Search Documents

By Silvia H. M. Grimaldi, Afonso H. Martins

The scope of this experimental work was to study the yttrium extraction and stripping behaviour in a solvent extraction system with mono(2-ethylhexyl)2-ethylhexylphosphonic acid (IONQUEST 801) in a chloride system The study was performed for only one contact between organic and aqueous phases The experiments were carried out according to a factorial design. Due to the statistical analysis and its experimental proof, the optimum conditions for maximum yttrium loading into the organic phase of the extraction stage were 16 minutes for time of contact between phases, 980 rpm of stirring intensity and pH=2.3 for the aqueous phase of the sovent extraction system. The optimized experimental conditions by the statistical approach for the stripping stage were: time of contact between phases equal to 20 minutes, 1050 rpm of stirring intensity and 1.75 M HCI into the stripping aqueous solution.

Jan 1, 1995

By Alfredo P. Vargas

Industrial flotation of sulfide ores is 80 years old. It has gone through many advances to date. However most flotation operations are still struggling to improve performance, which as a worldwide average is at the 90% level. What can be done to push the ceiling to 95% or better without performing finer primary grind, nor without duplicating flotation plant capacity? Such "unique task" can be performed by the low volume high capacity new flotation equipment known as the JAMESON CELL, when used as, "post-scavenger" of final plant tails. Improved efficiencies are obtained mainly from two cases: -Particles which never contacted a bubble. -Particles sheared-off by cell turbulence due to reduced number of hydrophobic sites. The application reverses conventional trend of using large volume mechanical cells by trade-in with smaller efficient equipment: resulting in reduced capital expenditures and operating costs. Outstanding "pre-rougher" applications are also presented.

Jan 1, 1993

By A. A. Kornyshev, M. Burstein, S. T. Hall

The surface "roughness" of mineral particles has long been known to influence the fundamental process of particle-bubble attachment and other subprocesses in froth flotation. The physical nature of the surface of fine mineral particles can be analysed by determining their fractal geometry. A number of techniques are available to measure the fractal properties of mineral particles, these include gas adsorption, mercury porosimetry, neutron or X- ray scattering and image analysis. From the resultant Richardson plots or their Fourier-space analogs, the fractal dimension of flotation feed and product samples can be determined. Textural characteristics of particles have an influence on the stability of 3-phase flotation froths and the selectivity of recovery in the froth. Decrease of the equilibrium froth height for particles of higher fractal dimensions was experimentally established. The induction time of quartz particles of different fractal geometry has also been studied.

Jan 1, 1995

By William Mark Hart

Newmont Mining's executive management launched an initiative in 1999 that was designed to engage the entire workforce in a continuous effort to systematically drive inefficiency out of the corporation. Built on a foundation of teams and teamwork, Gold Medal Performance (GMP) has had a significant and positive impact on the reduction of costs. At the same time, it has increased productivity, improved cash flow, and helped Newmont to further enhance health and safety programs. Currently, more than a hundred teams are working on improving line-balancing production and external communications at all levels of the corporation. The training and rigorous set of tools avail- able to and used by these teams were designed to help them improve communications, identify inefficiencies and their financial impact, develop and implement solutions, and finally, to measure the results of the process enhancement. GMP harnesses the energy, creativity, and productivity of the entire workforce.

Jan 1, 2001

By Slobodan Vujic

Production of building materials such as are stones, sand, gravel etc., is characterized by a relatively low economic value and requires reasonable transport costs. That is why we are often faced, in our practical work, with the fact that within the framework of a relatively small area several open pits of building materials are, developed side by side while neither ecological, urban and spatial nor location factors have been taken into consideration. Numerous locations together with heterogeneous factors. point undoubtedly to the problem of planning the open pits locations for building mateials as a very serious and complex one. Even when certain localities are in question, it is rather a difficult task to present a real state and encompass all the, important location factors by mathematical model ling. This paper presents one of such models for solving the problem of selecting a location for building materials open pit.

