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By Z. D. Hora

Several deposits of crystalline magnesite are known in southeast British Columbia. Deposits at Cross River and Marysville have been thoroughly explored, but as yet there has been no commercial production.

Jan 1, 1984

By Z. D. Hora

Sedimentary phosphate-bearing rocks are found over a considerable area of so utheastern British Columbia that extends from Fernie east to the Alberta-British Columbia boundary and from the International Boundary northward to the headwatei: s of the Elk River. Phosphatic beds occur at the following four stratigraphic levels: 1. lower part of the Banff-Exshaw sequence of Mississippian age; 2. lshbel Formation of Permian age; 3. base of the Fernie Group of Jurassic age; 4. belemnite bed within the Rock Creek Member of the lower part of the Fernie Group. To date, considerable tonnages of phosphate rock have been proven in the area. However, no commercial production has been initiated because of a relatively low P2O5 grade. Data on assays and thicknesses of the phosphatic beds are in part recalculated from the paper by Telfer (I 933) and in part from assessment reports filed at the British Columbia Ministry of Energy, Mines and Petroleum Resources.

Jan 1, 1984

By Roy Sage

Overview ? History ? background to current programs ? Kyoto status ? Support for technology development ? Support for GHG reduction ? Sources of information History ? 1988 - Toronto Conference - The Changing Atmosphere ? Proposed target ? CO2 levels reduced to 20% of 1988 levels by the year 2005 ? 1992 - Canada signed Framework Convention on Climate Change at the UN Conference on Environment and Development in Rio de Janeiro in June 1992 ? Canada launched the National Action Plan on Climate Change ? Kyoto protocol adopted in principle in 1997

Nov 1, 2002

By G. L. Spence

Prevention of cuprous and cupric oxide formation on stored ETP copper rod is a major concern for copper rod and wire producers. During normal storage periods copper oxide layers can increase from less then 100 A to more then 1000 A exceeding ASTM specifications and discoloring the rod surface. Various types of corrosion inhibitors are tested and compared in effectiveness for prevention of copper oxide formation on stored copper rod. Aromatic triazole compounds are also compared to a non-azole containing compound.

Jan 1, 2007

By H. Ito, T. Takasu

A leaching process for recycling small car motor scraps dismantled from End- of - Life -Vehicles (ELV) was investigated using waste pickling acid in steel work. Steel parts of mortar scraps were leached by waste pickling acid and Cu wire was recovered as pure Cu in the process. Pickling acid solution after leaching could be recycled in an ordinary process for waste pickling acid solution. High grade FeSO4 agent could be produced using H2SO4 as a pickling solution.

Jan 1, 2004

By H. R. Kempthorne

"The Property of Bevcon Mines Limited, including a recently acquired adjoining south group, occupies an area of 2,625 acres in northeast Louvicourt township, Abitibi county, Quebec. It is situated 17 miles east of Val d'Or at the junction of provincial highways 58 and 59.Gold was first discovered in the area in 1931 by the late S. B. Jowsey on the present property of Buffaddison Gold Mines adjoining to the west. However, it was not until the winter of 1944-45 that diamond drilling encountered encouraging results on the Bevcon claims. During the period 1946-1948 a shaft was sunk to 1,000 feet and considerable development undertaken from the 500-foot to the 1,000-foot levels. Between 1947 and 1950 approximately 24,000 tons of dump ore and 48,000 tons of ore by stoping were milled at Perron Gold Mines. The favourable results of these tests prompted the decision to construct a milling plant at Bevcon. The mill began operating in July 1952, and presently has a capacity of 800 tons per day. In 1953 the shaft was deepened to 1,600 feet and is currently (1955) being driven to 2,225 feet.Total production of gold to the end of 1954 has been 101,024 ounces from the milling of 697,427 tons of ore of an average grade of 0·163 ounces per ton.GeologyThe Bevcon orebodies occur in a granodiorite stock which has an east-west length of approximately 4 miles and a maximum width of 1 1/2 miles. The property covers the central portion of the stock and its contacts with the Keewatin volcanics. Approximately one-third of the northern contact and one-half of the southern contact are contained within the Bevcon claims. The granodiorite has been cut by acid (feldspar porphyry) and basic dykes trending east-west. A younger diabase dyke, 300 feet wide, strikes northeasterly across the property 1,000 feet east of the shaft.The main ore zone, striking east-west, lies between the more northerly porphyry dyke and the north granodiorite-greenstone contact. It has been extensively sheared, fractured, altered, and mineralized by gold-bearing solutions. It is approximately 2,000 feet Jong from the west boundary towards the diabase dyke. The shaft is centrally located and passes through the south contact of the ore zone at the 500-foot level. The zone increases in width and trends northerly with depth, due to the porphyry and greenstone contacts having average dips of 80 degrees and 70 degrees respectively to the north. Thus on the uppermost or 500-foot level the width is 150 to 200 feet, and at the present bottom level at 1,600 feet the width is 400 to 500 feet.Another gold-bearing zone has been indicated 200 to 400 feet south of the main ore zone by limited surface drilling."

