5 g/ton for Rh, whereas, an individual catalytic converter weighing about 1 - 2 kg contains on average 1.56 g Pt, 0.62 g Pd and 0.156 g Rh (Upadhyay et al., 2013). Moreover, recovery of PGMs from spent auto-catalyst offers other advantages like, simple process, low cost and less pollution, as compared to recovery from primary resources (Dong et al., 2015).Therefore, technologies to recover PGMs from spent auto-catalyst has become attractive in the recent past and their recycling contribution has been accounted for 35% Pt, 26% Pd and 36% Rh of the quantity consumed in the production of auto-catalysts (Johnson Matthey, 2016)."

Jan 1, 2017

By Michael Klichowicz, Holger Lieberwirth

"For a detailed prognosis of mineral comminution processes, simulation tools like DEM still pose various challenges. Less realistic mineral structures can affect the results of simulation models such as bonded-particle models (BPM). Hence, in order to design mineral processes with these models as tools, representative mineral input data should be used. The article shows, how realistic 2D-structures can be modelled by taking advantage of the parameters identified by the Quantitative Mineralogical Analysis (QMA). Important quantitative parameters can be derived by analyzing three orthogonal thin or polished sections. For this reason point, line, and area analysis are applied. The mentioned parameters precisely describe the texture and structure of minerals. The newly developed software is able for the first time to semi-automatically analyze images of mineral structures using QMA. Moreover, statistically equivalent structures of minerals can be modelled using the QMA- parameters. Generating synthetic, but equivalent mineral structures opens the door for more reliable BPM based simulations. Within future research, the procedure will be adopted to generate 3D-structures. Therefore, QMA-based routines that already have been applied to generate 2D-models shall be utilized as basis. The aim of this procedure is to synthesize realistic microstructures based on certain statistical figures in order to improve comminution simulations.INTRODUCTION Due to its increasing capability, the use of computer technology is permanently intensifying in the design of mineral processes. The recent past has impressively shown that computer models can enhance the understanding of mineral processing. There is in fact a rising number of research activities, which are using simulation approaches to study various aspects of it. Weerasekara et al. (2013) give a comprehensive overview over the application of discrete element modelling (DEM) in the science of comminution.Nonetheless, using simulation tools such as DEM in general still poses a challenge. For a detailed simulation of a mineral comminution process with DEM, bonded particle models (BPM) appeared suitable in the past. The following issues, however, affect an appropriate prediction when modelling with BPM:• Simulations with high numbers of particles may need a lot of time for computation. • Internal modeling parameters like the spring and damper constants in DEM have to be adjusted by comparing its specific crushing behavior in the simulation to reality.• In order to use DEM for prediction of mineral processing, it is essential to validate the correctness of the models and assumptions, which is sometimes difficult. As Weerasekara et al. (2013) have stated it is crucial that the DEM method as well as the DEM code work properly.• It is challenging to implement the complex geometric structures of real minerals into the model."

Jan 1, 2016

By A. Y. Senchenko, Y. V. Kulikov

"Different methods aiming at specific energy calculation and design of AG/SAG circuits are used in mining. They include JK DWT/SMC test, SAGDesign test and CWi/RWi/BWi tests. The simplest methods with no secret equations and giving energy required for grinding in kWh/t were proposed by F.?. Bond and J.H. Starkey. D.J. Barratt proposed to use results of CWi/RWi/BWi tests for AG/SAG mill sizing. The present paper gives an alternative for forecast of specific AG/SAG energy. The principle is similar to the theory proposed earlier and consists in cumulative AG/SAG energy calculation using indices of rod and ball grinding (RWi+BWi) without impact crushing index (CWi). Then total energy is divided between two grinding stages using special formulas based on extensive statistical information. The forecast indices of AG/SAG and ball grinding are similar to the SAGDesign testing results. Hereinafter the predicted indices are used for mill sizing of the whole grinding circuit. The method considered in the paper enables prediction of AG/SAG energy based on the test results according to Bond method. The proposed method version was not widely published earlier. The aim of the work was to elaborate cost-effective, reliable and accessible way to determine specific AG/SAG energy. At this stage of method development, it is recommended to use it only for works at preliminary Geometallurgy stage (Scoping, Pre-Feasibility). At design stage the obtained data should be confirmed by appropriate testing using alternative JK DWT/SMC and SAGDesign methods.INTRODUCTIONAppropriate crushing and grinding testing is required to design efficient comminution circuits. It is obviously important to obtain accurate information about ore hardness properties since the main energy consumption at the plant is associated with comminution processes. Moreover, it is required to apply the processes that make it possible to minimize operating costs and efficiently use capacity of the installed equipment installed.When studying ore hardness properties, it is required to take into account that breakage of the material is performed using different equipment. That is why accurate selection of the equipment and the circuit calculation without relevant testworks is impossible. Ideally, the testworks should provide answers to the following questions: determination of ore hardness properties, determination of specific energy consumption for comminution as well as obtaining of sufficient amount of statistically significant results from the tests. The results from crushability and grindability testworks in the first place provide assessment of ore hardness properties and in addition correlate with throughput of the respective equipment. The data obtained can be used for modeling of comminution circuits at the stage of the technology development"

