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By A. Bascetin, A. Nieto

One of the most difficult problems in mining operation is how to determine optimum cutoff grades of ores at different periods over the lifespan of the mine that will maximize the net present value (NPV) of the mine. Cutoff grade optimization maximizes the NPV of a project subject to capacity constraints in the mine, mill and the market.. This paper describes the determination of a cutoff grade strategy based on K. Lane’s algorithm adding an iterative optimization factor calculated for every year during the live of the mine to maximize the project’s NPV. The introduced algorithm is a windows based program developed at Virginia Tech which coded in visual-basic within a spreadsheet environment (Excel). The resulting cut-off windows based program is a user-friendly tool which calculates interactively different mining cutoff grade scenarios. The benefits of the methodology are demonstrated using a hypothetical case study. The authors have observed an improvement of the total NPV using this iterative approach using a year by year optimization factor.

Jan 1, 2007

By P. Venkatasubramanian

The selection of a mining method for a mineral deposit is a complex decision problem. Human judgment, based on experience with mineral deposits and geologic conditions, remains the single most important input of the decision-making technique. If the use of artificial intelligence, in particular the developments in expert systems, is taken to its logical conclusion, the experience of the domain experts could be incorporated into a decision-support expert system. A knowledge-based decision support system for mining method selection for ore deposits has been designed whereby the domain knowledge is represented as production rules and organized in a semantic tree representation. This model is written in the PROLOG language. While the verification difficulties of expert systems models are recognized, an example of the model's decision on the mining method for a given ore body is presented and shown to be consistent with the decision made by human experts. In addition, plans, for further verification of the model are delineated.

Jan 1, 1992

By Gerald H. Luttrell, Joe Shoniker, Jaisen N. Kohmuench, Christopher J. Barbee, Michael J. Mankosa

The HydroFloat technology was specifically developed to upgrade phosphate sands that are too coarse (>0.6 mm) to be efficiently recovered by conventional flotation methods. In this novel process, classified feed is suspended in a fluidized bed that has been aerated using an external sparging system. The air bubbles selectively attach to particles that have been made hydrophobic through the addition of a fatty acid collector. The teetering effect of the fluidized bed forces the low-density bubble-particle aggregates into the overflow, while hydrophilic particles are rejected as a high solids content underflow Since the HydroFloat is actually a density separator, the process can treat much coarser feeds than would be possible using traditional flotation processes. In addition, the high solids content of the teeter bed promotes bubble-particle attachment and reduces the cell volume required to achieve a given capacity. This paper presents test data from ongoing pilot-scale trials of the HydroFloat cell in the phosphate industry.

Jan 1, 2002

By N. R. Joshi, A. D. Agate

It is estimated that more than 80% of phosphate rock output in the world is used for fertilizer production. In India, there are only a few high-grade deposits of phosphate ores; therefore, most of the requirement for phosphatic fertilizers is satisfied with imported DAP (diamino phosphoric acid). Due to the drain on foreign exchange reserves, this import-dependent, essential commodity is in short supply in India and, therefore, is sparingly used by farmers. In addition, of the added phosphorus, normally 80% becomes unavailable to plants because phosphorus complexes are formed in soil, causing deleterious effects on plants. In our laboratory, this problem was tackled by using a bacterial consortium of phosphorus-solubilizing bacteria. It resulted in the speeding up of seed germination and increasing available phosphorus in the soil by 14%, over a period of 80 days. To use the low-grade deposits of phosphatic rocks available in India near Hirapur, Madhya Pradesh, India, which contain high amounts of iron, beneficiation through microbial means was used for phosphorus removal. Beneficiation was achieved partially through removal of extra iron by oxidizing ferrous iron from the ore by a Thiobacillus species after removal of impurities containing both silica and iron, instead of sieving and cleaning the ore using different techniques. This resulted in a cleaner ore, with nearly 70% of such impurities removed. The factors for beneficiation technique were standardized at the laboratory level and are being used for scaling up of the process. Thus, the beneficiation of phosphatic rock from Hirapur will be an important first step of phosphorus production in India.

