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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 S. Bassignani, D. Ippolito

In Italy at the moment there is a program which involves for the future the exploitation of two uranium mines which are now in the research stage. About one hundred and fifty workers are at present employed in those facilities. An health physics surveillance program is under way and has been designed to fulfill the requirements due to the future exploitation of the two mines. A complete evaluation of the total dose (external + internal) received by the workers will be given together with a detailed analyses of the technical methods employed for such evaluations. The external doses are evaluated on the basis of individual TLD dosimeters, while the evaluation of the internal doses is mainly due to an enviromental survillance program of the radon and radon daughter air concentration inside the mines. The criteria established for the assessment of the sampling procedures, sampling intervals and dose evaluation related to the radon doughter exposure are reported. The external dose received by the workers are lower than 0.2 m Sv~month and the internal exposure less than 6.4 IO-3 J.h.m-3 /year or using the old units 2 WLM/year.

Jan 1, 1981

By D. R. Spears, D. A. Stanley

The US Bureau of Mines investigated the fundamental aspects of shear-flocculation using a rapid, in-situ particle size analyzer. Silica was stirred in the presence of an aliphatic amine to determine the effects of collector coverage, stirring speed and solids concentration on the kinetics of shear-flocculation. The results showed that shear flocculation is a two-stage process. In the first stage, which occurs during the first 1-2 min. of the reaction, the mean particle size increases rapidly, and in the second stage, an equilibrium is set up between the rates of floc growth and floc decay. Collector dosage affected the position of the equilibrium by altering the number of surface sites for particle-particle attachment. A minimum stirring speed was necessary for shear flocculation, which was dependent on solids concentration and collector dosage. This stirring speed was the minimum necessary for particles to overcome the electrostatic energy barrier, and that results in keeping the conditioned particles dispersed. Larger particles flocculated more rapidly. At very high stirring speeds, large flocs became unstable, resulting in a narrowed particle size distribution in the slurry.

Jan 1, 1995

A new separator, known as the HydroFloat cell, was developed to overcome the limitations of traditional flotation cells in recovering coarse particles. The HydroFloat cell separates particles based on differences in mass after the selective attachment of air bubbles to the hydrophobic component of the feed stream. Proof-of-concept testing, utilizing phosphate matrix, heavy mineral sands and anthracite slag, indicated that significant improvements in separation efficiency can be achieved using this air-assisted teeter-bed system. Based on the encouraging laboratory results, a pilot-scale HydroFloat cell was fabricated and installed at a central Florida phosphate plant. Test data collected using the pilot-scale unit suggest that the BPL recovery of the +35-mesh plant feed can be increased by snore than 40% through the application of this new technology. This improvement is particularly beneficial due to the very high grade (-73% BPL) of the +16-mesh particles in the HydroFloat concentrate. This article describes the theoretical basis for the development of the HydroFloat cell and provides an overview of recent laboratory and pilot-scale test results.

Jan 1, 2002

By Richard Jr. Ray, Richard Druesedow

The Virginia Operations of Consolidation Coal Co. include a diversity of mine fan configurations which have been tested to quantify pressure losses through the inlet ductwork. Airflow and pressure measurements were taken at four shaft sites to calculate losses for the 90-degree bend at the top of the shaft and the self-closing dampers or closing doors located between the shaft and fan. Velocity contours were then developed from the test data to determine flow patterns in each fan system component. In addition, yaw and pitch angles of airflow through the fan annulus were measured to evaluate turbulence levels created by various inlet ductwork designs. The test results indicate that proper design of the shaft collar and ductwork arrangement for main mine fans can substantially reduce system pressure losses and air turbulence. BY minimizing the pressure drop experienced on the surface, these design improvements enable the bulk of the total pressure developed by the fan(s) to be utilized in the mine.