Jan 1, 2016

By M. R. Khalesi, S. Bellec, C. Bazin, D. Hodouin

This paper proposes a classification model to predict the split coefficient of gold ore particles as a function of the particle size and gold content. The model is calibrated and validated using data obtained from the sampling of an industrial grinding circuit. Model calibration is based on a complete simulation of the circuit and involves parameters related to the gold grain distribution in the ore as well as a grinding and liberation model. Since cyanide is added into the studied grinding circuit, assumptions related to gold dissolution in the mills are made to allow simulation results which reflect industrial behaviour patterns.

Jan 1, 2011

By S. A. Luciani

"In 1957, an asbestos orebody was discovered in the northern sector of the Ungava Peninsula of the Province of Quebec, an area now identified as Asbestos Hill. The deposit is situated on a plateau 1700 feet above sea level and 42 miles inland from Hudson Strait. It is a bleak, iso. lated location of typical arctic environment. Fifteen years were to pass before the first shipment of ungraded fibre was made in 1972. These years we1•e occupied with field surveys and investigations, diamond drilling, engineering design, evaluation of investment and operating costs, and construction. The problems normally associated with mine development were further complicated by location, isolation, and the extreme cold and permanently frozen ground of the arctic regions. Unique to an isolated arctic operation are the organization of support facilities and services, procurement and retention of personnel, construction of access roads and airports, and scheduling of product out and supplies in during the short summer period of sea navigation."

Jan 1, 1976

By E. S. Moore

DEEP oxidation and-secondary enrichment of ore deposits, although so important in many parts of the world, are comparatively rare in the Canadian shield. Intensive glaciation during the Pleistocene epoch accounts for their rarity. Glaciation has cost Canada much in the destruction of not only enriched ore deposits, but placers that must have been developed near our numerous gold deposits during the long period of weathering that pre-ceded the Pleistocene. There seems to be a very common misconception regarding the average depth of rock that has been removed from the shield by glaciers. These bodies of ice are usually given credit for the removal of the greater portion of the thousands of feet of rock that we know has been eroded from this large area since Precambrian time. As a matter of fact, the average thickness of solid rock removed can be measured in tens rather than even hundreds of feet, although very deep erosion has resulted in some sections where the glacial ice has been constricted in depressions, such as deep valleys and lake basins. On the other hand, there are few areas within the shield where the glaciers have not disturbed practically all of the mantle rock and some feet of the underlying bed-rock. The chances of finding deeply oxidized cappings and enriched ore deposits are therefore comparatively few and these have been found chiefly where favourable structural and topographic conditions for their formation and preservation have existed. Faulting has been responsible for several of these deposits, and easily decomposed rocks, such as. sulphides and carbonates, have been very important factors. Topographic features, such as high and resistant hills, favourably situated with respect to the ore deposits have, in a few cases, played a part in providing protection from glacial erosion and in furnishing head for the descent of surface waters. At least four cases of oxidation to depths quite abnormal in the Canadian shield have so far been found in Ontario. These are the Helen and Josephine iron mines in the Michipicoten district, the Keeley silver mine in South Lor-rain, and the Ross gold mine in Hislop township, Cochrane district. A deeply oxidized zinc deposit of unusual interest occurs in the Precambrian rocks in New York State, not far from the Canadian border, and there arc the well-known iron deposits in the Lake Superior region of the United States.

Jan 1, 1938