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By Y. K. Yen, J. D. Miller, C. L. Lin

Particle size segregation is a common phenomenon in many particulate processes and has many undesirable effects. The size segregation which occurs on a belt conveyor causes a serious problem for on-line particle size measurement using image-based techniques. Whether particle size distributions measured from the top layer of the belt are representative of the total particle population is largely dependent on the degree of size segregation. Therefore, it is important to understand the nature of such size segregation in order to make appropriate corrections for on-line particle size analysis. Monte Carlo simulation has been used to provide segregation information on particles with simple geometry and the results can help to determine important factors in experiments with irregularly shaped particles. It is expected that the relationship between the particle size distribution of the top layer and that of the entire particle population on a belt conveyor can be formulated as a model based function.

Jan 1, 1997

By P. H. Williams

Experiences gained using computers in the mining and geological environment have shown that it is quite rare for a system or the data it stores to be truly stand alone. Just as the mining enterprise aims to have a smooth integration of operations from exploration through mining and extraction to sales, so it should develop all its information systems within an overall framework or architecture which covers the applications and data as well as the computer hardware and communications. This paper discusses methods of achieving such an architecture, and describes some of the benefits it can have on the development and implementation of information systems. The key aspects are the identification of the business functions and the data that they use, and ensuring that the IS plan supports the overall objectives of the enterprise. Hardware and communications policies should be based on the plans for the applications and data, rather than the reverse.

Jan 1, 1986

By Kenneth A. Gutschick, Harry L. Francis

A large number of minerals and chemicals (Table 1), some mineral-derived, are used in the treatment of both potable water and domestic sewage waste water and solids (Anon., 1990). In water treatment there are ten principal process uses as shown in Table 2 (Anon., 1990), which also lists the major chemicals in each process. Since lime (calcium oxide, calcium hydroxide, and dolomitic lime) is the largest chemical (by tonnage) used in water treatment, this chapter will deal primarily with this product. Note that it is included in five of the process uses shown in Table 2, and that indirectly it is also used in at least one other category (taste and odor control, where lime is used with potassium permanganate to provide optimum pH condition). POTABLE WATER TREATMENT Water Softening The biggest use for lime in water treatment involves water softening, where it serves to reduce carbonate hardness caused by dissolved bicarbonate and carbonate compounds. Currently there are more than 1000 domestic water softening plants (Table 3) located in most sections of the country, but particularly in Ohio, other midwestern states, Florida, and Texas, where limestone bedrock abounds (Anon., 1990). Among the other uses for lime in water treatment are coagulation, disinfection, and removal of heavy metals due to high pH softening, removal of certain radioactive and organic compounds and fluorides, neutralization of acidic water, removal of silica, particularly with dolomitic lime, and removal of color. Most of the above advantages accompany water softening, although at some plants lime is used specifically for one purpose, such as silica removal with dolomitic lime, minimizing pipeline corrosion by addition of lime to correct an aggressive water, and others. Hardness in water comprises two types - carbonate hardness, caused by dissolved calcium and magnesium carbonates and bi- carbonates, and non-carbonate hardness caused by dissolved non- carbonate salts, particularly calcium sulfate, calcium chloride, magnesium sulfate, and magnesium chloride. Total hardness is the sum of the carbonate hardness and non-carbonate hardness. Waters are classified as soft (0 to 75 mg/L as CaCO,), moderate (75 to 150 mg/L), hard (150 to 300 mg/L), and very hard (above 300 mg/L). Most water plants strive to reduce total hardness to about 100 mg/L, although in recent years the tendency in some cities has been to allow a little higher value in order to reduce both chemical costs and the amount of water softening sludges produced. There are four basic types of softening plants: lime softening, primarily to reduce carbonate hardness; lime-soda softening, for reduction of both types of hardness (in some plants caustic soda is used in place of soda ash, but it is more costly); split lime-zeolite, where a base exchange mineral is employed in place of soda ash (this system also requires salt [sodium chloride] to regenerate the zeolite mineral); and finally zeolite softening, which is generally used in small systems for private houses and small municipalities. Principal disadvantages of the latter system are its relatively high cost and the salt requirement, which introduces considerable quantities of soluble salts into the waste water discharge system.

