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By Steve Simard

Suite aux excellents résultats, obtenus avec la technologie des détonateurs électroniques dans des chantiers longs trous de grandes dimensions, nous avons décidé d?étendre cette technologie dans les ouvertures, dans le dynamitage de piliers et dans différents chantiers complexes. Cette technologie nous a permis d?effectuer l?abatage de chantiers avec un très grand nombre de trous sans détériorer le terrain. L?équation est bien simple avec les détonateurs électroniques, plus gros sont les dynamitages moins de fois les épontes se font ébranler, moins de blocs d?effondrement se retrouvent dans les points de soutirages entre les dynamitages et plus la fragmentation est meilleure. La flexibilité d?opération que nous avons obtenu avec les détonateurs électroniques est difficilement quantifiable, mais elle nous a permis de maintenir notre rythme de production mensuelle même avec certains chantiers complexes. Il est bien certain que l?utilisation des détonateurs conventionnels a encore sa place dans une mine conventionnelle comme Beaufor, mais l?utilisation des détonateurs électroniques a aussi sa place dans certaines situations spéciales. Pour terminer, bien que la technologie des détonateurs électroniques soit encore dispendieuse, nous pensons encore l?utiliser pour optimiser certains dynamitages et ainsi maintenir notre flexibilité d?opération.

Oct 1, 2004

By J. Seidel

In 2009 Newmont Mining Corporation’s annual global spend on grinding media reached $94M USD, having doubled in the five years since 2004. The major contributing factor to the spend escalation during this period was unit consumable price, with total media consumption also rising as a function of annual ore tonnes milled. In an effort to better understand and manage the growth of this expenditure a significant supply chain management program was implemented. This was complemented by a series of technical initiatives focussed on grinding media specifications, quality management and the prediction of grinding media wear rate as a function of physical ore characteristics. This paper discusses the methodology and outcomes of these activities.

Jan 1, 2012

By R. G. Bradburn

"Brenda Mines Limited is a low grade open pit mining and milling operation located near Peachland, British Columbia. The mill was brought into production in late 1969 at a rated capacity of 24,000 tons per day. Tt currently treats an average of 30,000 tons per day of an ore that has an average grade of 0.130% copper and 0.030% molybdenum.Description of Crushing and Grinding CircuitsRun of mine ore is delivered to a primary gyratory crusher. The minus seven inch product is separated into plus and minus one inch fractions on two parallel vibrating screens. The fine product is conveyed directly to the mill fine ore bins, while the coarse fraction is sent to a 45,000 ton stockpile.Material from the stockpile is fed to two standard cone crushers which operate in an open circuit with five secondary vibrating screens. The minus five-eighth inch product from these screens is conveyed to the mill fine ore bins while the coarse fraction is fed to four shorthead cone crushers. These crushers operate in closed circuit with the screens."

Jan 1, 1981

By R. J. Chase, C. Davies

"The Merelani graphite-tanzanite deposit is located in northeast Tanzania, 14 kilometers south of Kilimajaro International Airport and in close proximity to the towns of Moshi and Arusha. The graphite mineralization is hosted by relatively undeformed linear Proterozoic metasedimentary gneisses, several of which have been subjected to hydrothermal alteration resulting in tanzanite mineralization. Exploration work comprised detailed geological mapping coupled with pit and trench channel sampling and a subsequent 1500 meters of diamond drilling. In addition, metallurgical tests have shown the graphite to be of unusually coarse flake size, crystallinity and high purity.Feasability studies have shown the economic viability of a major coarse flake graphite deposit with the measured resource to 50 meters in excess of 9 million tonnes assaying over 85 graphitic carbon. Production is due to start by the end of the first quarter of 1994 with the processing plant design capacity initially set at 15 000 tonnes per annum.In addition to graphite production, tanzanite will be produced through selective mining within the graphite open pit in the upper horizon and from underground workings within the lower horizon.The Merelani graphite-tanzanite deposit will be the first major orebody to be exploited through means of private funding since Tanzania gained independence"

