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By J. Y. Kim, S. L. Chryssoulis

Lead ions that originate from galena during the processing of complex sulfide ores migrate onto the surfaces of sphalerite and iron sulfide minerals. This results in poor selectivity during differential flotation. Generally, in sulfide ore processing, the lead-activated minerals float in the Cu/Pb rougher circuit. The surface lead complicates the zinc flotation circuit by lowering the concentrate grade. The effect of lead in the differential flotation of sphalerite from Cu-Pb-Zu and Pb-Zu ores is discussed. Plant and laboratory-test data are interpreted by determining the surface compositions of individual grains of sphalerite and iron sulfide particles. For the first time, surface compositions were determined by using laser-ionization mass spectrometry (LIMS) and time-of-flight secondary ion mass spectrometry (TOF-SIMS). Cationic and cationic species on the surface were analyzed to elucidate the phenomena. It was proven that these new techniques are very useful in understanding the basic mechanisms of a sulfide mineral-flotation system.

Jan 1, 1997

By K. G. Sutterer, P. T. Wang, R. Sweigard

One possible alternative for the disposal of flue gas desulfurization (FGD) by-products is to use it as backfilling support material in highwall mine adits. The finite element method was used to analyze the variation in stresses and displacements within and around a highwall adit backfilled with FGD materials. The engineering properties of the rock material and the optimum mix of the FGD materials were obtained from laboratory tests. Finite element analyses show that, for the case in question, the roof displacement would decrease about 48% and the peak stress could be decreased by about 58%. The study indicates that fairly weak FGD materials can eventually lead to the stability of backfilled highwall adits.

Jan 1, 1998

By Michael Francis, Chris Darton

More than 55 km of tunnels have been constructed by TBM in the last 12 years to refurbish and upgrade the high voltage cable network in London. These include a tunnel of 20km length using EPBM machines in both clay and granular soils. Route selection was made with reference to subsurface structures, existing ground conditions, using suitable shaft locations addressing environmental concerns. The complex interfaces to manage included obtaining of consents to the coordination of multiple suppliers. The paper describes how all these challenges have been met successfully and how technology has been employed to provide for safe construction and operation in the congested urban environment.

Jan 1, 2003

By Robert A. Jankowski, Natesa I. Jayaraman, Jay F. Colinet

The U.S. Bureau of Mines evaluated the dust control effectiveness of two-phase flow systems in a full-scale model mine using a mockup of a Joy 14CM continuous mining machine. In a two-phase flow system, air and water flow simultaneously through the nozzle. Air pressure varies from 10 to 60 psi, and water at 30 to 50 psi. Coal dust was introduced at the face, and dust concentrations were monitored at the operator locations and in the return. When compared with a conventional spray system, a symmetrical two-phase flow system reduced dust levels during the box cut by 43 pct at the operator location, and 30 pct in the face return. Dust levels, however, increased at the off-operator position during the slab cut. A directional two-phase flow system reduced dust levels at both operator locations by more than 90 pct in the box cut mode. While the use of two-phase flow systems will reduce respirable dust levels and water usage, it requires an air supply to the miner. Moreover, the ability of the two-phase flow system to redirect the dust cloud makes nozzle orientation a critical factor.

Jan 1, 1991

By F. Grandjacques

INTRODUCTION Selective Reduction of Nickel in Oxidized Ores Oxidized nickel ores, either garnieritic or lateritic, contain much more iron than nickel. The regular carbon reduction in an electric furnace is operated in such a manner that the greater part of iron oxides is reduced simultaneously with nickel oxide, resulting in a low nickel content ferronickel. In order that the nickel content of residual slag may be suitably low, -excess carbon must be fed so that the carbon content of the ferronickel thus obtained is that of casting iron. The metal also contains other impurities such as silicon, chrome, etc. In order to convert the casting iron into slightly carburized ferronickel with high nickel content, the greater part of the carbon and more than half the iron contained therein must be oxidized by means of oxygen. Energy is thus consumed as carbon, and power to reduce iron oxides, and more energy is consumed as oxygen to re-oxidize the iron contained. This method can be economically adopted for nickel ores with grades ranging around 2. 5 to 370, but it gets excessively costly when nickel grade falls below these values. This is why, for nickel ores with low nickel grades and high iron content, studies were conducted to develop a selective reduction process which, while reducing only a small part of the iron oxide, would provide efficient reduction of nickel oxide. Rich ferronickel is thereby obtained, with nickel content ranging around 30 to 50%. Due to the presence of slag with a high iron oxide content, the metal thus

