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By F Cesnik, P Griffin, S Green

In July 2004 a flotation concentrate regrind circuit was commissioned in the æHigh GradeÆ Ridgeway concentrator at NewcrestÆs Cadia Valley Operations. This was the culmination of two years of project testing, process design and planning which commenced shortly after commissioning the concentrator in March 2002. During the two-year project evolution alternative grinding technologies were evaluated from conventional ball milling through to sand milling. A Detritor mill was eventually selected for the duty and the criteria on which this selection was based will be presented. As the project evolved so too did the equipment sizing with the concentrator quickly exceeding design capacity of 4 Mtpa and currently averaging 5.6 Mtpa, the process design had to accommodate this and future potential throughput increases. This paper will focus on the supporting testwork, circuit surveys and concentrate properties which were used as the design basis for the project. The economic evaluation which led to the project receiving board approval in November 2003 will also be presented. Detailed design and construction management issues will be discussed as will preliminary results and findings up to November 2004.

Jan 1, 2005

Traditional techniques for extracting pillars in thick underground coal seams in India are reviewed. Problems encountered are principally control of roof strata and low recovery. Recently developed mechanized methods and projected newer techniques are discussed.

Jan 1, 1986

The mine planning and operational aspects of applying Continuous Surface Miner (CSM) technology to Australian coal strip and open cut mines is investigated for both existing and planned deposits. CSM produc- tivity as a function of geomechanical properties, formation thickness, mechanical availability and in-pit physical constraints, are considered. Productivity and operational costs are derived from current production machines and from first principles.

Jan 1, 1989

Mining has long been an important activity for the people of Australia. The Aboriginals used rocks and minerals in their culture many thousand years before European settlement. It was not until 1840 that silver-lead ore was discovered in the Mount Lofty Ranges, and developed as Australia's first metalliferous mine.

Jan 1, 1995

The reduction of titanium tetrachloride to trichloride can be achieved by employing hydrogen and electric arcs. It is possible to produce melts containing up to 50% TiCk in the eutectic mixture of LiCl/KCl by striking a D.C. arc at the surface in the presence of hydrogen and TiCl. vapour. If the electrode IS made to just penetrate the surface of the salt mixture, a hot zone results from the' high resistance contact with both lower chlorides and sintered titanium may be produced. The sintered metal forms just below the melt surface while the trichloride forms at the gaslIiquid junction.The "hotspot cathode" appears to offer a solution to the problem of producing coherent deposits as the spong'e metal can 'be continuously withdrawn in a similar manner to the "calcium process".INTRODUCTIONConsiderable interest has been shown for some years in the possible development of a cheap electrolytic process for the extraction of titanium metal, since a method using simple materials and cheap electric power would materially reduce the cost of production. Even when cheap starting materials are used, however, there exist several general difficulties in the operation of plant which both limit the speed of production and increase the cost of the product. It happens that most of the techniques so far tried produce a powder as cathodic deposit, and when this is the case the following difficulties arise:1. The whole contents of the bath must be treated with solvent in order to extract the 'metal powder which may itself tend to oxidise, and thus become contaminated.2. Fine metal powders, which often contain residual entrained salts, are less easy to consolidate by arcmelting than metal sponge.