Jan 1, 1994

By Ron Jackson

The report gives a general method for the geological evaluation of a gold deposit. Recognizable parameters associated with gold mineralization are used to develop a model of an orebody. The California Mother Lode is used as an example.

Jan 1, 1987

By Kurt O'Bryan, Gary Beerkircher

WaterFlush Technology offers maximum comminution performance benefits over to­day's more common comminution methods. These benefits will be presented with case studies of existing installations, and the projected performance gains for circuits scheduled to begin operation in 1992.

Jan 1, 1992

By Rein Buisman, Michael Fullam

This paper outlines the general operating principles, benefits and applications for the Pansep Screen. The Pansep is a continuous fine screen developed in 1997 capable of processing high volumes of fine mineral f actions continuously, and at small apertures.

Jan 1, 2000

By Carlos Andrade

An engineering endeavor involves the creation of an expansive, environmentally conscious reinforced sloped MSE wall system. The objective is to enlarge a flat mining work area. Situated in southern Arizona, this mine is dedicated to extracting essential resources such as Manganese, zinc, silver, and lead, crucial for advancing clean and renewable energy initiatives. The project necessitates the implementation of a Mechanically Stabilized Earth retention system. This system aims to both expand the mine’s working area and facilitate access to underground tunnels. The expansion pad must be robust enough to endure the substantial loads exerted by heavy mining machinery. The wall’s reinforcement components are strategically designed to counteract the challenges posed by aggressive soil conditions with low resistivity. Furthermore, they must be resilient against potential damage during installation. The system’s ease of transportation is crucial due to challenging access conditions, and its design must allow for efficient drainage. A significant consideration is the integration of a face system that fosters vegetation growth and seamlessly merges with the existing flora of the area. In addition, plans include the construction of an access road downslope from the wall. The chosen solution involves a reinforced sloped system with a 70-degree incline. The wall’s surface is adorned with an erosion control mat, intended to promote the proliferation of vegetation. For added durability, the wire basket units are equipped with galvanized wire featuring a polymer coating. High tensile strip bonded geogrids, featuring a robust polyester core, provide essential reinforcement. The completed wall is an impressive feat, spanning 1500 feet in length and soaring to a height of 45 feet. It stands as a testament to innovative engineering in harmony with environmental and functional considerations.

Feb 1, 2024

By S. E. Phillipson

The MSHA Technical Support, Roof Control Division's primary evaluation tool for coal pillar designs is the Analysis of Coal Pillar Stability (ACPS) program. However, ACPS is limited to evaluating interactions between two seams at a time, which is not ideal for complex multiple- seam scenarios. Further, it does not recognize the influence of strata properties in the interburden and cannot be used to evaluate individual pillars. We apply the Rocscience RS2 two-dimensional finite element program as a complement to ACPS. Complex multiple-seam scenarios can be characterized by a modified pillar stability factor where the ACPS single-seam development pillar stability factor is multiplied by the ratio of average single-seam development stress to the stress in the critical pillar at the multiple-seam stage, using the values of o as predicted by RS2. Several series of test examples involving two-seam analyses with isolated remnants, gob-solid boundaries, and high extraction areas of varying width were used to calibrate simulated gob properties such that the ACPS+RS2 method generated results that matched a traditional ACPS Stability Factor to within 13%. As high-extraction areas become wider and deeper, progressively stiffer gob is simulated by increasing the Young's Modulus property in RS2. After achieving calibration with the test series, three examples of complex multiple-seam scenarios were evaluated, using reasonable properties for strata types and thicknesses based on core log data. Resulting modified stability factors are reasonably close to those predicted by ACPS, although affected by units of sandstone in the interburden and gob shadows superimposed on remnant structures. This tends to show that even in complex multiple-seam conditions, applying ACPS to the worst-case interaction should usually result in an acceptable pillar design.

