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By Kostas Fytas, Sebastien Perreault

This paper presents EOLAVAL, an integrated mine ventilation design software. In its new expanded version it is a user friendly and fully interactive computer package. The features of the new version are a graphics interface fully compatible with Autocad files, an integrated database of fan characteristics and the optional use of the thermodynamic approach in carrying out network simulations. This software can be used in underground mine ventilation planning: mine ventilation network analysis and simulation, economic design of airways, auxiliary ventilation design, calculation of a mine air heating plant, and evaluation of the natural ventilation and pressure losses in a mine shaft. This paper presents a case study illustrating the use of the computer package in mine ventilation design.

Jan 1, 2002

By James F. Lemons

The potential production of cobalt from nickel sulfide deposits in Canada, from nickel laterite deposits in the Pacific Islands, and from the copper deposits of Zaire and Zambia will be a function of the cost of recovery of the primary nickel and copper products. This cost of production varies significantly for these deposits and is related to the differences in the cost of labor, energy, and supplies, to production technology, and to the grade and recovery of nickel, copper, and cobalt. This Bureau of Mines paper investigates these cost and technology differences as they relate to the cost competitiveness of the deposits in Canada, Zambia, Zaire, and the Pacific Islands.

Jan 1, 1984

By I. Yu. Melekestseva

Two types of hydrothermal massive sulfide fields were discovered in the Mid-Atlantic ridge (MAR) in the last twenty years. The first type associates with basalts and includes the TAG, Snakepit, Broken Spur, Lucky Strike and Krasnov hydrothermal fields. The second type is related to ultramafic rocks and represented by the Logatchev, Rainbow and Ashadze hydrothermal fields. In 2007 a new, probably, the largest cluster of hydrothermal massive sulfide field on the MAR (Fig. 1), related both to basaltic and ultramafic rocks, was discovered at 13°31'N of the MAR (Beltenev et al., 2007). [ ]

Jan 1, 2008

By B. Hearn, O&apos

Falconbridge, Ltd. operates six mines (the strathcona, Fraser, Lockerby, Onaping, East and Kidd Creek) in the Sudbury and Timmins districts of northern Ontario (Fig. 1). These mines vary in depth to approximately 1500m and experience a wide variety of ground conditions. Problems of greatest concern include rockbursting, backfill pillar stability, wall and pillar stability, and the use of cable anchors. A study was initiated approximately two years ago to identify how numerical models could aid in the examination and possible understanding or solution of these problems. This paper discusses the use of numerical models at Falconbridge and describes a case history of their use in examination of rockbursting at the Strathcona Mine.

Jan 1, 1988

By S. K. Kawatra, S. Valluri

With increased CO2 emissions from steel and coal industry, there is great opportunity to capture CO2 and utilize the captured CO2 for economic advantage. The primary goal is to develop energy-efficient processes that reductively couple CO2, an abundant and renewable carbon source, for the production of value-added chemicals such as methanol, ethanol, and oxalic acid. These chemicals can be used elsewhere in the refining process or sold as valuable by-products. Geological sequestration, in comparison, has no economic return. Current CO2 utilization research at Michigan Technological University focuses on electrochemical reduction of CO2. Electrochemical reduction of CO2 to hydrocarbons and other chemicals is a complex multistep reaction with adsorbed intermediates. The exact reaction mechanisms leading to various products are not clear from the literature to date and will likely change over the range of conditions like pH, electrode potential, electrolyte medium, catalyst, etc. This paper will present different ideas and their viability to utilize CO2 as a feedstock to produce several value-added compounds. INTRODUCTION Carbon dioxide (CO2) emissions into the atmosphere will need to be drastically reduced to curb the various undesirable effects of climate change. The large contribution in total CO2 emission originates from coal or natural gas power plants, and a considerable amount from steel plants. Average CO2 emissions in the US from steel industry is 2.9t CO2/t steel (Global CCS Institute 2013). Capturing the available CO2 from the steel and coal industries for economic advantage is a win-win situation for the industry. This technology is not only important scientifically but is also vital for a sustainable future. The various ongoing investigations can be categorized as biochemical, thermochemical, photochemical, and electrochemical approaches. Among these, the electrochemical method shows the most promise as an efficient form of CO2 conversion technology, because of its many advantages like high reactivity under ambient conditions and good extensibility from small- to large-scale processes1 BACKGROUND Extensive research has been done on the chemistry of transforming carbon dioxide into more useful products. Methods are known to convert carbon dioxide into a wide variety of substances, including methanol, isobutanol, carbohydrates, methane, carbonates, urea, formic acid, oxalic acid, carbon monoxide, epoxides, formaldehyde, and so on. Several of these (carbohydrates, formaldehyde, isobutanol etc.) are primarily results from biological processes. The rest are results of strong reduction reactions or electrolytic reduction. In short, electrolytic reduction can be used to form methane, methanol, formic acid, oxalic acid, carbon monoxide from carbon dioxide2. CO2 reduces at the cathode in an electrolysis cell. These processes have the general form of generating the carbon dioxide anion radical (2⋅−) and allowing it to react with itself or the electrolyte3. Catalysts can be added to influence the formation of the anion radical or to suppress side reactions3. The electrolyte, catalyst, voltage, electrode material and CO2 content are all known to effect the reaction pathway. Table 1 shows the overall reactions and energy requirements for electrochemical conversion of CO2 to chemicals

