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By Mitchell J. Willis

Recovery of fine particles has been considered to be a major limitation of the classical flotation process. However, the beneficiation of kaolin, a naturally occurring fine ore, via flotation has been practiced over the last 40 years. Kaolin is valued as a white pigment, and therefore, the goal in kaolin flotation circuits is to remove the colored impurities to result in an acceptable brightness product. Kaolin flotation originated with a novel carrier flotation process, and later on carrier less flotation techniques were developed. The collector chemistry utilized to beneficiate kaolin is based on fatty acids, and recently hydroxamates have been successfully used. The purpose of this paper is to cover the flotation practice in the kaolin industry in terms of the history and the reagent schemes.

Jan 1, 1999

By Meliton M. Garcia, Satya Harpalani

This paper discusses the results of an investigation carried out in an underground mine to characterize the volatile by-products adsorbed on airborne particulates following the detonation of four common explosives including ANFO. The primary objective of this study was to determine if any organic amine compounds, particularly nitrosamines, and any polycyclic aromatic hydrocarbons were produced and trapped in the dust that a miner might inhale during the workday. The production of these substances is of great concern because of their suspected carcinogenic nature. The results of the study indicated that a large variety of the by-products are adsorbed on the particulates generated, and thus remain airborne following the detonation of explosives. The major by-products retained by the dust were bis(2-ethylhexyl) phthalate, and aliphatic hydrocarbons with carbon chains ranging from C12 to C28. One explosive, a water gel, produced the polycyclic aromatic compound, trimethylnaphthalene. No nitrosamine compounds were detected.

Jan 1, 1989

By Stephen R. La Brooy, Tong Deng, Pritam Singh, David M. Muir, A. J. Monhemius, G. W. Warren, E. Peters

The controlled addition of ammonia to cyanide solutions inhibits the leaching of copper minerals but extracts up to 80% Au using as little as 10% of the cyanide compared with conventional cyanidation of copper-gold ores. The solubility of copper minerals and copper speciation in solution is dependent on NH3, CN-, pH and Eh. Rotating disc and electrochemical studies show that gold is leached by a mixed Cu-CN--NH3 complex with either Cu(II) or O2 as oxidant. This complex is slowly oxidised to CuCN and Cu(OH)2 by air.

Jan 1, 1993

By Johann Engelbrecht, Stéfan de Bruyn, Petrus van den Heever

A system for the on-stream X-ray diffractometric determination of mineral phases in slurries was developed in response to the mining industry's need for process control during the beneficiation of industrial minerals. The instrumentation for and results from testwork conducted at a phosphate rock beneficiation plant in Florida are discussed. Results show that the concentrations of the minerals apatite (var. francolite) and quartz can be accurately determined every few minutes, so that adjustments to the flotation circuit can be timeously executed from the control room. The on-stream measurements can ultimately be integrated into an automated plant control strategy. Estimates of savings on reagent and staffing costs, as well as the benefits from consistent grades and greater recoveries, have shown that the investment in such a system could often be recovered in less than a year.

Jan 1, 1999

By P. M. Solozhenkin

The proposed technology of antimony calcine processing includes ferrochloride leaching of calcine, reducing solutions, hydrolysis of hydrochloride solutions with antimony oxochloride isolation, synthesis of antimony trioxide by SbOCl neutralization and its drying, regeneration of hydrolysis solutions. The optimum parameters of separate stage of process has been determined and the chemical character of process has been given. During the leaching of calcine we succeeded to transfer 92.16- 95.66% antimony to solution. On the worked out sheme we attained recovery of antimony to antimony trioxide near 90 .5% Antimony triozide contains 99.5% Sb2O3. The composition of sinter burdens for pigments preparation "Naples Yellow" different colours from brightly-yellow, yellow and lightly yellow has been proposed. Three-sulfuretted antimony-antimonic cinnabar have been prepared by precipitation of antimony solutions by potassium sulfur-bearing solution. The prepared compounds correspond to inorganic pigments for artistic paint. The amorphous antimony-ferrous black we prepared by aluminium cementation of hydrochloric antimony solutions. The ferrous black were used as artistic paints and for coating of metals by antimony.

