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By Randy Sandrik

Sampling has evolved at two large underground limestone mines as conditions and product requirements have grown tougher over 100 years of mine life, requiring innovative techniques to insure delivery of high purity limestone. Sampling insures delivery of consistent product to customers at the lowest possible cost. Statistical considerations have evolved from simple data collection to predictive and process capability analysis. Sample methods include borehole samples, face (using a proprietary face-sampling device), and total plant feed automatic, process, and final product sampling. Lessons learned, while keeping costs at historically low numbers, include the importance of geological models, exploration drilling density, face sampling, and blending of ore.

Jan 1, 2005

By A. R. Laplante

The mineralogy of the Joe Mann mine differs from that of other deposits of the Chibougamau area that are exploited by Les Nines Camchib Inc. It is characterized by very fine first generation gold and very coarse second generation electrum. Successful processing required adjustments of the processing flowsheet, which includes gravity, flotation, and cyanidation. A study of coarse gold liberation in the gravity/grinding circuit is described. Modifications to the flotation circuit and the reconditioning of a small capacity cyanidation circuit are presented.

Jan 1, 1989

By C. J. Konya

When blasts are designed, the assumption is made that all blastholes release near ideal energy. In many types of mining operations, some blastholes release very little useful energy. These blastholes will be called malfunctioning blastholes. Recent studies indicate that on many types of blasting applications, 30 percent of blastholes are malfunctioning. This malfunctioning routinely occurs on the operation and is not an unusual occurrence. This paper will discuss the cause of malfunctioning blastholes and methods to minimize the detrimental effect on both safety and costs.

Jan 1, 1988

By F. Kennedy

Consolidation Coal Company (Consol) supports an active R&D effort to improve the safe, productive mining of coal and to utilize coal in an environmentally acceptable manner. Attention will be focused on degasification of coal seams, continuous coal transport systems, earth sciences activities, and coal combustion. Brief mention will be made regarding the SO2 emissions control programs. The research program constitutes about 1.0% of Consol coal sales which positions Consol as the preeminent coal company supporting broad-based research addressing the full spectrum of the various problems associated with utilizing the nation's abundant reserves of economical, readily available fuel.

Jan 1, 1989

By R. J. Smith

Hornestake's Mclaughlin Mine is the first commercial application of pressure oxidation pretreatment of gold prior to cyanidation. Inherent to the autoclave process are several liquid/solid separations. Flocculant consumption represents a significant portion of the consumable reagent costs at McLaughlan. This paper focuses on the efforts of the Operating, Metallurgy and Engineering groups to improve thickener operation and minimize flocculant consumption. An operating philosophy incorporating feed solids control, increasing flocculant dilution water and minimizing flocculant solution shear has resulted in a reduction in 1986 flocculant costs of $0.054/t ($0.06 st) versus 1985 costs. Additional changes are projected to result in a further cost reduction of $0.20/t ($0.22/.st) in 1987.

Jan 1, 1988

By R. H. Sailors

During the last 15 years, the North American Mining Industry has experienced increasing usage of cast high chromium white iron grinding media in wet grinding applications. First introduced into the cement industry (klinker grinding) where wear rate reductions of four or five times have been realized compared to steel balls, this same grinding media serve the iron, copper, and phosphate markets by resisting not only impacts and abrasion, but also corrosion which occurs in wet grinding. In these markets, single mills containing 250,000 kg of grinding balls are not un-common and hence the economic potential with respect to lower wear rates can be significant. Add to reduced wear rate the increased production efficiency that is possible and it is readily understood why much of the mining industry uses cast high chromium grinding media. Metallurgically, the alloys used consist of a martensitic matrix containing hard M7C3 eutectic carbides. Carbon (2.0 to 3.5%) and chromium (12 to 277.) are characteristically used to arrive at the desired properties.

Jan 1, 1989

By Frank F. Aplan, Robert S. Thomson

A placer ore jig, typically used to recover fine gold, tin and diamonds from alluvial ores, has been modified to remove fine pyrite from minus 6.4 mm (-114 inch) coal. In parallel tests, it proved to be far superior to two conventional coal jigs, the Baum and the Baum-feldspar, in removing fine pyrite from coal. The Pan-Am placer jig was found to remove essentially all of the +28 mesh pyrite and from 99% to 90%, decreasingly, in the 28 to 200 mesh range. This jig also showed a superior performance to the Baum-Type jigs in removing fine coal from its associated refuse. The superiority of the Pan-Am placer jig is related to the strong emphasis given on the suction stroke and, hence, on consolidation trickling, whereas the Baum jigs principally emphasize the pulsion stroke during jigging.