Jun 25, 2024

By W. Hopkin

INTRODUCTION Necessary science and technology are not well established for the design of responsible treatment and disposal of arsenical residues from refractory gold ores. Specifically, there is uncertainty about the precise composition and behaviour of oxidised arsenic species in these wastes, and an analysis of possible chemical behaviour suggests that potentially difficult control and disposal problems remain to be so 1 ved. In tackling these the undoubted toxicity of arsenic in excess and its bad press should not blind one to the realities of actual behaviour in the environment, and that some adverse behaviour inevitably has to be to 1 erated as a cost in return for the recovery of an operation's gold for society. The problem is to minimise any such cost. Each refractory ore will be different. Many will contain so little arsenic that it will cause only trivial problems in disposal, but there remain others with significant arsenic content, say in the order of 1% or more, to cause concern. As already implied, concern can be over emphasised but equally underestimated. The balance which must be struck in the design of responsible disposal in the widest sense requires objective and practical assessment of a complex range of chemical, biochemical, engineering and economic design factors, all of which should involve the process design team in constructive dialogue with the 1 oca l regulatory authorities. In British terms, the general objective should be the Best Practicable Environmental Option. Arsenic is ubiquitous in waters, rocks and soils and all living things. Its compounds undergo natural geochemical and bi ochemi cal cycles including powerful adsorption and precipitation processes which return to nature all leakage from the inevitable disturbance of mining and extraction operations. Within limits, all life is tolerant to its presence, and adaptation and detoxication processes occur to deal with local excesses.

Jan 1, 1991

By D. S. Choi, D. L. McCain

INTRODUCTION Coal is forecast to be an increasingly important and economical source of energy for the future as the supply of oil and gas declines relative to overall energy demand and perhaps in absolute quantities produced. With the decline in productivity, especially in underground mining, in the early seventies coinciding with the need to produce greater quantities of coal for market, a gradual change from room-and-pillar mining to longwall mining has been taking place in the United States. Consolidation Coal Company (Consul) produces about 50 million tons of coal per year with approximately 66% being from underground mines. Most of the mines are located in the Appalachian Region in the States of Pennsylvania, West Virginia and Virginia, and in Ohio and Illinois. Coal is produced by the room-and-pillar mining method with continuous mining machines in addition to an increasing number of longwall mining faces. Continuous mining machines will continue to be used for driving longwall development entries as well as in areas where partial extraction must be practiced in order to support the overburden rock because of surface structures or in areas that cannot be subsided, or where unfavorable geologic conditions limit the application of the longwall mining methods. ROOM-AND-PILLAR MINING METHOD Some background in the room-and-pillar mining method may be helpful to provide perspective. This method has been widely practiced since the beginning of coal mining in the region. It is a flexible system because it can provide either partial or nearly complete extraction, and coal pillars can be left where needed to support surface structures or oil or gas wells or because of unfavorable geologic conditions (Choi, Dahl and McCain, 1980).

Jan 1, 1983

By Ivan C. Machado

In full autogenous grinding (FAG Mills) the ore itself determines almost exclusively the product size that will be produced, as opposed to conventional steel-media grinding where the product size can be "engineered" by changing media size, feed size, feed rate, classifier cutpoint size, etc. SAG Mills are in the middle of the way, since they offer some room to engineer their product size by properly defining some critical process variables, such as feed size, ball charge and size, mill charge and speed. SAG Mill product P80 values are typically in the range of 500 µm (35 US mesh) to 2000 µm (10 US mesh.) Whenever it is possible to determine an optimum value for the SAG Mill product P80 value (which will be the Ball Mill fresh feed F80 value), the Engineer should define the process variables that will yield a SAG product size as close as possible to the optimum calculated P80 value. In general, a coarser SAG product will draw less power from the SAG Mill and more power from the Ball Mill, and conversely, a finer SAG product will draw more power from the SAG Mill and less power from the Ball Mill. Metal consumption analyses also have to be taken into consideration, for they typically account for 30% to 45% of the total grinding cost. This presentation addresses the issue of defining an optimum SAG Mill product size (X=P80), during the design phase of the SAG and Ball milling circuits, from a general perspective, i.e., the SAG product size that will lead to an overall SAG Mill - Ball Mill optimum performance. Bond's Third Law approach is used, as well as the SPI (SAG Power Index), and also the generally accepted equations and Engineering Practice currently utilized to design SAG Mill

