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By X. Nie

A new one-step process was developed to completely eliminate iron and directly obtain pure Ni, Co, and Cu chloride catholyte from nickel rich matte by low temperature (400 0c) chlorination roasting of Ni, Co, and Cu with HCl and leaching with water (PH 7). The effects of roasting temperature, time, oxygen potential and HCI addition and leaching temperature, pH, H2S04 addition and residue sulphur on the recovery of metals and purity of leaching solution were investigated. More than 99 % of Ni and Co and 95 % of Cu in the matte was directly extracted into the solution while 99.995 % of Fe remained in the residue. The iron concentration in the leaching solution was less than 3.6 X 10-5 mol/L.

Jan 1, 1994

By Michel Grenier, Gopal Kunchur, Stephen Hardcastle

This paper presents the findings of a dust study in a typical fluorspar processing plant. The primary purpose of this study was to identify employees and occupational groups exposed to high dust levels and determine compliance with personnel regulations for regular and extended work shifts. The range of airborne concentration of respirable silica and fluoride compounds in specific areas and on personnel was determined. State of the art dust monitoring equipment and tracer gas techniques were used to measure dust concentration, pinpoint dust sources and map major airflow trends in the mill. Results of the survey indicated silica dust concentrations in excess of permissible limits being produced mainly by crushers at the south end of the building. Tracer gas releases and gas chromatographic analysis further showed that prevailing south to north air currents tended to carry and spread dust produced by the crushing operations throughout the process plant. Airborne concentrations of fluoride compounds measured during the study were always well below the prescribed threshold limit value (TLV) for the contaminant. Recommendations, including a mechanical exhaust ventilation system on crushers and transfer points, scheduled preventive maintenance on existing bar sprays and wearing of personal protective equipment were made which significantly improved the work environment. Further testing conducted after Installation of the dust extraction system revealed significant improvements in most areas of the mill.

Jan 1, 1991

By David D. Rabb

Leaching or solution mining, a relatively simple and economical process for beneficiating metallic ores, is likely to find increasing application in the treatment of low-grade ores that are impractical to mine by any other means. This process may be carried out in two different ways: 1. Dump leaching, where the ore is moved from its original location to be leached at another site. 2. In situ leaching, where the ore is leached in place by introducing the leach solution at the top, letting it flow down through the ore under gravity, and then recovering it plus the dissolved metals it contains.

Jan 1, 1969

By Stryker Magnuson

While probe drills are not strictly necessary for all projects, the incorporation and use of probe drills and pre-grouting adds capability and insurance to boring operations. Water ingress and unstable ground can be resolved before becoming a problem and resulting in costly delays through the use of enhanced, 360-degree probe drilling setups. To do this, proper design of the array of drill ports in the shield, matched to the possible ground conditions, is critical. For ground with exceptional water and instabilities expected, additional probing locations are low-cost additions that can lower risk and increase efficiency. In this paper we will look at recent and ongoing projects including the Lower Meramec Tunnel and Jefferson Barracks Phase 2. We will detail the design of those probe drill arrangements, and our overall recommendations for probing/grouting systems that best suit challenging ground conditions and keep projects running smoothly.

Jun 13, 2023

By Norbert Patzelt, Johann Knecht, Wolfgang Baum

The principle of high-pressure interparticulate comminution has been used very successfully since the mid 1980's for grinding a wide range of different materials. A number of reports about operating experience have already been published. High-pressure grinding rolls (HPGRs) are currently making their debut in the mining industry. Experience is being gained with test machines, particularly for the comminution of hard rock. In the grinding of diamond-bearing ore, (Fig 1) interparticulate comminution has already become the standard for liberating the diamonds from the matrix. The advantages of interparticulate comminution are also recognized for the grinding of concentrates (chrome ore, iron ore). Numerous HPGRs are being used very successfully in this field. A testing plant for first-time industrial grinding of coarse, very hard and highly abrasive copper ore was built at Cyprus Amax's plant in Sieretta, Arizona (Fig. 2). The operating experience gained here showed that the grinding of very hard ores places particularly high mechanical demands on the mill. While the machine itself meets the high availability requirements, the wear-protection system proves to be the most sensitive point. Naturally, the properties of the ore to be ground exert a considerable influence on the lifetime of the grinding rolls. This paper describes the wear mechanisms and the wear­protection systems designed to combat these.

