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By C. Yu, B. Dejun, Y. Weilu, Z. Minglin, K. Htet Oo, Z. Suiyi, L. Xin, Q. Wensheng, K. Hua

Grinding sludge is a gel-like hazardous waste generated in large quantities during metal cutting processes. Conventional calcination and hydrometallurgical treatment of oil-rich grinding sludges emit flue gases and generate insoluble residues. This study proposes CH2Cl2-assisted phase separation under mild conditions to enhance oil removal and metal recovery by overcoming encapsulation effects. Neodymium iron boron grinding sludge, containing 10.4% oil, 8.3% neodymium, 4.5% praseodymium, and 55.8% Fe, was selected as a representative material. Complete dissolution was achieved using a dichloromethane/hydrochloric acid mixed solvent, producing an organic phase enriched with oil, carbon and grease, and an aqueous phase rich in Nd, Pr, and Fe. The aqueous phase was processed to sequentially precipitate a double salt containing 98.58% Nd/Pr and an iron yellow product with 99.97% Fe. This approach provides an effective and economical strategy for the simultaneous recovery of oil and metallic products from grinding sludge, avoiding harsh conditions or costly equipment, offering significant potential for practical on-site industrial applications.

Aug 3, 2026

By C. Gómez, E. Rubio, L. Alfaro, R. Cuba, C. Morante, J. Jarufe

The increasing global demand for metals compels the mining industry to optimise production methods and planning to meet rising needs. However, as mining operations extend deeper, the risks associated with mining-induced seismicity and rockburst hazards become more critical. This paper presents a novel and practical methodology for integrating seismic hazard considerations into mine production planning. By analysing historical seismic and mine production data, the methodology develops actionable guidelines for addressing short-term planning challenges. In contrast to traditional reliance on unwritten miner experience or time-intensive numerical modelling solutions, this approach offers a streamlined and timely framework for decision-making. The proposed framework is applied to a case study of a Peruvian polymetallic mine utilising the sublevel stoping method with backfill. The results demonstrate the methodology's ability to optimise short-term operational decisions, striking a balance between production efficiency and safety standards, and highlighting its potential for broader application in the mining industry.

Aug 3, 2026

By M. A. Dippenaar, J. L. van Rooy, R. Bush, M. Maoyi, A. Lotriet

Effective management of unsaturated fluid flow in open-pit excavations is critical, as mining disturbances like blasting can enhance fracture connectivity, permeability, and water infiltration, thereby compromising slope stability. This study evaluates infrared thermography as a non-invasive tool for detecting seepage zones in a fractured rock highwall at an open-pit quarry in South Africa. Field-scale measurements and photogrammetry data are used to gain a better understanding of unsaturated flow behaviour in fractured rock masses. Passive infrared thermography established baseline thermal anomalies associated with natural groundwater seepage, revealing distinct cooler surface patterns in highly fractured domains that aligned with geotechnical mapping. Active infrared thermography using controlled injection of cold water into the high wall enabled real-time thermal monitoring, confirming preferential channelling along lithological contacts. The findings demonstrate that infrared thermography is a powerful and reliable technique for remotely evaluating areas susceptible to seepage on high walls, highlighting its promise for improving hydrogeological risk assessment in mining operations.

Aug 3, 2026

By F. D. Agrensa, J. Hadjigeorgiou, S. J. Thorpe

The recent introduction in underground mines of mechanical hybrid rockbolts has been driven by efforts to eliminate the use of resin in heavily fractured ground. Mechanical hybrid rockbolts consist of a steel tendon mechanically anchored within a friction unit. Installation of mechanical hybrid rockbolts is percussion-driven by the rock drill and the mechanical anchor is subsequently activated using rotation. The bolt configuration and installation process overcome issues associated with hole closures and the use of resin. Recent work has focused on understanding the behaviour of the rockbolts under quasi-static and dynamic conditions but there is scant information on the anticipated performance in corrosive underground environments. This paper reports the results of a comprehensive accelerated corrosion investigation of the principal components of mechanical hybrid rockbolt, which can aid in establishing the long-term suitability of mechanical hybrid rockbolt in corrosive environments.