Jan 1, 1994

By Bernard Vigneault

Les critères de qualité de l?eau pour les métaux visant à protéger la vie aquatique sont présentement basés sur les concentrations totales. Cependant, la complexation (association de ces métaux avec des ligands en solution) peut diminuer de façon importante la toxicité des métaux sur les organismes aquatiques. Pour évaluer l?importance de la complexation pour diminuer la toxicité des métaux dans les effluents miniers et métallurgiques, nous avons étudié la spéciation des métaux et la toxicité chronique de différents effluents miniers et métallurgiques. La phase dissoute des effluents a été échantillonnée à l?aide de la dialyse in situ et la spéciation du cuivre, du zinc et du cadmium a été calculée à l?aide du modèle d?équilibre chimique WHAM. Les concentrations de métaux libres ont également été mesurées à l?aide d?une technique d?échange ionique. Les concentrations de métaux libres calculés et mesurés indiquent que la complexation est importante dans les effluents miniers, particulièrement pour le Cu. Pour relier la spéciation des métaux et la toxicité chronique, nous avons mesuré en parallèle l?inhibition de croissance de l?algue Selenastrum capricornutum et des larves du poisson Pimephales promelas de même que l?inhibition de la reproduction du cladocère Ceriodaphnia dubia. (tests de toxicité chronique inclus dans le programme de suivi des effets environnementaux du règlement fédéral sur les effluents de mines de métaux). En absence de thiosels, aucune mortalité a été observée pour l?ensemble de ces tests et il n?y a pas eu également d?inhibition la croissance de la larve de poisson P. promelas. L?inhibition de la croissance de l?algue S. capricornutum, n?est pas reliée aux concentrations de métaux traces mais plutôt par aux concentrations de calcium. Les inhibitions de la reproduction du cladocère C. dubia sont reliées aux concentrations de métaux dissoutes et libres et non pas aux concentrations totales de métaux, démontrant l?importance des effets de la spéciation chimique sur la toxicité des métaux. Nos résultats indiquent que l?inhibition de la croissance de l?algue l?algue S. capricornutum est due aux concentrations élevées de calcium retrouvées dans les effluents miniers et que les concentrations totales de métaux ne peuvent être utilisées pour prédire la toxicité chronique vis à vis le cladocère C. dubia.

Nov 1, 2002

By Anne-Laure Bonnet

Les connaissances acquises au cours des dernières décennies sur les gîtes de métaux de base et précieux intensément métamorphisés (p. ex. Vokes, 1991; Cornell et al., 1992; Zaleski et Peterson, 1995) ont permis d?élaborer des guides d?exploration pour de tels gisements dans les terrains de haut-grade métamorphique (Spry et Scott, 1986; Rubin et al., 1993; Hand et al., 1994; Spry, 2000; Spry et al., 2000). Un transfert de ces connaissances à la cartographie des vastes terrains gneissiques non différentiés de la province de Grenville permet d?affiner l?approche cartographique nécessaire pour reconnaître les systèmes hydrothermaux métamorphisés en terrains vierges et peu diagnostiques puis d?en discriminer les divers halos d?altération (Corriveau et al.,1996, 1997, 1998, 2003; Williamson et al., ce volume). Cette approche prend en compte les « empreintes métamorphiques » observées sur le terrain, telles que les variations des assemblages minéralogiques, du mode et de la composition des minéraux métamorphiques, pour reconnaître des roches présentant une composition inhabituelle caractéristiques de protolites altérés par hydrothermalisme. Ces empreintes citées cidessus sont facilement reconnaissables dans les terrains de haut-grade où la recristallisation induit un grossissement des grains qui permet de déterminer la nature et le mode des minéraux dès les levés de terrain. Cette approche raffine la compréhension des terrains de haut-grade métamorphique et illustre que leur complexité (i.e. polyphasage de la déformation et du métamorphisme) n?est pas forcément une limite à leur exploration. Elle a donc été utilisée systématiquement lors des levés de terrain réalisés dans le cadre d?un projet de l?Initiative géoscientifique ciblée de RNCan. La zone cartographiée se situe le long de la marge sudest du Groupe de Wakeham dans le secteur est de la Province de Grenville. Deux régions ont été plus particulièrement étudiées, celle du lac Musquaro (SNRC 12K10, 11 et 14) et la région côtière comprise entre Kégashka, La Romaine et Baie des Loups (SNRC 12K1, 2, 3 et 7) (fig. 1).