Jan 1, 1995

By D. Krzyszton, P. Czaja

Mining explosions in rocks originate stress waves of great intensity, which crush the surrounding rocks and are then propagated as a seismic wave. Seismic waves are the cause of dynamic loading of pillars and their subsequent destruction. In calculating safe dimensions for inter-room pillars, not only the stresses conditioned by overburden pressures should be taken into consideration, but also the dynamic stresses caused by explosion. This is of particular importance for pillars with great specific acoustic impedance which have been destroyed mainly by the reflected seismic wave. It is possible to take dynamic loading into consideration in the calculation of pillars when the parameters of the propagation wave, the dynamic elastic constants of rocks, the strength properties of rocks, the strength properties of rocks subjected to dynamic loads and the parameters of the blasting charge are known. An example of the calculation for the safe width of an inter-room pillar subjected to the seismic effect of an explosion is given and the possibilities of reducing the dynamic loading of pillars are discussed.

Jan 1, 1982

By R. M. Damodaran

The flotation performance of Florida phosphate rock was evaluated in terms of the mixing behavior of reagents and particulates during anionic conditioning of phosphate slurries. The various conditioning variables that influence mixing, namely, solids loading, agitation speed and conditioning time, were investigated to determine their effect on reagent coating of the particles. The phosphate recovery was used to monitor the conditioning efficiency. The mixing characteristics of the phosphate feed were evaluated in terms of the ratio of the mixing power (P) to the minimum power (Pm) required to keep the slurry in suspension. It was found that mixing conditions govern the conditioning time required to obtain a high recovery. Reagentization was slower at lower P/Pm ratios. At higher P/Pm ratios, the flotation recovery was optimized, and the agitation speed was found to have no significant effect. Optimum mixing conditions were obtained for a74 wt% slurry at an agitation speed of 450 rpm (47 radians/sec). Under these optimum mixing conditions, the collector dosage required for an improved recovery was lower and the conditioning time was shorter.

Jan 1, 1997

By Milton E. Wadsworth, Ximeng Zhu

Impurity metals can markedly influence the anodic dissolution of gold in the presence of cyanide. Several important findings related to the influence of lead are reviewed and some new observations presented. Based on the effect of pH, the scan direction, and voltage, it may be shown there are three separate voltage regimes where lead influences the anodic dissolution of gold. These are related to Pb°/ HPbO2, Au-Pb /HPbO2, and HPbO2/PbC2; oxidation-reduction reactions which provide low resistance paths for electron exchange. The gold dissolution rate was determined by direct solution analysis and is compared to the rate implied by electrochemical measurements.

Jan 1, 2005

By C. C. Nolan

As the size of the mills get larger and the liners get heavier, abetter means had to be found to handle liner replacement. McLellan Industries is famous for their innovative ideas andwas called upon by an engineering company to develop a mill liner crane. The first crane was developed for Similkameen about 1969 to serve a 32' Ø X 14' Long SAG Mill. The next was Island Copper in Port Hardy, B.C., the same size as Similkameen in 1970. At that time, we took existing hydraulic cranes and modified them to meet the mill configuration. In 1973, we developed a completely new approach for the Southern Peru copper mine at Tacna, Peru for a Ball Mill, size 16'-6" Ø X 19' Long. Each installation required a design study to meet the change in mill size, trunnion size, elevation of floor to feed trunnion, area at the feed or discharge end of the mill. We have supplied self-propelled units as well as lift in. When there is no room at the feed end and if the mill has a trunnion overflow discharge, we have the mill supplier provide a structural frame to span the sump and move the mill liner handier into position with the use of the overhead crane or a mobile crane.

Jan 1, 1999

By Richard Hogg, Heechan Cho

Investigations of long-time grinding of fine quartz (to about 80% passing 0.35 pm) in a 0.6 liter stirred-media mill are described. Breakage rates and primary breakage distributions have been determined based on extensive characterization of the ground products by laser scattering/diffraction and gas adsorption. The results indicate that, while there is qualitative similarity between the breakage parameters for ultrafine and conventional (coarse) grinding, there are important, quantitative differences. In particular, it is found that primary breakage distributions become significantly narrower in the submicron sizes. The trend can be described using double-truncated log-normal distributions in which both a maximum (breaking) size and a grind limit are specified. The breakage distributions become progressively narrower as the size being broken becomes finer. Breakage rates follow a typical, consistent pattern in which the rate decreases with size according to a simple power law. Further decrease in the rates seems to occur after very long grinding times when the entire mill contents become finer than about 1µm. The effect is explained as a result of changes in the rate/size relationship in the submicron range.

