Search Documents

By Frank J. Hirner

Economic open-pit and surface mining often call for ever increasing volumes of lower grade materials. So it is important, often critical, to develop precise expense and production estimates for the large electric mining shovels now in use. An electric shovel's basic application is to "shovel up" material, starting at ground level with the dipper moving up into a working face or bank. It's impractical to dig below ground level with a shovel, except briefly or in unusual circumstances. The shovel working face is "the bank," whether the material is dug from natural bed or blasted. The shovel's digging attachment, the boom and dipper handle, is built in standard and long range configurations. A standard digging attachment is normally used for loading into haulage equipment. The long range attachment is normally used for side or hack casting to a spoil pile. It is also used fir loading into haulage equipment placed above shovel ground level, as in some coal loading applications. Shovel clipper size and hauler capacity should he matched so that a hauler can he loaded in three to four shovel work cycles. Five cycles is usually the limit of good practice. If fewer than three cycles are required, the hauler is too small. More than five cycles indicates possible excess harder waiting time for loading, or shovel waiting time for too few haulers. Full dipper loads, including the last dipper or ''pass, " are essential for economical shovel and hauler match. Consistent need for a final partly full dipper to fill the hauler shows an improper match between the two.

Feb 1, 1981

By E. G. Kelly

Because of the nature of the breakage in the Barmac vertical spindle impactor, the 80% reduction ratio is very small, so that when the energy efficiency is calculated by Bond's method, it appears to be very low. However, the product size distribution contains a high proportion of fines. It is argued that the production of these fines accounts for the high energy consumption, and Bond's method is modified to account for this, by considering the crusher to be, effectively, a number of smaller crushers in parallel, each having a different reduction ratio.

Jan 1, 1988

By Dan Walker

The success of the heap leaching process for extracting precious metals from low grade ores in many cases depends on successful agglomeration of clay fines. This paper relates the development of a new agglomera­tion agent, named Leachit, that has demon­strated an ability in some ores to decrease leaching time. Data from a commercial test­ing laboratory is presented to illustrate a comparison of leaching efficiencies with other agglomerative agents, such as lime and portland cement. Conclusions will point out certain advantages of Leachit to the heap leaching gold recovery industry.

Jan 1, 1992

By A. Ferreira Morgado, P. de Souza Santos

The sodium smectitic clays (bentonites), have more industrial applications in that class of mineral, a driving force to obtain this mineral. In Brazil, there are several occurrences of smectitic clays, unfortunately they are polycationic, with a distribution of several exchangeable cations, where the cation sodium occurs in minor quantity. In this work, the original polycationic smectitic clay was firstly proper characterized and then treated with sodium carbonate obtaining homoionic sodium smectitic clay. The rheological tests in the optimized sodium smectitic clay showed good results for drilling fluids, typical of a sodium bentonite ones.

Jan 1, 1999

By James McMaster

The Kamyr Countercurrent Tower Leaching Process is intended to combine, in a single tower, thickening, leaching, separation and clarification of pregnant solution, and washing of leaching chemicals from the tailing pulp. For a gold or silver metallurgical plant, the flowsheet would consist of crushing and grinding, cyclones for size control and partial thickening, the Kamyr tower, and a gold or silver recovery system of either carbon in solution, zinc precipitation, or direct electrowinning. Ancillary systems for the Kamyr metallurgical plant would include cyanide preparation, fiber preparation and recovery, and flocculant preparation.

Jan 1, 1990

By Ian J. Corrans, Gary Johnson, John E. Angove

Activox® is a hydrometallurgical process used to oxidise sulphide concentrates. The process is based on two relatively simple, established unit operations; i.e. fine or ultra-fine milling (UFM) and pressure oxidation under mild conditions. An under-standing of, and ability to control the pulp chemistry during oxidation has resulted in the successful Activox® treatment ( on a batch scale) of a wide variety of sulphide flotation concentrates; • pyrite/arsenopyrite + gold • pyrite/chalcopyrite + gold • pyrite/chalcocite + gold • pyrite/enargite/tetrahedrite + gold Oxidation rates are rapid (1-2 hours retention time) and gold

Jan 1, 1995

Dunn has written an excellent paper providing a wealth of advice on what is often the most costly consumable in the mineral processing plant. As he pointed out, grinding media selection and quality control can play a major role in successful plant operation. Owing to the economic importance of this topic, there are some important factors related to media sizing that I believe merit further comment. Dunn made reference to a slightly simplified version of the Azzaroni (1981) equation and pointed out its successful use for the Henderson SAG and Climax ball mills.

Jan 1, 1991

By Peter S. Schneidkraut

This paper will discuss the Final Tunnel Linings which were placed in 6700m of a 2.32m inside diameter precast concrete lined interceptor sewer tunnel in Staten Island, New York. Two methods were employed to install the final tunnel linings. One method involved forming and placing a polypropylene fiber reinforced concrete cunnette invert, followed by an arch pour. The second method involved the jacking of reinforced concrete pipe into the tunnel, followed by a low density cellular concrete backfill grout. These two methods will be described and compared.