May 1, 2003

By H. J. Chalmers

"Since the advent of large volume flotation machines, Cominco Ltd. has actively studied possible application of such machines to their various milling operations. A number of installations have been made and more are on the drawing board. This paper gives a description of these units, information as to choice of equipment, and information as to operating experience. Mechanical and operating details of six installations are summarized. Three different types of machines are discussed.Pine PointThe original Pine Point zinc flotation circuit comprised conventional roughing with two stages of cleaning. Over the years with increase in feed tonnage there have developed two adverse conditions; namely, a reduction in zinc concentrate grade coupled with an increase in MgO in the concentrate. This resulted in higher freight payments along with more severe smelter penalties. An intensive test program, in 1971, showed that the concentrate grade could be raised by 1.5 units of zinc along with a reduction in MgO from 0.8% to 0.47.. Subsequently this was done by adding two additional stages of cleaning using 16 cells of Denver 200-V's. The project was completed in January 1973 at a cost of $510,000 to give an estimated annual savings of about $390,000.Selection of the Denver Model 200-V was based on minimum floor space requirement, availability, and favourable operational and maintenance experience with Denver 100’s. As it happens it was possible to ""shoe-horn"" the 16 cells into place with a minimum of plant alteration. Some problems have been encountered with a tendency to ""sand up"" at high pH, particularly at the corners. Otherwise operational service has been very good."

Jan 1, 1974

By Akira Miura, Katsuyuki Sato, Yuken Fukano

JX Nippon Mining and Metals Corporation has developed the JX Iodine Process, which is an innovative and patented copper-leaching process for low-grade primary sulfide ores. This process consists of the irrigation of ferric iron and a low concentration of iodide solutions. One-meter column leaching tests were conducted on ore samples from two different mines. At the end of experiments, the total copper recovery exceeded 70% for Sample A and 50% for Sample B with the iodine method, which was significantly higher than that with conventional ferric leaching of 14% for Sample A and 20% for Sample B. To elucidate the reason for the JX Iodine Process effectiveness, cross sections of leached residues were studied. Reaction products were confirmed around chalcopyrite even in the central area of particles in Sample A, however, reaction products were recognized at a depth of only 1 mm from the ore rim in Sample The resistance of Sample A to the leachate appeared to be lower than that of Sample B because Sample A had a high permeability and porosity, whereas Sample B had been affected strongly by a potassium alteration. No reaction products were visible on conventional leaching samples, even at the ore surfaces. INTRODUCTION Hydrometallurgical copper leaching (heap leaching or dump leaching) has been used extensively for copper recovery from oxide and secondary-sulfide ores, but not for primary copper sulfides, which contain mainly chalcopyrite as copper minerals. Although they are major resources of copper, primary copper sulfides are difficult to process because of their refractory nature. Extensive leaching studies have been carried out to leach primary copper sulfides (chalcopyrite), including biological and chemical, using a variety of oxidants and additives to enhance copper recovery. Watling (2013) reviewed acid-chloride-oxidizing agents with chalcopyrite. Abdollahi et al. (2015) tested silver as a catalyst for bioleaching with a chalcopyrite-bearing molybdenite concentrate. Hiroyoshi, Miki, Hirajima and Tsunekawa (2000) found a specific redox-potential zone for high-speed chalcopyrite leaching by controlling the ratio of ferric and ferrous iron. However, no ambient-temperature economic process has been developed for leaching primary copper sulfide, which usually has a low copper grade.

