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By Maurizio Marezio Bertini

Ammonia - ammonium sulfate solutions were sparged in a glass reactor with a SO2/O2 gas mixture (2% SO2 and 98% O2) to leach copper from pure chalcopyrite and chalcopyrite concentrate. The SO2/O2 mixture produces higher and faster extractions than O2 by itself. The effect of temperature, particle size and free ammonia concentration was investigated. The fastest and highest recoveries were obtained at 80 oC from a chalcopyrite concentrate with a d80equal to 13 m, with about 83 gpl free ammonia, an average pH equal to 8.75 and a stirring speed of 500 rpm. The extraction process was controlled by diffusion through a product layer, according to the shrinking core model, with an activation energy of 41 kJ/mole.

Jan 1, 2003

By Zenjiro Asaki

The copper concentrate particles dissolve quickly into the molten matte in the smelting furnace of Mitsubishi Process, which indicates that the sulfide smelting is essentially a gas/liquid reaction. In this paper, theoretical calculation has been made on the rate of oxidation of FeS component in the matte to form FeO by rising gas bubbles using the penetration theory. The results showed that all the oxygen in the bubble of 1.2 cm in diameter, which is the maximum stable diameter, is consumed in 3 ms. This time required is sufficiently short, and it results in the actual operation of smelting furnace of 1100% oxygen-efficiency. These calculations indicate that most smelting reactions are completed just under the lance, except slag formation.

Jan 1, 2002

By Kejun Liu

Platinum and palladium are usually dissolved together and followed by separation. In this study, the selective leaching of platinum and palladium from a secondary resource, such as dental waste, by using chloride solution (hypochlorite and chlorate) has been developed. Results indicate that about 100% of palladium could be initially extracted by the combination of 0.3 mol/L sodium hypochlorite (NaClO) and 0.068 mol/L sodium chloride (NaCl) at pH 1.2 and 298K in 1.5 hours, or the combination of 0.005 mol/L sodium chlorate (NaClO3) and 6 mol/L hydrochloric acid (HCl) at 298K in 0.5 hour. About 100% of platinum could be extracted from the residue by the combination of 0.47 mol/L sodium chlorate (NaClO3) and 12 mol/L hydrochloric acid (HCl) at 298K in 2 hours.

Jan 1, 2003

By Leszek Blacha

Since several years aog there is noted an increasing importance of the metallurgical vacuum technologies. This refers mainly to the extra furnace steel treatment processes, melting of steel and special alloys in the induction and arc vacuum furnaces, as well as refining processes of nonferrous metals. In the presented work, there is discussed a phenomenon of evaporation of volatile components of metal bath under reduced pressure with description of kinetics of this process. In this article are presented are the evaluation of the mass transfer coefficients in the melt and gaseous phase. Based on results of our own research on removal rate of impurities from liquid copper (bismuth, lead) in vacuum refining process, it is determined the thickness of hypothetical boundary layer in the gas phase. This allowed to formulate a general kinetic equation defining the evaporation rate of gaseous components from metal bath. The values of mass transfer coefficients determined from this equation were compared with experimental results by other authors working on the evaporation effect of melt components of metal alloys.

Jan 1, 2006

By Justin Karl, Ali Gordon, James DeMarco, Yongho Sohn

"Aluminum metal-matrix composites are lightweight materials that have the potential to supplant steel in many applications. The current work helps to identify the parameters that confer maximal strength and ductility. Torsion tests were performed on the as-cast aluminum metal-matrix composite A359-SiCp-30% at a variety of temperatures and twist rates. Dependence of material properties on temperature and strain rate were identified from equivalent stress-strain curves constructed from the reduced data. Examination of the microstructure was performed on the as-cast material and on fracture surfaces. A temperature-and strain rate-dependent constitutive model was applied to simulation of the mechanical response of the torsion specimen. Trends in material properties corroborate and extend trends identified previously under tensile loading with regard to temperature and strain rate dependence. Shear properties of simulated specimens agree with properties obtained through experimentation.IntroductionAluminum metal-matrix composites (A1-MMCs) have become increasingly popu1ar in recent years. While unreinforced aluminum alloys have low densities and high ductilities, they are not suitable for many applications due to their lack of strength and stiffness. To provide added strength and stiffness while maintaining favorable densities, it has become common to reinforce aluminum alloys with silicon carbide in various forms, although usually the inclusions are in the form of whiskers or particles. The result is a composite material with superior specific strength and stiffness. While whisker-reinforced composites are expensive due to the necessity of processing by nonstandard techniques and have low transverse properties when rolled, particle reinforced Al-MMCs have transverse material property values almost as high as the longitudinal properties and are not as expensive to process as whisker-reinforced Al-MMCs [1]."

