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By Ahmet Geveci

[Generally accepted formula related to sulfur slag-metal distribution ratio is given by the following equation: [ ] According to the above equation it can be deduced that sulfur distribution between slag and metal is governed mainly by metal composition (?s term), slag composition (slag basicity and in turn sulfide capacity), oxygen potential of the system (ao¬¬ term) and temperature(related to equilibrium constant, K). In this study, the results of ladle furnace operations conducted in Erdemir-Iron and Steel Works Co. (Turkey) in relation to sulfur removal, have been given. Typical ladle furnace slag analyses of 4937K quality steel have been presented. Activity coefficient of FetO,?FetO, have been calculated with the relation obtained fromthe literature. Activity calculations have been performed with the program written in Mathcad. The changes in activity of aFetO in the slag phase,, have also been studied in relation to the sulfur removal: The relation between % Decrease aFetO and %DeS (measured)have been investigated for 4937K runs and someother types of steel produced in the Erdemir Plant. Related to ladle operations %desulfurization defined as [(%Sinitial-%Sfinal)/S%initial]*100 values have been presented for different steel qualities.]

Jan 1, 2006

By Sylvie C. Bouffard

The need for a better understanding of the heap biooxidation pretreatment of pyritic refractory gold ores has prompted us to develop a rigorous mathematical model of the process. The hydrological structure of the model takes the form of lateral stagnant pores in contact with a uniformly distributed gas stream and connected to vertical plug flow channels, as suggested by the results of an independent study of column hydrology. A model of pyrite oxidation kinetics was derived based on electrochemical leaching theory and the results of potentiostatic stirred tank and column tests. The growth rates of attached and planktonic iron- and sulfur-oxidizing cells are modeled with separate Monod expressions over three separate temperature ranges corresponding to mesophiles, moderate thermophiles, and extreme thermophiles. Isothermal column tests validate the model simulations. Excellent fits of several leaching indicators (potential, extent of sulfide oxidation, iron concentration, cell numbers) reveal the rate-limiting step to shift from particle kinetics to oxygen gas/liquid mass transfer with increasing temperatures and pyrite head grades. Competition for oxygen between sulfur- and iron-oxidizing microorganisms lowers potentials and slows down pyrite oxidation. This modeling tool may assist engineers in the design and operation of heaps to give more complete gold liberation in a shorter time.

Jan 1, 2003

By S. F. Cheng

Among the many extraordinary features of the rare earths are their magnetic and magnetoelastic properties. The rare earths, e.g. Tb, Dy, Nd, Sm, are known worldwide for their large magnetocrystalline anisotropy and magnetization, which has led to the importance of magnetic rare earths as vital ingredients of modem permanent magnets. In this paper, we focus on the strain dependence of these giant effects which gives rise to huge magnetostrictions, magnetomechanical couplings, and ?E effects. Magnetostrictions greater than 10-3 have been measured at temperatures as high as 500 K. At low temperatures magnetostrictions reaches -1%. ?E effects - 10. No other solid state material has matched these values. A proper balance of magnetic anisotropy and magnetostriction, plus a proper choice of crystal axes lead to alloys which can switch large quantities of energy between the internal (magnetic) and external (mechanical) states with the application of small triggering magnetic fields. In addition to the traditional use of these materials in transduction, they are particularly valuable for smart systems where reliability and robustness are needed such as active structure stiffening and active vibration control.

Jan 1, 1997

By Peter Koh

The velocity solid charge attains when dropping down concentrate chutes is an important boundary condition when developing mathematical models of flash furnace burners and reaction shafts. In this work an experimental rig was developed to measure the velocity attained when nickel concentrate and sand were dropped down a vertical pipe 3m long. The velocity measurements showed that the nickel concentrate did not fall as individual particles. The measured values of the velocity approached, but did not attain, those calculated for solid bodies, the disparity being attributed to friction at the pipe wall and fluid drag losses. After falling 2 m velocities between 5-6 m/s were attained. The analysis was extended and applied to understanding the intermittent problem of puffing which sometimes occurs from the top of the concentrate chute. The pressure at the bottom of the chute is the net result of two opposing pressures, namely that developed by (a)the process air entering through the velocity control device, and (b) the solids falling down the concentrate chute. Flow back up the chute occurs when the former exceeds the latter. The process air pressures in the burner were obtained from CFD simulations of a full burner. Variables considered included air speed through the velocity control device, drop height and furnace draft. The analysis was useful in highlighting the operating conditions which were conducive to puffing and in establishing procedures to minimise its occurrence.