Jan 1, 2019

By M. Duncan

Lightweight, high-pressure cylinders for compressed hydrogen storage are essential components for fuel cell vehicles. Storage volume and mass are two key considerations. Current on-board hydrogen storage systems are based on a maximum pressure of 350 bar. While 350 bar systems are excellent solutions for many applications, some situations require higher storage densities due to space restrictions. As a result, significant research and development work has been expended by cylinder manufacturers, systems providers, testing agencies and automotive manufacturers to develop 700 bar systems with reduced storage volumes. Dynetek Industries Ltd. has proactively developed several 700 bar storage cylinders based on a seamless aluminum liner over wrapped with a carbon fiber composite. This paper presents the challenges and processes involved in the design, testing and certification for Dynetek Industries Ltd. 700 bar cylinders. This paper also provides reasoning for further volume and mass optimization of compressed hydrogen cylinders through the establishment of realistic cylinder usage parameters in standards. In particular, the overly conservative fill life requirement for cylinders is examined.

Jan 1, 2005

By C. B. Webber

"Sherritt Gordon's experience with rubber mill liners began in 1964 at the Lynn Lake Farley Mine and continued at the Fox Mine in 1960, and the Ruttan Mine in 1973. This paper describes the history of the performance of rubber mill liners at the three mine operations.LYNN LAKE - FARLEY MINEThe Lynn Lake Farley Mine, which ceased production in 1976 due to exhausted ore reserves, was a 3500 T.P.D. copper-nickel operation; consisting of two parallel rod mills followed by three stages of ball mill grinding. A circuit modification in 1964 necessitated one of the tertiary ball mills to be used as a pyrrhotite regrind mill. This 8' x 5' Hardinge conical mill drawing 225 HP was initially installed with steel liners and lifters. After several months of operation a routine inspection revealed severe channeling and washing behind the liners which was threatening to erode the ball mill shell. It was thought that the highly acidic condition in the mill, due to grinding 100 º6 pyrrhotite, was accelerating the wear of the steel liners. At this time it was decided to reline the mill with rubber liners to see if the wear problem could be relieved, and in December 1964 a set of Skega rubber liners were installed."

Jan 1, 1981

By Z. D. Hora

Sev_eral dozen si lica occurrences have been reported from various parts of Brit ish Columbia. Some represent hydrothermal veins or parts of pegmatite bodies; other are recrystall ized sandstones. Several vein type deposits were mined for smelter flux and as a source of white chips for stucco dash and simi lar products. Some quartzites were studied as potential sources of high-grade silica for ferrosilicon and silicon metal production. The province's only production of silica for ferrosilicon has come from a pegmatitic quartz plug near Oliver in southern British Columbia. Its reserves are now practically depleted.

Jan 1, 1984

By M. P. Amsden

"Ecstall Mining is a wholly-owned subsidiary of Texas Gulf Sulphur at Timmins, Ontario. The mill tonnage is 10,000 tons per day of two different ores, a copper zinc ore and a silver lead zinc ore, producing about 2400 tons of concentrates per day. These are as a copper concentrate, a high silver zinc concentrate, a low silver zinc concentrate and a silver-lead concentrate. For flotation recovery a very fine grind is required, about 80% minus 325 mesh and the concentrates produced are 40% minus 10 microns.The thickened concentrates are pumped to the filter floor for filtering and drying. The filtering and drying section is separated from the flotation section by a wall and is controlled from a dryer control room by one operator.Two operating panels are located in this control room. One contains stop-start controls for the thickeners, filter motors and vacuum pump motors, and stop-start controls for dryer feed conveyors and dryer product conveyors to concentrate load-out bins, as well as ammeters for conveyor drive motors. Dryer throughput is regulated by Merrick Type L weightometers located on the dryer discharge conveyors and recorded on tons per hour strip charts.The second panel contains the temperature strip charts, furnace drive ammeters, scrubber and exhaust gas controls, burner controls and panel alarms for the four dryers.Filtered concentrates are dried in Nichols-Herreshoff, multiple hearth, dryers consisting of nine hearths (zinc) and seven hearths (copper and lead). There are two dryers for handling zinc concentrates and one each for copper and lead concentrates. The dryers are heated by burning natural gas. Each zinc dryer handles 1,000 t.p.d. and the copper and lead dryers 750 t.p.d. each.Multiple hearth dryers are unusual in the base metal mining industry and the reasons for selecting them in preference to rotary dryers are as follows:1) The concentrates could only be filtered to 15 to 17 percent moisture. These sloppy filter cakes would be extremely difficult to handle in rotary dryers."

