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By Bern Klein, A. Tugba Cebeci, Libin Tong

"Sensor based sorting faces two main challenges related to limited capacity/throughput and the ability of sensors to accurately discriminate based on estimated grades. This paper is aimed at improving sensor discrimination. Sensors have the ability to measure more than a single response. X-ray fluorescence (XRF) can detect and provide concentration information about a range of elements. Similarly, electromagnetic sensors (EMs) can generate magnetic susceptibility and conductivity responses over a range of frequency levels. The sensors thereby provide a response signature rather than a simply a single response that is a proxy for a metal grade. Furthermore, integrating sensor responses can improve the discrimination of metal bearing rock from waste. A study was conducted on a gold ore to assess sortability using XRF and EM sensors. A multi-variable regression approach was used to develop models that included a range of responses. Correlations improved significantly when compared to single response correlations. The approach showed that both positive and negative correlations contributed to the improved correlations. Stepwise regression simplified the models and showed that 2nd order interaction effects can be important. The approach also showed that combining different responses can improve discrimination accuracy. An important outcome of the study was that an ore that had been consider not to be sortable was determined to be sortable through the application of an approach that used the sensor responses in a more intelligent manner.INTRODUCTIONMining is aimed at recovering valuable minerals from their host rocks. Many methods are used to recover valuable minerals, and finding efficient and cost-effective ways is the key in research and production. . Ore sorting technology is fitting this definition. It not only discards waste rocks away from the concentrator but also recovers metal bearing ore particles that could be lost to the waste dump. The benefits of ore sorting include increased energy efficiency and reduced water and reagent usage in the downstream operations (Bamber, 2008; Gunson, Klein, Veiga, & Dunbar, 2012; Mazhary & Klein, 2015; Robben, Wotruba, Robben, von Ketelhodt, & Kowalzcyk, 2013)."

Jan 1, 2016

By Craig H. B. Leitch

"In describing the alteration of porphyry systems, the term ""secondary K-feldspar"" appears to be an oversimplification. A better term would be ""alkali feldspar"" alteration, because in actual fact the replacement feldspars show gradational changes from an albite, which is important in some systems, to an alkali feldspar containing minor orthoclase molecule, to true orthoclase.There are several textural varieties of secondary alkali feldspar present in the porphyry systems studied from British Columbia, Australia and New Zealand. These include, in apparent increasing order of alteration intensity: clear albite (An10); patchwork albite (An5-10); chessboard albite (An0-10); ""irregular albite "" (An0Ab100 to Ab90Or10); untwinned ""anoralbite"" (Ab90Or10 – Ab70Or30); and orthoclase (Ab40Or60 - Or100)·The exploration significance of these varieties of alkali feldspar is that their gradation in composition, from sodic to potassic, may be linked to a corresponding increase in intensity of alteration. Thus, there is a tendency for more sodic alteration feldspars to characterize weak, sub-economic deposits, or the fringe zones of stronger deposits; the more potassic alteration feldspars may provide an exploration vector toward more highly mineralized zones."

Jan 1, 1981

By Craig H. B. Leitch

"In describing the alteration of porphyry systems, the term ""secondary K-feldspar"" appears to be an oversimplification. A better term would be ""alkali feldspar"" alteration, because in actual fact the replacement feldspars show gradational changes from an albite, which is important in some systems, to an alkali feldspar containing minor orthoclase molecule, to true orthoclase.There are several textural varieties of secondary alkali feldspar present in the porphyry systems studied from British Columbia, Australia and New Zealand. These include, in apparent increasing order of alteration intensity: clear albite (An10); patchwork albite (Ab5-10); chessboard albite (An0-10) "" irregular albite "" (An0Ab100 to Ab90r10); untwinned "" anoralbite"" (Ab90Or-Ab70Or30); and orthoclase (Ab440Or60-Or100)·The exploration significance of these varieties of alkali feldspar is that their gradation in composition, from sodic to potassic, may be linked to a corresponding increase in intensity of alteration. Thus, there is a tendency for more sodic alteration feldspars to characterize weak, sub-economic deposits, or the fringe zones of stronger deposits; the more potassic alteration feldspars may provide an exploration vector toward more highly mineralized zones."

