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By E. Sehner, G. Van Weert

Metal chloride pyrohydrolysis is a fifty year old technology, operating satisfactory in many plants around the world, mainly on ferrous chloride, The capabilities and costs of its two equipment options (spray roaster and fluid bed pyrohydrolysis) are well known. Why is the technology not more widely used in mineral processing, beyond the production of MgO and upgraded TiO2slag? After briefly reviewing chloride vs. sulphate process characteristics and existing plant operations, this paper will discuss pyrohydrolysis options for the mine developer using the processing of ilmenite, siliceous zinc oxides and oxidic nickel / cobalt ores as examples.

Jan 1, 2003

By Gary A. Kordosky, R. Brantley Sudderth

The solvent extraction process as it applies to the recovery of metals from solutions on a comnercial basis is described. The four types of classes of sol vent extraction reagents are explained: 1) solvation, 2) acidic, 3) ion-pair, and 4) chelation, and examples of each type of reagent system are given. The uranium and copper extraction examples, using the ion-pair and the chelate reagent types respectively, are presented in greater detail to illustrate the more subtle aspects of reagent evaluation and selection. Practical experiences in the laboratory and at some operating plants are a1 so discussed.

Jan 1, 1986

By Eric C. Schwamberge, Clem A. Pelletier, Deborah L. Muggli, George W. Poling

The Pit Lake at Island Copper has evolved into a 3-layered meromictic system. Acid Rock Drainage (ARD) is collected and injected into the lake at 220 m depth via 2 diffuser systems. In situ dye studies were conducted during 2 differing hydrological regimes in order to determine the behavior of the ARD plume within the Pit Lake. Results indicated that when runoff from the waste dumps was low, the injected ARD remained within the bottom half of the intermediate layer of the Pit Lake, initially below depths of 90 m. However, when runoff from the waste dumps was high, the injected ARD at -220 m depth rose through the intermediate water column layer rapidly, but did not breach the top pycnocline at -10 m depth. Overall, the system is currently performing as a mixing bowl with a strong boundary or cap at the upper pycnocline. maintaining mixing below the 10 m depth water level.

Jan 1, 2000

By Andrew I. Hustrulid

The discrete element method has successfully been used to model the behavior of material flow in transfer stations. With position, velocity, and applied forces for every particle and boundary in the simulation available at increments of 10-5 seconds, the next critical step is the presentation of this data in a concise and beneficial form. This paper discusses several methods of presenting the data from discrete element simulations that are used to improve the performance of a transfer station. These measurements are also used as a learning tool to better understand and visualize how material transfers from one belt to the next.

Jan 1, 1998

By L. M. Petrie, D. C. Marozas, S. E. Paulson

The US Bureau of Mines (Bureau) is conducting research to evaluate the potential for developing an in situ leach mining process that will selectively extract manganese from oxide ores, leaving gangue relatively undisturbed. To accomplish this, a geochemical approach based on deposit-specific information, such as mineralogy and geology, is used to constrain the operating parameters of the system. Among the studies being conducted are: • leaching experiments to define reaction mechanisms and kinetics, • detailed petrologic characterization at the microscopic scale to assess manganese distribution and leaching efficiencies, • deposit characterization and evaluation, and • development of potential manganese recovery schemes. Data from these studies are being used to develop engineering design information for an in situ mining process. Specific details of the Bureau's research project are discussed, including results obtained to date.

Jan 1, 1993

By A. Bleier, E. D. Goddard, R. D. Kulkarni

The influence of the collector structure on the amine (RNH2, R=alkyl) flotation of quartz has been systematically investigated using a modified Hallimond microflotation cell. This study focuses on the effect of varying chain length, branching in the alkyl group R, polyfunctionality of the collector molecule, and alkyl substitution on the nitrogen atom. In addition, adsorption at the solution/air interface and electrokinetic results for the solid/solution interface were employed to further elucidate the role and the interrelation of the structural parameters in the flotation process. Estimates of an electrical double layer attractive energy between the bubble and the solid particle are made.