Jan 1, 1956

By A M. Robertson, R Lefebvre

Air movement and associated oxygen transport through waste rock dumps has the potential to significantly enhance the rate of oxidation of pyrite-bearing material. While this is a desired outcome for most heap leach operations, airflow in waste rock storage facilities can result in significant increases in generation and acceleration of acid rock drainage. Hence, a good understanding of internal airflow through waste rock dumps is required to control ARD and minimise any associated liability. The principal mechanisms contributing to airflow and oxygen transport in a waste rock pile include: diffusion; advection due to a thermal gradient (chimney effect) and/or wind pressure gradients; and advection due to barometric pumping. While diffusion is typically limited to a near-surface zone of a few meters depth, advection and barometric pumping have the potential to move air (and oxygen) to much greater depths into the pile. In general, the more permeable the waste rock material, and the greater the height-to-width ratio of the waste rock pile, the greater is the potential for advective air movement. The reactivity of the waste rock material as well as the coarseness (hence air permeability), and the spatial variability of these properties within a pile, have a strong influence on the magnitude of thermally induced advection. In contrast, air movement due to barometric pumping is controlled by the waste rock porosity, changes in ambient air pressure and the heterogeneity of air permeability of the waste rock dump. Results of field monitoring and numerical modelling using TOUGH AMD are presented to illustrate the concepts on air movement in waste rock piles discussed in this paper. During the design and construction phase, airflow can be controlled by judicious placement of reactive waste rock and use of selective placement techniques to control the internal structure of the waste rock facility (eg introduction of horizontal layering, prevention of inclined, high-permeability, channels (æchimneysÆ)). Several closure measures are available to minimise airflow including: placement of a low-permeability cover to reduce air entry; and placement of a non-reactive cover material to isolate reactive material from the zone of active airflow and/or regrading of the waste rock pile to obtain a geometry and internal structure less susceptible to advective airflow.

Jan 1, 2003

By Biao Q, Mizuta Y

Thermal constants such as thermal con- ductivity and thermal diffusivity of rock and coefficient of heat transfer of airway wall are the most important characteristic values which decide accuracy of prediction calcula- tion. However, quality of rock is not homoge- neous and water content in rock varies with location and so, a method for in-situ measure- ment of thermal constants must be taken in. The method developed by us is to measure in- situ rock temperatures at two different depths from airway wall. It is simple and we found its accuracy is good enough in the engineering Sense.

Jan 1, 1988

By Barnett LJ

The Kellogg slag fuming model is extended to apply to the Port Pirie plant which uses recuperative heating of secondary air. Exten- sive investigations of plant operations pro- vide parameters for use with the model, and verification that the resulting model provides simulation which is very close to actual plant performance. The model is used to_deter- mine optimum slag fuming operating conditions, and the results of several other investigations with the model are briefly described.

Jan 1, 1975

Experience in evaluating grade control at operating mines has shown that a number of similar errors re-occur in diverse settings. These can be broadly classed as technical errors, and procedural or grade contra management errors. Examples of typical errors are presented a; generalised case studies. A brief explanation of why the recommender solution worked is also presented for each case.

Jan 1, 1993

The complicated mining-geological conditions in the Kuzbass have led to some difficult mining situations in the past. Now, with historical data, supplemented by geomechanical information and measurements, together with an appropriate kinematic theory, a more reliable basis exists for prediction and control of the geomechanical state during extraction, with caving and with backfilling. Continued progress and improving reliability comes from data banks and computations, and now prediction of geomechanical situations is upgraded by more routing measurements and monitoring. Not only in the Kuzbass, but throughout the USSR, 14 dedicated groups are ready to solve various specific problems of prediction an control of geomechanic situations with assured increase in the quality of mining.

Jan 1, 1991

By T Lancaster

The Mount Gordon operation, consisting of the Esperanza open cut mine and the unique Mount Gordon Ferric Leach processing plant, is operated by Western Metals Copper Ltd at Mount Gordon, 125 km north east of Mt Isa. The processing plant treats predominantly the secondary copper sulphide minerals, chalcocite and covellite. The gangue consists of massive pyrite and a range of silicified siltstones. The processing plant utilises a conventional single stage SAG/cyclone milling circuit, followed by low-temperature/low-pressure autoclave oxidation to produce copper in solution. The pregnant leach solution is treated via conventional SX/EW technology to produce copper cathode. Currently the plant is operating at a nominal production rate of 48 500 tpa copper. The Mount Gordon Ferric Leach technology is the worlds first integrated pressure leach/SX/EW process to be used to treat copper sulphides on a full plant scale. In the last six months, July to December 2001, the plant has emerged from a two-year postcommissioning phase to achieve steady state operation. This has been characterised by high plant availability and consistent production performance in excess of the name plate capacity of 45 000 tonnes. Production rates will continue to increase over the next 12 months to over 50 000 tpa via a planned process of incremental improvements. The pressure leach circuit has consistently achieved availabilities exceeding 95 per cent over the past 18 months. Notwithstanding this, the leach circuit still has a much greater requirement for planned maintenance than SX/EW. For much of the Mount Gordon processing plantÆs operating life, the leaching process has constrained production. Recent developments arising from detailed mass and energy balance modelling have now significantly improved leach capability, resulting in the plant bottleneck being shifted to electrowinning. In order to balance the capabilities of the two circuits however, the surge capacity between leach and SX/EW was increased substantially. This effectively de-coupled the higher capability but lower availability leach circuit from the lower capability but higher availability SX/EW circuit. As a result, electrowinning utilisation has increased to in excess of 98 per cent, which is reflected in a higher overall plant throughput.

