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By Lary L. Speakman

Typical heavy metal removal system generate a great deal of waste that must then be discharged somewhere. Using Bio-Fix Beads developed by the Bureau of Mines in combination with other waste stream minimization processes, Harrison Western Environmental Services has developed a "zero" discharge operation. Data from current on-site operations will demonstrate the effectiveness of the Harrison Western approach. For 1992 Annual TMS meeting,: "Future Trends and Innovations" Material category Key words: Residues and Effluents Technical category Key words: Extraction and Processing.

Jan 1, 1992

By Edouard Asselin, Guikuan Yue

"In the present study, electrochemical measurements, especially cathodic potentiodynamic polarization (CPC) and cyclic potentiodynamic polarization (CPP), have been employed to study the kinetics of ferric reduction on chalcopyrite in aqueous Fe( II )-Fe(III)-H2S04 solution at 25°C and 70 °C. Results from the calculation ofspeciation in the above solution reveal that, at both 25 °C and 70 °C, the real Fe3+/Fe2+ ratio is much lower than the nominal ratio, which leads to smaller values for the reversible potential of the ferric/ferrous couple based on the Nemst equation. Exchange current densities of the ferric/ferrous couple were obtained by extrapolating the cathodic linear Tafel line to the reversible potential and are on the order of 10-7·10-6 A/cm2 at 25°C and 10·6-10-5 A/cm2 at 70 °C, respectively. The transfer coefficients were about 0.35-0.38 at 25°C and 0.35-0.45 at 70 °C. Polarization plots of CPC and CPP under different nominal Fe3+/Fe2+ ratios are in good agreement at 25 ·c and at 70 °C. Based on the obtained exchange current densities, the rate constant k, was calculated and is on the order of 10-1 cm/s at 25 °C and 10 1 cm/s at 70 °C.IntroductionChalcopyrite is the most abundant copper mineral in nature, accounting for about 70% of copper reserves in the world [I]. In recent years, the metallurgical industry has been searching for a hydrometallurgical process as an alternative to pyrometallurgical treatment due to high emissions of S02 and capital costs associated with smelting. Activity in this area has increased recently due to some inherent advantages associated with hydrometallurgical processing, such as the possibility of treating low-grade ores (increasingly more abundant in the case of copper) and easier control of waste, with the attendant benefits to the environment [I]. Chalcopyrite is highly refractory under most hydrometallurgical conditions, owing to the formation of an anodic passivation layer on the chalcopyrite surface which renders the process kinetics very slow. Most of the currently proposed processes are based on sulfuric acid with ferric ions and/or dissolved oxygen as oxidants. Sulfuric acid is preferred over all other leaching reagents in terms of cost, environmental friendliness, and ease of its regeneration during electro-winning. Some of these processes have been piloted in attempts to implement these technologies on an industrial scale,"

Jan 1, 2012

By A. C. Cascalheira, L. M. Abrantes, M. Savic

This paper reports our results on the application of a novel process for the spontaneous and sustained reduction and recovery of elemental silver and gold on an electroactive polymer surface. This work incorporates the metal recovery from photographic films (silver) and goldsmith residues (gold), by direct contact of metal containing solutions with polymer. The performance on such process of electrochemically and chemically prepared polyaniline (P ANI) is evaluated. SEM coupled with EDX and XRD analyses confirmed the presence of metallic silver and gold deposited onto polymeric material.

Jan 1, 2000

By Jay Black

In the thiosulfate gold leaching process gold is oxidized to Au+ by a copper(II) ammine catalyst and complexed by thiosulfate. Copper(I) complexes, formed during gold oxidation, are reoxidised to Cu(II) complexes by oxygen. In this study, we present the results of a spectrophotometric study of the Cu(I)-NH3-Cl system, which follows on from our recent investigations of speciation in the Cu(I)-Cl and Cu(I)-S2O3-Cl systems and is part of a detailed study of copper(I) speciation associated with the gold leaching process. Formation constants for Cu(I)-NH3-Cl complexes have been determined by modeling the systematic changes in the UV spectra that occur as the concentration of the components is varied. The analysis of the data indicates that three Cu(I)-ammonia complexes are present, i.e., [Cu(NH3)2]+, [Cu(NH3)Cl2]- and [Cu(NH3)2Cl] and their respective log Kf values are 11.13, 8.33 and 10.79 at 25°C. Investigations of the oxidation of Cu(I)-NH3-Cl solutions by oxygen in the atmosphere are also presented. These experiments indicate that the reaction of copper(I) complexes progresses through various intermediates. The presence of many copper(I) and copper(II) complexes in ammonia thiosulfate solutions complicates the task of determining optimal conditions for gold leaching. Further studies are needed to identify the complexes and chemical processes that are important in the Cu(I)-NH3-S2O3-Cl system.

