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By Stuart Ratcliffe, Denis Kidby

The development of Vitrokele™ Technology over the last 10 years is reviewed with reference to mine site piloting and com­mercial applications. The first mine site piloting was conducted in Australia in 1989 followed by a further six continuous site trials in Australia, Canada and the USA. These major pilot plant studies are complemented by over 50 laboratory scale batch and pilot testwork programmes. The first commercial plant using Vitrokele™ Technology was the Connemara project commissioned in Zimbabwe in 1995. Subsequent to this, three commercial scale projects have been designed using Vitrokele™ to recover precious metals, base met­als and cyanide. The various projects are discussed with relation to the differ­ing flowsheets applied to each particular case.

Jan 1, 1998

By Victor C. Storhok, Batric Pesic, Marlyn D. Ballain

No1ihwest Alloys produces magnesium from dolomite by reduction with ferrosilicon and aluminum. This process produces alkaline by-products in quantities that allow their consideration for use as commercial products. Two such products are dicalci­um silicate, termed as Di-Cal, and magnesium oxide, termed simply MgO. The alkaline properties of these materials offer acid neutralizing power, comparable to traditionally used lime. Thus, the materials warrant study for their use in various appli­cations where neutralization of acidic waters or process solutions are required. One such application is the treatment of acid mine waters with the objective of removing heavy metals. The chem­ical stabilities of the produced metal precipitates are critically important, from an environmental point of view, for their safe disposal in tailing ponds. The EPA regulates waste material dis­posal according to the results from TCLP testing. In this ongoing study, three mine waters were selected for treatment with Di-Cal and MgO. Lime was used as the control for these experiments. The waters were collected from the Bunker Hill mine, Berkeley Pit, and the Blackbird Mine. In addi­tion to testing the chemical stability of produced metal precipi­tates by the TCLP procedure, two other parameters were studied as well. They are: 1. the effect of water pH on stability, and 2. the effect of pH on the stability of resulting precipitates. In the first three months of study, it was found that neutral­ization with Di-Cal results in precipitates that range from equiv­alent to superior in performance as compared to those produced using lime for the waters from all three mines. An additional beneficial characteristic of precipitation with Di-Cal is the fast filtering characteristics of produced precipitates, when compared to the precipitates produced by lime. This property may be of significance when considering the improvement in drainage of tailing ponds and the volume of solids produced. This paper will discuss in detail the stability of metal precipitates with respect to various pe1iinent metals found in mine waters of Berkeley Pit (Cu, Zn, Mn, etc.), Bunker Hill (Zn, Mn, Ni and Co), and Blackbird Mine (Cu, Co).

Jan 1, 1998

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 Emily Wortman-Wunder

While the mood at the 2013 annual joint meeting between the Pittsburgh Coal Mining Institute of America (127th Annual Meeting) and SME Pittsburgh Section (68th Annual Off-the-Record Meeting) in Canonsburg, PA was subdued following a rocky year in the coal industry, attendance was down only slightly, to 300, and overall, the meeting?s focus was optimistic about the future of coal. The conference began by addressing one of the central challenges of coal mining head-on with a keynote address on the status of safety in the mining industry. Noting that two more U.S. miners had died in 2013 than by the same date in 2012, the National Mining Association?s (NMA) Senior Vice President of Regulatory Affairs Bruce Watzman made a plea for a new approach to safety. He described the NMA CORESafety initiative, a program that promotes proactive safety measures versus a compliance-driven model. CORESafety, described in more detail on pp. 29 of this issue, focuses on developing successful ways to change company cultures of safety and behavior. Other industries that have adopted this approach have seen dramatic drops in fatalities, including the Australian mining industry, which has seen its annual fatality rate drop to nearly zero even while the number of people employed in the industry has soared. The rest of the morning?s sessions explored what is arguably the industry?s biggest challenge right now ? maintaining the social license to operate.

Jan 1, 2014

By Daniel W. Kappes

In late 1995 at the Randol symposium in Squaw Valley, I gave a paper which described the Itos project flowsheet. At that time, project construction was nearly completed and stmtup was close. This paper describes the ltos operation since then. To summa­rize things, startup occurred partially in late 1995 with full start­up of all components in about mid 1996. From then until now, April 1998, the plant has been running at partial capacity and has yet to achieve full production rates.

