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The ER&S Company operates a copper sinter plant, blast furnace and converter smelting complex at Port Kembla. Eighty percent of the smelter feed is dirty copper concentrates that contain some lead and zinc. The remaining twenty percent of the smelter feed is copper bearing secondary materials, some of which contain lead, zinc and tin. A predominately lead/zinc fume is produced during the smelting and converting of this feed mix. The composition and tonnage of fume produced at Port Kembla has varied over the years as the smelter feed sources have changed. The economic processing of the fume has always been dependent on the value of the metals contained in the fume and on the fume composition. Both pyrometallurgical and hydrometallurgical methods have been used to treat the fume for the recovery of some or all of the following metals - lead, zinc, tin, copper, cadmium, silver and bismuth. A detailed description of the treatment methods that have been investigated and used to process ER&S fume is given.

Jan 1, 1984

By D Millette, F Gay

Surface tailings are finely ground waste materials produced in all mines after the mineral or metal has been removed from the metallurgical process. Current methods for disposal of tailings involve constructing dams, dumping into existing waterways, and depositing as backfill underground. Each method has its drawbacks in terms of cost, level of complexity, safety and environmental concerns. Backfilling is the process whereby waste material (generally metallurgical tailings, prepared aggregates or a combination) is placed from the surface back underground into open mine workings via conveyor belts, hydraulic or pneumatic pipes or gravity. In the backfill process common difficulties are expensive placement costs, equipment wear and the ability to meet early and long-term strength requirements. Traditional tailings transportation in pipes involves the use of water as the transport medium. Foam technology involves the introduction of micro-air bubbles that replace the water as the main transport medium. This air can be removed after placement if necessary, by the addition of a defoaming agent. This could produce an under-saturated stable cake. Foam technology has the potential to revolutionise surface tailings disposal and backfilling by providing a less expensive and environmentally safe alternative to those just described.

Jan 1, 2000

Due to collapsing copper prices during 1974/75, a rapid changeover was made at the C.S.A. mine from mechanised cut and fill stoping with incline access to the more economic long hole open stoping method. In 1974/75, 20 per cent of total production came from open stopes. For the 1976/77 year-to- date, more than 80 per cent of total production has been won from open stopes. As a result, mining performance has improved considerably. Stops, drilling performance has increased by more than 50 per cent since the changeover from extension rod, 50 mm diameter cut and fill uphole drilling to 115 mm diameter in-the-hole hammer drilling of holes up to 65 m long. Stops blasting performance has improved from 750 tonnes to 950 tonnes blasted per manshift. Open stope primary blasting per- formance is much higher, but reduces to 950 tonnes per manshift when secondary blasting and firing of hung drawpoints are taken into consideration. Ground control, the most expensive and least productive aspect of cut and fill mining, is almost entirely eliminated in long hole open stoping.

Jan 1, 1977

Deep lead mining by methods other thanconventional open-cut techniques has not been effectively employed in Australia in -the second half of this century. The reasons for this are essentially economic, and are related particularly to the labour intensive nature of the methods involved as well as the high consumption of support materials. These methods have been adapted in recent times to undertake bulk sampling programmes in deep leads. Although some consideration is given to surface-oriented hydraulic and solution mining applications, the prime function of this paper is to investigate the possible application of modern underground methods to deep lead exploitation. As deep leads are not currently being worked (with the exception of some minor operations on the Eastern seaboard), these applications remain essentially untested. They have, however, been conceptually developed following several years of small scale deep lead development. Current mineral economics, particularly with respect to gold, combined with the known extent of partially - or totally - unexploited mineralised leads demonstrates the necessity to investigate all possible means of ore extraction.

Jan 1, 1985

The subject of the present paper will be combustion of fuel and as the combustion of fuel requires a certain amouut of air to effect combustion the question might be asked what is air?Air is composed, we will say, principally of two gases, oxygen and, nitrogen, but our business is with the former gas, and its leading feature as a supporter' of combustion. In point of fact no fire will burn without its presence, nor can animal life be sustained when this gas ls absent, because it is the life-sustaining element. For example, if we take a piece of charcoal, which is pure carbon, and burn it in the open air combustion takes place in the union of the carbon of the charcoal with the oxygen of the air, forming the compound known as carbonic acid (0.0.)The rust we see on iron and other metals is a kind of slow combustion, which is termed oxydation. When oxygen unites with any other element heat is given off in the process, and it may be here stated that the most intense heat is produced, by burning the two gases-oxygen and hydrogen in precisely the same proportions as that forming water.