Aug 3, 2026

By G. Danha, C. Lebudi, O. P. Oladijo, V. Moyo

Percolation vat leaching offers mid-tier artisanal and small-scale gold mining a practical compromise between heap and agitated tank systems. However, the common practice of sequentially using mercury amalgamation and cyanidation causes severe metallurgical and environmental failures. This review demonstrates that static artisanal and small-scale gold mining vats suffer critical oxygen starvation, triggering cascading geochemical hazards. Residual elemental mercury (Hg0) acts as an aggressive reagent sink, rapidly exhausting localized cyanide to generate highly mobile, toxic mercury-cyanide complexes. Concurrently, oxygen depletion retards sulphide ore oxidation, precipitating elemental sulphur (S0) and polysulfides that passivate the native gold surface. To mitigate these bottlenecks, this paper proposes low-complexity interventions: solid oxygen-release compounds (CaO2), hypochlorite pre-oxidation, and trace lead nitrate to sequester sulphur. Ultimately, formalising the sector requires the absolute decoupling of amalgamation from cyanidation and a transition toward modular, mercury-free vat systems.

Aug 3, 2026

By R. Tinsley

Project-finance risk assessment is mature and approached systematically. Mining industry due diligence remains fragmented with specialists addressing different aspects of the project such as reserves/JORC, environmental impact, commodity market, even financial analysis/ modelling. Each professional has a natural tendency to believe that the risk factors they have examined are the key ones necessary to be reviewed, as if their review will stand in isolation from others in the way a project materialises. By first laying out the project risk categories and risk matrices, this paper examines the due diligence process with a keen eye to the risk assessment and overlap/interaction. Some cross fertilisation of due diligence techniques from other industry sectors is placed into the mining context. Six case studies are then presented with regards to due diligence features in each project's feasibility review or financial information/ offering memorandum. A power case first shows the differences between the due diligence expectations of banks versus bond financings. Then some Australian and Indonesian mining development cases are analysed to see the due diligence learning points. Some of these were project/due diligence failures. The conclusion focuses on the value of a systematic risk assessment for project evaluation, all from the project-finance perspective.

Jan 1, 2007

By Alexandra Amiel

Tarkwa Gold Mine is owned by Gold Fields Ghana, IAMGOLD and the Government of the Republic of Ghana in a 71%, 19% and 10% ratio. The mine is operated by Gold Fields Ghana. This large, low-grade, open pit, gold mining operation is located in Tarkwa, in the Western Region of Ghana, approximately 320 kilometres by road, west of Accra, the capital of Ghana, West Africa. In the Financial year ended June 2007, the operation mined a total of 108 million tonnes of which 22 million tonnes was ore. The mined ore is processed through three gyratory crushers supplying two heap leach pads (North and South) and a carbon-in-leach (CIL) plant. Before the 6 Sigma project commenced, the current fragmentation was resulting in sub-optimal feed size to these crushers. It was decided to use 6 Sigma methodology to improve the fragmentation. A defect was defined as a fragmentation analysis indicating less than 95% passing 750 mm. The objective was to improve fragmentation in order to achieve a constant throughput to the north heap leach crusher of 1500 t/hr, a 5% increase in pit loading efficiency and a 50% decrease in rock breaker hours, equipment damage costs and in-pit sheeting costs respectively. However, this was not to be achieved at the expense of grade control as Tarkwa is exploiting a low grade, high volume deposit and therefore ore dilution must be kept to a minimum. This paper is intended to take the reader through the various 6 Sigma phases of the project (Define ? Measure ? Analyse ? Improve ? Control) which have resulted in a 10% reduction in loading times, of which half has been attributed to improved fragmentation, as well as a substantial increase in blasted stocks. The focus has been on both drilling and blasting parameters as both processes had to be taken into account. These parameters are technical but personnel factors were also identified and dealt with as they arose. In order to measure the impact of any change in the process parameters on the fragmentation size distribution, cameras have been acquired. One has been installed looking into the bowl of the north crusher and the other one was dedicated to field observation, of individual blasts. Both are used for on-going fragmentation analysis. At Tarkwa, mining efficiency is strongly dependent on good fragmentation as well as the presence of un-blasted ?toes? on the pit floors. Crusher throughput depends on an acceptable ore fragment size. Compliance to plan with regards to actual hole depths was temporarily monitored by manual hole dipping, but, this is now being replaced with a fully automated Drill Data Management system developed by Sandvik and Modular Mining. The Six Sigma methodologies, using control charts based on data collected in the field, allowed the mine to improve methods with regards to the control of blasted material. It also enforced the implementation of a quality control programme encompassing the entire Drill and Blast process.

