Search Documents

The electrochemical dissolution of gold and other noble metals in hydrochloric acid using alternating current has been investigated. The experimental results show that this technique is efficient for dissolving pure noble metals and offers prospects for their extraction from wastes and poor ores.

Jan 1, 1992

Since 1960, the Dongchuan Copper Mining Bureau, Yunnan Province, China, has treated copper oxidised ores by sulphidisation - flotation technique only to recover copper. In order to improve the metallurgical performances and economics of flotation, extensive development work has been carried out during the past 30 years: several specific flotation flowsheets have evolved from the originally selected `stage - grinding and stage - flotation' flowsheet to suit various ores; the overall grinding size of the ores has been increased from 80 per cent - 200 mesh to 90 per cent - 200 mesh, resulting in significant increase in copper recovery; the substitution of CaS for NazS proved to be successful in sulphidisation of copper oxidised minerals, and also in avoiding the depressing effect of Na2S on copper sulphide minerals; the application of a number of activators of copper oxidised minerals, especially ethylene diamine phosphate, has considerably improved the flotation performance and decreased the consumptions of other reagents. Finally, the combined use of sodium hydroximate with butyl xanthate has been shown to be effective in enhancing the floatability of both copper oxidised and sulphide minerals.

Jan 1, 1993

By A S. Ray, P S. Thomas

The characterisation of the surface area and porosity of opals derived from Tintenbar, a volcanic environment, and Lightning Ridge, a sedimentary environment, using nitrogen gas adsorption at -196¦C is reported. Both opal types were found to have relatively low surface areas and displayed little porosity. The low surface areas observed is indicative of the ability of silica to infill voids and interstices. Thermogravimetric analysis of the samples before and after degassing was carried out to determine the amount of water removed by the degassing process. Negligible difference was found in the water content before and after degassing in the case of the Lightning Ridge sedimentary opal, while the Tintenbar volcanic opal was found to have lost more that 60 per cent of its water during the degassing process. These differences were ascribed to the differences in the silica structure of the opals with the Lightning Ridge opal having a denser cage structure, which traps the molecular water, while a more open structure is postulated for the Tintenbar opal, allowing the water to be relatively easily removed.

Jan 1, 2008

By Reimer TH

The model described in this paper has been developed for and in close collaboration with the Bong Mining Company Ltd, Liberia/West Africa. When working an irregular deposit a de- tailed short term production schedule becomes necessary in order to ensure an equal and homo- genous concentrator feed. If the irregularity of the ore body exceeds a certain degree, blen- ding facilities have to be provided between the mine and the concentrator, but even then sche- duling of the mine production is inevitable to meet the given requirements of the blending bed and to keep these conditions steady for at least some of the successive periods. To assist the planning department in set- ting up optimal production schedules a computer model has been developed using a linear pro- gramming approach. The deposit is divided into equally shaped blocks containing defined quali- ties and quantities of ore and/or waste; from which one has to select those quantities of ore which will meet the requirements of the blen- ding bed. The objective function of the model

Jan 1, 1977

By Whiten W. J

Data from ball mills of a wide range of sizes are analysed using detailed mathematical models and non-linear least squares fitting techniques. In this way model parameters are obtained describing the behaviour of ball mills over a wide range of mill sizes and operating conditions. These parameters define the flow and breakage of each size fraction of ore in the mill. Flow of coarse particles through the mill is found to depend on the proportion of coarse particles present. The breakage rates of coarse particles are found to decrease markedly with mill diameter for mills over 3 m in diameter.Simulation of grinding circuit throughput at constant productsizing for different mill diameters shows that throughput is proportional to theoretical mill power consumption for mills up to about 3 m in diameter. Thereafter the throughput gradually falls below that indicated by power consumption, the decrease becoming quite significant for large diameter mills. Simple qualitative physical arguments are presented to explain this behaviour. The models developed have applications to ball mill scale up. Work on their further development is continuing.

