Search Documents

By Woodcock J. T, Rummel P. H, Sparrow G. J, MacRae C. M

An automated method, which is believed to be the fastest in the world and which can be used by mineralogically-untrained technical assistants, has been developed for the rapid location of native gold particles and other gold minerals down to 1 pm in size in ores, concentrates, and tailings using a scanning electron microscope. Searching of a 25 mm diameter polished block in 1 pm steps usually requires 3-4 h. Examples of the location of native gold and gold tellurides in drill core sections, in crushed ore samples and gravity and flotation concentrates, and in various metallurgical test products are given. The results have application in ore exploration, in guiding metallurgical test programmes, and in assessing metallurgical per- formance in testwork and in operating plants.

Jan 1, 1991

In south-eastern King Island, sediments and lavas of possible Upper Proterozoic to Lower Cambrian age have been intruded by Lower Carboniferous granitic rocks.Within the contact aureole of the Bold Head adamellite north of Grassy the sediments and lavas have been metamorphosed to hornblende hornfels facies grade. The thermal gradient within the contact aureole was small, as the hornfelses exhibit no mineral zoning over a distance of 700 ft from the adamellite.Skarns occur both within the adamellite near its contact with the country rocks, and within the country rocks as partial replacements of three dolomitic limestone horizons. The latter type, the exoskarns, commonly have an andradite-salite mineralogy and carry economic concentrations of scheelite. These resulted from the replacement of carbonate beds due to both diffusion and infiltration metasomatism. Silica, tungsten, minor sulphides, and water were introduced from the adamellite, while aluminium and iron diffused from the enclosing pelitic sediments. Calcium released during marble replacement countered the loss of iron and aluminium in the pelitic hornfelses transforming them to diopside-rich rocks.Endoskarns within the adamellite are the result of two way diffusion across the contact; calcium, aluminium, and iron diffused from sediment to adamellite as silica, potassium, sodium, and water diffused from adamellite to the sediments. From estimates of the lithostatic pressure and mole fraction of CO2, the mineral assemblages of the hornfelses imply that the temperature of metamorphism lay between 530° and 710°C. This temperature range is in good agreement with minimum temperatures, between 610° and 710°C, for the recrystallization of the marbles of the contact aureole, calculated from the determinations of the solid solution of the magnesite molecule in calcite.

Jan 1, 1971

By T G. Vizcarra, T J. Napier-Munn, A T. Karbowiak, M G. Hart

Squeezing extra performance from existing equipment (‘sweating the assets’) is key to continuous improvement initiatives, particularly during times of cost cutting where the option of spending additional capital to facilitate circuit upgrades can be severely constrained. A common challenge, however, is identifying the best combination of settings for different process variables, as their effects can be camouflaged by interactions with other process variables and, of course, noise in historical data.This paper describes a recent investigation at Boyne Smelters Limited to identify strategies to coarsen the product of its dry, fixed-speed, open-circuit AG mill, without the need for installing pre-screens prior to the mill. The product is used as insulation material for the reduction of alumina to aluminium, and an excessively fine product was inhibiting the ability of the cover material to dissipate heat from the underlying anodes. The approach was to undertake a series of experiments, designed according to statistical criteria, to elucidate the effect of key process variables (feed blend and power draw) upon the product sizing. The results provided clarity about what strategies would encourage the production of a more desirable mill product (with some surprises). The study is a good example of how properly designed experiments can identify hidden potential in processing circuits, thereby mitigating the need for capital-intensive upgrades.CITATION:Vizcarra, T G, Hart, M G, Karbowiak, A T and Napier-Munn, T J, 2018. Getting the most from existing processes: using cleverly designed experiments to optimise the line 3 AG mill at Boyne Smelters Limited, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 207–216 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By P N. Duan, Z G. Liu, M S. Chu, X X. Xue, B Liu, G J. Cheng, T Jiang, J X. Liu