Jan 1, 2006

By Yang Tian-zu

Sodium pyroantimonate which is widely used as the clarifier in the glass industry and as the synergist in anti-flaming industry respectively has a production history of about 30 years in China. At present there is the production capacity of about 20,000 tons per year in China and China is chief producer of sodium pyroantimonate. In this work the production processes adopted by the producers of China, the operation conditions and the product qualities of sodium pyroantimonate prepared by different preparation methods have been summarized, and on the basis of comparing the advantages and disadvantages for each process the most advanced method - the air-oxidation method was introduced in detail. The production processes of sodium pyroantimonate mainly include the method of oxidation by sodium nitrate, the oxidation method of hydrogen peroxide, the potash salt method, the chlorination method and the air-oxidation method etc. The method of oxidation by sodium nitrate in which the crude antimony oxide, sodium carbonate and sodium nitrate are separately used as the raw material, the flux agent and the oxidant, has the advantage of short and simple technological process, but low grade quality of sodium pyroantimonate and bringing about serious environmental pollution are the disadvantages and this method has been substituted by other methods. Sodium pyroantimonate can be directly prepared by the hydrogen peroxide oxidation method with the advantages of simple technological process, high grade quality of the product and little environmental pollution. High grade quality of sodium pyroantimonate can be also synthesized by the potash salt method, in which industrial antimony white, the hydrogen peroxide, potassium hydroxide and sodium hydroxide are applied as the starting material. The disadvantages of these two preparation methods are high production cost and high requirements on the raw materials. The chlorination method with the crude antimony oxide, hydrochloric acid and chlorine as the raw material has the advantages of low production cost and high grade quality of the product. However complex process, high requirement of anti-corrosion for the equipments and producing plenty of waste water limit its application. The air-oxidation method with stibnite/jamesonite concentrate, sodium sulfide, and sodium hydroxide as the raw material and atmosphere as the oxidant is a newly developed method and its advantages are low production cost and the complex raw material can be treated by this method and its disadvantage is that the quality of sodium pyroantimonate is lower than that prepared by the oxidation method of hydrogen peroxide and the potash salt method.

Jan 1, 2006

By Jun-ichiro Yagi

A mathematical model has been developed for simulating the blast furnace operation with carbon composite agglomerates charging based on multi-fluid theory and reaction kinetics. In this model, the behaviours of carbon composite agglomerates are considered on the basis of previously reported conservation equations and experimental research on the reduction rate of carbon composite agglomerates. A series of calculations are performed to examine the effect of charging carbon composite agglomerates. The model calculation gives two-dimensional distributions of process variables and information on the overall operational parameters. It reveals that in-furnace temperature levels significantly decrease and the reduction of carbon composite agglomerates is retarded with carbon composite agglomerates charging ratio. The furnace performance is remarkably improved with the increase in carbon composite agglomerates rate. The productivity tends to increase while coke rate and total reducing agent rate show decreases at the different degree.

Jan 1, 2006

By Kang-In Rhee

Nonferrous metal recycling not only provides energy saving and environmental benefits but also is a significant factor in the supply of various types of metals used in our society. Recycling plays an important role in establishing the sustainability of materials. The total amount of recycled nonferrous metals by weight accounts for less than 5% but their value is larger than 50% compared to ferrous metal recycling which consists of about half of the total metal recycling in weight. This paper describes trends and typical achievements in nonferrous metal recycling and overviews the present and future of nonferrous metal recycling technology and business in Korea.

Jan 1, 2006

By N. R. Green, N. J. Humphreys, D. McBride, T. N. Croft, M. Cross, D. M. Shevchenko

"Centrifugal casting offers a route to high quality products in difficult to cast high temperature low superheat alloys and thin section molds. Under centrifugal forces metal is forced into thin sections and can fill thicknesses of less than a millimeter. However, due to the high liquid metal velocities there is a high risk of surface turbulent flow and air entrainment within the liquid metal. The combination of interacting flow-thermal-solidification phenomena and associated defects is a challenging modeling task which the authors have previously described and validated. Capturing the metal-air interface, on what are inevitably complex three dimensional geometries, results in highly computationally expensive simulations and simulating a single cast can take weeks on a single processor. This contribution reports on modeling a complex centrifugal cast, gas entrainment, bubble transport and solidification, employing meshes of up to a million elements and investigates the scalability of the model on high performance clusters.Introduction The ultimate goal of any casting procedure is to produce a defect-free product. For difficult to cast alloys, such as Titanium, centrifugal casting has a number of advantage over conventional gravity methods [1]. In the casting of thin sections, such as turbine blades, the metal is forced into the thin sections under centrifugal forces. The centrifugal force can overcome the backpressure due to surface tension and the metal can fill mould sections with thicknesses substantially less than a millimeter. However, the materials used in these castings [2] tend to be highly reactive and requires low superheat. High liquid metal velocity gives rise to a high risk of free surface turbulent flow and of associated entrainment through free surface turbulence [3] and trapping of gas present in the flow [1]."