Jan 1, 1993

By Jack K. Lemley

This paper will provide an update of the Channel Tunnel Project including a discussion of the overall legal structure and management organisation. It is important to understand the mission that TML, as a design/build contractor, has undertaken and how the various interfaces have evolved between the other entities involved in the project. The paper will describe the evolution of the management organisation and the approach to completion of our contract, recapping the historic events and moving into a projection of how we will manage the completion of this very large transportation system.

Jan 1, 1991

By Joseph F. Peters

The paper will begin with the physical parameters of design in a wire saw. These will include such things as the type of wire used, abrasives, horsepower of operation, and drive components. It will then go into the many uses of wire sawing in the quarrying and finishing of granite. This will include a step by step program of the removal of a block unit of granite from the quarry site through the finished slabbing and jointing in the plant. After this, there will be a small insertion of possibilities of wire sawing techniques in underground excavation work. This would be speculative only. I will use the example of powerhouse type of excavation work given to me by Dr. John Reed, and try to explain how I would attack this type of work using wire saws. Several slides of both design criteria and actual installations were shown.

Jan 1, 1997

By Matthew J. Hrebar

A comparison of hydraulic shovels (HS) versus front-end loaders (FEL) is commonly made when an excavator with some degree of mobility and medium reach is required. These applications are often found in hard rock open pit and surface coal mining applications, among others. The purpose of this paper is to present a comparative economic study of the two excavators. Production data was collected from both HS and FEL manufacturers as well as operating mines. Availability, operating costs, and estimated operating life were gathered from operating mines, while capital costs were obtained from manufacturers. The data was limited to studies and operations which included both types of mid-size excavators. The economic study is followed by a discussion of other factors considered by mine operators in excavator selection. The study was originally made for a presentation at the 23rd Intermountain Minerals Conference at Vail, CO.

Jan 1, 1992

By J. W. Leonard

A mine's productivity can be significantly increased by using physical and chemical methods to increase the bulk density of newly mined coal. Increases in coal bulk density allows greater amounts of coal to be placed in ships, barges, railroad cars, trucks, shuttle cars and scoops. Increased bulk density can help increase productivity by increasing throughput of container-based, materials-handling systems. Small, easy-to-achieve changes in mining operations are required to obtain the increased productivity. This article deals with chemical methods used to increase coal bulk density. The results and discussion are based on experiments performed in the laboratory. Research at the University of Kentucky using a chemical method shows that an increase of about 15% in bulk density can be achieved using typically small quantities of commercial reagents. This increase in bulk density can produce a proportional increase in the productivity of a mine.

Jan 1, 1992

By Mark L. Mott, Michael P. Synder

The Mine Safety and Health Administration has developed a program to improve the decision making process of personnel involved in mine emergency situations. The Mine Emergency Responsiveness Development Program (MERD) has been designed specifically for fires and explosions in underground mines. This program addresses the responsibilities and organizational requirements that are necessary during rescue and recovery operations of a mine emergency . Specific skills and knowledge are required to manage an organization of personnel under conditions of intense stress, such as a mine fire or explosion. As a result, the MERD program develops these skills by providing role playing emergency simulations. This role playing provides the participants with the opportunity to experience problems, explore solutions and interact with other personalities which may exist during mine emergency situations. This paper presents the standard procedures for the MERD program developed by the Ventilation Division of the Pittsburgh Health Technology Center.

Jan 1, 1991

By Pat Gochnour, Jim V. Rouse

Advances in the design and construction of heap­leach pads and process plants have greatly reduced. the potential for accidental releases of process olut1on. While workers in the field, and regulatory agencies such as the EPA have long recognized that the potential effects of any spills would be short term in nature due to cyanide attenuation and degradation (Engineering-Science, September, 1986, Pyrih, 1990, Rouse and Pyrih, 198, Rouse and Pyrih, 1991 ), unfortunately the general pubhc has held a perception that such a spill would be an environmental catastrophe. Few factual data on actual accidental releases have been available to dispel such a concept. Such data now exist and shoul? be disseminated to show that prompt response, using a combination of chemical oxidation, natural attenuation, and enhanced biodegradation of cyanide, can limit the effects of such rare releases, in both time and space.

Jan 1, 1992

By G. Henry, S. J. Domvile

Arsenic management practices at the Con Mine in Yellowknife, Northwest Territories have evolved over the last fifty years of operations under changing regulatory, economic and technological conditions and incentives. As a result of a processing upset in the mine' s arsenic trioxide reclamation plant circuit in August 1988, arsenic levels in the mine' s tailings pond rose from 30 to over 100 mg V. At these arsenic levels, water treatment operations were unable to meet water licence discharge criteria and the mine itself was under risk of closure due to limited water storage capacity. Under these internal pressures, the mine initiated its own research initiatives designed to restore water treatment operations. The new process developed from the mine's research, utilized the mine's existing water treatment plant hardware but introduced a pretreatment step involving a discrete sludge recycle and removal system. In February 1989, water treatment operations resumed under the new process.