Jan 1, 1999

By D. A. Barr

The Galore Creek copper deposits lie in the Stikine River district of northwest British Columbia, a largely undeveloped region which possesses rugged mountain terrain with deeply incised valleys which support dense undergrowth. Timberline is normally at about 1300 m (4265 ft) and the higher levels contain glacial systems and large ice fields with peaks rising to 3500 m (I 1,483 ft). A location map of the Galore Creek area is given in Fig. 1. In the late 1920s, field parties under the direction of F.A. Kerr (1948) of the Geological Survey of Canada completed geological surveys of the district. Primary access for this work was provided by riverboats on the Stikine and Iskut Rivers. Kerr's party had to contend with extremely difficult travel conditions that required considerable backpacking, augmented by pack dogs in certain cases. Absence of ground control led Kerr to establish his own topographic maps. Among the geological data established was the recognition [ ] that small bodies of orthoclase porphyry in the district are often well mineralized with base metal sulfides. Copper mineralization in the upper Galore Creek valley, a tributary of Scud River which flows into the Stikine River some 80 km (50 miles) south of the small settlement of Telegraph Creek, was originally discovered during aerial reconnaissance by M. Morrison and W. Buckholz while prospecting for Hudson Bay Exploration and Development Co. Ltd. in 1955. Malachite- and azurite-stained out- crops in several parts of the Galore Creek watershed are clearly visible from distances of 500 m ( 1640 ft) or more. Claims were staked in 1956 and the copper showings were partly mapped, trenched, and investigated by shallow diamond drilling. Because of the remoteness of the area and higher priorities for expenditures elsewhere, no further work was undertaken and most of the claims were allowed to expire.

Jan 1, 1991

By D. Kruse, M. Sanaei

"3D finite element models of the Segmentally Lined Shaft (SLS) structure are simulated as means of numerical analyses of the system’s structural behavior. Top-down constructed rings, comprised of precast concrete segments, create a large diameter, relatively shallow underground space that can be utilized for various applications. To further investigate the effects of soil conditions and different loadings on the shaft structure, the FE model was run under various boundary conditions. Simulations include a) effects of various soil layers on the SLS, including a circumferential boundary of modified ground, b) effects of various soil layers on the SLS without any ground modification, c) Seismic analysis of the SLS with ground modification and d) Seismic analysis of the SLS without any ground modification. Comparing the analyses outcomes emphasizes the significance of the inclusion of the ground modification boundary in the structural performance of the SLS. INTRODUCTION TO SLS Underground structures are classically built rectangular in shape, which normally requires a two-step construction process beginning with installation of temporary shoring to support earth loads during the excavation, followed by the construction of the permanent structure. Attractive and practical alternatives are circular shafts referred to as segmentally lined shafts (SLS). The structure consists of a stacked series of rings formed from an assemblage of precast concrete segments. Top-down constructed systems of large diameter, relatively shallow SLS structures provide both temporary earth support during excavation and permanent structural support for many civil and building applications. The circular shafts sustain the lateral earth pressure mainly through hoop-stress mechanism, resulting in improved stability and structural efficiency. Cylindrical shell structures with large diameter to wall thickness ratios are prone to buckling under external pressure. In typical designs of small diameter shafts and tunnel linings with small diameter to wall thickness ratios, nonlinear buckling analysis (i.e., nonlinear geometric analysis) is usually not considered, since the buckling capacities for those structures are much higher than typical pressures encountered at their design depths. With an economically viable wall thickness, buckling becomes a critical issue, which should be addressed, for circular shafts with very large diameters. In the design and construction of the SLS, the stability of the structure can be improved by modifying the soil surrounding the circumference of the shaft to a limited thickness and to about 10 ft below the finished shaft structure. This thick wall of soil mixed with cement creates a composite integrated structure while serving additional purposes such as ground control and ground water seepage cutoff."

Jan 1, 2016

By James W. White

From Modular's first truck-dispatching system for Phelps Dodge Corporation in 1979 to today's alliance between Modular and Komatsu, Ltd., innovation has been Modular's main product. This paper describes the growth of a mining products supplier and the philosophy and decisions behind that growth.

Jan 1, 1998

The paper describes the procedure of data inquiry on the structure of mineral production in Austria and selected results. Goal of the endeavor was to gain more tangible insights into the mining industry as a basis for regulation balancing economical, ecological and social aspects.