Jan 1, 2008

By M. Tangstad, M. Zhu, M. B. Folstad

The dissolution rate of silica (SiO2) into different compositions of SiO2-CaO-Al2O3 slags was studied at 1500° C and 1550 °C under an inert atmosphere of argon. The results show that the dissolution process is controlled by mass transfer of SiO2 in the slag. The experimental results were used to evaluate the dissolution rate, which was found to increase with increasing CaO/Al2O3 ratios as well as with increasing temperature. Boltzmann–Matano analysis was applied to obtain a profile-based effective chemical inter-diffusivity. The extracted inter-diffusivity coefficients decrease systematically with increasing SiO2 content and fall in the range of ~10-12 – 10-13 m2/s. These low values imply intrinsically slow diffusion-controlled SiO2 enrichment, so that approaching equilibrium is unlikely within the residence time of descending materials in industrial furnaces.

Aug 3, 2026

By S. Swanepoel, M. W. Erwee, Q. G. Reynolds, R. Fourie

Unexpected excursions in electrode hoist position are occasionally observed on direct-current arc furnace plants producing ferrochromium, and are not readily explained by changes in electrical power supply or known process disturbances. One possible mechanism for this is variations in feed reductant balance altering the freeboard gas composition and, hence, the thermophysical properties of the arc plasma, changing the arc's effective electrical resistance. This hypothesis is investigated using an integrated computational modelling workflow comprising thermochemical equilibrium simulations in FactSage, plasma property calculations using the open-source minplascalc tool, and magnetohydrodynamic arc simulations using the open-source plasmaArc solver. Three reductant balance conditions were examined across a range of effective slag temperatures. Results show that while the reductant balance does influence freeboard gas composition and certain plasma properties (particularly electrical conductivity and radiation emission coefficient when lower slag temperatures are considered), these two effects act in opposing directions and largely cancel one another. Arc voltages and resistances are consequently not significantly different between reductant conditions. It is concluded that variations in feed reductant balance are unlikely to be the primary cause of the observed hoist excursion events via this mechanism, and directions for future investigation are proposed.

Aug 3, 2026

By B. S. Xakalashe, M. Khama, Q. G. Reynolds

Pre-reducing chromite with hydrogen offers significant benefits, including reduced energy consumption in downstream smelting and lower carbon dioxide emissions. To leverage these advantages, it is essential to develop computational models that facilitate the design, optimisation, and control of the process. Full scale models such as 3D computational fluid dynamics models are often used to investigate the multi-scale flow physics in heterogeneous reactors. However, these models impose prohibitive computational expense in the modelling of heterogeneous reacting flow systems. The high computational expense prevents the use of high dimensional systems in real time control and online optimisation of reacting flow systems. In order to facilitate incorporation of predictive models in the heterogenous reacting flow systems control loop, computationally efficient reduced order models are required. Owing to these requirements, a reduced order model for pre-reduction of chromite with hydrogen was developed with the view to rapidly predict the performance indicators for pre-reduction of chromite with hydrogen. The Thiele modulus method was used to develop the reduced order model, and the model results were compared to isothermal pre-reduction experimental results at a range of pre-reduction temperatures from 1200 oC to 1400 oC. The model predicts the degree of reduction, diffusion of gases through the product layer, unreacted core radius of the grain radius, and local and global conversion. The final conversion across all temperatures as predicted by the reduced order model deviate from the experimentally calculated conversion by a maximum relative error of 2.7% while the initial conversions differ significantly, reaching a maximum error of 65%.