Jan 1, 1949

By M. Eikerling

The full competition between mass transport and reaction in PEMFC unfolds in cathode catalyst layers (CCLs). Recently developed models provide vital insights into effects of thickness and composition on effectiveness of catalyst utilization and performance. However, the CCL's key function in liquid water removal is rather unexplored. Studies of water balance in PEMFCs focus mostly on other cell components. Notwithstanding this prioritization, a simple calculation shows that the CCL is the PEMFC's favourite medium for conversion of liquid water into vapor. Porous structure and wetting properties steer the interplay of evaporation, transport and reaction. A model will be presented, that links pore space morphology, composition, distributed properties (concentrations, pressures, reaction rates, potential) with global performance (critical phenomena). It reveals how problems of flooding in the fuel cell could be mitigated by properly adjusting catalyst layer structure and operation conditions and under which conditions all liquid water arriving in the CCL would leave it as water vapour through the CCL/GDL interface. Results for a simple variant of the model emphasize the role of the CCL as a watershed for the whole cell.

Jan 1, 2005

By C. Phan

This paper outlines opportunities provided for enhanced management and process control by ISA PROCESSTM technology. ISA PROCESSTM technology has the core advantage of offering the potential for vastly improved electrode handling systems. This fundamental characteristic has enabled ISA PROCESSTM technology to develop management and process control systems that are modular, minimalist in their complexity and tailored to a tankhouse operating environment. A review will be presented on the current status of management and process control in ISA PROCESSTM tankhouses covering the central issue of electrode handling as well as electrolyte circulation systems, voltage monitoring, cathode plate tracking, and product tracking. Particular reference will be made of the recent development by Xstrata Technology (XT) and their technology partners, VRT Systems, of an Radio Frequency Identification (RFID) based solution for tracking ISA PROCESSTM cathode plates. The system encompasses fixed readers which identify plates passing through the stripping machines and the use of sophisticated tracking and database software enabling the development of cathode asset management and operational strategies. The performance of individual plates and batches of plates can be tracked through a full service history.

Jan 1, 2007

By Paul Stothart

Context ? Industry is active in urban, rural, and remote regions ? Faces a range of environmental challenges and ?social license? issues ? There are also Aboriginal and northern issues ? Also very active internationally, with associated challenges ? Environmental/social groups often target the industry ? The important contribution of the industry should not be overlooked Useful Minerals and Metals Minerals are intrinsic to the residential, municipal, communications, and transportation infrastructure of modern life. Examples: Hybrid motors - nickel hydride batteries Water purification systems ? nickel, rare earth elements Catalytic converters - cerium Screens and monitors - several rare earth elements Clean electricity - uranium Circuitry - gold, copper, aluminium, lithium, titanium, silver, cobalt, zinc Instruments - copper, silver, nickel, cobalt, copper, brass Protective products ? zinc, calcium carbonate, sulphur

