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By Jamie W. Pardy

The objective of the Canadian International Development Agency program is to facilitate the efforts of the people of developing countries to achieve self-sustainable economic and social development in accordance with their needs and environment. The British Columbia Ministry of Energy and Mines (BCMEM) is the executing agency for the four-year Peru Minerals and Metals Public Sector Assistance Project which began in December 1998. The primary beneficiary is the Ministerio de Energía y Minas del Peru (PMEM). The project is designed to address mine health & safety, environmental management and mineral resource information. Project activities currently underway include joint development of: an inspection system, a mine rescue system, an enhanced and e-Commerce capable mineral information website, environmental guidelines for industry and standardized ministry evaluation criteria for environmental impact assessments and closure plans. In addition, reports on management options for mineral concentrate transportation, storage and handling, and on mine reclamation security policy have been delivered at workshops.

May 1, 2001

By T. Nagasaka, T. Miki

Suppression of CO2 and waste such as slags discharged from iron- and steelmaking processes are some of the typical major issues for the protection of global environment and sustainable growth of steelmaking industry. Utilization of active phytoplankton growth will be one of the best options to stabilize and suppress carbon dioxide at high-efficiency. Inorganic minerals such as C, 0, N, Si, P and Fe are necessary for phytoplankton multiplication. It is crucial for supply of nutrition into seawater effectively for phytoplankton multiplication to understand the dissolution behavior of some elements from steelmaking slags into seawater. The morphology of the precipitated phases in steelmaking slags during cooling period was investigated in the present work. The dissolution behavior of some elements from steelmaking slags into artificial seawater has also been studied. The effect of nutrient dissolved into seawater on phytoplankton multiplication, some examples of marine structure made from steelmaking slag, and estimation of CO2 fixation amount by marine phytoplankton are also discussed.

Jan 1, 2004

By Masatake Haruta

Gold can be deposited as nanoparticles on a variety of support materials by coprecipitation or deposition-precipitation of Au(OH)3, grafting of organo-gold complexes such as dimethyl-Au(III)-acetylacetonate, mixing of colloidal Au particles, and vacuum deposition. Owing to the moderate adsorption of at least one of reactants (for example, CO) on the edges and corners of Au nanoparticles and to the activation of the counter reactant (for example, O2) at the perimeter interface with the supports, supported Au nanoparticle catalysts exhibit unique and practically useful catalytic properties at relatively low temperature below 473K. They have already been commercially used for deodorizers in rest rooms in Japan and will find growing applications in indoor air quality control, pollutant emission control, production of hydrogen energy carrier, and innovations in chemical processes. Cluster science of Au may also open an exciting area of research showing some magic numbers for dramatic changes in reactivity.

Oct 1, 2003

By J. W. Matousek

Tonnage oxygen plays a critical role in the primary production of two of the most important industrial metals - copper and iron - and minute quantities of oxygen play equally critical roles in determining the properties of the market products. For refined copper, oxygen in the final metal is balanced between maximizing electrical conductivity, neutralizing the effects of harmful impurities, and ensuring that the metal takes on the desired "set" during casting - the surface texture and physical properties required for subsequent rolling and drawing. For refined iron, oxygen must be removed to minimize reaction with carbon during cooling from the molten state with the generation of CO and CO2 - leading to a loss of carbon and the creation of "blow-holes" in the solid ingots and the potential for defects in rolled and forged products. This paper reviews the thermodynamics of oxygen in molten copper and iron at the levels of primary interest to production metallurgists.

Jan 1, 2014

By Brian Putland, Fred Kock, Leigh Siddall

Single stage semi-autogenous / autogenous (S/AG) milling has become a common design for a variety of ore types with the advantages of being comparatively low capital cost and flexible for future expansion. The single stage SAG/AG milling option is ideal for starter projects with significant exploration and expansion potential. Currently a number of the largest SAG mills designed are installed in single stage configuration. This paper discusses the challenges associated with the process design of single stage SAG/AG milling circuits, the design flexibility required to ensure a robust circuit and the operating techniques adopted at successful installations.