Jan 1, 1997

By Maurice Deul

Certain health and safety hazards occur entirely unexpectedly in some subterranean excavations. Although ground support is not the subject of this paper, ground failure can result in large and often uncontrolled flow of fluids into an excavation. Even when there is no ground failure, the disturbance of nature's equilibrium between rock or unconsolidated alluvium or rubble and the contained fluids poses severe problems to a well planned operation. Optimum conditions for safe operation cannot be the sole criterion for site selection. Some mineral deposits form in zones of structural weakness, others form where hydrothermal alteration substantially weakens the enclosing rock, and tabular deposits such as coal and evaporites inevitably undermine large areas. Excavation to acquire mineral values cannot be relocated. The same is often true for tunnels driven to connect distant points by the most direct route. Rivers and mountains cannot he avoided, and the cost of lengthening a tunnel--by even a fraction of a percent--must be strongly justified. No responsible engineer will knowingly select a dangerous route for excavation, but to what extent do engineers attempt to assess the health and safety hazards that may be reasonably expected? How, specifically, can methane explosions, water and sand flooding, dangerous dusts, toxic gases, thermal shock and radar poisoning be eliminated or minimized through systematic advance planning?

Jan 1, 1974

By S. A. Bunk, W. P. Wood

In the early 1980's BHP identified several potential gold deposits in West Africa. One of these deposits was located in Mali, near the village of Syama. As a result of extensive explo­ration activities, an oxide ore as well as an underlying sulphide ore was identified. After agreement with the government of Mali was reached the development of the deposit was undertak­en. The plan for the development of the mine included the treat­ment of the oxide ore followed by the treatment of the underly­ing transition and sulphide ore. The development of the deposit was extremely aggressive. Following the approval of the project in early 1989, engineer­ing was started, equipment purchased sitework was started, and the first ore was introduced in December of 1989. This was accomplished in spite of the difficulties of the site. These diffi­culties included: • remote site location without air or road or water access • no existing infrastructure including water, power, or communication • high health risks • limited construction and manufacturing support in West Africa The operation began with a conventional crushing/grind-ing/CIL/elution and electrowinning facility. The facility was designed to treat 2000 metric tonnes of ore per day. After start­up in December of 1989, the operation was improved to the point that plant throughput was averaging nearly 3000 tpd and running at 92 to 93% availability.

Jan 1, 1996

By Lyman H. Hart

Michiquillay is a major copper deposit situated about 70 km (44 miles) northeast of Cajamarca in northern Peru (Fig. 1). It occurs largely in quartz monzonite in a shatter zone produced by the intersection of northwest- and northeast-trending fault systems. The geology is described by Hollister and Sirvas (1974). The ore deposit was drilled in 1963-1964 by Asarco, with results indicating a resource of 575 Mt (634 million st) averaging 0.72% Cu-0.03% Mo. A decision to bring the project to production has been deferred because world capacity to produce copper has been more than adequate to serve world requirements since 1964. The chain of events leading to the discovery of Michiquillay was set in motion by a decision by the management responsible for the Chilete mine to undertake an investigation of the surrounding area for a possible supplementary source of mill feed to bolster its decreasing lead-zinc reserves. Chilete, located 100 km (62 miles) inland from Pacasmayo, is the most northerly, important mining project in Peru, and little was known of the mineral potential north and east of that point. Relatively unimpressive reports of Colonial silver mining had attracted little investigation, and little was known of the regional geology. One study by Benavides (1956) had been made of the Cretaceous in the region of Cajamarca.