Jan 1, 2003

By Anders Salwén

In 1975 T. Nishizawa and A. Chiba reported on observed deviations from the ferrite-austenite local equilibrium in several diffusion couples based on the Fe-Cr system. In order to try to verify these results the austenite-to-ferrite transfonnation in a Fe-20 %Cr-Invalid Code [Fe-]-%Cr diffusion couple held at 1100 for 100 hours has been simulated. The simulation model is based on the postulated principle of maximum dissipation rate of Gibbs energy during transformation, which allows non-equilibrium interface conditions. Keynotes: Computer Simulation, Austenite-to-Ferrite Transfonnation, Diffusion Couple

Jan 1, 2003

By N. A. McKay, J. G. Davison

"Heap leachable ore deposits from many countries have been submitted for process mineralogical evaluation and laboratory testwork. Numerous factors must be addressed and integrated by the mineralogist, geologist, metallurgist and engineer. Projects encompass grass roots exploration, preliminary petrographic analysis, predictive and process mineralogy, dye penetration analysis of rocks and thin sections, metallurgical beneficiation testwork and plant optimization studies. The significance of mineralogical factors, such as geological controls, degree of oxidation, dye amenability, liberation, deleterious minerals, refractoriness, and the impact of mineralogy on gold recovery and process considerations, will be presented.ABSTRACT ONLY"

Jan 1, 1997

By M. Cloete, C. MacLagan, A. Newall

This paper initially gives a brief overview of Zinc Corporation of South Africa Limited (Zincor). The original design parameters of the Zincor roasters are compared to the current operation, and the requirements for efficient roasting are listed. Roaster operational problems experienced during the early to mid 1990's are outlined. A description of the investigation and the outcome to increase overall roaster availability are given. The history and the development of the use of oxygen at the Zincor roaster operation, with an account of the associated operational experiences, are explained.

Jan 1, 2000

By Zbigniew Smieszek, Ryszard Chamer, Ryszard Prajsnar, Zygmunt Kurek

"Lead-containing wastes processed at the IMN’s Division in Legnica originate mainly from dry and wet dedusting installations of the technological lines for copper production. These are lead dusts and lead-zinc dusts characterised by the specific properties resulting from the chemical composition of the Polish copper concentrates. Besides lead, they contain many accompanying metals and impurities such as zinc, copper, sulfur, chlorine, potassium, sodium, and also bituminous substances. Processing of lead-containing dusts is conducted in the installations of rotary-rocking furnaces heated with gas-oxygen burners fitted with auxiliary systems for cleaning process gases and refining re-circulating dusts. The processing technology utilizes innovative process and technical solutions enabling disposal of lead-containing wastes from copper metallurgy and from non-ferrous metals industry according to the BAT recommendations and to the guidelines specified in integrated permission. In this paper, the main technological aspects of processing lead-containing dusts at the IMN’s Division in Legnica have been presented.IntroductionCrude lead is obtained in Polish lead metallurgy from various primary and secondary materials, such as Zn-Pb concentrates, lead-bearing dusts of copper metallurgy and battery scrap. In zinc smelter Miasteczko Slaskie S.A. crude lead is produced from sulfide and oxide Pb-Zn concentrates in ISP process. Orzel Bialy S.A. and Baterpol Ltd. produce crude lead in short rotary furnaces in the process of smelting products of mechanical battery scrap separation– desulfurised or not desulfurised paste and metallic fraction. KGHM Polska Miedz S.A. and IMN Divison in Legnica produce crude lead in rotary furnaces in the process of smelting of polymetallic dusts and slimes from copper production processes."

