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In the last 30 years numerous mining plants have been developed in North America but only a handful of these have required freezing the area where the shaft was sunk. The most recent mine shaft to be sunk using this technique is located on an island off the coast of Louisiana. The project required the input and skills of numerous people in several companies, including the owner, engineers and contractors. The Cote Blanche installation is one of several mines in the area which extract salt from a dome which extends under the Gulf of Mexico. The geology of this area is, however, markedly different from others in the region because there is approximately 460 ft of water logged soil above the salt dome. Because it is not possible to sink a shaft in ground that is this soft, the overburden where the shaft is located must be frozen before excavation can take place. The Cote Blanche mine is a producing facility which was built in 1958 by the Carey Salt Company. The original facility included a 14 ft diameter production shaft and a 7 ft-8 in diameter service/ventilation/escape shaft. This system was installed by The Cementation Company. In 1996 the owner decided to improve both the mine ventilation and production hoisting system by installing a third shaft. This shaft would be designed to extract 650 tons per hour from a depth of 1600 ft and provide 500,000 cfm of ventilation to the mine at a maxium design pressure of 4 in WG. These parameters resulted in a requirement for a 16 ft finished inside diameter concrete lined shaft and a headframe designed as a pressure bulkhead. Because the mine would operate from one level only, the most efficient hoisting system for the application was determined to be a ground mounted koepe running on rope guides. With these criteria fixed Cote Blanche embarked on a program which would see construction start in June 1998 with the first salt produced in February 2001 at a cost of $US18M. The major players in the design and construction were G.L. Tiley & Associates Ltd., BLM Bharti Engineering, Freezewall Inc., Phillips Mining, Geotechnical and Grouting Inc., Don Hart Consulting and Dynatec International.

May 1, 2002

By Mahmoud Shakeri1

Various types of thin-walled structures have been frequently used as energy absorbers to mitigate the adverse effects of impact and hence protect the vehicle structure under consideration when subjected to different loading conditions. Compression tubular structures that buckle in a progressive manner, can be used to advantage, providing inexpensive and versatile, but nevertheless weight and stroke efficient energy absorbers. In this paper quasi-static nonlinear finite element simulations are performed to study the effects of number of corners of the cross-section, wall thickness, plastic hardening rate of material, foam-filler and load angle on deformation mode and mean crushing force of tube. Crush strength increases as the number of corners of the cross-section increases, though it almost saturates for the number of corners beyond 11. Higher plastic hardening rate stabilizes the collapse pattern. Foam-filled tubes seem to have higher critical load angles in oblique loading and display a more stable and gradual decrease in mean load over the transition region. Substantial decrease in the initial peak load and dynamic load at any a given deflection was observed as the load angle increases. The investigation of bitubal arrangements and Multi-cell tubes reveals that these may be preferable to monotubal specimens due to the presence of the inner profiles. In addition, a comparison is conducted between the numerical and experimental results of the mean forces of some special angle elements. Good agreement is obtained.

Oct 1, 2011

"At the May 15, 2006 and the May 1, 2007 Canadian Securities Administrators (CSA) Canadian Institute of Mining, Metallurgy and Petroleum (CIM) meetings in Vancouver and Montreal, CSA requested CIM consider certain issues arising out of the CSA review of Technical Reports and public disclosure, in general, regarding the practice of estimation and reporting of Mineral Resources and Mineral Reserves. The following is a summary of the issues raised by the CSA and the responses of the CIM.Preamble: At the May 15, 2006 and the May 1, 2007 Canadian Securities Administrators (CSA)-Canadian Institute of Mining, Metallurgy and Petroleum (CIM) meetings in Vancouver and Montreal, CSA requested CIM consider certain issues arising out of the CSA review of Technical Reports and public disclosure, in general, regarding the practice of estimation and reporting of Mineral Resources and Mineral Reserves. The following is a summary of the issues raised by the CSA and the responses of the CIM Reserve Definition and the CIM Estimation Best Practices Committees (the Committees). This information is intended to provide the Qualified Person (QP) with further guidance when estimating Mineral Resources and Mineral Reserves and in preparing a technical report written under National Instrument 43-101 (NI 43-101). Several members of the CIM Reserve Definition Committee, the CIM Estimation Best Practices Committee and some members of the Committee for Mineral Resources International Reporting Standards have reviewed these issues and provide the following commentary.Issue 1. - CSA requested CIM review and comment on the selection of an appropriate commodity price to be used in Mineral Resources and Mineral Reserves estimates.Commodity prices are used in the estimation of Mineral Resources and Mineral Reserves and in the economic analysis of a property. In times of rapidly changing commodity prices, or when prices are at the extreme ends of a commodity price cycle, the QP has a difficult job in selecting an appropriate commodity price.• The selection of appropriate technical variables, including commodity price, is clearly the responsibility of the Qualified Person (QP). The QP must describe the reasons for selecting these variables, including price, in the technical report.• The definition of a ""Mineral Resource"" contains the wording ""reasonable prospects for economic extraction,"" therefore, a QP must select economic parameters, including commodity price, that will result in an estimate of Mineral Resources and Mineral Reserves that have ""reasonable prospects for economic extraction""."