Jan 1, 1991

By Michael L. Nave

An existing coal mine's raw coal 60 inch conveyor system had become productivity bound by a capacity of 3,500 tph. The existing conveyor drives were fixed speed wound rotor induction motor drives installed in 1983. The fast track upgrade installed variable speed medium voltage variable frequency drives to speed up the conveyor to a capacity of 5, 000 tph. The installation took place over a one week system shutdown during Christmas 2000.

Jan 1, 2002

By M. C. Fuerstenau

With increased emphasis on controlled blasting, which is the first and least-costly stage of comminution, ore grindability and plant throughput can be increased by 5% to 10%, and energy savings of up to 10% appear possible. Crushing and grinding efficiencies are presented for ore blasted under regular and adjusted field conditions. An economic analysis of drilling and blasting through crushing and grinding is presented, suggesting that cost savings approaching 10% may be achieved

Jan 1, 1997

By M. A. Candia

Stability analyses were performed on the La Libertad, Nicaragua existing tailings embankment in order to determine the conditions for the minimum buttressing required for stability of the dam as a short term measure. Two critical sections, shown in Figure 1, were investigated under static, drained and undrained conditions for existing and modified geometries. The existing geometries reflect the "as built" topography of the dam, and the modified geometries reflect the implementation of a toe berm to buttress the slope. For these geometries drained and undrained conditions as well as different elevations of the toe berm were evaluated against a factor of safety.

Jan 1, 1996

By Charles G. Zink

Early anthracite "deep mining" methods, production, manpower. underground transportation, labor, safety and reserves are reviewed and compared to the present and to future requirements which must be met in order to economically win the fourteen million tons of untapped reserves and to keep the product competitive in the market place.

Jan 1, 1971

By George M. McArthur

General Statement In Montana, as in most states, the requirements for water quality control are becoming more restrictive. What was once accepted practice is now obsolete. The planning and construction of water quality control facilities has taken on new importance. Past practices and new ideas must be examined to meet the challenge. By this paper we hope to encourage the exchange of ideas for the improvement of water quality control techniques. Both the mining industry and governmental agencies should benefit from such an exchange. The following is a summary of the work done and in progress by The Anaconda Company in Butte to provide an improved water quality related to production processes. We invite your comments. Acknowledgements This paper would not have been possible without the efforts of many individuals and departments in The Anaconda Company, including the Environmental Engineering Department, Mr. Frank J. Laird, Director; Montana Operations, Mr. M. K. Hannifan, General Manager, and their assistants.

Jan 1, 1972

By E. T. Pecina

Bioleaching is a viable option for the processing of auriargentiferous refractory ores with high arsenic content. The application of mesophilic (A. ferrooxidans and ?L. ferrooxidans?) and thermophilic bacteria of the genus Sulfolobus (S. solfataricus and S. acidocaldarius) as oxidant treatment before the cyanidation of an industrial arsenical pyrite concentrate is presented. The results show that extraction of gold and silver increases due to bio-oxidation caused by mesophilic bacteria and results in a maximum gold recovery of 68%. In all strains studied, biooxidation resulted in an average silver recovery of 50%. The results showed that all evaluated strains were sensitive to solids content (5 to 20%) and average particle size (75 and 38 µm) of the concentrate.

Jan 1, 2010

By G. G. O. O. Uwadiale

Starting from a crude ore assaying 45.6% Fe, a fine-grained oolitic iron ore was concentrated by the oil agglomeration technique to 90% Fe recovery and 65% Fe assay. The ore required grinding to minus 5 µm to effect adequate liberation, and the technique yielded optimum results at pH 9. The roles of pH, collector, and bridging liquid concentrations on selectivity and yield of iron minerals in the concentrates are discussed.

Jan 1, 1991

By S. A. Abetel Sabour

In this work, the block theory was applied to determine the safe limit of the angle of face slope at Limestone quarry of Assiut cement company in order to decrease the occurrence of dangerous potential key blocks. Four joint sets were observed and measured at the face. Computer program based on the vector analysis technique was developed to determine the removable block codes. Stereographic projection was also used in this work to determine the removable block codes and to calculate the maximum limit for the angle of dip of the free face, which was found to be 77°.