Aug 3, 2026

By R. Snodgrass, G. Marsden, K. van der Merwe, R. Hundermark

The Southern African Ni-Cu-PGM smelting industry has evolved significantly from 1937 to date. As demand for platinum group metals has increased, smelting technology development has been closely linked to the need to process more concentrate, but also to changes in the chemistry and mineralogy of concentrates from the various platinum group metals-containing reef types. Early technologies relied on blast furnaces and Great Falls converters, but from the late 1960s, electric furnaces and Peirce Smith converters were commissioned. In the early 1990s, the introduction of water-cooled copper plate coolers into the slag zones of the primary furnaces enabled greater power intensity and throughput, with further intensification from the early 2000s requiring the use of deep-cooled copper coolers. Converting technology was also modernised to include a top submerged lance converter in one instance. Approaches to converter slag cleaning have evolved from recycling slag to the primary furnaces, to milling and flotation or electric furnace slag cleaning as the Cr2O3 content in slags has increased. The shift in the 1990s from Merensky ore derived concentrates to those from UG2 ores impacted the process design for the primary furnaces, with UG2 concentrates having lower matte falls and higher Cr2O3 levels. Conversely, concentrates derived from Platreef and Great Dyke ores, with high matte falls and lower Cr2O3 levels, have introduced other challenges. Furnace designs and operating philosophies have been improved to better handle these ranges of concentrates, the resulting slags and superheated mattes, the containment of which is non-trivial. The smelting of non-roasted concentrates in the primary furnaces gave rise to rapid corrosion of the copper coolers, and triggered development of corrosion mitigation strategies. Advances in SO2 emissions control have transitioned from single contact sulphuric acid plants in the 1970s, to the adoption of double contact acid plants, tailgas, and dual-alkali scrubbing in the early 2000s. Low SO2 strength off-gas streams from primary furnaces are abated in some cases, with technologies such as the Sulphacid process introduced from the early 2000s and the Wet-gas Sulphuric Acid process from the early 2020s. With advances in process intensification, increases in operating temperatures and throughputs, and use of water cooling, consequences of furnace failures have become more severe. Water leaks into the molten material environment, primary furnace containment, and slag granulation have been particularly challenging. Technologies, operating, and maintenance philosophies have been developed for prevention and mitigation of failures, and the adoption of process safety management approaches has yielded systematic benefits. With the outlook in demand for PGMs changing as a function of automotive requirements, smelting technology will continue to evolve for further enhancement of safety and environmental protection, reduced costs, and greater efficiencies.

Aug 3, 2026

By M. Tadie, D. A. Barrett, B. von der Heyden, R. Cromarty

This paper investigated the prereduction of ferruginous manganese tailings from the Nchwaning mine by isothermal reduction between 650 °C and 1050 °C. The treated tailings underwent subsequent magnetic separation to upgrade the Mn/Fe ratio and manganese grade so that the tailings can be used as high-quality ferroalloy feedstock. The tailings contain recoverable manganese but is penalised by elevated and complex iron content. There is a high degree of mineralogical variability found in the untreated tailings. Iron is present both as hematite and in solid solution within manganese minerals such as bixbyite, braunite, and braunite II. A hydrogen atmosphere was used in this paper as it is sufficiently reducing to produce metallic iron that can be separated magnetically. Lime and silica additives were investigated to determine their influence on Fe reduction kinetics and globule formation, which impacts the separability of Fe and Mn. Optical microscopy and SEM analysis of the treated material revealed distinct metallurgical behaviour between iron reduced from hematite – forming larger globules (50 µm to 600 µm) – and iron reduced from Mn-hosted phases, which formed smaller globules (0.1 µm to 2 µm). Relatively milder reducing conditions achieved the highest Mn/Fe ratio of 4.52 and an Mn grade of 57 wt.%. While below the desired target specification (Mn/Fe of at least 7.5 wt.% and Mn grade of at least 44 wt.%), this can still be met by blending the product stream with other low-grade Mn ores that contain minimal Fe. These findings highlight the potential for the upgradation of ferruginous manganese tailings.

Aug 3, 2026

By A. Moss

The Palabora Mining Company has successfully extended the life of its operation by developing a 30 000 tpd block cave underground mine below the now closed open pit. The process of transitioning from surface to underground mining has been technically, operationally and managerially challenging. This has been due to a number of factors, in particular, the development of a block cave in a very competent rock mass. The competence of the rock mass is clearly demonstrated in the open pit that preceded the block cave, one of the steepest deep open pit excavations in the world. With cave breakthrough, however, the pit was ?instantaneously? deepened by 400 m causing a major failure of the north-west wall involving close to 100 Mt of waste material.

Jan 1, 2006

By M. Royker

Gold has been demonstrated as a possible catalyst for oxidation reactions. Some evidence for a possible promotion effect of platinum has also been recorded. The influence of platinum as promoter for Au/?-Al2O3 prepared via anionic ion-exchange for the oxidation of glycerol was investigated in a batch reactor at 60°C. It is inferred that the addition of platinum reduces the catalytic activity and the rate of deactivation, resulting in an overall higher final conversion of glycerol with increasing platinum loading. The addition of platinum to the catalyst favours the formation of the desired product, glyceric acid.