By H R. Watli, K L. Davies, J A. Johnson

Novel microbial isolates that readily oxidise iron and sulfur were recovered from samples collected from a spent chalcopyrite/pyrite test heap. Methods were developed to enrich and isolate microbes that thrive in low pH environments and utilise iron and/or sulfur as sources of energy. Screening of these isolates revealed diverse substrate utilization (sulfur, ferrous ion, chalcopyrite, pyrite, glucose) as well as growth at temperatures between 30 - 50¦C. When native isolates were employed, shake flask leaching tests of chalcopyrite concentrate resulted in higher copper yields in comparison to laboratory reference strains Acidithiobacillus ferrooxidans (DSM 583) and Sulfobacillus thermosulfidooxidans (DSM 9293). After 700 hours several native isolates had leached between 20 - 30 per cent more copper than laboratory reference strains during experiments conducted at 45¦C. This research has established a unique culture collection of mining microbes that readily adapt to Australian conditions. Exploitation of these microbes may result in improved leaching kinetics and copper recovery from Australian chalcopyrite ores as demonstrated from shake flask leaching tests. Whilst this research provides a capability for Australian mineral sulfide ores, this technology can be easily adapted to suit ores of any origin resulting in more effective and efficient microbial leaching.

Jan 1, 2004

The patented "Epytensic" pump of Minnovation Ltd, a multiple piston pump, is used widely on shearer loaders and by partial high pressure watcr jet cutting strategically in relation to cutter picks not only improves cutting rates, but saves power and increases the life of gearboxes and picks, as well as improving dust suppression. The "Face Side Pump", also a piston pump, located on the ranging arm gearhead has advantages over gateroad pumps and shearer body pumps. The "Extraction Drum", hydraulic air mover system, linked with the above innovations and high pressure water, have further advantages in methane and dust removal. Some modifications providing these systems need workshop applications but most are possible underground with minimal changes to shearer profiles and advantages of minimising hosing, along with the other advantages stated.

Jan 1, 1991

When Australian voters elected a Labor Government in March 1983 the value of the Jabiluka uranium deposit as an asset of Pancontinental Mining Limited effectively evaporated overnight. The day before the election, Jabiluka was Pancon's principal asset, with the Company's 65% stake in the deposit having a market value of the order of $US1 billion. This value had been set by an agreement reached with a potential customer, who was prepared to pay $US150 million for 10% of Jabiluka. The months before the election had been the culmination of ten years of unremitting effort to bring what was then the world's largest reserve of high'grade uranium ore into production. These efforts had included two and a half years of negotiations with the local aborigines, as well as exhaustive environmental studies and conceptual mine planning. All domestic approvals required to develop the Jabiluka deposit had been given to Pancontinental and marketing efforts had successfully placed about 50% of the expected uranium production with overseas utilities. It appeared that Jabiluka was about to emerge as one of the world's great mining enterprises. The election of a government with an anti-uranium policy stopped Jabiluka dead in its tracks. Pancontinental's largest asset had effectively become worthless and the Company appeared to be facing a bleak future.

Jan 1, 1987

By Ritchie I

Copper minerals are often associated with gold ores. These create processing problems since cyanide solutions are not selective for gold alone. Copper minerals are also leached by cyanide, and typically each one per cent of `reactive' copper in the ore consumes about 30 kg t 1 cyanide. Once in solution, copper cyanide species create further processing problems as they adsorb onto carbon along with the dicyanoaurate ion. These problems make conventional cyanidation of gold ore uneconomic if the ore contains too much copper. As a result, methods of economically processing gold-copper ores are becoming of increasing importance.One of the more promising methods of treating these ores is by selective leaching of the gold by an ammoniacal cyanide solution, a method first described by Hunt in 1901. This method is already in commercial use in Mauritania, treating copper/gold tailings. In general terms, the addition of I - 2 g U1 ammonia to a standard cyanide leach solution causes a significant increase in gold extraction and decrease in copper extraction. However, early testwork on this system has concluded that the optimal leach conditions are critically dependent on ore composition, and the mechanism is not well understood, making predictions of best conditions impossible.

