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By Richard Ladyman, Ken Baxter, G. B. Siddall

The IPS process, developed by Baxter and McAuley, was first applied in Australia in 1984 at Browns Creek in NSW where a small 300kg batch plant was in operation for a number of years. To date a further 14 plants have been installed. While a number of engineering companies have engineered applications of the technology, a majority of the plants constructed to date have been constructed by Como Engineers who have a reference list of 9 installations with batch capacities up to 3.0 t.

Jan 1, 1996

By J. H. Lammers, John Turney

The Eskay Creek Project was interesting in many respects, includ­ing extremely high grade of precious metals, refractory nature of the ore, carbonaceous content of ore resulting in preg robbing, and high content of many heavy metal sulfides in addition to the usual iron sulfides. Although the process plant was never constructed, extensive testwork was conducted and a flowsheet for the treat­ment of the effluent form pressure oxidation was developed as a basic engineering package. The flowsheet included removal of iron and gypsum by neutralization, selective recovery of copper by zinc precipitation, and recovery of zinc by solvent extraction and electrowinning. The zinc recovery produced a significant impact on the project economics. The waste water from the process met the environmental requirements for British Columbia.

Jan 1, 1996

By G. A. Hayes

The range of gold ores tested at AMMTEC LTD over several years has resulted in the requirement to analyse for the mode of occurrence of gold in order to assist selection of ore processing options. The aim of this paper is to describe the laboratory testwork and analytical procedures which have been of benefit in detail­ing the mode of occurrence and mineral associations of gold and hence being of value in developing an optimised ore processing route. The range of ore and mineral assemblages described include relatively simple pyrite and free milling ores, more complex pyrite plus arsenopyrite gold ores and the quite com­plex associations of gold in copper bearing ores or with car­bonaceous mixed sulphide ore assemblages. The aim of this paper is to describe the laboratory testwork and analytical procedures which have been of benefit in detail­ing the mode of occurrence and mineral associations of gold and hence being of value in developing an optimised ore processing route. The range of ore and mineral assemblages described include relatively simple pyrite and free milling ores, more complex pyrite plus arsenopyrite gold ores and the quite com­plex associations of gold in copper bearing ores or with car­bonaceous mixed sulphide ore assemblages.

Jan 1, 1996

By Shawn Healey

The Mineral Hill Mine, owned and operated by TVX Gold Inc., is located in the Beartooth Mountains, 5 miles north of Gardiner Montana, U.S.A., which is the north entrance of Yellowstone National Park. Mining is carried out underground using ramp attack cut and fill as well as room and pillar mining. The mine currently employs approximately 145 people and is producing 550 tons per day at a grade of around .21 oz/ton.

Jan 1, 1996

By Gerd A. Schroth

For many years, the automatic preparation of samples prior to elemental analyses has become quite common in several indus­tries, including aluminum, cement, non-ferrous and steel. Modem automatic preparation of powdery, granular or metallic samples which initially emerged as leading edge technology, has become state of the art and a proven technology.

Jan 1, 1996

By I. Dunlop, A. Goulsbra, R. Dunne

Mineral liberation or more aptly the particle size at which cost effect liberation is attained is an important mineral processing parameter. This implies that not all the mineral is liberated as further size reduction is not economically warranted. For ores of low grade minimising both the comminution capital and operating costs are crucial aspect to ensure project visibility. As a consequence the focus of attention for the most part is direct­ed to 'coarsening the grind" ahead of any downstream process­ing treatment. In most cases, recovery will be sacrificed to pro­vide for 'more tonnes' of capacity and in general this is eco­nomically justifiable. Preferential liberation and its measurements is an aspect of mineral processing that has created much attention and contro­versy. It is not the purpose here to discuss this matter in depth other than to state in broad terms that if an ore from the same source is subjected to comminution by two different methods, such that the product particle size distribution is similar, and subsequent downstream treatment demonstrates substantial dif­ferences in recovery, then there is reason to believe that prefer­ential liberation has occurred. Comminution by high pressure grinding rolls (HPGR) is a relatively new technology claimed to have two major advan­tages over conventional comminution. Firstly and more impor­tantly is the ability to improve comminution power efficiency. Power reductions of 10 to 40 percent being claimed. (Pagett et al (1995), Sargent (1995)). A secondary benefit claimed is that preferential liberation can occur. Generally, for HPGR there is a natural tendency of the product to have a skewed particle size distribution to the finer size. This in its own right could manifest itself in improved leaching and preconcentration performance. The question remains that if in using another comminution device, other than a HPGR, to produce a similar product size distribution as the HPGR, will there be any difference in downstream between the products from this and a HPGR.

