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By Michael G. Strominger, Anthony E. Gross

The development of precious metals ore agglomeration with a cement binder, by the U.S. Bureau of Mines, has allowed the economical heap leaching of low grade gold ores (<0,05 oz/ton) over the last decade, Even with the Bureau of Mines technology, numerous operations continue to experience channeling and blinding problems. A research project was undertaken at Nalco Chemical to address situations where improved agglomeration is needed, By increasing the incorporation of fines into the agglomerates,the segregation of ore by size which occurs from handling will be reduced and channeling minimized. A stronger agglomerate will reduce fines migration during leaching and prevent blinding of the heap, Both of these changes will give an even flow of barren solution throughout the heap and give solution contact with all of the ore. This paper presents the development of polymeric agglomeration aid, Nalco 9760 which has given a higher rate of and a higher total gold recovery in plant evaluations.

Jan 1, 1990

By Rodrigo Jerez

The mining business in general, and coal mining in particular, is exposed to frequent and significant swings in the business cycle. Marginal coal production enters the market place in a nearly perfect competition. It must be priced aggressively if market share is to be gained. The minimum price acceptable from the standpoint of the producer is reached at the point where total variable cost are recovered. Competition occurs as companies move to reduce their variable costs in an effort to cover some portion of their fixed costs at reduced market prices. Production planning and scheduling plays a critical role in reducing costs. Multiple scenarios based on changing market conditions require that competing firms have tools available to evaluate the economic impact of transportation, blending, and processing options. In certain applications, significant cost savings can occur as a result of blending or altering preparation levels. Linear programming provides a tool with which to evaluate options and acts as a like between the mine plan and marketing decisions.

Jan 1, 1992

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

By Bernie W. Martin, Duncan MacLennan

Building a new tunnel to accommodate CN North America&apos;s needs for double stacked container traffic for the next 100 years presented new and unprecedented challenges. Innovative approaches to contracting, especially the Negotiated Compressed Process (NCP), TBM design, project management, and the regulatory and approval process, were all required to deliver a new tunnel to meet the needs of CN North America within the approved completion schedule of 39 months compared to a traditional approach of 45 to 48 months. The NCP resulted in trimming 6 to 9 months from the project schedule, at a great saving of direct and indirect costs. The Negotiated Compressed Process is an innovative formalized approach to risk sharing for complex infrastructure projects. Ads were placed in the international trade journals and a short list of "approved" contractors and suppliers was developed. The approval process for this international project involved contacts with over two hundred agencies, departments and interested stakeholders.

Jan 1, 1995

By Eric Jackson

The presentation describes the operation and field test results of a seafloor massive sulphide prospecting system. The prospecting system is deployed from a work-class ROV, and it features a new and innovative electromagnetic ocean floor conductivity sensor. It also includes magnetometers, a multibeam sonar, and subsea cameras. The prospecting system has been used in two exploration campaigns - one in the territorial waters of Papua New Guinea (PNG) in 2007 and again in 2008 in both PNG and Tonga waters. The 2007 campaign used the prototype sensor, and the 2008 campaign used a Mark II version. Correlations between drill core samples and EM conductivity results are excellent. New prospecting system data will be used to help plan future core drilling locations. The presentation discusses the principle of operation of the EM conductivity sensor, discusses improvements made in the EM sensor and the overall prospecting system, and shows exploration results. Keywords: seafloor massive sulphide, geophysics, ocean floor, subsea, electromagnetic, conductivity, magnetometer, multibeam, core drilling

Jan 1, 2008

By S. K. Kawatra, S. J. Ripke

Finely disseminated iron ores compose much of today&apos;s reserves. After removing the silicate gangue, the resulting fine iron oxide concentrates require pelletization with a binder to enable transportation and reduction. Binders can be used more efficiently if their binding mechanisms can be completely understood. Typically, bentonite clay is needed as a binder to improve the strength of the pellets. Bentonite is an effective binder at a relatively low cost, but costs could be reduced further by replacing bentonite with even lower-cost binders, such as high-carbon Fly-Ash Based Binder (FBB). In this study, it was found that bentonite binds by a physical mechanism, while FBB binds by a chemical mechanism. These mechanisms were determined to be incompatible. Partial replacement of either binder with the other reduced dry magnetite pellet compressive strengths below the industrially acceptable value of 22.2 newtons (5 lbf). Activators and accelerators that activated the fly-ash deactivated the bentonite. The incompatibility of these two binders is explained.