Jan 1, 1972

By X. J. Guo, Q. K. Wang, S. P. Zhong

With depletion of traditional clean copper reserves and fast expansion of the global copper demand and smelting capacity in the past decade, more and more copper smelters have to treat copper concentrate with increasing content of complex arsenic-bearing minerals. Developing economically viable and environmentally reliable methods and approaches for arsenic control in copper smelting has become more critical for sustainable growth of the copper industry. This paper will report the recent effort of Zijin Mining Group Ltd. in developing processes for improving arsenic control and management in the Zijin Copper Smelter. The arsenic distribution and balance data for matte smelting, converting and refining operations in Zijin Copper Smelter is reviewed for understanding of the current challenges in arsenic control. The processes developed for treating the arsenic bearing waste acid bleed stream from the smelting-converting off-gases wet cleaning circuit and the arsenic sludge produced in the refining electrolyte purification circuit for arsenic disposal are discussed. INTRODUCTION With fast expansion of the global copper smelting capacity to meet the world copper demand and depletion of traditional clean copper reserves, more and more copper smelters have to treat copper concentrate with an increasing content of complex arsenic-bearing minerals. China is the world largest copper consumer and also has the largest copper smelting and refining capacity, but majority of its smelting capacity relies on supply of imported copper concentrate. In order to meet the increasing copper demand and ease the tight supply of clean copper concentrate, the Chinese copper industry has to look at the domestic opportunity of developing non-traditional copper resources, specifically those of lower grades, more complex mineralogy, and increasing level of deleterious elements especially arsenic and also process imported copper concentrate with increased arsenic content. Due to a significant and growing environmental issue associated with arsenic contamination, developing economically viable and environmentally reliable methods and approaches for arsenic management and control in unlocking the maximum value of such arsenic bearing copper resources has become more critical for sustainable growth of the industry.

Jan 1, 2019

By D. Magoon

The metals industry has enjoyed a resurgence in prices and demand for its commodities during the global surge in economic activity that began in 2005. This success has brought with it an unprecedented demand for professionals in all sectors of our economy. Nowhere is that more true than in the mining and metallurgy sectors. However, this welcome improvement follows on the heels of almost two decades of challenging markets for the mining and metallurgy. Our sector's protracted economic slump created a paucity of demand for professionals that had several consequences. Our industry came to be viewed as a low ?tech, uninteresting place to work. Low demand for professionals encouraged students to seek other career options. Reduced demand for graduates, coupled with diminished program funding by our sector, resulted in dramatic shrinkage in university mining and metallurgy programs. This paper explores the lessons to be learned from our recent economic history and discusses some strategies for addressing our image issue. Attracting and retaining good employees is also strongly influenced by a company's reputation and record as a good employer. This reality is very well illustrated by the findings of an international survey undertaken by Towers Perrin in 2005 of 86,000 employees of mid-sized and large companies in 16 countries. The key findings related to attracting and retaining employees are presented. These findings are also discussed in the context of their specific applicability to the mining and metallurgy industry.

Jan 1, 2007

By Roger Lacroix

Fuel cell application to mining has been indicated to be potentially beneficial to underground mine worker health and to energy efficiency. In order to define the economic advantages of using hydrogen fuel cell vehicles, a detailed study of operating and capital costs associated with underground loaders and power supply infrastructure has been carried out. The results show that for a typical medium-size mine, operating costs and infrastructure costs are less for the fuel cell option versus diesel. The reverse occurs for capital costs owing to the currently higher cost of fuels cells versus diesel engines. This disparity is expected to decrease given the decline in price associated with fuel cell technology advances. Related market issues for fuel cell manufacturers are also presented. Despite the difference in cost, the resources and mine infrastructure required to operate loaders, and base design of the mine loader, is similar for diesel and fuel call versions.