Jan 1, 2019

By Robert Dunne, Paul Gelfi, Vernon Martins

The New Celebration Gold Mine is located 32 km south of the regional mining centre of Kalgoorlie. The current mill throughput is 1.7 million tonnes per annum with a gold production of around 120,000 ounces per year. The main source of ore for the mill comes from the Hampton Boulder and Pernatty pits. Over the last two years the oxide reserves from these pits have been depleted and the harder primary sulphide ores are now being processed. This change has led to a decrease in cyanide extractable gold.

Jan 1, 1991

By Pierre Louis, Jacques Duparque

ACTIRED is a new process for gold and silver elution from activated carbon based on the addition of hydrazine, needing no extra investment and which generates a systematic increase in elutions kinetics. This process either operates at a lower temperature and maximizes financial gain or reduces elution time or operates at a compromise between these two options taking into account the needs of each plant. Industrial use of the process at SNC Lastours, France (Zadra elution column 3,5 bars -125°C) has proved at 95 ° C the following points:

Jan 1, 1995

By G. C. Kachel

During the past two years, there has been an increasing acceptance of process automation among ferrous, non-ferrous and non-metallic rock processing operations in an attempt to keep total unit costs in line in a market situation where labor and material costs are rising almost daily. Previous technical papers (1) (2) (3) (4) (5) have described, in considerable detail, instrumentation and automatic control devices that have been successfully applied in a wide variety of crushing and grinding facilities. While many of the basic control philosophies that evolved almost ten years ago remain essentially unchanged, new components and devices have been developed during the past two years that permit these philosophies to be better implemented in operating plants. Some of these devices and their application will be discussed with particular emphasis placed in describing the basic control philosophy employed as well as some of the hardware or components comprising typical crushing and grinding circuit control systems. Before any instrumentation or automatic control system can be successfully devised for a specific facility, there must be a clear understanding and agreement by supplier and user as to the control system objective. In the case of a crusher feed rate control system, the objective is generally to maximize thru-put of a given finished product size. While this is often the case in a grinding circuit automatic control system, the reasons may be entirely different. Taconite processors whose end product is to be pelletized, generally attempt to control their grind within narrow limits to optimize balling action. Other milling operations are more concerned with obtaining metallurgical liberation and can, in many cases, tolerate wider swings in finished grind.

Jan 1, 1969

By Bradley V. Nelson

A number of improvements in the ventilation system at the Henderson Mine have been made during the past several years. A key to these improvements was the installation of a computerized monitoring and control system. Employees can determine the status of any of hundreds of devices in seconds through the use of this monitoring system. Mine dewatering pumps, the water treatment system, the ore haulage system, electric power usage as well as other devices are controlled and/or monitored. Ventilation parameters which are monitored include air flow volumes and carbon monoxide as well as the status of main surface fans, mine doors, and ventilation raise doors. Main underground fans are also constantly monitored and can be controlled remotely. These underground fans can be programmed to automatically start and stop to follow work schedules, optimizing air quality while reducing power cost. Mine air heating costs have been reduced by replacing an electrical resistance heating system with a direct fired natural gas heating system at the portal of the ore haulage tunnel.