Jan 1, 1982

By Itoh K, Sakai K, Tsuji K

In Japan there exists a strong demand for mechanical excavation for tunnelling bacause the blasting method which produces much vibra- tions and noises is restricted in its applica- tion due to the fact that there can be many cases where tunnelling sites are located ad- jacent to residencial areas as a result of Japan's being a thickly inhabited country. Pressing demands for and deep interest in the mechanical excavation method have been shown by the circles concerned with reasons that it produces smooth cutting surface and causes less overcutting of profile as a result of the diffusion of NATM (New Austrian Tunnel- ling Method) in the recent years. This has caused a strong desire of the users to apply the conventional mechanical excavation method that has been used mainly for soft rock cutting also to the field of hard rock cutting. In order to meet such needs of the tunnel- ling industry, further research and development have been continued to have successfully real- ized the Boomtype Tunnelling Machine for Hard Rock.

Jan 1, 1987

By Towsey C. A

Significant advances in regional geochemical exploration techniques have been made over the last 5 years in the search for gold deposits. This has occurred largely by the development of the bulk cyanide ex- tractable gold (BLEG) also known as the Bulk Cyanide Leach (BCL) tech- nique. The technique has been developed and designed for Australian conditions and has two main ad- vantages over the pan concentrate technique preferred by many ex- plorationalists, viz:,. 1. It is designed to collect ultra fine gold common to epithermal and other north Queensland types of gold deposits. 2. The large sample (approx.5 kg) allows very low detection levels, ranging between 0.1 and 0.05 ppb Au. The use of the BLEG technique in exploration has led to the discovery of the Wirralie gold deposit and numerous other epithermal gold prospects previously undetected by pan concentrate and minus 80 mesh (pathfinder elements) surveys in the Drummond Basin.

Jan 1, 1989

By Glastonbury J. R

Commercial operation of the Sherritt Gordon process in Australia for the leaching of nickel sulphides has promoted an investi- gation of the factors which influence extraction kinetics. This portion of the investigation has been directed towards the physical and chemical nature of the concentrate and the physical evi- dence of the mode of extraction. Details of the particle size distribution, mineral composition and chemical composition are given. The dis- tribution of various minerals in different size fractions and magnetic fractions is discussed. An electron microprobe was used to determine the composition of individual grains in the concentrate. The solid residue from an ammonia oxi- dation leach was subjected to microphotograph- ic examination, X-ray diffraction analysis and scanning by an electron microprobe. Clear evidence was obtained for a shrinking core mode of kinetic extraction with an amorphous iron oxide product layer contrary to previous reports that the latter is pseudomorphic with the original mineral.

Jan 1, 1973

The global recession of the 1980s drove commodity prices down and intensified cost competition. The 1990s saw a restructuring of the mining industry with the survivors adopting new technology, significantly increasing workplace productivity and reducing capital and operating costs. Major changes in mining industry business strategies evolved in the late-1980s including the development of miner - supplier - manufacturer - partnerships, cultural changes in work practices and common goals between the partners to reduce the cost of production. These industry trends are putting new demands on mining machine manufacturers and dealers both on the `hard' side of the machine business, such as research and product development programs, and on the `soft' side in terms of business processes, use of human resources and communication. The paper describes several mining industry trends as identified by a large supplier to the industry, and discusses the impact they are having, and will have, on mining machine development and the provision of product support services to the industry.

Jan 1, 1995

It has long been recognised that applications of the Net Present Value (NPV) investment decision making methodology can have serious deficiencies in situations where investment can be delayed and, once made, various options allow increases or decreases in the level of output. NPV valuation can undervalue the project if it does not incorporate future flexibilities or ""options"". It is important to realise that a proper valuation of a project (ie, valuation of its future cash flows) must incorporate an analysis of optimal future decisions involved in managing the project. Current valuation cannot be divorced from a consideration of future decision making. There is now a considerable amount of literature, mainly academic, identifying and exploring ways of remedying these deficiencies in the application of NPV. While the necessity of period by period analysis is sometimes acknowledged, little if any practical illustrative model building has been published to date, aside from algorithms using continuous time stochastic processes which deny access to the uninitiated.