Jan 1, 1981

By Joerg Hammerschmidt, Marcus Runkel, Steffen Haus

Given the limited number of new plant construction, focus is turning to the optimization of existing metallurgical roasting plants. To meet the goals of high process efficiency with limited capital expenditure, plant owners are looking for new strategies, including digitization and expert support. As a supplier for numerous roasting, gas cleaning and sulfuric acid plants, Outotec has intensified its effort in recent years to develop solutions to accommodate increasing customer need. This article presents a short review on how Outotec is applying advanced control tools for the fluidized bed industry. Focus will be given on how to transfer the existing technology (used in selected Zinc roasting plants for over a year now) to copper roasting. Outotec has developed the Pretium Roaster Optimizer, a system based on heat and mass-balanced simulation models. Direct experience with this technology will be shared and will highlight similarities to the Partial and Sulfate Copper roasting processes. Pretium detects equipment and plant bottlenecks and provides consistency in process development. The Pretium program combines 24/7 advanced online digitalization tools, along with expert personal support when required. INTRODUCTION Fluidized bed reactors have been used for commercial-scale zinc and copper roasting since the 1950s. While the principles of roasting remain unchanged, over time, the technology has advanced to improve process control of roasting plants. In the past, environmental and safety standards were the driving forces for improvement of equipment and plant design. Today, the emphasis is on plant efficiency and optimization. Another change has come in process control philosophy. While plant control and operation have traditionally been the responsibility of owner/operators, they have now shifted to include both integrated digital tools and specific know-how from engineering companies. This can be seen from the earliest design stages through commissioning and into production, as evidenced by zinc roasting plants in Mexico, Brazil and Turkey.

Jan 1, 2019

By Wengui Su, Qi Zhang, Junce Wang, Zhijun Ma, Xingyuan Weng

"Mesoporous materials with large specific surface area, pore size, and pore volume have been widely used in many fields such as ion exchange, gas separation, adsorption, and catalysis. Mesoporous materials prepared using natural zeolite have the advantages of both acid and alkali resistance. In this work, mesoporous materials were prepared using natural zeolite as the starting material and diethylenetriamine (DETA) as a template. The resulting samples were characterized using scanning electron microscopy (SEM), X-ray diffraction (XRD) and N2 adsorption-desorption experiments. The influence of the crystallization temperature and crystallization time on the specific surface area, pore volume, pore size, and morphology of the resulting mesoporous materials are also discussed. Our results show that for an increase in both the crystallization temperature and time, the average pore size first increases then decreases, while the specific surface area first decreases then increases. Based on this work, we concluded that the optimal crystallization temperature was 2003 and the optimal crystallization time was 60 h. These conditions gave an average pore size of 17.93 nm, a pore volume of 0.048 cm3g-1, and a specific surface area of 16.48 m2g-1.INTRODUCTIONMesoporous zeolite, as the name implies, is a highly porous crystalline zeolite. This material is of interest due to its high hydrothermal stability, its adsorption and diffusion properties for macromolecules, and its excellent selectivity and activity as a catalyst. In recent years, it has become a hot spot among research of porous catalytic materials and has been widely used in petroleum and natural gas processing, fine chemical processing, various adsorption and separation tasks, and other uses (Carvalho & Urquieta- Gonzalez, 2015; Teh, Triwahyono, Jalil, Mukti, Aziz, & Shishido, 2015)."

Jan 1, 2016

By J. E. Danoczi

Shore Gold Inc. (Shore) is presently designing a diamond processing plant for the Star and the Orion South kimberlite deposits in the Fort à la Corne area kimberlite field in central Saskatchewan. The first step in the plant is diamond liberation and occurs in the comminution section. Diamond liberation is the process of breaking up the kimberlite rock, as ?gently? as possible since essential to the diamond liberation process is the minimization of diamond damage, particularly for the larger, high value diamonds. The Southern African diamond mines traditionally use Jaw and Gyratory crushers as their primary comminution method. However, these diamond mines generally process the harder, competent kimberlite that is located in the diatreme zone as well as the root zone of the volcanic pipe. Softer kimberlite is typically located in and around the crater area of a volcanic pipe and it is this source of kimberlite that makes up the majority of kimberlite for both the Star and Orion South deposits. These softer kimberlites can be readily broken up using abrasion and attrition imparted by AG mills, this being the preferred method of comminution for minimizing diamond damage.