Jan 1, 1998

By Gordon Lewis

The Penjom Gold Mine is one of the world's worst preg-robbing gold ores, yielding very low recoveries from traditional CIL methods. Gold recovery from the cyclone underflow was targeted to recover as much gold as possible in the absence of the fine preg-robbing carbon. Gold is recovered by intensive cyanidation and tabling of a gold concentrate produced by gravity from the cyclone underflow. The circuit was designed together with Gekko Systems and uses their InLine Pressure Jig and InLine Leach Reactor technology to reject the preg-robbing carbonaceous material and obtain high recoveries from the gravity concentrate before over grinding the carbon and sulphides. The gravity and intensive cyanidation circuit now recovers almost 50% of gold in new mill feed, with unit recovery in intensive cyanidation of up to 90%, the highest unit recovery in the plant. Operating costs for the gravity and intensive cyanidation circuit are under US$2.50 per oz, while the cost to recover gold from the cyclone overflow is -US$200 per oz. (not including common costs of milling, stripping and electrowinning). Figure 1 shows the increase in gold recovery due to the gravity and ILR circuit coming on line at Penjom.

Jan 1, 1999

By John Batty, Rennie Stallknecht, Dave Dew, Rennie Marais

GENCOR was contracted by Lonrho Plc of London to design a treatment plant for the benificiation of ores from the Amantaytau Goldfields in Uzbekistan (CIS). The testwork required for determining the design parameters was conducted at GENCOR Process Research in Randburg South Africa, on large bulk samples of ore shipped from the CIS. The initial milling and flotation testwork was designed to both optimise the conditions for maximum gold recovery, and to provide flotation concentrate for subsequent testwork. The concentrate produced was fed to a pilot scale BIOX® plant, and at the client's request a portion was shipped to specialists in roasting and pressure oxidation technology for comparison. Besides the testwork conducted at the GENCOR Process Research Laboratories in South Africa, the client also requested that the testwork be repeated at the Ingichki Research centre in Uzbekistan to demonstrate to their CIS joint venture partners that the results obtained in South Africa are reproducible and to demonstrate the ease of operation of a BIOX® plant. Pilot scale equipment was air freighted to Ingichki where the results of the testwork obtained in South Africa were successfully duplicated. BIOX® technology was shown to achieve higher gold recoveries than either roasting, whole ore roasting or pressure oxidation.

Jan 1, 1995

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 E. K. Albert

Title IV of the 1977 Surface Mining Control and Reclamation Act (SMCRA) provides for an abandoned mine reclamation fund. This fund, taken from fees collected from operating coal mines, provides capital for the reclamation process. The Act directs the Office of Surface Mining (OSM) to collect the fees based on coal production. Monies from the abandoned mine lands (AML) fund are distributed through two programs. The first provides OSM with capital to use in emergency situations resulting from abandoned mine sites and reclaiming high priority sites in states without established AML programs. The second distributes the money through a state's AML program in the form of grants. To provide for a flexible and customized selection procedure for AML projects, a management information system (MIS) that combines scientific selection procedures is being developed. This system employs objective and subjective methods developed in systems research in recent years. The MIS component is an essential part of any selection process involving large numbers of potential projects. It must contain all the necessary project parameters that can be applied to the selection of projects whether or not they are to be used in the immediate selection criteria. In addition, variable selection criteria will allow ‘what if’ types of inquiries for comparison of differing selections and benefits.

Jan 1, 1990

By C. A. Fleming, C. J. Ferron, E. S. Makande, P. Mason

Several small mines are producing refractory gold concentrates in Zimbabwe and, owing to the small scale of most of these operations, their output is processed in a central custom roaster in Kwekwe. Owing to the wide variations in the feed to the roaster, the efficiency of the old Edwards roaster is deemed unsatisfactory with gold recovery from concentrate as low as 70%, and alternative processes were evaluated to improve this situation. Various processes for oxidizing refractory arsenopyrite/pyrite concentrates to liberate gold prior to cyanidation are known. In practice, only two have to date met with wide industrial acceptance, pressure oxidation and roasting. Owing to the ·high arsenic and antimony levels of some concentrates in Zimbabwe, the only viable roasting alternative would be two-stage air-roasting of concentrates in two reactors, as practiced at Giant Yellowknife, Campbell Red Lake and New Consort. This process, however, creates an arsenic disposal problem, and produces gas of fairly low SO2 content, requiring a large gas handling system for acid production. On the other hand, there are currently four commercial pressure oxidation plants treating refractory gold ores (McLaughlin, Mercur, Getchell and Goldstrike) and three treating concentrates (Sao Bento, Porgera, Campbell). One other concentrate oxidation plant is being constructed (Con), and several more are being considered.