Jan 1, 1999

By S. Behl

A major limitation in developing successful selective, flocculation schemes is the difficulty encountered in adsorbing the polymeric flocculant only on the desired substrate. In this paper, a correlation between selectivity of flocculant adsorption and separation efficiency is outlined, and a potential technique to achieve selective adsorption of flocculants is discussed.

Jan 1, 1994

By Menzhans Guo

A coal bunker basically acts as a buffer and regulator to reduce the interruptions between its proceeding production system and succeeding haulage system so as to maximize the availability of the whole system. Although such a role has long been recognized, quantitatively studying it is still rarely seen in the literatures. Its unique characteristics, coupled with numerous transitional states, make it very complex to describe the state transitional process in analytical models and, also very difficult to seek an analytical solution. Moreover, the analytical models inappropriately consider the state of bunker being full or empty as a kind of failure, therefore, by no means can they realistically describe the impact of the difference between rates of coal flowing to and from a bunker on the system availability. In light of this, Monte Carlo simulation methods are suggested to reach an approximate solution. In comparison, simulation methods are simpler and more effective than analytical approaches. Applications of simulation methods to a Northern colliery for determining bunker size from the viewpoint of maximizing system's availability are discussed. The results are satisfactory.

Jan 1, 1992

By S. J. R. Lowrie, J. S. Edwards, A. D. Jones

A small scale model has been constructed to simulate air and gas flows on a full scale retreat longwall coal face. Scaling relationships were derived to define how the main aerodynamic properties of the full scale could be preserved in the small scale model. These scaling requirements include: a minimum value for the Reynolds number for the flow on the face in order to maintain turbulent flow with a constant non-dimensionalised coefficient of turbulent dispersion; a constant Richardson number to maintain similitude for the formation of layers of buoyant gas; scaling of the permeability of the waste so as to obtain the same proportion of seepage flow through the waste; pressure gradients due to the ventilation and to the density difference (between the air and the gas layer) were kept in proportion; and in the waste, the relative contributions of inertial dispersion and molecular diffusion were approximately in proportion. The complementary roles of computational fluid dynamics (CFD) and aerodynamic scale models for simulating mine ventilation are discussed. The physical model is described and an example presented of simulations of the effect of changes in mining condition on the effectiveness of gas control in retreat longwall coal faces.

Jan 1, 1995

By Frederick P. Schwarz

Sample preparation and analysis can impose devastating errors on assay data. Minimizing these errors by testing and procedural redesign may be critical to assure representative assays and project success. Replicate samples, taken at any volume-reduction and/or analytical step in a sampling procedure, generate replicate assay values whose relative differences constitute a set of data. Variance of this data judges the addition to total sampling error imposed by the step generating the replicates. A variance more than (11.5%)' is excessive for a single step. Sample volume increase and/or comminution at a step will reduce variance for that step. Rejects from well mineralized intercepts can provide bulk samples for testing.

Jan 1, 1989

By R. M. Bowen

To help solve problems associated with the optimization of complex coal preparation systems, a mathematical model has been assembled which can simplify calculations pertaining to the core of the plant, i.e. the coal cleaning section. It uses algebraic expressions, derived by fitting hyperbolic equations to Mayer curves, to calculate optimum settings for a specified array of coal cleaning units and feeds. This is done without search procedures, and with usually only minor iteration of a simple calculation to specify optima within 0.02% of specified product ash contents. The key to the calculation is a relationship derived via the analytical geometry of conic sections facilitating easy application of the incremental ash theory of separations. The model has been assembled in a generalised form to cater for N processes in parallel, each giving M separations to produce P final products. Examples are given involving assessment of some complex circuit options.