Jan 1, 2012

By J. Day, Matthew X. Yao, Lijue Xue

Hardfacing overlays are commonly applied on the shroud Z-section of turbine blades for enhanced wear resistance. Among various processes that are used to apply the hardfacing overlays, the plasma transferred arc (PTA) welding process offers several advantages including lower heat input, less base material dilution, rapid process time, and reduced operating cost associated with the capability to apply materials in the powder form. The development of a robust PTA process is crucial for overlay performance and repeatability, particularly in the aerospace industry where a quality intensive manufacturing environment prevails. For this reason, the Taguchi method of experimental design was selected to develop a test plan. A 4-factor 3-level (L9) orthogonal array (OA) was used in the experiment. The L9 OA allows for a more detailed (3 level) investigation of critical process parameters, namely plasma gas flow rate, traverse speed, powder feed rate, and arc current. Two hardfacing materials, Stellite 694 and Tribaloy T-800, both Co-based wear resistant alloys, were investigated by deposition onto a cast IN738 Ni-based superalloy substrate. Performance measurements of the hardfacing deposits included deposit hardness, substrate hardness, deposit density (porosity), degree of cracking/inclusions, and a quantified visual inspection. The procedure resulted in optimized PTA hardfacing parameters for both Stellite 694 and Tribaloy T-800 on IN738 turbine blade material.

Jan 1, 2004

By Dennis L. Murr, James E. Wennen

"The through-put and energy efficiency of an autogenous (AG) grinding mill are adversely affected by variability in rock size and rock competency. This applies to both fully autogenous and semi-autogenous (SAG) grinding circuits. In this paper we focus on an approach to overcome the problem of inconsistent mill through-put related to variability in mill feed size and rock competency. The focus is on ores containing hard, competent rock. This approach consists of preparing feed to an autogenous mill that contains 20% coarse media rock and 80% of material crushed to pass 37 mm. Results of pilot-scale testing for two iron-ores will be presented to show that a 10% to 12% reduction in unit energy consumption is possible with prepared feed, compared with feeding the mill with conventional primary crusher discharge.INTRODUCTIONIn the past 30 years or so, autogenous grinding and semi-autogenous grinding have been the comminution technologies of choice for most mining and mineral processing operations. These technologies saved both capital and operating expenses associated with the installation and operation of multi-stage crushing and screening plants required for conventional rod mill – ball mill circuits. However, SAG and AG are inherently inefficient in terms of energy consumption, especially for very hard ores. In cases of hard ore, changing characteristics of rock fed to the mills causes wide fluctuations in mill capacity, which contributes to the inefficiency. Rising electric power costs make this the most expensive unit operation used in the extraction of valuable minerals from an ore. The objective of the concept discussed here is to reduce the energy consumption in AG grinding for hard ore and eliminate the use of large-diameter steel grinding balls that are required for SAG grinding"

Jan 1, 2012

By T. McCallum, B. Wellbrook, T. Ratnaweera

Leaching of copper (Cu) concentrates produces elevated concentrations of Cu and acid, which makes solvent extraction (SX) processing more challenging. Maintaining extraction targets can be more difficult with higher pregnant leach solution (PLS) grades, and variability of PLS Cu and acid can lead to increased chemical iron transfer. Diluting concentrate leach feeds with an existing heap leach inventory makes SX processing easier. However, considerations about how much to dilute and where to distribute the flow into the SX configuration must be carefully evaluated, given their impact on metallurgical performance. In this paper, characteristics of a concentrate leach feed are discussed, along with considerations for processing by SX. Also reviewed are pilot plant results of concentrate leach distribution into SX and plans for commercial testing. INTRODUCTION Hydrometallurgical processing of copper concentrates continues to gain interest from the industry. Treatment by smelting and electrorefining continues to dominate, accounting for ~80% of global copper production, but is faced with its own challenges (Li et al, 2017). The case for increased hydrometallurgical processing has been discussed as high grade ore deposits are diminishing, capital costs for smelting are high, and the environmental aspects present challenges for sustainable practice. The hydromet copper industry is also turning a corner as easily leachable copper oxide deposits are depleting, and excess SX-EW capacity exists in certain regions. The transition to hydrometallurgical processing of copper concentrates will take a bit of effort as leaching of copper sulfides is difficult and byproduct credits must be considered. Various POX leaching processes have been studied and proposed to the industry as viable practices. Of the many processes, commercial use has been practiced with the Mount Gordon Copper Process, total and partial pressure oxidation by Freeport-McMoRan at their Bagdad and Morenci, Arizona complexes, the Sepon Copper Process in Laos, and the bioleach BIOCOP™ process in Chile (Dreisinger, 2016).