Nov 1, 2011

By Nickvinder Bhath, Johnson Matthey Plc, Jamie Baker, Daniel Kim, Jeff Lucht, Shijie Wang

"Precious metals (PM) in copper anode slimes are traditionally recovered by pyrometallurgical processes. Due to the compliance with increasingly stringent environmental regulations, it has made hydrometallurgical processing an attractive method for recovery of precious metals, including relatively inert metals such as gold and platinum group metals (PGMs). In this paper, a new method to recover PGM from complex and difficult feed streams is described. Using a proprietary Advanced Ion Exchange (AIX) adsorbent which has a high selectivity for PGMs over other metals and can achieve high PGM mass loadings with a series of incredible pilot test data plus the business case generated from the study results are also presented in the paper.INTRODUCTIONPrecious metals in copper anode slimes are traditional recovered by pyrometallurgical processes. Due to the compliance with increasingly stringent environmental regulations, it has made hydrometallurgical processing an attractive method for recovery of many metals, including relatively inert metals such as gold and platinum group metals (PGMs). Fully hydrometallurgical processes for extraction and recovery of gold and silver from copper anode slimes were employed in major copper refineries since 1995, which was first developed at Rio Tinto Kennecott Utah Copper.In Rio Tinto KUC process, the wet chlorination and gold solvent extraction were utilized to enable recovery of gold and silver as well as other metal compounds. The availability of water and the interaction and amenability of gold processing in water-based solution makes it possible that gold and silver are produced in only five days, compared with a traditional pyrometallurgical process that took 45 days. Most copper refineries are still following the tradition, but the use of hydrometallurgical technologies is increasing as the world demand for metals increases, energy utilization, and environmental viability."

Jan 1, 2016

By N. Torres, G. Melcher

"An alternative to building new copper smelters, because of either stringent environmental regulations or in order to expand current plant capacity, could be achieved through the retrofitting of old reverberatory furnaces by making use of tonnage oxygen. The CONTOP® technology offers unique advantages over other techniques for this purpose, especially regarding substantial reduction in bath, capital and operating costs. This is possible to achieve since the reverb throughput could be largely increased with no major structural modifications to the furnace.The following options are offered to the smelter operators: dirty concentrates can be treated in an adjacent Contop system, or the cyclones can be mounted on the reverb roof for either dual operation or full Contop operation. ln the tatter case the furnace will be used as a settling chamber and f or slag c1eaning by top blowing with reducing gases.By incorporating Contop technology, the furnace throughput can be increased, higher malle grade, fixation of sulphur from furnace off-gas and substantial savings in energy consumption are possible to attain.IntroductionCopper smelting has been revolutionized during the last quarter century to such an extent that the standard type of plants consisting o f roasters and reverb furnaces seem a thing of the past, or almost. Though the building of new, more energy efficient smelters is a very likely opportunity for a grassroots plant, it would be hardly justifiable to replace an old existing plant unless there are heavy environmental or economic constraints(1,2,3)."

