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By Kenneth N. Han, Jianshe Liu

Various techniques used in the removal of metal ions from effluent streams have been reviewed. These techniques include recovery of metals by biological treatment, chelating agents, adsorption, ion- exchange and chemical precipitation. The main thrust of this paper however, is concerned with the removal of cadmium and zinc ions from the solution by adsorption utilizing liquid fluidized beds. The bed particles used were silica of 150x200 mesh. The range of the concentration of these ions studied was 10-3 to 10-5 M. Important variables examined included flow rate, concentration of metal ions and amount of bed particles. A mathematical model describing the concentration profile of metal ions in the axial direction in liquid fluidized beds has been developed. The equation of continuity was solved numerically and the results were used to predict the recovery of metal ions in fluidized beds.

Jan 1, 1992

By C. R. Zegarra

Extraction of manganese, gold, and silver from a low-grade manganiferous-silver ore was investigated by thiourea leaching followed by standard cyanidation. The levels of reagent concentrations in this investigation were 0.0 -1.0 M thiourea and 0.0 -1.0 M sulfuric acid. Temperature and agitation speed were maintained at Z5 °c and 300 rpm, respectively. The dissolution of gold, and silver was shown to be dependent mainly on sulfuric acid and thiourea concentrations. In general, 50.0 % Ag, 98.0 % Au, and 75 % Mn were recovered from a Mn-Ag ore by thiourea leaching. Overall silver extraction of 98.0 % was obtained by cyanidation after thiourea leaching. Thiourea leaching of sodium bisulfite leach residues was also studied, and the total extraction of gold and silver were 97 % and 40 %, respectively. Finally, a two-stage thiourea leach was also investigated.

Jan 1, 1988

By I. K. Gilmore

PCS Phosphate operates an open-pit phosphate mine in the central coastal plane of North Carolina. The company has mining and refining facilities located on the south shore of the Pamlico River. Phosphate ore is recovered at the Aurora facility by open-cast mining techniques. Walking draglines and bucketwheel excavators remove the overburden and mine the phosphate ore. The mined ore is slurried about 8 km (5 miles) to the processing plant. At the plant, the phosphate ore slurry is passed through screens to remove material coarser than 2 mm (10 mesh) and then pumped through hydrocyclones to remove material finer than 75 mm (200 mesh). The resulting phosphate and sand mixture is treated with various reagents and subjected to an anionic flotation process. A cationic flotation process removes the sand from the final phosphate concentrate.

Jan 1, 1995

By P. C. O. Chukabarah

Atkinson's resistance square law is the cornerstone equation for traditional expression of energy losses in mine ventilation engineering. But the nomenclature for the various forms of energy losses are often confused for one another, misapplied or misinterpreted. These forms of energy were re-examined from thermodynamic and fluid-dynamic perspectives. Resultant expressions showed that both incompressible and compressible flow regimes in underground mines can easily be accommodated. Given the well-known three major energy forms, which are equivalent to one another but numerically unequal, corresponding equations to Atkinson's (pressure loss) for headloss and workloss were derived. The thermodynamic weight relational resistance ([w] s2/m5) associated with energy per unit weight (headloss) was dimensionalized for the first time. Also, normalized Atkinson-like equations for headlosses and worklosses were derived to ease direct computations in mine ventilation practice.

Jan 1, 1995

Continuous improvement has become the watchword of the 1990s for most iron-ore-processing operations. In many instances, this improvement has been achieved through stepwise application of advanced control techniques to optimize operations. The benefits of this stepwise application have been great. However, they have fallen short of the full potential offered by the prospect of overall plant optimization. The successful integration of computers, instrumentation and control software throughout a plant promises to deliver an additional 3% to 5% of productivity in even the best-run plants (Herbst and Bascur, 1984). LKAB is Europe's largest iron-ore producer and a leading implementer of advanced control technology. In the late 1980s, LKAB introduced advanced control in its concentrator at Kiruna, Sweden to improve plant performance through higher productivity, greater efficiency and lower costs at each processing step.

