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By Ronald J. Allain

Water soluble polymers play an important role in many industries. The mining industry is dependent on these materials to help accomplish many solid-liquid (water) separations. Mechanical devices alone are not capable of achieving the degree of separation needed. Mechanical and chemical separations act in concert to accomplish the necessary separation. The history of the use of water soluble polymers has gone through several evolutionary phases and I believe we are facing another of these phases. At first, various natural products were common - starches, gums, and various polysaccharides. These were replaced by the synthetic polymers based on copolymerization of various vinylmonomers mainly in conjunction with acrylamide. The use of these polymers and their needs continues to grow. This paper will cover a brief overview followed by a look at the future of water soluble polymers. A focus will be on applications of water soluble polymers in the mining industry.

Jan 1, 1994

By Ivan C. Machado

In full autogenous grinding (FAG Mills) the ore itself determines almost exclusively the product size that will be produced, as opposed to conventional steel-media grinding where the product size can be "engineered" by changing media size, feed size, feed rate, classifier cutpoint size, etc. SAG Mills are in the middle of the way, since they offer some room to engineer their product size by properly defining some critical process variables, such as feed size, ball charge and size, mill charge and speed. SAG Mill product P80 values are typically in the range of 500 µm (35 US mesh) to 2000 µm (10 US mesh.) Whenever it is possible to determine an optimum value for the SAG Mill product P80 value (which will be the Ball Mill fresh feed F80 value), the Engineer should define the process variables that will yield a SAG product size as close as possible to the optimum calculated P80 value. In general, a coarser SAG product will draw less power from the SAG Mill and more power from the Ball Mill, and conversely, a finer SAG product will draw more power from the SAG Mill and less power from the Ball Mill. Metal consumption analyses also have to be taken into consideration, for they typically account for 30% to 45% of the total grinding cost. This presentation addresses the issue of defining an optimum SAG Mill product size (X=P80), during the design phase of the SAG and Ball milling circuits, from a general perspective, i.e., the SAG product size that will lead to an overall SAG Mill - Ball Mill optimum performance. Bond's Third Law approach is used, as well as the SPI (SAG Power Index), and also the generally accepted equations and Engineering Practice currently utilized to design SAG Mill

Jan 1, 1999

By R. Bhaskar

Although the health effects of airborne dust in underground coal mines are well recognized, a lack of understanding remains about the fundamental mechanisms of dust generation, transportation, deposition and dust-lung reaction. This study was intended to contribute to the understanding of dust transportation and deposition mechanisms in underground mine airways. Data from in-mine experiments carried out under controlled conditions in a straight section of a longwall panel with three different airflow velocities and two different types of coal dust (bituminous and semi-anthracite) were used to determine the turbulent deposition rate of dust particles. Measurements of ambient dust concentrations and deposition along the mine airway were obtained and the total dust deposition velocity (rate) was calculated. The deposition velocity of turbulent diffusion was estimated based on the experimental data and theoretical equations. The effects of airflow velocity, particle size, particle density and distance from the dust source on gravitational, turbulent and total dust deposition are discussed along with related conclusions.

Jan 1, 1995

The implementation of NAFTA in January 1994 was expected to have small but beneficial effects on the Mexican economy, mostly through increased investments. Mexico's mining industry was especially likely to benefit, as mineral investment funds would be diverted to the now safer Mexico and away from similarly endowed but more risky Latin American mineral economies. The results during the past two years have shown that it is government and macroeconomic factors that influence investment flows, rather than the fine tuning of trade flows through so called 'free-trade" agreements.

Jan 1, 1997

In 1996, O&K Orenstein and Koppel Inc. announced big plans to increase its presence in the US mining market. Even though the company, a part of Ger- man-based O&K Mining GmbH, has been in the United States for about 100 years, it has lived in relative anonymity. That despite being one of the largest makers of hydraulic mining shovels and excavators in the world. The plan must be working. In the 14 months through December 1996,O&K increased its sales to surface mines and quarries in the United States by 250'70, according Rolf Weber, company president. "In the next five years, we anticipate total revenue from our US operations will grow from the current $50 million to $200 million," he said. "Toward that end, we have concentrated our efforts on the supply of reliable, high-output machinery and responsive service after the sale."

Jan 1, 1997

By Song Xiaotian

In this paper the enviroment in which Tong Kuang Yu mine, China is developed is described. Geological and geomechanical environments which pose difficulties in the design and optimization of Block Caving are discussed. According to mine conditions, caving process simulation was carried out using Displacement Discontinuty Method and relationships between stress distribution .and undercut parameters were established in accordance with different undercut sequence. Based on simulation the influences of caving parameters on caving probability, drift instability and ore-draw control were analysed in order to optimize Block Caving Mining. On the basis of simulation and mathematical programming, the optimal sequence is proposed essential to satisfy the safety, production and other restrictions.