May 1, 2008

By A. Hasselbring

Sub-Level stoping was used in this country at least as early as 1912, at the Magpie mine in Michipicoten. The fundamental principles of the system are the same wherever it is used, but modifications have been adopted in the Michigan iron mines and in several Canadian mines. It is a system whereby a suitable body of ore may be developed quickly and worked cheaply, with a low initial expense, and by miners of quite ordinary ability. The basic method, described in the following pages, may be modified to meet conditions where one or more factors are not in accord with normal sub-level stoping requirements. In suitable ground, sub-level stoping is probably the most satisfactory method yet devised for underground hard-rock mining. It is so simple, straightforward, and safe that no special training of a crew is necessary. Any miner capable of drifting and raising can carry on the work necessary for sub-level stoping after the shaft has been sunk. The method is suitable, however, only for reasonably wide ore-bodies, the minimum width of ore to which it can be economically applied being somewhere in the neighbour-hood of thirty feet. The development programme is simple. Assuming, for purposes of illuslustration, an ideal ore-body, two thousand feet long, dipping nearly vertical, and varying in width from forty to a hundred feet, this programme would be as follows. The shaft should be sunk on the footwall side about sixty feet outside of the ore-body and near its centre. Levels are then established at suitable intervals, usually 125 feet. On each level, a cross-cut is run to the ore-body, and there a main-haulage drift is driven in either direction to the end of the ore. Cross-cuts are then run at 25-foot intervals, so that ore-chutes can be spaced about 25 feet centre to centre each way. It is not necessary that these cross-cuts be extended to the walls of the ore-body, if the position of the walls is known; they are extended just far enough to make room for the correct location of the chutes.

Jan 1, 1934

By J. Holder

"A key barrier to vertical mineshaft construction is the construction access required for workers. A suspended work stage is used to provide this access for the mechanical, electrical and structural applications and other tasks. Work stage design is complicated considering the numerous types of construction activities that are executed simultaneously, the confined environment in which the work stage operates, the significant corrosion attack that is present, the weight limitations imposed by the mechanical hoist systems, and the risks associated with worker safety. Also complicating the design, these structures and their construction environment can vary with time. Hence, they can be described as 4D structures. The author has discovered significant synergies and advantages with integrating engineering design with detailed three-dimensional (3D) fabrication design. The significant reduction of minor design errors needing field correction will be underscored. The tender process is also accelerated since the design output is fabrication shop drawings including a detailed quantity takeoff output which lists each component required and its specific quantity. The paper presented will document the numerous advantages to the project using this approach. INTRODUCTION A key barrier to vertical mineshaft construction lies in the access for the workers to execute the construction. Suspended work stages are used to provide this access for the mechanical, electrical and structural applications as well as other tasks. The design of such work stages is complicated considering the numerous types of construction functions that need to be executed simultaneously, the confined environment in which it operates , the significant corrosion attack that is present, the weight limitation imposed by the mechanical systems for suspension, and the risks associated with worker safety. Also complicating the design, these structures and their construction environments can vary with time. They can be described as 4D structures with the fourth dimension being time. This design is a time consuming process. The post tender award is meticulous and requires strong teamwork between the steel fabricator and the consulting engineer. This teamwork may or may not be present and is dependant on the experience and relationship the team members have working together as well as other factors."