Jan 1, 2000

By Alex Ruzycki

Gold Fields-Mesquite is a 7.5 million ton per year heap leach operation located in the Maj ave Desert of Southeastern California. Extraction of gold is carried out on multiple lifts, with over 33.3 million tons of ore leached since the inception of operations in 1985. The delineation of the gold left in heap residue is a formidable task. Gold removed from active leach areas can be routinely monitored through sampling of emerging solutions but exact recoveries from specific heaps remains nebulous due to factors such as cross flow between sections buffering effects from multiple lifts, and releaching. In order to better quantify ultimate heap recoveries and increase releach efficiency, Mesquite initiated a residue drilling program. The project progressed through an evaluation of sampling protocol, drilling of residue by reverse circulation, entry of assays into a software package capable of producing grade-based contour maps, and a production scale releach test that evaluated the system's ability to predict residue grade.

Jan 1, 1992

By Lyda W. Hersloff

As decommissioning of various radioactively contaminated facilities begins, the question of appropriate residual surface contamination becomes an issue. Surface contamination can result in exposure to people via inhalation, ingestion, and external radiation exposure, There is therefore the potential of exposure to workers involved in the dismantling of a facility as well as members of the general public acquiring salvageable equipment, tools, and building materials. The levels established as acceptable for unrestricted use by national and international organizations vary by as much as an order of magnitude for certain radioactive materials. The calculated doses associated with some acceptable contamination levels can be significant. The principle of ALARA, as low as reasonably achievable, is therefore a necessary element in establishing surface contamination levels for a specific site. Some components in evaluating site specific surface contamination levels for unrestricted use, especially removable contamination, include evaluations of the historical use of a facility, the mixtures of radioactive materials a&sociated with surface contamination, and resuspension factors for various materials.

Jan 1, 1991

By Fred Woodcock, A. R. Laplante

A laboratory technique is presented that uses the Knelson Concentrator and a relatively small sample to predict the amenability of a given gold ore to gravity recovery. The technique applies to develop­mental orebodies as well as retrofitting existing plants. Justification for this approach is discussed. Actual results of the technique applied to existing and prospective circuits are presented and discussed.

Jan 1, 1993

By L. M. English

When plotted as head vs. volume, fan curves start high and decrease in head with increasing volume while mine head curves start low and rise with increasing volume. Their intersection is the system operating point But wait a minute: Isn&apos;t head loss a negative number, a debit? And isn&apos;t fan head an energy addition, a credit? This, as every ventilation instructor knows, is often a stumbling block to student or audience comprehension. It is possible to use the intuitively correct curves -pressure losses as negative values and energy additions as positive values -and still obtain the correct operating point: adding the two curves produces a third curve that intersects the x-axis at the operating point, the point at \\tIich the fan energy input exactly matches air circulation energy loss. Using this technique also makes it easier to account for outside influences on the system, such as natural ventilating pressure; with the standard approach it is quite easy to add or subtract such influences to the wrong curve. This approach can be extended to the graphical solution of any series/parallel circuit or ventilation net\wrk. The results are the same, and the approach is logically consistent and less confusing.

Jan 1, 1997

By III Boxley

Most of us realize that our nation&apos;s roadways are under ever-increasing stresses, from higher traffic counts to increased tire pressures and their resulting loads. At a time when the interstate system as originally envisioned is completed, and the National Highway System is being drawn to replace it, it is appropriate that we examine design and construction methods for the next century. The stone industry shares a common desire to produce high quality, cost-effective roadways that perform over time. The superior sub-grade and road base structure provides for the superior roadway. Since I am neither an engineer nor a contractor, I will not attempt to suggest design or construction methods. What I can do is share my company&apos;s experience in supplying road base materials by using a historical perspective in Virginia and some trends in the market that we have observed. Road building and related non-building construction are still far and away our largest markets as an industry. If we can help to improve the end product of our biggest customers, we add value to our own product. Indeed, in a time of budget constraints and competing demands for government dollars, we must show value over the life of a pavement structure to ensure their long-term funding.

Jan 1, 1996

By Charles C. Y. Chen, Duane R. Skidmore

Batch leaching of Ohio #1, Ohio #4A and Ohio #5 coals was conducted with the thermophilic. sulfur, oxidizing microorganism: Sulfolobus acidocaldarius. Four different size fractions of each coal, with median sizes of 508, 200, 90, and 49 microns, were subjected for 10 days to leaching in a 5% coal-water slurry at 72°C and a pH of 2. Release rates and extent of sulfate and iron I1 and I11 ions from the coals during the leaching process and distribution of sulfur forms (sulfate, pyritic and organic) in the coal samples before and after treatment were determined. Data indicated that Ohio #1 coal, with an initial sulfur content of 0.6%, showed no significant changes with leaching in total sulfur content or forms of sulfur. The Ohio #4A coal, with initial total sulfur content near 5%, yielded product, for sizes below 200 microns with 90% reduction of pyritic sulfur while the extent of organic sulfur removal varied with coal particle size. Results similar to those for Ohio #4A were observed on the Ohio #5 coal, which had an initial total sulfur content of 3% and a final sulfur content near 1%. The findings were interpreted in terms of basic biological, chemical and physical mechanisms.

