Search Documents

By Artmont G. J, Palmer K

Alluvial gold is an ideal exploration tracer to bedrock source and indicator of bedrock mineralisation style because (i) gold occurs in a wide range of deposit types, (ii) primary composition is sensitive to style of mineralisation, and (iii) it is a heavy resistate mineral that is readily preserved and easily sampled. In regional exploration of the Central Ranges of Irian Jaya, alluvial gold mineralogy has been applied to maximise the information return from panned concentrate sampling and to focus exploration effort. Primary gold is a solid solution of Au+Ag¦Cu¦Hg, ¦ trace Pd, Te, and Sb. In general Ag¦Hg increase and Cu decreases with inferred decreasing temperature of formation, and gold from particular mineralisation styles has signature compositions that can be used as indicators of bedrock mineralisation type. Furthermore, the abundance of alluvial gold is an indicator of the economic potential of a catchment. The convergent continental-oceanic plate geology of the Central Ranges is conducive to a wide range of mineralisation styles. Mineralogy of gold in ophiolite, skarn, porphyry, mesothermal vein and possible VHMS environments is characterised from alluvial and bedrock samples, and the use of gold mineralogy in prospecting at regional scale through prospect definition to drilling is demonstrated.

Jan 1, 1995

By Isaev EN, Levin LE

New data on the geology of the Late Jurassic to Holocene sediments cover of the World and associated mineral resources (oil, gas, ferromanganese nodules, ores of massive sulphides and other metals) have been compilled in the Atlas at scale 1:25,000,000 and 1:10,000,000. The work was performed by scientists from four Institutes of Russia (VNllzarubezhgeologia, VNlloceangeologia, Vernadsky Institute of Geochemistry and Analytical Chemistry of the Russian Academy of Sciences and Geological Institute of the Russian Academy of Sciences). The Atlas shows variation of thickness and formational composition of the large complexes (Upper Jurassic-Early Cretaceous, Upper Cretaceous- Eocene, Oligocene-Neogene, Pliocene-Pleistocene), distribution of oil/gas and ore deposits in each complex, data of deep- sea drilling (leg 1-130), thermo-pressure condition in the sedimentary basins within Circum-Pacific Rim.

Jan 1, 1995

The Central Andes in Peru, Chile, Bolivia, and Argentina, contain two contiguous terranes which were accreted i, Gondwanaland between the end of the Devonian and the end of the Triassic. These terranes, Arequipa in the north, anni Chilenia in the south, differ from each other in the timing and style of their metallogenic development. However, they contain over 90% of the Central Andean porphyry copper resource. The copper porphyries in the Arequipa terrane are Paleocene to lower Oligocene in age, whereas the Chilenia deposits are mid-upper Cretaceous and mid-upper Miocene. Porphyry copper deposits occur outside these terranes, but are all Miocene in age. Miocene porphyry-style mineralisation also exists in the Arequipa terrane, but is copper-deficient and gold-rich. The accreted terranes may have favoured porphyry and other styles of copper mineralisation because they possessed relatively thin continental crust compared to adjacent parts of the Andes. Crustal thickening which commenced at about 30 Ma in the Arequipa terrane coincided with a major change to polymetallic, precious metal mineralisation which commonly displays high sulfidation charcteristics.

Jan 1, 1995

By David A. Collins

Red Dome Gold Mine classifies ore types within the pit by gold and copper grades. Copper grades are further distinguished by total copper and cyanide soluble copper levels. At present, Cyanide Soluble Copper samples take six hours of agitating before they can be assayed. This agitation time produces results which are a proportion of the total cyanide amenable copper. This relates to our plant's performance. Frequently the total copper result is needed before we can begin the cyanide soluble copper analysis. This caused a protracted tum around time. Mennetech Pty. Ltd has produced a catalyst proven by David Martin Menne to accelerate the cyanidation of gold. David said that the information at hand indicated that Leach WELL TM also accelerates the leaching of cyanidable copper substantially. Test work was undertaken on-site at Red Dome Gold Mine to investigate the potential of Leach WELL TM to reduce the leaching period and therefore, the overall tum around time required for cyanide soluble copper determinations.

