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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 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 Charles Dr. Li, John Dr. Box

Selective flotation and adsorption behavior of zircon and rutile under hot soap conditions have been examined. Conditioning temperature, pH and washing steps were shown to control the flotation selectivity. The adsorption of the sodium soap of oleic acid at zircon- water and rutile-water interfaces was investigated through micro- electrophoresis and adsorption density measurements. The soap adsorption on the zircon surface increased markedly with increasing temperature due to a strong chemisorption/surface reaction, and was almost independent of pH. In contrast, the soap adsorption on rutile decreased at high pH values. A simple physisorption plus hydrophobic interaction appeared to be the principal mechanism for the soap adsorption on rutile at moderate temperatures (below ~70(C), beyond which it may change to chemisorption through an activation process. Water wash, particularly under acidic conditions (pH 2-3), of the rutile particles treated with soap, will lead to a desorption of the soap from the rutile surface by forming an acid salt precipitate.

Jan 1, 1995

By C. Patrick

Annually, the US coal industry generates and must dispose of over 200 million st (180 million t) of coal refuse, expanding a major environmental problem. The purpose of this research was to investigate the feasibility of utilizing coal refuse as an aggregate in concrete. This paper reports on findings of the initial phases of a project to determine the viability of replacing traditional concrete blocks with refuse blocks for use in ventilation stoppings in underground mines. Refuse, collected from three active preparation plants in eastern Kentucky, was used as the primary as aggregate in the preparation of concrete cylinder. Stress-strain analyses on the refuse cylinders yielded compressive strengths of from 59% to 77 % of the control-group strengths. Low variability within the groups was found while significant differences between the groups existed. On-going determinations of the effects of weathering on the refuse cylinders is being conducted and will be completed in early 1995. The research results are favorable for the future direction of the overall project objectives.

Jan 1, 1997

By Don C. White

Santa Rosa is a mid-Tertiary, volcanic-hosted, gold-silver deposit. Current proven and probable reserves are 8.9 Mt (9.8 million st) grading 1.5 g/t (0.044 oz/ st) gold, minable by open pit and amenable to heap leaching. It is the product of hydrothermal mineralization along an arcuate segment of a caldera collapse ring fault in a probable maar volcanic setting. This segment was later broken by radial faults. Gold at Santa Rosa occurs principally as electrum, finely disseminated through intermediate tuffs, and associated with pyrite. The nearby Alto de la Mina deposit displays stockwork silica-pyrite-gold in a tectonically and hydrothermally shattered andesite flow. Miocene epithermal mineralization was accompanied by central silicification and pyritization and more distal argillization. An andesite flow cap rock at Santa Rosa played a pivotal role as an upward permeability barrier. Highest gold grades and most intense alteration occur closest to the ring faults and immediately beneath the andesite flow. Supergene alteration effects on the gold distribution are minimal.

Jan 1, 1995

By R. J. Sweigard

Many states are considering the need to establish or modify policy relating to the disposal of coal ash. One of the primary concerns is the impact of leachate from the ash disposal sites upon groundwater and nearby bodies of surface water. A detailed site investigation was conducted at a coal ash disposal facility associated with a power generation station. The disposal site is situated alongside a major river. Monitoring wells were installed and soil samples were taken for characterization. Groundwater models were used to simulate migration of leachate from the disposal site toward the river. Such models have the potential to be used to verify regulatory compliance. This paper addresses the validation and adaptability of these models to this case and their usefulness as possible tools to be used in future environmental audits.

Jan 1, 1993

Coal that meets customer specifications is often stored in silos prior to being loaded into railcars. However, it is often found that, after loading, the coal contained in a particular car does not meet customer specifications. This can occur because of the variability inherent in the coal and because of segregation, mixing and flow inside the silo. Some contracts now require the coal in each car to be within specification. Silo flow models are used to predict quality in such cases. However, developing an accurate silo flow model for each case is difficult and time consuming. This paper examines the viability of using an online analyzer in conjunction with a feedback circuit to optimize the quality of the coal being loaded into trains, so that each car meets the quality specifications.

Jan 1, 2002

By J. Hong, K. Han, C. Park, C. Yoon, H. Yoon, N. Kim

The contents of three platinum group metals (PGM-platinum, palladium and rhodium), from the spent automotive catalyst, and two NIST SRM (National Institute of Standard and Technology Standard Reference Material, Used Auto Catalysts) were determined by the X-ray fluorescence (XRF) spectrometry. The XRF technique has been proven to be a fast, effective and accurate method in determining not only PGM but also other solid materials of less soluble for wet digestion analysis. The detection limit of the XRF analysis is better than that of the inductively coupled plasma mass spectrometry which usually requires significant dilution to avoid high dissolved solid concentration. However, the XRF technique suffers from a strong matrix dependent problem. The objective of this study was to examine the applicability of the XRF analysis where the sample matrix was not exactly the same as the standard materials with particular reference to PGM analysis. This study enabled to compare the effect of various matrices including alumina, iron, copper and nickel on determination of the contents of PGM.