Jan 1, 2012

By Xinghua He, Shujing Zhu

"In this paper, the chemical composition, the content and the leachability of heavy metals in dredged sludge are tested and analyzed. It is shown that the leachability of Pb and Cr exceeds the leaching toxicity standard, and so the dredged sludge is considered as hazardous waste and must be solidified. The effect of solidifying the dredged sludge by the hydraulic ash-slag cementitious composites is studied, and it indicates that the heavy metals can be well immobilized if the mass fraction of the dredged sludge is appropriate. The heavy metals are immobilized within the hydraulic ash-slag cementitious composites hydration products through either physical fixation, substitution, deposition or adsorption mechanisms.IntroductionDredged sludge is classified as a hazardous waste because it usually contains concentrated heavy metals and chlorinated organic compounds, as well as soluble salts, and is also composed of very fine particles. Moreover, inorganic pollutants are typically associated with soluble compounds, which are, therefore, highly leachable from dredged sludge when dredged sludge is contacted by a liquid medium[l1. Thus, dredged sludge must be stabilized in order to reduce its environmental impact on the final disposal site. The frequent means of dredged sludge disposal used include(!) Chemical stabilization (2) acidic extractionChemical stabilization is translating mobile heavy metals into low dissolution and low toxicity form through chemical reaction. The commonly chemical medicaments are sodium hydroxide, soldium sulfide, thiourea, EDTA. But Zhao et al [ZJ found sodium hydroxide is not fit for Pb stabilization, the other three are effective, but the chemical properties of sodium sulfide are not stable, thiourea and EDTA are very expensive, and so it is very difficult to apply them. Moreover, because of the complexity of heavy metal conformation and dredged sludge composition, it is very difficult to find a cheap and prevalent stabilization medicament in point[31 ."

Jan 1, 2013

By Thomas Brynjulfsen, Merete Tangstad

"Manganese ore fines, generated during mining and transportation, can not be added to the submerged arc furnace directly as they will prevent even gas flow through the burden. Low gas permeability in the burden will lower the degree of pre-reduction of ore and subsequently increase the carbon and energy consumption of the process. In order to utilize manganese ore fines in the furnace they are agglomerated into sinter, pellet or briquettes. The agglomeration process will however change the reduction properties of the ore. In this work the melting and reduction properties of sinter has been investigated.The melting temperature and melting mechanisms has been studied. The mineralogy of the raw ores and agglomerated has been found using XRD, and the composition established using EPMA(WDS). The effect of adding fluxes such as dolomite and quartz has also been investigated.IntroductionManganese metal is produced in a submerged electric arc furnace or in blast furnaces. The reduction of manganese oxide in blast furnace has in the recent years become more unusual due to the high consumption of reducing carbon material[5]. Manganese metal for alloying in steel usually contains silicon and iron, and are therefore called ferro manganese and silicomanganese.During mining, transportation and handling the manganese ore is broken up into different size fractions. The larger lump are used directly in the electric arc furnace, but the finer materials can not be added without treatment. The fine ore can disrupt the flow of CO and CO2 gas through the burden, subsequently reducing the degree of pre-reduction. The fine fractions must therefore be agglomerated into larger lumps, in order to promote gas flow. This can be achieved through a number of different processes. The agglomerate used in this work has been sintered, which means that is has been partly molten and reduced, in order to create bigger lumps."