Jan 1, 2012

By Hang Goo Kim

A mathematical analysis based on equilibrium modeling has been developed to describe the distribution behavior of minor elements such as Pb, Zn, Bi, Sb, and As among gas, slag and recovered copper phases during the reduction of copper oxide in slag cleaning with CO gas. The results show that large fractions of the impurities transferred to slag during smelting or converting are recycled to the recovered copper metal. It is also shown that there is a limit to the recovery of copper from slag because iron oxides are also reduced to form a copper-iron alloy at low oxygen potentials. The effects of various operating parameters such as temperature, the activity of FeO, the initial amounts of the elements in the slag and CO content in process gas, on the behavior of these minor elements are discussed. The predicted results were compared with the results of a pilot plant operation in which pulverized coal was used as a reductant. Consistent trends between the two cases were obtained.

Jan 1, 1992

By Lifeng Zhang

The transport of fluid, heat and particles (bubbles and solid inclusions) in flowing molten steel is investigated in steel refining ladles, the continuous casting tundish, continuous casting mold and strand, and steel ingot casting processes. Inclusion removal from the molten steel by flow transport and bubble flotation, and inclusion growth by collision and diffusion are discussed. Removal of impurity elements such as [C] and [O] during steel refining are reported.

Jan 1, 2006

By V. V. Geikhman

The paper updates the Plant experience in the development and implementation of an advanced environmentally friendly zinc production technology complying with the technological and economic level of producers in the world and the standards of maximum permissible gas emissions stipulated by the Russian legislation. General water recycling engineering allowed to ensure 95.6% water rotation level. All solid wastes formed during treating zinc concentrate are processed into marketable products or semiproducts and sold. As a result of implementing innovation techniques production at the Chelyabinsk Zinc Plant is non-waste.

Jan 1, 2006

By R. W. Hammack

Results for the treatment of a problematic mining wastewater using bacterial sulfate reduction (BSR) are presented. Specifically, a BSR pilot treatment plant (250 L per day) was used to treat Berkeley Pit simulant to discharge standards with the selective recovery of separate Cu- and Zn-sulfide concentrates. Concentrates recovered in these tests contained greater than 50 % of the target metal and met specifications for sale to existing smelters. The biological component of the treatment was found to be surprisingly robust. Scaling and solid/liquid separation problems were encountered but considered normal for sulfide treatment. For Berkeley Pit water, capital costs for BSR treatment was found to be comparable to high-density sludge lime treatment. The value received from the sale of recovered copper ands zinc concentrates paid for all the operating costs.

Jan 1, 1999

By Kalathur S. Narasimhan

Powder metallurgy is a net shape process competing favorably with machining, stamping, forging and castings. The growth of ferrous powder metallurgy over the past four decades reflect the advancements in materials technology, compaction technology, sintering technologies and other related fields. This presentation gives a brief background on how materials technology evolved.

Jan 1, 2006

By Mieke Campforts

The usefulness of the water-cooled probe technique to experimentally study slag solidification and freeze lining formation in pyrometallurgical reactors is evaluated. With this technique a layer of solidified slag is formed on a water-cooled probe that is submerged into a liquid slag bath. The influence of the submergence time and the heat input is examined. The solidified layers are analyzed with light microscopy, electron microscopy, electron probe micro-analysis and X-ray diffraction. Thermodynamic software is used to interpret the solidification microstructure. The results demonstrate that the technique is useful to understand freeze lining formation.