Jan 1, 1989

By Joseph F. Shirley

Introduction Inorganic depressants are chemicals added to the froth flotation process to maintain or produce hydrophylic surfaces on one or more minerals so they will remain in the pulp rather than attach to the air bubbles. Whether a depressant will be effective in depressing a given mineral depends on how it is used and the environment in which it is used. Some depressants must be added and conditioned into the pulp before the collector is added. Other depressants can be added in the presence of previously added collectors and effectively depress the desired minerals. Often the concentration of depressant relative to the collector concentration is critical to making an economic separation. It should be noted that some depressants will only work when specific collectors have been used. Some reagents such as sulfuric acid and hydrogen peroxide essentially act as depressants by altering the previously added collectors so that they are no longer effective. Some depressants such as sodium ferrocyanide are only effective in a very limited pH range and an essentially collector free environment. Major Depressants CaO Milk of Lime is by far the most used depressant both in tonnage and dollar value. Although it is most commonly listed as a pH modifier, it is also an important depressant for pyrite in copper and copper molybdenite flotation plants. Although a simple pH adjustment will often depress pyrite, there are times when grinding with fresh milk of lime is required to obtain optimum depression. Lime is also a molybdenite and gold depressant. NaSH Sodium hydrosulfide is by far the most commonly used reagent to depress copper and iron sulfide minerals in by-product molybdenite flotation plants. NaSH also depresses gold, silver sulfides and silver chloride. ZnSO4 Zinc sulfate is commonly used to depress sphalerite in lead-zinc and copper-lead- zinc flotation plants. It has also been used to effectively depress talc in by-product molybdenite circuits at a pH of 6.5.

Jan 1, 1986

By D. Elsworth, M. Bai

The influence of mining on the hydro-geo-mechanical environment can be greatly modified by alternating mining geometries. The limiting magnitudes of surface subsidence and groundwater flow over the mining area, as a result of mine geometric changes, can be reasonably predicted through the coupled finite-element model introduced in this paper. The model has been verified using real and conceptual case studies which reveal that changes in strata conductivities are strongly related to the strata deformation induced by mining. The greatest modification of hydraulic conductivities occurs within the caving or severely fractured zones. The study indicates that narrowing the panel face width will substantially reduce both the intensity and extent of mining damage to the overlying strata, limit surface subsidence and constrain the change in hydraulic conductivity to a reduced scale and smaller extent, particularly as mining depth increases.

Jan 1, 1995

By Allen V. Reicks

Modern conveyor pulleys are welded steel structures subjected to dynamic loads. In this paper, fatigue notch and fracture mechanics methods are applied to several weld joints on typical pulley constructions. These methods are used to analyze field applications and are correlated with laboratory testing. Generalized approaches are presented which provide high confidence in pulley design with corresponding high reliability.

Jan 1, 1996

By J. Partyka

Fumes produced during blasting operations in underground mines are defined in this paper by an equivalent contaminant source. The primary goal is to establish a method which would allow all those parameters not measured directly to be determined reliably from field data. The parameters to be identified are the diffusion coefficient , and the position and size of an equivalent source. The diffusion-value is computed from the peak concentrations taken by two monitors located in the drift. The first monitor is placed close to where blasting pollutants join the main stream, while a second monitors is moved downstream a some distance from the first point. The position and size of the dust source and the total amount of dust produced during blasting are determined from the data recorded by only one monitor.

Jan 1, 1991

By D. J. Kennedy, W. G. Klinowski

Over the past few years the Cape Breton Coal Research Laboratory's staff designed, built, tested and proved the necessary hardware, software and methodology of tracer gas based surveying techniques applied in the field of mine ventilation. These methods are now used routinely in a variety of applications where traditional anemometric methods do not provide the required accuracies or cannot be effectively employed. Irregular or highly turbulent flows, leakages, geometrically complicated or highly obstructed airways are just a few examples where traditional anemometry can produce unacceptable errors in calculated ventilation parameters. Tracer gas based ventilation techniques have been used in many problematic situations where the standard ventilation methods are inadequate. One such problem, faced by many mine operators, is the emergency imposed by the ever present threat of a mine fire. An understanding of the propagation of smoke contaminants and the demonstrated integrity of appointed escape routes can save lives and property during a fire. That knowledge can be gained quickly and inexpensively by the application of tracer gas smoke simulation methods. The concept of controlled air recirculation has recently gained considerable attention in the mining industry. While mathematical models can be used to predict performance, the ultimate proof of a ventilation system's performance can best be provided by a tracer gas based simulation of contaminant levels. Fan performance tests and assessment of auxiliary ventilation systems are highly dependent on accurate definition of airflows; precise data can be easily obtained by tracer gas based volumetric surveys. This paper contains a brief description of the equipment and the methodology of tracer gas based ventilation techniques and presents typical examples of their use

