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By R. J. Sweigard, R. V. Ramani

Estimated costs and revenues can be used in evaluating postmining land use alternatives. However, postmining land use decisions have to be made in an environment complicated by several additional factors. These factors, including cultural, natural, and managerial issues, are not as easily quantified as costs and revenues but may be more important determinants. There fore, some approach is needed to attach relative weight to the various factors. The concept of fuzzy sets assembled into a structured hierarchy facilitates analysis of the relative value of individual factors and their impact on each alternative under consideration. In this paper, a method is presented that employs fuzzy set analysis to evaluate postmining land use plans on the basis of these nonquantitative factors.

Jan 1, 1988

By V Leus, J. Kallioinen

The large size of the modern flotation cells and the high product flow rate from them has increased the importance of optimal flotation of all the particle sizes and of process control. By treating all the subprocesses of flotation separately a new family of flotation cells and a new concept of optimizing the flotation of coarse and fine particles in separate units but in the same row of flotation cells has been developed. The paper discusses the possibility to enhance coarse particle flotation by varying the froth residence time. A function has been developed between the residence time of the froth, air rate and the froth removal rate of coarse apatite particles. The response of apatite flotation to different control variables has been studied and modelled. The results show that the BPL assay response depends not only on the control variable used but also on the feed assay to the cell. There exists an feed assay dependent region within which the froth assay can be controlled by using the froth residence time as the control variable. These regions can be used to tune a rougher-multistep cleaner circuit to optimal.

Jan 1, 1993

By Erich U. Petersen, J. B. Hiskey, William J. Tafuri, Donald M. Hausen, X. H. Jiang, Douglas N. Halbe, G. Ramadorai

The extraction of gold from chloride solutions with activated carbon is examined. It is shown that the uptake of gold by activated carbon from chloride solution follows a mechanism whereby gold is reduced to the metallic state. Metallic gold appears as deposits both on the carbon surface and in pore space within the carbon particle. The deposition rate is dependant on the carbon particle size and pH. At low initial gold concentrations, the initial rate is insensitive to gold concentration. Sodium hypochlorite exhibits an adverse effect on the reduction reaction. The overall loading and initial rate of reduction are both decreased in the presence of NaC10. The effect of iodide on the loading of gold was also examined in an attempt to overcome the superficial deposition of gold on carbon.

Jan 1, 1990

By Zhen-lu Zhao

The manipulators possibly used in underground mining must deal with unpredictable obstacle while keeping certain positions and orientations of end effector, and in some cases, are required to possess redundant joints in order to be more flexible. This kind of manipulators might be fitted with jumbo drill or platform as auxiliary to potentially deal with some utility works in versatile way, such as installing rock bolts, guniting, blasting, charging, surveys and measuring work, etc.. This paper describes numerical procedures of performing inverse kinematic problems for redundant manipulators .The procedures, based on the generalized pseudoinverse of Jacobian matrix, are developed to lead to kinematic solution at both singularity and ill conditioning, and to guarantee continuous sequence of positions of the end effect or. Furthermore, the solution to optimization and obstacle avoidance is investigated. A numerical example is shown to illustrate the approach.

Jan 1, 1989

By C. H. Rawlins

Deep bed media filtration is used as a tertiary treatment step (after hydrocyclones and flotation cells) to remove fine oil droplets and solids from oilfield water before reinjection disposal or to remove particulate material from surface waters used for waterflood injection. Oil and solids injection requirements are typically <5 ppm concentration at <2 micron diameter. The preferred media for produced water filtration is walnut or pecan shell, however the use of this media has evolved by trial & error and the fundamental mechanisms that occur during separation and media cleaning have not been investigated. A project was initiated to fill in this knowledge gap by analyzing the physical, mechanical, chemical, and hydrodynamic properties of six types of granular filtration media (12/20 mesh size): garnet, silica, anthracite, pecan shell, English walnut shell, and black walnut shell. Comparison of bed packing, oil wetting, attrition resistance, particle strength, and fluidization has led to an understanding of the preferred filtration media for separation of fine oil droplets and solids.

