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By Peter J. Alderson, M. P. Evans

The application of conveyor belting in bulk materials handling is crucial to the success of most mining enterprise selection of the cover rubber grade and thickness has a direct bearing on the cost per ton conveyed. Current and future demands placed on belt covers by higher speeds, increase capacities and greater lifts means today's cover will not be adequate for tomorrow's applications. The simple selections of RMA Grade I and I1 and MSHA above and below ground need to be expanded upon. This paper describes various new approaches for selecting conveyor belt covers for specific applications. It also presents examples of material and compounding techniques available to the belt manufacturer to improve the performance of their covers.

Jan 1, 1996

By N. K. Riddle

In many mines, it is typical to stockpile material for milling based either on analyses from exploration and blasthole drilling, or on the observation and judgment of experienced personnel. New analytical instruments make it possible to perform multiple, rapid analyses of as-mined samples at or near the mining face, so that sorting into stockpiles can be much more accurate. Using data and operating practices from a phosphate mine, a model was developed to simulate the function of analytical instruments in ore-grade control and ore stockpiling. With this model, it is possible to determine the recommended sampling points and sample frequency to obtain the desired confidence limits on the stockpile analyses.

Jan 1, 2003

By Stephen B. Doppler

INTRODUCTION Following the world stock market debacle in October 1987, it would have been foolhardy to expect that securing equity funding in 1988 would be easy. Indeed, major equity financing's for gold mining companies have until recently been few and far between in the weeks and months following Black Monday. As a result, gold bullion loans have taken on an increasingly important role among producing firms in the industry. During 1988, the role of bullion loans has become increasingly complex and controversial. Some observers herald the emergence of a new breed of bullion loans - such as the 1,000,000 ounce loan to Newmont Mining, and the 400,000+ ounce facilities drawn down by Bond International Gold and Placer Pacific - as both increasing the public's awareness of the technique, and representing the dawn of a new age of gold financing. But are these recent loan facilities significantly different than those issued worldwide during the early to mid 19801s? Similarly, observers have voiced concerns regarding the role that gold loans play in the world's bullion markets, specifically in relation to their impact on prices. Have the new generation of mega-loans depressed current and future prices? Has the current surge of bullion loans irrevocably changed the nature of the gold market? Is there an upper limit on the number and size of gold loans?

Jan 1, 1988

By Ramon S. Pizarro, W. Joseph Schlitt

Introduction Trying to synthesize innovations occurring in gold processing is not simple. At present, this technology is exploding, brought about by the high price of gold. This price has compelled the mining industry, as a matter of survival, to produce gold. The frantic search for gold deposits continues, from glacial areas to tropical jungles. The search has been fruitful. New exploration techniques have helped to locate deposits. Some are amenable to conventional processing techniques. Others are in unusual settings that challenge the ingenuity of extractive metallurgists. Ore deposits containing traces of invisible gold, refractory mineralization, and impurities and deleterious materials that previously defied treatment are now being profitably processed. Metallurgists have developed various processing methods and equipment for gold ore treatment that reflect differences in ore characteristics, grade, mineralogy, reserves, topography, climate, and location. These processes can be categorized as: • For nonrefractory or readily leachable gold ores - vat leaching, heap leaching, and agitation leaching. • For ores containing free gold - gravity concentration methods, followed by mercury amalgamation, and • For refractory gold ores - flotation, roasting, pressure oxidation, followed by cyanidation leaching. In actual practice, a combination of these processes may be required. This is because gold mineralization, although usually simple, may be associated with other mineral species or with clays that make the ore difficult to treat. Furthermore, after the gold has been solubilized to form a cyanide complex, one of two important processes must be applied to recover the gold. These ore zinc cementation (Merrill-Crow process) and Carbon adsorption, desorption, and electrowinning. New techniques for leaching and recovery are also advancing. These will become the bases for the next generation of gold processing plants. Nonrefractory Gold Ores Nonrefractory ores with readily leachable gold are among the .easiest to treat. Even so, non-refractory ores from epithermal deposits are likely to contain too much clay. When these ores are damp, they may clog the screens and cone crushers. Depending on the type of process, scrubbing the crushed ore is very effective in overcoming clay problems. After dewatering, the slimes enter the cyanidation process and the thickener overflow is stripped of gold values and recycled. Semiautogenous (SAG) mills are also gaining popularity due to lower capital costs and ability to treat wet, sticky ores. If properly sized, the secondary crushing and screening plants, together with a secondary ball mill, can be eliminated. When the ore is of such a low grade that it can not support fine grinding, vat or heap 'teaching may be applicable. These systems are being actively applied in the US and elsewhere. Rapid construction and low capital costs are important features of these plants. Vat leaching is ideally suited for fast leaching ores and small tonnage deposits located in areas with harsh winters or wet tropical climates. For effective vat leaching, the ore is crushed to less than 25 mm (1 in.), agglomerated with lime or cement to control fines, and leached with sodium cyanide solution (upflow or downflow). The degree of size reduction is a tradeoff between increased costs of comminution and improved gold recovery from smaller particles. However, the size of material