Jan 1, 1979

By Timothy F. Markey, Brian C. Strohm

This paper presents a case study which applies risk assessment techniques in evaluating potential environmental problems associated with past waste disposal practices at a 65 acre non-ferrous metals and metal alloys manufacturing facility. Waste management activities at the site involved a number of surface impoundments for gangue material, neutralized acid rinse waters, acid rinse sludges, demolition debris, storm water runoff, stockpiled ores, and a permitted residual waste landfill. As a result of these activities, the She contained 9 identifiable waste management areas impacted by over 35 potentially hazardous chemicals and metals. Extensive environmental data obtained from investigations at the Site revealed heavy metal and volatile organic chemical contamination in various environmental media. These data were utilized to evaluate potential risks to human health and the environment. The human health risk assessment estimated potential health risks to workers, residents, and Site trespassers under current and expected future uses of the Site. Areas of the Site were identified which were considered to present potential health concerns under the various exposure scenarios. Results from the human health risk assessment were utilized to develop cost effective risk based soil remediation goals protective of the public health and environment.

Jan 1, 1992

By D. R. Tweeton, L. W. Lake

A modified push-pull field test and a computer model of cation exchange were developed to aid in evaluating cation exchange parameters prior to in situ mining. Reliable determination of these parameters is essential when modeling restoration of ground-water quality. The field test involves a much larger volume and much less disturbance to the ore sample than is feasible with laboratory measurements. This test can be per¬formed in two or three weeks. It is relatively inexpensive, requiring one injection-production well and two or more wells for collecting samples of leach solution. The use of the model in interpreting test results is illustrated with field data from an in situ uranium mine. Much of the research was performed by the University of Texas at Austin and was partially funded by the US Bureau of Mines.

Jan 1, 1987

By C. Flores, R. Y. Wan, M. C. Fuerstenau, T. S. Jordan

Most oxidized manganiferous silver ores contain manganese associated with silver and are not amenable to conventional silver extraction methods, including direct standard cyanidation techniques. However, it is known that dissolution of the manganese might yield a suitable material from which silver can be recovered by conventional methods. In the segregation process, which involves heating the ore with a small quantity of salt and with a source of reducing agent to 680°C - 800°C, the silver is volatilized, migrates and is reduced to metallic silver particles. Conventional cyanide leaching is applied to the resulting calcine. Laboratory investigations have been conducted on a manganiferous silver ore analyzing 0.02 % Cu, 0.09 % Pb, 0.33 % Zn, 12.55 % Mn and 187 g/ton Ag to study the influence of roasting temperature and time, quantity of salt and quantity of coke on silver extraction by the application of segregation roasting followed by cyanidation. Cyanide leaching tests were carried out at room temperature on the segregated calcines produced by using an alkaline cyanide solution containing 2.0 lb/ton of NaCN at pH 11 for 72 hours. The results indicated that 97.8 % of silver extraction can be attained at 850°C, with 2.0 % salt, 1.0 % Coke and 30 minutes of roasting time.

Jan 1, 1993

By V. T. McLemore

The Steeple Rock district in New Mexico is a major epithermal gold-silver district that exhibits district zoning. Five types of ore deposits occur within the district: •base-metal veins (with gold and silver) form the center of the district and occur along the Carlisle fault, •gold-silver veins along northwest-trending faults and outward from the base-metal veins, •copper-silver veins along the margins of the district, •fluorite veins along the margins of the district, and •manganese veins along the margins of the district. Areas of older acid-sulfate alteration occur throughout the district and also exhibit the following zoning: massive silica/chert zone (inner), silicified zone and clay zone (outer). This alteration overlies regional alkali-chloride (propylitic to argillic to sericitic) alteration. Synthesis of available data suggests the acid-sulfate alteration is related to a shallow, but older, epithermal hot-springs system. Subsequently, younger epithermal veins formed along faults.