Jan 1, 2004

By Terence G. McCusker, Bruno Dietl

The only previous attempt to use a tunnel boring machine in the rock formations encountered in New York City was unsuccessful. However, technology has been developed since then which made a new attempt a practical proposition. Nine thousand feet each of 8'6" and 11'0" diameter tunnels were driven in Manhattan schist using Jarva TBM's together with 1100 ft. of the smaller diameter driven conventionally in Inwood marble and earth. (1) The selection of tunneling method was largely based on the need to avoid community reaction and hazardous tunneling conditions where the larger diameter tunnel passed beneath residential structures in poor condition in seamy and blocky rock. Experimentation with cutters and cutter mountings indicate that good cutter life and ease of change are available. It was found practical to use unusually large muck cars for an efficient muck disposal system. Conventional tunneling was successfully executed beneath a subway station whose invert was less than seven feet above the crown of the tunnel. Attempts at chemical consolidation and dewatering were unsuccessful in the earth section which was completed under compressed air.

Jan 1, 1974

By S. C. Brown, R. C. G. Oliveira

Surface wettability, or contact angle, dictates a number of multiphase ensemble interactions that influence particulate dispersability and adhesion behavior (e.g., filler compatibility] in addition to a number of other phenomena including biocompatibility and bulk powder segregation. The wettability of particulate surfaces significantly impacts nearly all process industries; however, the available techniques to access this quantity are either relative, or tedious-and are application or industry specific. In this study, key features of existing techniques have been combined to design an improved method to delineate particle wettability that is simple, versatile and capable of providing reproducible measurements in an industrial environment.

Jan 1, 2003

By Sushil Bhandari

A computer model is developed for the problem of dispersal of dust (suspended particulate matter) resulting from blasting operations in surface mines. Undulated surface (lower boundary) simulation was carried through sixth order polynomial by least square approximation. Segmentwise terrain simulation was linearly added to build ground feature extending either side of the blast location. Assuming the initial dust concentration in the vertical column to. be uniform and treating the finite vertical line sources as a series of point sources to height, H varying from zero to top of the dust mushroom, integration was done of the concentration effects from H = 0 toL tan[0] (L = horizontal distance of the blast location and [0] is the angle of the top of dust cloud from the point of observation). Using frame of reference moving with the mean wind, the ground level 'concentration (GLC) has been computed over the undulated terrain. Standard deviation (s) of concentration has been parameterized based on mixed layer similarity theory in convective boundary layer.

Jan 1, 2002

By Richard J. Adams

Coal jigs have played a predominant role in U. S. coal preparation for fifty years. Recently, an improved fine coal jig has been used to prepare the middle size range coal. These efficient machines are changing the historical thinking about jigs and is consistent with trends in coal preparation throughout the world. The performance achieved and operating cost savings are causing a change in fine coal cleaning strategy. With the exception of a handful of operators, fine coal jigs are generally not well understood by the industry. The objective of this paper is to provide some insight into the past use of fine coal jigs and their potential in the future. Improved Fine Coal Jig Since the mid 701s, an improved fine coal jig has been employed to an important niche in preparation, the 19 mm x 100 M range of cleaning. Several factors due to mining and liberation considerations have caused an expansion of this middle range of coal resulting in a host of challenges for coal preparation engineers. Fine coal jigs have been commissioned in several installations in North America to handle these important applications as shown in Table No. 1.

Jan 1, 1988

By Steven J. Schatzel

A study was made of frictional ignitions in the underground coal mining industry from 1980 to 1992. The population of frictional ignitions was correlated to a variety of potential contributing factors including the mined coalbed, geographic location, mine production, methane gas emissions, and the type of mining equipment in use. The number of frictional ignitions reported in 1991 and 1992 surpassed the annual totals in all previous years included in the study. Most frictional ignitions occur during cutting operations at a coal face by a continuous miner. The average coal production of mines experiencing frictional ignitions is greater than the average of all underground coal mines throughout the survey period. Methane drainage may have produced a drop in the ratio of gas emissions to coal production (E/P) in mines experiencing frictional ignitions.

Jan 1, 1995

By G. S. Dobby, N. J. Contini, S. W. Wilson

Scale-up and simulation of flotation columns requires construction of mathematical models which employ, as a minimum, rate constants for quantifying particle recovery in the collection zone as well as split factors for quantifying froth zone performance. To date, measurement of these rate parameters has proven to be difficult, due to the interdependent nature of the collection and froth zones. This paper describes a technique for making these measurements. The method requires recovery data from two modes of operation: countercurrent and cocurrent. In cocurrent flow slurry is fed at the bottom of the column and tailings are withdrawn a short distance below the froth interface. Countercurrent mode is conventional operation. The critical difference is that particles which are dropped out of the froth in cocurrent mode are immediately lost to tailings, while in countercurrent mode the particles are subjected to recollection. Fitting of the measured recoveries to the equations that describe flotation in the two modes yields rate constant or recovery values for both the collection and the froth zones.

