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By A. J. Douchane, J. M. Shirley

The high grade gold and silver Ken Snyder Mine is located in north-central Nevada, in Elko County, adjacent to the town of Midas, approximately 240 miles to the east­northeast of Reno and approximately 60 miles to the northeast of the town of Winnemucca. The Midas Joint Venture (MJV), an equal partnership between Franco-Nevada Mining Corporation, Inc. and Euro­Nevada Mining Corporation, Inc. with Franco-Nevada Mining Corporation, Inc. being the joint venture manager, owns the mine. In May 1997, Kilborn Denver, now SNC-Lavalin America, completed a bankable feasibility study and proceeded with detailed design, procurement and construction management. In mid December 1998, MJV not only poured their first gold several months ahead of schedule, but were already operating at full production. In addition, the construction of this US $84 million mine, mill and related facilities were completed on budget. Operating cash costs are US $78/oz. This paper describes how this was accomplished.

Jan 1, 1999

By P. J. Hyde

Cyanide is a significant contributor to the cost of producing gold. Any reduction in consumption that can be achieved through more reliable measurement and/or more efficient management of dosing rates can have a significant financial impact. An automated analyser, by its mechanical nature, is not prone to the variations of human operators, particularly notice­able from shift to shift. Reducing the standard deviation of the measurement (ie, reducing noise ), the automated measurement will give the metallurgist a truer picture of the underlying patterns of usage. The combination of automated analysis with on-line operation and a control loop provides timely information that is efficiently utilised in the management of the plant. Until the release of the Chemtronics On-Line Cyanide Analyser (OTA3000) about 12 months ago, the Australian experience with automated analysers (especially on-line) had been substantially negative. Since its release, the Chemtronics instrument has outperformed both manual titrations and other automated instruments, gaining an enviable reputation for accuracy and reliability in the process. The instrument is built around the technique ofpotentiomet­ric titrations, in which the potential of an indicator electrode is measured as a function of the volume oftitrant that is added to the sample. As the cyanide in the sample is depleted, the potential on the indicator electrode changes rapidly, producing a typical sigmoidal curve. The OTA3000 takes the first differ­ential of the curve, identifies the apex of the peak as the endpoint and reports the result in parts per million of sodium cyanide. The OTA3000 accepts the peak as valid only if it exceeds a certain minimum height. That minimum height is a programma­ble parameter and is used to optimise the relationship between sensitivity and the rejection of spurious peaks. The instrument will track cyanide trends through both positive and negative slopes of any magnitude, but it will provide a warning if it the slope becomes excessive, not because it affects the instrument but because it means that something unusual is occurring in the tanks. There are a limited number of conditions under which the instrument will produce a result of zero. In these cases the OTA3000 holds any output lines at the last valid result while it repeats the titration. This feature was incorporated for reasons of stability in a feedback loop.

Jan 1, 1995

By A. Goulsbra, S. Gregory, P. Gelfil, V. Martins, R. Dunne

As a general rule for gold treatment the presence of reasonable amounts of 'coarse' free gold will dictate the use of a gravity circuit. The actual particle size of gold that constitutes the por­tion of' coarse' free gold can vary widely. The larger its size the more troublesome it is, mainly because of the tendency for this gold to quickly settle out from slurries in regions of relatively low velocities. There are a multitude of places where 'coarse' gold can find a resting place, namely, in chutes, between and behind lines, in pump hoppers and in pumps themselves. Fortunately, the problems associated with recovering very 'coarse' free gold, say greater than Imm, is rare on most gold mines that have grinding and cyanide leaching circuits. For these operations it is common practice to have a gravity circuit situated within the milling circuit to recover 'coarse' free gold. Should the 'coarse' free gold constitute 15% to 20% of the total gold in a deposit then its recovery by gravity separation is seri­ously considered. As a gold mine 'matures' the availability of soft oxide ore decreases and the likelihood that harder ore having sulphide gold association increases. To maintain gold production rates in this situation either the gold grade of the treated ore must increase or more ore needs to be treated. In the latter case this is achieved by installing more grinding capacity, an expensive option, or coarsing the grind, with the downside of loss in gold recovery. In general the less expensive capital options is fol­lowed. There is, however, some upside to improve recovery when reasonable quantities of sulphide containing gold are pre­sented that can be recovered by flotation or gravity separation. Concentrates produced from these unit operations can be finely ground and reintroduced to the cyanide leach circuit to improve gold recovery. This scenario is a much less costly option than one where all the ore is ground finer. In this paper the experiences of recovering gravity gold from the Telfer Gold Mine, and gold associated pyrite from the New Celebration Mine will be discussed.