Jan 1, 1996

By Young C. Kim

Determination of the minimum sampling requirements of the run-of-mine (ROM) coal is very important for the purpose of meeting contract specifications. It is also important for the purpose of meeting emission regulations at a coal-burning power plant, such as the one located at Homer City, Pa. The classical statistical sampling theory can be applied to this problem, if ROM coal samples are known to be spatially (or serially) uncorrelated. On the other hand, the estimation variance concept from the Matherson's geostatistics must be used, if the samples are spatially correlated. Conditional simulation technique combined with simulation of the existing mining method is used to determine under which circumstances ROM coal samples do not preserve the spatial correlation. Only after establishing the degree of correlation that exists among ROM samples, an optimal sampling scheme can be devised using either the classical statistics Or the geostatistics. The minimum required sample volume can then be calculated using the well-known Gy's formula. This paper describes the results of the above investigation using the Helen coal mine data of the Homer City Owners. Empirical guidelines for determining the degree of correlation are also provided for coal mine operators.

Jan 1, 1986

By Kal V. S. Sastry

Modeling and simulation are two major tools available to a mineral process engineer for a consistent and systematic process analysis. The application of these tools to the analysis of specific mineral processing unit operations is well documented in the literature; nevertheless, they are used only to a limited extent in the industry. This is because the fundamental principles of modeling and simulation in the context of mineral processing context are not available. This paper represents the first in a series of papers planned to meet this need. General principles of process modeling and a unified mineral process model development methodology are presented. A simple example of model development using the flotation unit operation is given. A discussion of the practical significance, challenges and opportunities associated with mineral process modeling is included.

Jan 1, 1990

By T. E. Walsh

I will address two important alternative energy resources, solar and geothermal, with emphasis on their potential application in electric power generation. As a result of this presentation, I hope to leave you with a realistic view of the principal technology options that are being developed or that are available. Solar Types of Collection In terrestrial solar applications, the biggest challenge is to find ways of collecting the sun’s relatively low intensity energy so it can be converted economically to useful thermal or electric energy. Fig. 1 shows that there are both natural and technological ways of collecting solar energy. In nature we find that solar energy aids in the production of biological growth, rainfall, and wind, all of which can, in one form or another, be put to use in the production of heat or electric power. The sun’s rays also are collected and stored naturally in the form of heat in the upper layers of the ocean which can be put to use in the production of electric energy by means of ocean thermal energy conversion (OTEC) approaches. On the technological side, the sun’s rays can be intercepted by materials that directly absorb and convert its energy to low-grade heat, or by mirrors or lenses that focus the rays onto a material to produce high-temperature heat. The higher temperature systems can be used to drive efficient heat engines in the production of electricityy. The sun’s rays also can be collected on photosensitive materials, in either a direct or concentrated form to generate DC electricity directly. The systems I will discuss employ all of these means of collection and conversion, excluding biological and hydroelectric. The former is too exi

Jan 9, 1980

By Reed S. C. Rogers

The most widely used machines for grinding coal to the sizes prescribed for the pulverized coal firing of furnaces, boilers, and kilns are the vertical ball-race, roller-race and roller-bowl types of mills. However, the increased use of coal has led to an increased use of tumbling ball mills for coal grinding. Specifically, air-swept ball mills are now a part of many dry pulverized coal firing systems, offering the advantages over vertical mills of lower maintenance costs and the ability to handle strong or abrasive (high ash) coals. The current use of wet ball mills is to prepare coal-water slurries for direct combustion, although in time they may also find routine application for preparing slurry feed for coal gasifiers. In either application, wet ball mills ofer the advantages that coal grinding and wetting can be accomplished in a single step, and that the mills are readily used with fine wet screens to assure top size control in the slurry product. The simulation of tumbling ball mills with mathematical models has reached a fairly advanced stage, but the concepts have been applied only recently to coal grinding. As this paper will demonstrate, however, significant progress has been made in the use of models in ball mill circuit design for coal grinding. Included is a description of the techniques used for simulation, recommended parameter estimation methods, and demonstrations of process engineering calculations for large scale coal grinding circuits.

