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By V. Rajaram

A mine fire or roof collapse may necessitate the reversal of main fans to isolate the fire or provide an escapeway. Hence, to assist the mine operator in estimating the flow and pressure during reversal, Engineers International Inc. conducted a laboratory and field study of the reverse performance characteristics of main mine fans. Laboratory tests were performed using a 2.4-m (96-in.) diam vane axial fan to establish the forward and reverse performance characteristics under controlled conditions. Subse¬quently, a field test was conducted in a Colorado oil shale mine during which two 2-m (79-in.) diam fans were reversed. The data obtained indicate that reverse performance characteristics depend on the blade angle and the hub-to-tip ratio. The quantity in the reverse mode ranged from 30% to 65% less than in the forward mode, and the static pressure was directly proportional to the square of the quantity.

Jan 1, 1987

By Eric K. Albert

Computer oriented simulation techniques can be effective in the design and analysis of complex mining systems. In fact, a number of computer software products are available for mine systems simulation. However, previous models have tended toward being either data-intensive and deterministic, or data-limited and highly stochastic. The need for a fully integrated package with a simplified user interface has never been more apparent. In this paper, the design of a surface mining simulation model documented in Albert (1986) is described. The basic features of the surface mining system and their counterparts in the simulation model are discussed. The methods and algorithms used to implement these subsystems are presented. Considerations of information management and software design are illustrated, especially as they apply to the application of the package by a mining engineer. An example is provided to demonstrate the concepts embodied in the model and to show how a surface mine is simulated from mine parameters.

Jan 1, 1989

By Rick Sarkisian, Albert D. Bonneau, David Keech

The Drummond Co. Inc.'s Shoal Creek Coal Mine Slope Belt Conveyor transports 5000 mtph (5500 tph) of material over a length of 1400 m (4600 ft.) and a lift of 3609 m (1180 ft.). Four 1500 kW (2000 hp) motors power the 1830 mm (72 in.) Goodyear Flexsteel 5800 steel cable belt. In May 1993, Dodge Manufacturing was selected to design and build the conveyor pulley assemblies for this conveyor. The conveyor includes five pulley assemblies. The 2135 mm (84 in.) diameter by 2135 mm (84 in.) face primary and secondary drive pulleys were designed for a resultant belt load of 3060 kN (688,000 Ib.) This paper describes the design and manufacture of the two drive pulley assemblies. Design details included are component evaluation, material selection, locking assembly selection, bearing selection and lagging selection. Manufacturing details include material procurement, welding process, lagging installation and component assembly. Quality control procedures are also discussed.

Jan 1, 1996

By James Warren Andrews

The values of saturated water vapor pressure from steam tables have been found to be inaccurate for mine ventilation usage because the effect of air on the saturated water vapor was disregarded. Presented here are the newest and most accurate currently available tables from the National Bureau of Standards (NBS). Also included are: (1) a formula for correcting the saturated water vapor pressure for temperature and altitude. (2) a formula for computing unsaturated water vapor pressure, and (3) a formula for air density. Because Systeme International (SI) units are used in the formulas, conversions are given from U. S. conventional units to SI units. The intent of this paper is to show by means of six steps the accurate calculation of mine air density for use on modern computers.

Jan 1, 1989

By Alexandr A. Abramov, Svetlana M. Angelova, Oleg P. Maljuk

In this paper the effect of the ratio of grinding and grindable size classes (ore lumps, particles and grains) and the guantity of intermediate size classes in the feed of the primary wet autogenous grinding "Cascade" mill is studied and the features of the influence of these factors on the mill capacity are shown. On the basis of the experimental data from Lebedinsky mineral processing plant, where magnetite guartzites are processed, a coefficient of the "total ratio of size classes" in the feed of 9x3 m "Cascade" mill was estimated. It helps to get an evaluation of the effect of ore size classes ratio in mill media on the mill capacity and to work out some ways for its optimization in closed or semiclosed technological circuites of primary autogenous grinding. The operation of the specific energy effects for some intermediate size classes, removed from the mill as circulating load, is proposed to improve its efficiency before regrinding in "Cascade" mill and decrease negative influence of such classes accumulation in the mill media.

Jan 1, 1995

By J. R. Sturgul

Computer simulation models of working mines can be a great benefit to mining engineers. Such models have been used in mine planning (how many trucks-shovels to have, when to add new equipment, etc.) and mine design (should a dispatch system be purchased, where is the optimum location, for mine equipment, etc.). A simulation model can be thought of as a dynamic representation of the mine. It can be easily changed to reflect a variety of situations. A major problem for the engineer is how to present the results of the simulation study. This has now been overcome by means of animation to present the results of the simulation. The main simulation languages in use for discrete system simulation are SLAM, SIMAN and GPSS/H. Each has animation with SLAMSYSTEM for SLAM, CINEMA for SIMAN and PROOF for GPSS/H. Animation with SLAM and CINEMA have been on the market for several years whereas PROOF is a relative newcomer and has features not found in other animation software. This discussion will be confined to PROOF. Some of the comments will apply to all simulation and animation software.