Jan 1, 1997

Water is a key resource input to copper heap leach operations in both quality and quantity. A number of recent developments in analysis of the technology have shown that water consumption can be optimised. The leach consumption has been generally considered in terms of minimisation of the evaporative loss by changing the application method (drippers or wobblers). Modelling of the irrigation effects on leach rate has shown that the poorer surface coverage from drippers has an adverse effect on the leach extraction rate. This is particularly evident in the early part of the leach. The use of different irrigation systems during alternate parts of the leach cycle can have benefits in minimising the water consumption without an unacceptable outcome from extended extraction times. By combining the leach rate effect with the evaporative loss estimates, an economic decision matrix can be generated to allow the operator to select an appropriate leach irrigation strategy, combining both irrigation delivery and irrigation rate. In the SX-EW plant, the total quantity of EW bleed and SX scrub stage bleed (both for iron control) can be reduced to an absolute minimum. The economic minimum may be different depending on the cost of producing the high-quality water used to replace the bleed streams. Adjustment of the SX process, in particular use of multiple entrainment control steps, can provide significant reductions in the total bleed and make up requirements.

Jan 1, 2003

By H R. Watling, W van Bronswijk

Of the various copper sulfides in the EarthÆs crust, chalcopyrite is by far the most common. This mineral is also the most difficult to leach, with hydrometallurgical extraction processes characterised by prohibitively slow kinetics. While a number of processes, including leaching at atmospheric pressure and temperature, pressure leaching at higher temperature, and bioleaching of concentrates in stirred tanks and whole ores in heaps have been demonstrated to some extent, there is currently no full-scale unit process for the hydrometallurgical extraction of copper from chalcopyrite ores. Titan Resources NL operated a test bacterial heap leach at Radio Hill, Western Australia in 2001, to extract nickel and copper from a mixed sulfide ore that contained significant amounts of chalcopyrite, pentlandite and pyrrhotite. A proprietary mixed bacterial culture was used to inoculate the heap, and the nickel and copper were precipitated from the resultant solution as mixed hydroxides. Although 65 per cent of the copper from the Radio Hill heap was eventually recovered, the rate of extraction followed an unexpected trend, as the initial rates of copper recovery were much slower than column tests had suggested. It was postulated that this was due to dissolved copper precipitating as covellite or chalcocite in the most poorly aerated zones within the heap, ie furthest from the aeration pipes at the base. It was further hypothesised that the lack of oxidants (oxygen, ferric iron) and the likely inactivity of bacteria in these areas limited the re-dissolution of such secondary copper precipitates. In this study the above hypothesis was tested in column experiments using the same mixed sulfide ore and a synthetic leach solution. One set of columns was aerated and another set was operated without aeration. Results showed that precipitation of copper occurred regardless of whether the column was aerated or not. The results suggested that pH of the leach solution played a significant part in the precipitation of the copper. Further column tests revealed this to be the case. These results are described here in detail.

Jan 1, 2004

Basicity(aO2−) has been known to affect the physicochemical properties of molten slags in the metallurgical processes. However, because of the impossibility of direct measurement of single-ion activity, various indirect measures such as capacity, redox equilibrium of transition metal ions, activity of basic oxides, and (theoretical) optical basicity have been proposed; but these basicity measures have been restricted within slag systems and the interaction between measuring elements and slag components has affected the quantitative estimation of slag basicity. Recently, since it was reported that solubility of noble metals in molten slags could be an indirect measure of basicity, the influence of slag basicity on the solubility of platinum and silver has been reported. The reaction mechanism of platinum dissolution into basic slags has been reported, whilst that in acidic slags has not (Nakamura and Sano, 1997; Sano and Nakamura, 1997; Nakamura et al, 1998). Richardson reported that the solubility of metals such as cupper, gold, silver, and lead in the CaO-SiO2-Al2O3 slag was presumably dependent on the atomic radius and the accommodation ability of the silicate network (Richardson, 1974). Swinbourne and You measured silver solubility in the Na2O-SiO2 slag over a wide range of oxygen partial pressure and suggested that silver would be present as both Ago and Ag0.5 in the slags (Swinbourne and You, 1999). For brevity, these previous works discussed the dissolution mechanism of silver into the slags based on the existence of silver as a neutral or molecular species. However, because the almost chemical reactions occurring in the slag are affected by the basicity, the reaction formula with O2- ion is required based on the ionic characteristics of the slag such as desulphurisation and dephosphorisation reactions as given in Equations 1 and 2, respectively.