Jan 1, 1988

By Douglas W. Fuerstenau, Douglas M. Deason

The depletion of high grade siliceous phosphate ores is bringing about a search for economically processable replacements. The processing of unexploited dolomitic sedimentary phosphate reserves has numerous problems including the similar surface properties of the carbonate and phosphate minerals and the presence of significant concentrations of dissolved species in the flotation pulp. In this paper, inorganic adsorption and surface transformation phenomena exhibited by the dolomite/apatite systems are examined in detail. Electrokinetic, adsorption, and flotation results indicate that when placed in a common solution, these two minerals interact significantly, with a corresponding strong influence on flotation using a physisorbed collector. Such behavior can have strong implications for flotation plant practice.

Jan 1, 1993

By G. Belardi, G. Marruzzo, P. Plescia

This paper presents the results of grinding tests performed on magnetite from Kiruna (Sweden) and on chromite from Skoumtza (Macedonia. Greece). Stresses were measured by XRD, which determined the variations in the characteristic structural spacings of the minerals both before and after, grinding in a HSM/250 Herzog laboratory ring mill. Anal Isis of the magnetite and c hromite crystallinstallin was performed hi measuring the broadening of the strongest diffraction peak (311). .Also, structural analysis on chromite was carried out using the Mikheev model. Ultrafine-grinding tests on the magnetite and chomite demonstrated that this type of treatment can induce profound variations m the surface-stress state. These included plastic variations of the cell followed by "chemical" stress with oxidation front the stricture to form hydroxide or carbonate, films. This can have a great influence on the mineral reactivity to flotation reagents

Jan 1, 1996

By V. K. Paruchuri, J. D. Miller, J. Nalaskowski

An understanding of forces responsible for the stability of dispersions of colloidal particles when interacting with each other in aqueous solutions is of great interest academically and industrially. When water-soluble polymers are adsorbed onto colloidal particles, various effects on the stability of their suspensions can be expected ranging from steric stabilization to bridging flocculation. The possibility of detailed characterization of such systems using direct measurements of interaction forces between particles can help in further improvement of existing technologies of solid-liquid separation. An atomic force microscope (AFM) colloidal probe was used to measure the interaction forces between a silica sphere and a silica substrate in the presence of water-soluble polymers. Poly(ethlene oxide) (PEO) with three different molecular weights (7,000, 43,000, and 63,000), each with a very narrow molecular weight distribution, were used in this study. The interaction forces measured with the AFM over an extended time scale are discussed in terms of the adsorption kinetics measured through in-situ FTIR/IRS measurements.

Jan 1, 2003

By Malcolm J. McPherson, Satya Harpalani

A thorough knowledge of coal permeability and its variation with factors like stress conditions, and time, is useful in simulation studies of mine ventilation and coalbed methane recovery, as well as characterizing coalbed methane reservoirs. An experimental investigation was carried out to study the gas flow characteristics of coal to enhance the under- standing of the mechanism of methane flow through it. The work consisted of measurement of permeability of coal samples under triaxial stress and an examination of the physical structure of coal using electron microscopy. Effort was made to fit the experimental data to several phenomenological models that have been used to describe fluid flow through porous media. It was realized that gas flow through coal cannot be described by models that assume this flow to be through a bundle of capillary tubes. However, results suggest that this gas flow could be predominantly through fractures and cracks in coal, and this could be represented by flow between parallel plates.

Jan 1, 1986

By Colin C. Harris, Jie Zheng

While applications of stirred media mills for fine particle production have continued to increase, there is a lack of understanding of operating behavior and power requirement. Investigations in laboratory stirred media mills have been carried out with grinding media, limestone and yttria stabilized zirconia. The torque required to rotate impellers immersed in dense particulate media with supernatant versus impeller rotational speed displays four regions marked by sharp transitions: transition from static to dynamic friction; channel- ling; dispersing; and centrifuging. Equations, including dimension- less group correlations of power and modified Reynolds number, for relating power, speed, impeller and tank dimensions and design, media size and density, solid concentration, and other relevant variables have been established. Scale-up guidelines with respect to power consumption are also proposed. The best operating conditions for grinding limestone in the laboratory stirred media mill have been identified. Complexation by the polymer during ultrafine grinding of zirconia has been found to cause extraction of yttrium into solution with possibly significant changes in the surface chemical composition of the product.

Jan 1, 1995

By Richard V. Beck, Donald R. East, Jeremy P. Haile

In view of the increasing use of heap leach operations in the mining industry and the critically important performance of the leach pad liner in both the economic and environmental aspects of the design, it has become essential that the designer fully understand the factors affecting the performance of the liner. Minimizing the loss of pregnant solution through the leach pad liner is obviously of paramount importance to the economic efficiency and environmental compliance of the heap leach operation. Losses through the liner are a function of the hydraulic conductivity of the liner material and the hydraulic gradient across the liner. This applies to both natural and synthetic materials. The hydraulic gradient across the liner is a function of the build-up of solution above the liner, which in turn is determined by the permeability of the heap material, the slope of the liner, the drainage path length and the leachate infiltration rate. A relationship incorporating each of these parameters and their effect on the hydraulic head acting on the liner has been developed in terms of the Dupuit criterion, assuming one- dimensional flow with vertical accretion.

Jan 1, 1987