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By Hutton W

The Argyle Diamond Mine is the first significant diamond producer in Australia. The project has been developed with new concepts in circuit design, process control technology, organisational development and training. After its first year of operation, the Argyle Heavy Medium Separation Plant has proven extremely efficient in recovering diamonds. Apart from cyclone wear, no major problems have been encountered. Ferrosilicon consumption is well below the design level which is a reflection of the sound design of the medium circuit. An Audit Plant continuously monitors the Heavy Medium Separation Plant tailings for diamond loss.

Jan 1, 1987

By K. Koneko, T. Nokoyama, S. Shibato

SEYBOLT et al.' have detected various silica films formed on a 3 pct Si-Fe alloy after heating at low oxygen potentials with the electron diffraction method, and they have made some observations on the H,0/H2 ratios required to form them. The purpose of this note is to describe the structure of the oxide film formed on either mechanically or electrolytically polished surfaces of a 3 pct Si-Fe alloy containing small amounts of manganese after heating at low oxygen potential. The samples were prepared from a Si-Fe alloy made in the laboratory using electrolytic iron, 76 pct ferrosilicon, and 76 pct ferromanganese, vacuum-in-

Jan 1, 1969

By P. Bevilacqua, G. Ferrara

Hydrocyclones and other dynamic separators are normally fed with pulps consisting of water and solid particles. The solids usually consist of particles of different sizes, shapes and densities. Except in the special case of monocharacteristic particles, the particles are segregated by these differences in size, shape and density. Segregation is magnified by the high values of centrifugal acceleration in the hydrocyclones. This paper develops a segregation theory that indicates the major variables involved. Experimental data on segregation under different operating conditions for mixtures of magnetite and/or ferrosilicon and nonmagnetic minerals are reported.

Jan 1, 1997

By Hall ST, Miles NJ

Recently an inorganic salt, sodium polytungstate (SPT), has become available that allows the preparation of non-toxic solutions of relative densities up to 3.1. It is relatively expensive and at the higher relative densities achievable, highly viscous. Alternative inorganic compounds may in the future be identified that overcome these limitations. The Australian Mineral Industries Research Association Ltd (AMIRA) has initiated a project to examine possible alternatives. However, it has been found that by the addition of finely divided ferrosilicon to solutions of SPT, relative densities of up to 4.0 can be achieved. A laboratory technique for density fractionation of sized mineral samples utilising this finding has been developed. This is currently being extended to study the potential applications of such liquids and suspensions in dynamic systems for mineral, coal and recycled waste separations.

Jan 1, 1993

By M. F. Williams, L. G. Hendrickson

In classification of pulps bearing magnetized ferro-magnetic particles, depolarizing is of great importance. If size separation is to be effective, particles must be individual rather than in flocs. Depolarizing is also practiced in heavy medium separations in which ferrosilicon or magnetite is the medium. When particles of ferromagnetic material have been removed from a magnetic field, residual magnetism causes agglomeration. The term depolarizing refers to the operation of reducing or eliminating this residual magnetism and may thus be considered magnetic deflocculation. The terms demagnetizing and randomizing are also used.

Feb 1, 1956

By H. L. Hollis

The paper read by Mr. George J. Snelus, in 1894, before the Iron and Steel Institute of Great Britain* so fully and ably described the Walrand-Leghisel process that there remains very little to add beyond recording some changes in practice, made since that date, and observed by the writer last summer, at several continental works, and the further fact that the process has now been for some time in successful operation in this country. Briefiy stated, the Walrand-LegBnisel process is an addition to the Bessemer operation, with the object of obtaining quiet and more fluid steel, and consequently sound castings and ingots. This is achieved by adding ferro-silicon at approximately the time of flame-drop in the ordinary Bessemer operation, and making an after-blow. The high calorific power of silicon is well known, and the rapid combustion of it immediately before

Jan 1, 1897

By P Wollants, B Blanpain, R Ding

Vacuum oxygen decarburisation (VOD) is the refining process used by ALZ (Genk, Belgium) for their production of stainless steels. The process consists of three stages: oxygen blowing at a pressure of 100 mbar, degassing, and reduction of the slag with ferrosilicon at 5 mbar. The magnesia-chromite bricks used in the slag zone of the ladles suffer from acute wear. In this paper results obtained from a program to improve the refractory life span are presented. The dominant wear phenomena were identified with an electron microscopy study of bricks taken from different locations in the ladle. Concurrently a dynamic model for the vacuum oxygen decarburisation (VOD) refining process was developed. The model calculates the elementsÆ oxidation rate during the blowing oxygen stage and allows the continuous calculation of the change of the metal, slag and gas composition throughout the VOD process. From these activities a general scheme of the refractory wear was worked out and measures to improve the refractory life were proposed and implemented.