Jan 1, 2019

By Jessica Hurst, Mark Holdsworth, Jeff McKay

"In 2002, Kennecott Utah Copper Copperton Concentrator installed an Expert Control system for optimization of their SAG and Ball milling circuits. The advanced process control has been well received and is utilized well over 95% of the time. In the years since, many lessons have been learned and many advances have been made. Improvements have produced millions of dollars of benefits and have included directly controlling feedrate with complex logic as opposed to using a bearing pressure controller, modifications to how sound is used for control, modifying logic for maximizing asset utilization and using advanced control for automating equipment restart. INTRODUCTIONRio Tinto’s Kennecott Copperton Concentrator produces copper, molybdenum, gold and silver. The mill has 4 SAG mills (SAG 1-3, 34 foot diameter and SAG 4 36 foot diameter), 8 ball mills and copper and molybdenum flotation plants, as seen in Figure 1. The 2010 average data is shown in Table 1.In 2002, a Metso Cisa OCS Expert Control system was installed at Copperton for SAG and Ball mill advanced control. The expert control was first placed on SAG 2; data from the first few weeks compared with operator performance indicated approximately an 11 percent increase in throughput. After full commissioning, the system was gradually refined further by plant personnel to develop key performance indices based on SAG feed size, refinement of the sound setpoint for control of mill speed and throughput, specific rules to help the adjustment of speed based on loss of a feeder, etc. With the addition of the pebble crushing circuit, the expert control began utilizing a model estimation of crushed pebble bin level to help stabilize the impact of returned crushed and uncrushed pebbles on the SAG mills. As the ore and limitations change, it is necessary to evolve the SAG logic to better handle any constraints."

Jan 1, 2012

By K. Ski

Three series of membranes were prepared by blending polyvinylidene difluoride (PVDF) or poly(vinylidene difluoride-co-hexafluoropropylene) [P(VDF/HFP)] with sulfonated poly(ether ether ketone) (S-PEEK), sulfonated polysulfone (SPU), or sulfonated polystyrene, in order to develop novel PEM membranes suitable for melt processing. By means of incorporating fluorine-containing block copolymer into the blended system, acceptable proton conductivity and low water containing PEM materials were prepared. The effect of sulfonated poly([vinylidene difluoride-co¬hexafluoropropylene]-b-styrene) block copolymers as compatiblizers was investigated: conductivity was enhanced for S-PEEK/fluoropolymer blends. Microstructures for the blends were examined by transmission electron microscope (TEM) and scanning electron microscope (SEM).

Jan 1, 2005

By E. C. De Matos

The Uranium Province of Lagoa Real is located in the mid-south region of Bahia State, Brazil. Uranium is the only mineral wealth, occurring mainly in the form of uraninite. The region has been searched for uranium since 1971 and 35 anomalies were detected, distributed over 1200 km2. Seven are now taken as deposits, accounting for reasonably assured resources of 100.000 tons of U3O8. This paper describes the geological aspects of the area, the exploration and mining activities done so far by the state company INB and the perspectives for the near future, when a raise in the country?s uranium demand is expected.

Aug 1, 2010

By C. G. Anderson

With demand and prices for copper and gold at near record high levels, coupled with a lack of readily treated orebodies, the emergence of environmentally sound hydrometallurgical treatment of enargite concentrates has become a priority. This paper will outline the application the industrially proven technologies of low pressure and temperature NSC (Nitrogen Species Catalyzed) pressure leaching and ASL (Alkaline Sulfide Leaching) for the recovery of copper and gold from enargite. Copper can be recovered as cathode metal or as a clean concentrate suitable for smelting. Gold is recovered by smelting, conventional cyanidation or alkaline sulfide hydrometallurgy. Coupled with this is the effective precipitation and stabilization of arsenic as scorodite and ferrihydrite.

Jan 1, 2007

By Michael J. Beare

Requirements of both local permitting and international fundraising are forcing increasing numbers of projects in Russia and CIS to carry out dual technical studies. The principal focus of Russian mining project design is to satisfy local regulatory requirements. However, the technical documents are not generally accepted by international banks for project finance outside Russia. Similarly, international study documents are not accepted for permitting in Russia. The purpose of this paper is to compare and contrast Russian and international approaches to mine technical studies and draw conclusions from this. The Russian design and permitting system is centered around two key statutory technical documents termed the TEO Konditsy and the TEO Project. These documents are subject to regulatory approval and are broadly equivalent to the international prefeasibility study and the feasibility study respectively. A comparison of study criteria suggests similar approaches are used for the main technical disciplines in project design by the time projects are at the point of construction, but there is divergence on environmental matters where the OVOS (Russian ESIA equivalent) differs from an ESIA in some significant areas. The key differences relate to project footprint, level of technical detailed required for baseline studies, level of public consultation, consideration and disclosure of information, labour, coverage of community and social issues and the preparation of a Social and Environmental Management System (SEMS). It has been noted that the Russian Design Institutes often leave the detailed economic analysis until after the TEO Konditsy. A common problem is design teams tend to look for ?technological solutions? without due concern for project economics. The end result of this can be mines that are overcapitalized and hence sub-optimal. It can be concluded that Design Institutes have the monopoly on Russian permitting reports and this is likely to continue. Similarly, Russian institutes generally do not prepare feasibility studies to international standards and this is likely to continue to be the case. Therefore to achieve the requirement of dual technical studies, the international consultants and Russian Design Institutes will need to cooperate on a joint work program. Key issues will be to ensure the most appropriate option studies are carried out at the right stages, that project economics are considered throughout the study, and that the environmental work program covers the additional studies necessary for the ESIA.