Jan 1, 1995

By J. G. Groppo, B. K. Parekh

Column flotation testing was conducted on the flotation feed slurry obtained from a preparation plant located in the Southern Illinois coal basin. The column flotation tests were conducted using three different bubble generating devices: a static sparger, a gas saver and a foam jet. Each of these devices was tested with three different types of frother and various column operating variables to provide maximum combustible recovery, minimum product ash and maximum pyrite rejection. The results show that column flotation provided improved flotation performance, in terms of combustible recovery as well as ash and pyrite rejection, for each of the bubble generating devices. However, the effectiveness of each bubble generating device was dependent on the type of frother used. Alcohol frothers were most effective for use with the static sparger, somewhat less effective for the foam jet and ineffective for the gas saver. Glycol frothers were effective for all three bubble generating systems, providing high combustible recovery (>90%); low clean-coal ash (4-6% ash) and high pyrite rejection (70-80%).

Jan 1, 1994

By N. I. Aziz, B. Srinivasa Rao, R. N. Singh

The control of respirable dust and its subsequent exposure to miners is essential for improved safety in longwall mining. The extensive variation in face conditions and operations of longwall make numerical modelling an attractive approach in both the development and evaluation of dust control devices. Three dimensional finite element computational fluid dynamics code FIDAP was used to model air velocities and the effect of dust control techniques on dust concentrations at a typical longwall face. The effect of shearer body on airflow characteristics in a longwall face was analysed with both antitropal and homotropal ventilation systems. Path traces of particles introduced near the shearer drums was also simulated. Initial modelling results were validated using field trial results at three operating longwall faces. Results of simulations tallied very well with the field results.

Jan 1, 1993

By J. A. Brierley, Arpad E. Torma, Victor C. Storhok, C. L. Brierley, Batric Pesic

Chemical and electrochemical studies were performed during bioleaching of cobaltite concentrate with Thiobacillus ferrooxidans. The two principal minerals present in the concentrate were pyrite and cobaltite (CoAsS). During chemical studies, the effect of pH on dissolution rates was examined under uncontrolled and pH-controlled conditions. It was found that in the pH range 1.5-3.0 there was no pH effect if the initial pH was not controlled (maintained). When the initial pH was controlled, the leaching of Co, As, and Fe depended strongly on pH. Electrochemical studies were performed by using cyclic voltammetry and constant potential techniques. A sequential reaction mechanism was proposed for dissolution of cobaltite.

Jan 1, 1993

By N. R. Paterson, D. A. MacFadyen

A late-1980 airborne EM/magnetic method test over the State Line kimberlite area of Colorado-Wyoming shows weak but recognizable anomalous responses to the known pipes. The magnetic survey indicates the presence of several shallow subsurface bodies adjacent to the known kimberlites, which are interpreted as possible blind diatremes. The survey data, in profile and contoured map form, has been correlated with geological map information available at the time. It can serve as the basis for reexamining kimberlite distribution in the area, taking into account geological findings during the recent work on known bodies.

Jan 1, 1987

By D. E. Walsh, J. T. Hollow, H. K. Lin, J. L. Oleson

At the Fort Knox Mine, Fairbanks, Alaska, carbon fines are generated during stripping, acid washing and kiln regeneration operations. Because of their gold value, carbon fines are collected by a filter press. Samples of the carbon fines show that they consist of 20% to 30% carbon, 70% to 80% grit and 0.17 to 0.68 g/kg (5.0-19.9 oz/st) gold. About 80% of the gold values in the carbon fines used in this study are in the form of recrystallized free gold grains, with the balance being the adsorbed gold on the carbon. High recoveries of gold and carbon were obtained from the fines in laboratory tests using froth flotation, with a high rejection of the grit. More than 95% of gold and 90% of carbon can be recovered by three stages of gold flotation followed by two stages of carbon flotation. Key words: Gold recovery, Activated carbon, Flotation

Jan 1, 2003

By John B. Comer

Compelling evidence indicates that at least the plateau bauxite of northern and central Jamaica formed from volcanic ash. The predominance in plateau bauxite of zircon grains younger than the host limestones and the relative abundance of zircon grains having idiomorphic form support a direct ash-fall origin for much of the bauxite parent material. Based on revised mass balance calculations, not enough of the middle Eocene to lower Miocene host limestones have been dissolved to make an important contribution to bauxite. Likewise, the pre-middle Eocene rocks of Jamaica have made only a very small contribution to plateau bauxite; they may have made a more significant contribution to the graben bauxite of southern Jamaica.

Jan 1, 1984

By V. T. Vacariu, P. D. Georgescu, N. Tomus

To assess the potential for radioactive pollution unique to the environmental conditions of the Bacau phosphogypsum waste dump, surface samples were taken, drillings were performed on the entire waste dump's height, and the Ra226 distribution on the height and surface considered to contain a medium content of the radium of 0.57 Bq/gr was studied. Thus, the waste dump's radioactive potential was estimated at 30-40 Ci in equivalent Ra226. Also analyzed was the granulometric composition of the phosphogypsum and the distribution of Ra226 on granulometric orders, which indicated that the radium was concentrated in the very fine fractions. Parameters were set up for the classification by hydrocycloning to obtain a fine class (less than 41 microns) having a radium content of more than 0.9 Bq/gr and a coarse class having less than 0.37 Bq/gr. A chemical process was devised for removal of the radium from the phosphogypsum with the possibility for recovering the contained sulfur.