High-chromium vanadium-titanium magnetite has not been exploited and made full use of on a large scale so far due to the immature utilisation technology and the reality that the utilisation efficiency of valuable metals still urgently needs to be improved. In the present paper, the isothermal reduction kinetics and mechanism of high-chromium vanadium-titanium pellets were studied at 800–1100°C. The mineral composition transformation of pellets before and after reduction was analysed by means of X-ray diffraction (XRD), and the microstructures were examined by scanning electron microscope (SEM) equipped with energy dispersive X-ray (EDX) to reveal the elemental distributions. The effect of reduction temperature on the volumetric swelling degree and cold crushing strength was also studied. It was found that reduction temperature has a large effect on the reduction rate of pellets, and the increase in reduction rate is more obvious in the range 1000–1100°C than 800–1000°C. The volumetric swelling degree of pellets increased with increasing reduction temperature, while the cold crushing strength decreased. The transformation of mineral species can be expressed as Fe2O3 ? Fe3O4 ? FeO ? Fe, Fe2O3·3TiO2 ? Fe3O4· (2FeO·TiO2 ) ? 2FeO· TiO2 ? FeO·TiO2, (Fe0.6Cr0.4)2O3 ? FeO· Cr2O3 ? Cr2O3 , and Fe2O3· VO/V2O3 ? VO. The apparent activation energy of the reduction reaction was calculated to be 44.3 kJ/mol, and the reduction rate is controlled by the combined effect of interfacial chemical reaction and gas diffusion through the porous product layer. The rate controlling steps were further studied by calculating the resistance percentages. The interfacial chemical reaction was found to be predominant in the initial reduction stage, with the percentage effect of gas diffusion through the porous product layer gradually increasing during reduction.CITATION:Cheng, G J, Xue, X X, Liu, J X, Liu, Z G, Chu, M S, Jiang, T, Liu, B and Duan, P N, 2015. Reduction kinetics and mechanism of pellets prepared from high-chromium vanadium-titanium magnetite concentrate, in Proceedings Iron Ore 2015, pp 349–358 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Jul 13, 2015

By J Borthwick, M Yusi, M Douge

Feasibility studies form a vital and significant component of the project delivery cycle. They are at the heart of the valuation process. This paper focuses on variables which can affect a project and how these are assessed as part of the decision-making process through feasibility studies. Test work and site selection needs; the degree of engineering required to meet the study requirements and the quality of owner project information are discussed. Also, local factors including permitting needs, social, environmental and government relations are considered. Engineering and site factors are crucial in the estimating process. The interaction of detailed engineering, engineering assumptions and estimating methodologies are therefore examined. The ownerÆs perspective is considered along with risk analysis, which is fundamental in project feasibility study activities. The impact of this is also discussed.

Jan 1, 2009

Modern mining and coal cleaning techniques lead to the generation of large quantities of fines which give rise to problems in their storage, handling, transportation and further processing. Pelletisation, a method of particle agglomeration, can alleviate such problems. This paper provides a brief overview of the principles of pelletisation and a survey of the coal pelletisation literature. Then it reports results from an experimental investigation of the effect of surface active reagents on coal pelletisation. Finally the paper is concluded with a few remarks on applying the results from the experimental study to practical coal agglomeration.

Jan 1, 2000

By Kallioinen J

This paper discusses different possibilities to enhance coarse particle flotation using forth manipulation and improved flotation cell design. Experiments were carried out in laboratory, pilot and industrial scale ranging from 0.0015 to 100 m3/axle. During the work it could be shown that the conventional idea of one single flotation cell type for both fine, immediate and coarse flotation of coarse and fine particles need different impeller tip speeds and a different froth control objective for effective operation. For optimal operation for coarse feeds the tip speed must be reduced and the froth vertical velocity must be increased to compensate the respective drainage velocity and also the water film thickness must be taken care of. Turbulent eddies below the froth interface should be suppressed. The paper discusses the effects of different froth manipulation variables like froth vertical velocity and froth residence time to the recovery and selectivity. A function has been developed, between the residence time of the froth and the flotation cell's ability to produce an improved concentrate grade as a function of different operating and froth manipulation variables.

