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By Hutchings SG, Skimmings T

This paper describes the results of the field application tests at Miike Colliery on the integrated automatization of the longwall mining system for medium thick coal seam. The purpose of the research is to develop an automatic longwall mining system which can be controlled accurately from outside of the face, and the ultimate goal is an eliminate of men from the face. Presently, the field test is being conducted in Yotsuyama mine following to a success in the performance test on surface. Remote Batch Control System for shield supports has been adapted to operate all supports from the control panel located at the entrance of the face. Remote monitoring and control system of the drum shearer has also been tested. The system makes it possible to operate the shearer either at the main gate or full automatic. Productivity and safety will be substantially improved as those systems enable to eliminate all workers from the face under the severe working conditions with high ground pressure and hot and humid atmosphere due to increasing mining depth. So far, we have been satisfied with the results of the field test and those system will be an effective countermeasure to operate the face with a high risk of rock-burst.

Jan 1, 1987

By J Rayo

Andean countries (Chile, Peru, Bolivia and Argentina) have 42 semi-autogenous mills (SAG) in operation and there are more than 30 projects in the pipeline that consider SAG mills. At the end of the next decade, the total amount of SAG mills in this area will likely be close to 100.There is a lot of reliable operational information collected by JRI Ingenieria Sociedad Anonima, the author’s engineering company, for more than 20 years and processed by statistical software, to be used as a reference for design basis of future projects or to improve operations by comparison. JRI Ingenieria Sociedad Anonima has reliable information related to the performance of more than 50 per cent of the Andean SAG plants.The paper presented considers a set of graphs that summarise the collected and verified SAG plants technical data. The figures will show key parameters as circuits and equipment data, energy consumption, technical availability, utilisation rates, throughput variability, pebble productions, steel consumption and others.The data is compared with typical design basis of several engineering companies and the main differences are analysed and/or commented on.CITATION:Rayo, J, 2014. Comparison of semi-autogenous mills operations in Andean countries, in Proceedings 12th AusIMM Mill Operators’ Conference 2014 , pp 283–296 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Sep 1, 2014

By D La Rosa, A Jankovi, A Dance, W Valery

This paper presents the methodology for optimising blasting and comminution processes in terms of fragmentation developed by Metso Minerals Process Technology Asia-Pacific and South America (MMPT). The methodology is called process integration and optimisation (PIO) and involves a number of steps: benchmarking, rock characterisation, measurements, modelling/simulation of blasting and comminution processes and where required, material tracking. The measurements collected while at site are combined with rock characterisation and definition of ore domains to model the complete process chain. These data are used to develop site-specific models of blast fragmentation, crushing, grinding and flotation. This allows customised blast patterns to be developed that optimise both crushing and grinding performance. For each domain, blast designs are recommended to generate the optimal fragmentation size for downstream processes. The objective is to minimise the overall cost for the entire process and the changes often have a positive impact on the mining operation. Process constraints such as wall stability, ore dilution, muck pile characteristics, size of mining equipment, size and installed power of crushing and milling equipment and other process bottlenecks are considered in the blast designs. This methodology has allowed many operations around the world to significantly increase their production: generating typically five to 20 per cent higher concentrator throughput. A number of case studies will be discussed in this paper to describe the structured approach taken and demonstrate the benefits that are achievable. This paper will focus on the role of blasting in the optimisation of the entire mine to mill process chain and discuss elements of the PIO methodology: rock characterisation, fragmentation modelling and measurement, the relationship between fragmentation and mill throughput and material tracking.

Jan 1, 2007

By T Weldon

In the last 15 years, it has become increasingly popular to win gold and silver from carbon strip solutions with electrolytic æsludgeÆ cells. The precious metal sludges produced in the cells are washed to the cell bottom and pumped into filters. Most new operations are specifying sludging cells, and many older operations are being retrofitted with up-to-date electrolytic sludge cells and filters. The new sludging cells are generally more energy efficient than older cells, but more importantly, the cell operations to remove product are much less labour intensive, cleaner, and the operator need not have physical contact with the electrolytically produced metal. A case study of a major North American gold producer (50 000 kg/yr) that removed old style stainless steel wool cathode cells and installed new sludging cells and sludge filters is presented. The effect of various impurities is discussed.