Jan 1, 1995

By Darryl J. Butcher

The Akjoujt Project is operated by MORAK SA, a company incorporated in the Islamic Republic of Mauritania. MORAK is jointly owned by General Gold International SA (A wholly owned subsidiary of General Gold Resources NL.), SAMIN, and the International Finance Corporation. The project was devel­oped to treat approximately 2.1 million tonnes of TORCO (Treatment of Refractory Copper Ores) tailings containing an average 3.2gAu/t, and 0.75%Cu/t. The process involves the use of ammoniacal cyanidation for gold extraction, and conventional carbon adsorption, and eventual desorption, of gold values. This is believed to be only the second commercial application of this leach chemistry in the world. The other being a small vat leach operation on the Paris Mine Dumps. (This operation was described by Mr M Ruane in a paper to a previous Randol Forum.) Initial work on the process, and the Akjoujt process design assumed that the reaction involved was anaerobic. This paper describes the operating experience, plant trial, and eventual installation which has lead MORAK to the conclusion that the process is not anaerobic, but requires oxygen, or an oxidant to proceed.

Jan 1, 1995

By Robert S. MacPhail, Bret G. Cousins

Many copper-bearing ores with associated gold use Sodium Isopropyl Xanthate (SIPX) as a flotation agent. In general, SIPX will float to some extent other minerals that may not be desirable, such as pyrite. FLEX 31 is a chemically enhanced SIPX product with many of the same properties as SIPX. But FLEX 31 has the ability to reject more pyrite from concentrates and improves copper recovery when using up to 50% less FLEX 31 than is required if using SIPX. Copper activated minerals such as sphalerite and arsenopyrite show increased recoveries as well using FLEX 31. Tests have been performed on copper/zinc ores and an arsenopyrite/pyrite ore.

Jan 1, 1995

By Gary Jobson

The Mt Todd Gold Mine is owned and operated by Zapopan NL, and is located 300km south of Darwin near the town of Katherine. The crushing plant and heap leach facility, which has operated since November 1993, has recently been expanded to treat 6 Mtpa with 1995 budget gold production reaching 120,000 oz from a head grade of 1.12 git. The process flowsheet and equipment are described, with innovative key features including:

Jan 1, 1995

By Mike D. Adams

Testwork was conducted on loaded carbon samples from a small gold mine in South Africa. It was shown that a 75% saving in reagent consumption in the Zadra elution circuit could be achieved by adopting a cyanide-free elution approach, i.e. by cutting back the NaCN level from 1 % to nil, and the NaOH level from 3% to 1 %. This process change was also shown to result in a 20% improvement in the elution kinetics. Furthermore, it was also shown that a 50% enhancement in elution rate over the current situation could be achieved by use of an eluant containing 0.5% NaOH and 0.15% NaCN, corresponding to an 84% saving in reagent consumption. A further improvement in elution kinetics was found to occur by increasing the NaCN level to 3%, but this would lead to a concomitant increase in reagent consumption, due to the decomposition of cyanide at high temperatures. The presence of base metals loaded onto the carbon was also found to have a significant effect on the elution. Copper tends to adsorb as Cu(CN)2- during the adsorption stage, and acid washing converts this species to CuCN. Copper in this form is not eluted during cyanide-free elution, whereas it is eluted during a conventional cyanide elution, consuming the initial cyanide in the process. The elution data was analysed and the fit to a simple model was verified.

Jan 1, 1995

By P. M. May, J. S. Solis, G. T. Hefter

Chemical speciation plays a critical role in many areas of gold processing. These include the formation of HCN in plant liquors, interference by copper in the extraction efficiency of gold, the recovery of adsorbed gold, and the behaviour of plant effluents in the environment. Thermodynamic modelling provides a cost-efficient method of rationalizing and even predicting of chemical behaviour. Unfortunately, because thermodynamic data for cyanide complexes are of poor quality and few are known under hydrometallurgical conditions. Such models are currently of limited use. This paper describes recent work on the thermodynamics of cyanide complexes of a range of metal ions. Data will be presented on the stabilities and enthal­pies (heats) and entropies of formation of a variety of metal ion species determined by potentiometry and calorimetry. Particular emphasis will be placed on the Cu(I)/CN- system.

