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By K. O. Johnson

Contaminant transport of mine and mill tailings is controlled by the hydrologic flow regime and the geochemical mobility of the contaminants. Contaminant' mobility is primarily determined by chemical reactions occurring within an interface zone between the tailings and soil The large geochemical differences between tailings and groundwater create a disequilibrium in the groundwater with respect to the soils when seepage from tailings enters the groundwater. Precipitation and dissolution reactions involving the major chemistry occur to return the perturbed system to chemical equilibrium between groundwater and minerals. Retardation of trace elements depends upon the chemical character of the groundwater and the adsorption substrates. In the case of uranium mill tailings, the mobility of contaminants is controlled primarily by precipitation/dissolution reactions which neutralize the pH, modify the Eh (redox potential), and produce highly adsorptive substrate for retardation of trace elements.

Jan 1, 1988

By James H. Nulty, Joseph S. Roti

Wetting agents used for heap leach gold applications would appear to have technical merit in aiding in recovering higher levels of precious metal. Many questions, however, remain as to whether they will function in practice, on what type of ore are they effective and if there are any negative affects associated with their use. A series of experiments are conducted at Bateman Labs, Sparks, Nevada, to determine under what conditions reagents of this type are useful. Carbon kinetics test work was also performed to determine if there are negative aspects associated with carbon loading with the use of these treatment chemicals. This paper outlines the results of these research evaluations, the general chemistry associated with action of wetting agents on leach ores and future work which is planned to further determine the viability of these products in the mining industry.

Jan 1, 1998

By Robert S. Hendricks

The paper describes the design and operation of a Shaft Boring Machine (SBM). The machine has been developed by The Robbins Company. It is anticipated that the prototype, which will bore shafts in the 6.1 to 7.3 m (20 to 24 ft) size range, will be placed in operation during 1985. This pioneering application of rapid excavation technology is expected to lead to significant improvements in the cost and speed of shaft construction. The technical and economic factors which have limited the employment of Shaft Drilling and which caused unsatisfactory results with earlier attempts at Shaft Boring are reviewed. The design criteria adapted to overcome these problems are discussed. Cost and performance estimates are presented and are compared to conventional sinking methods. Factors that influence the application of the SBM to specific projects are reviewed.

Jan 1, 1985

The solution mining review did not arrive in time for publication in the May issue. The term solution mining is commonly used to refer to heap leaching, dump leaching, in situ mining and bore hole slurry mining technologies. The US Bureau of Mines is continuing with research in these areas. Commercial application of these technologies is progressing. There is an ongoing cooperative research project between the Bureau of Mines and the Santa Cruz Joint Venture to evaluate in situ copper mining at a field site near Casa Grande, AZ. The project is currently in the environmental permitting stage. The Bureau is preparing an environmental assessment for the project as part of the National Environmental Policy Act. The Bureau is also continuing with laboratory experiments to study the leaching characteristics of atacamite ore from the field test site, as

Jan 1, 1993

By James C. Norman

The boron review arrived too late to appear in the June issue. The US was the world's second largest producer and the largest consumer of boron compounds during 1990. Boron mineral concentrate and chemical production in the US totaled 1.13 Mt (1.2 million st), including 565 kt (662,800 st) of boric oxide (B2O3) in 1990, according to US Bureau of Mines estimates. Total value amounted to $404 million. This was slightly higher in production than 1989 but down in value, reflecting a softening in boron product prices. Total world production of boron mineral concentrate and chemical tonnage in 1990 was estimated at 3 Mt (3.3 million st), which corresponds to about 1.3 Mt (1.3 million st) of BO,. World production in 1990 was about the same as in 1989.

Jan 1, 1991

"In the mining industry, high-level commitments to adopt sustainability have been made at the corporate levels of mining companies, but there continue to be problems when attempts are made to adopt these high-level sustainability aspirations and translate them into appropriate targets and methods at the more-specific operational level. The integration of sustainability principles into day-to-day minerals processing operational decision-making processes has unique challenges that are not addressed adequately by current tools and methodologies. A proposed methodology to achieve integration of sustainability at the operational level will direct the systematic and rigorous identification and characterisation of sustainability issues in an operation. The methodology allows different approach strategies for assessment, comprehensive accounting of sustainability indicators and has the ability to identify sustainability issues which may have significant business implications that cannot be identified using traditional analysis processes."