Jan 1, 2010

By S. Zaman, John Bulter, M. E. Defoe, Franklin T. Davis

This section deals with the carbon minerals and materials: graphite, tar sands, gilsonite, and diamond. as well as sulfur and the sulfides of mercury, arsenic, antimony, and bismuth. Table I contains the production figures for each of these commodities in the United States and in the world. Specifications for concentrates are also summarized as are prices for concentrates at the time the section was written. In each chapter an attempt has teen made to describe the more common commercial mineral involved with the commodity, the processes used to recover and concentrate the minerals, as well as geographical areas where these processes are utilized.

Jan 1, 1985

By J. Iannicelli

High intensity, high gradient magnetic separation can economically remove weakly paramagnetic contaminants down to 0 1 micron from industrial minerals This process is employed by all waterwashed kaolin producers in Georgia where seventeen huge magnetic separators are used to upgrade this product As a result, reserves of kaolin in Georgia have been doubled Design improvements have steadily increased the efficiency of separators and reduced power consumption below 300 KW for a nominal 65 TPH unit Beneficiation of ultrafine minerals is discussed based on pilot plant results on bauxite, ball clay, calcium carbonate, glass sand, talc, and numerous other minerals Operating parameters of the process are reviewed and some alternative equipment configurations discussed

Jan 1, 1983

By L. Adler

Determining whether a railroad locomotive will skid under varying conditions is a fairly routine, pervasive problem. However, some of the equations provided are wrong, others are at best murky. All require correction or clarification. Skidding during heavy braking is a crucial safety problem, possibly resulting in loss of control and collision. It can also be an economic detriment, ruining wheels and tracks and, by inhibiting acceleration, causing reduced full-speed times. While skidding is less likely for rubber-tired equipment, a comparable problem exists for tractor-trailers operating on poor surfaces. The primary reference is to the SME Mining Engineering Handbook (pp. 14-11, Eqs. 7 and 8), which is taken as authoritative and normative (Brantner, 1973). Fundamentally, the physical weight of the locomotive can never be negative (-). However, based on this reference it can be negative on adverse grades, during braking (Eq. 7), and on favorable grades, whether accelerating or braking (Eq. 8). Additionally, it should be noted that the term rW should be Rw. To avoid having the locomotive weight turn out negative, "absolute value" brackets must enclose the right-hand expression of both equations. Also, the weight of locomotive can be greater than the right-hand side value introducing the common "greater than or equal to" symbol (>_). While these alterations are easy to make, the use of the algebraic sign associated with each term is still confusing, as

Jan 1, 1991

By H. Polat, M. Polat, S. Chander

A high shear treatment step was observed to improve flotation of coal. The effect of high shear treatment (HST) was a strong function of coal rank, however. For the low rank coals the HST produced loose, open-structured agglomerates which decreased the entrapment of ash minerals. For the high rank coals, the high shear treatment promoted detachment of low-floating particles from the agglomerates that ordinarily formed in a flotation cell. The extent of agglomeration and detachment of particles from the agglomerates was a function of the amount of dodecane and coal rank. To obtain desired efficiency of separation ethylene-propylene oxide block co-polymers were used. The results showed that the HST-flotation technique increased the ash rejection considerably for both high and low rank coals, though the mechanisms were different.

Jan 1, 1995

By R. Fedors, T. Ghezzehei, D. Or

The phenomena of dripping into cavities (e.g., tunnels and drifts) within an unsaturated fractured porous medium under ventilated conditions was studied to improve estimates of dripping rates, drop sizes and the chemical composition of droplets that could affect the integrity of high-level nuclear waste packages placed in drifts. The sensitivity of dripping rates and water chemistry to ventilation was analyzed at various flow rates using analytical expressions linking flow on fracture surfaces to drop formation and evaporation. The model was tested using laboratory experiments involving machined aluminum slabs designed to represent a simplified morphology of a fracture face intersecting a cavity and using natural fracture surfaces from a welded tuff Comparison with ten years of data on dripping in natural caves showed good agreement with model predictions. In particular, for low dripping rates, evaporation due to ventilation leads to larger drop sizes and alters drop chemistry by increasing the concentration of solutes in the drop relative to that in the water flowing on the fracture face.