Jan 1, 1986

By D. Lelinski, R. Bokotko, J. D. Miller, J. Hupka

Air-sparged hydrocyclone (ASH) flotation is a new, promising technology, and, since its conception, numerous applications have been successfully tested. Nevertheless, research and development efforts have continued to improve the technology with respect to operating conditions and design considerations. Results, from experimental studies on bubble generation in the ASH system are presented in this paper. Bubble size distributions generated during ASH operation were determined using a high-speed photographic technique. The influence of many factors, including surfactant concentration, water flow rate, and porous-tube pore size have been studied. Test results indicate that these process variables have a profound effect on the bubble size distribution. With an increase in surfactant concentration or water flow rate (shear field), the bubble size distributions become narrower and shift toward smaller average bubble diameters. However, the influence of pore size is more complicated. Depending on the experimental conditions, the average bubble size was found to range from about 100 to 300 µm in diameter.

Jan 1, 1997

By Richard R. Radel, Jack Barry

Contract required excavating 2,000 If of 14' horseshoe tunnel in rock, a 95' deep work shaft on shore, and a 50' deep intake shaft located in the middle of the Niagara River just above Niagara Falls. Large quantities of H2S were encountered in the range of 20 PPM with ventilation. Peak levels of 40 PPM were recorded. The original designed ventilation system required only a volume of 10,000 CFM to meet OSHA requirements. The volume of air was increased to 50,000 CFM to dilute the H2S to al- low workmen to work and comply with OSHA H2S action levels. The second phase of the tunnel consisted of placing 72" ID X 20 foot long concrete reinforced pipe in the tunnel. When the tunnel was holed through and both shafts were open, a substantial amount of work was required to take place in the shafts which eliminated the possibility of placing a bulkhead to secure proper ventilation. The ventilation team designed a jet system airlock. The design of this system was to bring fresh air down the work shaft in two duct systems; one 30" diameter and one 24" diameter. Following the excellent work of Jan Wolski (7th Mine Ventilation Symposium chapter 58) our design incorporated nozzles located approximately 100' in by the work shaft. The velocity of the 24" diameter duct was 6,365 FPMD2.2 MPH. The velocity of the 30" diameter duct was 6,117 FPMl69.5 MPH. Both systems were on blow and being that air expands at 3112 degrees per side this high velocity of air expanded and created an air bulk head through which men and the large sections of concrete pipe could be passed without any delay or additional cost to the project.

Jan 1, 1997

By Heinz Hoberg, Fred Ulrich Schneider, Rudolf Diegel

The risk of contamination of dumped tailings and ground water by coal flotation reagents has been investigated by using the 14C-radiotracer method for adsorption and desorption measurements. The results indicate, that a high amount of the reagent components adsorbed on the tailings if there was no coal in the pulp. In coal flotation however a competitive adsorption behaviour could be observed, with the effect that only a low quantity of reagents adsorbed on the tailings. Mobilization tests showed, that only small quantities of reagents could be desorbed by rinsing water. Therefore the contamination of ground water should be low.

Jan 1, 1995

By S. N. Mukherjee

Maintenance of equipment in Longwall faces plays a vital role in face performance. This is more prominent when shortage of spare parts and trained personnel occurs. A study was made in an operating Indian Longwall face for identifying the types and meantime between failures. Though the duration was not enough and study was not very elaborate, it revealed certain interesting facts. The machine availability was found to be poor, though a maintenance schedule was followed. Failure of simple parts like AFC chain connectors even resulted in loss of production of 10 times the complete chain cost. This pinpoints that a proper maintenance schedule is to be developed considering the human factors and local conditions existing in the particular country. Operations research techniques could be used in the process.

Jan 1, 1989

By H. J. Sohn, S. G. Doo

A systematic study was carried out to investigate the reduction reaction mechanism of oxygen on pyrite surface using electrochemical techniques. The polarization curves showed two distinct regions, the Tafel region for superoxide formation and limiting current region for diffusion of dissolved oxygen to form hydrogen peroxide. These results were confirmed with a-c impedance measurements.