May 1, 2009

By A. P. E. Dirige

In order to maximize the recovery of ore in variably dipping ore zones of moderate width, cemented backfill is normally placed to serve as structural support. With the intention of saving on costs, backfill of low cement content can be used, which are often supported by a sillmat of higher strength. The stability of the low cement backfill face, exposed during adjacent mining, must be carefully studied to provide very effective, safe and economic mining operations. Improper design of these stope support structures may result in fill mass failure resulting in relaxation and failure of the stope walls, with consequent losses of production, ore dilution, and in safety problems. This paper presents a study conducted to assess fill performance during adjacent pillar mining and to provide a comprehensive understanding of backfill behaviour, the failure modes that may occur and the consequences to production, ore dilution and to safety problems, and accurately predict their stability. The design study investigated the effects of stope width and height, orebody geometry and inclination, and wall roughness on the stability of cemented backfill during adjacent pillar mining. Fill properties used were based on paste fill specimens cured for 28 days. Paste fill performances were assessed based on analytical and numerical modeling studies for the different mining conditions. Analytical modeling was carried out using limiting equilibrium analysis and numerical modeling was carried out using FLAC3D. The modeling results suggested that, for stopes that are inclined with smooth wall rock conditions, backfill failure, driven by the fill self-weight, has minimum dependency on the binder content and is reduced by resisting forces developed on the footwall-fill contact. For inclined stopes with rough wall rock conditions, wall roughness contributes significantly to the stability of the backfill during adjacent pillar mining. The analytical modeling approach was demonstrated to be useful in providing some approximate parameters for predicting the behaviour of paste fill exposed faces during adjacent mining, but cannot predict the mode or mechanisms of failure. Numerical modeling not only assess the stability behaviour of paste fill free faces, but also is able to provide a better idea of paste fill failure modes and possible failure mechanisms. The depth of failure and the potential for instability for a simulated stope filled with paste fill can be predicted, and may be useful in estimating the mass of material that could possibly fail and ore dilution levels.

May 1, 2009

By R. W. Brock

This subject is too broad and comprehensive to be dealt with adequately and authoritatively in this paper. It calls for the knowledge and experience of many men, but the results from such collaborative effort would be of great value, particularly if similar reports of the principal mining districts of the world were made on a standardized basis so that conditions everywhere might be directly and accurately compared. In considering conditions affecting mining in British Columbia, unfavourable as well as favourable factors must be taken into account. The unfavourable are apt to loom large and to be exaggerated rather than minimized; for it is human nature to see the blackness of the cloud rather than the silver lining; to think that one's own undertaking is beset with peculiar difficulties, and to attribute lack of greater success to out-side causes rather than to personal shortcomings. It should be recognized, however, that there is no country where the conditions for mining are ideal. The ideal mining country is the product of imagination, invested with every favourable condition found anywhere, but with none of the unfavourable conditions that are always present in reality. So if British Columbia has some handicaps to the industry, it is in good company. What is important is that the advantages compensate for the disadvantages, that the balance will compare favorably with that of competing states, for mining, like every other industry is competitive, and the cost of one's product must have a definite relationship to its price in the world's market.

Jan 1, 1924

By Don Peel, Jeremy Richards

Abstract - Aggregates (sand, gravel, and crushed stone) are low unit-cost products extracted in very large volumes for the construction of buildings, roads, and other infrastructure essential to modern society. Because of their low unit value, transportation costs are a key factor in resource economics, and deposits are commonly developed close to market (i.e., close to towns and cities, or along low-cost transportation corridors). This proximity results in potential conflict with residents over land use, disturbance, and pollution. Management of aggregate resources in Alberta is examined in the light of resource geology and distribution, and governance. A case history of development of the Calahoo-Villeneuve deposit is described, and the conflicts between residents and developers that led to establishment of an Area Structure Plan (ASP) are explored. The plan sets limits to, but at the same time safeguards, resource extraction, and defines terms for compensation to residents through a voluntary levy on production (Community Enhancement Fund). This fund is used to support community activities and to pay for a groundwater monitoring program. The ASP is examined within the context of the "Seven Questions to Sustainability" as set out by Mining,Minerals and Sustainable Development-North America (2002). It is concluded that the ASP, for the most part, provides a good model for conflict resolution and sustainable resource development, which could usefully be applied in other jurisdictions. The ASP was developed at a municipal level, and adoption at a provincial level would aid sustainable development of aggregate resources across the province.