Jan 11, 1984

By M. Takayasu, J. Y. Hwang, F. J. Friedlaender, G. Kullerud

Al unite has been used as raw material for producing alumina and potassium sulfate fertilizer in Russia for many years. In the United States, this mineral has not been commercially processed though reserves of 5 to 10 billion tons of alunite ore have been estimated. Major constituents of these ores are quartz and alunite. The minerals are finely intergrown and liberation occurs below 10 µm. Adequate separation techniques for such ultrafine particles have not been developed. A new method for the beneficiation of al unite ore is proposed in this study. This method utilizes a small amount of fine magnetite upon which the liberated quartz is selectively flocculated. The co-flocculated magnetite and quartz are then separated from the alunite in a high gradient magnetic separator. Clean products, e.g., an al unite concentrate of 90% grade with 80% recovery, has been obtained from Utah ore. Techniques for selective co-flocculation of magnetite and quartz, separation of the carried quartz, and recovery of magnetite after separation are discussed.

Jan 1, 1987

By William Mayrsohn

IMTRODUCTION The marketing aspects of a new precious metals property is often not considered until the mine actually begins production. At this point in time it is often too late or too expensive to change the mine's final product and not enough time to do an effective marketing program. MINE PRODUCT The rule for determining the mine's final product: The higher the gold and silver content, the greater return of metal at the lowest post-mining cost. . Dore Bullion: Most advantageous Advantages: - Highest return of metal. - Lowest refining cost per ounce of gold and silver. - Very compact and easy to ship in small quantities. - Easy to assay. - Assays between mine and refiner are comparable. - Melt losses are very small at the refiner. - Outturn of gold and silver 20-30 days for quick cash flow. - Gold/silver refiners can return or purchase metal soon after arrival at a nominal financing cost.

Jan 1, 1987

By L. Stas

The authors have been interested in stress measurements in the rock mass for a long time. This paper describes the development of new apparatus for stress measurements in a rock mass. The principle of stress measurement by this device is based on the relief method as applied on the conical shaped surface of the bottom of a borehole. The design started based on the experience of K. Sugawara and Y. Obara who have been using the compact conical borehole over-coring system (CCBO). The conical shape of the strain gauge probe CCBO makes the fixation of the probe in borehole easy and, also, makes the measurement of stress in independent directions possible. The principle of the measuring method, the preparation of the borehole, the design of the probe for continuous measurement of stress during the course of overcoring are described. Also, a simplified version of the probe for long term monitoring of stress variations in the rock mass by means of the inserted body method and the initial laboratory results and in-situ testing of the development sample are described. Additionally, testing was done regarding the possible glues in relationship to the creep effect for this case.

Jan 1, 2006

By R. E. Gertsch

A mobile-modular carbon adsorption mill design and operation for small to medium sized heap leach precious metal mines is presented. In the mobile-modular strategy, charcoal columns with adsorbed metal move from small strategically located carbon adsorption loading stations to a central stripping facility and back. The design has many advantages: 1) It scales-up from pilot plant to full production. 2) It has low capital requirements. 3) Operational costs are competitive with other systems. 4) Mill production can react quickly to changes in ore grade or property area. 5) The solution circuits are simple and easy to maintain. 6) Charcoal damage is reduced.

