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By Sidiney Nascimento Silva

Em parceria com a UniSoma, empresa especializada em soluções analíticas baseadas em otimização, a CSN desenvolveu e implantou uma solução sob medida para o planejamento de sua cadeia de redutores. A solução é composta por dois módulos básicos - Embarque® e MIX®, que dão suporte às decisões de caráter tático-operacional relativas à cadeia de abastecimento de combustíveis sólidos, abrangendo desde a aquisição das matérias-primas até o seu consumo nos vários processos siderúrgicos -coqueria, altos-fornos e sinterização. O Módulo Embarque®, tático, possui uma “inteligência computacional”, na forma de um modelo matemático, que trata, de forma integrada, três subproblemas correlacionados: a programação do abastecimento, o planejamento de mistura e de produção, dos vários processos, e o planejamento de estocagem ao longo do tempo. O modelo fornece soluções de compromisso entre os objetivos de custo e qualidade. O Módulo MIX®, otimizador operacional, é usado para definir a programação das misturas a serem realizadas no curto prazo. O trabalho apresenta não apenas os aspectos técnicos da solução, mas também os desafios enfrentados durante a sua implantação e os resultados percebidos com a sua utilização.

Aug 1, 2018

By Sung-Hyun Park

Core sediment samples collected from the KODOS area of the Clarion-Clipperton Fracture Zone in the NE Equatorial Pacific were analyzed for chemical and mineralogical compositions to investigate the depth- and time-related variation of paleoenvironmental and paleoceanographic conditions during their deposition. These core sediments are divided into three layers from top to bottom by its color; 1) brown layer (Unit I), 2) pale brown layer (Unit II), and 3) black brown layer (Unit III). Geochronology of 10Be indicated the depositional age of Quaternary for Units I and II and of late Pliocene for Unit III with a potential short hiatus between them. Analyses of interelemental correlation identified three major groups of elemental groups that show moderate-to-strong correlations: 1) Al, Ti, K, and Fe representing for terrestrial alumino-silicate fraction of sediments, 2) Ca, P, REEs, Cu, and Zn for biogenic apatite, and 3) Mn, Ni, and Co for hydrogenous Mn-oxide. With an exception, Fe content was very high and showed fair correlations with Mn, Ni, and Co in Unit III. Unit III shows high smectite but low quartz and illite contents compared to the overlying two units, indicative of reduced supply of terrestrial materials. In a meanwhile, major elements (Fe2O3, CaO, P2O5), minor elements (Cu, Zn) and REEs are highly enriched in Unit III compared to the upper two units. All these elements other than Fe reflect the fraction of biogenic apatite, which indicates higher fraction of biogenic components in Unit III. This is also supported by higher amount of smectite formed by the consumption of siliceous biogenic components. The reduced supply of terrestrial material and/or increased productivity of surface water at the time of Unit III deposition are attributed to Pliocene warming preceding Northern-pole glaciation during Quaternary. Unit III also includes clinoptilolite and unidentified 8Å mineral, likely amphibole, that are absent in Units I and II, suggestive of the possibility of different source region and/or materials during Pliocene. Higher contents of Mn and Fe in Unit III are likely due to the high fraction of Mn-oxide that was formed by diagenetic process after deposition.

Jan 1, 2003

By Sábata Marla Reis Durães Oliveira

Este trabalho tem como objetivo o uso de modelos termodinâmicos da literatura e termodinâmica computacional no estudo de dessulfuração de ferro-gusa através de misturas CaO-Fluorita e CaO-Sodalita. As experiências foram realizadas com a adição de diferentes misturas destes sistemas em ferro-gusa a uma temperatura de 1400°C. Os resultados dos testes foram analisados e comparados com os obtidos pelos modelos termodinâmicos da literatura e o software de termodinâmica computacional ThermoCalc. Através dos modelos da literatura foram calculados basicidade óptica, capacidade de sulfeto (Cs) e partição de enxofre (Ls). Pelo software ThermoCalc foram calculados o teor de enxofre de equilíbrio no metal, fases sólidas, e a quantidade de líquido em cada uma das misturas dessulfurantes utilizadas no processo a uma temperatura de 1.400ºC. O ThermoCalc mostrou-se mais preciso que os modelo da literatura na análise da capacidade de dessulfuração das misturas utilizadas neste trabalho.