Jan 1, 2002

A methodology is described to integrate heap leaching into a CIP operation. The paper firstly describes what is meant by a 'systems approach'. A broad view of the objectives of integration of heap leaching into CIP is given, followed by the components of the system, and then a description of the methodology for integration. The seven stages of integration are given as determination of distribution of gold, sampling, metallurgical testwork, conceptual study, pilot heap operation, pit modelling and pit optimisation. The final result is a series of optimised curves which determine the maximum value of the orebody, and the optimum cut-over grade from CIP to heap leaching.

Jan 1, 1992

Tyre cost at Mount Morgan Limited had been 24% of the truck operating cost. Comprehensive tyre testing resulted in a reduction in tyre costs of about one third. A record of the evaluation techniques may enable the selection of tyres that are most suited to particular conditions. Rubber characteristics, rubber quantity, tyre design, road conditions, dump conditions and inflation pressure were found to be sig- nificant variables. Measurements of tyre temperatures at the breaker strip were used to select the tyre design and inflation pressure required for Mount Morgan Limited's conditions. Relugging of tyres was discontinued as a result of tyre testing.

Jan 1, 1974

George Fisher Mine, near Mount Isa in northwest Queensland, has been producing Pb-Zn-Ag ore since the late 1980s. It consists of two separate underground deposits, George Fisher South and George Fisher North. These two deposits are drilled and modelled separately but are crushed and hoisted as a single stream. The Pb-Zn concentrator in Mount Isa processes ore from George Fisher Mine and Black Star Open Cut, with production also from the Isa Lead Mine until January 2006. This paper outlines the steps involved in setting up a robust reconciliation system for George Fisher Mine, in conjunction with requirements of the Pb-Zn concentrator, Black Star Open Cut Mine and the Mount Isa Lead Mine. Good quality input data and commitment to training have contributed to establishing a robust and effective reconciliation system. Reconciliation data has highlighted several other continuous improvement opportunities.

Jan 1, 2006

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 Moore R. F, Macias L. F

The Filbara region of northwestern Western Australia contains several known occurrences of mafic/ultramafic rock assemblages which may host platinum group element (POE) mineralisation. This paper deals with occurrences at Munni Munni and Andover. The Munni Munni complex is of particular interest because it is known to contain PGE mineralisation and is currently undergoing active exploration. The US/Australia Joint Scanner Project of October 1985 collected airborne scanner data for the BMR over Munni Munni. Such an ultramafic-mafic complex had not been previously researched with advanced remote sensing instrumentation. Extensive investigation of data from the NSOO1 (Thematic Mapper Simulator) scanner resulted in successful differentiation of gabbroic and ultramafic rocks, and also subdivision within the ultramafies. Similar differentiation could not be achieved using conventional Landsat MSS imagery and aerial photography. Encouraged by those results and in support of BMR field research into the mafic-ultramafic suites of the region, data from the Landsat Thematic Mapper (TM) instrument were investigated to attempt differentiation of the ultramafic and mafic rocks in the Andover complex some 50 km to the northeast of Munni Munni.