Jan 1, 1990

Africa is rich in natural resources, much of which remain untapped. Despite that, international mining companies have largely stayed away from the continent due to political instability in many countries, lack of infrastructure and the inability to gain control of mineral deposits. Today, optimism is growing concerning African mining. Many of its nations are moving toward privatization of their mining industries. They see it as a way to improve the lives of their populations and become politically stronger. Ministers from 22 African nations were Denver, CO in June for the World Bank's Multilateral Investment Guarantee Agency's Fourth Annual African Mining Investment Symposium. The three-day symposium drew more than 400 mining executives and government representatives. Foreign mining investment in Africa is on the increase. In 1996, international mining companies spent about $418 million on exploration. That is more than double the $190 million spent in 1994. Mining executives say the mining climate in Africa is improving because countries are privatizing the industry and rewriting mining laws that encourage natural resource development. They estimate that private mining firms now control about 80% of mining today. Mine development will help lift the living standards for Africans, the ministers said. The average income for ordinary Africans is about $500 a year. If this new mining boom continues, citizens of nearly all African nations will reap the benefits of better infrastructure and government services, as well as more higher paying jobs, the ministers said. They also issued a word of caution to mining companies attempting to join in the African boom. Concerns are being raised about the treatment of villagers and the environment. In the past, foreign companies would "behave about like colonial masters," said Gerald Ssendaula, natural resource minister for Uganda. Africa is in a different position now, he said. "Now we are solving our own problems." Mining companies must respect local communities or risk creating unrest that will threaten fragile new governments, said Akolang Tombale, chief geologist for Botswana. On the other hand, he said villagers must accept that mining development will benefit them. "They feel these are their natural resources. There must be a mutual interaction between the companies and the people."

Jan 1, 1997

By G. H. Lewis, C. L. Krcil, N. S. Harding, D. E. Havekotte

INTRODUCTION Limestone injection work was completed in a 440-kW (1.5-million Btu per hour) pilot-scale combustor in preparation for a 50,000-kg/h (110,000-lb per hour) industrial steam boiler limestone injection test program. The main objectives were to: (1) identify the important variables that affect sulfur capture, (2) determine the maximum SO2 removal, and (3) determine the effect of limestone addition on furnace operability and heat transfer. A more detailed report is given by Lewis et al. (1985). The test program was divided into two phases. The objectives of Phase I were to determine the important variables that affect SO2 reduction and to investigate the effect of limestone addition on combustor operation and heat transfer surfaces. The objective of Phase II was to determine, using only the important variables identified during Phase I, the conditions that resulted in the greatest sulfur dioxide reduction. Phase I Test program Using one limestone, five variables were identified as having an effect on SO2 reduction. These are noted with their respective ranges: heat release rate [103 to 166 kW/m3 (10,000 to 16,000 Btu per hour-cu ft)], Ca/S molar ratio (0 to 3), flue gas oxygen concentration (3% to 5%), additive particle size [90% -150 µm (-100 mesh) and 90% -45 µm (-325 mesh)], and burner stoichiometry (SR = 0.75 and >1.15). A 2.3% sulfur northern West Virginia coal, pulverized to a nominal grind of 70% -75 µm (-200 mesh), was burned for the tests. The limestone used was obtained from a Maysville, KY, quarry and contained 51.75% (wt) CaO. An 11-run statistically designed program (plus three duplicates) was used to screen the five variables. The effect of limestone injection on the combustor heat transfer surfaces was determined by comparing the heat transfer rates through a slag panel and fouling probes during periods with and without limestone injection. Combustor operation was determined by noting any operating problems that occurred during the tests. Test procedure After furnace wall temperatures had stabilized at operating conditions, heat transfer surfaces (slag panel and fouling probes) and the convection section were blown clean, and a four-hour test was begun. The

Jan 1, 1987

By Merrill P. Allen

The Vernal phosphate rock concentrator is located in the Uinta Mountains near Vernal, Utah. Ore is sedimentary rock from the Phosphoria Formation. Truck and shovel mining is done at a rate of 11,500 TPD. Run of mine ore is crushed and then milled through a SAG mill and ball mill to minus 16 mesh. Milled ore is deslimed using cyclones and hydrosizers. Sands are conditioned with fatty acid, petroleum sulfonate, diesel fuel and frother prior to primary rougher and cleaner flotation. Primary flotation tailing is milled to 95% minus 48 mesh, deslimed in cyclones, conditioned using reagents previously described, and then processed through rougher and cleaner scavenger flotation. Product of scavenger cleaner concentrate is upgraded by reverse flotation of dolomite. Flotation concentrates are combined and dewatered, pulp being milled to 99.5% minus 65 mesh and then thickened to 65% solids. Product is pumped from storage through a 10 inch, 94 mile pipeline to a conversion plant at Rock Springs, Wyoming. Mill tailing is stored behind an earthen dam, water from the settled tailing being reclaimed for mill use.