Jan 1, 1991

By Helen Joyce, Larry Twidwell, Jay McCloskey, Eric Dahlgren, Andy Hadden

The reduction of dissolved selenium oxyanions from mine wastewater utilizing an elemental iron cementation technology on been studied on a laboratory scale at Montana Tech of The University of Montana and on a pilot scale at MSE-Technology Applications as a water treatment process potentially capable of removing dissolved selenium to GO WL. Laboratory and pilot scale studies using elemental iron have demonstrated effective removal of dissolved selenium. Enhanced selenium reduction rates have been demonstrated when galvanically coupled iron/copper and iron/ nickel are utilized. The laboratory and pilot scale results are presented and discussed.

Jan 1, 2005

By W. V. Harper

The travel path of a freed radioactive particle in an aquifer must be estimated from a limited number of available samples. This paper discusses geostatistical methods that minimize the 'uncertainty' associated with the predicted hydrologic surfaces and the predicted travel path. However, any estimation method will produce a single smooth predicted path. This 'sensitivity' will he evaluated using a geostatistical simulation method. The techniques will be illustrated using published data from the Wolfcamp and Pennsylvanian aquifers in the northern Texas Panhandle.

Jan 1, 1990

By H. J. M. Rose

Arising out of the world energy crisis and the increasing demand for nuclear fuels, the Elliot Lake operation of Denison Mines Limited is currently expanding its facilities to meet its increased contractual obligations of some 90,500,000 kg of uranium oxide between now and the year 2011. The mining of uranium is subjected to increasingly stringent environmental controls by governmental and associated agencies so as to safeguard the health of the employees. A heavy burden of responsibility is thus placed on the Ventilation Department to ensure, through efficient planning and good control, that satisfactory ventilation conditions prevail throughout the entire operation. Management realized at the outset of the present phase of this expansion, that the establishment of a properly organized and administered Ventilation Department would be essential to ensure that long term production goals are achieved within the numerous constraints imposed by existing legislation. The paper describes the formation of the department by recruiting technically competent, but largely inexperienced, ventilation personnel, their practical training programme, the departmental structure and the operational and control responsibilities of the ventilation staff.

Jan 1, 1980

By S. K. Kawatra, S. J. Ripke

During iron ore pellet production, bentonite clay is used as a binder. Typical pellet plants spend from $3 million to $5 million annually for the clay. If bentonite dosages could be reduced by using it more efficiently, a significant cost savings would result. If the binding mechanisms can be completely understood, procedures can be developed to use bentonite more efficiently. Classical bentonite bonding theory is based on the behavior of bentonite at low percent solids and high mixing shear rates. Under these conditions, bentonite was understood to expand, disperse into platelets, and dry into a bonding "film" or "gel." However, these are not the conditions that exist during pelletization, which is carried out at high percent solids and relatively low shear rates. In this paper SEM imaging was used to identify and explain the bonding mechanisms of bentonite on the surface of magnetite concentrate. It was determined that bentonite would form a fibrous network under the proper conditions and that the formation of these fibers corresponded with an increase in the bonding of particles by the bentonite.

Jan 1, 2000

By David Wright, Colin Burns

Successful leaching of gold depends on appropriate chemical conditions; contact between leach solution and the gold particles; separation of the leach solution from the solids and extraction of the valuable ion from the solution. Irrespective of the leaching method employed the chemical conditions required are similar as is the dependence of solu­tion/gold contact on liberation. The various leaching methods available vary in the means by which gold/solution contact and solid/liquid separation are achieved. The essential difference between heap or vat leaching techniques and those involving agitation of a slurry is dependence on percolation for effective gold/solution contact. The most significant factor preventing uniform percolation is the presence of fines or clays. The quantity and character of the fines fraction is ore type dependent and may result from crushing, degradation during stacking or leaching, or the natural size distribution of the ore. The problems associated with fines can be aggravated during stacking and preparation of the heap. Segregation during stacking can result in concentration of fine particles at the centre of heaps. Further concentration of fines may also occur during irrigation by the movement of the fine particles with the solution. The end result is that the areas in which fines are concentrated become areas of low permeability. The contact between leach solution and the ore in such areas is, at best, slowed down dramatically and, in some cases, prevented altogether. The consequences of this phenomena are slow leaching and a reduction in recovery. The conventional solution to this problem is well known. Agglomeration of ore prior to heap leaching is practised widely. The effect of agglomeration is to immobilise the fines by causing them to adhere either to each other or to larger ore particles. The net effect is that the ore behaves as if no fines were present. The use of agglomeration is limited only by its cost, the most significant components of which are the cost of binding agent, commonly cement, and the capital cost of the agglomerating equipment.