Jan 1, 1988

Most internationally traded iron ore resources are derived from multiple mine sites, transported to a port facility where they are blended and possibly further processed prior to shipping. Provided the proportion of contributions varies over a number of shipments an estimate can be made of the bias introduced by mine site sampling, analysis and materials handling systems, using zero-intercept multiple linear regression. Further regression applied to the residuals allows the error variances for the source mines to be estimated. Various sampling strategies are used by the industry. All have shipment-loading sampling on which payment or at least provisional payment is based. In most cases sampling prestockpile is used at mine sites to verify estimated production grades. Train grades are estimated from mine stockpile grades and in some cases train grades are verified by port input sampling. The methodology used is presented in this paper. Simulated data have been used and do not reflect the actual performance of any operator. The merits of the various systems and the implementation and potential limitations of our method are discussed more fully in a companion paper (Ziegelaar and Everett, 2010).

Mar 1, 2010

By Miovski P, Hooft P. V

In the majority of recently commissioned gold mines granular activated carbon is used to adsorb gold from alkaline cyanide pulps or solutions. At the same time the carbon also adsorbs many other inorganic and organic species, most of which lower the activity of the carbon. Removal of these foulants is necessary before the carbon is reactivated and recycled. Standard practice for re- storing carbon activity involves high temperature treatment in a kiln - an apparently straightforward unit operation which is not always satisfactorily carried out. This paper presents the results of some fundamental work carried out on the thermal reactivation of carbon in a laboratory rotating pot kiln. The effects of temperature and steam addition on carbon activity were examined and compared with the activity of carbons obtained from a number of commercial kilns. Carbon was also reactivated using a small-scale Rintoul Furnace in which carbon was resistively heated by the direct passage of an alternating electric current. It was established that both elevated temperatures and the addition of steam to hot carbon generally enhanced its activity although peat-based extruded carbons responded a little differently to coconut shell types. Other measurements made included the weight loss and the hardness of carbons as a function of reactivation conditions.

Jan 1, 1987

By S R. Grano, M Vera

This paper deals with two separate case studies investigating the froth phase performance and characterisation of two industrial rougher/ scavenger flotation circuits. Froth phase performance was quantified using a mass balance approach to estimate froth zone recovery. Measured characteristics of the froth phase included frother solution concentration determined by gas chromatography, and the time taken for an equilibrium froth sample to decay to one-half of its original froth height. The latter measurement is referred to as the æfroth half-lifeÆ and is strongly linked to froth stability. Special methods and techniques developed to preserve frother in solution and to measure froth half-life are briefly described. The frother type in the first case study was a mixture of straight and branched alcohols, whilst the frother type in the second case study was a mixture of alcohols, aldehydes and triethoxybutane. The first case study focussed on a flotation circuit treating a low-grade ore containing only a small fraction of floatable copper sulfide minerals, while the second case study focussed on a flotation circuit treating a higher grade complex sulfide ore containing significant quantities of chalcopyrite, galena, sphalerite and pyrite. It was found that froth zone recovery of valuable mineral generally decreased down-the-bank of the two industrial rougher/scavenger circuits. Moreover, decreases in froth zone recovery significantly limit the overall cell recovery of valuable mineral achievable from the plant scavenger cells. However, the decrease in froth zone recovery could not be linked to the removal of frother from the pulp solution to the concentrate product in the preceding rougher flotation stages. Measurements of residual frother in solution suggested that, approximately, only five to ten per cent of the added frother was removed into the rougher/scavenger concentrate, with the remainder appearing in the scavenger tailings. This finding suggested there was apparently adequate frother in solution in the scavenger stages.

Jan 1, 2005

Large scale rhyolitic volcanism is an important process at some convergent plate margins because it leads to chemical differentiation of the upper.-crust and is responsible for the production of long lived near surface thermal anomalies; the Taupo Volcanic Zone is.a Quaternary example. The main features of the magmatic systems-of the zone. are the existence of large high level chambers containing homogeneous silicic magma which erupt at intervals of thousands to tens of thousands of years. Geochemical work on the deposits resulting from these eruptions has shown that with few exceptions the magmas have been remarkably uniform in their . composition throughout the history of the zone although individual batches with lifespans of the order of. one hundred thousand years can be recognised by subtle differences in trace element ratios. Basalt is a rare proportion of the rocks exposed at the surface but has played a major role as a medium for heat transfer and as an end member in chemical mixing processes.

Jan 1, 1987