Jan 1, 2005

By Dunn J, Nguyen G, Graham J

A pyritic gold concentrate from the Golden Mile, Kalgoorlie, was roasted over a range of temperatures in a pilot scale fluid bed reactor. The calcines were subsequently cyanide leached. Mineralogical studies of the con- centrate, calcines and leached residues were also undertaken. Calcines produced at 500'C gave the poorest gold extractions and high cyanide consumptions. Gold recoveries of approximately 90 per cent were obtained from calcines produced at 550-600'C but higher roasting tempera- tures resulted in an increase in the residual gold content of the leached calcine. There is some evidence of flash smelting of the pyrite at the higher roasting temperatures and encapsulation of gold particles. Mineralogical examination of the calcines shows that the mechanism of oxidation is temperature dependent. At 500'C pyrite is directly oxidized to hematite with a concentric layered texture which appears to inhibit lixiviant access to enclosed gold particles. At higher temperatures the conversion sequence pyrite-pyrrhotite-hematite produces a spongy calcine which al- lows easier penetration by the leaching medium.

Jan 1, 1991

By S Jeon, K Aikawa, M Ito, A Kusano, I Park, N Hiroyoshi

In mineral processing of complex sulfide ores containing copper (Cu), lead (Pb), and zinc (Zn), flotation has been commonly used. Typical Pb mineral in the ores is galena (PbS), while some types of the ores contain anglesite (PbSO4). This article reviews our recent studies on the effects of coexisting PbSO4 on the flotation of complex sulfide ores, and a method to suppress the floatability of sphalerite (ZnS) in the presence of PbSO4 was proposed. Comparison of flotation experiments for different types of model samples showed that PbSO4 makes the separation of Zn from Cu difficult; that is, for the model sample containing PbS without PbSO4, Zn could be separated from Cu, while when the model sample containing PbSO4, Zn was recovered together with Cu as froth. Solution analysis and thermodynamic calculation suggested that Pb2+ was released from PbSO4 and reacted with ZnS to form PbS, acting as an adsorption site for the flotation collector, xanthate. This would be the main reason for high floatability of ZnS in the presence of PbSO4. As a method to suppress ZnS floatability for the ores containing PbSO4, a pre-treatment of the ores to remove PbSO4 prior to flotation was proposed. The results of model experiments using mixture of ZnS and PbSO4 showed that ~97 per cent of PbSO4 was dissolved within 30 minutes of pretreatment using ethylenediaminetetraacetic acid (EDTA) as extractant, and thus ZnS floatability was markedly suppressed. Moreover, Pb2+ extracted from PbSO4 during the pre-treatment could be recovered as zero-valent Pb by the cementation using zero-valent Fe as a reductant. The details of ZnS flotation in the presence of PbSO4 and the effects of the pre-treatment are discussed based on the results of surface analysis like XPS.

Aug 24, 2022

By S Servant, T J. Bidwell

Paste backfill technology is gaining rapid acceptance in the Canadian mining industry. The authors were able to work on four different mining sites employing paste technology in their operation. In each site the paste backfill is prepared with very fine tailings containing significant amounts of sulphur minerals. The research program involved laboratory testing on samples prepared in the laboratory, on control samples obtained at the backfilll plant during pouring into the stopes and on core samples obtained from drilling in backfilled stopes. The laboratory testing provided detailed knowledge of the mechanical behavior of the paste backfill. The need for a means of measuring the in-situ mechanical properties of the backfill became clear. A review of various trials published in literature and an evaluation of available technology suggested the Cambridge Self-boring Pressuremeter. A first field campaign confirmed the efficiency and dependability of this instrument leading to the conclusion that it offers a very good method for the in situ measurement of paste backfill properties.