Jan 1, 1995

By L. G. Sobral, J. E. Hoffman, T. J. Keefe, A. J. Monhemius, O&apos

The kinetics of electrodeposition of gold from dilute solutions of alkaline KAu(CN)2 at different gold and free cyanide concentrations on a gold rotating disk electrode were investigated by use of a steady-state linear potential scan technique. The design and performance of a laboratory electrowinning cell with a reticulated nickel cathode, operating in the flow-through mode, for the removal of low levels of gold ions from aqueous cyanide media is described. During the batch recirculation of oxygen-free gold cyanide solutions, the gold concentration was reduced from 10 ppm to <0.5 ppm with current efficiencies of up to 80%. The influence of solution flow rate through the cathode and of the pore size of the reticulated nickel foam is discussed. The removal of gold ions from solutions of low ionic strength was also investigated.

Jan 1, 1993

By J. H. Fewings

The rapidly escalating capital costs for new projects, or extension of existing projects, has placed greater emphasis on maximum use of existing resources. Thus, when increased grinding capacity was required to achieve metal production from lead-zinc ores a number of alternate approaches were studied. The most cost effective way of achieving the required 5% increase in grinding circuit capacity was to install upgraded instrumentation and computer control of grinding - Fewings, Wickham and Wiseman (1). Once the computer installation cost had been borne by the financial returns from that project, other projects involving computer control were economically viable on an Incremental cost basis. These Included centralised control of tailings thickening and return circuit water distribution, centralised control of the crushing plant and use of the computer as a data processor for an on-stream analysis system for flotation slurries.

Jan 1, 1979

By J de Cuyper, S. Ramachandran, L. A. Vazquez, N. L. Grauerholz, W. Freyberger

A novel process is described for the selective flotation of scheelite from low-grade (- 0.5% W03) tungsten ores having appreciable quantities of calcareous and siliceous gangue minerals. Specifically developed for the Tempiute, Nevada facility of Union Carbide, the process yields tungsten concentrates exceeding 15 percent W03 with at least 85 percent recovery. This condition was not achieved through conventional processes. This process consists of conditioning the ore pulp with judicious amounts of lime, followed by soda ash and sodium silicate as modifiers. The scheelite is then floated using a mixture of oleic and naphthenic acids as collector. Contrary to the common observation as to the deleterious effects of calcium in fatty acid flotation systems, lime addition is found to be beneficial in achieving satisfactory results. The process has also shown excellent results on a Brazilian scheelite ore.

Jan 1, 1976

By John C. Schneider

In the mid 60's Prochem & Hydrochem Development, it's research division, developed the high efficiency Maxflo impeller. Since the Maxflo impeller had a design that had proven to be very efficient in gas-liquid-solid contacting, it was a natural extension to apply this design to flotation & the research commenced in the mid 80's. An opportunity to test the energy savings occurred at Dickenson Mines in 1987, & comparative results with existing conventional flotation cells showed a marked increase in capacity, grade & recovery with 25% less power applied. This r success was followed by the installation of the fist agitated Flotation Colunm (5ft. dia. x 25ft. tall). As a result of the Dickenson success, Hydrochem started a comprehensive 2-part research program in 1988. At Randol Gold Forum 1988 a paper by Hydrochem was pre

Jan 1, 2000

The Coal Utilization review arrived too late to appear in the May issue. Coal utilization technology is improving due to the urgency with the 1990 Clean Air Act and the incentives provided by the Clean Coal Technology (CCT) program. Advances in the CCT are the subject of this report because of their broad industry application, support and involvement. Clean coal demonstration program Projects in the $5 billion Clean Coal Technology program are jointly funded cooperative agreements - not contracts - between government and industry. The industry participant in each project contributes at least 50% of the total cost. The participant takes primary responsibility for the project and is awarded any patent rights for inventions that may occur during the demonstration. The government, on the other hand, ensures that schedules are met, costs are controlled and project objectives are met.