Jan 1, 2000

By Stephen E. Erickson, Donald G. Oss

The need for instrumentation and automatic control of the various parameters in the heavy media process of iron ore beneficiation has been apparent for some time. Continued demands for higher grade, competitive products from the Mesabi Range have made it necessary to increase the efficiency of the process in every possible way. In a typical heavy media flow scheme for iron ore beneficiation (Fig. 1) a sized, prepared feed (generally about minus 1 ¼ in. to plus ¼ in.) is fed to a heavy media separatory vessel, along with a ferrosilicon slurry. A separation of the feed is made on the basis of specific gravity. Low density particles overflow a tailings discharge weir, while high density ore particles sink to the bottom of the high density pool and are moved away to the concentrate discharge chute.

Jan 5, 1962

By Roshan B. Bhappu, Thomas J. Lien

The DYNA WHIRLPOOL Processor (DWP) is a cylindrical dynamic heavy media vessel. It is used to beneficiate fine ore sizes from one and one-half inches in diameter down to 65-mesh. Process units available treat up to 80 tons per hour. Units can be manifolded for higher capacity plants. Finely ground magnetite and ferrosilicon are used for media. , Installed capital costs are from $4,000 to $6,000 per ton hour of feed. Operating costs are from $0.30 to $0.50 per ton of feed. The DWP is used to beneficiate metallic and non-metallic ores and coal. The OCC Vessel is a static heavy media separator used to beneficiate coarse ore up to six inches in diameter and auto scrap. Process units available treat up to 300 tons per hour.

Jan 1, 1978

No. 230. Two engineers, technical graduates, three to five years, experience. One to take charge of 'pyrite mining in Canada; the other to assist in the mining work at the head office in New York. Salary for the right man, $5000. No. 231. Two young engineers, preferably men who have just graduated from college who are looking for an opportunity to work up with a reputable mining company. Men who have had some practical experience will be considered. No. 232. Assayer. Wet analyses, principally of lead, zinc, sulphur and insoluble. Assayer will also have some mill sampling and experimental work in a new flotation installation, as well -as control of regular mill operation and development-work samples front the mine. $75 to $100 per month and board, according to experience of candidate. No. 233. Engineer to lay out, erect and operate calcium carbide and ferrosilicon plant in the State of Washington. One furnace, 1500 hp. No. 234. Professor of metallurgy for school of mines in western state. $3000 per year to man properly qualified for the work.

Jan 9, 1917

By Laszlo Valentyik

To separate minerals on a small scale according to their specific gravity, heavy liquids are used, but because of high costs and health hazards they cannot be used in large scale plants. In order to substitute heavy liquids, finely ground solids like magnetite and ferrosilicon mixed with water and clay for the required specific gravity are employed. The clay present in the medium acts as a stabilizing agent since the coarse heavy media solids would sink very fast to the bottom of the container if they were mixed only in water. The optimum amount of clay varies for different processes, but it is generally between 3-6% by weight concentration of solids. As the pseudo-plastic nature of polymer solutions has excellent suspending properties, investigations were conducted at the Institute of Mineral Research to ascertain whether polymers could be used commercially as suspending agents for finely ground heavy media.

Jan 1, 1973

By Marshall T, Nicholson DS

Reserves of high-grade quartz gravel, lignite and timber suitable for the production of silicon metal and ferrosilicon on large scale occur within 40 miles of Bluff Harbour. Undeveloped hydroelectric power resources on the Clutha River are located within 50 miles of the most promising quartz gravel deposits while ooencastable lignite, potentially suitable for electric power production, occurs in the same locality as the quartz gravels. A preliminary study of production economics indicates that the commercial feasibility of silicon/ferro-silicon production would depend mainly on the cost of electric power, total capital cost of plant, and the market value of the products. The proximity of Bluff Harbour is advantageous for the export of products.

Jan 1, 1971

By Laszlo Valentyik, John T. Patton

A conventional heavy-media separation process utilizes a mixture of finely ground solids like magnetite, ferrosilicon, or shale and water. The always-present clay in the medium acts as a stabilizing agent since the coarse heavy-media solids would quickly sink if they were mixed only in water. As the pseudoplastic nature of polymer solutions has excellent suspending properties, laboratory investigations were conducted at the Institute of Mineral Research on whether polymers could be used as suspending agents for finely ground heavy media. The preliminary results (published previously) of the laboratory research studies have shown that sufficient stabilities of heavy media can be obtained at a relatively low polymer concentration. This paper is a continuation of the previous work and it presents some of the results of recent studies where the rheological properties of the heavy-media suspensions were studied in a newly developed settling tube and the already familiar concentric-cylinder-type consistometer. In the investigations bentonites as a stabilizing agent also were included so that comparative results would be available to the plant engineer to assist him in the choice of the most suitable material for stabilizing various heavy media.