Jan 1, 1984

By D. R. Murray

"In 2017, Nutrien Allan Potash remediated a portion of the concrete liner in the production shaft. A set of underslung work platforms and collection boxes were used in conjunction with hydraulic splitters, jackleg drills and hand chippers to excavate and remove the broken concrete. New concrete was placed with the original pressure relief design, using a shaft slip form. Shortly after excavating, it was found that the estimated breaking rate and amount of original concrete in-situ was under estimated. Fifteen feet of excavated concrete (2719cu.ft) and ten feet (of replaced concrete was completed on April 28, 2017, and operation of the production shaft was returned to mine operations. During February 2019, Nutrien Allan Potash began remediation of a portion of the concrete liner in the service shaft. The project is different than the 2017 project, as the remediation has occurred during normal running operations and occurred only on night shift. Rather than hydraulic splitters and hand chippers, the new method includes a concrete saw and mechanical excavator from a working platform. The selected method is based on the lessons learned from the 2017 project in the production shaft. The service shaft project was scheduled to be completed in July, 2019. INTRODUCTION Nutrien Allan Potash is located approximated 75 km east of the city of Saskatoon, Saskatchewan, Canada. There are currently two shafts at Nutrien Allan Potash: the Production Shaft and the Service Shaft, transporting people and material from surface to a depth of 3,335 ft. The Production Shaft was completed in 1967, with one section of grey cast iron tubbing installed in the Blairmore formation between the 1605 and 2037 ft Levels. A second set of cast iron tubbing was installed in the Duperow formation between 2203 and 2463 ft Levels in 1999. The remainder of the concrete as of todays standards is designed as a pressure relief liner. The Service Shaft was completed in 1968, with one section of grey cast iron tubbing installed in the Blairmore formation between the 1600 and 2048 ft Levels. A second set of cast iron tubbing was installed in 1981, with 169 ft installed through the Duperow formation. The remainder of the concrete as of todays standards is designed as a pressure relief liner. PRODUCTION SHAFT REMEDIATION During the second quarter of 2015, the Mine Engineering team were notified of an area of concern in the production shaft. The shaft specialists of Golder Associates Ltd (Golder, formerly Alan Auld Canada) were contacted to complete an inspection of the production shaft liner with emphasis on the area of concern. Based on the inspection and documentation review, it was determined that the concrete at the 2804 foot elevation had been broken out for some time and was retained with #8 rebar bolts with resin encapsulation. The broken concrete was encroaching on the clearance to the conveyance."

Jan 1, 2019

By J. W. Scott, G. G. R. Falkenberg

"The Syncrude project is an integrated complex designed to mine, extract and upgrade bitumen from the Athabasca tar sands to produce 129,000 barrels per day of synthetic crude oil. This paper provides a brief general description of the location, history and geology of the tar sands and the overall organization and structure of the project. The major emphasis and the bulk of the detail presented deals with the extraction plant; a material handling and mineral processing installation designed to treat 312,000 tons per day of tar sand feed.History of the Tar SandsThe Athabasca tar sand deposit was recorded in 1788 by Peter Pond, however the first serious geological mapping and exploration did not begin until 1915. Little interest was taken in the deposits until the Second World War, when the governments of Canada and Alberta conducted an extensive exploration program. In addition a number of pilot plants were sponsored during the 1940 -1950 decade. The hot water separation process was successfully demonstrated on the pilot plant scale during 1948 -49, and was established commercially in 1967 in the G.C.O.S. plant. The Syncrude plant, due to come on stream in April 1978, also employs the hot water separation process."

Jan 1, 1978

By E. G. Parker

"Sherritt's zinc pressure leaching process converts zinc sulphide concentrates directly to zinc sulphate solutions and elemental sulphur. Thus, one pressure process step replaces both the roasting and leaching operations of the conventional roast-leach route. In addition, high single-pass extractions eliminate the need for residue treatments to recover unleached zinc. Because pressure leaching produces elemental sulphur, rather than sulphur dioxide, acid plants and smoke stacks are not required, and air pollution control and work-place hygiene are greatly improved. .In 1977, Cominco Ltd. and Sherritt Gordon Mines Limited jointly operated a three-tonne-per-day pilot plant to demonstrate pressure oxidative leaching of Sullivan zinc concentrate and the subsequent separation of elemental sulphur. The process consisted of regrinding the concentrate, continuous leaching at 150°C at elevated oxygen pressures in a four compartment autoclave and the subsequent recovery of elemental sulphur, either in the molten liquid form from a decantation autoclave or as a flotation concentrate. Of the zinc contained in the concentrate, 97% was extracted in 90 minutes, and 96% of the sulphur was converted to the elemental form.Following the successful pilot campaign, Cominco began building the world's first commercial zinc pressure leaching plant. This plant, which was in operation by late 1980, will eventually treat about 25% of Cominco's planned zinc capacity of270,000 tonnes per year.This paper describes the general process principles, the results obtained from the pilot plant and the integration of the process into Cominco's operations at Trail. The application of pressure leaching to a ""grass-roots"" plant is also discussed, and compared with conventional roast-leaching."