Jan 1, 2003

By Leibniz University, D. Zapf

"The demand for gas storage operations with high withdrawal rates and operation modes different to a seasonal storage regime requires a more detailed rock mechanical consideration of thermal induced stresses in the vicinity of the caverns. This means that the change of gas temperatures during operation and the consequences of these temperature changes on the stressing of the salt rock mass must be taken into account in the rock mechanical dimensioning. Within the rock mechanical calculations a loading history, i.e. a pressure versus time dependency, has to be defined. As rock salt has a time dependent material behavior stress redistributions in the rock salt mass take place even under constant internal pressure conditions. Therefore not only withdrawal and filling periods but also the duration of phases with nearly constant internal pressure is significant for the resulting state variables. Within the paper the differences and consequences for the rock mechanical recommendations are discussed. As a result it can be concluded that recommendations with respect to minimum operation pressure as well as for maximum withdrawal rates can be answered only in connection with the respective time intervals."

Jan 1, 2015

By N. Hiroyoshi

In the leaching of chalcopyrite with sulfuric acid solutions, the copper extraction rate reaches a maximum at a given redox potential. This article reviews our studies on the determination of the optimum redox potential for chalcopyrite leaching. Shaking flask and column leaching experiments for a chalcopyrite concentrate were performed under various conditions, and the results were analyzed using a normalized redox potential defined from a reaction model assuming the formation of an intermediate CU2S from chalcopyrite. Factors, such as metal ion concentrations, solid/liquid ratio, and presence of iron-oxidizing bacteria, caused significant variations in the copper extraction versus time plots. However the copper extraction rate versus normalized redox potential plots were independent of the above factors and the copper extraction rate reached a maximum at the normalized redox potentials around 0.43. Converting the normalized redox potential to the solution redox potential gives the optimum redox potential for chalcopyrite leaching as a function of cupric and ferrous ion concentrations. This semi-empirical equation can be used to predict the optimum redox potential during leaching operation, and is useful to design the redox-controlled heap leaching for chalcopyrite.

Jan 1, 2007

By T. Yalcin

"This paper describes a process that can provide high rates of dewatering and that has the potential of bringing significant savings in tailing disposal costs. It involves a three-stage, closed-circuit operation employing a hydrocyclone, a settling cone and a thickener. The mill tailing, with adjusted pulp density, is first fed to the hydrocyclone. The underflow from the hydrocyclone goes to the settling cone for further dewatering. The overflows from the hydrocyclone and the settling cone are sent to a thickener which, with the addition of a flocculant, gives a clear liquid effluent and a dilute underflow which is recycled back to the hydrocyclone. The underflow of the settling cone is a material with as high as 78% pulp density and is suitable for direct disposal or for use as mine backfill.INTRODUCTIONDewatering is an essential process for the disposal of mill tailings and forms an additional cost item in milling operations. Cost-cutting measures are therefore desirable in this area as in any other stage of milling. One way of achieving this is through increased rate of dewatering which would require smaller dewatering units with correspondingly lower capital and operating costs."

Jan 1, 1987

By Frands Jensen, Erik Eriksson

"Haldor Topsoe’s Wet gas Sulfuric Acid (WSA) technology has been proven in a number of industries converting sulfurous gasses to concentrated sulfuric acid. In the metallurgical sector plants have been delivered handling SO2 gasses from copper, zinc, molybdenum, and lead ore. WSA has high energy efficiency and allows autothermal operation from feed gas strengths as low as 3.0% (volume). Recent variants of the WSA process have been developed that allow very high SO2 conversion efficiencies of over 99.9%. This paper describes the technology, its advantages and industrial achievements.The WSA technology is well suited for production of concentrated sulfuric acid of commercial quality from the sulfur dioxide (SO2) gas that inevitably emerges from the metallurgical processes. Some of the features that make the WSA technology attractive for this application are:- High SO2 conversion rates (up to 99.99%)- High energy efficiency leading to a low autothermal point (~ 3% SO2)- No need for gas cooling and drying to produce concentrated sulfuric acid- No production of waste- Very low cooling water consumptionThis paper describes the WSA process principles and highlights features that make this process attractive for handling SO2 gases."

Jan 1, 2014