Jan 1, 2012

By W. Mackenzie

The development of a resource project inevitably requires the investigation of a vast range of issues across most engineering disciplines - mining, metallurgical, chemical, civil, electrical, mechanical and environmental - as well as the geosciences. It is also a characteristic feature of the resource industry that no two orebodies - and hence no two development projects - are the same. So these technical issues have to be addressed to a greater or lesser extent in evaluating any resource project's development potential. Not surprisingly then, technical issues tend to predominate when assessing the development potential of a project in the process typically referred to as `doing a feasibility study'. But the principal purpose of a `feasibility study' is to determine whether a development opportunity makes good business sense, not just whether it is technically possible. Resolution of technical issues is often seen as the primary focus of a feasibility study, whereas in reality, these technical issues are the basis upon which an asset delivery and business plan is built. This is not to say that technical issues are unimportant - they are a prerequisite to the demonstration of a project's viability. The feasibility study process must therefore demonstrate that not only have the technical issues been satisfactorily addressed, but also that the broader commercial, economic and social issues have been considered in the development of a comprehensive business plan, which includes an assessment of the risk-reward profile of the proposed development. This paper will present a framework for the conduct of `feasibility studies' and provide guidance to minimum standards and best practice.

Jan 1, 2007

By B. G. Meyburgh

E. H. D. Carman: The results achieved at Buffelsfontein Gold Mining Company Limited are very encouraging and it seems certain that as far as the conventional uranium recovery process is concerned solvent extraction must entirely supplant the old resin ion exchange process. The operational costs given by Mr Meyburgh indicate that the chief cost items in solvent extraction are reagents. In other words 38.4 per cent of the operational cost at Buffelsfontein is due to the replacement of the organics lost from the plant. It is reported from a wide field of experience that loss, particularly of amine, is a direct function both of the quantity and nature of finely divided suspended solids in the pregnant solution and the extent to which the design of the mixers causes the formation of secondary dispersions which do not easily separate in the settler. There is in addition the unavoidable loss of amine due to its solubility in the aqueous solution which is thought to be about 4 p.p.m. In order to minimise solvent losses therefore, efficient clarification at the head of the solvent extraction plant would appear to be a most important requirement. For this reason the newly erected plant at West Driefontein Gold Mining Company Limited has two Funda Pressure Filters each with a filtering area of 540 sq. ft. which are together designed to handle up to 440 g.p.m. of filtrate. This plant has not yet been commissioned but preliminary testing indicates that suspended solids in the sub micron size range which do not settle even on protracted standing of the solution, will rapidly blind the clarifiers. This should not affect solution clarity but frequent backwashing adds to the cost of precoating. The difficulty was countered in the laboratory with continuous additions of filter aid in addition to the precoat but, as Table 11shows, cost of filter aid is high and its use will have to be optimized against organic losses due to less efficient clarification. This will need much careful observation over a relatively long period of time. Costs shown in Table 11 are based on Mr Meyburgh's figures adjusted to probable conditions at West Driefontein Gold Mining Company Limited. The assumption based on small scale testing is that it will cost 5.2c/ton in filter aid to clarify filtrate to a level of about 5 p.p.m. of suspended solids, in order to restrict the amine loss to 10 p.p.m. which is likely to be equivalent to an entrained organic loss worth approximately only 2.6 cents per ton. Of course poor clarification as mentioned earlier is only one of two or even more causes of organic losses and it seems obvious on the above basis that the operation and economics of pressure clarification will need close investigation. A second important consideration at West Driefontein has been the design of the pump-mixers which must perform the dual function of phase mixing and providing the necessary hydraulic gradient for counter current flow of the two phases. The arrangement is shown in Fig. 1.

Jan 10, 1970

By A. Morley

It is difficult to evaluate exploration properties in a manner that is transparent, repeatable and easily re-calculated to cater for different geological interpretations, but the risk-based assessment methodology, the Geological Risk Method, developed and described by Lord et al (2001) attempts to satisfy all these criteria. This paper examines a case study example based on valuations of exploration projects conducted by SRK Consulting using this methodology, and describes some of the advantages and limitations of the method.

Jan 1, 2007