Jan 1, 2019

By T. Gonzales, S. Thakurdin

The conducting of risk reviews is an essential activity in ensuring safe operating conditions, both during project design phases and for existing facilities. The following paper presents a structured approach to the conducting of risk reviews for existing operations, including descriptions of supporting documentation and guidelines for on-site review activities. The conducting of regular site risk reviews and safety audits is crucial in ensuring the continued safe operation of existing facilities, particularly in the copper industry where numerous processes and unit operations can present catastrophic risks, both in terms of loss of life and financial liability. The structured approach presented aims to provide a logical and comprehensive analysis of risks to align safety-related facilities and procedures with current industry best practice and ensure consistency across multiple client operations. INTRODUCTION The production of copper, whether by pyrometallurgical or hydrometallurgical process routes, carries significant inherent safety risks. Production volumes are relatively large, often requiring complex processing routes, multiple production trains and a variety of supporting ancillary facilities. Furthermore, considering the relatively large size of ore reserves, copper production plants can have operational lives well beyond the typical design duration of 20 years. In this context, the conducting of regular risk reviews is essential in ensuring safe operating conditions and aligning facilities with current industry best practices. Risk reviews and safety audits can take various forms and have various areas of focus. The methodologies and approaches described below relate specifically to catastrophic risks, defined broadly as risks that carry the potential for multiple fatalities and significant financial losses. Focus is given to existing facilities and does not consider the risk-related activities such as hazard and operability (HAZOP) studies conducted during plant design. The structured approach presented aims to provide a guide for effective site- based audits and a logical analysis of risks identified. RISK CLASSIFICATION Table 1 provides a typical summary of the classification of risk types and the associated consequence categories and descriptions. It illustrates the descriptions of a catastrophic risk in terms of the broad categories of Health & Safety, Environment, Financial, Image & Reputation and Legal & Compliance. In terms of the Financial category, numeric costs ranges are often prescribed depending on the financial characteristics of the specific operation and the associated parent company.

Jan 1, 2019

By J. N. De La Vergne, J. S. Redpath

"The authors make recommendations that they believe will improve the efficiency of a mining company's use of a mining contractor's services. The recommendations are in the form of specific ""DO"" or ""DO NOT"" instructions, giving explanations and covering the contracting process from the end of the feasibility study to the end of the job. IntroductionThis paper is an attempt by the authors to set out some of the things which they feel an owner should consider to achieve maximum effectiveness from mining contractors. It is based on our experience as contractors as well as our experience as consultants to owners. Should this paper create the impression that we feel all the responsibility lies with the owner, this is neither our intention nor our belief.Before the Tendering Process BeginsUse Defined EstimatesIn Feasibility Study DO NOT estimate your cost or schedule by telephoning contractors and asking them for ballpark figures. The only kind of estimate that is worth anything is the one that is clearly defined on paper and bears the signature of the author. This type of time or cost estimate takes time to prepare. In general, the estimate will be worth what you pay for it.Ensure Adequate FinancingDO NOT ask contractors to tender on a project unless the funds have been approved for it. Remember that, depending on the size of the job, it will cost the contractor from $5,000 to $50,000 to prepare his tender. When financing is not assured, a single contractor should be approached regarding a detailed estimate and he should be paid for it. Contractors should not be expected to finance speculative mining ventures."

Jan 1, 1980

By C. Sorel

The PAREX code has been developed since the nineties by CEA and AREVA to describe the PUREX process implemented in the French fuel reprocessing plants. It enables the calculation, either in steady or transitory states, of the behaviour of the different elements of interest at each process step. The high customized structure of the software allowed the implementation of various phenomenological models describing solvent extraction systems dedicated to uranium purification from crude ore to spent fuel. After qualification of the implemented models, the code was used to perform the design of flowsheets, for safety demonstration analysis or for operational assistance.

Aug 1, 2010

By A. Innus, R. Pelletier, C. Allaire

Refractory used for molten aluminium confinement is typically assessed separately for thermo-physical properties and molten aluminium resistance. This present work provides a case study comparison of four commercial refractory products that were subjected to a test procedure that combines mechanical impact, thermal shock with molten aluminium contact. The main conclusion of this work is that physical and mechanical property values by themselves do not, and cannot, predict the response of refractory to potential interactions between molten aluminium contact and thermal shock and mechanical impact. Adequate physical simulation is imperative to quantify the effect of such interactions.