Jan 1, 1986

By Robert H. Marshall

The application of simulation to production planning at a large, complex open-pit mining operation proved to be challenging and enlightening. The mine is divided into two separate pits and several dump areas which are served by the same truck fleet. The operating system consisted of shovels of two different sizes, wheel loaders, and a fleet of three different truck types moving material from seven source locations to ten dumping sites. The interconnecting haulroad network included many common segments. There were operating constraints unique to the system, such as: traffic rules; manpower limitations; shovel, material-type, and destination priorities and production limitations; and a unique, non-centralized dispatching method for truck distribution. The truck distribution was further constrained by the matching of trucks to shovels, loaders, and destinations by truck type. The gathering and transformation of input data as well as the evaluation of results and validation of the model were also challenging. Despite a high level of sophistication in production reporting, some input data were neither readily available nor backed by field observation. As a result, many innovative techniques had to be used to develop realistic input data and to validate the simulation results. Nevertheless, this case study definitely proved the feasibility of applying computer simulation techniques to short and long range mine planning and budgeting at a large, complex mining operation.

Jan 1, 1982

By Yu. P. Astafyev

The, control of drilling and blasting is a complicated dynamic system whose aim is to ensure safety and prepare rock of required grade and the standard level of broken material reserves Unlike other processes drilling and blasting, as an object have the following features: -a large variety of drilling and blasting methods due to specific conditions of blasting, various types of drilling equipment, schemes-of blasting, types of explosives and others; -relative continuity of drilling, the character of mammoth blasts being discrete; -increased requirements to the safety of blasting;; -a great. number of control parameters, some of them having a qualitative characteristic but not a quantitative one; -availability of feedforward and feedback with other mining processes in terms of time and space. These features predetermine the hierarchical structure of an automated system of planning and control of drilling and blasting (fig.1). The system is implemented on the basis of unity of the data base and in interre lation with other problems of controlling mining operations. An automated system of this kind makes it possible to take optimal decisions actually on all the levels and stages of operations, with rock having been blasted before extraction.

Jan 1, 1986

By Sizhe Tan

An open pit mining operation can be considered as a production system with at least two products: ore and overburden (waste). A primary mine planning task is to schedule the production of ore and waste over its life span subject to several technical and economic constraints to maximize some objective such as the overall profit from the operation. Two major constraints are (i) the feasible combinations of ore and waste productions and (ii) the limiting function for ore production as a function of mine life. The task in scheduling production and stripping ratio (ratio of waste to ore production) is to find an ore production curve below the upper bound function of ore production, and a stripping ratio curve within the feasible domain of ore production and overburden removal while maximizing the defined objective. Zn this paper, feasibility of developing computerized optimization models to perform such a scheduling process is explored. Two optimization models are proposed for the task. In the first approach, a linear programming (LP) model is employed and in the second, a dynamic programming procedure (DP) is outlined. In these models, in addition to the consideration of the two major constraints mentioned earlier, various other contributing factors such as interest rate, equipment purchase cost and installation schedule, operating cost, and equipment idle cost are incorporated. An example is provided to illustrate the LP model application.

Jan 1, 1992

By I. H. Keith

INTRODUCTION The following papers describe the extraction of nickel in the form of ferronickel from the Dominican laterites. The Falconbridge process was developed initially in the Falconbridge Metallurgical Laboratories and subsequently in several successive stages of pilot plant operation in the Dominican Republic. In the course of this work we came to believe that there is advantage in piloting on site. Mining, metallurgical and geo-political considerations all have major impact and that belief has been borne out by commercial plant experience. Lateritic nickel ores differ substantially, even within the same orebody, in their amenability to extraction methods. The Falconbridge process takes account of the heterogeneous nature of the deposit. Three years of geological field exploration led to ten years of process development after it was realised that the then known metallurgical processes would not give economical extraction from the Dominican ores. In addition to establishing the viability of a novel pyrometallurgical approach, it was necessary to verify design parameters for a very considerable scale-up to prototype commercial operation. The plant was eventually constructed within the original estimates of time and cost. Unique features contributing to the technical and commercial success of the project are described. Additionally, some bold extrapolation based on pilot plant work, eventually proved to be quite conservative. The mine is not a conventional open pit operation, but is perhaps better characterised as an earth moving job. Novel application of mobile equipment led to great flexibility in the mine, where operation of several mining fronts is essential to maintaining uniformity of ore feed to the plant. The practical aspects of almost total acceptance of the oversize run-of-mine material through a high-capacity unit,