Jan 1, 1998

The Abra mineralized body is regarded as a significant new style of mineralization for its environment. It is a blind polymetallic deposit, located in the Bangemall Basin of Western Australia. It was discovered by Geopeko in 1981 by diamond drilling a coincident magnetic gravity target, which revealed a large low grade epithermal Fe-Ba-Pb-Ag-Cu-(AuW) deposit, hosted by chemogenic and clastic sedimentary rocks, overlain by 200-500 m of clastic sedimentary rocks, of Middle Proterozoic age. The mineralization occurs as an upper stratabound phase, and a lower vein "stringer" style phase within a pervasive chlorite alteration envelope.

Jan 1, 1987

By G Showers, R Triglavcanin

The complexity of understanding the whole thickening process to achieve real performance improvements cannot be underestimated. The last significant change in feedwell design was more than 15 years ago with the introduction of self-dilution systems û firstly with OutotecÆs Autodil, followed by FLSmidthÆs E-Duc. Now, following many years of extensive in-house research, including close collaboration with AMIRA and the CSIRO, Outotec has launched the next generation Vane Feedwell. The Vane Feedwell has been globally patented and installed at various sites. This paper briefly outlines the feedwellÆs development using CFD modelling and its subsequent performance in a æreal lifeÆ site installation. Plant results of the first commercial Vane Feedwell, in a mineral sands application, are discussed. The Vane Feedwell was retrofitted so comparative data of pre- and post-installation is shown.

Jan 1, 2009

A sample of fifty fractured low chromium-molybdenum alloy drill steel rods was investigated. Each rod was of the forged collar integral tungsten carbide type in common use in Australia.Examination of a new rod of the same type showed that a zone of spheroidized carbide about 0·25 in. wide was present about 12 in. from the shank end.Examination of the fractured rods revealed that 78 per cent. of failures occurred within 0·25 in. of the spheroidized zone at the shank end but in the main stem of the rod rather than actually in this softened zone where it might be expected to occur.This predominant type of failure at the shank end in the steel rods is caused by a highly anodic region corresponding to the first stages of spheroidization of carbides present in the steel. Accelerated corrosion in the narrow band havil\g this structure induces the formation of stress-concentrating corrosion pits, 78 per cent. of failures in this region being due to corrosion fatigue.The remaining 22 per cent. of failures, occurring in the as-rolled stem, were due to either corrosion fatiglie if failure were initiated at the water-hole surface of the drill rod, or to a decarburized outer surface if failure originated at this surface.Temperatures producing spheroidization were determined as 6007600C.Evidence suggests that approximately 75 per cent, of shank-end failures in all forged collar drill rods can be attributed to corrosion fatigue occurring preferentially in that section showing partial spheroidization of carbides· produced by the forging and hardeningoperations.Methods are suggested for reducing the frequency of fatigue failures in drill rods.INTRODUCTIONAn integral part of all tunnelling operations through rock is the drilling of suitably placed holes i:n.to which explosive is subsequently rammed and exploded.The drilling operation, whether for metalliferous mining or for general civil engineering constructional work; is...