Jan 1, 2008

By John Jiang, Yeonuk Choi, Olivia Wang, Gus Van Weert

"As part of a general review of processing double refractory ores through Barrick Gold's autoclaves/CIL facility at Goldstrike, Nevada, blanking the gold cyanide adsorbing native carbon in the ore with hard (m.p. >55°C) paraffin wax was proposed. To avoid interference from other ore constituents in the exploratory testwork, commercial activated carbon was substituted for native carbon in the ore to establish the best conditions for de-activation of carbon with molten wax.IntroductionDouble refractory gold ores present two barriers to gold extraction. The first is generally a physical barrier: the gold is encapsulated or dispersed in a matrix which is impervious to the gold lixiviant. In most cases, including the Goldstrike deposit, this involves a pyrite or arsenopyrite matrix, although minor gold may also be dispersed in competent silica (quartz) or iron oxides. Gold can be rendered accessible by oxidative destruction of such sulphide matrices. At Goldstrike this is practised by roasting and autoclave oxidation (POX). It is the latter route to which this paper refers.The second barrier refers more correctly to gold recovery. Gold may be extracted from the autoclave oxidized solids with cyanide, forming a gold cyanide complex. One characteristic of this complex is that it adsorbs on graphitic surfaces. This behaviour is used advantageously on a large scale by gold millers, who use man made activated carbon particles to remove the gold from solution during leaching: the Carbon-In-Leach, or CIL process. The gold bearing carbon particles are larger than the ore solids and can be separately recovered by screening. Goldstrike uses the CIL technology to recover gold after autoclave oxidation."

Jan 1, 2012

By Matthew Tunnicliffe, Akram Alfantazi, Paul Nesbitt, Farzad Mohammadi

"Lead and its alloys are proper candidates for anodes in electrowinning processes mainly because they are insoluble in the leach solutions and relatively cheap. However, the annual cost of corrosion problems associated with these anodes is millions of dollars. In this study lead-silver and lead-calcium anodes were tested under typical nickel electrowinning conditions and the effect of chloride on the corrosion performance of the anode materials was investigated. Corrosion rates of the anodes were calculated using the discharge plateau (reduction of lead dioxide to lead sulfate) after galvanostatic experiments. It was found that lead calcium anodes have the highest corrosion rate both in the presence and absence of chloride. Surface morphology of the electrodes was studied using SEM and the corrosion products were characterized using XRD.IntroductionLead (Pb) is usually the preferred material for commercial anodes since it is insoluble in the leach solution and the costs are manageable. One advantage of using an insoluble material as an anode is the higher purity of the cathodic deposits and better quality of the end product. During nickel electrowinning, metallic nickel is deposited on the cathode while oxygen evolution reaction (OER) takes place on the anode. In practice, relatively high potentials are necessary for the reaction to proceed at the desired rate because of the high overpotential of OER on lead. Lead anodes get oxidized in typical electrowinning conditions and usually have two to three years of lifetime. Although the price of each anode is insignificant, the overall cost of corrosion of these anodes is considerable, which is due to the large number of anodes used in a plant, typically two to three thousand. Therefore, corrosion is a significant problem associated with lead anodes in commercial nickel electrowinning plants and industries show interest in addressing this problem. Corrosion of lead electrodes in acidic environments has been previously the subject of many research studies [I-7]. It has been reported that, during the anodic polarization of lead, several phases may be present on the surface, depending on the potential range that is being studied [8]. Lander showed that lead is oxidized at potentials higher than 0.252 YsHE with tetragonal lead monoxide being the main reaction product [9]. At 0.666 YsHE lead can transform to lead dioxide; however, it is not stable and transforms to lead sulfate and lead oxide. At potentials higher than 1.684 YsHE, lead dioxide is eventually a stable phase and forms a protective layer on the surface [I 0, 11]. Under conditions of a typical nickel electrowinning plant, usually a 200 A/m2 current density is passed through the electrodes."

Jan 1, 2012

By D. G. C. Robertson

Counter-current staged reactors offer several advantages over batch reactors for mass transfer between two phases. Several metallurgical reactor designs have utilized the counter-current principle, e.g. the WORCA and QSL processes. But before the principle can be widely adopted, it will be necessary to overcome several significant problems. These include the need to minimize longitudinal mixing in a single reactor or to use several separate staged reactors and to carry out different reactions in sequence, e.g. phosphorus oxidation and sulfur reduction. Theoretical and experimental approaches to these problems will be discussed in the paper.

Jan 1, 1988

By A. I. Okunev

The investigation results are submitted on separation into layers in the systems Cu (Ni) - Fe - Ca - 0 - S - (Si), as well as on physico-chemical properties of oxide - ferrite, oxide-sulfide melts (density, surface tention, viscosity, electric conductivity), on kinetics and oxidation macromechanism of iron and sulfur in the oxide-silicate, oxide-ferrite and oxide-sulfide melts, kinetics of reduction of oxide-silicate and oxide-ferrite systems. Conditions are discussed for copper, nickel and zinc recovery from oxide-silicate and oxide-ferrite slag in liquid and solid states. Some promising technique is the technique of future, as is considered.