Jan 1, 1976

By F. N. Kissell

The US Bureau of Mines undertook a study of those factors influencing worker escape from an outby coal mine fire. The results of this investigation were two-fold. First, those factors affecting escape from a mine fire were defined, and second, the relationships between these factors were identified. Although the individual components had been studied before, little information was available on their interdependence. Fault tree analysis was used to evaluate the miner escape scenario. After constructing the fault tree, a two-phase analysis of the tree was conducted. During the first phase, the minimal cutsets of the fault tree were identified and ranked. These sets were the smallest sequence of events leading to fatalities during the fire. This ranking revealed that reduced evacuation delays, improved self-rescuer training, and improved stopping construction were important in controlling fatalities during escape from the mine fire. The second phase involved additional analyses of the fault tree. These evaluations were started by first determining occurrence probabilities for each event in the fault tree. Two types of sensitivity analyses were then conducted. The first analysis dealt with changes in event probabilities and their impact on the likelihood of fatalities. The final sensitivity analysis considered dramatic reductions in the probability of fire fatalities. This revealed what event probability values were necessary to reach this level. These results have revealed various remedial actions that could be used to improve the survivability of an outby mine fire.

Jan 1, 1990

By J. T. Crawford

Computer techniques for open-pit limit analysis were introduced into Kennecott Copper Corp. (KCC) during the early 1960's. The first computerized approach used block matrix mineral and economic models, and a removal increment mining simulator. A detailed description of the approach was published in the May issue of Mining Engineering (Carlson, et al., 1966) and also in Chapter 30.3 of the SME Mining Engineering Handbook (Pana and Davey, 1973). Since then, many refinements have been made to improve the system and the resulting pit limit design. The fundamentals, however, generally remain unchanged. Computerized open-pit limit analysis is presently used by Kennecott's open-pit copper properties and by the Quebec Iron and Titanium Corp. The system and the fundamental evaluation techniques it represents are cornerstones of all open-pit mine planning activities within KCC. This case study describes a typical example of open-pit limit analysis within KCC. The case involves a copper sulfide porphyry deposit with additional minor amounts of molybdenum, gold, and silver. The ore-grade mineralization within the pit design will be mill feed for a sulfide ore concentrator, and subore grade mineralization will be classed as waste and placed on dumps. The contributions to production and profits from dump leaching are insignificant, having minimal effect on the pit economics and design, because the material responds poorly to leaching solutions.

Jan 1, 1979

By J. W. Stevenson

The need for a separate ventilation department within the management team was recognized by the management of U. S. Pipe and Foundry before the company was purchased by Jim Walter Corporation in January, 1970. Because the coal beds of the deep underground coal properties owned by Jim Walter Resources lay 1300 to 2200 feet below the surface, efficient mine ventilation practices are essential through shaft openings varying from 16 to 22 feet in diameter. The extremely high methane gas quantity indicated to be in the coal bed because of the depth of cover and documented by various U. S. Bureau of Mines tests and demonstrated by early mining proved the need to implement this early management decision. At U. S. Pipe and Foundry mine ventilation was a function of the Mining Engineering Department with ventilation personnel assigned to the mine receiving their day to day work assignments from the mine manager or mine foreman. At Jim Walter Resources, the General Manager - Ventilation reports to the Senior Vice President, Mining Engineering, who reports directly to the President, Mining Division, Figure 1 (Company Organization Chart). Position descriptions are static; however positions are dynamic and consequently the degree of emphasis of specific duties and responsibilities change depending not only upon the aptitude of the individual performing the job but also upon his ability to meet the needs of his supervisors; and ultimately upon his ability to react to the economic forces directing our society. The following describes the duties and responsibilities of the General Manager - Ventilation, Figure 2.

Jan 1, 1980

By Andrew Neale

ERIC GUTIERREZ: With that, we'll go ahead with the final speaker of the day, Andrew Neale. Andrew has a master's of science degree in mineral processing from the University of Alberta. He worked at the Falconbridge in Sudbury area, also at Brenda Mines, and then he became part of the Brenda Process Technology group in British Columbia. He joined Freeport in late 1993 in Indonesia, and was involved in process control and automation. He is now the senior manager of metallurgy in New Orleans. He's responsible for designing Freeport's new 100,000-ton-per-day expansion concentrator, which is currently being commissioned. Please welcome Andrew. ANDREW NEALE: With the ongoing explosion in digital computing power, there seems to be no limit to what can be modeled, simulated, and controlled in the mineral processing plant. However, at each stage of development of a control system, it is necessary to complete a cost-benefit analysis for justifying the move to a higher level of control. Incremental improvements in plant performance, while often significant, must be weighed against the costs of implementation and long-term maintenance. This presentation will provide examples of what the author believes are misplaced or misguided process control efforts and make a case for the KISS principle as applied to process control.