Jan 1, 1993

By Alfredo Dammert

The paper presents the results of a model built at the World Bank in order to analyze the aluminum industry. Bauxite demand for the year 2000 is estimated as a function of alumina refineries' requirements and of non-metal uses for bauxite. Bauxite supply by countries or regions depends on economic factors such as investment costs, operating and transportation costs, as well as on tariffs and levies. Various scenarios are considered as a result of varying the assumptions of the model.

Jan 1, 1984

By Mark J. Zdunczyk

Short Mountain Silica mines the Clinch Formation, an orthoquartzite, for silica sand. The operation is located near Mooresburg, TN, about 80 km (50 miles) northeast of Knoxville. Short Mountain is a local geographic name given to an area of resistant sandstone (Fig. 1). The area is part of the Clinch Mountain system that extends from eastern Tennessee to southwestern Virginia. The thick sandstone unit is more technically called a quartz arenite (orthoquartzite) that forms most of the mountain. In 1980, a Knoxville resident brought the Clinch Formation - Short Mountain in particular - to the attention of the large silica-sand producers as a potential silica-sand mine. Working with a local contractor who owned several hundred acres on Short Mountain, the Knoxville resident contacted interested companies. Many silica companies reviewed the property including Ottawa Silica Co., Pennsylvania Glass Sand Co. (both now US Silica Co.),Unimin Corp.,The Morie Co. and others. AFG Industries was the main market for the glass sand product from this potential mine. It had two plants, both within trucking distance from the site. All the silica sand producing companies, however, declined to develop the site. A few years later, Unimin Corp. decided to drill and evaluate the deposit. From that evaluation, Unimin leased the property but later dropped it. The relatively limited market for the Short Mountain product as well as Unimin’s recent acquisition of Carolina Silica were reportedly instrumental in the company’s decision to let go of the lease. Several other companies-unrelated to the silica sand industry - looked at the site but no one was interested in developing it. In 1986, J.D. Nicewonder, owner of coal mines in Virginia and Kentucky, was approached to investigate the site. Nicewonder began to develop the site with the intent to produce glass sand to supply AFG Industries. In May 1988, the first shipment of sand was trucked to AFG Industries.

Jan 1, 1992

By R. Hiebert, M. Canty, S. Beckman

An innovative biological process is described for the treatment of cyanide-, metals- and nitrate-contaminated mine process water. The technology was tested for its ability to detoxify cyanide and nitrate and to immobilize metals in wastewater from agitation cyanide leaching. A pilot-scale demonstration is described in which a pilot plant was constructed to demonstrate the technology on a mine process-waste stream at a mine in Nevada. The demonstration was performed jointly under the Mine Waste Technology Program (MWTP), funded by the US Environmental Protection Agency (EPA) and jointly administered by the US De¬partment of Energy's (DOE) Western Environmental Technology Office (WETO) under Interagency Agree¬ment Number DW89938513-01-0. The Superfund Innovative Technology Evaluation (SITE) demonstration program was also involved in the project. MSE Technology Applications Inc. (MSE), Butte, MT, was the contractor responsible for conducting the project, and Pintail Systems Inc., Aurora, CO, was the technology provider. The pilot-scale unit was field-tested at Echo Bay's McCoy/Cove Mine southwest of Battle Mountain, NV. The biotreatment process was considered successful in destroying cyanide in the mine process water. The process was also determined to be effective in removing metals. The pH was consistently neutralized and nitrates were successfully removed from the mine process water. From the results of these pilot-scale tests, it was concluded that the biotreatment process potentially of¬fers an innovative, cost-effective alternative for the treatment of mining wastewaters.

Jan 1, 2000