Jan 1, 2011

By Steve Lloyd, Mary Anne Antonioli, Byron Darnton

Pegasus Gold Corporations' Montana Tunnels mine began oper­ation in March 1987. The process plant at startup consisted of a bulk flotation circuit followed by leaching of the reground bulk concentrate. The leach residue then advanced to selective Pb/Zn flotation. This original circuit had its share of problems, and the leach circuit was abandoned after six months. The bulk flotation circuit was modified to selective Pb/Zn flotation at this same time. Gravity concentration was researched early on, prior to selecting bulk flotation with leach as the flowsheet of choice. Flotation was deemed to be more practical than gravity due to the lower capital and operating costs. No further work was done concerning gravity concentration until 1990 when it was decid­ed to investigate ways to diminish the occurrence of free gold reporting to the flotation tailings.

Jan 1, 1996

By Dale C. Matthews

The Getchell Gold Hine is located about 40 miles northeast of Winnemucca, Nevada. Gold was discovered at the mine in 1934 and production was started in 1938 and ended in 1967 for its first phase of operation. Gold production during this period was about 800,000 ounces. In 1983, FirstHiss Gold Inc. purchased the property and initiated an exploration program that proved minable reserves of about 1,300,000 ounces of gold remained in the mine. During the exploration period, metallurgical testing was conducted to determine the most economical process that could be utilized for recovery of gold from the very refractory ore. After extensive investigation, pressure oxidation of the ore was selected, Engineering for the new plant commenced in 1987 and construction was completed in 1989 at a cost of about $87,400,000.00, not including financing cost.

Jan 1, 1990

By Johann Knecht

Due to lower specific investment and operating costs the tendency towards large scale equipment will remain. For the design engineers not only the stresses in the mill structure and manufacturing are of importance but also transportation to and erection on site. A scale up of the design of smaller sized units on the pantograph principle may not always give the best approach to the job in this respect. This paper covers recent developments in the design of large size equipment where the huge dimensions call for designs being different to the well known ball and SAG mill concept with cast conical endwalls. The first part describes the features of the biggest ball mill in the world, whereas the second part provides some details of the largest shell supported SAG mills being currently in the manufacturing process.

Jan 1, 1993

By Rudy Rogers

When Gas hydrate formation rates have two steps: a nucleation induction step and an agglomeration step. Hydrate induction in distilled water is extremely slow because of lack of nucleating particles. Our laboratory found that synthetic anionic surfactants greatly improve both hydrate induction and agglomeration because the surfactant?s hydrophilic head absorbs water molecules and the hydrophobic tail absorbs hydrocarbon gas molecules, creating necessary nucleation sites. Vast hydrate deposits inhabit seafloors. What is the seafloor hydrate nucleating mechanism? We find that nano-particles of smectite clays (bentonite and nontronite) are hydrate-nucleating sites in sea-water-saturated, packed porous media, especially when trace quantities of anionic biosurfactants adsorb on the clay particles. Microbes and their bioproducts proliferate around seafloor gas hydrate accumulations. The seafloor microbe-mineral-hydrate synergy is explored in this paper. Keywords: gas hydrates, biosurfactants, crystal nucleation, smectites

Jan 1, 2008

Rinker Materials Corporation (Rinker) operates construction aggregate operations in 15 states across the US. Thirteen of those operations are located in Florida, where Rinker produced approximately 40 million tons of aggregates in 2002. Because the deposits being mined in Florida are shallow sedimentary deposits of limestone and natural sand, with the deepest being approximately 75 feet deep, abundant acreage is mined annually. Rinker mines about 300 acres/year in Florida alone, and because there are so many wetlands and complete avoidance is nearly impossible, there are also wetland impacts. Thus, there is ample need for reclamation and mitigation, which presents an opportunity to involve local school groups with the planting and monitoring of these various projects. Rinker has successfully worked with a half dozen or so schools on these projects, involving students from grade school through college, with surprising success and outstanding results.

Jan 1, 2004

By Rick T. Richins

Despite what may be overwhelming evidence that natural degradation of cyanide and cyanide attenuation in hydrogeochemical processes are capable of reducing or eliminating potential water quality problems associated with heap leach facilities, the recent sharp increase in the price of gold and wide interest in the cyanidation process has focused all regulatory eyes on cyanide leaching. Regulations continue to increase, design criteria are more strict, and detoxification requirements approach or exceed the level of detectability. Current governmental regulation of mining and milling operations using cyanide varies considerably from state to state. The lack of regulatory consistency at this level is largely attributable to the current Bevill Amendment exclusion of mine wastes as potentially hazardous wastes, the undefined status of the Environmental Protection Agency's ongoing mine wast study effort, and the mining industry's reluctance to develop a consistent policy regarding state versus federal mine waste regulation.