Jan 1, 2002

By D. C. Torre

The coal mining industry has long recognized the need for a system capable of hauling mined coal from the face in a continuous flow. More than 30 years ago, successfully operating continuous haulage systems were first placed in the field. There were a few individually successful applications. However, the truly successful use of such systems really only began in the early seventies. Today, a variety of systems are available from a number of manufacturers. Even so, continuous haulage has not achieved the acceptance and application it would seem to have earned. There is a need for more productive, cost-effective, and safer methods of hauling coal from the face. There is also a need to speed up development for longwall operations. And continuous mining is not really "continuous" unless it is supported by a reliable continuous haulage system. Despite all this, most of the coal producers have failed to exploit the successful continuous haulage systems offered by several manufacturers. In the 1970s, many of the top coal producers tried a continuous haulage system but gave up on it and on the concept. In some cases, major coal companies had systems operating successfully in one mine, or even one division. But their use did not spread to others of their mines or divisions. Frequently, their use was eventually abandoned, even in mines where it had been successful.

Jan 1, 1990

By Masahiro Lnoue, Kenichi Uchino

Airflow velocity vectors by a forcing auxiliary fan at a heading face were measured in an actual size model gallery and an actual mine. The location of an outlet of ventilation duct gives significant effects on the airflow at the heading in the gallery. It was also found that there were several stagnated regions which may have danger of methane accumulation. The flow were also examined using the visualization technique by laser light in a reduced scale model. The flow in reduced scale model showed similar behavior to those observed in actual size galleries. The air velocity at the outlet has no significant effect on the airflow. It was found that a region to be ventilated by the direct flow of the exhaust fan is limited to a relatively short distance but a secondary flow region is generated near the heading face. CFD ( Computational Fluid Dynamics ) method was also developed to examine the airflow. The calculated results coincides with those measured by actual and reduced scale models. It is concluded that the CFD is useful tool for the analysis of ventilation at the headings.

Jan 1, 1997

By G. E. S. Valadão

This paper is concerned with studying the dewatering behavior of three samples of iron ore products. The objective is to improve the industrial filtration performance by taking into account the laboratory results. Mineral samples came from the Iron Ore Quadrangle in the state of Minas Gerais, Brazil. These samples represent products from the industrial processing of hematitic ores. The samples have almost the same chemical and mineralogical compositions, but they have different size distributions and different specific surface areas. The filtration tests were performed using a modified Büchner funnel apparatus. The results indicate that size distribution and specific surface area have significant influences on dewatering behavior. For Sample 1, the addition of flocculant and/or surfactant was not essential to improving filtration performance. For Sample 3, the cake porosity and the cake thickness were influenced by the addition of the flocculant. On the other hand, the simultaneous addition of flocculant/surfactant decreased the cake formation time and reduced the cake moisture. For Samples 2 and 3, it was also observed that the industrial operation could be improved by taking into account these laboratory results. Key words: Dewatering, Iron ore, Hematite, Filtration, Flocculation, Surfactant

Jan 1, 2003

By M. Niinae, Y. Nakahiro, T. Wakamatsu

In some cases, the extraction and separation efficiency of metals with a combined extractant are better than those with either extractant alone. However, the extraction and separation efficiency of metals with a combined extractant are not always better than those with either extractant alone. As part of the fundamental studies on the extraction and separation of metals with combined extractants, the extraction and separation efficiency of Au and Fe(III) added as an oxidizer in the leaching of Au from a sulphuric acid solution containing thiourea, and the extraction and separation efficiency of Nd and Sm from hydrochloric acid and sulphuric acid solutions were examined. The combined extractants for Au and Fe(III) were di(2-ethylhexyl) phosphosphoric acid (D2EHPA)/tri-n-butyl phosphate (TBP), D2EHPA/trioctyl phosphine oxide (TOPO). tri-n-octylamine (TOA)/TBP and TOA/TOPO, and those for Nd and Sm were D2EHPA/TOA. D2EHPA/TOPO. 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester (EHPNA)/TOA and EHPNA/TOPO

Jan 1, 1994

By Ronald E. Heuer

It is not possible to accurately predict water flow into rock tunnels during construction, because all of the relevant factors cannot be accurately determined ahead of time. But an estimate is needed, because water inflow can be a major problem during construction, hence also a major concern for project design. There currently is no simple, generally accepted method of estimating inflow. This paper describes a semi-empirical method for estimating possible water inflow based on borehole water pressure test results, using correlations from previous tunnel experience. The method provides an estimate of percentages of tunnel length which will experience different intensities of long term steady state inflow, and provides an estimate of possible initial heading inflow. The method is applicable for distributed sources of water inflow due to rock mass features such as systems of joints and bedding planes, and accounts for different boundary conditions of water head and recharge. The metric system flow units used in this paper are liters per minute (L/min) and liters/minute/meter of tunnel (L/min/m), to be compatible with rock mass classification systems commonly used today.