Jan 1, 1992

By Frank T. Wheby, Edward M. Cikanek

A computer performs all logic and computations customarily done by hand in preparation of engineers' estimates or contractors' bids on tunnel-shaft systems. The program described is based on construction methods, work forces and equipment selections corresponding to the current state-of-the-art of rock, soft ground and cut-and-cover tunneling. The program contains logic to permit estimates of cost of complicated tunnel-shaft systems; it is not necessary to input quantities, as the program calculates those from the tunnel design that is internally generated. In any estimate, the program bases its cost computation on user-input requirements and site conditions, such as tunnel shape and size, shaft depth, ground characteristics, construction methods, and other factors. To provide great flexibility, the user of the program is provided with options for accepting designs built into the program or overriding these designs by his own inputs. An illustrative example is presented.

Jan 1, 1974

By Donald L. Bott

A computer model called the Quality Compliance Model was developed to optimize the mine planning and sequencing in area coal mining with respect to the limit on pounds of sulfur dioxide per million BTU imposed by regulations. The objective of the model is to maximize the amount of high sulfur coal mined from various benches while meeting the specified compl'ance standards. Given multiple seams and multiple benching operations, the mining sequence from each pit is simulated. The rate of mining is controlled such that the in-pit blending will maximize the usage of high sulfur coal and meet compliance standards. The compliant coal can be stockpiled for usage at a later date, or it can be disassociated. This calculation can be based on any given rate of production, i.e., from as small a unit as a unit train to as large as monthly or yearly production.

Jan 1, 1982

By Frank K. Mattson

The Minerals Processing Section of Surface Combustion is currently engineering and erecting a plant designed to produce 400,000 LTPY of 95% metalized pellets from raw magnetite concentrate, This venture is the first domestic commercial facility that will manufacture pre-reduced pellets as an integral part of a process to produce steel. Surface Combustion has developed the methods that will be used. Midrex, a division of Surface Combustion's parent company, Midland-Ross, will own and operate this plant. The site is adjacent to the City of Portland, Oregon on a 15 acre hydraulically-filled area on the east bank of the Willamette River. Either filter cake or concentrates in slurry form will be purchased from Marcona in Peru, delivered to the dock facility by ocean vessels and distributed to a pond for wet storage. Reclamation from the pond will be with a conventional dredge delivering concentrate to a thickener.

Jan 1, 1968

Acid mine drainage is still a common problem in the northern Appalachian high sulfur coal region despite mining and reclamation practices applied to control it. Mining companies must treat water with alkali to raise pH and precipitate metals in order to discharge the water into receiving streams. Common chemicals used to treat drainage are limestone, hydrated lime, soda ash briquettes, caustic soda, and ammonia. Each chemical has advantages or disadvantages under specific conditions. A simple spreadsheet program was developed to evaluate costs of treating acid mine drainage across several specified water quality parameters and time horizons. Caustic soda and soda ash were shown to be cost effective for treating low flows and low acidity over short time periods. However, as quantity of water increased, quality decreased, and time horizon increased, the ammonia and hydrated lime systems were found to be much cheaper than caustic soda.

Jan 1, 1991

By D. R. East

Recent experiences within certain sectors of the international mining industry suggest an underestimation of the environmental risks associated with the design of mine waste-management facilities. These experiences show that the technical and managerial challenges of responsible mine waste management is not always fully appreciated. Unfortunately, the image of the mining industry's environmental performance is negatively impacted by a relatively few number of failures. This negative view overrides the many positive contributions made by the majority of mining companies. The fact that these failures continue to occur in developed and developing countries is indeed re¬markable and indicates a degree of risk-taking approaching unacceptable levels. The design requirements for tailings storage facilities are, in many cases, more demanding than those of conventional water dams because seepage of fluids that contain dissolved metals may pose a greater threat than the mere loss of water.