Jan 1, 2003

By Aimee Williamson

Bio-mining is a cost-effective, energy efficient and potentially environmentally protective method of exploiting a variety of ore deposits, from high-grade base metal deposits of nickel to lower-grade uranium deposits such as are found in the uraniferous quartz-pebble conglomerate beds of the Quirke Syncline, Elliot Lake, Ontario, using bacterial metabolic processes are used to enhance the solubilization of the metal(s) of interest. The cost effectiveness of bio-mining in Elliot Lake depends on the bacterially-influenced dissolution metals of economic importance, as well as on the ability to suppress microbiological activity following the release to solution of the economically important elements. This poster provides an overview of elemental recovery results and release kinetics for more than 50 elements. The data is obtained using a combination of advanced spectroscopic tools (ICPAES and ICP-MS) to analyze solutions obtained from a series of environmentally controlled biologically mediated uranium ore extraction experiments. The focus will be on rare earth elements, potential environmentally toxic elements, and metals of economic importance. Furthermore, the importance of these findings will be put into an economic and geologic context for the re-development of the mining industry of the Elliot Lake Camp.

Aug 1, 2010

By Steve Dismuke, Tom Diment

In December 1994, Polaris decided to investigate the use of cemented rockfill (CRF) to supplement the existing frozen rockfill system. Extraction plans for the remaining ore reserves required a backfill with superior stiffness proper-ties and capable of developing high early strengths. Although CRF has been used success-fully at several mining operations, there was the additional challenge of making a reliable cemented product in permafrost conditions. There was also the challenge of procuring and storing one year’s supply (13 000 tonnes) of bulk cement. By the spring of 1995, following three months of research, test work and process design, the decision was made to proceed with the procurement and construction of a 3000 tpd batch plant. An ambitious completion date of December 1995 was set. Team Manufacturing of Langley, British Columbia was awarded the contract, complete with the considerable task of having the batch plant fabricated and ready for sea lift shipment by August, 1995.

Jan 1, 1996

By E. V. Manlapig, U. Erol, V. Ross, K. Tshimanga

Lonmin RoM ball mills are treating two types of feed ore produced by conventional mining and mechanised mining methods. It was reported that reduction in mill throughput was observed when treating the mechanised mining ore. Detailed grinding surveys were conducted for troubleshooting. Ore samples were collected for breakage characterisation using a JKRBT based on different particle density components. XRD analysis was conducted to investigate the association of minerals with density components. The plant surveys and the breakage characterisation tests all suggested that the two mining methods did not significantly affect either the ore breakage properties or the RoM mill performance. Instead, the mill discharge open area exerted a remarkable influence on mill throughput. The RoM ball mill operated at Lonmin K4 Concentrator has been proven to be a versatile mill that performed stably with variations in feed size distribution and feed ore changes by different mining techniques. The reasons are elucidated by the multi-component breakage characterisation and the plant surveys data.

Jan 1, 2012

By F. King, R. Sutherby, J. Been

With thousands of kilometers of buried oil and gas pipelines throughout the country, carrying flammable, high-energy hydrocarbons, the integrity and safety of this transportation and distribution network are paramount. The pipeline industry has the primary responsibility for pipeline safety and has in many ways taken the lead in dealing with safety issues. Over recent years, regulatory demands have increased, requiring operators to comprehensively evaluate their pipelines through indirect and direct inspections and to manage risk through integrity programs. Mechanistic and correlative models have been developed that assist in the prediction of pipeline integrity and the determination of reassessment intervals. These lifetime prediction models are based on decades of laboratory research as well as pipeline operating data, material data, and field monitoring data pertaining to soil conditions and CP. An overview is presented of an integrated approach towards the development of such models for the evaluation of external cracking and corrosion of transmission lines.