Aug 16, 2017

By Józef Czernecki

Chalcocite-bornite concentrates of KGHM contain, similarly to chalcopyrite concentrates, 20-30 wt.% Cu but several times less iron (2-7 wt.%) and sulphur (9-12 wt.%). Another useful characteristic of KGHM concentrates is the presence of organic carbon (5.5-8.5 wt.%) in them, which serves as fuel in the flash smelting process. The main contaminants of the concentrates are lead (1.3-2.5 wt.%) and arsenic (0.05-0.4 wt.%) which require appropriate technological treatment in order to remove them from the copper pro-duct. Chalcocite-bornite concentrates are processed in KGHM by two different processes: ? a flash smelting process (Glogow 2 Smelter) ? a shaft smelting process (Glogow 1 Smelter, Legnica Smelter) The shaft smelting process used in the Glogow 1 Smelter and in the Legnica Smelter has higher production costs than the flash smelting process of HM Glogow 2. Additionally, the shaft smelting process employs several concurrently running installations (six dryers, seven briquetting lines, six shaft furnaces, nine converters), the operation of which, including maintenance, requires significant financial expenditure. Therefore, the Company is currently considering the substitution of the shaft furnace process in the Glogow 1 Smelter and in the Legnica Smelter by the one stage flash smelting process located in the Glogow Smelter, with output equaling the copper production capacity of both smelters, i.e. 320 000 ? 350 000 t/a. There are two technological options being considered which differ from each other in their man-ner of flash slag cleaning. In the first, the slag cleaning would be the same as in the existing Glogow 2 Smelter, i.e. the slag would be cleaned by pyrometallurgical reduction of the oxide copper and other metal compounds in the electric furnace in order to produce waste slag containing below 0.6 wt.% Cu. However, the other option of the flash slag cleaning would be carried out in two stages. After preliminary slag reduction in the electric furnace to 3-5 wt.% Cu, there would be flotation of the partially reduced slag.

Jan 1, 2006

By Lívia Lopes de Oliveira Goulart

Visando garantir o nível de qualidade dos produtos e o controle do processamento do aço para atender aos requisitos dos clientes e das normas técnicas aplicáveis e manter-se competitivo no mercado de aços longos com redução contínua de custos, um dos grandes desafios das aciarias elétricas é promover o aumento do rendimento de suas ferro-ligas melhorando ao mesmo tempo os processos de desoxidação e dessulfuração, além da limpeza interna do banho. Este trabalho teve como objetivo avaliar o efeito da adição de carbureto de cálcio durante o vazamento das corridas do aço 1026-D nestas variáveis, através da análise estatística e termodinâmica de dados de corridas experimentais, com e sem adição de carbureto de cálcio. Foi demonstrado que a adição desse insumo melhora de forma significativa os parâmetros metalúrgicos de qualidade do material e reduz o custo de transformação para a fabricação desse produto através da redução do consumo de ferro-ligas.

Aug 16, 2017

By N. Dahata

B206 aluminum?copper alloy has a potential for wider use in the automotive industry due to its light weight and relatively superior mechanical properties as compared to aluminum-silicon alloys. The possibility of casting this alloy via Lost Foam Casting (LFC) has not been investigated in detail. Therefore, the effects of foam types (T170B standard untreated EPS and T175-brominated EPS), coating types (Styro Shield 5553 and Styro Shield 5554), copper level (4.5 wt % and 5.0 wt %) and titanium levels (0.5 wt % and 0.25 wt %) were related to fillability, microstructure and microporosity. The metal velocity in T175 EPS pattern was higher than that in T170B EPS pattern. For T175 EPS pattern, the total solidification time was 3% higher and the loss of temperature for decomposition of EPS was lower than those in the case of T170B EPS pattern. The grain size, porosity level and maximum pore size were quantified using Light Optical Microscopy (LOM) and image analysis. The casting with T175 EPS pattern showed larger grain size relative to that with T170B EPS pattern. The porosity level and the maximum pore size decreased significantly when the titanium level was increased from 0.05 wt % to 0.25 wt %.