Jan 1, 1979

By F. P. Schwarz, A. J. Erickson, S. M. Weber

The Mount Hope stockwork molybdenum exposit, Eureka County, Nevada, occurs in a small igneous cauldron complex 32 to 38 mybp in age. The deposit is characterized by alteration zones and mineralized shells symmetrically distributed around multiple intrusives. For samples from the 25 000 meters of 1981-82 drilling, an appraisal of error in in-house sample preparation and in commercial assaying has been made. After splitting, drill core is crushed and reduced in volume (8:1 at 10-mesh, 8:1 at 70-mesh, 6:1 at 200-mesh) to supply 25 grams of 200-mesh pulp for replicate analyses. A 0.5 g portion of the pulp is used for dissolution and atomic absorption analyses. Factors which initially generated unacceptable data variances have been minimized by planning, repeat analyses, introduction of standards, and routine monitoring. Assuming that error between replicate assays defines a Gaussian distribution with its average ideally equal to zero, precision (from preparation including core splitting and analysis of 8400 pairs of molybdenum samples) is on the order of + 25%. The error distribution is not biased. Accuracy is approximately 4% lower than absolute as determined by replicate assays of commercially prepared samples.

Jan 1, 1992

By L. G. Tejada, T. Sjursen

In the production of ferronickel at Falconbridge Dominicana's plant in the Dominican Republic the Reduction Plant plays a vital role by partially reducing the nickeliferous oxide ore, and pre- heating the charge to the electric furnaces. Ore is agglomerated in the form of pillow-shaped briquettes which are screened and fed to 12 open-top shaft furnaces. Hot (over 1250°C) reducing gases are partially cooled (less than 1150°C) and introduced through a set of primary tuyeres. The reducing gas rises counter-currently to the flow of solids. A portion of the partially spent reducing gas is withdrawn at the furnace top and recirculated through a set of secondary tuyeres, 1800 nrm above the primary tuyeres. Together with the recycle gas a controlled amount of air is also added to react with the partially spent reducing gas in order to preheat and dry the charge in the upper part of the shaft furnaces. The calcine is discharged through three discharge legs and pusher block assemblies into open-top refractory lined cars. These cars are then hauled to the electric furnace, parked over selected feed ports, and discharged through bottom gates. The furnace exhaust gas is de-dusted in cyclones and then passed through Venturi scrubbers. The slurry is fed to a thickener, filtered, and recycled to the ore receiving hopper in the ore preparation area. Dust generated throughout the plant is collected, wetted to conform with briquette press feed, and recirculated in a controlled manner through the feed system.

Jan 1, 1979

By H. J. Marais, P. C. van Aswegen

The Biological Oxidation (BlOX®) Process for the treatment of refractory gold ores was commercialized in 1988. During the last decade, the technology has developed into a mature, commercially viable process, with five additional operations commissioned, including operations at Sao Bento in Brazil, Harbour Lights and Wiluna in Australia, Ashanti in Ghana and Tamboraque in Peru. With ongoing development, the efficiency and cost effectiveness of the process have both improved, making it an attractive alternative to conventional refractory treatment processes such as roasting and pressure oxidation. The bacterial culture is robust and can withstand the normal fluctuations experienced on an operating plant. The plants are simple to operate, making it ideal for remote areas. The scale-up potential of the process has been proven, and it can be applied to large refractory ore bodies. The process is environmentally friendly. Neutralization of plant effluents produces precipitates that comply with the most stringent environmental regulations.

Jan 1, 2000