Jan 1, 1996

By Paul Hosford, B. Thrall

There has been a surge of exploration activity and interest in mineral properties located in cold Northern climates, with gold and copper properties as the two most attractive targets. There are already a number of mining operations located in the Arctic, for example, Red Dog, Polaris, and Lupin, all located in the Canadian Arctic. The logistics of sustaining operations, the engineering design and construction methods for such inhospitable regions are now relatively well understood. However, at least three of the proposed new mines in the Yukon Territory, Canada are designed to be heap leach operations. Rescan Engineering has recently completed Feasibility studies for two heap leach operations in the Yukon, one of which, the Brewery Creek Mine, is now in operation. The purpose of this paper is to explore some of the engineering and operating concepts that have been developed to make heap leaching an appropriate process method for gold recovery in a cold climate. Many of the readers will be familiar with the general and specific details of heap leaching, and it is not the intention of the authors to deal with any of the established "do's" and "don'ts" that have been addressed in numerous previous papers, but only with those pertaining to cold weather operations. This paper also examines these design concepts in specific relation to the results of the first winter's operation at Brewery Creek Mine, the first "far" North heap leach operation.

Jan 1, 1997

By Matthew Horsnell

Greenbank Terotech is a member of the Halley & Mellowes Group of Companies and is accredited t AS3902. Greenbank has been involved within the wear resistant lining industry for over 20 years. Initially supplying cast Basalt piping systems through to the present day breakthroughs with SiTech cyclone linings. The challenge of finding the most cost effective cyclone lining has been a difficult process. Over the years many varieties of ceramics have come and gone. In particular within cyclone applications, many people have become disillusioned with the term "Ceramic." In practice, it was discovered that if a ceramic worked in one part of the plant, it did not necessarily work in the cyclone area. A good example of this is Alumina chute and pipe linings. An Alumina lined cyclone underflow bend would provide exceptional wear resistance, whereas an Alumina Spigot would have failed miserably. After Alumina's were tried, Silicon Carbides were experi­mented with. The results in many trials were mixed. What worked at one mine did not work at another. The results did not conclude decisively that ceramics were here to stay within the hard rock cyclone area. It was then that Greenbank Terotech started to look at the reason "Why do some linings work and others don't." We came to the conclusion that the matrix holding the particles together had to be the key to a successful cyclone material. At the time we looked at materials such as Alumina Bonded Silicon Carbides, Metallic (Aluminium) Bonded Silicon Carbide, 99% Alumina Ceramics and Nitride Bonded Silicon Carbides, but all these materials either suffered from chemical attack on the Aluminium matrix (via cyanide) or the matrix simply was not hard enough causing wear rates to be excessive. It was then we looked at SiTech. SiTech is a unique material in that the primary particles are Silicon Carbide, but the matrix is made up of a Secondary Silicon Carbide formed within the reaction bonding process.

Jan 1, 1995

By Kristin Hemlein

Mining project development, permitting, environmental regulatory and compliance issues in Uzbekistan and the CIS are every bit as complex as those in the western world. The vast array of environmental permitting, monitoring and reporting regulations for mine project development and operation in the CIS are based on existing Soviet environmental regulations and policies which have remained in place after these countries gained independence from the former Soviet Union. The approach to mine project permitting in the CIS differs from the western world. Similar pre- feasibility, baseline data collection, and environmental monitoring requirements allow the project proponent to coordinate preparation and submission of documentation to support project permitting for Uzbek regulatory requirements with environmental requirements imposed by financial institutions and western environmental compliance structures. Implementation of generally accepted western environmental best management controls and monitoring into mine design, construction, and operation will not, however, ensure automatic compliance with Uzbek environmental regulations. Uzbek environmental compliance requirements that differ from western requirements include: 1) development and maintenance of an environmental database constructed specifically to address annual, biannual and quarterly statistical reporting requirements for emissions of "environmental pollutants" from the facility into air, surface water, ground water and soil; 2) preparation and submittal of specific permits for water utilization, hazardous waste storage and disposal, landfill construction and operation, and stack emissions inventories; and 3) procurement of approvals from the Uzbekistan State Committee for Nature Protection (generally analogous to the US Environmental Protection Agency). This paper outlines and summarizes the regulatory requirements for mine site permitting and the procedures for environmental monitoring and reporting during mining operation in Uzbekistan and the CIS.