Jan 1, 2006

By Mary C. Jennings, Peter F. Marcus

This paper examines the dynamics of aluminum consumption (all products), scrap recovery and primary aluminum capacity for the Western World through 1995, with particular emphasis on the U.S. aluminum industry. The relationship between the prices of ingot, sheet and extruded products is also explored.

Jan 1, 1986

By S. J. Chadwick

The majority of small gold plants constructed around Western Australia were designed for short lives and treatment of oxide ores. The crushing plant frequently bore the brunt of capital cost savings resulting in inadequate design and equipment selection. The exhaustion of oxides and progressionto more competent ores is _ resulting in plant operators seeing their he majority of small gold plants constructed around Western Australia were designed for short lives and treatment of The net result of many of extended operating hours, low inability to achieve fine mill blow out in operating costs, the above is throughput, feeds and a oxide ores. The crushing plant frequently bore the brunt of capital cost savings resulting in inadequate design and equipment selection. The exhaustion of oxides and progression to more competent ores is resulting in plant operators seeing their operating costs spiral upwards. Steps taken at Jubilee mine to improve plant productivity and lower mechanical failure will be discussed. operating costs spiral upwards. Steps taken at Jubilee mine to improve plant productivity and

Jan 1, 1991

By Jim McMaster, Charles W. Kenney

The role of oxygen in cyanide leaching ia well understood in the gold industry. Oxygen enrichment has taken on a real, practical meaning to operators with the were to evaluate the effect of oxygen enrichment on the kinetics of heap leaching gold ores, to examine methods of oxygen application in the heap, and to develop preliminary economics for the process. Several series of column tests were completed increasing preaeration, applications. use of pure oxygen for leaching, and in CIL in the test program. Oxygen enrichment may have a significant place in heap leaching as well. In preliminary column tests sponsored by Kamyr at Hazen Research, Inc. , oxygen-purged columns showed an increase in both the leaching rate and maximum recovery of gold and a reduction in cyanide consumption compared to columns run with air. Potential benefits of using oxygen in heap leaching include faster leaching kinetics, shorter cycle time, higher recoveries, and more efficient use of permanent or reusable pad space. The concept requires confirmation of technical and economic feasibility on a commercial scale.

Jan 1, 1990

By Sean E. Armstrong, Deepak Malhotra

The current trend in gold ore processing is the development of lower grade or highly refractory deposits. The perplexity of treating low grade oxidized ores has been adequately addressed by heap leach technology. However, refractory gold ores are very difficult to positively characterize the gold association within the mineral matrix. Gold accompanied with refractory sulfitlc or carbonaceous mineralization can often be sub­micron In size and occur interstitially. Mineralogical examination of these ores Is difficult, expensive, and occasionally Inconclusive. Hence, the metallurgist Is given little information for the selection of processing alternatives. The purpose of this paper Is to demonstrate the use of diagnostic leach procedures to assist the metallurgist' s decision-making process to solve some of these problems. By sequentially liberating and/or leaching gold associated with specific minerals, the amount of recoverable gold in each stage can be determined. Through careful interpretation of the results obtained by diagnostic leaching, the metallurgist can devise a flowsheet for treating the ore or solve a problem at an existing plant

Jan 1, 1992

By Stuart K. Nicol, Malcolm D. Engel, Neville T. Moxon

Ion flotatir,n of gold is a process being developed to selectively float extremely dilute aurocyanide liquors using a novel surface active complexing agent. The principle of ion flotation is also applicable to a wide range of other metal-containing solutions. The market potential of the gold flotation process would be enhanced by the possible combination of the gold recovery capabilities with both cyanide recovery and metal removal. For example, recovery of copper cyanides from a return liquid strean1 would be a useful means of reducing operating costs and satisfying environmental pressures to treat tailings dams. Experimental work is described where samples of tailings solution from a far north Queensland gold mine were subjected to ion flotation to remove copper cyanide species from a clear recycle solution. The form in which these products was removed was of secondary importance compared to the need to produce a clean solution for use in the plant. Recovery of the anionic copper cyanide species was accomplished using a quaternary ammonium surfactant.

Jan 1, 1991