Jan 1, 1981

By T. Hadley, Northern Minerals Ltd, C. S. Griffith, T. A. Safinski, K. H. Soldenhoff, M. Fainerman-Melnikova, A. Manis

"ANSTO Minerals and Northern Minerals have been working together since 2012 on the process flowsheet development for the Browns Range project for the recovery of the heavy rare earths (Dy – Lu, + Y). Initial efforts were directed toward defining the most efficient and direct flowsheet for the Preliminary Feasibility Study (PFS), issued in June 2014, then towards the Definitive Feasibility Study (DFS), issued in February 2015. These goals were achieved by undertaking comprehensive laboratory and continuous piloting programs. Further improvements to the flowsheet following the DFS have been made. This publication provides an overview of the evolution of the process flowsheet based on these laboratory and piloting programs from the PFS through the DFS and beyond.INTRODUCTIONNorthern Minerals Ltd (Northern) has been working on developing their flagship project at Browns Range for the recovery of the heavy rare earth elements (HRE, Dy – Lu, + Y). The project is located in the north of Western Australia as shown in Figure 1. The Total Mineral Resource at the project is currently estimated at 8.98 Mt @ 0.63% total rare earth oxides (TREO) comprising 56,663 t of contained TREO using a cut-off grade of 0.15% TREO. Of the Total Mineral Resource, 58% is classified as Indicated Resource, with the remainder in the Inferred Resource category.The deposit is characterised by breccia-hosted, hydrothermal, HRE-rich, xenotime mineralisation. The main gangue mineral associated with the xenotime is quartz. The distribution of rare earths (RE) observed for the xenotime mineralisation at Browns Range is presented in Figure 2. Extensive test work has shown that the xenotime can be readily beneficiated to between 20 – 40% rare earth oxide (REO) using a process consisting of crushing and grinding, followed by magnetic separation and flotation steps. Continuous piloting of this process was conducted on ~80 t of trench-sourced ore in late 2013 at SGS Perth, to produce ~2 t of ~20% REO mineral concentrate (MC) for hydrometallurgical testing. The composition of the MC produced during piloting is presented in Table 1."

Jan 1, 2016

By Robert B. Parsons

"The annual onslaught of provincial budgets and tax changes is complete, and once again the Canadian taxpayer is being asked to dig deeper into his pocket to fund old and new programs. It is noteworthy that 1987 tax reform promised lower taxes, but a broader fax base. Five years later, we still have the broader tax base, but the lower faxes have gradually crept up to pre-tax reform levels. Surprise! Surprise!IntroductionThe last edition of Tax Notes commented on some important proposals announced in Manitoba's 1992 budget. In this issue, Tax Notes summarizes the 1992 budget proposals of British Columbia, Ontario and Quebec. These budgets reflect the continuing trend of transferring responsibilities and the related costs-from the federal government to the provinces. As well, the budget papers bear witness to the respective governments' political stripes. British Columbia, Ontario and Quebec are seeking higher tax revenues. Only Quebec continues to acknowledge the importance of the mining industry in its annual budget documents."

Jan 1, 1992

Fatalities Incident Four people perished May 15 ? 17, 2006 ??Doug Erickson ??Bob Newcombe ??Kim Weitzel ??Shawn Currie Incident details available at: ??http://www.mediaroom.gov.bc.ca/sullivan_mine/ ??sullivan_mine.htm Outline Immediate facts/observations from incident ?? #1 Shaft Waste Dump closure program ?? Technical investigations under Panel guidance ?? Findings to date and direction ?? Broaden awareness of potential risks