Jan 1, 1988

By C. Hecker, J. A. Garcia

To determine the kinetic reaction mechanism, electrochemical experimental techniques of stationary polarization, linear voltammetry and faradaic impedance were used. Gold electrodeposition experiments were realized using an electrolysis cell, provided· by a rotary disk of vitreous carbon and or' platinum counter electrode of platinum mesh and reference electrode. Using an automatic measurement system voltarnmograrns and Nyquist faradaic impedance spectra were obtained. In this paper, responses for different cases were analyzed through faradaic impedance criteria, considering several kinds of diagrams obtained. The importance diffusion influence of aurocyanide ions and adsorption as controlling steps previous charge transfer was verified. A model of proposed mechanism is discussed.

Jan 1, 1997

By M. Benavides

An experimental study is carried out With sulphide ore obtained from Bailadores-Venezuela as well as artificial concentrates. Concentrates of the minerals from froth flotation are fused to study equilibrium between the matte and slag phases. The first part of the work deals with obtaining a concentrate by flotation experiments with collective and selective reagents, with acceptable metallurgical recovery, studying the influence of different parameters in the process. The second part gives the results of the experimental investigation. on thermodynamic equilibrium in smelting which facilitates knowledge of the elemental processes, giving bases for the possibilities of reducing the loss of metal in slag.

Jan 1, 1983

By James P. Bennen

Limited efforts have been made to recycle/reuse-spent refractory materials in the steel and aluminum industries of North America. The driving force is usually part of a larger waste reduction program. -Economic or legislative forces have not been a driving force for spent refractory recycling/reuse. Past and current spent refractory recycling / reuse practices will be reviewed, with emphasis on specific programs at steel and aluminum companies. Program goals and progress of the joint Office of Industrial Technologies-DOE/Steel Manufacturers Association program directed at spent refractory reuse with electric arc furnace steel producers will also be discussed.

Jan 1, 2000

By Myung Bae Kim, Yong Hack Lee, Woll Seung Lee

The Slag Fumer is the first Ausmelt furnace system adopted at the Onsan Refinery of Korea Zinc. This plant continuously treats the QSL lead smelting slag in the molten state. It has developed progressively since its first commissioning in October 1992 and has generated a confidence that it can produce an environmentally acceptable slag for use in cement manufacture and recover the zinc and lead in the slag as a fume oxide. This paper provides the operating experiences accumulated during the last eight years of operation, a summary of problems and solutions, and the current status of the operation.

Jan 1, 2000

By P. R. Seidl, R. C. C. Ribeiro, J. C. G. Correia

"More than 95% of asphalt pavement materials consist of aggregates. The highway and construction industries consume a huge amount of aggregates annually causing considerable energy and environmental losses. The aggregates are usually produced from neighborhood aggregate quarries or form natural aggregate sources. The use of marble and granite wastes from quarries as aggregates might help meet the increasing demands and slow down any detrimental effects on the environment. Chemical and physical results showed that the use of marble and granite wastes from quarries in the asphalt production is quite fusible. Consequently, granite sawmills would perform a clean technology. This technology would also have an economical impact by not spending on basalt extraction.IntroductionThe granite fines generated from sawmills of ornamental rocks comes as a great problem and it lacks undeletable solutions. This problem involves the preservation of the environmental and constitutes one of the subjects more critical the point of view of social beneficiation of the population. The Cachoeiro de Itapemirim County, Espírito Santo State, Brazil is an example, of this problem. In this area, the granite and marble fines generation is around 15.000 ton/year.The problems generated by these residues affect with more emphasis the animals, such as the cattle, which inhaled the water content fines of granite and this residue accumulate in their lungs. Other great problem observed is the sanded of the river and the reduction of aquatic life.This problem is beginning to be set out due to performance of Center of Mineral Technology (CETEM), and of several other organisms of Rio de Janeiro State, aiding the sawmills owner’s. This help consists of teaching the best procedure of discard the residues and studies for its use, for instance the production of mortars, tiles, bricks and road pavements [1]."