Jan 1, 1995

"Outotec’s TankCell® e500 flotation cell was commissioned during 2014 at the Kevitsa Mine in northern Finland. The TankCell® e500 is the first cell in this size class (500m3) to be run in an operational duty and it has been working as the first rougher in the copper flotation circuit. Treating around 850tph with an average grade of 0.3% Cu the TankCell® e500 has run with an average copper recovery of 71% and an average enrichment ratio of 50. In addition the cell has proved to be very energy efficient, operating with a specific energy of around 0.4kW/m3 under production conditions. This presentation will provide a review of the installation and operation of the TankCell® e500 at Kevitsa and will summarize the results found in the published literature from the various testing campaigns conducted around the cell. INTRODUCTION The TankCell e500 was installed and commissioned at the Kevitsa mine in northern Finland in 2014. Post startup the cell was initially run for testing and optimization with various test campaigns undertaken. but was subsequently taken into a production duty (Mattson et al., 2015a). At Kevitsa the cell is run as the first copper rougher replacing the previous two copper roughers (both 160m3) in this duty. The unit is running at between 38-40% solids at a feed rate of approximately 850tph. Since operational the average copper recovery from this single cell has been around 71% copper. This is typically with an enrichment ratio of around 50 being fed with an average head grade of 0.3% copper. More details on the circuit configuration and production performance of the e500 at Kevitsa can be found in Mattson et al., (2015a) and Murphy et al., (2016). In addition through the optimization program with the use of a variable speed drive controlling rotor speed it was found the the e500 was very energy efficient under production conditions. During this work the cell was found to run at a specific energy of around 0.4kW/m3 which exceeded design expectations (Xia et al., 2015)."

Jan 1, 2016

By J. G. Mansanti

The metallurgical response of a deposit's various ore types usually has a strong impact on the flowsheet design of most mineral processing plants. This impacts the materials handling, equipment selection, capital and operating costs, and plant availability. Because of the rapid leaching characteristics of Chimney Creek ores a variation of the conventional gold plant, carbon columns and CIP was proposed. The proposal consisted of a washing stage which was installed between the typical leaching and CIP stages. The circuit was simulated in the lab and was modelled using a computer program to evaluate the metallurgical impact and the effect on the system's mass balances. Also, actual plant data was reviewed comparing the results that were achieved with the results that were expected.

Jan 1, 1988

By L. Adler

In spite of distractions from glam-our areas (ground control, computers, etc.), excavating and bulk handling in mining remains paramount but is now undergoing dramatic advances. The massive intervention of mining and civil engineers as "engineer-users" into the tight, exclusive, and specialized bond between the equipment operator ("operator-users") and the manufacturer (mechanical engineers "and sales "reps") has now occurred. Three developments have accelerated this: 1) larger, more costly, complex, specialized, and innovative equipment; 2) a more profound understanding of the equipment, operations, and working conditions (encumbered space); and 3) a concurrent thrust into "high-tech," (automatic and remote controls, sensors, automation, artificial intelligence, and even robotics) and human factors (workload intensity, work-station design). This has produced a well-defined professional discipline, including construction and even military engineering. The mine plant, and to a lesser extent, the mine face, is now being monitored. Equipment conferences, journals, and centers at universities and agencies have multi-plied. The discipline's impact on future mining now becomes more apparent.

Jan 1, 1988

By A. Pratt, G. Deschênes

This paper quantifies the detrimental effects of pyrite and stibnite on gold leaching kinetics. Means to reduce the effect of these minerals by addition of lead nitrate and oxygen are presented. A significant retarding effect was observed when the pyrite concentration was 20%. A pretreatment with lead nitrate reduced the extent of gold surface coating by Ag, Fe and S. Stibnite, at a concentration as low as 20 ppm, significantly affected the gold leaching kinetics through forming a passivating film of Sb(V) oxide possibly Sb2O5. The most practical way to alleviate the effect of stibnite is to leach the materials at a moderate pH with addition of lead nitrate. A low temperature reduced the efficiency of lead nitrate to counteract the effect of stibnite. The increase of dissolved oxygen is not favourable to alleviate the coating of stibnite on gold.