Jan 1, 1991

By David G. Abbott, Frank Coluccio

This paper will discuss the construction of nearly 165 m (540 ft) of 3.5. m (138 in) o.d. reinforced concrete pipe to replace an existing utilidor under the Duwamish River in Seattle, Wash. The project required that two 27.4 m (90 ft) deep shafts be installed for use as jacking and reception shafts during the tunneling operation, and permanent vaults once completed. Soil conditions to be excavated consisted of soft saturated sand and silt with a 21.3 m (70 ft) water head. This required the shafts to be constructed using ground freezing techniques and the tunnel installed by pipe jacking, using a Mechanical Earth Pressure Counter Balance (MEPCB) slurry shield. The original utilidor was constructed between 1924 and 1925, and has since been deliberately flooded because it is considered to be structurally unsound.

Jan 1, 1995

By P. Brooks, W. LaRochelle, J. M. Tranquilla

EMR's recently commissioned Pilot Plant in Fredericton, N.B. Canada, the latest and largest in the company's sequence of prototype and demonstration systems, is being used as a process development facility for mining clients worldwide. Fitted with two microwave reactors and 75 kW generators, this plant is designed as a two-stage continuous processor with a throughput in the 5-10 tpd range depending upon the material feedstream. This facility has been used principally to calcine pyrite and arsenopyrite gold concentrates although it can readily accommo­date carbonaceous materials as well as a wide range of other ore types. Engineering details of the plant and the results of the first nine months of operation are presented. The plant has proven very successful as an advanced process development facility as well as a basic production unit module.

Jan 1, 1998

By Claus Becker

The Mixshield is a tunnelling machine for water bearing soft soils. Developed on the basis of the Hydroshield, it extents the application of this machine to cohesive soils. The design of the drum-type machine allows three different applications 1. As shield with liquid supported face and hydraulical mucking 2. As Compressed-Air-Shield 3. As Earth pressure balanced shield. The Mixshield is employed on three big contracts 1. a 6.3 km ring tunnel in Hamburg, outer diameter 5.95 m, with a new developed segmented concrete lining 2. a 1.9 km pipe-jack job near Cologne, o.d. 3.6 m 3. Metro Lot 3 in Lille/France, o.d. 7.7 m, 3.2 km long with segmented concrete lining and a most sophisticated separation-plant The site experiences will be reported.

Jan 1, 1987

By H. M. Breza

Recovery of phosphate concentrate at Texasgulf’s Aurora Mine has received increased attention as existing mine and plant production capacity limits are reached. Improved mining techniques and mineral processing of waste streams offer the potential to increase phosphate production without major expansion. Innovative processes are being identified to maximize pit mining recovery and to minimize waste stream losses. This results in more effective use of the phosphate. Texasgulf Inc., is a wholly owned subsidiary of Elf Aquitaine. The Aurora phosphate rock mine and refining facilities are located in North Carolina on the south shore of the Pamlico Sound. Phosphate ore is recovered by open- cast mining techniques. Draglines and other earthmoving equipment are used to uncover and mine the phosphate ore. The mined ore then is slurried and pumped about 8 km (5 miles) to the processing plant.

Jan 1, 1994

By S. K. Nandy, K. F. Unrug

The behavior of the immediate shaly roof within a drift mine in eastern Kentucky, operating in the Coalburg seam, was monitored with roof bolt dynamometers. The dynamometers used were capable of providing readings up to a maximum load of 66.72 kN (15,000 lbs), + 0.022 kN (5 lbs). To observe the influence of moisture on the rate and extent of roof deterioration, 57dynamometers were installed on roof bolts anchored in intake and neutral airways. Monitoring was conducted during the period January 1985 through January 1986, in order to cover a full cycle of dry and wet mine conditions associated with seasonal changes. Analysis of the data showed a trend of roof deterioration induced by condensation and eventual penetration of moisture within the immediate roof bedding planes, leading to rapid disintegration of the mine roof.