Jan 1, 1993

By Donald L. Gaughenbaugh

Under the terms of the 1970 amendments to the Clean Air Act, the EPA established national ambient air quality standards for a number of pollutants. Sulfur dioxide (SO2) was one of these pollutants. These ambient air quality standards have had perhaps their biggest impact on the power utilities. In an effort to meet the air quality standards set forth by the EPA, utilities using high sulfur fuels have been forced to install flue gas desulfurization (FGD) systems. The majority of FGD systems in operation today are nonregenerable systems, that is the by-product of the system is disposed of, usually into settling ponds. Limestone slurry is the most common reagent used to remove SO from the flue gases. The calcium carbonate (limestone) slurry interacts with the flue gas, absorbing the SO2 and forming a by-product of calcium sulfate/sulfite which is disposed of.

Jan 1, 1986

Direct force measurements were conducted using an atomic force microscope (AFM) to study the mechanism of copper-activation of sphalerite. The force measurements were conducted between a sphalerite plate and a hydrophobic glass sphere in xanthate solutions of various pHs. The glass sphere may represent the hydrophobic air bubbles interacting with minerals during flotation. The force measurements conducted with unactivated sphalerite in 10') M KEX solutions did not show the presence of hydrophobic force. On the other hand, the results obtained with copper-activated sphalerite at pH 9.2 and 4.6 showed strong hydrophobic forces. However, the results obtained at pH 6.8 showed no evidence of hydrophobic force, which provides an explanation for the difficulty in floating sphalerite at neutral pH.

Jan 1, 1998

By E. R. Hoskins

The Gulf Coast States ranging from South Texas to Alabama contain vast resources of lignite ranging in energy content from about 4000 to 7000 Btu/lb (as-received) with sulfur content ranging from about 0.5 to 2 percent. Currently, the strip mining rate is about 35 million tons per year in Texas and essentially zero in the other Gulf Coast states. Estimates of future mining rates are as high as 310 million tons per year by the year 2000 with 240 being in Texas. In this paper, we examine the life cycle of the surface mineable lignice based on the most recent estimates of surface mine recoverable resources with two scenarios. The first indicates that a 310 million tpy rate could be sustained for only 15 years while the second scenario suggests that the 310 million tpy could be sustained for 25 to 30 years. If lignite resources are required beyond those that are surface mineable, the deep basin lignite will be developed. Five strategies for developing deep basin lignite are discussed.

Jan 1, 1983

By Huaiyu Liu, Shan Liu, Dashang Chang, Maixi Lu, Yaqun He, Yali Kuang

The expert system for coal preparation plant design mainly solves the crux--separation flowsheet design and optimization of product structure. There are twelve basic flowsheets available in the system which are representative of financial plants. The system can select better flowsheets automatically according to the property of feed and scale of plant. Then, it can choose the best flowsheet and product model from the better flowsheets through analysis and optimum calculation. The expert system is made up in Turbo Pascal 6.0 and consists of three sub-systems: Lump and grain coal system, coal slimes processing system, and raw coal system. Several representation methods, such as production rule, procedure, and object-oriented programming, are used to express the expert's knowledge in the system. To decide the optimum product structure, Zangwill's method is used to make an advance product model. The expert system has the performance of interpretation strategy, by 'tracer" technology and pre-arrangement text, and of learning new expert's knowledge.

Jan 1, 1996

By Q. Xu

The new process consists of the selective coalescence of fine hematite particles by fine magnetite. The gangue minerals are dispersed by some dispersant; thus it can be separated by desliming. This process is particularly suitable for fine-grained hematite/magnetite-type deposits.

Jan 1, 1989

By Gerhard Mücke

Geothermal and operational reasons in the German coal mining industry make it necessary to an increasing extent to climatize coal faces and headings by means of refrigeration plants. Air coolers installed on coal faces as well as in gateroads play an important part in such climatization. They must transfer, under difficult conditions, the refrigerating capacity supplied by central or de-central refrigeration plants from the chilled water to the air in the workings. The performance data of two new types of coalface coolers and of two different types of gateroad coolers were measured in two testing stations under different thermo- dynamic conditions with dust-free fresh air. As air coolers must be installed particularly at working points with a high .dust load the heat exchanging surfaces are fouled for the most part causing an essential reduction of the refrigerating capacity. The investigations therefore were extended to measurements with a certain dust load in the intake air of the coolers.

Jan 1, 1980

By Kal V. S. Sastry

Mineral processing simulation has come a long way since its beginning about thirty years ago. With our increased understanding of mineral process systems and the advent of new software and hardware technologies, we can visualize an ideal mineral processing simulator. This paper attempts to identify a number of desirable features of an ideal mineral process simulator and to describe the exciting trends in making such an ideal simulator a reality.