Jan 1, 1993

By X Li, M-F Zhou

"An EXTENDED ABSTRACT is available for download. A full-length paper was not prepared for this presentation. The Yinachang deposit in south-west China contains large amounts of Fe, Cu and rare earth elements (REEs). Apatite in this deposit records complex REE mineralisation and remobilisation processes.Fe-Cu-(REE) mineralisation at Yinachang occurred at ~1700 Ma, and three stages of alteration and mineralisation are identified: Na-(Fe) alteration, Fe-(REE) mineralisation and Cu-(REE) mineralisation. In the Fe-(REE) mineralisation stage, REE-rich apatite formed together with magnetite. In the Cu-(REE) mineralisation stage, fluids undersaturated with REEs interacted with early-formed REE-rich apatite, during which large proportions of REEs, especially light REEs (LREEs), were leached from apatite.At ~840 Ma, apatite experienced a second interaction with fluid. In that process, REEs were removed from the apatite structure but immediately reprecipitated into new phases within the apatite. Thus, numerous REE mineral inclusions including bastnaesite, monazite and minor Y-phosphate occur in the apatite. There are also a very small portion of LREEs that were transported out of the apatite, resulting in the growth of bastnaesite and monazite grains outside the apatite.This study demonstrates that REEs can be mobilised in multistage hydrothermal activities and highlights the significance of fluid compositions for REE transportation and deposition behaviours in hydrothermal systems.CITATION:Li, X and Zhou, M-F, 2015. Hydrothermal rare earth element mobilisation processes in the Yinachang Fe-Cu-(REE) deposit, south-west China, in Proceedings PACRIM 2015 Congress, pp 265–270 (The Australasian Institute of Mining and Metallurgy: Melbourne)."

Mar 18, 2015

The main factors controlling the electro- winning of zinc from impure aqueous sulphate electrolytes are reviewed. Zinc, hydrogen and impurities are deposited at the cathode. The current effic- iency for zinc is increased by increasing zinc/ acid ratio and current density and by decreas- ing temperature; and may be unchanged, increased or decreased by the presence of impurity ions. A qualitative comparison of observed and predicted impurity effects is in reasonable agreement. Quantitative treatment of the effects of impurities and cell additives is not available. A tentative explanation of the time dependence of current efficiency in the presence of some impurities is provided. The forms in which impurities are deposited is substantially unknown. Impurities may be classified according to the extent of cathodic deposition. Procedures for control of cathodic deposition of impurities are outlined. The main anodic reactions are the forma- tion of oxygen, manganese dioxide and sulphuric acid. Minor reactions include the oxidation of lead, silver, cobalt and chloride. The site of the anodic reactions and the reactions generat- ing manganese dioxide are uncertain and may change with time of operation. The anode behaves crudely as an oxygen electrode with

Jan 1, 1977

Petroleum exploration in the Australian arid zone has been proceeding at an ever-increasing pace, subject to financial fluctuations, since the 1960's. The impacts of petroleum exploration in the arid zone are less than they would be for corresponding operations in. e.g. a forest area: in this context, Australia is fortunate in that its major petroleum producing (and prospective) , basins are offshore or in the arid zone. In addition. the other major sources of impact in the Austrlian arid zone, namely pastoralism, tourism, and rabbits, tend to be concentrated around areas of particular conservation significance, whereas petroleum exploration is not. Despite this, the cumulative impacts of exploration are sufficient to have caused concern to government regulatory authorities and some sectors of the general public. Exploration is now subject to a range of environmental constraints with various degrees of legal enforceability. To enable exploration to continue without public opposition, the industry, and government agencies charged with regulating or supervising it, must demonstrate that the net benefits of exploration exceed net costs, including environmental costs. One particularly simple and cost-effective technique for increasing the net benefit/cost ratio of exploration is to reduce the net environmental costs by minimising and mitigating the impacts, both primary and secondary, of seismic acqisition. This is best achieved by a combination of preventive and restorative techniques: careful line positioning and low-impact (or zero) line clearance, coupled with simple rehabilitation of bladed lines. Line clearance without bulldozer blading - e.g. by rolling or simply pegging and trafficking, perhaps with tracked rather than rubber-tyred vibroseis - is one promising approach currently coming into use. Rehabilitation by grading soil banks ("windrows") back on to bladed tracks, though not yet in widespread use, has proved very successful in the limited areas where it has been applied to date.