Jan 1, 1995

By Paul F. Ph. D. Ziemkiewicz, Courtney D. Black

According to the American Coal Ash Association, 105 million tons of coal combustion products (CCP) were produced by the power generating utilities in 1997. Of that total, 1.68 million tons were used in mining applications (ACAA, 1997). Results have ranged from the environmentally beneficial to neutral and, in some cases, detrimental. Twenty years ago coal ashes: bottom and fly ashes constituted nearly all CCPs. With the shift to new emission control technologies at power plants, however, large volumes of new products are being generated. Many do not lend themselves to traditional ash applications such as cement formulation. Many CCP disposal sites are not documented with reliable pre and post application monitoring. In this report we discuss types of CCP, their relevant characteristics and the mining environment. We have attempted to identify a range of documented applications and to draw conclusions about their environmental effects including benefits and adverse impacts.

Jan 1, 2000

By Jaye Pickarts, Bret Boster, Jack McPartland

Pegasus Minera de Chile, Ltda. is completing three phases of metallurgical evaluation on the Pullalli project to develop a preliminary process flowsheet. A project feasibility study is in progress. The feasibility study includes a proposed process flowsheet designed based on results from the multiple stages of metallurgical evaluation. Phases I and II of metallurgical evaluation included laboratory scale heap leach and milling cyanidation testwork on multiple drill core composites and bulk ore samples from the Pullalli Project. Phase Ill included pilot scale milling/cyanidation testwork on Pullalli drill core composites. The proposed flowsheet includes selective mining and separate processing of low grade and high grade ores. Low grade ore will be crushed and heap leached. High grade ore will be milled leached for 12 hours in an agitated cyanidation circuit. After 12 hours of leaching, sands and slimes will be separated and the sands will be washed using a counter current cyclone (CCC) circuit. Partially leached and washed sands will be added to the crushed low grade ore for heap leaching treatment and permanent placement. Partially leached slimes will be thickened in a high capacity thickener and will be processed in a CIP circuit. Leached slimes will be placed in a tailings impoundment.

Jan 1, 1996

By P. J. Ryan

December 1988, Phelps Dodge Corp. brought an underground gold mine into production in the republic of Botswana. The mineralization is associated with steeply dipping shear zones in Archean greenstones of the Tati schist belt. The gold is intimately associated with sulfides and is refractory in nature. The deposit is being exploited by underhand open stoping methods. Vertical and inclined shafts are used to hoist the ore to the surface where it is treated by conventional crushing, milling, and flotation, followed by fluid bed roasting with cip elution and carbon regeneration. Adjacent deposits are being explored with a view to increasing production. Legal and taxation aspects of operating in Botswana are discussed.

Jan 1, 1991

By André Vervoort

The roof behaviour in room and pillar panels during the development of roadways and the subsequent pillar extraction was monitored underground and numerical simulations were conducted. For several underground sites, a satisfactory, correlation was found between underground measurements and three-dimensional numerical simulations using a boundary element code in the linear elastic domain. However, to simulate bed separation, and roof block collapses more complex models were required, of which examples are presented.

Jan 1, 1992

By Paul D. Tavares, John Forbes, Eric R. Drooff

As the existing major U.S. - Canada rail tunnel was too small to accommodate double-stack container cars, Canadian National Railways is constructing a new parallel tunnel with a 50% greater diameter. Starting in Sarnia, Ontario, the new shallow-cover bored tunnel runs under a large research building and several other structures in an oil refinery before travelling under the St. Clair River. Maximum predicted settlements to be caused by the 9.2 meter diameter earth pressure balance TBM in the soft St. Clair till were in excess of 100 millimeters. As such, these settlements had the potential to cause severe damage and disruption to the existing refinery. In order to reinforce the soft clays below the refinery research building and other structures, and to compensate for settlement caused by the tunnelling, the ground improvement method of Soil Fracture grouting was successfully applied for the first time in North America. This paper will describe the details of both the soil fracture grouting application and the elaborate electrolevel remote monitoring system used.

Jan 1, 1995