Jan 1, 1996

By E. J. Rogans, W. N. Cartner

Carbon technology has largely superseded filtration plants as the more acceptable gold recovery technology. This has, over the last two decades, provided a tremendous driving force for the development of new equipment. One of the main focus areas of this technological development is the development of effi­cient interstage screening systems. Several variations of exter­nal and internal screens are available, with the more recent shift away from air cleaned units to mechanically swept units. This paper discusses the development of one such mechanically swept interstage screen and how the development led to the suc­cessful implementation of a carousel type of CIP operation. The first generation Pump-cell emerged as a consequence of the success achieved with the mechanically swept NKM screen, The idea was to modify the screen to incorporate the functions of pumping, screening and agitation in a single drive unit, the screen generating sufficient lift for interstage slurry flow so that all contactors would be at the same level. This sys­tem was further incorporated as a high intensity modular CIP contactor, i.e. low slurry residence times combined with high carbon concentrations. A discussion on the kinetic gold adsorp­tion theory and its manipulation in the design of the pump-cell concept is discussed in a paper published in a previous Randol Conference< 1), Testwork carried out at Vaal Reefs proved the concept of the Pump-cell on a pilot plant scale<2), which resulted in the building in 1990 of the first large Pump-cell plant at West Witwatersrand Gold Mine designed to treat 340m3 of pulp per hour and , even though the plant operated successfully with respect to gold recovery performance, a few problems were experienced with the basic engineering design(3),

Jan 1, 1996

By Dan Mackie

Commissioning of a 150 tpd continuous vat leaching pilot plant at Ariel Resource's San Martin Mine began in October, 1995. Functioning of the systems proved to be as designed. Initial tri­als, however, were besieged with problems associated with clay fractions that were much higher than in the ore originally tested. Nevertheless, leach rates were good in the initial and subsequent trials. Difficulties with the viscous solutions generated by the clay fraction continued, requiring modifications to the solution collection methods and investigation of flocculant types and mixing points. Trials with deslimed ore and sand feed demon­strated continuous flow. Current modifications will be tried in late May, 1996, along with selected flocculants, with the objec­tive of leaching continuously without the need to deslime.

Jan 1, 1996

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 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 Douglas R. Shaw

The results are discussed herein of laboratory and pilot scale research which has demonstrated some exciting prospects for the exploitation of refractory gold resources by heap leaching. The research examined practical and cost effective methods of chemical; i.e., non-biological, oxidation pretreatment of refrac­ tory old ores to enable successful conventional cyanide heap leachmg. The work has focused on regenerable chemicals, in order to minimize process consumable costs. A nitric acid method has emerged which offers rapid oxidation rates (eg, 0.5 to 6 hours) on ore samples crushed typically to% to ¾-inch. Gold recoveries in simulated heap leaching tests, after nitric acid oxidation of crushed ores, were as high as approximately 80 to over 90%, in contrast, typically, to negligible gold solu­bilities without oxidation. Nitric acid oxidation was effective when applied to several sulfide-bearing refractory gold ores which required either partial or essentially complete sulfide sul­fur conversion for high gold solubilities in cyanide. Ores rich in organic preg-robbing matter also were treated successfully, as were ores which contain significant quantities of acid-consum­ing constituents. Base metals also were recovered with nitric acid oxidation from some of the ores which contain these ele­ments. The work related oxidation and solution diffusion behav­iors and the important physical, textural, and mineralogical characteristics of the different ore types. Conceptual-level feasi­bility studies have defined the principal capital and operating cost components of the nitric acid method, sufficient to allow reliable comparisons with other oxidative technologies.

Jan 1, 1996

By E. A. Devuyst, G. H. Robbins

The Inco process can be retrofitted into a typical heap operation with minimum capital. Capital cost for a mid to large size heap would be less than 1 cent/ton. Operating costs are typically in the order of 8 cents/ton. Ammonium bisulphite is the preferred reagent. The process provides the equivalent of fresh water r?1s­ing and thus minimizes the time of the _nnse program. A typical heap (the Snow Caps Mine, California) was rinsed completely

Jan 1, 1996

By Chris Campbell-Hicks

Methods used for assay of gold values in resource estimation, grade control or downstream processing are based almost entire­ly on Fire assay or Aqua Regia techniques. Both these tech­niques frequently produce spurious results. The mechanism of error is explained. Major decisions are made based on this often flawed data. This is what our operating budgets and projected cash flows are based on. Project economics demands metallur­gical accountability for performance predicted. Accountants and more astute members of the board are often not sympathetic to gold out-tum from plant production which is occasionally or consistently less than that predicted. Equally importantly, better than budgeted gold out-tum, resulting from under assaying will produce reconciliation or accounting problems (surplus cash flow) often denying correct timing of expansion or acquisition. Both these scenarios can be avoided if 'real world' extractable gold values are presented to financial managers at all stages. Such extractable gold results are now possible, and compared to fire assay and aqua regia, the assays are faster, cheaper, simpler and more accurate.