Jan 1, 1998

By G. Bloomsburg, R. E. Williams, S. D. Vincent

A modeling scheme is developed to simulate the hydrogeologic effects of mine design and development in unsaturated rock. Simulations are conducted using the UNSAT2 finite element computer program and hydrogeologic data from the site of a proposed mined-out waste repository at Yucca Mountain, NV. Results of the simulations are analyzed for: •variations in the direction of ground water flow and in the distribution of pressure head caused by the design of the mined out openings; and •mine design variables that affect the predicted rates of mine water inflow. Evaluating the hydrogeologic impacts of mine design and mine development in unsaturated rock is significant in several respects. Characterization of the preemplacement of wastes along the fastest path ground water flow system at the Yucca Mountain site has been a primary research effort. Ultimately, however, the degree to which waste isolation is achieved will depend largely on the post-mining hydrogeologic environment as altered by the mine design and on the radionuclide inventory and resulting heat effects of the repository. Therefore, an ongoing characterization of the proposed mined-out nuclear waste repository at Yucca Mountain, NV, is recommended. Modeling results indicate that: •mined out openings will affect the movement of ground water, both in rate and direction; •hydraulic effects of mine development depend on the hydrogeologic environment and on mine design geometry; •mine water inflow is possible in the unsaturated zone, even for mines developed in hydrogeologically homogeneous rocks; and •mine water inflow can occur at values of down ward flux that are appreciably less than the saturated hydraulic conductivity of the overlying rocks.

Jan 1, 1991

By H. J. Marais, P. C. van Aswegen

The Biological Oxidation (BlOX®) Process for the treatment of refractory gold ores was commercialized in 1988. During the last decade, the technology has developed into a mature, commercially viable process, with five additional operations commissioned, including operations at Sao Bento in Brazil, Harbour Lights and Wiluna in Australia, Ashanti in Ghana and Tamboraque in Peru. With ongoing development, the efficiency and cost effectiveness of the process have both improved, making it an attractive alternative to conventional refractory treatment processes such as roasting and pressure oxidation. The bacterial culture is robust and can withstand the normal fluctuations experienced on an operating plant. The plants are simple to operate, making it ideal for remote areas. The scale-up potential of the process has been proven, and it can be applied to large refractory ore bodies. The process is environmentally friendly. Neutralization of plant effluents produces precipitates that comply with the most stringent environmental regulations.

Jan 1, 2000

By Leonard G. Austin

INTRODUCTION Run-of-mine (ROM) coal generally falls into two major groups: that from underground mining (continuous mining machines) and that from strip mining. Continuous miners produce a finer product and strip mining a coarser product that is crushed to produce the desired size. Further size reduction depends on the proposed use or uses for the coal. For example, for pulverized coal power plants as a rough general rule, the coal is ground or pulverized to 80% less than 200 mesh (0.075 mm) before it is blown into the boiler furnace as a coal-air suspension. For solvent-refined coal processes, the desired size is about <30 mesh (< 0.60 mm); in fluidized bed uses, the coal is typically < 8, in. (< 1.6 mm); for Lurgi pressure gasifiers, the desired size is 1 to 2% in. (25 to 63 mm). Coal preparation plants typically work with a coarse size fraction of 6X 1/14 in. (150X32 mm). The past decades has shown a steady increase in the tonnage of coal cleaned, 1 but it seems probable that the next decades will produce much wider applica- tion of deep coal cleaning before use and that the stages of crushing and pulverization from ROM coal to end use will be integrated with coal cleaning processes. Since different cleaning processes work better with different ranges of coal size and the degree of cleaning possible is intimately connected with the size of coal, a systems design engineer will need as much information as possible concerning the size distributions produced by different types of machines and how these can be modified by different ways of operating the machines. In general, the following questions will be of concern: 1.What type of crusher or grinder is best, or most satisfactory, for reducing a given feed size and type of coal to a desired product size? Frequently, the desired product is smaller than some nominal size, but with as few fines as possible, or the fraction in some size range has to be as high as possible. 2. How big does the machine have to be for a given throughput rate? 3. How much electrical energy (or its equivalent) is required per ton of product? 4. How does the size distribution vary with change in throughput rate, and is a control scheme necessary or desirable? 5. Can the size distribution be readily varied if desired? 6. What is the optimum way to operate a machine in a given system? This section will emphasize certain general principles which guide us in answering these questions. PARTICLE SIZING Since particle size and size distribution are the raw information with which we work, it is worthwhile to review the terminology used. In this regard, see

Jan 1, 1991

By M. C. Roberts

Metal producers are now suffering through a major downturn in prices for their products even though it has only been a few years since they were enjoying high prices. From an historical perspective, the current situation is another of the cyclical downturns that often occur every five to seven years. This paper uses time-trend decomposition techniques to identify the cycles and statistical methods to find the duration of these cycles for a variety of metal prices. Given some idea of how long and severe these cycles typically are, the mining industry can better plan to weather the downturns and take advantage of the upturns. For example, timing investments in new projects to take advantage of the cyclical upturns can dramatically improve project profitability.