Jan 1, 2008

Environmental and public concerns and the banned use of cyanide for the recovery of gold in some parts of the world have heightened the search for an alternative lixiviant to cyanide. Thiosulfate appears to be the most promising alternative to cyanide due to thiosulfate being non-toxic, relatively cheap compared to cyanide and generally gold recoveries are similar to those of cyanide. The most widely researched thiosulfate process is one where copper ions and ammonia are added to the solution. This paper reviews the leaching of gold in thiosulfate solutions and the contributions of the research at Monash University to the understanding of the gold oxidation reaction in thiosulfate solutions, the solution chemistry when copper ions, ammonia and oxygen are present, the influence of the changing solution chemistry on the gold leach kinetics, and the application of thiosulfate in the leaching of gold from ores. It is clearly shown that the gold oxidation rate is hindered in thiosulfate solutions. In the presence of copper ions the gold oxidation rate though is significantly enhanced and thus is why copper(II) is more effective than other oxidants in the thiosulfate leach system. The copper-ammonia-thiosulfate leach solution chemistry is shown to be very complex, especially in the presence of oxygen as the rate of thiosulfate oxidation increases and the majority of the copper ions are not maintained in the copper(II) oxidation state. The thiosulfate oxidation rate must also be maintained low as an intermediate thiosulfate oxidation product hinders gold leaching. In optimising the recovery of gold from ores with copper-ammonia-thiosulfate leach solutions it is important to evaluate and minimise any negative effect an ore may have on the leach solution chemistry and hence gold leaching.

Jan 1, 2003

By Tarek M. Abd El Hamid, Suzane Ali

"Treatment of industrial waste materials is created serious problem in Egypt. Aluminium sludge is generated as a by-product from aluminium household industry which contains significantly high alumina content exceeding 90%. This by-product randomly disposed and creates serious environment problems to locate community. To develop the treatment process of this material, the recovery of high purity alumina and identify the potential application is being the primary objective, This paper represents the recovery process of alumina process waste sludge High purity alumina material <99.8% aluminium oxide with originate particle size 0.125-0.420mm and apparent density 0.39g/cm3 was obtained with a specific surface area 139m2/g. Alumina produced was modified by cerium oxide doped alumina. The catalytic activity and selectivity was investigated in conversion of iso-propanol via dehydrogenation reaction yielding only acetone indicating an excellent selectivity the dehydrogenation. The presence of 10% CeO2 increase in the catalytic activity of 82% for the originated alumina. Introduction Approximately 20 thousand tons of aluminium waste produced in Egypt in 2006 with increasing amounts expected in succeeding years. A part of this waste contains organics impurities which coexisted with aluminium waste as a result of manufacture final aluminium products, waste usually content <1 to 2 wt% of organic carbon. It's generally admitted that the organic species are present in the form of lubricant oils used in rolling and pressing equipments for aluminium sheet. Both industry and government face possible high-cost disposal problems that more magnified by large volume of waste produced. The alumina recovery leachable study conduct in this paper had the following objectives: 1- Develop a process that can provide an environmentally acceptable residue and also recover the available alumina. 2- Evaluate the alumina produced in terms of grade and catalytic application."

Jan 1, 2008

By Takahiko Okura

"It is said that the energy and resources crisis will come before long because the lifetime of known deposits of crude oil and common metals such as Pb, Zn, Cu is estimated to be less than 50 years. Establishing the sustainable society by means of resources-recycling has become an absolute necessity.The non-ferrous metals industry in Japan has been involved in the resource- recycling business for many years, along with the introduction and enforcement of various legislations to preserve the environment and natural resources. Including process-linkage during various manufacturing activities, the non-ferrous metals industry, the iron-making and cement industries are treating considerable amounts of recycled materials and wastes, in an environmentally-sound and economic manner.The Mining and Materials Processing Institute of Japan has submitted “The present and issues in Japanese non-ferrous metals and recycling industries.”The topic of the paper is to highlight the actual conditions within the resources-recycling structures and the present issues.IntroductionGlobalization has been changing the world, introducing the spike of energy and metals price. In addition, the preservation of the environment has also been strongly facing the crisis and many people have been aggrieved by both shortage and the increment in the price of the meals.In the world of metals, even though their reserves are coming depleted, the production rates are increasing, and then the industry has to enhance their productivity under stricter environmental regulations. The Japanese industry experimented the same scenario some 40 years ago, facing big pollution problems, but concurred them and enhanced the technology to overcome the more severe regulations. It will be fruitful to present the current situation in the Japanese industry for the world. The present issues are also presented."

Jan 1, 2008