Jan 1, 1995

By David M. Mchaina, Steve Hardcastle, Michel Grenier

An overview of the process employed to assess arsenic exposure levels at a gold mine is provided together with the recommended control measures. Arsenic and its compounds are regulated in Ontario as designated substances in all workplaces except mines and concentrators. There is a proposal to remove the exemption for mine and concentrators. If the exemption is removed, the mining industry will be required to adopt the proposed exposure Limit of 0.01 mg/m over 40 hours. There are many mines in Ontario which will be affected by this new regulation. To determine the extent of which workers are exposed to Levels exceeding 0.01 mg/m , an assessment program was initiated at the mine. The main objective of the program was to determine the effect of the proposed regulation on underground and surface operations in term of compliance if it becomes Law. The data obtained from the assessment program shared that only 1ML of the workplaces monitored for arsenic indicated levels above the proposed limit of 0.01 ,/yard all workplace levels were below the present Limit of 0.2 mg/m .

Jan 1, 1992

By Travis S. Wellman, Jon C. Volkwein

The Bureau of Mines conducted a study to assess the impact of a directional water spray system on a unique single inlet dust scrubber on a low profile mining machine. Tests were conducted in a full scale model mine using a Joy 12 CM 10-AA continuous mining machine. Tracer gas was introduced at the face and concentrations of the tracer gas were monitored at the face and in the return. Various parameters included: mining position, depth of cut, brattice setback and combinations of scrubber, directional sprays or symmetrical sprays. Results indicated that either directional or symmetrical water spray configuration improved the ventilation effectiveness of the scrubber by a factor of 2 to 3. Average face ventilation effectiveness (FVE) values for all testing of the scrubber and directional sprays were 0.95, versus 0.37 for a standard 6 m (20-ft) blowing curtain without sprays. No FVE values were less than the standard 6 m (20-ft) blowing results.

Jan 1, 1989

By A. R. Zambrano

Equations for power draft, capacity and work input for predicting the performance of industrial grinding mills are derived based on torque measurements using a laboratory instrumented mill. These derivations are based on mechanical principles and on the first-order kinetics of the grinding process. Rittinger's, Kick's and Bond's laws express work input as work index (Wi) times a particle size function. It is proposed that these laws are only particular cases of more general expressions having the particle size function raised to an exponent, i.e., the work exponent (We). Case studies illustrate the excellent prediction of the Wi - We models compared to the three mentioned laws, and, from the data, the corresponding general mill-sizing equation is derived. Key words: Grinding mills, Comminution, Work index, Mill sizing

Jan 1, 2003

By R. W. Hutson

One of the fundamental precepts of experimentation is the isolation of a single variable to quantify its individual effect. Unfortunately, the variability of natural rock joints has frustrated such isolation. This variability and the high cost of securing a large member of natural joints has lead to increasing experimental dependence on stage shearing, artificial tension fractures and/or model materials. The new apparatus described herein allows for the first time replication of real joints with field scale asperities. It employs a diamond band-saw blade with computer controlled feed table to cut joints with high precision. The feed system is capable of placement to tolerances similar to those of a high quality computer plotter. The accompanying software allows the table to cut any desired joint shape (repeating or non-repeating) within certain, over-all size limitations. Resulting joint surface dimensions and roughness as well as shear resistance indicates that the joint surfaces are reproduced with a precision similar to that possible for the control of other experimental variables such as normal and shear forces.

Jan 1, 1986

By B. K. Mishra, S. P. Mehrotra, Anand Katti

Particle-size monitoring has become routine plant prac¬tice, and on-line measurement techniques have facilitated the proper control and monitoring of particle size. In this paper, the progress on an on-line size measurement technique using a y-ray source is discussed. The tray is emitted from a nucleonic density gauge (NDG) that serves as a slurry den¬sity-measurement device. This unit is calibrated and tested to predict the slurry density. Batch experiments were conducted to study the variation in slurry density of different types of ores, namely, quartz, bauxite and hematite. This data, in turn, is used to predict the size distribution of the solid particulate material making up the slurry. To calculate this size distribu¬tion from the slurry density, the theory of incremental sedi¬mentation is used. Experimental results show that the pre¬dicted size distribution compares well with the actual size distribution, as measured by the Andreasen pipette technique. Finally, a simplified scheme is proposed to monitor on-line size distribution using the nucleonic density gauge

Jan 1, 2000

By R. E. Johnson, W. Kat, B. R. Palmer, van Sandwijk A., G. Van Weert, S. Honingh