Jan 1, 1995

By F. K. Letowski

Leaching of zinc sulphide concentrate by nitric acid which is simultaneously regenerated by oxygen in the reactive froth has been investigated. The reactive froth was formed by a recycled zinc sulphate electrolyte containing nitric acid, a mixture of gaseous 02 and NOx, entrapped in the foam and particles of the zinc concentrate suspended in the foam. In the reactive froth the multiple regeneration of nitric acid proceeded owing to the encapsulated oxygen and amount of nitric acid used can be considerably lower than in the continuous liquid phase. 93 to 97% of zinc was extracted to a solution containing 30 to 409/1 HNO, during 40 to 60 min of leaching in a batch reactor without regeneration of nitric acid. 50 to 100% of the consumed nitric acid was regenerated during continuous leaching in froth carried out in the ‘flotation column’-type reactor at 80 to 90°C and under pressure of 100 to 200kPa. The rate of HNO, regeneration in the froth was proportional to oxygen pressure and inversely proportional to nitric acid concentration in the froth. A two-stage process flowsheet is proposed. In the first, the reduction stage, removal of nitric acid from the leach solution directed to standard purification and electrolysis is carried out by its reduction to nitric oxide using fresh concentrate in the froth. In the second, the oxidation stage, nitric acid is continuously regenerated by oxygen in the froth.

Jan 1, 1995

By Marvin Barnes

The Sacaton mine is a relatively new open¬pit copper mine owned by Asarco, Inc., which has been in production only a few years. The mineral deposits consist of two ore zones; a western, near-surface zone minable by open-pit methods, and a deeper eastern zone which will have to be mined underground, probably by block caving. The copper deposits are related to small quartz monzonite intrusives implaced into Precambrian granites. Both rock types act as hosts for the copper mineralization, which has been secondarily enriched sufficiently to constitute ore. In the western zone the enriched supergene chalcocite has been subjected to postenrichment oxidation processes with partial destruction of the chalcocite blanket. The deeper eastern chalcocite zone has not been as severely affected by later supergene processes. Several mineralogical populations are represented in the total copper deposit. Leached capping overlies the chalcocite enriched zone, and in the western ore body there is a very irregular interface between the leached and enriched zone, which is complicated by oxide copper minerals irregularly distributed. Primary lower-grade chalcopyrite mineralization occurs below the enriched zone. When mining commenced near the top of the enriched zone, considerable difficulty was encountered in correlating the actual grade of ore in place with the estimated grade of the mining blocks. The mineralogical complexity and fairly wide spacing of diamond drilling made reliable grade estimation of individual ore blocks a difficult procedure.

Jan 1, 1979

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

Overview In 1992, US coal supply and demand were shaped more by weather conditions and the export market than by the economic recovery. Preliminary data compiled by the Energy Information Administration (EIA) (Table I) show that coal production declined slightly to 902 Mt (994 million st). Consumption, though, rose by about 1 % to 811 Mt (894 million st), trailing the 2.1 %growth in Gross Domestic Product. Contributing to the decrease were a sizable drop in coal exports and some coal stock withdrawals. Consumption increased largely because electric utilities turned to coal to offset a shortfall in hydroelectric generation caused by a drought in the Northwest. Apart from this, the demand for coal-fired generation was dampened by a mild winter in the northwestern and northcentral United States, and a cool summer in the central and eastern parts of the Nation. Coal use by other consumers was about the same as in 1991. The average delivered prices of coal to all consuming sectors decreased slightly in 1992, reflecting soft coal markets (Fig. 1). US coal exporters experienced a set-back in 1992 mostly because of losses in the European market. Total coal exports fell by 6% to 93 Mt (103 million st), the first decline since 1987. Coal stockpiles at the end of 1992 were about 1.8 Mt (2 million st) below 1991, despite stock buildups by some electric utilities in the East. Stocks were built up as a hedge against possible coal miners' strikes after the Feb. 1, 1993, expiration of the contract between the United Mine Workers of America and the Bituminous Coal Operators' Association.