Jan 1, 2012

By M. Rockandel

"Universal Dynamics Ltd. of Vancouver, Canada has developed, patented and commercialized the ""REMERC"" process for the treatment of mercury contaminated sludges and soils. Mercury is extracted into an acidified and oxidizing, sodium chloride brine solution. REMERC was initially developed to treat mercury contaminated EPA listed wastes (K106) generated by the chlor-alkali industry. More recent work has expanded the capability;' of REMERC to include remediation of mercury contaminated sites, equipment and building materials.In the process mercury is currently recovered from solution by cementation on iron powder in an agitated reactor. The process recovers high purity elemental mercury (99.9% purity). Cementation typically recovers about 90-95% of the mercury in 30 minutes. Higher recovery is not necessary because of the recirculation of the leach solution. When treating highly contaminated chloralkali wastes (5-13% mercury content), REMERC will reduce the mercury laden solutions from 400-1,000 mg/L mercury to 50-100 mg/L. In the treatment of less concentrated wastes «1,000 mg/kg mercury) such as those encountered in site remediation, the treated solutions will generally contain 10-20 mg/L mercury. Cementation while being simple and able to achieve the required recovery has the. undesirable properties of; requiring a solid-liquid separation and adding iron to solution which must be precipitated, ultimately increasing the weight of residue to landfill. .The potential advantages of electrolysis were recognized early in the development of REMERC. Mercury electrolysis is well known in gold and chloralkali processing. Initial testwork utilized a liquid mercury cathode and a coated titanium anode both common to chloralkali producers. The mercury cathode appeared susceptible to polarization and solution impurities significantly affected performance. Agitation of the mercury pool improved performance but it was still not possible to achieve the reduction objectives. Current efficiencies were low, near 10%, and it was apparent that a relatively large cathode pool would be required to limit the current density. A number of electrode combinations with and without a membrane were then tested in a vertical electrode' configuration but the desired performance was not obtained."

Jan 1, 1997

By Veronica Escobar

This paper presents results from a two month pilot evaluation of EMEW® technology at CODELCO Radomiro Tomic, in Chile. A prime focus in the test programme was to assess the technology?s capabilities to recover high quality copper from the Radomiro Tomic electrowinning tank house bleed stream. The EMEW® cell developed by Electrometals Technologies Ltd. tolerates substantially higher levels of contaminants than those found in conventional tankhouse, operating at high current densities while maintaining high cathode copper quality all the way down to low copper concentrations. To maintain high copper purity in a copper electrowinning (or electro-refining) tank house, a continuous bleed of solution must be taken from the tank house inventory to prevent build-up of contaminants, and resulting degradation in cathode quality. In an SX-EW operation, this bleed stream is normally recycled back to the solvent extraction circuit, but is occasionally sent to the raffinate pond to re-enter the leach circuit. Return of the bleed stream to the solvent extraction circuit creates a continually recycling load of copper in solution, which may reduce overall plant capacity and expansion potential. Return to the leach circuit has a similar effect, and methods to reduce its impact are always under consideration. The use of the EMEW® technology allows for direct and efficient recovery of near 100% of the contained copper instead of recycling. Tests were run at ambient temperature on bleed electrolyte using current densities which varied between 250 and 1100 amps per square meter, with copper concentrations between 38 and 1 g/l. A profile of maximum allowable current density with respect to concentration was developed, showing that high grade copper can be obtained at all levels of concentrations tested, by choosing an appropriate current density and electrolyte flow rate. The results of this programme show that the recirculating bleed electrolyte from an SX-EW operation can be converted into an expansion in copper production at a comparatively low investment cost.

Jan 1, 2003

By James J. Reilly

This paper recounts a history of the contribution of Dr. Gary Sandrock to the science and applications of metal hydrides from 1974 to 2006. It includes a bibliography that cites selected publications over the course these years and which constitutes an important public record.

Jan 1, 2006

By Chi Ru?an

Sollutions of ammonium chloride, nitrate and sulfate were studied in extraction of rare earths absorbed on a low-grade, kaolilnitic ore recently discovered in southern China. The results of percolation leaching tests and the recovery of the rare-earth values from these solutions are presented.

Jan 1, 1989

By Li Rongxing

A general regular solution model put forward in this paper defines a general interaction parameter that includes both composition and temperature dependence. On the basis of this model, analytic express of solution excess properties was obtained by least square fit using the composition and temperature relations in binary alloy phase diagram. After some solution excess properties analytic expresses of correlated binary alloy system obtained, the analytic express of ternary alloy system could be obtained by superposition of general geometrical model. The ternary alloy system Pb-Sn-Zn has been predicted in terms of this method and the result was very in agreement with actual measured value.