Jan 1, 2004

By H. Kuboyama

The synergistic effects of polymer additives such as gelatin and polyethylene glycol) (PEG) and Cl- on Cu electrodeposition have been investigated by measuring the polarization curves for Cu deposition, by rotating ring-disk electrode technique and by AC impedance measurements. The cathode potential for Cu deposition was greatly polarized in solutions containing both Cl- and gelatin or PEG, showing evident synergistic effect of polymer additives and Cl- on Cu deposition. The cathode potential was shifted to the less noble direction with increasing the concentration of Cl- in solutions containing polymer additives and showed the maximum polarization at Cl- concentration range between 0.1 and 1 mmol/L. The rotating ring-disk electrode technique revealed that Cu deposition in solutions containing small amounts of Cl- proceeded with initial formation of adsorbed intermediate CuClad. The Cole-Cole plots obtained by AC impedance techniques suggest that the reduction of CuClad is suppressed by polymer additives. The morphology of Cu deposited from solutions containing both PEG and Cl- showed the compacted surface composed of smaller grains due to an increase in the overpotential for Cu deposition.

Jan 1, 2007

By Masakazu Daté

Moisture effect has been studied for the CO oxidation over Au/TiO2, Au/Al2O3 and Au/SiO2, in the range of H2O concentration over four orders of magnitude. It has been found that the catalytic activity is generally enhanced by moisture in the reactant gas. The enhancement is as large as two orders of magnitude. Response to the moisture concentration, however, depends on the support oxide, indicating different contributions of the support to the reaction steps. The moisture effect is reversible and the activity is mainly determined by the amount of moisture absorbed by the catalyst. The apparent activation energies are not significantly influenced by moisture for Au/TiO2 and Au/Al2O3. On the contrary, non-uniform conversion curves versus temperature observed for Au/SiO2 are drastically changed, which indicates that the reaction over Au/SiO2 does not take place at low temperatures without moisture. The moisture effect may be probably attributed to the decomposition of carbonate species accumulated during the reaction, while the ?OH group might directly participate in the reaction pathways as a promoter.

Oct 1, 2003

By H. Soto, J. Jara, F. Nava

A method has been developed to recover cyanide and copper from cyanidation effluents contaminated with thiocyanate and copper-cyanide complexes. Copper is precipitated as copper thiocyanate or as copper cyanide depending on pH and the concentrations of thiocyanate and cyanide present in the effluent. The copper precipitate presents good dewatering characteristics and can be easily separated from the effluent by thickening and filtration. The solution containing the bulk of the cyanide is then oxidized with ozone to transform the remaining thiocyanate into cyanide. This results in a regenerated solution rich in free cyanide that can be recycled to the cyanidation process. Careful control of the pH of the solution is required. First pH of the effluent is lowered to optimize the precipitation and oxidation stages, then the pH is restored to an alkaline value to regenerate the cyanide solution. Recoveries of over 96% copper are obtained. Free cyanide in the regenerated solution corresponds to up to 160% of the total cyanide contained in the original impure effluent. (The balance being accounted for by the cyanide obtained by the oxidation of thiocyanate). The efficiency of the thiocyanate oxidation stage is 85% to 90%. The method has been demonstrated at bench scale with effluents of various cyanidation plants of northern Quebec. A preliminary economic evaluation indicates that the procedure would be profitable for effluents rich in copper and thiocyanate. This is the case for most barren bleeds of Merrill Crowe and heap leaching operations and also certain CIP tailings of gold ores containing copper impurities. Environmentally the procedure is a better alternative than the current detoxification methods based on the oxidation of cyanide that do not allow for copper recovery and that have difficulties in producing a final effluent with acceptable levels of contaminants such as ammonia, thiocyanate and copper.