Jan 1, 2007

By Ramon Fraga Resende

O distribuidor é o último equipamento revestido de refratários em contato com aço líquido e que pode afetar a qualidade do produto. Nesse equipamento, a massa de trabalho é responsável por proteger o revestimento de segurança e evitar a contaminação do aço. Apesar das preocupações em relação ao “pick up” de hidrogênio e consumo de gás, as massas “spray” tem sido uma tecnologia dominante para o revestimento de distribuidor na América do Sul. Nos últimos 20 anos, outras tecnologias entraram no mercado com o objetivo de reduzir a necessidade de água e de gás e aumentar a disponibilidade de distribuidor. Embora essas tecnologias apresentem algumas vantagens, quase 80% das usinas siderúrgicas da América do Sul ainda usam massas “spray”. Isso se deve principalmente aos benefícios como flexibilidade, baixo custo, baixo consumo e alto isolamento térmico. Este trabalho tem o objetivo de discutir as principais vantagens e desvantagens das massas disponíveis no mercado.

Oct 30, 2017

By D. C. Hilty

C. E. SIMS*—This is a most interesting and important paper. It is important from two standpoints. First, it has as-spects of being highly accurate and therefore extremely useful to the operating man in showing how far he can go in oxidizing carbon from a steel bath while retaining chromium and the effect of temperature on this limit. Fig 5 is undoubtedly the highlight of the paper, and in checking it against available data, it seems capable of predicting actual results. The other important aspect is the apparently significant fact that reactions within a steel bath, such as between carbon and an oxide, are homogeneous reactions which do not require equilibrium with an external phase. In this case, it seems obvious that the reaction and the equilibrium established were between dissolved carbon (or carbide) and dissolved CrO. The classic reaction which requires equilibrium with solid Cr2O3, did not fit the data. It was recognition of this principle that made Fig 5 possible. G. R. FITTERER*—It might be in assuming the CrO is dissolved in the metal that you are actually approaching the correct factor for activity. If that is true and if the percentages that were used represent an equilibrium constant, this would mean, in effect, that the minimum temperature at which chromium would be reduced by an equivalent percentage of carbon would be about 2400°F from your equation. I believe that is in line with my experience particularly if you deal only with low percentages. J. CHIPMAN†—The author in discussing the equilibrium of the reaction offers two choices of explanation. One postulates an effect of chromium on the activity coefficient of carbon; it would require perhaps more data than are available to us at the present time to test this thoroughly. The other postulate which he offers is a reaction with CrO. This explanation is consistent with physical and chemical principles provided that a solid phase CrO is present, and that is essentially what he is postulating. If that oxide were present one would expect and, I think, almost require the kind of results that he obtained. The weakness of that postulate lies in the lack of confirmatory evidence regarding the presence of solid CrO as such. This should offer an interesting subject for further study. It seems a pity that the theoretical arguments revolving around CrO should have obscured for a moment the very real excellence of this paper. E. CARTER*—I think there is a problem that presents itself in practical application where the metal temperature is from 3200 to 3300 and the temperature desired in pouring is considerably less. B. M. LARSEN†—I get the impression from some of the work that was done earlier that there is probably a localized zone of high temperature at the slag metal interface which effects the removal of the carbon. Without that I wonder if the effect is possible to have a localized superheat and an equilibrium there favorable to low carbon content and