Jan 1, 1987

By S. R. Rao, J. A. Finch, E. El-Ammouri, K. Ngoviky, P. A. Disten

Sludges produced by lime treatment of acid mine drainage (AMD) can contain significant quantities of base metals which represent both a potential hazard and a loss of values. A new technique for metal recovery from sludge is proposed by combining selective acid leaching and adsorption of metal ions by activated silica sol. The process is demonstrated on two AMD sludges, one containing primarily nickel and the second zinc. They were first treated with sulphuric acid (pH 3.5) to selectively leach the target metals and then activated silica sol was added to the leach solution to adsorb the nickel and zinc. Thickening and centrifuging gave about 90 percent rejection of the input volume to effluent. The adsorbed metals were redissolved by strong acid into a concentrated solution relative to the feed and the silica sol was recycled.

Jan 1, 2000

By Steve Kral

Competition in the gold mining industry throughout the world has become fierce in recent years. The challenge facing operations personnel is to produce more gold for less money. Likewise, the explorationist&apos;s charge is to find more gold in a more cost-efficient manner. That means using new technology to find new gold deposits and expand present ones. More accurate mapping instruments are available to geologists in the search for new deposits. Advanced geophysical and geochemical methods enable explo¬ration teams to review previously mined districts in their search for minable reserves. Four technical sessions on the geology, exploration, and development of gold deposits were part of the program at `world Gold &apos;89,&apos; a Gold Forum on Technology and Practices," held by SME and The Australasian Institute of Mining and Metallurgy in Reno, NV, Nov. 5-8, 1989.

Jan 1, 1990

By G. Roy, C. B. Pettersson, S. Nandagiri, D. J. Ivor-Smith

The Coastal Water Authority&apos;s 2,740mm/2,590mm (108 in./102 in.) pipeline, known as the Northwest Lateral Project, will transport raw water from an existing pipeline over 14.3 km (8.9 miles) to the City of Houston&apos;s East Water Purification Plant. The new pipeline crosses under Houston Ship Channel and Greens Bayou in tunnels at approximately 30.5m (100 feet) and 25.9m (85 feet) depths, which present unique experiences in tunneling under open bodies of water in the Gulf Coast&apos;s soft ground conditions. An earth pressure balance TBM is being used for the deep tunnel sections where the ground demonstrates high overload factors and variable conditions ranging from clays to silty sands. This paper discusses the design approach for the tunnels and shafts, ground conditions, constructability, and selection of the primary lining system.

Jan 1, 1989

By N. R. Sainath

This paper discusses a laboratory investigation that studied the microscale flow characteristics of copper ores and the variation in flow behavior resulting from flow of leach solution. Fractures in 40- and 100-mm-diam (1.5- and 4-in.-diam) cores were first mapped by visual inspection. The permeability of cores to water-stressed in a triaxial stress field representative of in situ conditions - was estimated. The samples were then exposed to 20g/L (2.7 oz/gal) sulfuric acid and the experiment was repeated. The porosity and the rate of recovery of copper from the specimen during leaching were also studied. The measured permeability of unleached samples with no visible fractures ranged from 10-16 to 10-19 m2 and it increased as leaching progressed. The porosity increased significantly with leaching, while the rate of copper recovery decreased.

Jan 1, 1994

By B. K. Mishra, R. K. Rajamani, R. Venugopal, P. Songfack

Millsoft is a computer-simulation software that predicts the performance of large industrial grinding mills. This software surpasses all other tumbling-mill analysis techniques available today because it is based on fundamental laws of physics instead of empirical correlations. Graphical user interface (GUI) forms simplify the specification of the following design and operating parameters: mill diameter, length, speed, charge density and size distribution, lifter material and geometry. All of these parameters are taken into account in the discrete element numerical technique that constitutes the essence of the simulation software. In turn, the software produces a visual animation of grinding-charge motion, predicts mill power and gives the distribution of impact energy. In this paper, a case study of an 8.5-m-(28 ft-) diam SAG mill is used to illustrate the application of Millsoft for mill design and trouble shooting.

Jan 1, 2000