Jan 1, 1977

By P. G. Barnard

Losses of alloying metals in furnace flue dusts, grinding swarfs, and mill scale produced during the manufacture of stainless steel are substantial. About 25 million lb Cr, 8.7 million lb Ni, and 150,000 lb Mo and other critical metals can be made available annually for recycling by a process developed by the Bureau of Mines. Stainless steel wastes pelletized with a portland cement binder were reduced in a small electric-arc furnace by a two-stage process to produce a recyclable alloy containing Cr, Ni, Mn, and Fe. The initial reduction was with carbon; the second, with ferrosilicon. Results are compared with previously reported laboratory induction melting tests. A 2,000-lb demonstration test of the process in a commercial electric-arc furnace is also described. Data are also presented on three 1,500-lb tests made using various slag conditions in the electric-arc furnace. Recoveries up to 99 pct of the Fe, Cr, and Ni contents of stainless steel wastes were obtained in using the process.

Jan 1, 1977

By Yue Gong, ChuanJie Cai, Jing Chen, Shaobo Zheng, Huigai Li

"MnS-AlN duplex precipitates were successfully extracted from electrical steel slabs by means of non-aqueous solution electrolysis. The three-dimensional duplex morphology became visible using emission scanning electron microscope (SEM) JSM-6700F and energy dispersive spectroscopy (EDS). The precipitation sequence of MnS and AlN in the hot process can be predicted via the three-dimensional duplex morphology. Thermodynamic calculations were carried out on account of the chemical compositions of the steel studied in this paper. The results verified that AlN nucleated on MnS, which precipitated earlier during cooling process of electrical steel. Based on the results, the material compositions and rolling temperature can be adjusted to modify their precipitation timing and morphology. This is conducive to the growth of MnS-AlN duplex precipitates and reducing the obstacles to grain growth. Finally the magnetic property of electrical steel would be improved.IntroductionElectrical steel is a kind of ferrosilicon soft magnetic alloys with extremely low carbon content. It is mainly used in the manufacture of motors, generators, transformers and varieties of teleco=unications equipment. Non-oriented electrical steel requires isotropic high magnetic induction and low iron loss [l, 2]. Precipitates in steel have a great influence on its performance [3]. On the one hand, the indirect effect of precipitates on magnetic properties is to restrict grain growth in high temperature annealing process. On the other hand, the direct effect is pinning of domain wall motion, which leads to increased hysteresis loss."

Jan 1, 2013

By I. M. Morsi

The present study investigates the feasibility of using some materials as start-up slags for the extraction of magnesium metal from Egyptian dolomite ores by the Magnethermic technique. The reduction of roasted dolomite (dolime) takes place in a closed evacuated electric arc furnace (small Magnetherm reactor) using ferrosilicon as a reducing agent and liquid start-up slag as a reduction bath under an inert atmosphere. The operational parameters affecting the stabilization of the start-up slag composition and the extraction of magnesium such as reducing agent stoichiometry, reduction temperature, and time were investigated. The dolomitic charge was in the form of sintered briquettes. The charge was reduced under an argon atmosphere in the Magnetherm reactor for constant period and constant temperature. The results showed that the clinker can be used as a start-up slag for the magnethermic process. Also, the optimum conditions for the extraction process were found at 2XSi stoichiometry to give maximum reduction of 80% after 15 minutes reduction time at a temperature of 1550°C. XRD and XRF measurements were used to determine the phases present and the extent of reduction of magnesium, respectively. Keywords magnesium, dolomite ore, magnetherm, magnetherm reactor, silicothermic reduction.