Jan 1, 1989

By W. E. Horst

Raw materials and mineral products are crushed, ground, or pulverized for a variety of reasons. Some of the most important reasons for size reduction are: to liberate marketable mineral species from a matrix of commercial minerals and gangue, to promote rapid chemical reaction through exposure of large surface area, and to produce a material with desirable size characteristics for handling, utilization, and storage. Comminution processes are currently used on vast tonnages of raw material annually. In the mineral industries where mineral products and other solids are processed, the various size-reduction unit operations represent a major portion of the manufacturing costs. The comminution process is an expensive unit operation from the stand- point of both capital and operating costs. Power consumption is large, and the energy conversion to useful work is very small regardless of the size-reduction system. In energy terms, about 1% of the all electricity generated throughout the world is expended in crushing and grinding operations by the cement industry alone. Comminution is a general term for size reduction that may be applied without regard to the actual breakage mechanism involved. General type of size-reduction equipment include crushers, tumbling mills of various type, impact mills, fixed-path mills such as a roller mill, and fluid-energy mills. Some comminution machines accomplish

Jan 1, 1985

By K. Terhaar, K. Prisbrey

The objective was to determine operating protocols for a lead and silver column flotation cleaner being considered for installation at Sunshine Precious Metals Inc. &apos;s Kellogg mill in Northern Idaho. In this column, tetrahedrite and galena were floated, and pyrite and other gangue minerals, including siderite and silica, were depressed. The procedure was to develop a dynamic simulation using a linear transfer function approach. The transfer function related cause-and-effect variables such as the influence of collector and depressant dosages on recovery and grades. Bench-scale flotation tests followed by pilot column testing provided the data used to develop a linear transfer function. The transfer function was derived using a spreadsheet. This model was applied to simulate how the flotation column could be made to respond to disturbances in feed grade. The results were that xanthate, zinc sulfate and sodium cyanide were found to be suitable controls for grade and recovery. Simulations showed the best sequence of manipulations of these reagents, and these sequences are useful for future operator training. The conclusion was that linear transfer functions were able to simulate lead and silver recovery, develop scenarios for operator training and provide a foundation for future on-line control.

Jan 1, 2002

By P. L. Padgett, J. C. Hower

Five coals blended at a Midwestern United States power station were subjected to detailed analysis of their Hardgrove grindability. The coals, representing four distinct coal beds, are a low-sulfur, high-volatile A bituminous Upper Elkhorn No. 3 coal (Pike County, Kentucky); a medium-sulfur, high-volatile A bituminous Pittsburgh coal (southwestern Pennsylvania); a low-sulfur, subbituminous coal from the northern Powder River Basin (Montana); and two low-sulfur, subbituminous Wyodak coals from two different mines located in the eastern Powder River Basin (Campbell County, Wyoming). All samples that were processed in the Hardgrove grindability tests were also analyzed for their maceral and microlithotype content. The high-vitrinite Pittsburgh coal and the relatively petrographically complex Upper Elkhorn No. 3 coal exhibited different grindability behavior. The petrographic compositions of the Pittsburgh raw feed, the 16 x 30-mesh fraction (HG! test fraction) and the -30-mesh fraction (HGI test reject) are similar, suggesting that the HGI test fraction typifies the whole feed. The eastern Kentucky test sample is not as representative of the whole feed, with the HGI test fraction having lower vitrinite amounts than the rejected -30-mesh fraction. The Powder River Basin coals are high in vitrinite content and show behavior similar to the Pittsburgh coal.

Jan 1, 1998

By Gregory Owen Lewis, Mark William Johns

The use of resin-in-pulp (RIP) to recover dissolved metal ions from slurries is receiving increasing attention. A number of engineering aspects have been identified as crucial if a RIP sys­tem is to operate efficiently. These are the mixing of the resin and pulp, the transportation of the resin and pulp and the sepa­ration of the resin from the pulp medium. Evaluation of numer­ous alternatives revealed that air agitation is the most suitable means of mixing to effect uniform distribution of the adsorbent and to effect a high mass transfer rate, airlift pumps are the most effective method of transporting the slurry particularly as they are characterized by a low degree of resin degradation and sieve bends are the most suited means of effecting the resin/pulp sep­aration. This paper details the design of the reactor that incorporates the three identified unit operations and presents data obtained from the contactor when operated at a throughput of I 00 000 t/m. The airlift pump was found to be sensitive to pulp density and submergence ratio. The screening ability of the sieve bend was influenced by resin and the pulp density . The reactor is a cost effective, metallurgically efficient unit for the recovery of metal ions from high density slurries.