Jan 1, 1995

By Mark W. Johns

The design or optimization of a carbon-in-pulp (CIP) plant requires the determination and setting of a number of parameters to ensure optimum economic performance. A number of these parameters are either fixed, a function of the pulp, interdepen­dent, affect other parameters or outputs, so only a limited number of degrees of freedom exist from a metallurgical point of view. The traditional CIP contactor employs a low carbon concen­tration, a low agitation intensity and a reasonably long pulp residence time. The pump cell contactor employs a high carbon concentration, a high agitation intensity and a reasonably short pulp residence time. The two philosophies are dipolar in nature and the question arises as to which configuration is the optimum configuration for a CIP plant. The carbon particle size is shown to have a small effect on the capital cost of a CIP plant. A decrease in the pulp residence time, an increase in the pulp density, an increase in the carbon residence time, an increase in the agitation intensity and an increase in the number of stages are shown to have a positive effect on the capital cost of a CIP plant. The pulp residence time, the pulp density and carbon particle size are shown to have a small effect on the operating cost of a CIP plant. An increase in the carbon residence time, a decrease in the agitation intensity and an increase in the number of stages are shown to have a positive effect on the operating cost of a CIP plant. The optimum CIP plant, therefore, employs a short pulp residence time, the traditional pulp density, a long carbon residence time, the traditional carbon particle size, the traditional agitation intensity, and the traditional number of stages. Neither the pump cell configuration nor the traditional CIP configurations match the optimum configuration.

Jan 1, 1995

By G. S. Walker, W. van Bronswijk

The accurate determination of free cyanide and metal cyanide complexes is of increasing interest to Carbon-in-Pulp (CIP) gold extraction operations as cyanide consumption is an important economic factor in the processing of complex ores. Characteristically complex ores are high cyanide consumers and these ores usually contain a range of sulfide minerals e.g. covellite (CuS), digenite (Cu1,S), chalcocite (Cu, S), Pyrrhotite (Feci-x)S), marcasite (FeS2), arsenic and antimony sulfides and zinc sulfide. These minerals can consume significant quantities of cyanide, e.g. various copper(!) cyanide complexes such as CuCN, Cu(CN)2·, Cu(CN)/ and Cu(CN)/ can form, depending on the cyanide to copper ratio in solution. Measurement of free and complexed cyanide is thus a prerequisite for efficient cyanide dosage control. Free cyanide can be determined potentiometrically or amperometrically but the methods are prone to error and are laborious [1]. Metal cyanide complexes can be determined by reverse phase HPLC, however, the species ofa single cation (e.g. Cu(CN)i-, Cu(CN);2 and Cu(CN)/) elute as one species [2]. Additionally the high amount of suspended matter in CIP leach solutions tends to introduce errors. Raman spectroscopy has the potential to be used as an in­line or on-line method of analysis. Free cyanide and the cyanides of gold, silver, copper and iron have been studied in aqueous alkaline solutions with a view to developing such a method. Spectra were obtained with a Bruker RFSl00 FT-Raman spectrometer using a 1064 nm laser delivering 800 mW of power at the sample. Depending on the solution, 250, 1000 or 4000 scans at 4 cm-1 resolution were accumulated. The cyanide stretches observed were relatively narrow (10 15 cm-1 full width at half height) and well resolved (Figure 1 ).

Jan 1, 1995

By Peter J. Stewart

My first experience with carbon reactivation in the gold industry was at Whim Creek, Meekatharra some 15 years ago. Very little was known, in fact, carbon reactivation kilns in the gold room were a complete mystery. Ten years ago at conferences such as this the mystery was more as to why field kilns would not reproduce activities achieved in the laboratory. A carbon reactivation kiln manufac­turer was thought to be brave or stupid to speak at a venue such as this. Reactivation kiln design has improved dramatically in the past 10 years and with a few exceptions, most kilns operate well. May I suggest that now, the focus is on plant practice rather than kiln design, and that the basics of plant practice as it relates to carbon activity needs revisiting. As metallurgists like to talk on engineering, accountants on the Economy and vice versa, my presentation on Carbon Reactivation will focus on plant design and operation as it effects carbon reactivation. There have been some excellent papers published over the past 15 years on the basics of carbon reactivation in relation to gold processingl,2,}. Taken that kilns operate and are effective to a greater or lesser degree, plant design and operating practise have an enormous bearing on carbon activity, solution tail, carbon loss and other cost items. This presentation will not argue the merits of equipment used for the thermal reactivation of organically fouled carbon, questions on this subject are welcome over a drink after this session.