Jan 1, 1994

In this paper the reactions which may lead to particle hydrophobicity/hydrophilicity as a function of grinding environment-are reviewed. The results of pulp chemical investigations related to a Cu-Pb-Zn ore on a pilot plant scale and laboratory tests with a Pb-Zn ore to evaluate the effect of some inhibitors on grinding/flotation are presented. The flotation recoveries of the ores treated by conventional and autogenous grinding methods show only a marginal difference and the results favour autogenous grinding. Iron originating from several sources manifests in the form of insoluble hydroxy complexes in the pulps. Such metal hydroxy complexes are hydrophilic and coat the mineral surfaces indiscriminately. On the other hand, selectivity is a problem for pulps ground by autogenous milling. Some corrosion inhibitors used in the laboratory grinding/flotation tests on a Pb-Zn ore showed maximum reduction in the wear of the grinding media ranging from 25 - 36 per cent, depending on the type and concentration of the inhibitor.

Jan 1, 1993

Natural gas is a comparatively new fuel in Australia. It was first used in small quantities in Queensland in 1965, but it was not until 1969 that natural gas reached the capital cities Brisbane, Melbourne, and Adelaide in that order; then in 1971 it reached Perth. By the mid seventies, natural gas had secured a significant proportion of the energy markets in Queensland, Victoria, South Australia and Western Australia and in 1976 supply commenced in Sydney. In that year - 1976 - gas supplied about 12.5% of the total demand for primary energy in Australia excluding transport. In the current financial year - 1981/82 - natural gas is expected to supply nearly 19% of the market and forecasts for 1990 range up to 25%. From a starting point in the late 1960's when manufactured gas supplied a small but important proportion of the non-transport energy market - less than 3% - we have exper- ienced an average growth of nearly 24% per annum up to the present time.

Jan 1, 1982

By S Strohmayr, R Harvey, A See

Ernest Henry Mining Pty Ltd started production in August 1997. The Ernest Henry orebody consists of two distinct parts, a complex supergene ore zone overlying a primary ore zone. The economic copper minerals in the supergene ore were chalcocite, bornite, secondary chalcopyrite and native copper while the primary zone has only chalcopyrite. The variability of the supergene zone made concentrator operation difficult and predicting metallurgical performance using mineralogy essential to establish the capabilities of the concentrator. A paper presented at the 1998 Mine to Mill Conference entitled Mineralogy Controlling Metallurgy at Ernest Henry Mining (Barnes, Strohmayr, Brindley and Munro, 1998) presented the testwork and initial plant surveys that showed that the mineralogy of the ore controls the metallurgy of the concentrator. This paper presents the data obtained from the subsequent years of operation treating both the supergene and primary ore types. A review of the actual supergene mineral distribution in feed and subsequent recoveries compared to those predicted as part of the flowsheet design is also presented.

Jan 1, 2003

By Shinnosuke U, Zhang HE, Qian X

In this paper it is recommended that pyrite is to be separated as froth from arsenopyrite by selective depression of arsenopyrite in strong alkaline medium (1), by oxidation with chlorinated lime (II), by co-use of chlorinated lime with sodium carbonate (III), and by modification with `L' reagent (know-how) without filtering to get rid of residual copper ions after Cu activation (IV). The corresponding principles of these (new) effective methods were briefly discussed. The artificial mixture (1:1) of pyrite and arsenopyrite could be successfully separated, and concentrates of pyrite containing 2.12 per cent (I), 7.00 per cent (II), 2.60 per cent (III) and 3.16 per cent (IV) arsenic with recovery of 90.9 per cent (1), 89.5 per cent (II), 89.0 per cent (III) and 81.4 per cent (IV) respectively can be obtained by only one flotation. Some effective precautions were suggested to improve the separation of arsenopyrite and pyrite (or other sulphides) by flotation.

Jan 1, 1993

By Kershaw MG

At the Risdon plant of the Electrolytic Zinc Company of Australasia Limited, impurities toxic to the electrolytic production of zinc metal, notably arsenic and antimony, have traditionally been coprecipitated when precipitating iron as ferric hydroxide. With the development of a new lead/zinc mine at Elura, New South Wales, it was anticipated that the concentration of impurities, particularly arsenic, in the zinc sulphide concentrates treated at Risdon would increase. This suggested that an increase in the capacity of the iron purification step in the Risdon plant would be required to cope with the higher input of these impurities.Laboratory investigations showed that the additional capacity would be achieved, either by a massive increase in the amount of iron used as the "collector" in the process, or by a two-stage process. The latter approach was preferred as an increase in the amount of iron precipitated would lead to much higher operating costs and overloading of the existing equipment.