Jan 1, 1995

By Patricia O. Milley

Two years ago, AlliedSignal embarked on a journey to improve QUALITY. However, the focus of this endeavor was on the CUSTOMER and not the traditional product focus. It wasn't that a focus to improve product quality wasn't fruitful in the past. We've practiced it in the chemical industry for many years with significant results. But our industry today is in a survival mode and yesterday's way of doing business is simply not good enough. In the mining industry, we have to make lug strides in how we do business or face losing our customer base. As you are well aware, other parts of the world are importing our technology at a rapid rate. We must work smarter to stay ahead of our customers ever more demanding need for higher quality at lower prices. With this as a driver, throughout the Corporation we reviewed in depth how we support our customers to keep them competitive and sought to eliminate work which did not help them reach this goal. Our first year of emphasis was on tools: how to hold meetings, gather data, and how to make decisions. This sounds very basic, I know, but you can't begin to imagine how productive meetings can become when you start with an agenda and prework delivered days in advance, and agree at the start of the meeting what should get accomplished. In the second year, we applied these tools to our work processes. We mapped how we do our work, scrutinized each step for value to the customer, and then set to work on how we could do things better. The areas we concentrated on were customer linked commercialization of new products, manufacturing and materials management. Our discussion today will focus on the commercialization of new products.

Jan 1, 1994

By Barry R. Doyle, Ilsley Roger C., John Ramage

It was anticipated that settlement would occur when tunnels were excavated in weak organic soils with high groundwater levels in downtown Milwaukee. Because of the potential for damage to adjacent buildings, an approach was devised during the design to address this issue. In order to do so effectively, estimates of settlement trough geometry were made; buildings identified which were potentially at risk; the means of settlement measurement designed; and threshold limits of settlement and courses of action specified. Bid items were provided for underpinning the critical structures. The approach addresses the design issues and delineates the sharing of risk between the owner and contractor. The predicted and actual performance experienced are also discussed.

Jan 1, 1989

By O. Fernandez, M. Vesely

Abrasive grinding, leading to ultrafine product and "critical size" material buildup inside the mill, is proposed as the cause of high power consumption and low capacity in many fully autogenous grinding processes. Addition of steel balls (hence, semiautogenous grinding) or pebble removal and separate crushing have been used, with different efficiencies, to overcome the problem. Information and data for the conceptual analysis, basic design, and operation of a pebble crusher at the Los Bronces semiautogenous grinding plant is presented along with data showing a production increase of 1000 t/d (1100 stpd) and significant operating costs savings.

Jan 1, 1987

By Dennis V. D’Andrea, Peter G. Chamberlain, James J. Olson, William C. Larson

Blasts designed for in situ copper leaching must produce adequate fragmentation and permeability for successful leaching. Copper recovery depends to a large extent on the particle size distribution created by the blast, the permeability in the blast- fractured zone, and the ability to maintain solution flow with a minimum amount of channeling. This paper presents the results of Bureau of Mines experiments where core drilling was used before and after blasting to establish the degree of fragmentation. Data are presented from tests at the Sierrita mine of Duval Corp., and also from tests at the Emerald Isle mine of El Paso Mining and Milling Co. Copper recovery is predicted from fragment size distribution data using a computer model. Data from several blasts are used to show how predicted copper recovery is related to powder factor.

Jan 1, 1977

By D. J. Crawford

The Lucerne Valley Operations of the Minerals, Pigments and Metals Division of Chas. Pfizer & Co., Inca, are located about 5 miles south of the town of Lucerne Valley, California. These operations consist of several limestone quarries, a whiting plant which produces finely pulverized limestone products, a-kiln which produces granular quicklime and lime products, and maintenance shops, warehousing, shipping, and office facilities. Construction of the Lucerne Valley plant began in 1961 as the result of a decision to utilize large undeveloped reserves of limestone in that area. Quarry development was started in the following year; and by 1965, Lucerne Valley had become the principle limestone and lime facility of the Western Operations of the Minerals, Pigments and Metals Division.

Jan 1, 1967

By R. A. Wyman

What unusual features are there about finding, winning, and using the industrial minerals of Canada which may be of interest and yet not widely known. Have you, for example, ever wondered where the raw material for those distinctive greenish grey statuettes, so readily recognizable as Eskimo carvings, comes from? Although stone suitable for carving is obtained at several northern locations, in recent years the Federal government, the Quebec government, and one or two private companies have shipped supplies of various rock types from other sources to central distribution points in the Canadian north for the express purpose of providing Eskimo artists with raw materials for carving. Canada is well endowed with industrial minerals, the extent and variety of which may be observed by a perusal of Table 1. In this table, materials currently produced are shown in the left-hand column; materials which are bordering upon economic viability are listed in the middle column; and materials which have been found in Canada in possible exploitable quantity, but for which [ ]

Jan 1, 1970

By K. P. Madhusudhanan, R. K. Bhatia, K. S. Narasimhan, R. N. Singh

A typical case study of a coal washery of capacity 500 t/h raw coal input has been presented and discussed with particular reference to the techno-economics for flotation column vis-a-vis the conventional flotation cells, keeping parameters like input capacity and product ash same. The results presented indicate that substitution of flotation cells by columns in a coal washery results in advantages of increased fine coal recovery, better quality of concentrates, lower capital and production costs etc.,. The effect of increasing the specific capacity of the column by design modifications on the cost benefit is also analysed.