Jan 1, 2005

By J. E. Nesset

The past 50 years have been a golden era, not just for the CMP but also for the development and success of Canadian technologies in the field of mineral processing. The CMP has played a critical role of technology transfer agent, and the success of these technologies is also linked to the success of the CMP itself. The presentation will cover, in brief, the growth of the CMP from its origins as the Canadian Gold Metallurgists in 1964, with some 39 attendees, to the present day when the annual meeting sees 500 and more from a dozen countries. Also covered will be selected technology success stories from the 50th anniversary volume to be given to all delegates ‘Canadian Contributions to Mineral Processing Technology 1968-2018’. The volume itself highlights some 40 technologies that have been divided into five categories; process water treatment and minesite environment, technology innovations, innovations in operations, technology providers and university contributions. Some international perspectives will also be shared.

Jan 1, 2018

By Y. C. Kim

This paper discusses Air Liquide's patented SPALTM (Surface Protection Air Liquide) technology and process for the inerting of coreless induction furnaces using cryogenic liquid gas. Air Liquide Canada Inc., in collaboration with Riverside Brass and Aluminum Foundry Limited (Riverside Brass), conducted plant trials to demonstrate the applicability of the SPALTM technology for copper-based alloys. Results showed that with SPALTM, Riverside Brass benefited from a significant increase in metal yield as the level of dross formation was drastically reduced. Together with the many other benefits of this technology, SPALTM demonstrated to be a non-negligible cost-effective solution to reduce metal production costs. In an effort to optimize the argon flow, different flow rates were used and the oxygen level above the metal bath was measured to pinpoint optimal flow. The results of metal yield, charge mix, dross formation, and melt temperature are compared with and without argon. The metal yield improvements are dramatic and calculated net savings are presented hereunder.

Jan 1, 2007

By R. A. L. Drew, J. P. Immarigeon, F. Jalilian, M. Jahazi

In the present work TLP bonding of Inconel 617 is investigated. The influence of the main processing parameters i.e. time and thickness of the interlayer were studied with optical and scanning electron microscopy. Boron containing interlayers with two different thicknesses were used and the influence of various holding times from 5 min to 24 hours on the microstructure of the bond region was investigated. The results indicated that, for the testing temperature of 1065°C and holding times above 2 hours with an interlayer of 25.4 microns thick no liquid phase was observed. The same phenomenon occurred only after 6 hours for a 76.2 microns thick interlayer. Precipitate growth started at grain boundaries and continued inside the grains. The composition, size and morphology of the precipitates were studied using electron microprobe analysis. No noticeable changes were observed in the grain size of the base metal with increasing holding times.

Jan 1, 2004

By B. T. Lu, J. L. Luo, H. X. Guo

This paper investigated the synergistic effect in the slurry-erosion process of carbon steel. In line with the mechanisms of material loss, the synergism due to interaction of erosion and corrosion was divided into the corrosion enhanced by erosion and erosion enhanced by corrosion. The erosion-corrosion tests were conducted with A1045 steel in slurries containing silica sand. Experimental results showed that the rotating of the sample in corrosive media raised both OCP and corrosion rate, but the impingement of solid particles did not affect the corrosion current significantly. In the quiescent solutions, the Faraday's law gave a good prediction for the weight loss caused by corrosion but for rotating samples, the weight loss experimentally measured was virtually greater than that predicted by the Faraday's law, indicating that the corrosion-enhanced erosion could occur in corrosive fluids in absence of solid particles. A half-logarithm relationship was observed between the weight loss due to corrosion-enhanced erosion and the anodic current density.