Jan 1, 1995

By W lethlean, Laurie Smith

When coarse gold is present in an ore, there are advantages in physically recovering this gold in the grinding section of the ore processing plant. This reduces the risk of the coarse gold being locked up in the grinding section equipment, reduces the quantity of activated carbon to be eluted and reduces the risk of gold passing out of the cyanide leaching circuit only partially dissolved. The free gold may be recovered by various mechanical means utilising the significant difference between the specific gravity of the gold and waste minerals. Frequently, sulphide minerals and ball mill attrition steel in the form of fines and chips are present in the ground ore and behave in a similar manner to the gold in the concentrating process. These materials must be removed to produce a concentrate suitable for direct smelting and several stages of cleaning, sometimes utilising different physical principles, may be required. The removal of these materials invariably results in a loss of gold from the final concentrate. The rejected materials containing significant quantities of gold are returned to the grinding section, consequently the opportunity for a high and early recovery has been lost. The quantity of gold returned to the grinding section will vary according to the number and type of cleaning stages and the physical characteristics of the materials and the gold but surveys of the gravity concentration processes suggest that it may be as high as 50%. To maximise the recovery of gold from the primary gravity concentrate, some operations batch cyanide leach this concentrate with or without additional reagents. The method of agitation and solution recovery vary. The most common method of agitation is by a high-speed propeller mixer and the least expensive but time-consuming method of solution recovery is by decantation after settling and by repeated decant washing. The pregnant gold solution is either introduced into the main ore leaching circuit or the gold is recovered by direct electrowinning. After commissioning in 1994, Union Reefs Gold Mine (URGM) experienced below expected recovery of gold from the gravity concentrate generated from the Knelson Concentrators. It was shown that the recovery into the Knelson Concentrate was high but that the subsequent mechanical concentrating techniques of tabling and magnetic separation resulted in significant gold being returned to the grinding circuit.

Jan 1, 2000

By Scott E. Broughton, Robert T. Tape

Heap leaching requires containment and storage of cyanide solutions, the volume of which may increase dramatically following an extreme storm event or extended wet periods. This paper describes a computer operated solution storage model developed to assist in the management of these requirements. It results from the accumulative efforts of various Klohn Leonoff engineers working on a number of heap leach projects throughout the western United States for the past several years.

Jan 1, 1988

By R. Hogg, M. Polat, S. Chander

A fresh dust generator was designed and built in order to study the agglomeration behavior and other characteristics of freshly generated airborne dust. The size distribution of the freshly generated quartz airborne dust produced by the generator was measured both directly in air and after dispersion in water. It was observed that same dust particles had an apparently coarser size distribution in air than in water, suggesting possible agglomeration of the dust particles. It was also observed that the size distribution obtained by a cascade impactor was very similar to the liquid dispersed size distribution, implying deagglomeration by the impactor. The agglomeration was confirmed by microscopic observations of particles in air and those collected on a microscope slide. The extent of agglomeration played a decisive role on the fraction of the dust actually becoming airborne. It was also found that contamination of the airborne dust by the rolls of the crusher was almost twice as much as that of the product.

Jan 1, 1991

By Salama

In the conventional approach, the separator feed incremental masses are assumed to be concentrated at the midpoints of the density or size intervals and subjected to a model partition function. The resulting separation predictions would change if the locations of the incremental masses were changed. As a result. the predicted results depend on the choice of locations where the feed incremental masses are concentrated in the density or size intervals. A technique that utilizes the cumulative-mass-distribution of the circuit feed and the derivative of the partition (separation) function relative to density or size variables is proposed. The proposed technique eliminates the dependency of the predictions on choice of where the feed incremental masses are concentrated within the density or size intervals. Since the proposed technique is based on the cumulative masses at the upper limits of the density or size intervals, the technique produces a single prediction whereas the existing techniques produce predictions that depend on where the incremental masses are concentrated. In fact, it has been demonstrated that the existing conventional technique, in which the incremental masses are concentrated at the midpoints of the density or size intervals, is a first-order approximation of the technique proposed.

Jan 1, 2002