Jan 1, 1992

By Rod Knopp

Each year approximately 5,000 tons of a sulfide concentrate grading 1 ounce gold per ton are produced at this operation. The material is refractory and as shipping costs and custom smelter charges increase, options to process it on site are becoming more attractive. Three methods of treating the ore have been investigated in detail. The first option of ultra fine grinding the concentrate produces a 35% gold recovery with relatively low capital and operating costs. A second option of pressure oxidation is very capital intensive and has high operating costs but recoveries in the order of 95% are achievable. The final option, biological leaching offers both capital and operating costs which are less than pressure oxidation, while still achieving 90% gold recoveries. Bioleaching of gold concentrates has been gaining acceptance but there is a risk factor associated with this or any emerging technology.

Jan 1, 1990

By Ibrahim S. Balbaa, J. Terry Strack, James G. Hopkins

A microwave system for continuously reactivating carbon, used in gold processing, has been demonstrated at a gold mine in Ontario, Canada. The pilot unit produced reactivated carbon at a rate of 12 kg/h. Comparisons with the mine's existing reacti­vation kiln indicate that microwave reactivation technology has several clear advantages over conventional regeneration kilns. Upon completion of the original study, the microwave reacti­vation technology was further developed. An advanced rotary type microwave system that can be scaled up to reactivate car­bon at a rate of 120 kg/hr was designed and smaller pilot-scale equipment was commissioned and tested. Under an agreement with OHT, Harper International Corporation will manufacture, supply, and market the new technology. In addition to carbon reactivation, the rotary microwave system can be used in many other heating applications such as ore treatment, ceramic pro­cessing, and cleaning of minerals.

Jan 1, 1998

By Stephen Young

The continuous monitoring of free cyanide levels is an important part of gold recovery operations. Accurate and up to the moment knowledge of the free cyanide concentration can result in substantial cost savings by allowing reduced concentra­tions with lower fluctuations, while maintaining or increasing gold recovery. Reduced free cyanide levels also result in lower detoxification costs at the mill discharge which translates into further savings while meeting environmental requirements. As can be seen from the upper curve in Figure 1 (which is based on in-service measurements), without accurate monitoring and control, cyanide concentration fluctuates during the produc­tion cycle, and is maintained at a high level to err on the side of caution. The lower curve illustrates the improved control permitted by the installation of a CY ANCOR, giving a more consistent concentration over the process cycle, and safely allowing use of a lower concentration.

Jan 1, 1995

By H. Mercado G., J. R. Parga T

Mexico continues to be one of the main producers of silver, lead and zinc; although this leadership is ending because of the use of obsolete technologies, which is reflected in low recoveries of these processes. The country therefore requires to develop on new technologies in the field of nonferrous metallurgy, particularly be'cause it is the second most important source of foreign exchange. A novel method, presented in this paper, demostrates that refractory gold and silver can be extracted from a complex sulphide concentrate by a one stage pressure oxidation in an alkaline cyanide solution, this is achieved by simultaneous liberation_ and solubilization of the precious metals. Both gold and silver extractions are greater than 97%. Factors affecting recovery efficiency, such as: pH, lixiviation time in the reactor, temperature, particle diameter, pressure, % of NaCN and pulp density, were investigated. A summary of actual plant operations is also be included.

Jan 1, 1993

By R. C. Hopper, A. A. Mathews, T. A. Lang

DESCRIPTION OF PROJECT The Straight Creek Tunnel site is located approximately sixty (60) miles west of Denver, Colorado, on Interstate Route 70 in the vicinity of Loveland Pass, in the Rocky Mountains. The ultimate project will consist of dual two-lane vehicular tunnels with a building at each portal to house mechanical ventilation equipment and other installations. The tunnels run virtually east-west on an ascending 1.64 percent grade for a distance of approximately 8,900 feet, and will pass beneath the Continental Divide at an elevation of about 11,000 feet above sea level. The maximum cover is 1,450 feet and each tunnel is approximately 48 feet wide by 50 feet high as excavated. The work now under construction consists of the North Tunnel, which initially will have two-way traffic. Ultimately it will be the west bound lanes for Interstate 70. The completion of the North Tunnel will be the fulfillment of a long felt need for better communication through the high Rocky Mountains of central Colorado and is a vital link in Interstate Route 70. The early planning for a vehicular tunnel through the Continental Divide began in the late 1930's and between November, 1941 and May, 1943 an exploratory pioneer tunnel

Jan 1, 1997