Jan 1, 1998

By Earl H. Miller

The United States Potash Company was the original discoverer and first producer of under-ground mined potash ore in North America and commenced active production of potash in 1931. In July 1956, the company merged with United States Borax & Chemical Corporation and is now a Division of that corporation. The mine is located twenty-two miles east of the city of Carlsbad and the refinery is located sixteen miles south of the mine, The mine was placed where the ore was found and the refinery placed where there was sufficient water for a dissolving and re-crystallization plant. For twenty-three of the last twenty-six years, the potash ore was mined with the room and pillar method, taking approximately sixty percent extraction and leaving forty percent in pillars. These pillars are generally fifty-eight feet by fifty-eight feet square. Three years ago, it was decided that removal of as large an extraction as possible from these pillars should be commenced.

Jan 1, 1958

Shallow ore deposits are mined by surface methods but a depth is reached in the case of most deposits after which underground methods are applied for the extraction of the remaining ore. The determination of this depth and its analysis is the subject of this paper. In order to determine transition depth from open-pit to underground mining on the basis of the allowable and economically feasible overall stripping ratios, an economic-mathematical equation is first introduced. Using the achieved equation and an analytical procedure on a particular two-dimensional hypothetical tabulate deposit, an effective formula is then established. The formula introduced here, together with the procedure adopted, could be used in all similar mining situations by the mining design engineer.

Jan 1, 2010

By H. K. Lin

During slow-cooling crystallization of iron-making blast furnace slags, most rare-earth elements in the feed recrystallize as cerite-calcium while scandium and europium concentrate in a sheet-like "mineral". The mineralogy of this "mineral" is studied with one of the objectives being the extraction of the "mineral" from the slag for recovery of Sc and Eu. This "mineral" has been identified as one of the mica group minerals and can be named as rare-earth-bearing barium fluorophlogopite. The mineralogical characteristics of this "mineral" are investigated and discussed. This "mineral" can be effectively recovered from the slag by flotation with dodecylammonium acetate or a combination of dodecylammonium acetate and sodium oleate as a collector.

Jan 1, 1996

By Éder Domingos Oliveira, Carlos Antonio Morais, Ruberlan Gomes Silva

The objective of this work was to assess the influence of parameters such as residence time, solid content, and temperature in a process route towards purified rare earth liquor which could be adequate to produce marketable rare earth products. The steps of the process route proposed in this study comprised water leaching of a sulfated rare earth ore and removal of impurities through the purification of the rare earth sulfuric liquor, which is the product of the water leaching step. The sample used in the water leaching experiments was a sulfated rare earth ore produced by the reaction of a beneficiated rare earth ore with sulfuric acid followed by roasting at 700 °C for 2 h in a muffle furnace and cooling at 20 °C. The water leaching experiments showed that the best condition comprised a residence time of 30 min, temperature of 20 °C, and solid content of 10% w/w, resulting in a recovery of 71.3% of the rare earth elements (REE) and a lower impurity extraction, e.g., only 15.0% of Fe, representing the main impurity in the rare earth ore. Even when presenting low amounts of impurities, the rare earth sulfuric liquor still needed to be purified before it can be used in the production of marketable rare earth products. In the study, the rare earth sulfuric liquors were purified in two consecutive neutralization steps, first by dosing the limestone pulp to pH up to 3.5 and secondly by adding the lime pulp to raise the pH from 3.5 to 5.0. The application of two consecutive purification steps at 20 °C resulted in the highest overall REE recoveries (65.4%) throughout all the steps of the process, being 71.3% in the water leaching, 99.6% in the partial purification with limestone pulp, and 92.1% in the purification with lime pulp at 20 °C. Under this condition, there was a total elimination of Fe, P, and Th and a significant reduction in the Al, U, and sulfate concentrations in the purified rare earth liquor. The purified rare earth liquor attained through the experiment is expected to be amenable to be used in the production of marketable products due to the lower impurities/REO mass ratios.