Jan 1, 2003

By David R. Reid, Lawrence W. Talbot

INTRODUCTION In the mining industry, timing in land acquisitions can be of the essence. In order to secure promising lands, deals are often negoti- ated quickly and evidenced by letters of intent containing what the parties feel are the essential terms of the deal. In some cases, a company is willing to acquire land only if it can lock up a number of promising properties, and so a "non-binding" letter of intent is used to formalize the essential terms, while leaving the company without legal liability. Later, the letters of intent will be sent to a lawyer to prepare a formal acquisition agreement. Many times, how- ever, especially in a land acquisition rush, another company will attempt to better the deal prior to the execution of that formal agreement, and the first company will be forced to rely on the initial letter of intent, only to find out to its chagrin that it has no deal In other cases, the company holding the desired property is another mining company, and the negotiation of an option or joint venture is the only way the first company can acquire an interest in the desired land. In order to make its offer more attractive, it may have to reveal confidential or proprietary information about the property or the surrounding lands. Here, too, letters of intent are often used to formalize the essential points of the agreement. Once again, however, prior to the execution of a formal joint venture agreement, the transaction may collapse and the letter of intent prove to be only that. In this paper, the authors examine the dangers associated with the use of letters of intent and the specific provisions courts look for to find a binding contract, and consider how to increase the

Jan 1, 1988

By John O. Marsden

Technology development has played a crucial role in the minerals industry throughout history. The development of new technology allows mankind to produce metals and minerals at progressively lower cost of production in real terms, and therefore at progressively lower prices, improving their availability, accessibility and utilization worldwide. However, the developers of such technology are not guaranteed to reap the benefits from this effort: There is an expectation that technology developers will gain an advantage over their competitors. Is this a short-term benefit that results from a temporary cost or efficiency improvement, or is it a sustainable longer term "edge" that prevails even after metal or mineral price has been eroded by the implementation of a major step change technology? This issue is examined by reference to several case study examples in the copper industry. BACKGROUND The development and adoption of new technology has played a crucial role in the commodity minerals industry throughout history. As new, cost-efficient technologies are commercialized, the cost of production decreases, and this enables lower grade ore to be processed profitably. This in turn increases the availability and supply of the metal or mineral of interest, and ultimately (in a free market environment where the supply- demand balance determines price) inevitably decreases the metal or mineral price. This leads to the question: Why should mining companies invest in (new) technology development if the result is a decrease in the product price? The answer is to achieve competitive advantage, where the application of new technology enables one or more

Jan 1, 2004

By B. J. Arnold, B. W. Parker

Rosebud Mining Company added a classifying cyclone/spiral concentrator circuit addition to its McVille Preparation Plant, Freeport, PA, in mid-2002. This paper will describe the plant addition, which was implemented fully by plant staff, and review improvements in cleaning plant performance and economics.

Jan 1, 2003

By Graham Swan, Richard K. Brummer

The paper begins by describing an underhand cut-and-fill mining concept for a 50m thick, generally tabular though irregularly shaped orebody dipping at 30 degrees and occurring at a depth of between 2300 and 2700m in the Sudbury Basin. From this, the broad design requirements of a fill system are stated. Two and three-dimensional numerical models are then described which were built to evaluate the theoretical benefits of different types of fill reinforcement. Included in this evaluation are the effects of span, fill strength, fill tightness, as well as static and dynamic loading types. Results, supported by large-scale physical models, are presented to show the significance of reinforcement on stable, undermined fill performance. Finally the paper describes work which has been done to evaluate the suitability of so-called silicated cemented backfill. This system is, in principal, attractive for deep mining applications since transportation is in the "safe" hydraulic regime, while fill water run-off, segregation and shrinkage effects are potentially eliminated in the stopes. The results from various surface and underground trial pours are reported which substantiate the proposed use of this type of backfill at depth.