Jan 1, 1993

By F. M. Doyle, S. Duyvesteyn, K. Sreenivasarao

Toxic metals entering surface or ground water from sources such as metal finishing shop spills and abandoned mines can pose a significant threat to public health and the environment. Ion flotation and similar foam separation techniques show great promise for treating dilute, metal-contaminated solutions, and could also be used to treat effluents from many minerals and metallurgical processing operations prior to discharge. In ion flotation, an appropriate collector is added to the solution to form hydrophobic complexes with the metal ions. These metal-bearing species are then removed by flotation, usually with trace addition of a frother to stabilize the foam. In an effort to better understand the underlying scientific and engineering principles that determine the performance of ion flotation, the removal of Cu(II), Pb(II), Cd(II), Cr(II) and Cr(VI) has been studied using laboratory scale flotation columns in batch mode. The effects of the superficial air velocity, solution and froth height, nature of the collector, collector: metal-ion ratio, ionic strength and several frothers at low concentrations on the flotation kinetics are reported. Finally, results are presented on methods that might allow regeneration of collector and recovery of by-product metal from the foam product.

Jan 1, 1995

By David J. Brown, Richard C. Fountain, Marc V. Hurst

The Central Florida Phosphate District, one of the most productive phosphate districts in the world, has been mined principally within Polk and Hillsborough Counties, Florida. Recent development is extending the district southward into Hardee, Manatee, and DeSoto Counties. This area is known as the Southern Extension. The combined area of these two phosphate-bearing areas encompasses about 2,000 square miles. Structurally, the district and its Southern Extension lie at the southern end of the Ocala Arch and are flanked by the Hillsborough High to the northwest. South of this area is the South Florida Embayment. The Osceola Low lies to the east. The phosphorite within the Central Florida Phosphate District generally dips very gently (<0.1°) to the south. The boundaries of the central Florida Phosphate District are generally defined by thinning of the phosphorite due the adjacent structurally high areas to the north, west, and east, and by increased clay, CaO, and MgO content reflecting lithologic differences to the east and south. The Bone Valley Member of the Peace River Formation and reworked sediments of more recent age were the primary ore-bearing horizon in the Polk-Hillsborough County area. As those reserves are depleted, the less desirable phosphorites of the Peace River Formation are being exploited in the Southern Extension.

Jan 1, 1993

By R. Venugopal, T. C. Rao, M. Vanangamudi

Introduction The kinetic approach, to understand a process in detail, has been extensively used in the unit operations of many engineering systems. In green pelletization, the kinetic studies have been mainly oriented towards quantifying the growth mechanism (Kapur and Fuerstenau, 1964; Sastry and Fuerstenau, 1977; Capes and Danckwerts, 1965; Kapur and Fuerstenau, 1966; Kapur, 1972) and in a few cases, relating the rate of growth with added liquid content (Kapur and Fuerstenau, 1964; Newitt and Conway-Jones, 1958). Studies on the kinetics of green pelletization, in terms of the order of the kinetics are virtually non-existent. Sastry and Fuerstenau (1970) classified the agglomeration process into "free in-space" (dilute particle system) and "restricted-in¬space" (highly dispersed particle system) and noted that the former is a second-order process while the latter corresponds to a pseudo first-order rate process. The present paper attempts to describe the kinetics of green pelletization, in terms of order of the kinetics, using pyritiferrous shale as the material system. Experimental Pelletization experiments were carried out using -100 mesh pyritiferrous shale, in a laboratory disc pelletizer, at four intervals of pelletization time (15, 20, 25 and 30 min). The green pellets obtained were size analyzed. The size distribution of pellets has generally been represented by a single parameter such as the mean granule diameter, ratio of maximum and minimum pellet diameter, etc. In the present study, the d50 (50% passing size) of pellets has been considered to represent the size distribution of pellet. Kinetic equations The process of size enlargement is considered analogous to chemical reaction and a general kinetic equation of nth order for growth of pellets is given as