Jan 1, 1950

By P. Greenfield, C. C. Smith, A. M. Taylor

J. E. Harris (Berkeley Nucclear Laboratories, England)—Greenfield et al.11 attribute abrupt changes in slope of their log o/log i curves for heat-treated Mg/0.5 pet Zr alloy (zA) to &apos;atmosphere&apos; locking. It is proposed here that a more reasonable explanation of the apparent strengthening at low rates of strain can be based on precipitation either during the preanneal or during the creep tests. All the tests were carried out above 0.5 Tm where solute atmospheres are likely to be largely evaporated2 and can migrate sufficiently rapidly so as not to impose any &apos;drag&apos; on the moving dislocations. McLean3 has derived an expression for determining the temperature Tc above which, due to the high-migration rate of the atmospheres, Cottrell or Suzuki locking can play no part in determining creep strength. This expression, which holds for an applied shear stress of not greater than 5 X 107 dynes per sq cm is: Tc/Tm= 7/6.8 - log10? where i = secondary creep rate The values for T, corresponding to the maximum and minimum reported creep rates at each temperature have been calculated from the data of Greenfield et al. These are given in Table VII. All the test temperatures were above T,, the margin being greater for the higher temperatures and for the lower strain rates where the breaks in the log s/log ? curves occurred. Dorn and his collaborators14, 17 have studied systematically the effect of solute hardening on the creep properties of an A1/3.2 at. pet Mg alloy. In the temperature range where strain aging occurred in tensile tests, abnormally high-activation energies for secondary creep were obtained but at temperatures above 0.43 Tm, solute alloying did not have any effect on the creep parameters. Moreover, there have been no reports of any strain aging phenomenon during elevated temperature tensile tests with ZA material.18 Instead of the observed strengthening being due to atmosphere locking, it is now proposed that precipitates play an important role in enhancing the creep strength of the material. There are two possibilities—precipitation of zirconium hydride during the high-temperature preanneal and/or precipitation of the hydride or a-zirconium during creep. On the basis of the former the results can be interpreted in terms of a critical stress being necessary to force the dislocations through or over preexisting precipitates. From the latter, if the strengthening is due to pre- cipitation during the test then hardening should be associated with a critical strain rate. At low rates of strain, time is available during the tests for precipitation to occur either directly onto dislocations (thus pinning them) or generally throughout the matrix (which would impede dislocation movements). Examination of the data of Greenfield et al. suggests that both mechanisms may be operative since they observed precipitation during creep and also found that their alloys exhibited high-creep strength in the early stages of the low-stress tests, i.e., before creep-induced precipitation had time to occur. It is not easy to understand why they considered that precipitation of zirconium hydride is unlikely to occur at 600°C while it can take place in tests in air at as low a temperature as 200°C. Precipitation of the hydride during the preanneal cannot be ruled out merely on the basis of metallographic examination. Hydride precipitates in ZA type alloys are very small and can only be accurately resolved in the electron microscope.9 For example, in this laboratory20 hydride platelets with major dimensions <(1/10) µ have been observed by electron transmission through thin film specimens of hy-drogenated ZA material. Complex interactions between dislocations and such particles are illustrated in Fig. 12. Additional evidence for precipitation during pre-annealing is provided by the data presented in Greenfield&apos;s Fig. 1 and Table IT. These show that the creep strength at 200o and 400°C increases with the time of preanneal at 600°C. Such increases cannot be explained on the basis of increases in grain size alone for further improvements in strength were observed when the material was annealed for longer times than that required to stabilize the grains. Although the main discussion is confined to ZA material, similar arguments can be used against the strain aging hypothesis proposed to explain the binary Mg/Mn alloy data. In this case no precipitation is possible during the preanneal, but precipitation-hardening during creep can occur.

Jan 1, 1962

By Frank J. Skudrzyk, Vladimir F. Petrov

In compliance with the current Russian environmental legis­lation, possible impact of industrial activities on the environment is restricted by acceptable limiting values (maximal allowable concentrations - MAC) of individual chemical substances in the natural environment - water, atmospheric air and soils. These norms have federal status and are valid for the whole territory of Russia. Disposal of the substances, for which no MAC is estab­lished, is forbidden by the law. Many gold mining companies use cyanide in precious metal recovery. This paper overviews the Russian experience in pro­tection of natural water reservoirs from technogenic impact of cyanic technologies. Major toxic compounds, contained in liquid and solid rejects from hydrometallurgical treatment of gold ore using cyanidation, are cyanides (CN), thiocyanates (SCN) and cyanide metal com­plexes. Unlike western classification of various cyanide types, in Russia any inorganic cyanide compounds (simple and in com­plexes with metals), with the exception of iron cyanide com­plexes, are considered toxic and the acceptable limiting value is established for them. MAC is 0.05 mg/I for fish reservoirs and 0.1 mg/I for drinking water. For iron cyanide complexes MAC is 0.15 mg/I for fish reservoirs and 0.25 mg/I for drinking water. Russian norms for thiocyanates are practically as rigid - the acceptable limiting value for them in fish reservoirs is at the level of 0.07mg/l (0.15 mg/I for potassium thiocyanate) and for drinking water - O. lmg/1. Norms for metals are established on the basis of total content regardless of the form in which they are present in water - as cations or complex ions. It should be noted, that in case several toxic compounds of the same limiting value (for cyanides, thiocyanates and base metals the limiting value is toxicological) are present in water. Their allowable concentra­tion is calculated as the sum of actual concentration of each com­pound, divided by the corresponding acceptable limiting value, with the result not to exceed one (compounding effect). Differences in cyanide classification and the necessity to include thiocyanates dictate different analytical methods. This, in a number of cases, results in certain discrepancies in analytical results. Until recently chlorination was used as a basic process of detox­ification of wastewaters. Calcium hypochlorite powder or hypochlorite pulp, prepared of lime milk and chlorine shipped to the plant, were used as a reagent. Chlorination is an efficient method: it allows to completely destroy plain and complex cyanide, in addition to iron complexes, and thiocyanates. A good example of high efficiency chlorination can be found at the Mnogovershinniy mill near the Okhotsk Sea located in the salmon spawning area, for which we designed an automated chlorination plant for tailings dam. Since plant start-up ten years ago, the required concentrations of cyanides and thiocyanates have been kept at the MAC level required by environmental regulatory agen­cies and no harmful affects on ichthyofauna has been reported. One major drawback of chlorination is high cost of the major reagent, as well as secondary contamination of detoxified waters by chlorides. Secondary contamination by chlorides becomes obvious in the course of detoxification of wastewaters of com­plex composition, which require increased reagent consumption. Recent changes in economic conditions in Russia caused the necessity to direct efforts to reduce the costs of precious metals recovery, and in particular, wastewater treatment. We have con­ducted certain work in this direction and obtained positive results. We hope that our experience described below will be of interest to other specialists particularly taking into account the current low gold prices.