May 1, 2007

What Discounted Cash Flow Analysis can do for you: ?Provide an accurate financial analysis of a project for the first 25 to 30 years of operations ?Identify cash flow requirements ?Identify relative sensitivity of the project to the various input parameters ?Place a value on the resource in place after 30 years of operations ?Correct for errors in input parameters

May 1, 2010

By J. E. Gebhardt

Advances in computational modeling provide unprecedented process simulation tools for the process engineer to examine and explore options for optimizing heap leach operations. A phenomenological model developed within a computational fluid dynamic software framework provides a general heap leach modeling tool that describes reactive dissolution and fluid flow through the stockpile. A one-dimensional form of the model is used to parameterize the kinetic leach reactions for a mixture of copper sulfide and oxide minerals against data from operational leach tests. A two dimensional version of the model provides a means to investigate the effects of irrigation rate, lift height, air injection, bacteria limitations, and other factors on recovery and pregnant leach solution concentrations. The model was calibrated for the Nifty Copper operation and ore type in order to simulate heap performance. Model simulations are reported for the chalcocitetype ore and compared to process data. The application showed that the multidimensional nature of heap leaching causes heterogeneous effects that are not always adequately described by one-dimensional models. Irrigation flow rate and aeration effects were simulated for a multi-lift heap section, and model results indicated that air injection at the base of the second lift would be required to achieve expected copper recovery under these lift height and flow conditions.

Jan 1, 2007

By Rodolfo Zanella

Au/TiO2 catalysts were prepared by deposition-precipitation using NaOH (DPN) (~3 wt % Au) and urea (DPU) (~8 wt % Au), and calcined at various temperatures between 100 and 400 °C. They were characterized by UV-Visible, XANES, EXAFS and TEM. Their activity were tested in the reaction of CO oxidation at 5°C. After preparation, the gold species are in the oxidic state III. They begin to transform into metallic gold under air at ~100 °C for DPN and ~150 °C for DPU. At 200 °C, all the gold is metallic for the two preparation methods. The particle size increases from 1.5 to 3.5 nm with the calcination temperature. The catalytic activity for CO oxidation increases with the percentage of metallic gold, and it is maximum at 200°C for both types of samples. The activities (per mole of Au) are the same for the two types of catalysts. At higher temperatures, the catalytic activity drops. The decrease of activity is mainly due to a change of particle shape with the calcination temperature rather than to the increase of the particle size. At a calcination temperature of 200°C, the particles present small facets with rounded parts, and their outer surface contains a large proportion of low coordinated sites (steps and corners) while at high temperature of calcination, they are truncated octahedra with smooth facets.

Oct 1, 2003

By Chris Ryan

Operational excellence along with the need for a capital management strategy demanded an educated budgetary retirement age for haulage fleets, with uniform applicability. Given fleet size and volume of data for the Komatsu 830E fleet within Teck, this unit type was selected for development of a retirement age model suitable for all operations. The model is designed to act as a capital planning and fleet management tool aimed at minimizing costs. Life cycle parameters were examined to facilitate a visual and numerical representation of a fleet over a period of time. Physical availability and operating cost models were developed to obtain an understanding of the life cycle. These models became the drivers behind the fleet-wide retirement model. A wide analysis range of the equipment life cycle was used as it assured that the optimum retirement regime would be accurately captured. Average annual spend, including cost of operating and ownership was measured against the corresponding retirement age. Targeting the minimum within this range yielded the optimal retirement age.

May 1, 2010

By R. von Gal

Hazelett Strip-Casting Corporation has been producing the Hazelett® twin-belt casting machines for copper casting since the mid-1960s. The first commercial casters were developed for copper alloy strip and anode plate. In 1968, development work was started to adapt the twin-belt caster for copper bar casting to be rolled in-line into wire rod. Since then, 36 casters have been sold as part of the CONTIROD® system for the production of a substantial portion of the world's copper rod supply. A unique feature of the twin-belt caster is the mold's ability to comply with the size and shape of the cast bar as it shrinks during solidification. Maintaining contact between the mold and the bar provides a high rate of heat transfer as well as other benefits, including the prevention of surface imperfections caused by remelting in the mold. This paper will give an overview of the continuous evolution of the twin-belt caster technology with an emphasis on recent developments in compliant mold technology for copper casting.

Jan 1, 2007