Jan 1, 1955

The aquifer at Phosphate Hill, north-west Queensland, presents special management challenges. The site contains a phosphate rock mine, fertilizer plant and camp. All of the site water is provided by the Duchess Embayment Aquifer, located within the Burke River Outlier of the Georgina Basin. The Duchess Embayment is a triangular shaped, Cambrian marine sedimentary basin consisting of siliceous and calcareous phosphorites, shales, siltstones and sandstones. It is fault-bounded on all sides and has a regional dip of 5¦E. The aquifer is largely confined to the siliceous facies of the Beetle Creek Formation. It has a very flat potentiometric surface and an average thickness of 45 m with confining beds above and below. The siliceous facies derives from weathering of the calcareous phase and is highly transmissive while the calcareous zone itself contains less water and is dependent upon interconnecting fractures for its permeability. Recharge appears to occur where the siliceous facies crops out around the edges of, and within, the Embayment. Aquifer management issues revolve around two points: successful dewatering of the orebody for mining; and efficient management to maintain water quality and ensure supply over the predicted 30-year life of the project. Current operations are extracting water at levels much below that originally estimated. This is having a detrimental effect on mine dewatering with the SWL lowering at a rate slower than anticipated. As a result, ore parcels are now beginning to intersect the water table, providing a major constraint to the mining plan. The aquifer drawdown cone is extensive and very flat so to keep the water table at an appropriate level for mining the management plan will include more aggressive dewatering to lower the level of the entire aquifer. The additional water will either be disposed of downstream or stored in a holding dam or via the use of artificial storage and recharge. Water resource management will also need to maintain the current quality. About 37 per cent of the water currently extracted forms the low chloride supply required by the ammonia plant and the power station. This ratio is expected to remain applicable under any future operating conditions but the low chloride resource is restricted so will require prudent management to enable the supply to continue. At current usage rates aquifer recharge versus use will need careful monitoring to ensure that the resource remains viable in the long-term.

Jan 1, 2003

By Rowe J

The case study is based on the largest ore deposit at Mt. Lyell; the Prince Lyell deposit, comprising a regular lensoid mass of dissemina- ted and vein pyrite-chalcopyrite mineralisation. Reserve estimation employs conventional techniques, based on diamond drill hole and relevant development sampling data. Probable ore reserves are estimated using the contouring (isoline) method an longitudinal projections for ore thickness and accumulation (m %Cu) at a '0.8% Cu' cutoff. Final stope and pillar res- erve estimates (proved ore) are derived from designed ring tonnages and contoured accumula- tion for individual mining units, following more intensive sampling. Systematic grade control procedures have been adopted and individual stopes and pillars reconciled against mill production. The proved ore estimates have been found to com- pare favourably with the reconciled production.

Jan 1, 1979

This paper briefly reviews the background of mobile primary crushers and their current main areas of application. The benefits of applying mobile primary crushing and belt conveying systems are analysed. The impacts of applying such systems to different steps of the mine process are discussed, including mine development and planning. Application examples are used for demonstrating further possibilities to apply mobile primary crushing and belt conveying systems in mining projects successfully.

Jan 1, 2007

By J Harmse

This paper deals with the modernisation of the brakes on an electrically coupled Blair multi-rope hoist and covers the removal of the old calliper brakes and hydraulic control system, and its replacement with brake discs, disc braking units and hydraulic control systems. The paper covers the braking requirements of the hoist, which is made up of two electrically coupled single-drum hoists, together with the theory behind the choice of brakes and control systems supplied. The paper also covers the project logistics that were required in order to install and commission the new brakes and control systems with the minimum disruption to production on the only rock hoist on a major production shaft. Items covered include the modifications to civil works, pre-installation of bearing lubrication systems, brake discs and hydraulics and the interfacing of the new hydraulic control system to the existing electric control system. It had to be designed to be compatible to a new electric drive and control system due for installation at the end of 2005.

Jan 1, 2005

A general review of grinding mill steel liner evolutions/developments in recent times. The driving force behind these developments has been the mill operators desire to minimise the nett cost of their operation. These developments have resulted from a team approach between supplier, operators and reline crews. The move towards larger diameter high aspect mills, faster mill speeds, pebble ports and the use of large diameter grinding media has affected the traditional liner designs, which is placing higher demands on the supplier to meet these new working parameters and expectations. Operators are also taking closer ownership in the liners being supplied, as demonstrated by the development of their own mill liner specifications. This paper outlines some of liner developments and changes undergone at various milling operations around Australia and overseas (such as Cadia Hill, Kidston, Ok Tedi Mining, PT Freeport, etc) and where to in the future?