Jan 1, 1987

By K Vallo, T Haimi, J Pihlasalo, J Hamuyuni, M Lindgren, F Tesfaye

Decarbonisation of the steel industry has recently attracted a lot of research and technological development. Most of the technological developments are centred around the replacement of blast furnace (BF), which has been the main primary smelting furnace in the ironmaking step of steel production. Replacement of the BF is not an easy task because of BF’s many established capabilities over the years, especially its ability to use low-grade iron feed. In this regard, Metso has developed its own technology, Metso’s Outotec direct reduced iron (DRI) smelting furnace, to tackle this problem. The recently developed six-in line electric furnace for DRI smelting can be used for primary smelting of DRI from blast furnace grade iron ore. Unlike the electric arc furnace (EAF), the DRI smelting furnace can handle larger slag volumes that emanate from the high gangue in BF grade DRI. Therefore, fluxing plays an important role in operating the DRI smelting furnace. This paper presents fluxing options and proposes slag quality and operating windows for the DRI smelting furnace. Also, the effect of slag on refractory durability will be discussed.

Jun 19, 2024

By W B. Edgar, S C. Dominy

High-nugget effect vein-gold systems are generally considered to be one of the most challenging of deposit types to evaluate and exploit. To potential investors and mining companies, they are viewed as high risk because of the associated uncertainties in the grade estimate and general paucity of Ore Reserves at production start-up. However, despite the well-known risks, these deposits often have a grade upside that makes them potentially attractive. The reporting of resource grade is of importance and perhaps even more so is the reporting of the associated uncertainty attached to the grade estimate. The use of the grade estimate supported by a grade range is recommended to achieve more complete and useful disclosure. The definition of the grade range can be somewhat subjective, ranging from opinion based estimates through to data-based estimates and geostatistical conditional simulation. Whichever method used, the over-riding issue must be the provision of enough data of appropriate quality and full disclosure to the public of relevant uncertainties.CITATION:Dominy, S C and Edgar, W B, 2012. Approaches to reporting grade uncertainty in high-nugget gold vein projects, in Proceedings Project Evaluation 2012 , pp 95-108 (The Australasian Institute of Mining and Metallurgy: Melbourne).

May 24, 2012

By R Urie

Dilution and loss of ore during the mining process invariably occur in all underground mining operations. This dilution and ore loss can have a significant effect on the performance and value generated from a mining operation. Further, excessive dilution or greater than anticipated ore loss during mining is often one of the key reasons for the underperformance of a mining project when compared to a feasibility study or annual budget. Mining professionals often go to great lengths preparing detailed mine plans, schedules and economic models only to then apply high-level estimates or rule of thumb values for dilution and mining recovery that can ultimately lead to inaccurate forecasts for the performance of a mine with the resultant loss of value due to the mining of uneconomic material or the loss of potentially valuable ore. This paper discusses processes and practices that can be practically used to manage dilution and mining recovery in an underground mining operation with a focus on understanding and then maximising value. The processes cover items such as the definition and measurement of dilution and mining recovery, techniques for the estimation of dilution and mining recovery, consideration of the economic implications, management of dilution and mining recovery through the stages of the planning cycle, and practices to reduce dilution and improve mining recovery. Common misconceptions and omissions are also discussed.