Jan 1, 1995

By Kimberlie Staheli

A new sanitary sewer was installed in Pleasant Hill, California using microtunnelling methods. The project consisted of 693 meters of 1372 mm and 1981 mm concrete pipe. A Herrenknecht AVN 1200 was used to install the nominal 1372 mm pipe in three drives. The machine was then fitted with an oversized shield used to install the large diameter pipeline. This articulated shield allowed the excavation of a 2362 mm diameter hole with a 1524 mm machine-- a technique new to North America. This paper reviews the design considerations for the articulated shield and reports on the project challenges and solutions to overcome these challenges.

Jan 1, 1995

By D. Lelinski

Air-sparged hydrocyclone (ASH) flotation is one of the new promising technologies. Numerous applications have been successfully tested since its conception; nevertheless, research and development efforts have continued to provide for further improvements with respect to operating conditions and design considerations. Results from experimental studies on bubbles generation in the ASH system are presented in this paper. Bubble size distributions generated during ASH operation have been determined using a high-speed photographic technique. The influence of many factors including surfactant concentration, water flowrate, and porous tube pore size has been studied. Test results indicate that these process variables have a profound effect on the bubble size distribution. With an increase in surfactant concentration or water flowrate (shear field) the bubble size distributions become narrower and shift toward smaller average bubble diameters. However, the influence of pore size is more complicated. Depending on the experimental conditions the average bubble size was found to range from about 100 to 300 microns in diameter.

Jan 1, 1995

By Matsuhisa Y, Sakurai W, Shimazaki H, Peiming H, Fukahori Y

Oxygen and carbon isotope mapping of hydrothermally altered wall rocks was applied to the blind ore prospecting of skam Pb-Zn deposits in the Kamioka mining district, central Japan, where the wall rocks consist of heterogeneous rock units. The results (8180sMow of -1.1 to +17.3%o and 613CPDB of -5.0 to +4.8%o for limestones, and 8180SMOW of -0.8 to +12.5%c for silicate rocks) show isotope zonations of the wall rocks with depletions in heavy isotopes (180 and 13C) toward the center of mineralization. The isotope zonations likely formed by interaction of migrating thermal waters with the wall rocks during the mineralization. The heavy-isotope depleted zone, which indicates higher temperature or higher water-to- rock ratio of the system, occurs in the footwall of a fault, indicating that the fault played the role of main conduit of the ore-forming fluids. A heavy-isotope depleted zone was also found in an area, where significant mineralization had yet to be identified. Recent drilling in this area has intercepted a zone with a grade of 16.0% Zn, 0.8% Pb, and 35g Ag per metric tonne at a depth of about 360m.

Jan 1, 1995

By N. L. Piret

Primary and secondary copper smelting dusts are being generated in varying quantities with very dissimilar characteristics due to the different compositions of feed materials and the type of process utilized. After categorizing the multitude of dust types, the criteria for on-site and off-site recycling of smelter dust in terms of type and concentrations of the accompanying elements are established. Thereby, consideration is given to the important aspects of: ? optimization of copper recovery ? quality of copper product ? valorization of accompanying elements ? elimination and disposal of deleterious impurities ? minimization of impact on operation ? effects on operating costs ? environmental impact of dust treatment on overall process Existing commercial, emerging and proposed copper smelting dusts, pyrometallurgical as well as hydrometallurgical, treatment schemes are reviewed and evaluated technically, economically and environmentally in an attempt to streamline the vast number of proposed options. Thereby, the high selectivity achievable in hydrometallurgical dust processing due to it being complementary to the smelting process is expected to be given increased consideration.

Jan 1, 1995

By Thomas M. Keevin, Gregory L. Hempen

Natural resource agencies, under various regulatory authorities, are challenged with permitting underwater explosive use while at the same time protecting aquatic resources. Deciding on whether or not to allow use of explosives requires striking a balance between development and aquatic resource protection. A company's goal in underwater explosive use is to select methods that are both expedient and cost effective. Use of explosives is often the best alternative for engineering reasons or economic considerations. Over and above legal requirements, indiscriminate destruction of fish and other aquatic resources is not in a company's best interests because of concerns relating to public image, as well as the need to secure future contracts.