Jan 1, 2001

By J. D. Decker, T. E. Norman

Introduction Grinding is the reduction of ore and similar raw materials to particle sizes below the practical limits of commercial crushing ma¬chines. This size is about 36 in. (1 cm), in most cases, although some finer crushing machines are in regular use. The feed size to grinding machines may range upward to S in. in rod mills, and 12 in. or more in autogenous mills. The finest particle sizes produced in mineral processing operations result from grinding. Ordinary grinding of brittle materials is the result of impacting, rolling, and abrasion of heavy bodies, moving freely under the influ¬ence of gravity. These falling and rolling grinding bodies, which are usually of metal, must be much heavier and larger than the ore parti¬cles they break. This weight relationship is usually in excess of 100: 1. The sustained fall of the grinding bodies is obtained by placing them, together with the rock particles they grind, in a rotating drum or cylinder with horizontal axis, called a tumbling mill. The mill is nearly half full of grinding bodies and ore particles, which may be fed into one end and exit from the other through hollow trunnions which usually serve as the mill bearings. The mill lining must be thick to absorb wear and rough to prevent excessive slippage of the charge. The breakage of brittle rock or ore is accomplished by compression. The compression may be a rapid impact, from the fall and roll of a grinding ball, or it may result from the relatively slow and constrained motion as in a jaw crusher. Breakage by shear is a secondary result of the compressive motion. Ordinary rock has an extremely heterogenous structure with innumerable zones of weakness in which cracks, fractures, and breakages can form. When a rock is subjected to com¬pression it deforms. If the compressive force exceeds a certain critical value an incipient crack appears in the most fragile zones of weakness. This crack tip may first form on the particle surface or in its interior. When the first crack tip forms the compressive stresses immediately surrounding it flow to it, and this concentration of forces extends the crack and splits the rock. Other adjacent cracks may form during this extremely rapid process. Because of the nature of brittle particles, the work done in breaking them consists essentially of the work input required to compress them to the point at which the first crack tip forms. Breakage requires no appreciable additional energy input be¬yond that required for the deformation, since the stress energy already imported to the rock flows to the crack tip and extends it to breakage. Types of Tumbling Mills The general term tumbling mill includes the rod mill, ball mill, pebble mill, autogenous mill, and tube mill. It is of cylindrical or cylindro-conical shape and rotates about its horizontal axis. Rotational speed, liner type, and size and shape of tumbling media are selected to provide the desired operating conditions for the specific grinding application. Openings are provided through the mill ends for feed and discharge of the material being ground. A common feature of tumbling mills is the use of tumbling media

Jan 1, 1985

By Robert L. Virta

An asbestos substitute is any material that replaces asbestos in a commercial product. There are many asbestos substitutes, each with its own unique physical and chemical properties. Substitutes can be inorganic or organic, fibrous or nonfibrous, and natural or synthetic. They also can be used as a direct substitute for asbestos or as a replacement product. Probably in no other field is the diversity of substitute materials so great. The concept of asbestos substitutes is not new. The first major effort to develop asbestos substitutes was undertaken by the federal government. The United States has always been dependent on foreign sources for strategic-grade asbestos, and during World War II, the government was concerned that these supplies would be cut off. Strategic-grade asbestos was critical in many electrical and thermal insulation applications (electrical insulation, battery plate separators, flame-proof boards, insulation for rocket components, etc.). A reliable supply of nonstrategic-grade asbestos also was required for general civilian and military applications, such as in brakes, clutches, and construction materials. The government not only initiated a major search for deposits containing strategic-grade asbestos, it also funded research on synthesizing asbestos in the laboratory and developing products that did not contain strategic- grade asbestos. These efforts, as well as those conducted by the private sector, generally were unsuccessful. In the late 1960s and early 1970s, a second major effort to develop asbestos substitutes began because the general public was concerned about the health threat posed by the release of asbestos fibers during the manufacture, use, repair, and disposal of asbestos-containing products. Strict regulations covering the mining and manufacturing sector already had been enacted because of the issue of occupational exposure. The issue then became environmental exposures. Environmental regulations were enacted, and through time they became more strict. The combination of increasingly strict environmental regulation, maturing of some asbestos markets, and liability issues prompted many manufacturers to discontinue asbestos product lines or search for asbestos substitutes. As a result, asbestos usage dramatically declined from the 1970s to the present (Table 1).

Jan 1, 1994