Jan 1, 1997

By Gus Van Weert, Roy van Lier

It has been demonstrated for two totally different silver bearing and cyanide refactory concentrates that the formation of silver jarosite can be prevented through the addition of iodide to the autoclave feed. A molar ratio of r/ Ag+ of no more than 1 was sufficient to raise silver extractions in a subsequent cyanide leach from 4% after autoclaving without iodide addition to 98% for the sulpho-salt concentrate and from 15% to 97% for the pyritic acanthite concentrate. Flowsheet proposals will be discussed to prevent loss of the iodide additive. The use of chloride instead of iodide will also be reviewed.

Jan 1, 2000

By P. B. Hearse, R. L. Flood

TQM is a term of which most metallurgists have heard and a system of which some have had first hand experience. This paper is designed to encourage further thinking on TQM and how it can effect your organisation. Consideration of organisational culture and objectives are a prime pre-requisite when planning for the implementation of TQM. It is argued that there is no "brand" of quality culture of TQM which can be applied en masse to the mining industry. Definitions ofTQM are proposed, and the essence ofTQM as being about increasing customer service, improving the quality of goods and services, and involving people in their work is discussed, in conjunction with the concept of Customer as applied to the metallurgical industry and TQM. The integration of TQM into Quality Accreditation Stan­dards is then discussed. Finally, examples of the benefits that may be achieved with Implementation ofTQM into metallurgical and operations groups is presented, along with an analysis of the difficulties of implementation into our businesses and operations.

Jan 1, 1995

By Stanley Bunk

The fluidized bed was invented by Fritz Winkler of Germany in 1921. The first application in the U.S. was in the development of the fluidized bed catalytic cracking of petroleum in 1942. Today, fluid bed cracking reactors are an integral part of every oil refinery. When fluid bed technology was first considered for applications outside the petroleum industry it was recognized to have uniform temperature, close control of the gaseous atmosphere and excellent mixing between solids and gases. Roasting of sulfide ores and concentrates was an obvious match. The first application was a single stage roaster for gold refining in 1947. There have been over four hundred commercial fluid bed roasters built and operated successfully in the four decades since the fluid bed was invented. There are three general categories of roasting applications. The largest number of roasters fall into the dead roasting category which includes gold ore roasters. The other categories are sulfating roasters and partial roasters (Reference 1).

Jan 1, 1990

By Daniel W. Kappes

Until recently, the general expectation among mining compa­nies and financial analysts has been that the price of gold would remain on a generally upward slope. The recent drop in the price of gold has caused many people to re-think the issue. Of course, the price of gold is singularly difficult to predict, so it is difficult to tell which concept is correct. In the present financial situation, however, many junior gold companies are faced with the reality that money is hard to raise, and many senior gold companies find that they are facing a period of corporate losses even though they own solidly producing mines, As engineering consultants, Kappes, Cassiday has recently received several requests to review conventional milling projects to see if heap leaching is a more viable option. In regard to straight financial criteria such as return on investment and net present value, the question is usually fairly easy to answer. However, corporate decisions must often be based on less definable criteria. For instance, new stock issues tend to be more successful if they are larger, which tends to favor milling operations over heap leaches. The corporate issues are often subjective and difficult to generalize about, so I will con­centrate in this paper on a few financial concepts.

Jan 1, 1998

By Caren Caldwell, Leslie Thompson

1.1 Biological Process Description Pintail Systems, Inc. (PSI) has developed and in partnership with their clients in the mining industry has applied biological remediation processes for detoxification of spent ore and process solutions from heap leach operations. Contaminants that are treated to mine closure levels or drinking water standards include cyanides (weak acid dissociable and total cyanides), thiocyanate, nitrates and heavy metals. Biological processes are both site-specific and ore-specific processes. PSI specializes in isolating indigenous microorgan­isms from spent ore and process solutions and augments them in the laboratory for enhanced bio-detoxification in the field. Bioaugmentation in the lab is a key to successful heap bio-detox in the field. In PSI's bioaugmentation processes native microorganisms are isolated from the spent ore environment and are tested for contaminant remediation capacity. A majority of the indigenous microbes will be tolerant of the spent ore environment but will not contribute to contaminant metabolism. Indigenous enrichment or biostimulation of these non-working microbes by adding trace nutrients can competitively inhibit the working microbes. For this reason PSI focuses on the bioaugmentation process where non-working microbes are discarded and the working population is enhanced through stress, mutation and exogenous enrichment before it is re-introduced to the heap and process solutions.