Jan 1, 2006

By M. Olper, M. Maccagni, C. J. N. Buisman, C. E. Schultz

The key point of the CX-EWS process is the conversion of lead compounds, contained in the active mass of spent batteries, into lead sulphide. The obtained lead sulphide is leached with ferric fluoborate electrolyte to dissolve lead and oxidize the sulphur from sulphide to the elemental form. The lead-rich solution is fed into a diaphragm electrolytic cell depositing lead and regenerating ferric fluoborate. The introduction of sulphate reducing bacteria technology in the sulphidization step of the battery paste improves dramatically the economics of the CXEWS process, reducing the costs of chemicals, avoiding gypsum disposal and minimising the unit operations of the process. This paper describes in detail this technology change with reference to the economics of the process.

Jan 1, 2000

By Tian Li

Molecular crystal growth during gibbsite precipitation from caustic aluminate solutions under different flow regimes was investigated in three different laboratory precipitators. The gibbsite precipitation experiments were conducted at the same temperature, initial liquor composition and seed type. The Taylor-Couette precipitator and the stirred tank precipitator were operated, respectively, under the laminar and turbulent flow regimes, while the bottle roller precipitator was operated in a complex flow regime, where fluid flows are generated by the end-over-end rotation of the bottles. Comparison of the growth rate estimates from the different flow regimes showed good agreement, which suggests that the hydrodynamic regime has little or no effect on gibbsite crystal growth under the operating conditions employed in this work. The growth rate estimates from the current precipitation study showed a second order dependency on supersaturation and is consistent with a screw dislocation growth mechanism. The findings of the current work are in agreement with previous gibbsite crystal growth studies published in the literature.

Jan 1, 2003

By M. I. Kalashnikova

The leaching of metal nickel in copper sulfate solutions is investigated. It is established, that irre-spective of presence or absence of chloride-ion and oxidizer (oxygen) in system process can be divided into three stages, characterizing by restoration and oxidation of metals with formation of metal copper and cuprite and differing in the speeds of sedimentation of copper and transition of nickel into solution. At the initial stage of process along with allocation of metal copper it is be-sieged cuprite, that results in excess of speed of sedimentation of copper in comparison with dis-solution of nickel. At the second stage speed of transition of nickel into solution falls practically to zero, and sedimentation of copper proceeds on reaction of interaction of metal copper with copper sulfate solutions with cuprite formation. During the final period speed of transition of nickel into solution exceeds speed of sedimentation of copper due to course of reaction of resto-ration of cuprite up to metal. Influence of an ion of chloride and oxidizer on formation of various phases is revealed. It is established, that presence of an oxidizer results in increase in a share of cuprite in a deposit. With increase of the maintenance of chloride-ion speed of metal copper allo-cation essentially grows even at presence of an oxidizer in system.

Jan 1, 2006

By L. Ivanova, V. Tsukerman

"Dynamics of general economic growth is to a considerable extent determined by results of research, technical and innovation policies in the Arctic zone of Russia. Evaluating contribution of innovation-technological development of the economy in growth of the country’s GDP, scholars assign 70-80% to this factor’s share.Mineral formations, accumulated during industrial epoch, affect significantly economic and ecological situation in the Arctic region. On the one hand, production wastes destroy the region’s environment. On the other hand, technogenic mineral formations contain a lot of valuable scarce components. The amount of solid wastes increases annually.Transition to innovation economy provides re-comprehension of mining enterprises in society. Actions should be directed to radical renovation of production technologies. It will ensure rapid growth of competitiveness, increased demand and stronger position at the international market. Development of innovation technologies can be provided at the expense of active state and private innovation activities.IntroductionIn northern regions it is necessary to carry to the basic organizational-economic conditions of realization of industrial innovative policy: - orientation to all-round support of the basic and improving innovations making a basis of modern technological way; - a combination of state regulation of innovative activity to effective functioning a competitive market mechanism; - assistance to development of innovative activity in region, to the international transfer of technologies and To investment cooperation, protection of interests of national innovative business. Strategy of industrial development of regions of the North, connected with transition from conceptual resource-export and export-oriented models to resource-innovative model and in the further - is innovative-technological in view of a real condition of industrial productions, realization of domestic and foreign technologies and their subsequent development is considered."