Jan 1, 1992

By Martin F. Grier, Nicholas H. Kempton

The Mt. Todd Gold Project in the Northern Territory is a joint venture between Billiton Australia Gold Pty. Limited, a wholly owned subsidiary of Shell Australia Limited, and Zapopan NL. As manager of the project, Billiton is guided by Shell's corporate policy that foremost consideration be given to protection of the environment from unacceptable impact and that sound environmental programmes are to be implemented effectively at all company operations. This policy on Health, Safety and the Environment helps operating companies in addressing environmental matters in a systematic way and gives guidance on the practical implementation of a range of controls to protect the environment. Most importantly, it seeks to do this in a co­ operative rather than adversarial manner. In developing the Mt. Todd Gold mine the joint venturers' environmental objectives have therefore been to plan and operate the project consistent with the highest industry standards and community expectations and in accordance with all Northern Territory government requirements. A development strategy has been designed which minimises environmental effects. Planning priorities have focused on the successful co-existence of the mine with an endangered species of bird, the Gouldian Finch, which breeds in the area; the mitigation of impacts on surface and ground. water qualities; and the protection of significant Aboriginal cultural and archaeological sites.

Jan 1, 1991

By Rosa H. Harris

The world's largest gold dump leach operation, Minera Yanacocha S.A., has installed community assistance programs in Peru concerned with health, education, electrification, agricultural assistance and road improvements. The programs are conducted in a joint venture fashion in association with various organizations.

Jan 1, 1998

By Norbert Patzelt

Today the standard method for grinding ore is the wet process. This is mainly due to the fact that the downstream process is wet and considering the total circuit dry grinding is not the most eco­nomical method for the comminution of the ore. Presently in gold ore processing dry grinding is only applied in cases where whole ore roasting is required downstream from the milling plant or if organic carbonaceous matters and sulfides are the primary reasons for the refractoriness. Since dry ore can be fed to the roaster, a dry grinding mill can advantageously be applied. In cases where d1y grinding could be applied advantageously for instance if the ore contains water soluble material and wet grinding is not possible there are serious concerns prevailing within the industty against this technology due to several reasons. Besides of the aspects as discussed later in this paper, there are several plants in operation with little success and considerable operational prob­lems. The reasons for this often lie in the fact that the several com­ponents of such a plant are bought from independent sources with­out considering the system requirements. It is essential that the dry grinding plants require accurate design between drying, pneumatic transport and grinding of the ore in the circuit. This paper will address some of these concerns raised in the industiy from a mill vendor's view along with discussing the development for the selection and configuration of the various dty grinding circuits.

Jan 1, 1998

By N. D. Jagger, I. M. Arbuthnot

The recovery and destruction of cyanide in gold tailings is currently a topic of great interest for both financial and environmental reasons. The environmental problem is particularly important in the U.S.A. at present with the environmental lobby waging a campaign to eliminate the problem of migratory birds dying after drinking tailings dam wate. Tough legislation with severe fines and jail sentences for company executives have been introduced in several states for exceeding cyanide limits. To reduce cyanide levels in tailings dams chemical treatment, including acidification, alkaline chlorination, the INCO sulphur dioxide oxidation process and the Degussa hydrogen peroxide process amongst others are being. used. In addition several processes are at various stages of development for the recovery of residual cyanide from gold tailings. Among these is the process developed by Cyprus Gold and pilot tested by DSIR Industrial Development. This process uses air to strip cyanide from the acidified barren pulp and will be used at Cyprus Gold Mines Golden Cross Mine on the Coromandel Peninsula in New Zealand (Fricker & OWers 1990).