Jan 1, 2000

Before attempting to outline the Australian Stock Exchange's perspective on expert reports, I think it would be appropriate to explain to those of you -who are not familiar with the Stock Exchange listing rules on just when ASX currently requires companies to obtain an expert report and equally important to note, what the regulators have to say.

Jan 1, 1989

The different stages of the metallurgical evaluation of an ore resource and their importance to overall project evaluation are described. Particular emphasis is placed on the liaison that is necessary between the different members of the project team from the preliminary exploration phase through to the completion of the final feasibility study. Metallurgical input at the earliest stage is recommended. The incorporation of metallurgical and marketing data into ore reserve statements and the effect of the metallurgical evaluation on ore reserve classifications are discussed.

Jan 1, 1987

Commercial pelletizing commenced in 1955 to agglomerate very fine concen- trates which could not be fed directly to the blast furnace. Extensive develop- ment has taken place and is continuing. There are now three main heat hardening processes in use. Plants are operating, or under construction, throughout the world capable of producing in excess of 125 million tons per year of pellets from concentrates or direct mined orefines. The Whyalla Pellet Plant, which commenced production in May 1968, is examined in detail to illustrate the general principles of pelletizing. This plant converts high grade iron ore fines into high quality pellets at a rate in excess of 2 million tons per year.

Jan 1, 1971

By Roberts I. R

The movement of materials is normally associated with a number of problems, some more easily overcome than others. Orebodies are frequently located in remote areas to which transport lines have to be opened. In the case of Mount Isa Mines Limited, the geographical isolation from the major consumer areas necess- itates long lines of transport and communica- tion. The problems associated with transport of metals and minerals vary from time to time because of the changing industrial environment. The increased size of vessels, changes in handling methods, and the economic pressures brought on by increased costs of transport without any guarantee of aligned increase in metal prices all contribute to difficulties which have to be faced by the mining companies in their effort to reach the markets with their products.

Jan 1, 1974

By Lai KF

The Hellyer orebody is a fine grained, massive sulphide Pb-Zn-Ag- Cu-Au deposit located in western Tasmania. Initial testwork showed that the orebody would be difficult but not impossible to treat by conven- tional flotation. A staged programme-of work was commenced to demon- strate that marketable concentrates could be produced with satisfactory recoveries. Following laboratory testing of drill core to define two flowsheets, bulk samples of Hellyer totalling 20,000 tonnes were trialled at 6 tph in the Cleveland concentrator over six months. The high through- put and extended duration of the trials ensured maximum confidence in the results and that scale-up to subsequent plants would be with a mini- mum of risk. The milling trials were successful and the Cleveland concentrator was expanded in early 1987 to treat 250,000 tpa of Hellyer ore to produce 85,000 tpa of bulk concentrates. Late in 1987 construction commenced on a 1 mtpa concentrator at Hellyer to produce separate copper/silver, lead, zinc and bulk concentrates.

Jan 1, 1988

In the Ora Banda area of the Eastern Gold- fields, the ultramafic rocks tend to be more deeply lateritized than most of the surrounding rock types, and lateritic nickel concentrations have been formed. Extensive drilling_has shown that, of the two intermixed suites be- neath the laterite - an extrusive peridotite- pyroxenite suite and an intrusive, highly magnetic dunite - the latter weathers to a more nickel enriched laterite. The top horizon I of the laterite consists of ferricrete. Horizon II consists mainly of bands of secondary silica in a clay matrix, formed in the reworking zone around the water table and stranded as the weathering profile migrated downwards. Horizon III ('ºaprolite") is composed of serpentinite, magnesite, iron oxides and silica, and grades dowil to the fresh bock composed variously of olivine, ser- pentine, talc, amphibole-chlorite and iron oxides. The main locus of nickel deposition is the zone containing the bottom of horizon II and the top of horizon III. The water table is also at this general level. .

Jan 1, 1973

Current NSW Government policy requires searching for more than just minerals during an exploration program - add endangered fauna and archaeological relics for a start.

Jan 1, 1995

By Rosentreter N

Difficulties with froth flotation recovery and vacuum de- watering equipment for the treatment of fine coal have been investigated. Mechanical alterations to cyclone desliming banks, and flotation cells are described. A large disc filter has been replaced by two drum filters for dewatering, and the improvement in plant. operation is discussed:

Jan 1, 1978