Jan 1, 1997

By Brian Burdett, Terry I. Mudder, Robert T. Richins, James A. Stevenson, Michael M. Botz, Alan L. Wilder

The first Cyanisorb process was constructed in 1991 at the Golden Cross Mine in Waihi, New Zealand to recover cyanide from CIL tailings. The Golden Cross operation consists of an open-pit and underground gold mine with a conventional crushing, grinding and CIL circuit with Merrill Crowe zinc precipitation for gold recovery. Prior to disposal in the tailings pond, slurry tailings are stripped of cyanide at a pH of approxi­mately 7.5 using the Cyanisorb process. Mill throughput is approximately 2,500 tons per day (TPD), and CIL slurry tailings average 37% solids with a specific gravity of 1.27. CIL tailings WAD cyanide average 150 mg/L. The Cyanisorb process recovers approximately 85% of tailings WAD cyanide, produc­ing a slurry effluent with approximately 20 mg/L WAD cyanide. A second Cyanisorb process was commissioned at the NERCO DeLamar silver mine in southwest Idaho in May, 1992. The ore milling and silver recovery operation consists of crushing, grinding, a CIP circuit and Merrill Crowe zinc precipi­tation for silver recovery. Cyanide recovery is from clarified tailings with WAD cyanide ranging from 3 50 mg/L to 600 mg/L, producing an effluent with less than 30 mg/L to 60 mg/L WAD cyanide. Due to the presence of zinc-cyanide complexes in mill tailings resulting from the Merrill Crowe process, cyanide is stripped at a pH of approximately 5.5.

Jan 1, 1995

By S. R. La Brooy, P. C. Earley

Gold and Resource Developments NL (GRD) operates the Macraes Gold Project in East Otago in the South Island of New Zealand, treating a carbonaceous, refractory sulphidic gold ore. The ore is concentrated by flotation, then reground, followed by CIL cyanidation, to minimise loss to the preg-robbing natural carbonaceous material. As the mine has progressed there has been some variation in the preg-robbing nature of the ore, with average overall gold recovery generally in the range 70- 75 %. The Macraes Gold Project has been operating since 1990 and still has an estimated 11 year mine life, which has stimulated the continuing drive to enhance gold recovery. Testwork in 1994 showed there was no improvement in CIL gold recovery after conventional acid pressure oxidation of Macraes Gold Project flotation concentrate. Hence roasting was initially considered as the preferred option to improve gold recovery, being the only established technology to deal with both carbonaceous preg-robbing and sulphide encapsulation. However Newmont Gold Company pressure oxidation technology, as used at Twin Creeks in Nevada, has proved to be applicable to the Macraes Gold Project concentrate. Pilot scale testwork has shown that both roasting and pressure oxidation could achieve similar CIL gold recoveries on the concentrate. However, capital cost, simpler arsenic stabilisation, the ability to operate autothermally at a lower concentrate sulphur grade and simpler environmental consenting factors, has tipped the balance in favour of pressure oxidation. Overall average gold recovery is expected to improve to approximately 84% with adoption of pressure oxidation. GRD has appointed Minproc Limited as EPCM contractor to install pressure oxidation at the Macraes Gold Project, together with upgrading the existing flotation and grind circuits at a cost of NZ$ 30M (US$ 16M). Construction is 60% complete and on schedule for 1 October 1999 start up.

Jan 1, 1999

By Wayde Esplin

At the Barrick Goldstrike processing facilities in northeastern Nevada, sulfide ore is pressure-oxidized at a temperature of 440° F and 420 p.s.i. in six autoclave circuits. The low pH, high temperature, and abrasive characteristics of the oxidized slurry present many new and unique maintenance challenges. To meet these challenges, the Barrick Goldstrike autoclave department formed a reliability group in August 1998. One of this group's critical missions is to reduce both maintenance costs and unscheduled downtime through the application of predictive maintenance technologies and Reliability Centered Maintenance Analysis. This paper discusses some of the successes of the reliability program at the Barrick Goldstrike autoclave.