Jan 1, 1998

By Daniel Augusto Ferro

Devido crescente necessidade de elevação dos níveis de conformação em peças estampadas, existe uma demanda cada vez maior em ligas e processos diversificados que atendam as variadas exigências do setor de produtos estampados e posteriormente tratados termicamente para aumento de dureza. Desse modo desenvolveu-se a liga C80M (modificada), que é uma variante da liga C80U especificada na norma DIN EN ISO 4957 porém com adição de Cromo, entretanto a liga C80M ainda é pouco estudada e pouca informação técnica se tem a seu respeito. Com a finalidade de melhor conhecimento técnico dessa liga, foram conduzidos estudos de caracterização em amostras laminadas a quente e após processo de esferoidização posteriormente sendo revestidas com fosfato de zinco. Foram realizados estudos de composição química, microestrutura e propriedades mecânicas, além de levantamento da curva CLC através do método Nakazima em amostras com e sem revestimento de fosfato. Através dos resultados parciais encontrados, foi possível definir o lado da curva CLC relacionado ao estiramento da chapa bem como comparar o deslocamento e a força do punção no teste Nakazima conformando-se amostras esferoidizadas sem e com revestimento de fosfato.

Jul 30, 2018

By ALEXANDRE CALDELLAS BARBOSA

O objetivo desse trabalho é planejar e controlar a chegada de veículos para carregamento nas plantas ArcelorMittal Tubarao e ArcelorMittal Vega, apresentando uma agenda com os horários disponíveis para o transportador escolher. Esse processo de escolha de um horário disponível é suportado por uma agenda gerada pela usina, considerando as restrições operacionais e de capacidade de expedição por ponto de carregamento. Programar a chegada de veículos aumenta a previsibilidade da necessidade de recursos adicionais para realizar o carregamento e assim não gerar filas, não perdendo produtividade no processo de transporte com veículos parados. A ausência da programação tem uma abrangência muito maior que apenas perda de produtividade e atrasos, ela também eleva o custo total de transporte da cadeia de suprimentos. Visando aumentar a competitividade e melhorar a previsibilidade do processo de expedição, foi implementada a solução para regular o fluxo de chegada dos veículos, sistematizando o processo de agendamento do veículo para carregamento.