Jan 1, 1996

By James W. Furlow

A recent attempt by a major mining company to mine phosphate in Chatham County, Georgia, resulted in a study by the Georgia Department of Mines, Mining and Geology which was intended to evaluate the deposit as well as potential hazards to the major fresh-water aquifer of the area. The study found that the confining layer above the fresh-water artesian aquifer is sufficiently thick and impermeable to allow removal of the phosphate ore zone without significant salt water infiltration into the aquifer. Therefore, phosphate mining under proper supervision will not adversely affect the quality of water used by the city of Savannah nearby. Volumetric studies show that there is a minimum of 4,800,000,000 cubic yards of phosphate matrix containing an average of 22.5% BPL. At an approximate weight of 1.5 tons per cubic yard and a concentration of 22.5% BPL, there are about 1.6 billion tons of 100% BPL concentrate present. At a conservative factor of 50% at least 800,000,000 tons of 100% BPL concentrate could be recovered for market sale. In addition to the area discussed, evidence indicates that the phosphate horizon-may extend continuously out to sea for at least ten miles, and probably beyond.

Jan 1, 1972

By Ron Parks

High Pressure Grinding Rolls (HPGR) was introduced to the mineral processing industries in the mid-SO's as a tool for comminuting raw and processed materials. This tool made its an impact in the Cement Industry where it was used as a pre-grinder on existing ball mills, raw and finish grinding in a mill circuit and other various applications. This concept was a big success where the cost of power was high along with the desire to increase capacity. The HPGR reduced the power requirement and increased the capacity in the ball mill due to the finished product produced by the HPGR and the micro fractures in the coarse rock, which reduces the power required to finish grind the rock. This unit has found acceptance in many other industries including diamonds, iron and other selective applications. The diamond industry uses this tool for selective grinding purposes since the kimberlite rock is considerably softer than the actual diamonds. Therefore within a bed of material, kimberlite is crushed to fines and the diamonds are liberated and unharmed. The iron industry primarily uses this tool for concentrate comminution; however, there are installations using this tool as a pebble crusher and in an AG-pebble mill circuit.

Jan 1, 2000

By HJ Marais, J A. van Niekerk

An investigation was initiated by BILLITON Process Research and Gold Fields Limited for the efficient removal of thiocyanate and cyanide from leach solutions. This led to the development of the ASTERTM process, an acronym for Activated Sludge Tailings Effluent Remediation. The biological degradation of thiocyanate and cyanide in effluents provides an alternative treatment to the more traditional processes. This occurs with a large number of micro-organisms which include bacteria, actinomycetes and fungi. Cyanide and thiocyanate are degraded to ammonia and carbon dioxide. Most forms of cyanide-metal complexes are generally removed through a co.mbination of oxidation and sorption into the biofilm/biomass. Since the ASTER™ process has commercial applications, a patent has been lodged for the ASTER™ process. A culture containing thiocyanate degrading organisms has been deposited with the Australian Government Analytical Laboratories (AGAL). The identification of the bacteria is in progress. Tailings arising from a cyanidation process tend to contain cyanide and thiocyanate. The presence of these species prevents the recycling of this water upstream to a bioleach circuit due to its toxicity to the bacterial culture. Increasingly stringent legislation for the land disposal of cyanide containing solutions also necessitates the treatment of the solutions before disposal.

Jan 1, 2000

By R. S. Mateer

Linear programming on desktop computers is commonly used to optimize coal blending proportions. The objective function is usually the cost of the blend. The constraints consist of materials and heat balances as expressed as linear functions of the blend. This is illustrated in Example 1. Inclusion of a sulfur compliance constraint in more complex because the maximum permitted sulfur percentage is not a pre-specified constant. Rather, it is a function of the calorific power of the blend itself. The current limit of 1.2 pounds of sulfur dioxide per million Btu may be expressed as: [Sulfur Max%= 0.6 . Hl10,OOO with H in Btu/lb.] A proper constraint equation may be formed by defining for each coal a function that is the difference between the actual sulfur percentage and the maximum sulfur percentage. This may be regarded us an excess sulfur percentage. For Coal A of Example 1. this would be: [ Sulfur Excess%=0.5-0.6 13,000/10,000=-0.28] This value would be used as the coefficient of the weight proportions of this coal in the blend. The complete constraint equation would then be the sum of such terms for each coal set less than or equal to zero. This is illustrated in Example II. [ ]

Jan 1, 1995