Jan 1, 1990

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

The stability of mine roofs in permafrost zones is determined mainly by temperature and ice content. The deformation resulting from creep and temperature-dependent physical properties of frozen rock mass is the dominant component of total deformation. Roof bolts can consolidate the roof and control its deformation. In this paper, a finite-element model, for the analysis of the effects of roof bolting in a frozen rock mass is presented. The model includes the variables normally encountered when analyzing the effects of roof bolting in rocks. It also accounts for properties unique to frozen rock mass: creep deformation and the change in Young&apos;s modulus with changing temperature. The model shows that, as bolt spacing decreases, there is a trade-off between increased roof stability from increased mechanical support and decreased stability from increased conduction of heat into the frozen roof. This result was expected and shows that, for a given set of rock-mass conditions, including ice content, temperature, particle size, etc., there is an optimum bolt length and bolt density for minimum roof deflection.

Jan 1, 1997

By Neil B. Prenn

Drill-hole contamination has been a problem for many years. Contamination of rotary drilling has been well documented. More recently contamination in wet reverse circulation drilling has been noted by Echo Bay and others at the 1991 AIME annual meeting. Mine Development Associates (MDA) has worked on a number of projects at which contamination of drill-hole samples has occurred. Properties are commonly acquired with drilling accomplished by other companies and at times the only records of the drilling program are the drill-hole logs and assays themselves. Identification of contaminated zones is sometimes difficult to determine. Most geologists and engineers in the industry are aware of the magnitude of the problem, as contamination is a relatively common problem with wet reverse circulation drilling. MDA has developed a computer program to help determine if contamination has occurred when using reverse circulation drilling, based on cumulative distribution curves and by a process we call decay analysis. Most deposits are not homogeneous throughout the deposit, but exhibit a characteristic drop-off or decay of assay values around higher-grade drill-hole intercepts. Using graphs of this characteristic decay and cumulative frequency distribution, we can use the program to help determine contamination in several ways. This paper will discuss the use of decay analysis at three gold deposits where contamination is known to have occurred. In one of the deposits decay analysis was used, successfully to determine if contamination had occurred, while in the other two the decay analysis was used to verify our decay analysis procedure.

Jan 1, 1992

By Guiseppe Bonifazi

This work applies the definition of "separation function" already introduced in the paper presented at the XVIII IMPC. This &apos;function" (defined for a certain size distribution after comminution of an ore) refers to the recovery distribution of a mineralogical species in a product made up of all the particles having at least a given content of that species. Many tests would be required to determine the liberation function for each mineralogical species, particularly for complex ores. Several stages of comminution would need to be examined and the mineralogical composition of the particles of each grain size class would need to be analyzed for each process step. A quick and dirty method is shown for obtaining the "separation function". It is based on the processing of data from topological maps of polished and/or thin representative sections of ore. By superimposing grids of different sizes over these maps and with appropriate combinations of mesh sizes, it is possible to simulate the grain size distributions linked to different stages of comminution and then evaluate the mineralogical composition of each grain. The procedure is carried out full automatically and can simulate a complete treatment circuit, imposing cut-off grades for the products at each separation phase. It is also possible to predict the results of treatment processes that involve grinding phases. The procedure has been successfully applied to complex ores containing several useful components.

Jan 1, 1995

By A. Bumanis, K. S. Bawa

INTRODUCTION A rail rapid transit system called the "Metro" system is presently under construction in the Nation&apos;s Capital area. The agency responsible for the design and construction of the Metro system is the Washington Metropolitan Area Transit Authority, an independent tristate organization set up under an Act of Congress and financed by federal, state, and local public funds supplemented by revenue bonds. When completed, the Metro system will comprise nearly 100 route miles. About fifteen percent of this mileage is now under construction, while designs for the-remainder are in progress. The system is scheduled for completion in about eight years at a cost of approximately 3 billion dollars. The Metro system will involve nearly all types of construction generally used for rapid rail transit projects. About half of the mileage will be underground, comprising approximately 16 miles of rock tunnels, 10 miles of earth tunnels, and nearly 21 miles of cut-and-cover construction in earth (see Figure 1.). The remaining 51 miles of the system is planned to be constructed on the surface as at-grade or elevated structures. The system includes 86 passenger stations, 53 of which will be underground structures. Twelve of the underground stations will be large size chambers in rock while other underground stations will be constructed in earth as cut-and-cover structures. Thus, about one-fifth of the system will be designed as underground structures, namely tunnels and stations, in rock. Such designs in rock resulted from the existence of bedrock (schistose gneiss) at reasonable depths generally in the north and northwest