Jan 1, 2008

By Anatoly Sudnev, Vladimir Skorohodov, Igor Kudryavtsev, Boris Radionov, Dmitriy Panov

"In cobalt production technology at a stage of solutions purification manganous cake (slime) basically containing hydroxides of the specified metals is formed. The possibility of full cobalt recycling in the basic technology of metal production at slime processing with generation of pure manganous compounds is shown. After slime dissolution in sulfuric acid in the presence of reducers the solutions containing cobalt, manganese, nickel and other nonferrous metals are formed. Optimum conditions of selective precipitation major part of cobalt by sodium hydroxide from the obtained solution are defined, thus more than 95% of manganese are remained in the solution. The cobalt precipitate is directed to the basic technology and the solution is purified by sorption. The most effective sorbents are chosen, optimum modes of its use are found. Examples of manganese recovery from the purified solutions as MnO2, MnCO3, Mn(OH)2 with a ratio manganese : impurities more than 3000 are presented.In the processes of hard alloys manufacture and processing of cobalt-bearing primary raw materials various cobalt-manganous slimes are formed. After leaching by solutions of mineral acids the problem of cobalt and manganese separation becomes an actual. The common way of metals separation in a solution is the Shreyber’ alkaline method allowing rather selectively to precipitate of cobalt hydroxide by sodium hydroxide. However this way does not allow separating completely target metals because of transfer of some manganese in the hydrated precipitate, even at its rather low content.In the given work the results of researches to improvement of a traditional way by inclusion to hydrometallurgical technology of operation of sorption separation of the specified metals are presented. The main goal is definition of conditions to achievement of the complete removing cobalt at hydrolysis with the minimum sedimentation of manganese and the subsequent additional recovery of cobalt by ionites from the obtained solutions."

Jan 1, 2008

By Byung-Young Choi

Nitrogenated carbon films were deposited on the high-frequency induction hardened steels by ion beam assisted deposition. X-ray photoeleetron. spectroscopy and scanning electron microscopy were used to analyze the chemical content and the morphology of the coated steels. Rolling contact fatigue tests were performed using Polymet RCF-1 machine with a constant supply of lubricant. It was found that CNx films adherent to the steels substrates were formed by ion beam assisted deposition. It was also found in the rolling contact fatigued specimens that non-propagating crack was initiated in the white etching area indicating the maximum shear stressed, region, leading to surface failure.

Jan 1, 2000

By Robert S. Sokolowski

The future of Materials Processing in Space (MPS) in the Space Station Era is being assured today by a strong coordinated science program which looks to solve these problems, the answers to which serve to underpin the technical foundation upon which future metallurgical and materials processes will be built. The critical link between the product and process development activities that accompany this science endeavor is the "nuts and bolts" hardware that will ultimately operate in the space environment. Ground-based facilities including drop facilities and aircraft provide excellent product development and process concept study tools. Shuttle flights with Spacelab and commercially developed space facilities represent the evolutionary path to Space Station processing facilities. Today the most promising areas of MPS are crystal growth, containerless, and quasicontainerless processing. The unique features of these processes will be highlighted. Finally a more visionary perspective of MPS will be presented that incorporates the limits of today's knowledge with the economic "necessity" of tomorrow.

Jan 1, 1988

By Shunichi Ajima

PT. Smelting Co. was established in February, 1996 to construct and operate the Gresik Smelter and Refinery. The construction work of first Copper Smelter and Refinery in Indonesia was completed in the end of August, 1998 and it was put into the integrated test operation in December, 1998. Gresik Smelter and Refinery is designed to produce 200,000 tpy of copper cathode from copper concentrate supplied from Grasberg Mine of PT. Freeport Indonesia Company in Irian Jaya, Indonesia. As by product 592,000 tpy of sulfuric acid, 382,000 tpy of slag, 31,000 tpy of gypsum and 480 tpy of slime will be produced in the full operation. Major processes applied at Gresik Smelter and Refinery are: Smelter: Mitsubishi Continuous Copper Smelting and Converting Process ( Mitsubishi Process ) Anode Casting: Continuous Casting of Copper Anodes with the Hazelett Twin Belt Caster Refinery: ISA Process Acid Plant: Lurgi Mitsubishi Double Contact Process

Jan 1, 1999