Jan 1, 1998

By E. Ghali, L. Tremblay, M. Lanouette, J. McMullen, G. Deschenes

Since the start of this decade, our society has attached great importance to matters concerning environmental protection. Currently, most mining operations use the cyanidation process in working gold deposits. While this process is efficient, the dangerous aspects of cyanide are delaying the development and marketing of cyanidation in underground sites. There is a growing need to consider installing an underground leaching system that will make the processing of low-grade gold ore profitable by reducing certain major operating costs (transportation, crushing and grinding). Underground leaching is performed in two ways. The first way is in-site or underground and the second way is in-situ. CANMET (Harrison et al.), in collaboration with Dennison Mines, developed the underground leaching of uranium. This process is used commercially. Copper, salt and sulphur are recovered by in-situ leaching (Jacobson and Murphy). The recovery of gold and silver is under development (Van Staden and Laxen).

Jan 1, 1992

By S. Möllerherm

"Since the adoption of the Rio-Declaration in 1992 the concept of sustainable development is raising more and more awareness in public perception. The World Commission on Economic Development WCED has defined sustainable development as the concept that "meets the needs of the present without compromising the ability of the future generations to meet their own needs". The concept requires the integration of economic, environmental and social considerations into all decision making, fostering intra-generational equity through the alleviation of poverty by concentrating the benefits of development in lesser developed areas; and considering the needs of future generations to ensure that inter-generation equity exists. This paper is devoted to give a review of the current status quo of the discussion. It describes the achievements of the mineral industries on their progress towards sustainable development since the Milos Conference (SDIMI 2003), but also discusses future challenges and obstacles."

Jan 1, 2005

By Chris Joyce, Peter Ryan, Graeme Mcllveen

This paper briefly summarizes regulatory procedures and government agency roles and jurisdictions in each Australian State and Territory. The role of the Commonwealth of Australia and selected current trends in environmental regulation are also discussed. While the Commonwealth has played an active role in regulating specific commodities or mines through its powers over export licences, international heritage agreements and the Territories, such cases have largely been a result of response to specific public issues. This may change; the Commonwealth has established the Resources Assessment Commission and is canvassing the establishment of an Environmental Protection Act, aimed at the standardization of environmental standards through the creation of an Environmental Protection Authority. While the States, the Northern Territory and the Commonwealth lwve nominally different resource planning, environmental project approval and operational regulatory authoritit:s, the fundamental principles hinge on mining lease, planning and pollution control approvals.

Jan 1, 1991

By A. Russell, M. N. Hughes, Jack Barrett

The bacterial oxidation of arsenopyrite has been shown to be an efficient, economic and environmentally acceptable method for the liberation of any gold content . The mechanism of the process is not certain but is usually considered to involve direct and indirect reactions with respect to bacterial involvement. The direct reactions are those in which the bacteria attached to the mineral surface cause its dissolution, with dioxygen being the oxidant. The iron(III) produced in solution is the chemical oxidant in the so-called indirect reactions. Barrett et al 2 showed that a synthetic bio-oxidation solution (with no cells present) could dissolve up to 15% of an arsenopyrite sample, the products of the chemical oxidation being iron(II) and arsenic(III). This paper describes an extension of the investigation of the chemical process and its imp! ication for the mechanism of the bio-oxidation of arsenopyrite.

Jan 1, 1990

By James Y. Oldshue, Paul M. Kubera

Most coillillercial processing applications employing mixers in various types of slurry systems are continuous flow. These applications may also be multiple stage, with the stage number varying anywhere from two or three to ten or more. Two questions that usually come up at the beginning of any proposed pilot plant study are (1) can the pilot plant unit be operated batch-wise, and the results extrapolated both on the basis of scale and fluid motion to the full-scale tank which will be continuous-flow (and probably multi-stage), or (2) does the pilot plant need to be operated in a continuous-flow fashion, and if so, does the exact number of tanks/stages that are proposed for the plant need to be used in the pilot plant? We will consider these possibilities in sequence and present the principles involved in running some of the various pilot-plant arrangements.