Jan 1, 2000

By H. L. O. Huyck

A microcomputer equipped with spreadsheet, data management, and FOR- TRAN programming software is used to update and quantify a model for ranking seventeen economically important metal commodities in terms of market potential (Huyck, 1982). Weighted factors are used for the ranking: (1) demand growth trends, (2) end-use substitution vulnerability, (3) recycling trends, (4) price trends, and (5) cumulative demand versus world reserves factor. Price trends are defined using (1) price-vs.-year slopes (with prices in 1967 constant dollars) and (2) standard deviations of slopes (to indicate price volatility). Substitution vulnerability is defined as the percent of end-use which is replace- able by other commodities, and a factor indicating the likelihood of such substitution. Factors are normalized and linearly combined to produce a ranking of the seventeen metals. Microcomputer software is essential for organizing data and calculating statistical parameters and linear combinations of factors.

Jan 1, 1986

By W. F. Hahnert, P. A. S. Ralston

In off-line training of a rule-based controller, the significant measure of successful training is the quality of control provided by the generated rule set. In an adaptive or on-line control environment, performance is also measured by the ability to accurately maintain a satisfactory rule set, but within constraints on speed and/or resource availability. Very small population genetic algorithms, or microGAs, have been proposed as a means of capitalizing on the hill climbing characteristics of faster local optimization techniques while requiring less memory and retaining much of the robustness of traditional, larger population genetic search. A traditional genetic algorithm and a similar microGA are developed and applied to two control problems. The performance of these algorithms is analyzed with respect to (1) the quality of the rules learned, (2) the rate at which learning occurs, and (3) the memory resources required during learning.

Jan 1, 1993

By Harry Verakis

Electronic detonator systems are an advance in technology beyond conventional electric detonators for initiating explosives and blasting agents. Their use is widening into the mining operations of the U.S.A. Each electronic detonator system differs in design, construction, operation, and testing features and each system is different than “conventional” electric detonators. There are benefits of electronic detonator systems which serve to improve blasting safety. With the introduction of electronic detonator systems for mine blasting, issues were raised about the application of MSHA regulations for shunting and circuit testing. The MSHA regulations for surface and underground mine blasting operations address the use of “electric” detonators. Although electronic detonators are initiated by an electric pulse or current, their design is unlike “electric” detonators. To resolve the issues of shunting and circuit testing with respect to MSHA regulations, a technical and field evaluation of electronic detonators was made and the results are presented.

Jan 1, 2005

By M. C. Williams, T. P. Meloy

For over thirty years the Population Balance Model, PBM, has been the mainstream modeling method for comminution unit operations and comminution circuits. For commercial comminution circuits the method is based on erroneous physics and dubious numerical mathematical methods leading to non unique solutions that have little extrapolative value and faulty control strategies. In short the PBM is wrong. Given is a detailed analysis showing a number of non trivial flaws in the linear PBM. Moreover, a simpler model is presented that leads to a solution of the comminution circuit predicting the size distribution output over a variety of conditions. Because the linear PBM is firmly entrenched, an award is offered, $10,000, to any researcher that can use the linear PBM and its present numerical methods to predict the typical straight line, self similar, output of wet mills over a variety of grinding times.

Jan 1, 1992

By Greg Blerie

The requirements placed on belt conveyors grow increasingly complicated No longer is it sufficient for the conveyors to merely move material from "Point A" to "Point B. " Now these systems must be able to produce a specified flow, guaranteeing a plant can operate as scheduled without peaks and valleys in material flow and production rate. In addition, the conveying system must provide effective control, to minimize the problems and costs associated with the escape of fugitive material these problems include unscheduled shutdowns, premature equipment failures, regulatory headaches, poor neighbor relations, and health and safety issues. The key to accomplishing these goals is the loading and discharge of the conveyor belts. Fortunately, new designs for the chutes that accomplish conveyor loading and discharge can move material efficiently, without blockages and while minimizing the amount of dust generated This innovation is the development of engineered flow chutes