Jan 1, 1985

Autocompression and virgin rock tempera ture have a marked influence on the ventilation of the lower levels at North Broken Hill Limited N.S.W. To maintain comfortable working temp- eratures without penalty to working hours, increase in airflow or the cooling of the work area is necessary. The use of refrigerated air cooling is discussed. Ventilation of underground mining opera tions at North Broken Hill Limited is accomplished by downcasting air through No.3 shaft, the main operating shaft, 1581 m deep, with additional air through No.1 shaft (542 m) 2 and No.2 shaft (978 m), both no longer opera- tional shafts. Air is upcasted through No.3 ventilation shaft which is 4.9 m diameter and concrete lined, from the No.28 level (1140 m) to the surface. On the surface level of this shaft is a horizontally mounted Richardson 4800 mm diameter single stage axial flow fan with adjustable pitch rotor blades.

Jan 1, 1977

By Glastonbury J. R

The kinetics of the direct chlorination of, zircon in the presence of carbon was studied at temperatures between 9000C and 12000 C. From the experimental data it is prop- osed that the most likely mechanism for metal oxide (MeO2) chlorination is as follows: At I Surfaceon zMeO2+ZMeCl - MeOC12 (1) At Carbon MeOC12+C+Cl MeC14+CO (2) Surface It.is envisaged that this type of mechan- ism would occur for both the zirconium and, silicon. constituents of the ore. In the above mechanism; the surface re- actions appear to be fast and not rate controll- ing. In a carbon surface deficient bed the diff- usion of oxychloride intermediate through the boundary layer to the carbon surface becomes the rate controlling step. In a zircon surface deficient bed the diffusion of oxychloride away from the zircon surface controls the reaction. This postulated mechanism can be used to ex-, plain the observed experimental effects.

Jan 1, 1973

By Olden WH

A scheme is presented whereby the complexities of design and operation of a hydraulically powered coalmine support are modelled using the finite element method. This enables predictions to be made of the interaction of the support with its environment in a variety of operating conditions. The model is a two dimensional representation. The modelling scheme was applied in two case studies. In the first, the performance of a four leg support was uprated by increasing the front leg force. The finite element model enabled changes in overall support performance to be verified. In the second case study, the change in lateral force developed by a two leg support was assessed with changes in support operating height and floor foundation stiffness. The modelling scheme is capable of further development with the possibility of extending the model into three dimensions and the addition of control elements that would enable an actual mining sequence to be Represented.

Jan 1, 1992

Underground mine ventilation is now com monly simulated on a digital computer. Such a programme, incorporating natural ventilation has been modified by others to account for methane emission and elevated local tempera- tures. At Wollongong University, the pro- gramme was further developed and extensive interactive graphics incorporated such that any view of the three dimensional mine could be viewed, and superimposed upon that view are areas where a nominated parameter has exceeded a particular value - generally at a nominated time after a particular event and usually a fire/explosion of one type or another. A further programme was developed such that up to 20 'times' could be examined at a particu- lar location after say, a fuel rich fire at some other place in the mine. The output from this programme includes a plot of methane 1, smoke 1, temperature, pressure and air flow versus time - a most useful graphic to observe the limits of safe attendance in a particular Airway.

Jan 1, 1983

By Muchi I

To clarify the characteristics of non-uniform flow of gas through layered burdens of ore and coke, flow equations of continuity and motion were solved numerically taking account of the geometrical effect of a bed. The results are compared with that predicted by an approximate solution. A mathematical-kinetic model for determining the distributions of process variables over the region from the top to the melting level of blast furnace with the horizontal or the inclined layers of burdens is developed in consideration of the uneven gas flow. By the use of this model, the longitudinal and the radial distributions of process variables in an existing blast furnace in Japan were calculated with the aid of a digital computer. Computed results show that the process variables and the melting level change remarkably over the cross-section of the furnace and that the patterns of these distributions are similar to the results observed by other investigators.

Jan 1, 1975