Jan 1, 2006

By Ross Baldock, Ross Andrews, Gu Helin, Lan Xu, Markus Reuter, Song Xingcheng

"A commercial lead smelter using Outotec Ausmelt TSL Technology has been successfully commissioned and put into operation at Yunnan Tin Company Ltd operations near Gejiu City, in Yunnan Province, China. The plant was commissioned in July 2010 after three years in the design and construction phase. The process uses a three stage batch process to produce lead bullion and zinc fume, and a slag that is low in metal values. The paper provides details of this lead smelting project, including the theoretical evaluation of the multi-stage process chemistry, engineering design, plant commissioning and the final operation. Comparison of the design targets and actual performance of the plant is emphasized. The fast ramp-up to full production of the largest Ausmelt TSL lead furnace built to date is highlighted.IntroductionIn 2002, Ausmelt and Yunnan Tin Company (YTC) successfully commissioned a smelter to modernise the Yunnan Tin smelter in Gejiu City, Yunnan Province, China. A single Ausmelt furnace was installed by YTC to process tin concentrate and revert materials, to produce YT Brand tin product. The advanced Ausmelt Technology furnace at YTC replaced seven existing reverberatory furnaces and provided a flexible, energy efficient and environmentally beneficial system to complement the world leading refinery facilities of YTC."

Jan 1, 2012

By Eustathios S. Kikkinides

This work presents an integrated approach for the optimal design and control of hydrogen storage beds. A detailed 2-D mathematical model is developed for metal hydride beds and validated against experimental and theoretical literature results. Based on recent advances in dynamic optimization, the model is used to find the optimal process design and operating strategy in order to minimize the storing time, while satisfying, a number of operating constraints (such as pressure drop limitations, cooling fluid availability and maximum tank temperature). Trade-offs between various objectives, alternative design options and optimal cooling control policies are revealed illustrating the potential of the approach. In a further step the model is used to exploit the benefits between material and process design. Systematic simulation and optimization studies are performed at two different length scales (tank and adsorbent pore level) for carbon based materials. The macroscopic approach determines the optimal values of the sorption parameters while, based on these results molecular simulation techniques are employed to determine the pore size distribution of the adsorbents.

Jan 1, 2006

By Guozhu Ye

"One of the most essential problems associated with the treatment of EAF dust is its high content of halogens. For most thermal processes for zinc recovery, such as the plasma processes with a zinc condenser, the halides in the gas stream will form a dross phase that results in a low zinc yield. For those with zinc oxide as main product, such as Waelz oxides, the high halogen content in the product implies a great degradation of the product quality and the product can only be sold at a low price. Further processing of zinc oxide with high halogen content either by pyrometallurgical or hydrometallurgical processes will also result in process problems.This paper will review the pre- and post-treatment alternatives for halogen removal based on the comprehensive characterization work that has been carried out at MEFOS and the preliminary experimental results.The experimental results show that chlorine and fluorine content could be reduced to 450 ppm and 50 ppm respectively by selective sulfation, and to about 200 ppm by soda leaching. Selective sulfation of zinc oxide in the EAF dust will also be discussed."

Jan 1, 2000

By Zviad Kovziridze

Structure of celsian ceramics in BaO-Al2O3-SiO2system is studied with electron microscope in the entire temperature region of baking interval. The process of the pores filling and the full consolidation of material growth at comparatively high temperatures of baking intervals are described.

Jan 1, 2006

By Rauf Hurman Eric

In this review paper the effect of composition and temperature on electrical conductivity and viscosity of the slags encountered in electric smelting of PGM-containing sulfide concentrates is described along with their liquidus temperatures. Optimization of slag composition is attempted on the basis of opposite trends of viscosity and electrical conductivity. Metal losses to slag, matte-slag separation and matte settling are also discussed in conjunction with interfacial and surface tension concepts. The electrode immersed in the slag phase is the main factor in the design and operation of the furnace. The most important electrode parameters are the size and the positioning in the slag phase which are determined by the slag resistivity, furnace resistance, cell constant and power input. The flow of heat generated by the electrode current determines the energy distribution and furnace dimensions creating viscosity profiles within the slag phase which in turn affects the flow conditions. Thus the flow of slag is discussed together with furnace geometry, stirring action, buoyancy and electromagnetic effects and the action of the electric furnace as a settler is emphasized. A discussion on the design d production capacity of the furnace is provided which are based on considerations derived mainly from slag properties.

Jan 1, 2006

By Guo Xian Jian

In this paper, an alternative process to recover the value metals from polymetallic gold ore by FeCh leaching was proposed. In the process, gold was recovered by direct cyanidation from the leaching residue, the isolative electrolyte in chloride solution was selected to recover lead, the cementation with copper powder was used to recover silver and the solvent extracting was applied to recover copper and zinc. The total recovery of gold, lead, copper, silver and zinc in the process is 90.8%,96.05%,84.3%,81.98% and 54% to the bullion of gold, lead and silver and sulfate of copper and zinc, respectively. The process conditions selected for FeCh leaching are the temperature of 104°C, leaching time of 6 hours, Fe3+ content of 140 g/l and stoichiometry of FeCl3.

Jan 1, 1996