Jan 1, 1992

By E. M. Frizzell

In an effort to economically and efficiently enhance the erosion control aspects of present surface coal mine reclamation practices, the US Bureau of Mines has recently completed a two-phase research program wherein irrigation strategies and equipment developed under the first phase were field tested on three surface coal mine sites. The fundamental basis for the use of irrigation as a reclamation tool is to provide the plant moisture requirements as a supplement to prevailing natural precipitation, and thereby support the natural growth of drought-hardy native vegetation. Portable solid-set irrigation equipment and several irrigation strategies were tested on large 6-ha (15-acre) sites in Montana, Wyoming, and New Mexico. Results of these tests will be presented which include daily irrigations, precipitation levels, soil moistures, climatic data, and density cover and biomass of the native plants.

Jan 1, 1987

By Thomas Oberndorfer

Recent publications indicate that there is a rising interest in the field of mining method selection, and increasing efforts are being undertaken to develop satisfying solutions. Yet, computer assistance for mining method selection (MMS), or in other, terms assistance in the (pre-)feasibility state of a project, still lags behind the computer application in other mining activities. This is true for research as well as for application. This paper is intended as a contribution to the development in computer-assisted mining method selection, and focuses especially on underground hard-rock mining. It is structured in four main parts. The first deals with general aspects of mining method. selection within the process of mine planning, and with problems and requirements which derive from this specific situation. In the second part some numerical MMS-approaches hitherto published are briefly introduced, and investigations on these approaches are discussed. Based on .these experiences, in the third part an analysis of the complex system MMS is presented. It focuses on heuristics, influencing factors, objectives, assessment-routines and mining methods, and emphasizes the essential necessity of a profound mining method description (MMD) specially developed for the requirements of MMS and numerical processing. Accordingly the fourth part of this paper presents a mining method description model developed at the Department of Mining Engineering, Montan-University Leoben (MUL), Austria. It describes the consequences of the investigation, in particular the new mining method description model, on 'the design of a MMS-system. The paper closes with a outlook on the possibilities of an successful MMS-system being realised.

Jan 1, 1992

By M. Dosemeci, M. McCawley, J. McLaughlin, Z. Wu, F. Hearl, W. Blot, K. Peng

Proposals have been made by two organizations, the International Standards Organization (150) and the American Conference of Governmental Industrial Hygienists (ACGIH) for a revised respirable dust criteria and criteria for thoracic and inspirable dust. These criteria yield different results than criteria based on lung deposition patterns in assessing the hazards due to dust exposure. Since these differences are a function of the size distribution of the dust an analysis of dust size distributions from various mining operations was performed to determine the amount of difference that could occur. The dust size distributions available for this analysis were taken from U.S. coal mines and from Chinese metal mines. The mass of mechanically generated dust that will deposit in the alveoli was found to be in direct proportion to the ISO/ACGIH criteria estimates in the mines studied. Therefore, respirable dust estimates for substances such as coal and silica are not a problem. Estimates of exposure to diesel exhaust in these mines, however, were not always in the same proportion to the estimated alveolar deposition. Also, concern with an excess of bronchitis among miners may not be adequately addressed by the use of samplers conforming to the ISO and ACGIH criteria. The cascade impactors used to acquire the data for this analysis require four to eight substrates per sampler. For daily dust exposure assessment this method is cumbersome and time consuming. Therefore, two new samplers have been designed to meet the need for determination of deposited dust mass. These samplers follow the lung deposition curve rather than the penetration curves proposed by the ACGIH and ISO and require analysis of only two substrates per sample.