Jan 1, 1997

By J. Pflieger

The International Iron and Steel Institute (IISI - http://www.worldsteel.org) has initiated the development of a comprehensive freely-available, internet-delivered package of highly interactive e-learning resources for undergraduate students and steel industry employees. The resulting e-learning environment (http://www.steeluniversity.org) creates a ?one-stop? shop covering all aspects of steelmaking, steel products and applications, the underlying scientific and engineering principles, industrial and academic collaboration, as well as environmental and sustainability issues relevant to the steel industry. The module entitled ?Sustainability, Steel and the Environment? of the steeluniversity.org provides interactive e-learning resources on the following topics - Sustainability. - Principles of Life Cycle Thinking. - Environmental Life Cycle Assessment. - Application of Life Cycle Assessment. The aim of this particular module is to enable the learner to identify relevant environmental parameters over the life cycle of steel products as well as to learn about the resulting environmental effects and impacts. Furthermore he/she will be enabled to explain the basic idea of Life Cycle Thinking and Life Cycle Assessment (LCA) in terms of Goal and Scope definition, System Modelling, Life Cycle Inventory (LCI), Life Cycle Impact Assessment (LCIA) and Interpretation. In addition, the learner can explore selected LCA scenarios facing the steel industry and its customers in the automotive and construction sectors.

Jan 1, 2007

By Samuel Frimpong

In this paper, the authors present a typical mine profitability model. The method of generating system moments is used to examine the sensitivity of the profitability function to changes in the dependent variables, and to express the expected risk associated with undertaking the project in a predicted economic and technical environment. Profitability of a mining venture is a function of many variables ore grade, capital and operating costs, milling efficiency, ore reserve tonnage and annual tonnage, equity - loan structure, tax regime, etc. Estimates of the expected value and the variance of the profitability function are obtained by calculating the partial derivatives of the function with respect to the dependent variables, using the Taylor series expansion method to the second order. Sensitivity analysis is carried out by examining the effects of each variable on the profitability function, which is determined by the magnitude of the product of its partial derivative and variance. An appropriate probability density function, based on the expected value and the variance of the profitability function, is assumed to estimate the expected risk associated with the project. This expected risk is a measure of the area under the profitability density function below the appropriate, selected discount rate or the cut-off net present value (NPV). The results are compared with those obtained by using the Monte Carlo simulation technique, and they show that either of the two methods could be used to evaluate the probability of project failure or success with no significant difference.

Jan 1, 1992

By Thomas H. Koenning, William E. Bruce

The importance and complexity of the ventilation systems in many underground coal mines necessitates the use of digital computers to model the ventilation networks. The modeling procedures used by the Mine Safety and Health Administration (MSHA) utilize the MSHA-modified Penn State computer program. The basic techniques used by MSHA have been described in detail in NESA (now MSHA) Informational Reports 1066 and 1183 (1. 2). Two basic methods are utilized for modeling underground mine ventilation systems. The first modeling method is the use of actual air-flow, pressure, and fan-performance data acquired during a full air-pressure, air-quantity ventilation survey to develop a mathematical model of the ventilation system. The second modeling method is the design of a ventilation system using data obtained from calculation, from past experience, or from technical literature. The latter method would typically be used to design a ventilation network prior to developing a new mine. Regardless of which method is used for modeling, there is a need to know, or to calculate, appropriate resistance values to be used for airways and for the various ventilation control structures. Such data is typically difficult to obtain and this report is an attempt to summarize typical resistance values which may be used in designing ventilation networks for new mines or in simulating proposed system changes in existing mines. Illustrations are presented to show where some of the resistances typically are located and how they are modeled in mine ventilation net- works.

Jan 1, 1987