Jan 1, 1995

By William M. Luff

"The Bathurst area has recorded mining production as early as 1837, although the bulk of the production has come in recent years. Production has been mainly from the well-known massive sulphide deposits, but vein, gossan, and a variety of other deposits have also been mined. This paper summarizes the history of the mined deposits, along with tonnages and grades produced.A number of ""firsts"" have been noted in the Bathurst area. The A Zone deposit, located in the Heath Steele area, was the first in the world discovered using airborne electromagnetic methods. Heap leaching of gold from the gossan zone at Caribou was the first operation of its kind in Canada. The Keymet mine was the first base metal (lead-zinc) mine in New Brunswick. For the past few years, the Brunswick No. 12 mine has been one of the largest zinc mines in the world.IntroductionThe Bathurst area (Fig. I) first had mining production in 1837 when copper was mined from a deposit on the Nepisiquit river (MacKenzie, 1958). The majority of the production, however, has been in recent years from massive sulphide deposits, but there are also other significant operations.Table I is a summary of Bathurst area mineral production, showing concentrator feed tonnages and mill feed grades. The table does not include peat deposits, sand and gravel, dimension stone or rock quarries. Figure I is a general geology map of the Bathurst area, indicating deposit locations. The deposits are divided into four categories: massive sulphide, vein, gossan and other. The deposits in each category are described in chronological order of exploitation."

Jan 1, 1995

By Greg Brown

The underwriting of professional negligence has proved to be an evolving science. As with most insurance products coverage offered in the past was very broad but as legal precedent demonstrated to Insurers areas of unforeseen exposure policy documents per se have become more restrictive until today the insurance market through attrition have produced a basic policy structure with various purchasable extensions which together provide insuring professionals with coverage that has proved to be adequate for their needs. The basic policy provides indemnity and protection for fortuitous negligence. In a practical sense, however, professional indemnity policies are really a defence document in so far as policy holders are relying upon the expertise of Insurers to protect them in the event that a claim is made upon them. Whether damages are awarded is in many respects a secondary consideration, the most important factor is to ensure that policy holders are protected in terms of the legal defence mechanism. By way of illustration we are currently in the process of defending a large professional firm which purchased from us a policy with a limit of indemnity of $10M. The case has been running in a Supreme Court now for 14 months and the defence costs which we have incurred on their behalf are rising close to $8M as I put pen to paper. Defence costs of that magnitude would in effect terminally cripple all but the very largest professional operations in Australia. In more recent times coverage has been provided in Australia for breaches of the Trade Practices Act and similar legislation enacted in various States. No-one really appreciated the comprehensive impact which the Trade Practices Act would have on commerce in Australia. Most professionals thought that indeed they would be exempt from prosecution under this Act. The passage of time has clearly indicated that this is not the case and we have found that it is much more difficult to defend a claim involving breaches of the Trade Practices Act than it would be to defend a claim for breach of tortuous liability.

Jan 1, 1995

By Sammy Bansah, Komla Dzigbodi-Adjimah

Ghana, a major West African gold-producing country, took a crucial step in 1986 to allow private participation in mining ventures that had hitherto been state controlled and starved of funds. This decision has led to a three-fold rise in gold production with substantial local and foreign capital once again flowing into exploration and mining projects. Though the rise in gold export is due primarily to increased production from large mines such as Ashanti Goldfields Corporation, Billiton Bogosu Gold, Tebrebie Goldfields and Ghana Australia Gold that work primary lode gold deposits on quartz veins and Banket conglomerates, a fair amount of gold comes from placer gold mining from which two new mines have been developed at Kwabeng and Bonte during the current gold boom. Also, placer gold mining is important locally because the lower capital outlay required for its development enables many entrepreneurs to operate small concessions and provide employment for a large pool of unskilled labor. Placer gold exploration and development in Ghana is labor-intensive. Pitting is the most used method although few employ the mechanized (“Banka”) drilling. The advantages and disadvantages of the two approaches in the local setting are discussed. The gravel is normally sluiced and the gold recovered by amalgamation. The drawbacks to successful placer gold exploration in Ghana have been attributed to lapses in execution of exploration programs (Dzigbodi-Adjimah and Arhin, 1993; Dzigbodi-Adjimah and Gawu, 1994). However, the failure to recognize and set time frameworks and financial limitations for the various stages of placer gold exploration have spelt the doom of some projects. It is critical that the characteristics of the placer gold deposit be determined by efficient and cost effective means. A planned exploration supported by adequate flow of funds saves costs and leads to success. This article discusses the current Ghanaian situation and presents proposals from case studies for planning and budgeting placer gold exploration pro-grams for use in similar settings.

Jan 1, 1995