Mar 29, 2023

By D Cumming-Potvin

Incidents that trap miners in underground mines have serious consequences for the miners and the mine operators involved. It is of utmost importance that mine operators utilise all available tools when trying to locate and rescue trapped miners. From testing conducted at underground hard rock mines, Cumming-Potvin et al (2013) found that pre-existing microseismic monitoring systems, which are routinely used for seismic risk management, have the potential to be used for detecting and locating trapped miners.This paper reflects on the Anzac Day seismic event that trapped two miners at Tasmania Mine, Beaconsfield, on 25 April 2006. The Anzac Day event occurred at 2123 on a Tuesday evening. Rescuers were unable to confirm that the trapped miners had survived until 1930 on Sunday evening. It is not possible to speculate on how the rescue operation may have been different had the technology to use the microseismic monitoring system for the purpose of detecting the trapped miners been available. However, it almost certainly would have been different. The recent research project has demonstrated that knowing the fate of the Beaconsfield miners might have been achievable up to 100 hours earlier than was the case in 2006. That knowledge would have been invaluable to the rescue effort.By examining the seismic array at the Tasmania Mine, the reliability of detection over the working levels of the mine could be quantified. Had the methodology been available, adding six additional sensors (at a cost of $40 000), would have been sufficient to increase the likelihood of detection to greater than 90 per cent in the working levels of the mine. This was true both at the time of closure of the mine in 2012, and just prior to the Anzac day event.CITATION:Cumming-Potvin, D and Hills, P B, 2014. Use of a pre-existing microseismic monitoring system to detect trapped miners (with reflections on Beaconsfield 2006), in Proceedings 12th AusIMM Underground Operators’ Conference 2014 , pp 143–150 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Mar 24, 2014

The Argyle Diamond Mine came on stream late in 1985 as the world's largest diamond producer in terms of carat output. The design of the process plant, including the heavy medium separation (HMS) facility which provides the initial stages for separation of diamonds from gangue, evolved over a lengthy period of feasibility study and site investigation into the final form described in this paper. The commissioning was carefully planned and co-ordinated, and culminated successfully with handover of the plant on schedule and within budget. Problems encountered during .within were minimal and since then the plant has achieved greater than design throughput during its first year of operation. Darvr_ontmn

Jan 1, 1987

By B Dold

Western Europe is a dynamic region, with an emerging co-operation between the individual nations both politically, economically, technically and scientifically. The European Union, today with 15 member States and with a range of central European States applying for membership, is a catalyst for this Cupertino, using a combination of EU funds, for financing research initiatives, and legislation to enhance development of technology and environmental performance. Europe is a major net importer of metals but with a large potential for own production, in particular in the accession countries. The metals and mining sector is furthermore identified as having a large potential to generate wealth both in todayÆs EU and in the future, widened Union. This paper provides a chart of examples on the many research initiatives presently underway in Europe, addressing environmental issues related to mining. The list of programmes and projects does not claim to be complete; it is rather an illustration on the wideness of the approach, describing various ways for transboundary Cupertino. The approach taken by many of the programmes goes beyond the strict ARD scientific area and therefore only a limited number of the many programmes can be identified as ARD research programmes. Also national programmes, without EU funding, are operating, eg in Sweden, Germany, and UK. The picture is continuously changing with new programmes being commissioned and old ones being completed.

Jan 1, 2003

By Henderson J

Iron ore samples selected from the Deepdale, Iron Prince and Mt. Newman ore bodies have been pelletised on a pilot scale plant and subsequently reduced under laboratory conditions by hydrogen or carbon monoxide. Pellets approximately 1 cm in diameter have been reduced by hydrogen over the temperature range 5000- 900¦C and the results examined by thermogravimetric, microscopic, electron probe and x-ray techniques. After an initial time delay it was found that up to 95% reduction the rate of reduction could be described by a transport con- trolled porous model, in which the effective diffusivities of hydrogen in theòpr¦duct layer and the reaction zone are filar. Independent measurements of effective diffusivity supported the values obtained from the reduction data. ve 95% reduction the rate decreased markedly due to the formation_of retained wustite or fayalite. Comparison with reduction by carbon monoxide over the temperature range 7500 - 900¦C showed that the rate eduction by carbon monoxide was approximately five times slower than the rate by hydrogen. The rate of reduction was found to be a function of the properties of the pellets, which may account for the ely conflicting results that have been obtained in previous investigation on porous pellets.