Jan 1, 2000

By David C. Sanders, Rodney H. Sergent, Victor C. Storhok, Batric Pesic

In the past, considerable work has been done on the applica­bility of bromine chemistry in the extractive metallurgy of gold. While the research in this area spanned from the understanding of fundamental dissolution chemistry to the demonstration on a pilot plant scale, no work was done on the fate of discarded leach residues with respect to the stability of accompanied heavy met­als. Because the leach residues were the discharge products of halide/halogen systems, the general perception was that the con­tained heavy metals would be more susceptible to dissolution than in typical sulfate systems, thus causing increased environ­mental problems. A long-term study was performed to obtain the information on the stability of heavy metals contained in the leaching residues after bromination. The study involved the leach residues of three different ores, as well the precipitates prepared from the synthetic solutions (not presented here). The conclusion of this study is that the stability of solid residues produced by bromination leaching was same as the sta­bility of leach residues produced by leaching in the sulfate sys­tems. Also, contrary to the past expectations, the presence of bromide ions in the test solutions (up to 1 g/L NaBr) did not enhance the solubility of heavy metals (Cu, Zn, Pb, As) beyond the solubilities found in the sulfate systems.

Jan 1, 1998

By G. I. Voiloshnikov, A. F. Panchenko, N. S. Voiloshnikova

Low world gold prices stimulate development and introduction of economically efficient ( cost saving) technology for operating gold mills. This report covers the results of testing and introduction of CIL technology to recover gold from flotation concentrate of Samarta gold concentration plant located in Buryatia (Russia). This plant is treated the ore of Zun Kholba gold deposit using gravity and flotation of gravity tails as preconcentration processes. Till recently high grade gold gravity concentrate was smelted to gold bullion and shipped to gold refinery, gravity middlings were leached by cyanidation in cone type equipment developed by Irgiredmet and flotation concentrate shipped to copper smelter. The disadvantages of flotation concentrate shipping to copper smelter are following: high concentrate transport cost; problem with gold shipped balance; high cost of flotation concentrate treatment; comparatively low gold recovery. In this connection IRGIREDMET developed the hydrometalurgical technology for gold recovery from flotation concentrate. The flowsheet was developed on the base of laboratory, pilot plant and industrial scale tests conducted by IRGIREDMET in 1987-1997 and lrgiredmet experience on CIP process testing and industrial scale introduction in Yakutia [1-6]. The flowsheet is presented in Fig.1 and consists of following base operations: concentrate regrinding;

Jan 1, 1999

By Dr. H. Askew

The input needs of the steady state modelling process are outlined and a methodology for designing a plant survey to meet those needs described.

Jan 1, 1995

By Richard J. Frechette

Very few facilities containing hydraulically deposited tailings have been completely reclaimed and capped at this time. Design of a closure cap for a tailings impoundment has relied heavily on consolidation theory in order to achieve a cap that maintains sur­face drainage. Obtaining data for the consolidation evaluation can be difficult and costly. The author reviews the performance of two tailings impoundment closure caps that have been suc­cessfully installed and presents the experience gained from these projects with an emphasis on the ability to optimize cap design through post-operational monitoring prior to initiating cap con­struction. Using the optimization approach, a significant earth­work quantities reduction may be realized for the ultimate cap.

Jan 1, 1998

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 Gregory A. Vaka

Robins Engineers & Constructors, Inc. as the exclusive U.S. licensee introduced the PIPE CONVEYOR to the North American marketplace early in 1984. The sale of the first PIPE CONVEYOR in 1985 was a difficult task since the conventional troughed belt conveyor was the accepted and the most widely used means of continuous transportation of bulk materials handling in the world. Initially our clients viewed the PIPE CONVEYOR as a departure from the normal and accepted form of material handling. Since then, the parent company of Robins Engineers merged with Krupp of Germany to form KRUPP ROBINS, INC. in the United States. To date there are over 462 PIPE CONVEYORS operating worldwide with the majority of the long overland systems designed and installed by Krupp Robins, Inc. The PIPE CONVEYOR is now becoming the norm, viewed by those who are familiar with its capabilities as the preferred method of transportation for all bulk solids.

Jan 1, 1997