Jan 1, 1992

By John J. Gillis

There is an ongoing battle to gain general acceptance of fossil fuel byproducts as safe, economical and useful agro-industrial materials. Despite that, the US ash industry is witnessing a steady growth in the volume of coal burned, along with the production of greatly refined, higher-quality ash particulates. There are two principal reasons for this. Economics have caused an increasing number of US electric utilities to convert from oil-burning to coal-burning. And the Federal government has tightened specifications on fly/bottom ash production quality. Hence, it must be noted that new and more stringent Federal regulations were implemented in 1980. The resultant ash particulates are finer, more compact, and less heavy than in previous years. Additionally, the first shift from oil to coal in the US was initiated in December, 1979 by the New England Power Co. in Massachusetts. Coal is the most widely-distributed fuel in the US. And it is found in 38 states. The wide availability of this fossil fuel and its general cost-efficiency, coupled with the undaunted move of US electric utilities toward nuclear power, are major factors affecting the current statistics on ash generation (65.4 x 106 million tons). Interest in the use of coal in power plants is creating a unique ash disposal and use situation for ash producers as well as the Federal government. There are growing quantities of fly/bottom ash residue. Ash producers must decide how this byproduct can be dealt with effectively and profitably. At the same time, government agencies such as the US Environmental Protection Agency (EPA), are commissioned by Congress to assure that solid, liquid, or gaseous material released into the environment is not harmful or offensive to human health and the environment. Additionally, the Federal government is often responsible for establishing and enforcing guidelines and standards governing the use of recycled materials. Several standards and guidelines governing the properties and use of ash in the US have been established by governmental agencies as well as by the ash industry itself. Of these, some have been developed for ash use by a specific federal agency. Others apply to the entire industry. The following is a brief identification of the major specifications for fossil fuel ash: • US Corps of Engineers - These specifications were first established in 1957. They delineate the physical and chemical requirement for pozzolans used in mass concrete. These specifications applied only to Corps of Engineers' concrete construction projects for locks, dams, and other mass concrete projects until 1977. At that time, a joint effort between the American Society for Testing and Materials and the Federal government produced a modified specification that is now generally applied. The Corps of Engineers' ash, however, retained certain aspects of its specifications for its own use, particularly in the area of handling and shipping fly ash to its own projects. Prior to transporting the fly ash to the corps, all potential sources for the ash must be inspected and approved as a supply source. All silos must be filled, sealed, and tested before the ash is released for shipment. The normal test period for the ash is seven days, although several testings may require up to 28 days. Once the fly ash has been released, it can only be shipped to US Corps of Engineers' projects. All shipments are made with a government inspector present during loading. After a truck or railcar is loaded, the silo is resealed until the next shipment. This procedure requires three silos, and a minimum of 454 t (500 st) each should be considered for each storage unit. All silos are strictly committed to Corps of Engineers' use and are not available for other commercial shipments. • US Bureau of Standards - This Federal agency maintains a standard testing sample of nearly every product used in the US. The accuracy of the fly ash chemical analysis is measured by a regular cement and concrete reference laboratory (CCRL) inspection and based on test results from a standard sample of cement. • US Bureau of Reclamation - This agency pioneered several projects using fly ash and required Federal Standard Certification for pozzolans. • American Society for Testing and Materials (ASTM) - This nongovernmental organization began preparing standards for fly ash sold and used in the cement and concrete industry in 1947, at the urging of ash marketing firms. Current standards define chemical and physical requirements and is entitled, "Fly Ash and Raw or Calcined Natural Pozzolan for Use as a Mineral Admixture in Portland Cement Concrete (C 618-80)." • State Highway Specifications - Led by Alabama, many states are moving toward permitting - and in some cases requiring-the use of fly ash in portland cement concrete and with lime for base stabilization projects for roads and highways. • Federal Aviation Administration (FAA) - The FAA acts in an advisory capacity. It has final approval on design specifications for airport construction projects. The agency has established a set of guidelines permitting the use of fly ash, and has approved several fly-ash-specific designs. The most current FAA fly ash projects

Jan 8, 1984

By Gary Beerkircher

WaterFlush Technology and WaterFlush crushing offers significant operational ben­efits in gold milling operations. WaterFlush crushing is the technology that Nordberg Inc. has developed, tested and proven in an actual operation during the 1980's. Patents have been obtained for both the process and the apparatus of implementa­tion. WaterFlush involves volumetric process controlled water flow into the ore feed cav­ity of a WF cone crusher. While the addition of water in itself is not new, the con­trolled amount of water coupled with the WF crusher operating parameters are revolution­ary. The WF crusher is a specially designed version of Nordberg's Omnicone crusher oper­ating at higher speeds, with a reduced ec­centric throw and higher horsepower capabil­ity. The results are increased capacity, higher crushing energy input and a finer crusher product. The WF crusher product is a slurry containing 40-60% solids by weight.

Jan 1, 1990