Jan 1, 1996

By Neil E. Izatt, M. Andre de Ruijter, Ronald L. Bruening, Wesley Young

IBC Advanced Technologies, Inc. has developed ligands, ?amed SuperLig®, which have specific applications in the gold mdustry. These ligands use molecular recognition technology (MRT). One ligand has been developed to selectively recover gold and silver from tailings solutions and from pregnant Merrill-Crowe solutions. Another ligand removes free cyanide, _ th10cyanate, other cyanide species, as well as copper and other base metal cyanide complexes from leached gold-ore solutions. The development of these "species selective'' SuperLig® prod­ucts allows for the more efficient operation of gold recovery processes and opens up the possibility of the economic devel­opment of high-copper gold ores. The resulting gold eluate is a high grade and a high purity stream which will simplify the need for further refming. Engineered systems based on MRT consist of a few unit operations utilizing standard equipment and mate­rials of construction. The process is simple to operate, thereby lending itself to automated modular design, which is both eco­nomic to manufacture and to operate. Test results for the gold and cyanide-copper systems are presented in order to demonstrate the high selectivity and effi­ciency of MRT technology in recovering these species from solution. . IBC Advanced Technologies, Inc. (IBC) and Fluor Daniel, Inc. formed a strategic alliance in late 1994. The goal of the alliance is to combine IBC's scientific expertise in the MRT field with Fluor Daniel's engineering capabilities in the metal­lurgical industry. IBC has its headquarters in American Fork, Utah, USA, where research, development and manufacturing are conducted. Fluor Daniel is an international engineering and construction firm with head offices in Irvine, California, USA. Engineering efforts for the alliance are centered in the Fluor Daniel Mining and Metals Operating Company office in Vancouver, B.C., Canada.

Jan 1, 1996

By Daniel W. Kappes

The 1.8 million tonne Itos tailings deposit is the result of sever­al years of processing by Comibol of the San Jose and ltos Mine ores at Oruro Bolivia. The historic flowsheet consisted of a flotation circuit in which silver-bearing galena and stibnite were concentrated. Approximately half the silver in the ore was not recovered, and the existing tailings contain slightly over 200 grams silver per tonne, in the form of complex sulfides of silver, antimony, lead, and other metals coating grains of pyrite. An extensive laboratory program was conducted to exam­ine conventional processing l)lethods such as cyanide leaching and regrinding followed by flotation. However, the silver-bear­ing sulfides are in intimate contact with the pyrite and the pyrite comprises 30% of the total tailings weight. Cyanide leaching recovers only 40% of the silver and the cyanide consumption is uneconomically high. Flotation produces an upgraded, but still uneconomic, concentrate. For this reason, chloride leaching had been evaluated by Comibol, and in the mid 1980's Comibol undertook an innova­tive test consisting of two 300 tonne field heap leaches using a cold chloride solution. The tests were partially successful, but could not be applied to the bulk of the tailings which are already ground to 50% minus 200 mesh. In 1992, Kappes, Cassiday & Associates undertook to develop a hot agitated chloride leach flowsheet, and is current­ly constructing a treatment plant under a turnkey contract from a Bolivian company, Baremsa, S.A. Using this process, 85% of the remaining silver can be recovered, with significant by-prod­uct credits from antimony and lead. The project features hot, agitated acidic chloride leaching, filtration, crystallization of lead chloride, and precipitation of metals using iron scrap. Arsenic is removed from the precipitate by caustic leaching, and minor metals by furnace refining. Antimony is recovered as the oxide by cupelation, and silver is poured as <lore from the cupel. Production rate will be 600 tonnes per day. Startup is scheduled for late 1995.