Jan 1, 1991

By W lethlean, Laurie Smith

When coarse gold is present in an ore, there are advantages in physically recovering this gold in the grinding section of the ore processing plant. This reduces the risk of the coarse gold being locked up in the grinding section equipment, reduces the quantity of activated carbon to be eluted and reduces the risk of gold passing out of the cyanide leaching circuit only partially dissolved. The free gold may be recovered by various mechanical means utilising the significant difference between the specific gravity of the gold and waste minerals. Frequently, sulphide minerals and ball mill attrition steel in the form of fines and chips are present in the ground ore and behave in a similar manner to the gold in the concentrating process. These materials must be removed to produce a concentrate suitable for direct smelting and several stages of cleaning, sometimes utilising different physical principles, may be required. The removal of these materials invariably results in a loss of gold from the final concentrate. The rejected materials containing significant quantities of gold are returned to the grinding section, consequently the opportunity for a high and early recovery has been lost. The quantity of gold returned to the grinding section will vary according to the number and type of cleaning stages and the physical characteristics of the materials and the gold but surveys of the gravity concentration processes suggest that it may be as high as 50%. To maximise the recovery of gold from the primary gravity concentrate, some operations batch cyanide leach this concentrate with or without additional reagents. The method of agitation and solution recovery vary. The most common method of agitation is by a high-speed propeller mixer and the least expensive but time-consuming method of solution recovery is by decantation after settling and by repeated decant washing. The pregnant gold solution is either introduced into the main ore leaching circuit or the gold is recovered by direct electrowinning. After commissioning in 1994, Union Reefs Gold Mine (URGM) experienced below expected recovery of gold from the gravity concentrate generated from the Knelson Concentrators. It was shown that the recovery into the Knelson Concentrate was high but that the subsequent mechanical concentrating techniques of tabling and magnetic separation resulted in significant gold being returned to the grinding circuit.

Jan 1, 2000

By Donald H. Sargent

This paper focuses upon the changing character of the market for Western bentonite, and upon transportation methods and costs affecting this market. The basis for the data in this paper, in addition to public sources of information such as federal and state government agencies and the open literature, was a program of 57 face-to-face interviews with individuals knowledgeable in the bentonite production, consumption, and transportation industries. The study was performed in 1974 and 1975 by Versar Inc., for the Bureau of Land Management, Department of the interior.*

Jan 1, 1979

By A. H. Reitsema, Hans E. van Dam

In CIP, CIL, and Heap Leach gold recovery operations, a sub-optimal activated carbon performance invariably causes a significant loss of revenues. In this paper it is shown, how dedicated analyses of carbon samples can be used as a guide in plant performance optimiza­tion. Firstly, a brief outline is given of the most important methods of analyses, including the specialized methods not normally used by mining operations, but provided by carbon manufacturers. Then, a number of practical cases are discussed in which carbon sample analyses provided insight which allowed significant improvements.

Jan 1, 1995

By J. L. Waldron

This paper presents a theoretical tool used to analyze gold recovery problems at Dee Gold Mining Co. The first step in addressing the problem was realizing that lower gold extraction was linked to high silver grades, and could not be correlated to either the carbonaceous or sulfidic content of the ore. Analyses of metallurgical testwork, blasthole, and mill recovery data demonstrated that decreases in gold extraction correlatP� well to increases in silver extraction. Figure 1 illustrates this for 1991 mill operations. This was the starting point for the work described in this paper.

Jan 1, 1992

By Jeffrey R. Kelly, Paul M. Kubera, Richard A. Howk

Mixing of solid-liquid slurries is a unit operation that is widely encountered in the minerals processing industry. Applications may range from simple slurry storage in open tanks to complex chemical reaction systems under extreme conditions of temperature and pressure. The specific process requirements dictate both the degree of mixing required and the type of agitation employed to achieve the desired results.' Many continuous-flow process applications feature tanks operating in series to provide a discrete number of stages and a known residence time for the slurry. Because these tanks operate at a constant level in an overflow mode, the mixer must maintain uniform solids concentration and size distribution throughout the tank; failure to achieve uniformity results in accumulation of coarse solids in the tank, ultimately leading to a process or mechanical failure. Downward-pumping, axial-flow mixing impellers are widely employed to produce uniform solids suspension. The specific impeller type, number, size, and power draw is a function of each given situation. The use of high-efficiency, fluid-foil impellers (Figure I) has evolved as a recognized standard for these flow­controlled applications. Recent small-scale experimentation and full-scale experience has demonstrated that, when uniformity is required, capital and operating expense can be minimized by employing an additional upper impeller pumping in the upward direction.

Jan 1, 1995

By Michael Brittan

The Delkor Linear Screen represents an important screening innovation in the minerals industry. Applications geared to the enhancement of gold processing efficiency through coarse screening are presented. Recent developments in the use of the Linear Screen as a fine screening classification device in mill circuits are also discussed.

Jan 1, 1998