Jun 1, 2013

By A. F. Alsobrook

Specialty silica materials, as defined in this chapter, are rocks that consist predominantly of silica (SiO2) and are produced as chunks, round pebbles, and sawed or trimmed blocks and other shapes for nonconstruction applications. The rock types include quartzite, sandstone, novaculite, flint, chert, and vein quartz. Other terms used commercially include jasper, silex, lascas, and rock crystal. In its publication, Minerals Yearbook, the US Bureau of Mines (USBM) reports the production and consumption of some specialty silica materials under several headings. Quartzite, sandstone, and novaculite used in abrasive applications are addressed by the USBM under Abrasive Materials. Lascas, a type of vein quartz used in growing synthetic quartz crystals and in fusing applications, is discussed under Quartz Crystal. Silica gravel used in manufacturing silicon metal and ferrosilicon, as metallurgical fluxstone, and as a filtration medium is covered under Industrial Sand and Gravel. Information on

Jan 1, 1994

By G. Ferrara, P. Bozzato, B. Chinè

To obtain a reliable comparison between conical and cylindrical separatory vessels used in dynamic dense-medium separation systems, the following two studies were made: a study of the swirling flow in conical and cylindrical vessels using laser-Doppler velocimetry (LDV) and a study of the behavior of suspensions of magnetite and ferrosilicon in water in both separators. It was found that the tangential velocity profiles differ in conical and cylindrical vessels. In a conical cyclone, free vortex conditions affect the largest part of the vessel, while in a cylindrical vessel, the motion approaches that of a forced vortex, i.e., that of a centrifuge. It was also found that the conical vessel manifests higher centrifigal acceleration and very strong densifying (the density differential) and, hence, the density gradient inside the vessel is large. It was found that the cylindrical vessel manifests lower centrifugal acceleration and low densifying, i.e., low-density differentials, and hence, the density gradient inside the vessel is small. Also, due to greater densifying, the density cut-point in cyclones is higher than the operating medium density, while, in cylindrical vessels, the density cut- point is closer to the medium density. The results provide an interesting description of the differing behaviors of conical and cylindrical vessels, and they help explain the differences in pegormance between the two types of separators.

Jan 1, 2000

By Leon Keller, William R. Van Slyke, James Stukel

Two 4-ft wide DSM screens were installed during 1957 in one unit of the two-unit heavy media cy- clone section of the Holman-Cliffs concentrator at Taconite, Minn., following successful laboratory test work on a 1-ft screen. The two screens materially reduced the amount of media sent to the magnetic separator cleaning circuit. Wear life was good and fine size capacity was high. Briefly, the Holman-Cliffs heavy media cyclone plant uses -65 mesh magnetite as media and 10-in. diam., 30º Ni-Hard cyclones as separatory vessels. Feed to the plant averages 130 long tons per hr of -1/8 in. +65 mesh material. The conventional heavy media circuit uses drum or spiral type separatory units and treats +l/8 or 3/16-in. material. The medium is generally -65 mesh ferrosilicon. Ore and media are readily separated by screening at about 6 mesh. At this size, capacity is high and wear and maintenance are not excessive. The heavy media cyclone plant requires an efficient separation between +65 mesh ore and -65 mesh media. To reduce costs, however, the separation was made at a coarser size with the result that the media was un- duly contaminated and it was necessary to clean large tonnages of media and ore in magnetic separators. Due to the high capital cost of these units, their number was kept to a minimum and, consequently, they were overloaded. As a result, the separation between magnetic media and nonmagnetics was not sharp and the magnetite losses were high.

Jan 10, 1958

By B. M. Loring, I. R. Kramer, F. M. Walters

No observations on the mechanical properties of iron-manganese alloys have been published since pure manganese became readily available, either distilled manganese or electrolytic manganese. The purpose of this investigation was to determine whether iron-manganese alloys are essentially brittle, as reported by Hadfield,1 or whether the lack of ductility observed was due to impurities in the alloys that he studied. EXPERIMENTAL METHODS The alloys were melted in a 100-lb. high-frequency induction furnace with a magnesia crucible, using ingot iron and electrolytic manganese. The heats were split, the first giving six 18-lb. ingots and the second three. Each successive heat was higher in manganese and about 0.3 per cent silicon [ ] was added as ferrosilicon. The alloys forged without difficulty-and were given a 90 percent reduction to 3/4-in. rounds. The chemical analysis of the alloys is given in Table I. The forged rods were homogenized for [ ] 24 hr. at 1150°C. (2100°F.) and air-cooled. The alloys were tested in two conditions of heat-treatment: (I) as normalized from 870°C. (1600°F.) and (2) normalized from 870°C. and tempered for z hr. at 540°C. (1000°F.) and air-cooled. The tensile specimens were 0.505 in. in diameter with a 2-in. gauge length, and the impact specimens were V-notch Charpy. The proportional limit and yield strength were taken from the stress-strain diagrams drawn by a Peters recorder. The data obtained from the tensile test and the hardness measurements are given in Table 2. Specimens that were normalized are designated by N; those that were normalized and tempered by T. Alloy G was tempered after forging (D).

Jan 1, 1941