Jan 1, 2004

By R. V. Ramani, S. Skankar

Available literature on the effect of re-entrainment on overall airborne dust concentration in mine airways or the fundamental mechanisms of coal dust re-entrainment in mine atmosphere is scant (Shankar and Ramani, 1991). Therefore, as part of the Respirable Dust Center's ongoing research, the following three-part study was undertaken: •a study of the re-entrainment phenomena of anthracite and bituminous coal dust particles in a wind tunnel under the influence of varying air velocities; •a study of the same in the Lake Lynn Laboratory Mine of the USBM with both air flow and walking by personnel causing re-entrainment; and •the mathematical modeling and computer simulation of the re-entrainment phenomenon. In this paper, results from the re-entrainment studies in the wind tunnel and the Lake Lynn Laboratory mine are presented. Comparing the results from the two studies, it was observed that increasing the air velocity increased the rate of re-entrainment (Shankar and Ramani, 1994a) and the rate of re-entrainment decreased with the time of exposure of the source dust to the flowing air. In addition, when the source dust was composed of particles of different sizes, the airborne dust concentrations due to re-entrainment were higher than when the source dust was composed of particles of the same size. The contribution of airborne dust concentration due to airflow was negligible compared to the contribution due to walking.

Jan 1, 1996

By Peter J. Stewart

My first experience with carbon reactivation in the gold industry was at Whim Creek, Meekatharra some 15 years ago. Very little was known, in fact, carbon reactivation kilns in the gold room were a complete mystery. Ten years ago at conferences such as this the mystery was more as to why field kilns would not reproduce activities achieved in the laboratory. A carbon reactivation kiln manufac­turer was thought to be brave or stupid to speak at a venue such as this. Reactivation kiln design has improved dramatically in the past 10 years and with a few exceptions, most kilns operate well. May I suggest that now, the focus is on plant practice rather than kiln design, and that the basics of plant practice as it relates to carbon activity needs revisiting. As metallurgists like to talk on engineering, accountants on the Economy and vice versa, my presentation on Carbon Reactivation will focus on plant design and operation as it effects carbon reactivation. There have been some excellent papers published over the past 15 years on the basics of carbon reactivation in relation to gold processingl,2,}. Taken that kilns operate and are effective to a greater or lesser degree, plant design and operating practise have an enormous bearing on carbon activity, solution tail, carbon loss and other cost items. This presentation will not argue the merits of equipment used for the thermal reactivation of organically fouled carbon, questions on this subject are welcome over a drink after this session.

Jan 1, 1995

By John S. Newton

Modern high capacity underground mining machinery is a complex of mechanical, electrical and hydraulic components which have greatly increased capability over similar components of mining machinery of ten and. even five years ago. Looking into the future I feel certain in stating that there will be changes equally great in the coming five and ten year periods. With this premise in mind, I should like to bring to your attention some of the things that do and will have a continued major impact on the industry, particularly as they relate to the maintenance and operation of these machines of increasing capability. In underground mining today, nearly every individual plays a key role. A machine operator's importance in his work is comparable with that of the pilot of an airplane, a railroad engineman, a bus driver, a skilled machinist, a bulldozer operator and many others whose assignment is one of doing, by himself, with his hands and his brains all that the specially designed machine has been created to do. These machine operators are supported by a staff of skilled engineers, maintenance personnel, supervision, etc., but objectives are realized only when the operator maintains his schedule. What is being done and what can be done to make it easier for the operator to maintain his schedule which, as with the airplane, is constantly being improved? This question can be answered best, perhaps, by dividing the subject into four general categories - (A) Power Supply. (B) Control and Protective Devices. (C) Hydraulic Component Design. (D) Mechanical Design.

Jan 1, 1962

By I. Edgar Odom

Hectorite is a rare magnesium-lithium clay mineral that occurs at many places in the McDermitt caldera of Nevada-Oregon. Commercial development of several high purity deposits began in 1986. The hectorite that was precipitated in a lake environment formed after the collapse of the McDermitt caldera. Hectorite beds and lenses are associated with volcanic sediments, limestones, dolomites, zeolites and locally sandy bentonites. The high purity deposits appear to be associated with hydrothermal areas. The hectorite consists of extremely small, flake-shaped crystals. Calcium (Ca) is the predominant exchangeable ion. Its color ranges from white to light green. Commercial uses include high-brightness, magnesium-aluminum-silicate (MAS) products, organophilic clays, pulp retention and ceramics. The MAS is used as a suspending agent, binder, stabilizer and thixotrope in aqueous solutions for cosmetics, household cleaners, pharmaceuticals and miscellaneous industrial applications. Hectorite-based organophilic clays are used in printing inks and paints. The McDermitt caldera complex is located astride the Nevada-Oregon boundary west of the town of McDermitt, NV (Fig. 1). The structural complex is elliptical in shape, extending about 43 km (27 miles) north-south and 34 km (21 miles) east-west. This area was the site of extensive volcanism during the Miocene (24 to 18 million years). The complex consists of five overlapping calderas with the oldest at the south end of the complex (Rytuba et al., 1979). Each of the vent areas collapsed and is marked by a ring fracture zone. The ring fractures around the outer boundary of the caldera complex are shown in [Fig.1].