Jan 1, 2000

Qualitative measurement of respirable dust in metal mines is limited and an example of this is demonstrated at Northparkes Mine, where operational experience was sought for measuring dust standards and identifying exposure limits. However, relying on operational experience has limited value due to variation in observations from person to person and is based on visible dust (which is larger in size than respirable dust). However, with sophisticated dust measuring equipment, like the real-time aerosol monitor, dust concentrations can be accurately measured and recorded concisely. Research conducted as part of a collaborative agreement on behalf of Northparkes to launch an occupational dust monitoring program was implemented on the mine site. To form the basis of this research, it was hypothesised that no proper dust measuring testing at the mine site had been adequately identified. In addition, existing occupational hygiene monitoring programs did not adequately quantify employee exposures to these hazards. This project will outline the results of an occupational dust monitoring program, hence greatly improving the capacity to quantify the health risks posed to employees.

Jan 1, 2008

A review of the most widely used global extraction sequences in sublevel is undertaken. The review includes techniques used to extract massive as well as single or multiple steeply dipping tabular orebodies. The paper also deals with thick flat lying orebodies suitable for open stoping. Techniques used to minimise the effect of stress redistributions on a global scale are discussed for all the extraction sequences analysed.

Jan 1, 2003

Renison Limited produces high and low grade tin concentrates at an annual rate of 5000 tonnes of contained tin metal. In spite of the fine average cassiterite grain size, emphasis is placed on gravity concentration methods to produce a high grade final product. Cassiterite flotation is considered and operated as a gravity circuit scavenger responsible for approximately 15 percent of recovered tin metal as a fine grained low grade concentrate. Metallurgical problems mainly result from ore-type variations which may be aggravated by a number of circulating loads. The rationalisation of circuitry is being studied to provide more effective control by operators and to allow exploitation of current control and modelling techniques.

Jan 1, 1977

By Lunarzewski L

Gas problems, largely instantaneous outbursts of coal and gas, arose in the early days of coal mining in Australia, leading to attempts at predrainage often including destressing. With deeper mining and new gassy areas being mined, gas problems have increased. This has led to more research, such as into coal-gas relationships, and more practical trials into seam gas drainage in both the Sydney and Bowen basins. Predrainage techniques have been devised to suit the special Australian geological conditions and to take into account the erratic occurrence of CO, (nearly 100 per cent in some cases) in the seam gas. Better mining methods and other improvements are continuing. The introduction of post-drainage has been simplified by the adaptation of long established overseas techniques and equipment.Utilisation of seam gases in Australia is complicated by the presence of CO, but even with pure CH. little has been done.Seam gas drainage has some disadvantages such as the need for, and the dangers of, complex and rigorously controlled plant. Also drained coal becomes harder and dustier.

Jan 1, 1985

Traditional methods for the production of transition metals from their ores usually include the electric arc smelting of the ore or concentrate to produce a ferroalloy. This is subsequently refined to produce either a ferroalloy or to produce the metal or metallic carbide. Recent trends in the treatment of iron ores have seen the development of many processes for solid state carbothermic reduction followed by melting of the prereduced iron to produce steel and similar types of processes are under consideration for the production of ferroalloys. There are clear potential savings in energy and control of emissions from such processes. This paper discusses some research which is currently underway at La Trobe University into the solid state carbothermic reduction of chromium and tungsten ores to produce the metallic ferroalloy or the carbide for subsequent further processing. The kinetics of the carbothermic reduction of both chromite and scheelite were found to be dominated by gaseous CO rather than by direct carbon reduction. However the diffusion of carbon into the ore is certainly an important feature of the process. The production of tungsten carbide from the metal is the slow step in tungsten reduction. The development of phases during reduction were studied using a scanning electron microscope and an electron probe and knowledge of the phases produced allows analysis of the reduction process.

Jan 1, 1997