May 1, 2008

By John Smith

"The RTZ Corporation PLCFrom a company's point-of-view, a good investment decision is one which results in the purchase of an asset that is worth more than it costs. Thus, in order to judge the merit of an investment opportunity, it is necessary to estimate the value of the assets to be acquired.Discounted cash flow (DCF) analysis has become widely adopted by companies in assessing potential new investments. The principle is a simple one: invest in projects which have a positive net present value, and reject those which do not. However, perhaps because of its apparent simplicity, DCF analysis is frequently misused. Good practice in the use of the technique is discussed, together with several common misconceptions.Sound analysis requires sound data; thus, the valuation process relies heavily upon a wide range of specialists to provide the basic input from which cash flow forecasts can be built up. The analyst must maintain close liaison with these specialists from the outset in order to ensure that the data provided is indeed relevant and complete.IntroductionBefore turning to the main subject of this paper ""How Companies Value Properties"", it is of interest to consider first a slightly different question ""Why do Companies value Properties""? In other words, for what purposes are such valuations prepared? Certainly the commonest, and probably the most important circumstance in which a valuation is required is when the company is considering an investment opportunity. This may be the direct purchase of a property or group of properties from a third party, but could also be the opportunity to develop a new operation or expand an existing one.A very simple objective in making any kind of investment is to make our shareholders richer than they would otherwise have been. That is, to make investments whose value to shareholders exceeds the consideration required to acquire them. Thus the investment decision focusses on the difference between an asset's value and its cost.This distinction between ""value"" and ""cost"" is an important one. Study of a company's balance sheet may tell a lot about the cost of this company's assets, but very little about their value. Then again, it is sometimes argued that a business should be bought because this will result in assets being acquired for less than their replacement cost. This merely compares one cost with another, it says nothing about value."

Jan 1, 1991

By D. A. Stokes

"In October of 1980, Fording's 15 000-ton capacity clean coal silo was put into operation. The silo was unique in that it was designed to allow the mass flow of material, coupled with a sophisticated computer-controlled dynamic loadout/weighing system.On May 1, 1982, an explosion, attributed to a methane buildup, devastated the top of the silo. .As a contingent plan to minimize the effect of the production loss the conveyance to the silo top was reconstructed and the silo' was back in operation by mid-June 1982, although the silo top was left open to prevent further methane buildup. As dust emissions occurred during loading ofthe silo, an extensive study was undertaken to establish dust control for the silo, while at the same time providing methane detection and control.The study, conducted for Fording by the Cambrian Engineering Group of Calgary, involved an extensive search and investigation of existing coal silos. The study concluded that there IS no universally accepted method of controlling methane emissions in coal silos.The study also produced a unique conceptual design for handling methane, while at the same time, protecting the environment . Fording's Clean Coal SiloThe silo, located at Fording Coal's Fording River metallurgical coal operation, is utilized for the storage and load out of cleaned thermally-dried metallurgical coal.The silo was constructed in 1979 and 1980 to reduce unit train loadout times and to facilitate the handling of “special shipments"" of coal. The silo went into operation in October 1980, under manual control and utilized computerized, automated loading by February 198I.The silo is 21 m in diameter and 76 m high, with a nominal capacity of IS 000 live tonnes. The coal storage portion of the silo is 21 m in diameter and 48 m high, utilizing 2 steep-angled hopper outlets allowing mass flow of the stored coal during train loading. Each hopper has a control gate and a discharge chute, one chute for bulk loading, the other for trim loading of coal into the rail cars."

Jan 1, 1986

By G. R. Haiden, E. Henderson

"An LHD teleoperation and guidance system, developed at the Ontario Division of Inco Limited, has been demonstrated in operation at Copper Cliff North Mine (CCNM) since late September, 1993. The tests performed to date have evaluated the feasibility and production viability of multiple LHD operation, from surface by one operator.The systems technology required to accomplish this consists of an electronic monitoring and control package mounted on the LHD; a high bandwidth mining computer network capable of providing radio frequency coverage; and an operator control console which provides an operator workstation for multiple LHD operation.This paper discusses the systems required to accomplish the task of LHD teleoperation and guidance, the benefits of multiple machine operation and future research and development directions. IntroductionSince underground mining began, persolU1el have entered the mine workings to mine ore. Today, however, the rapid advancement of modem telecommunications, computer hardware and software technology has opened the door to remote mining technology that was considered unfeasible a few years ago. This paper discusses the ingredients of remote mining technology that have been developed at Inco Limited.Figure I represents an historical view of the application of electronics to LHD operation at Inco Limited. In 1980, the first radio remote controls for the operation of LI-IDs in large open stopes were tested. The successful application of this technology at Inco went hand-in-hand with the development and application of the Vertical Crater Retreat mining method. The combination of these two advances had a very positive effect on the productivity in the mid-eighties at Inco. In 1991, the Mines Research Department of the Ontario Division advanced remote control technology by developing a high capacity underground mining telecommunications system. This system is capable of moving voice, data and video information throughout the mine workings. The system is based on broadband communication technology found in most automated factories, with the added benefit of providing the information to and from mobile equipment through radio interfaces. The first test of the system consisted of an operator teleoperating a single LHD (on the 3000 ft level) from the surface. The next test on September 13, 1993, demonstrated the first production application of multiple LHDs being run from surface with a single operator."