Jan 1, 1992

By Broderick E. Davis

Each year, about 45 Mt (50 million st) of flotation tailings are discarded in Florida phosphate operations. These tailings only contain about 4% of the phosphate in the ore. However, more than half of the phosphate in the tailings is concentrated in the +600 µm (+28 mesh) size fraction at grades of up to 20% P205. Many phosphate producers have attempted to solve this problem by floating the +425 µm (+35 mesh) flotation feed separately. However, phosphate recoveries in these circuits are typically only 60%. For seven sampled phosphate operations, the phosphate content of the +600 µm (+28 mesh) fatty acid tailings ranged from 15% to 25% P205. In every case, the +600 µm (+28 mesh) fatty acid tailings was higher in grade than the overall flotation feed. Attempts to efficiently recover this coarse phosphate have apparently been unsuccessful at these seven phosphate operations. Recovery of this coarse phosphate would provide an additional 900 kt to 2.5 Mt (I to 2.7 million st) of phosphate annually and add an additional year to the reserves of these important deposits. A typical central Florida phosphate matrix is composed of three different mixtures of minerals. The +1.18 mm (+ 16 mesh) portion is chiefly phosphate pebbles and is beneficiated by sizing. The -106 µm (-150 mesh) portion contains virtually all of the clay minerals and is discarded in the hydrocyclone overflow. The -l mm +106 µm (-16 +150 mesh) material is a mixture of quartz and phosphate minerals.

Jan 1, 1993

By S. A. Shuey, E. E. Vidal, P. R. Taylor

The complex chemical make-up of electronic waste as well as the variability of feed material from post-consumer sources requires resilient processing systems that are able to handle a range of material without adversely effecting production. Several of the successful processes that are being operated by a number of large-scale metal producers are reviewed in this paper. This review outlines the processing path and final disposition of many of the important individual elemental components. Determining the chemical characteristics of processes is required to understand both metal recovery possibilities and controlling the fate of minor elements. The behavior of both the organic and metallic fractions of electronic waste during processing is evaluated thermodynamically and general conclusions are given. I

Jan 1, 2006

By Bruce A. Brown

Construction aggregate is the most important nonmetallic-mineral commodity in quantity and value that is produced in Wisconsin. Crushed stone is produced from the Precambrian crystalline rocks and the Ordovician and Silurian carbonates, and sand and gravel is extracted from Quaternary glacial deposits. Dimension stone is quarried from both the Precambrian crystalline rocks and Paleozoic carbonate rocks. Other nonmetallic minerals include industrial sand, lime, roofing granules, terrazzo aggregate, and peat.

Jan 1, 1999

By D. L. Schweyer, W. A. Munson, R. H. Hanewald

Discussed is the INMETCO processing of electric arc furnace (EAF) baghouse dusts from the specialty-steel and low-alloy industries. In addition, the INMETCO process has been modified to recover nickel, chromium and iron from many other waste materials including: •pickling solutions or filter cakes, •spent nickel and chromium plating baths, •carbon refractories from pickling tanks, and •superalloy wastes including baghouse bags. INMETCO is the only North American company presently capable of recycling nickel-cadmium batteries by high-temperature metals recovery. This process and the details of INMETCO's best demonstrated available technology (BDAT) test program are discussed.

Jan 1, 1993

By C. R. Copeland

Water sprays are a common method used to reduce particulate matter (PM) emissions. Various factors such as wettability, surface area coverage, fine particle engulfment rates, interparticle adhesion forces, suppressant penetration, and suppressant longevity have all been suggested as critical factors in achieving effective PM control. However, it has not been established which of these factors are the most important. Experimental work indicated that suppressant penetration is the most critical of these factors. Suppressant effectiveness was also improved using hygroscopic reagents which retained moisture, improving longevity. Maximizing suppressant penetration and improving suppressant longevity led to an average 86% reduction in PM10 concentrations in laboratory dust tower tests.

Jan 1, 2008