Jan 1, 2004

By J. Moyes

The Intec Copper Process is an internationally patented hydrometallurgical process for the extraction of pure copper and precious metals from sulfide concentrates. Developed and proven in Sydney, Australia at a cost of US$15m over the last ten years, the Intec Copper Process is now ready for commercial application. The Intec Copper Process has several notable advantages over both smelting and other hydrometallurgical processes. Starting from a base of substantially lower capital and operating costs than any other conventional or developing process, the Intec Copper Process is economically viable at capacity levels as low as 15,000tpa-Cu, and capable of accepting low grade and metallurgically complex concentrates. Precious metals are recovered within the Intec Copper Process circuit, without the need to re-treatment of the environmentally stable solid residues. The Intec Copper Process offers the lowest energy consumption of the available technologies, with no liquid emissions or production of noxious gases. Unlike smelting, sulfur is recovered in the solid residues in elemental form.

May 1, 2002

By Steven Aiken

The East Boulder Mine located in Montana, U.S.A. utilizes snowmaking to assist with mine water treatment for nitrogen removal. Nitrogen species, including ammonia, are common contaminants in mine water from underground mining operations. Snowmaking provides secondary treatment of nitrogen during the winter due to the chemical and physical processes that occur during snowmaking, in the snow pack and in the snowmelt. The primary processes include atomization, evaporation, sublimation and volatilization. The snowmakers also provide secondary treatment for nitrogen removal when used as evaporators and/or land application units during the summer. In 2002, the snowmaking process was successful at reducing total nitrogen in the mine water by up to 87%. If additional losses due to soil and root zone processes are included, total nitrogen reduction would increase to between 87 and 97%. Snowmaking is an effective nitrogen reducing treatment method during the winter when other treatment methods such as land application cannot be used.

May 1, 2004

By K. Madi, E. Yeugo Fogaing, S. Forest, M. Boussuge, L. Massard, M. Huger, Gaultm C.

This study has been carried out owing to the French research program PROMETHEREF, which aims to improve the knowledge of thermal and mechanical properties of industrial refractories at high temperature. In this frame, this paper relates a collaborative study between Saint-Gobain CREE, R&D Centre for Saint-Gobain Ceramics & Plastics in Europe (Cavaillon), the Materials Center P.M. Fourt of Ecole des Mines de Paris (Evry) and the Research Group on Heterogeneous Materials (GEMH) of ENSCI (Limoges). Data collected at high temperatures by using different means (bending tests, ultrasonic measurements,...) allows the identification of the high temperature behavior of two fused cast materials, produced by Saint-Gobain group for the glass manufacturing industry. The results emphasize the importance of the transformation of zirconia and of the viscosity of the glassy intergranular phase on the mechanical behavior. Damage under the form of microcracking caused by thermal expansion mismatch between the phases is also observed during cooling down at low temperature, when the material is elastic.

Jan 1, 2004

By Tom Setterfield

Monster Copper Resources ?Junior focused solely on IOCG deposits ?Founded by ex-WMC geoscientists ?Properties in Brazil, Wernecke Breccias (Yukon), Central Mineral Belt and Nova Scotia Nova Scotia ?JV with Wallbridge Mining Company ?Ongoing Story ?Presented as a case study in generation and implementation of IOCG exploration program

Apr 1, 2005

By R. Anthony Hodge

Who/what is ?community?? What are most communities interested in, what do they care about? What has happened in the past? What is happening today? What is hoped for tomorrow? What are the lessons and keys to success?

May 1, 2006

By J. Scalise

The paper covers a wide range of topics relative to filtration for continuous cast copper and aluminum. Subjects include system concepts, filtration concepts, system components, filter types, filter media selection, caster water filtration, coolant disposal, and recommended materials of construction.

Jan 1, 2007

By K. Feindel

The distribution of water in operating fuel cells must be carefully managed to optimize the performance, durability, and functionality of the system. For example, the ionic conductivity of polymer electrolyte membranes decreases as membrane hydration is reduced. Flooding at the cathode inhibits mass transport, and it can lead to failure of materials. Build up of liquid water in the gas flow channels of a fuel cell stack will create a non-uniform distribution of pressure drops across the individual cells. We will discuss the application of 1H NMR microscopy to investigate in situ the production and distribution of water throughout an operating H2/O2 polymer electrolyte membrane fuel cell. Polymer electrolyte direct methanol fuel cells posses high theoretical storage capacities as power systems for portable electronic devices. There are, however, two long-standing hurdles to development of practical methanol fuel cell systems. First, the electro oxidation of methanol at the anode of the fuel cell is poisoned by absorbed carbon monoxide, an intermediate in methanol electro oxidation. Second, methanol readily crosses over from the anode to the cathode of the fuel cell. This methanol crossover wastes fuel, and it poisons the electro reduction of oxygen at the cathode. We are investigating use of 2-propanol as an alternative to methanol as a fuel. 2-Propanol is less toxic than methanol, and it is less prone to crossover from the anode to the cathode. More significant, however, is that the electro oxidation of 2-propanol to acetone is faster than the electro oxidation of methanol because it avoids formation of adsorbed carbon monoxide. We will present active catalyst systems for the electro oxidation of 2¬propanol to acetone in fuel cells. We will also present methods to convert the resulting acetone back into 2-propanol, possibly leading towards rechargeable portable fuel cell systems.