Jan 1, 1996

By Norbert Patzelt, Johann Knecht

Future ore reserves of major gold producers in North America and elsewhere will consist of refractory gold ores. About 60 % of the current U.S. gold production is mined in Nevada. Several of the large gold operations in this state indicate that 40 to 90 % of their future ore feeds will contain refractory gold. To com­pound problems, average head grades for refractory U.S. gold ores had fallen from 8 - 9 g/mt to about 4 g/mt by 1991. In Latin America, 52 % of the gold operations will require milling for optimal recovery. Deeper reserves are, like in North America, refractory. Therefore a special treatment process is needed in order to allow for the gold ore to be leached downstream in a conven­tional cyanidation process for a high gold recovery. There are several options available for this oxidation process like treat­ment of the gold bearing ore in pressure oxidation, in a biooxi­dation or in a roasting plant depending on the reason for the refractoriness. If organic carbonaceous matters and sulfides are the prima­ry reasons for the refractoriness, whole ore roasting is a pre­ferred method for the treatment of this type of ore. Since dry ore is to feed to the roaster, a dry grinding mill is advantageous. For the dry grinding system, the moisture content and the ore char­acteristic is of importance. Those parameters decide the mode of the grinding system. For autoclave systems common wet grind­ing systems can be applied. This paper deals with technical aspects for dry grinding plants and gives an outlook on and pos­sibilities for new grinding systems.

Jan 1, 1996

By Paul A. Lahti

Independence Mining Company, Inc. (IMC) has for the past several years processed refractory gold ores at its Jerritt Canyon operation near Elko, Nevada. The ore is typical of those of the Carlin Trend and is refractory due to physical encapsulation of gold in carbon, pyrite, and arsenopyrite. It is also "preg robbing" due to the contained organic carbon that acts as a gold adsorber. Refractory ores require some form of pretreatment before cyanidation to enable economical recovery of gold. The metallurgical facility at Jerritt Canyon is unique in that it consists of two distinct pretreatment methods for the recovery of gold: a chemical process utilizing chlorine and a pyro-metal­lurgical process employing oxidative roasting. This paper pro­vides a comparison of the two methods highlighting flow sheets, pretreatment operation detail, performance comparisons, and pertinent environmental data.

Jan 1, 1996

By Eberhard Stolarski, Michael Tacke

When the oxidized surface gold deposits are mined out, the underlying refractory gold ores become the challenge of treat­ment systems. The size and value ofrefractory gold ore reserves are a function of recovery efficiency and operating cost. The start-up of LURGI's gold roasters at NEWMONT's Carlin site has established whole ore gold roasters as a key to high gold recoveries. The ores from several deposits of the Carlin trend are roast­ed utilizing LURGI / NEWMONT technology, which has achieved gold recoveries approaching 95%. This is in dramatic contrast to the traditional perception that roasting is limited to gold recoveries in the mid 80's. Extensive investigation in pilot scale is required to achieve stable high gold recoveries for most variables in the ore body. The key question for all pilot tests is the classic question of (ROM) run of mine ore roasting or concentrate roasting. All variables are dominated by the leaching/ recovery char­acteristics of the natural ores. The degree ofrecovery improve­ment by roasting / calcining establishes the frame of the eco­nomical conditions. The full range of flexibility is required for the design of the plant to allow for ore variations in heat values, combustible con­tents, agglomeration behavior and off-gas composition. The variables in the ore body influence, therefore, the price of the plant proportionally to its flexibility. Concentrates are usually fairly stable in composition, com­bustion behavior, heat values and particle size since they are a product of the very selective flotation process. Flotation is not the successful process step when the tailings remain high in refractory gold contents.

Jan 1, 1996

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 J. E. Cressman, Raj Devarajan

The declaration of bankruptcy by the operator (Summitville Consolidated Mining Company, Inc., SCMCI) of the open pit heap-leach operation at Summitville and the subsequent takeover of the minesite by the USEPA has been a high profile and largely painful event for the mining industry. Shadowed by the ovrall picture has been a continuous effort by technical and operational personnel to treat contaminated water and improve water quality while satisfying various management strategies and budgetary constraints. Summitville's operations history can thus provide a body of knowledge potentially beneficial to operators and managers of present and future mining projects presenting challenges from similar geology, mineralogy, topog­raphy, climate, water chemistry, financial and regulatory ele­ments. This discussion focuses on water treatment operations that occurred at the minesite, initially as part of mining production and reclamation, and later as part of USEPA's emergency response and remedial efforts. All of the treatment efforts have targeted the cyanide and metals contamination associated with process waters from the heap leaching activities, and acid mine drainage (AMD) containing metals such as copper, iron, alu­minum, manganese, and zinc in high concentrations.

Jan 1, 1996