Jan 1, 2004

By Katsunori Okaya, Toshio Inoue

Application of the discrete element method incorporating the simple kinetic model of the ball-to-ball and ball-to-wall interactions enables us to visualize the details of the grinding actions prevailing in the ball mills. We have developed a computer program to represent a generic mill model with which we can simulate tumbling mills, vibration mills, centrifugal mills and planetary mills. While the program can be used for various purposes including design of new equipment, one obvious application of it is the analysis of the conventional tumbling ball mills for better understanding and improvement. The purpose of this paper is to present a model and to observe its behavior in particular attention to the spatial distribution of the energy dissipation as well as the energy spectrum and their dependence on the major parameters such as mill speed, ball filling, liner configuration, slurry viscosity and the hardness of the ore.

Jan 1, 1995

By Robert L. Runkel, Kenneth E. Bencala, Briant A. Kimball

Thousands of abandoned and inactive mines are located in environmentally sensitive mountain watersheds. Cost-effective remediation of mining sites in these watersheds requires knowledge of the most significant sources of metals to surface waters. The significance of a given source not only depends upon the concentrations of a toxic metal, but also on the total mass, or load of metal added to the stream. To determine loads, we combined tracer-injection methods, to provide reliable discharge measurements on a watershed scale, with synoptic sampling, to provide spatially detailed concentration data. The resulting load profiles indicate which sources have the greatest effect on streams, where natural attenuation of metal loads occurs, and where ground-water inflows are located. This is part of the information needed for planning remediation of mine-drainage effects. The approach is illustrated by comparing zinc loading curves from three watersheds affected by mine drainage.

Jan 1, 2000

By Ralph D. Daley, Kevin E. Redinger

The production of coal/water fuel (CWF), a highly loaded mixture of finely ground coal, water, and chemical additives, presents a unique opportunity for significant ash and sulfur reduction through physical coal cleaning. Froth flotation can be integrated with the staged, wet, fine grinding inherent in the CWF production process. A laboratory scale research program was conducted to demonstrate the feasibility of a flexible, integrated coal cleaning/CWF process flowsheet. Performance of the conceptual flowsheet was examined for two coals of CWF commercial interest, Upper Freeport and Pittsburgh seam coals, from central and southwestern Pennsylvania, respectively. Several multi-stage coal flotation and reverse flotation circuits were evaluated. CWF was produced from the cleaned coal in each case at similar solids loadings and viscosities as observed for the raw coal. However, the ash loading and SO2 emission potential for each CWF had been significantly reduced.

Jan 1, 1988

By John Marsden

JIM ARNOLD: Our next speaker is John Marsden. John runs the concentrator complex at La Candelaria Project in Chile. John's a Royal School of Mines graduate and he wrote the book on gold metallurgy, The Chemistry of Gold Extraction, which, by the way, he dedicated to me-at least that's what my copy says. [laughter] John, go ahead. (Message shown on Projection screen) ‘Raulerson’s Rules Plant operators and maintenance personnel should be asked to participate early in the design process. This ensures that the plant will never be completed on time or within budget.’ JOHN MARSDEN: Good afternoon, everybody. My presentation this afternoon is going to be very short. It won't be as funny as Joe Keane's, but I guarantee you it will be a lot quicker. [laughter] That transparency isn't mine, actually. [laughter] You're trying to throw me off.

Jan 1, 1998

By William E. Foreman

The results of the electrokinetic study of the activation of quartz by divalent cations showed that the charge reversal was related to the point at which the cation hydrolyzed. The reversal was not due to the presence of solid hydroxide at the surface of the quartz but due to the charged ions in the solutions. The charge reversal for beryllium at a log molar concentration of 1x10-4 was observed at pH 5 and 9. The quartz was positively charged between a pH reading of 5 to 10. Magnesium at the same log molar concentration did not show a charge reversal from pH 2 to 12. The probable cause of the charge reversal was due to the ionized Be3 (OH)3+3 or Mg (OH)+ . Variations in the electrokinetics of quartz were minimized by heating the sample to 300° C.

Jan 1, 1968