Jan 1, 1996

By S. Sakurai

"Gravitational force is an external body force acting on underground structures. It should be noted that gravitational force cannot be replaced with the surface traction vector (Cauchy stress) which is an internal force. This fact should be properly taken into account in a numerical analysis of underground structures, particularly for structures such as vertical shafts, tunnels, and caverns constructed at great depths. It is obvious that the gravitational force must be conserved at all times.In conventional numerical analyses, the initial state of stress of the ground medium is firstly calculated under the gravitational field. This means that the gravitational force is replaced with stress (surface traction vector), and after that only the initial stress is considered in the calculation of the stresses and displacements of the structure. It should be noted that the initial stress is Cauchy stress consisting of a surface traction vector, while the gravitational force is a body force acting on the mass of the materials. This computational approach may be acceptable for elastic problems because the principle of superposition is valid for elastic materials. However, this approach becomes questionable for elasto-plastic materials because there is no guarantee that the principle of superposition is valid for them.Furthermore, another problem exists in elasto-plastic analyses: The stress state in a plastic zone must satisfy a yielding criterion such as that of Mohr-Coulomb. In order to make the stress state satisfy the criterion, an excess stress beyond the yielding criterion should be transferred to an elastic zone existing outside of the plastic zone. This seems to always be possible, because an elastic zone always exists, no matter how large of a plastic zone appears. In some cases, however, the excess stress cannot be transferred to the elastic zone because the gravitational force must be conserved. Therefore, it is obvious that the magnitude of stress around underground structures may become large and surpass the yielding criterion at great depths where a large gravitational force exists.In this paper, it is demonstrated that in a conventional elasto-plastic numerical analysis of a vertical shaft at a great depth, all the stress components around the shaft become very small, even though a large gravitational force exists. This strange result may be due to the fact that the gravitational force is not properly taken into consideration in the numerical analysis."

Jan 1, 2015

By A. Ghahreman

Activated carbon is proven to be able to catalyze arsenic oxidation in aqueous solution under acidic conditions. A commercially available granular coconut shell based activated carbon (AC) has been evaluated for catalysis of arsenic oxidation in this study. The rapid small-scale column test (RSSCT) has been developed to simulate and predict the performance of a carbon-based arsenic treatment system in a pilot scale reactor. Effects of residence time, aeration rate, and initial arsenic concentration in the influent solution on the AC catalysis of arsenic oxidation under dynamic and continuous conditions were studied by manipulating these parameters during RSSCTs. The effectiveness of the AC on arsenic oxidation was examined over the course of constant diffusivity based RSSCT operation. Residence time and initial arsenite concentration are proven to be the most effective impacting parameters on the arsenic oxidation process. For the 218 min residence time, the highest steady-state arsenic oxidation efficiency achieved was 98% with 1 g/L As(III) being treated at pH=1 under 0.05 L/min oxygen aeration. In a long-running RSSCT, the oxidation efficiency did not seem to deteriorate over a course of 666 hours operation, corresponding to 13986 mL total influent throughput volume. INTRODUCTION Arsenic is toxic to both animals and plants and inorganic arsenicals are proven carcinogens in humans. The increased extraction of low grade and complex mineral resources has introduced high ratios of arsenic into metallurgical processes. Discharge of arsenic by acid mine drainage resulting from mining activities has added intensive pressure on the need for proper treatment (Lawrence & Higgs, 1999). Since trivalent arsenite is more toxic and has lower affinity to solid surfaces for adsorption, many treatment systems initiate with an oxidation step to convert arsenite to arsenate and reach the ultimate immobilization of arsenic by the following precipitation of arsenate (Nazari, Radzinski, & Ghahreman, 2016). Scorodite precipitation has been studied extensively as a means of arsenic immobilization due to its high stability and negligible potential of releasing arsenic (Filippou & Demopoulos, 1997). As a stable ferric arsenate mineral, crystalline scorodite can contain up to 30 wt% arsenic (Paktunc, Dutrizac, & Gertsman, 2008). Arsenic must be in its pentavalent oxidation state in order for scorodite to be precipitated via oxidizing ferrous ions (Clancy, Hayes, & Raskin, 2013).

Jan 1, 2019