Jan 1, 1992

By A. Goulsbral, D. Harrison, R. Dunne

A programme to reduce cyanide consumption at the New Celebration Gold Mine, situated 32kms South of Kalgoorlie, Western Australia, commenced in the latter part of 1990. Cyanide speciation studies at the time identified that the major loss and consequently consumption was due to the hydrolysis of cyanide, The use of artesian hypersaline waters of high magne­sium content on gold plants in Western Australian Goldfields has meant that economically viable operating pH values during cyanide leaching are around 8.9 to 9.5. The high ionic strength in these waters does to some degree retard the hydrolysis reac­tion. Notwithstanding this, the formation of hydrogen cyanide and its loss due to volatilisation is the cause of the major loss of cyanide on most gold plants in the Kalgoorlie Goldfields. This paper discusses the aspect of oxygen addition during cyanide leaching to decrease cyanide consumption and increase gold recovery.

Jan 1, 1996

By Roy Norcross, Stephen Gos

For over 100 years Degussa has worked together with the min­ing industry not only providing quality products but also develop­ing technologies to support these products through value added goods and services. For cyanide, these technologies include leach enhancement processes such as PAL™ and Solidox™, and cyanide detoxification with peroxygen based processes such as SILOX™ and Caro's acid using our DegOX™ technology. Degussa has also made important advances in how sodium cyanide is packaged and shipped with our liquid NaCN plant joint venture with MSI, CYANCO in Winnemucca, Nevada, and our Advantage SLS™ solid to liquid cyanide delivery system. All of these innovative technologies developed to support NaCN in mining, provide value to our customers and show Degussa's commitment to Responsible Care·11.1 and dedication to product stewardship. With Responsible Care and the customer in mind, Degussa has developed Advantage CCS™ cyanide control system, which will soon be available for the North American market. Currently there are several CCS units in service installed by Degussa AG (Germany), and we are in the process of designing the next gen­eration of the CCS which should be completed by late '98. Based on our experience working with gold and silver mines all over the world, there appeared to be an opportunity to further assist our customers by providing a better more automated way to control their cyanide additions. By providing the mine with an accurate method for maintaining their desired cyanide levels in their leach circuits, we could help them avoid underdosing and the associated gold and silver losses, and overdosing the cyanide which not only wastes cyanide but may increase treatment costs as well. In the early 1990's, when we began to introduce our CCS units, there were several cyanide controllers and on-line analyzers avail­able. However, they appeared to be too complicated and not made to stand the harsh conditions inside a mill. This resulted in exces­sive downtime and poor analytical results. We also found that many units would be installed but not commissioned by the sup­plier. Based on these observations, along with filtration and con­trol problems on some existing units, Degussa decided to design its own cyanide control system based on our extensive knowledge of cyanide chemistry, using the best components available worldwide.

Jan 1, 1998

By Thomas D. Kaufmann

Introduction Mining has always been sensitive to the fluctuating income of downstream customer industries. The industry is now becoming more vulnerable to booms and busts as economic pulsations increase and demand for mining products shows little or no long-term growth. As the general economy has become more cyclical in the last decade, the capital-intensive primary industries have become more aware that timing as well as preparation of survival plans are vital in investment decisions. Strangely, however, some of us have not yet included the business cycle in our feasibility studies. Cyclic prices and volumes and fluctuations in profits and cash flows do not fit our linear models. The increased cyclical nature of our economy is recent and poorly understood. Forecasting peaks and troughs is still more an art than a science. Nevertheless, avoiding business cycle parameters can lead to error in value estimation and contingency planning of new projects. Metal and Mineral Industries More than half the iron and steel, aluminum, copper, lead, zinc, manganese, tin, nickel, molybdenum, cobalt, and chrome that we mine, smelt, upgrade, and recycle goes to construction, transportation, capital goods, and consumer durable industries. All are cyclical. Their products are consumed slowly, so replacement can be postponed in recessions. Purchases of such goods are usually financed by debt, and their customers are sensitive to highly cyclical changes in interest rates. During prosperous periods, people tend to buy capital goods despite high interest rates. Upstream industries also tend to be whipsawed by inventory cycles. With high interest rates and good transportation, downstream fabricators can lighten their inventories during recessions. They know that upstream suppliers can deliver supplies and raw materials immediately, And, with the advent of electronic accounting, the fabricator with timely inventory information can afford to hold fewer contingency stocks. Likewise, when recovery returns, inventories surge back through industry pipelines, accelerating demands on primary supplies. The price elasticity of most primary products is low. Their share of the value of finished products of the industries they supply is generally small. The 60 kg (130 lb) of aluminum in a car is vital. But whether it costs $80 or $130 will not visibly influence the demand for an automobile. With low elasticities of demand, the primary producer is hit with decreases (or increases) in prices and in sales volume, during recessions as well as recoveries.

Jan 6, 1984