Jan 1, 1994

By D. V. Krefting, D. R. Bennett

"The Cyprus Anvil Mining Corporation established a lead-zinc mine and concentrating plant at Faro in Yukon Territory in 1969. Following some 12 years of continuous operation from a single pit adjacent to the concentrator, the company decided to expand operations into two additional areas on the Vangorda Plateau. The two new deposits, known as Grum and Vangorda, are located some 15 kilometres from the existing concentrator.Confirmation of mining feasibility was followed by determination of the most practical and economical method of transporting the raw ore from the new mine sites to the existing concentrator. This analysis was carried out in two phases. The first phase reviewed the feasibility of alternative transportation systems on an 'order-of-magnitude' cost basis. This work identified systems worthy of more detailed examination. The second phase examined the preferred alternatives in greater detail.Initially, operating principles and parameters were established and catalogued. Then, based on these criteria, complete systems were developed utilizing alternative modes of transportation . In the overview analysis, some transportation modes were judged impractical and discarded, 'order-o f-magnitude' costs were developed for other systems and the most costly were eliminated . In the detailed study, the favourable systems were examined in depth which required development of accurate capital and operating costs, consideration of environ- mental impacts and an assessment of intangibles associated with the operation of a new development."

Jan 1, 1984

By Neil Schofield

"The estimation of recoverable ore reserves for feasibility in precious metal deposits such as Pine Creek must account not only f or the extreme variability of the ore grade but also for the complexity of the geology. Compatible models f or both must be adopted. Further, very selective mining demands reserve estimates be based on small selection units whose individual grades cannot be estimated reliably from the exploration drilling data.Multigaussian kriging is one method based on a multivariate normal model for estimating recoverable reserves under such conditions. In this paper, a non-mathematical description of the multigaussian model is presented together with its application to the Pine Creek Gold Deposit. The results, when compared to the first year of production, are encouraging for the model but not without surprises.Together, Part 1 and Part 2 of this study combine a detailed and geologically conditioned variogram analysis with an appropriate estimation method for a highly variable low-grade gold deposit. This and other studies of gold deposits familiar to the author show convincingly both that while the appropriate geostatistical skills and techniques are necessary to tackle the question of reserves, equally important but often discounted is the need for an appropriate and compatible geological model. IntroductionThe Pine Creek gold mineralization is associated with saddle reefs, and quartz and quartz- sulphide veining within the Enterprise Anti cline. The anticlinal structure is complex and, prior to mining, the mineralization was considered to be mainly strata controlled. Grades vary up to 160 grams in l .5rn core samples with coefficients of variation in excess of three.The estimation of the recoverable reserves for such a depo sit must account for both the geological complexity and the extreme variability of the gold grade.Part 1 of this work presented the geological model for the deposit and summary statistics 0 f the gold data. A detailed structural and variogram analysis considered both gold grades and the normal score (or gaussian transform) of these gold grades for different composite sizes."

Jan 1, 1988

By John H. Schloen

"The object of this paper is to review electrolytic copper refining as it was in 1954(1), as it is now in 1984, and to comment on the many improvements which have been made in the last thirty years.In 1954, and even in 1984, the ASTM specification B 115 for cathode copper was 99.90% minimum copper plus silver content and 100% minimum electrical conductivity, IACS standard. However, to meet competition and to satisfy the requirements of the fabricators and the electrical industry, the electrolytic refinery must supply a product of 99.95% to 99.96% minimum copper content, and 101fJlo minimum electrical conductivity.The range of cathode impurities reported by 20 major copper refineries in 1954 are given in Table I.The much more rigid British Specification, DD 78, for high-purity cathode copper, specifies individual elements, as well as groups of elements, as shown in Table 2.The Svenska test has been replaced by a similar procedure which uses 2.r mm diameter wire. The ISO test is the one listed in the DD 78 specification. In Table 3, corresponding values for the Svenska and ISO test s are given for various wire bar coppers."

Jan 1, 1986