Jan 1, 1999

By B. D. Shah, H. S. Soto

Lack of selectivity in mixed mineral flocculation can be attributed to one or more of the following factors: dissolved ion interference, hetero- coagulation, mechanical entrapment in flocs, and entrainment of fines between flocs. In a study of the apatite-dolomite system, it was determined that dissolved ions do not have a significant effect on selectivity. Heterocoagulation was minimized by choosing proper process conditions and addition of a dispersant. Mechanical entrapment was proved to be insignificant and efforts were made to reduce entrainment by choosing an appropriate method of separation of flocs from fines. A new factor termed "polymer induced entrapment," which occurs due to limited affinity of the polymer to the mineral that is not flocculated, is postulated to be the cause for the loss of selectivity.

Jan 1, 1988

By L. M. Gochioco

The Seismic Interactive Interpretation Workstation (S//W) provides a wide spectrum of utilities ranging from improving field acquisition techniques, data processing and interpretation of coal seismic data. The power of the workstation lies in the interpretation process where various sets of geophysical and geological data are integrated to form a network of information that is stored in a database. Computer models are generated from known borehole and geologic information and later cross-correlated with the processed seismic data. Structural and stratigraphic modeling techniques add another dimension to the interpretation process. Complex trace attributes highlight subtle features not easily observed in black and white sections. Using the computer workstation, the explorationist gains valuable insight and conducts more intelligent interpretation of seismic data through a more comprehensive network of data analysis.

Jan 1, 1992

By P. Somasundaran, C. C. Harris

The power consumption of stirred-media mills was studied using an approach developed from work on stirred reactors. Evaluated were the relationships of factors such as stirring speed and impeller and tank dimensions on the torque required to rotate disc and pin impellers immersed in dense particulate media. Data collected under carious experimental conditions were analyzed. The results were summarized and presented in the form of characteristic plots, general equations and dimensionless group correlations involving power and modified Reynolds numbers. Special attention was directed towards the rheological properties of the media, which was considered a non-Newtonian liquid, and hence the equation of power-law liquids was employed. A procedure for estimating the parameters of effective viscosity and scale-up guidelines (with respect to power consumption) are proposed.

Jan 1, 1996

By R. E. Ray

As coal reserves at shallow depths continue to be exhausted, a number of US coal companies are developing seams previously considered too deep to mine economically. Because of increased cover load, mines operating in deeper seams face unique ground control problems. In addition, the volume of methane gas in coal beds increases with depth, and ventilation requirements are much more stringent for deep mines than for shallower mines. When the longwall mining method is wed at great depths, ventilation, ground control, and operational considerations all influence the design of longwall panels. This paper examines these influences, particularly ventilation and operational considerations, on the feasibility of two-, three-, and four-entry longwall development panels in Jim Walter Resources' four deep mines.

Jan 1, 1988

By J. J. Davis, C. A. J. Fletcher, M. Li, T. Jancar

This paper summarises the experimental approach to spiral modelling at the Julius Kruttschnitt Mineral Research Centre, University of Queensland, involving the use of plastic density tracers to determine partitioning performance on three models of coal spiral. This work has led to phenomenological models of the three spiral profiles most widely used in the Australian coal industry. The results from a parallel computational fluid dynamics approach to spiral modelling currently underway at the University of New South Wales are also presented. The computational simulation has been successfully applied to generic spiral geometries and is capable of predicting the fluid phase three dimensional flow fields and corresponding free surface profiles for moderate Reynolds' number and Froude numbers. Simulation predictions are compared with experimental results from a Mineral Deposits LD9 coal spiral.

Jan 1, 1995

By H. Y. Sohn, M. Pérez-Tello, J. Löttiger

An investigation of the oxidation reactions of two industrial copper mattes was performed using dflerential scanning calorimetry (DSC) and thermogravimetric analysis (TGA) at heating rates of 20°C and 8°C/min, respectively. The temperature of incipient reaction, the total exothermic and endothermic heats of reaction and the weight change during the oxidation process were measured as functions of the oxygen concentration in the oxidizing gas, matte grade and matte particle size. The temperatures of incipient reaction measured from the DSC experiments were found to increase monotonically with all three input variables. TGA experiments showed that Cu2O and CuO CuSO4 are formed before the complete oxidation of Cu2S to CuO.

Jan 1, 2000

By J. G. Groppo, J. G. Justice, B. K. Parekh

Removal of particulates and/or metal ions from mineral/coal processing waste water is a necessity from the environmental point of view. This paper describes application of a novel AC- electrocoagulation technique to remove the particulates as well as metal ions using AC power. A series of laboratory tests conducted on a stable black water sample obtained from a sub-bitminous coal operation provided a clear supernatant (-10 NTU) from the suspension. The process also shows promise in removal of up to 90 percent of phosphate ions and other metal ions (copper and nickel) from solution. A preliminary economic evaluation of the process will also be included.

Jan 1, 1992