Jan 1, 2005

By Anthony Finch

Many mines combine open pit with underground mining, and on many occasions the underground mine is an extension of the open-pit. In these circumstances the decision about where the open-pit stops and the underground starts is crucial and driven by many factors. This paper looks at some of the ways that this cut-over can be calculated and specifically examines the calculation of it using modern mine optimization software. The paper provides a case study which will review various outcomes using these techniques, and demonstrates the influence of various factors on the optimal transition cut-over point. Biographies Mr Finch is a Divisional Manager and a Principal consultant at Snowden Mining Industry Consultants in Vancouver, Canada. At Snowden Mr Finch leads a team of engineers that perform mining engineering studies for projects around the world. Prior to joining Snowden Mr Finch was the Mining Manager at Barrick?s Henty mine in Tasmania Australia. Prior to that Mr Finch has held a variety of roles in both consulting and operations working for various organisations at various levels in the Asia Pacific region. Mr Finch gained a bachelor?s degree in Mining Engineering from the University of Queensland in 1986, and a bachelor?s degree in Economics from the University of Queensland in 1993. His expertise is in mine planning, mine optimisation and mine management. Dr Elkington is a Consultant at Snowden Mining Industry Consultants in Perth, Australia. He is responsible for the design and implementation of Snowden?s proprietary optimization software products. Prior to joining Snowden Dr Elkington completed his PhD in Mine Optimisation at The University of Western Australia, and bachelor?s degrees in Engineering (Hons) and Commerce from The University of Western Australia. He specialises in optimization and trade-off studies, and has consulted on projects across all major commodities and regions.

May 1, 2011

By Chris D. Veldhoen

If you ask most diamond drillers if they have ever encountered methane gas, the answer would probably be yes. This paper explores a serious methane gas explosion that the author experienced while diamond drilling at a northerly Ontario mine. It is hoped that by documenting this event, people may be alerted to the hidden danger posed by confined methane in underground workings. Methane gas tends to be a problem the deeper you get in any Canadian gold mine. Common procedure when encountering methane is to take readings at the collar of the hole and at different lengths from the source. Monitoring continues until the readings drop below 0.25 ppm. Methane is a tasteless odorless gas that is usually locked up in the seams of the rock or is a product of decaying organic material. Occasionally, the gas is released abruptly over a short period of time. Sometimes the gas can continue to vent for months or even years. In small concentrations, methane is relatively safe. In concentrations under 0.25 ppm methane gas is considered safe to work around. Concentrations over 0.25 ppm can become dangerous. During the summer of 2001, Chris Veldhoen was drilling at a gold mine in Ontario. There were three electric hydraulic diamond drills on the 39 meter level, approximately 5200 feet deep. Two Longyear LM 55 drills were about 40 feet apart and another LM 75 was about 2000 feet away. The two LM 55?s were set up to drill holes no deeper than 350 meters. All three drills had been set up on the same spot for more than a month. None of the three drills had ever encountered methane gas in the entire time they had been drilling on the level. On the day shift of July 13 2001, the driller on Chris? cross shift hit a small pocket of gas. He tested the hole and got a reading above 0.25 ppm. He proceeded to rope off the area with a ?DO NOT ENTER - METHANE GAS? sign and a rope denying access beyond the sign. On Saturday, July 14, Chris was instructed to install a Margo plug in the hole that was emitting methane gas. Methane is usually odorless, but occasionally when encountered underground, is accompanied by a rotten egg smell. As he walked to the drill, he could not smell methane gas. He proceeded to test the hole and got a reading of 0.22 ppm methane. This number was in the acceptable range for drilling, but he plugged the hole anyway.

May 1, 2004