Jan 1, 1988

By James L. Vanderbeek

INTRODUCTION Semiautogenous (SAG) grinding technology first started to be seriously considered for comminution circuit design in the mid-1960s as an alternative to the three-stage crushing circuits and rod-ball mill circuits in vogue at the time. Since this time the application of SAG mill technology has become widespread with over 250 mills larger than 20 feet in diameter sold (Jones 2002). The vast majority of concentrators constructed over the past quarter century have utilized SAG mill technology, and a SAG-based comminution-based circuit is generally the first choice considered for new projects. Since the first generation of SAG milling technology was applied, many lessons have been learned, and new supporting technologies have emerged which make the design, installation and operation of SAG &-based grinding circuits more robust and efficient. This paper will discuss the current status of SAG and associated technologies. MILL MECHANICAL DESIGN ISSUES Table 1 summarizes the manner in which SAG design capability has evolved over the past 30 years. Increases in mill diameter came slowly as the industry took a wait-and-see attitude as the technology of larger mill diameters was advanced. The first 32-foot- diameter mill was ordered in 1969. It was not until 1979 that the technology jumped to the 34-foot-diameter mill and 1988 for the first 36-foot-diameter mill. The first 38- and 40-foot-diameter mills were both ordered in 1996. At least five 38-foot-diameter and two 40-foot-diameter mills will be in operation by mid-2004. Advances in structural analytical techniques and increased computational power, coupled with field measurements of large operating mills, have increased the confidence of the mill suppliers in their designs and the operating companies in the viability of larger diameter mills. No failures of a 36-foot-diameter mill or larger have been

Jan 1, 2004

Lack of selectivity in mixed mineral flocculation can be attributed to one or more of the following factors: dissolved ion interference, heterocoagulation, mechanical entrapment in flocs and entrainment of fines between flocs. In a study of apatite- dolomite system, it was determined that dissolved ions do not have a significant effect on selectivity. Heterocoagulation was minimized by choosing proper process conditions and addition of a dispersant. Mechanical entrapment was proved to be insignificant and efforts were made to reduce entrainment by choosing an appropriate method of separation of flocs from fines. A new factor termed "polymer induced entrapment" which occurs due to limited affinity of the polymer to the mineral which is not flocculated is postulated to be the cause for the loss of selectivity.

Jan 1, 1986

By Joel Nonnweiler, Galen Samuelson Nagle

The Sacramento Regional County Sanitation District (SRCSD) has undertaken an interceptor expansion program to meet future wastewater needs associated with projected growth over the next 20 years. The Lower Northwest Interceptor (LNWI) will include over 17 miles (27 kilometers) of pipeline including 14 miles (23 kilometers) of dual force main ranging in size from 54- to 60-inch (137- to 152-centimeter) diameter and 3 miles (5 kilometers) of 120-inch (305-centimeter) diameter gravity pipeline. The estimated capital cost for the program is $331 million, with approximately $236 million in construction cost (as of November 2002). The project includes 4,700 feet (1,433meters) of tunnel including 2 crossings of the Sacramento River and one crossing of the Barge Canal, and 11 other smaller tunnel crossings beneath various creeks, sloughs, highways, and railroads. Preliminary design of the tunnels for the LNWI are discussed in this paper. The overall purpose of the preliminary design was to sufficiently define the project to allow planning level cost and schedule estimates to be performed. There have been changes to the project during final design including pipe sizes and configurations, tunnel and pipeline lengths and anticipated flows. This paper addresses only the preliminary design of the LNWI tunnels. Final design issues and changes made since completion of preliminary design are not addressed in this paper.

Jan 1, 2003

By D. T. Kirkwood

The practice of impounding mine water and liquid fine waste in underground mines is increasing. Often these underground impoundments are created by constructing seals or bulkheads designed to withstand the expected hydraulic pressures. Occasionally seals are built for another purpose, usually to act as explosion-resistant ventilation barriers. Due to factors such as clogged drain pipes or unexpectedly high inflow rates, these explosion-resistant seals sometimes become subjected to hydraulic pressures. The incidence of seal failures due to inadequate design and/or construction is also on the increase. Fortunately, to date, no lives have been lost by water seal failures, but a clearer understanding of the design and construction considerations specific to water seals is vital to keep this from occurring in the future. This paper presents technical considerations for the design and construction of seals which will specifically be required to withstand hydraulic pressures in underground mines.

Jan 1, 1995