Jan 1, 1970

By A K. Bhatnagar, S Saha, P Dixit, A K. Mukherjee, P Patra

TATA Steel’s R&D Division at Jamshedpur has developed a slime beneficiation process to recover iron values from iron ore slime. This process recovers iron ore concentrate containing 2.2 per cent alumina from a feed containing 7–10 per cent alumina. The reject generated from beneficiation of iron ore slime is treated as waste as the iron content in the reject is below 45 per cent. Effective utilisation of this waste is required for making the iron ore slime beneficiation process a zero-waste technology. In this connection several studies were made towards utilisation of slime waste. One of these studies revealed that slime waste can be used as a soil conditioner. Slime waste contains particles of size less than 10 micron and when these particles are mixed with soil in definite proportions, the porosity and the permeability of the mixture goes down. As a result, the water holding capacity (WHC) improves. This concept was evaluated through a series of tests at greenhouse level to optimise the soil to slime ratio. Finally, a pilot scale field trial was carried out over a period of three months using paddy rice as the crop. Three separate plots with compositions of: soil + organic matter comprising Farmyard Manure (FYM), (ii) soil and slime waste (2:1) + organic matter (FYM), and (iii) soil and slime waste (2:1) + organic matter (FYM) + Nitrogen, Phosphorus and Potassium (NPK) fertiliser were used for the pilot trial. The results showed a 20 per cent increase in the productivity of paddy rice for plot (ii) as compared to plot (i). This was due to the beneficial effect of slime waste in the soil. The addition of inorganic fertiliser such as NPK in the ratio of (4:2:1) further enhanced the productivity of paddy rice.

Sep 18, 2023

By M Miller

Operators of nickel laterite pressure acid leach and gold pressure oxidation technology frequently employ a series of steam condensing heaters to preheat the leach feed slurry. The heaters are an economic pinch point û although the thermal performance of the heaters is critical to overall process viability and operating cost minimisation, they are also a significant capital item and must be sized accordingly. Despite this, discussions of the factors underlying heater design are conspicuously absent from technical literature, and existing operations feature a conflicting range of heater sizes and configurations. This variety would suggest that at least some of the chosen heater designs are oversized. As part of its detailed design stage, the Ravensthorpe Nickel Project (RNP) constructed and tested a pilot plant heater to develop an understanding of the heating process and to ensure that the RNP heaters were appropriately sized. This testwork used RNP slurry at design density and viscosity on a 450 mm diameter, 6500 mm high column. The pilot plant testwork demonstrated the intrinsic efficiency of the direct steam condensation heating process, which was essentially independent of slurry density and viscosity. Presence of non-condensable gases in the steam phase decreased the heat transferred in certain circumstances, but heater performance remained consistent with thermodynamic limitations. Stagewise heat transfer within the column was rapid, and suggested either a very high slurry surface area or excellent heat transfer within the slurry phase. While the testwork did not set out to distinguish between these effects, physical evidence pointed to droplet formation in the inter-tray shower zone, giving a high heat transfer area. For scale-up purposes, the key facts were that the heat transfer rate was not limited by using high viscosity slurries and heaters could be designed using the principles applied to the smaller of those in existing operations. This paper discusses existing slurry heater designs, the current understanding from open literature, the pilot plant testwork, results and analysis, and scale-up to commercial sized equipment.

Jan 1, 2005

The original and most basic relationship between mining company and explosive supplier was a simple one of consumer and product supplier. The divide between the two was quite clear-cut with neither taking much interest in the activities of the other. The explosive supplier had little understanding or share in the outcome, efficient rock breakage and therefore impact on mining and milling. Likewise, the mining company did not encourage the improvement or development of products. The transactions were limited to product and funds. This environment does not encourage any form of knowledge sharing, trust or optimisation of the mining process.Conversely, there are now a variety of relationships to the point that the mining company may simply be an asset manager whereby all æoperationalÆ aspects are contracted out. For the drill and blast aspect this takes the form of a æRock-On-GroundÆ contract whereby the explosives company takes on design, drill, load and fire responsibilities and is paid a rate per volume of broken rock. This removes the majority of risk to the mining company derived from having to produce broken rock and guarantees the cost of a portion of the overall unit cost of mining. The onus is now on the explosives supplier to break rock to a specification as efficiently as possible.There exist a number of variations between the æbasic supplyÆ and æRock-On-GroundÆ. These contracts may also include value sharing to encourage the explosive supplier to optimise the mining operation to maximise profit.This paper looks at some of the drivers for the change in explosive supplierûconsumer relationships and examines the æprosÆ and æconsÆ of a few of the options.

Jan 1, 2004