In-plant recycling of dust from iron making BF's creates undesirable circulating loads of volatile trace elements such as zinc and lead. Disposal of such dusts creates environmental problems, hence a separate treatment is indicated. Since the bulk of the zinc and lead compounds occurs in the fine dust fraction; hydrocycloning the slurry from the BF gas cleaning operation results in upgrading the material for treatment. A process has been proposed, whereby the zinc and lead are solubilized from the fine fraction with spent hydrochloric acid from steel pickling. The stoichiometry of this autoclave oxidation process is adjusted to simultaneously precipitate, by oxyhydrolysis, most of the iron for recycling to the BF's. Lead and zinc are successively recovered from the filtrate as low chloride precipitates. This paper describes additional testwork, leading to the design of a pilot plant which was planned to begin operation in 1992.

Jan 1, 1993

By J. C. Squire, E. W. Baker, G. A. Sullivan, G. W. Flathers

A mine collapse severs communication with trapped miners. Landlines are crushed and commercially available radios cannot penetrate hundreds of feet of dense, conductive earth without the use of regenerative repeaters that may also be crushed. This paper describes a proof-of-concept device that uses seismic P-waves, instead of radio waves, to allow communication of a code that represents prearranged messages, including the safe haven location identifier, number of people and air quality, from trapped miners to aboveground rescue units. The transmitter designed is about 0.03 m3 (1 ft3) in size and can broadcast for four hours from its 27-kg (60-lb) battery pack. The receiver consists of a geophone and a 2.5-kg (5.5- lb) signal conditioning unit attached to a laptop computer, which displays the communication signal in real time. Testing in a bituminous coal mine with an MSHA representative revealed the device was able to transmit through 271 m (890 ft) of overburden, at 0° and 12° from vertical, using 500 W of power.

Jan 1, 2009

By Danqing Xu, A. W. Khair

This paper presents an analysis of mechanism of secondary fragmentation and respirable dust generation due to regrinding. In continuous miners, the recovered coal and uncleaned coal from the previous cutting cycle have to be transported through the circumference of the cutting drum, subjecting the coal to regrinding. Such regrinding comminutes the coal material utilizing kinetic energy, thus creating a great amount of respirable dust. The mechanism of a single particle subjected to regrinding is analyzed. A mathematical model is developed to describe regrinding in field conditions. The important factors influencing the comminution process are discussed in detail. Utilizing three types of coal seams, laboratory experiments are being carried out with an Automated Rotary Coal Cutting Simulator (ARCCS) to quantitatively evaluate the effects of some particular parameters, such as cutting velocity, depth of sump and properties of coal material, on breakage and on the amount of respirable dust generated. An orthogonal fractional factorial experimental arrangement is used to optimize experimental design. Preliminary experimental results are presented.

Jan 1, 1991

By A. A. Peshkov, N. A. Matsko, K. N. Trubetskoy

It is possible to divide the general objectives of a company into two components: maximum expected profits and viability over time. These components are designed to maximize the companies value over time. The evaluation of a project includes both a discounted cash flow (DCF) analysis and a risk analysis. The DCF analysis determines whether the project should be accepted or rejected, and the risk analysis helps to forecast possible deviations from the original estimates. However, the results of both methods do not allow for a quantitative comparison between the main objectives of the venture, and they do not resolve the issue of whether it is advisable to sacrifice immediate profits for future profits. This paper attempts to resolve this issue. The present research was carried out on mining projects with different waste-extraction schedules. Calculations were made using the US Bureau of Mines' usage-of-costs model. Russian experience in open-pit mining is reflected in this paper.

Jan 1, 1996

By Franc Runovc

The service hoisting plant in the mining transportation is an installation serving for the vertical transport of material and persons. An adequate mathematical model is presented for simple evaluation of the project parameters where different plant designs and the ways of transport are take into consideration. The technical and economical optimization procedure is added to the basic mathematical model of the project. This approach enables on one hand the optimization of the reconstruction of the multi-purpose hoisting plants in order to suppress possible bottle necks, while on the other hand it enables the determination of such values of the parameters of the choice and of the operation that the sum of total expenses per a transport unit' becomes the lowest. The optimization procedure is designed in such a way that all numerical data of the optimum hoisting plant are printed out together with the graphical representation of dependencies of the fundamental parameters in broader optimization region.

Jan 1, 1992