Oct 30, 2017

By Frieda Saicla Barros

Argamassas feitas com cimento são comumente usadas para revestimentos de paredes, pisos e tetos. Para proteção radiológica, estas argamassas são acrescidas de pó de bário, elemento atenuante contra radiações ionizantes. Este trabalho tem como objetivo principal comparar argamassas usuais utilizadas como revestimento de paredes com a argamassa baritada, cuja finalidade é proteção radiológica em ambientes sujeitos a radiação ionizante. Com base no objetivo proposto, estabeleceu-se a metodologia do trabalho constituída das seguintes etapas: caracterização dos materiais constituintes das argamassas por meio dos ensaios de análise química por fluorescência de raios-X, análise granulométrica, determinação das densidades experimental pelo método de pesagem e medição volumétrica manual dos corpos de prova, moldagem dos corpos de prova das argamassas normais e argamassa baritada (material comumente utilizado para proteção radiológica), avaliação das propriedades mecânicas e avaliação da atenuação da radiação X utilizando o programa Xcom. Por meio deste programa, foram simulados os coeficientes de atenuação em massa das composições, gerando curvas de atenuação, no intervalo de energia estimado a cada 0,01 keV. Em função destas curvas de atenuação em massa, verificou-se o desempenho das argamassas comparando-as com outros materiais desenvolvidos e com materiais de referência (chumbo).

Aug 8, 2018

By Senlin Xie, Wanlin Wang, Lejun Zhou

"The innovative development of multiphase slag in hot-metal treatment has attracted considerable attention due to the reduction of CaO consumption and minimal environmental emission. In order to improve the efficiency of dephosphorization and to reutilize the waste-slag as an alternative source of phosphate ores, it is important to increase the distribution ratio of P2Os between the solid solution (2CaO· SiO2-3CaO· P2O 5) and liquid slag. An investigation was carried out to study the effects ofNa2O and B2O3 on the distribution ratio of P2Os, the results indicated that the increase ofNa2O would enhance the distribution ratio of P2Os with the formation of solid solution (2CaO·SiO2-Na2O·2CaO·P2Os), while B2O3 has the opposite function, and changes the morphology of solid solution. The study would provide an instructive way for the design of multiphase slag and re-utilization of waste-slag.IntroductionIn order to meet the increasing demand for high quality low-phosphorus steel, it requires a high efficient hot metal dephosphorization process. The current slag system for hot metal treatment contains large amount of solid CaO dispersed in liquid slag, which introduced a large amount of CaO consumption due to its low solubility, especially when CaF2 was restricted due to the environmental concerns. Therefore, new refming method to improve the utilization efficiency of CaO by using a solid/liquid coexisting multiphase slag was proposed, and the studies regarding to solid solution formation mechanism, mass transfer behavior of phosphorus and the phase relationship for multi-phase slag have been conducted. [1-6]Normally, hot metal dephosphorization slag consists of CaO--SiOz-FeO--P2O 5, and it has been approved that 2CaO·SiO2 forms a solid solution with 3CaO·P2Os at the hot metal treatment temperature over a wide range of compositions. [7] Kitamura et al [8] pointed out that the (2CaO·SiO2-3CaO·P2O 5) solid solution plays an important role in dephosphorization, and it has been regarded as an absorbents for phosphorus to lower the phosphorus content in liquid phase, which makes it more capable for future dephosphorization. l Besides, the multiphase slag has the potential to be recycled as a source of phosphorus, if the (2CaO· SiO2-3CaO· P2O 5) solid solution could contain high phosphorus content, and it can be separated from FeiO matrix 8hase due to the large difference of their magnetic properties under the strong magnetic field. [10, 11]"

Jan 1, 2014

By Darlene Souza da Silva Almeida

Superduplex são aços inoxidáveis bifásicos de alta liga que, para alcançar suas excelentes propriedades mecânicas e de resistência à corrosão necessitam de um rígido controle sobre sua microestrutura, em especial sobre dois aspectos: relação ferrita/austenita e precipitação de fases deletérias. As transformações metalúrgicas que ocorrem durante o ciclo térmico de soldagem podem modificar tais aspectos e, consequentemente, causar grave degradação das propriedades destes materiais. Buscando contribuir na investigação de parâmetros adequados para a soldagem destes aços, o presente estudo tem como objetivo avaliar a influência do aporte térmico e do gás de proteção sobre tais transformações por meio da avaliação da microestrutural final de juntas soldadas. Para isto seis chapas do SAF2507 foram soldadas via processo GMAW utilizando três aportes diferentes (0,5; 1,5 e 2,2 kJ/mm) e dois gases de proteção distintos. Após a soldagem, a microestrutura das juntas foi caracterizada via microscopia óptica e microscopia eletrônica de varredura e os resultados mostraram que o aumento do aporte térmico elevou significativamente a quantidade de austenita tanto na ZTA quanto na ZF e que a utilização de gás de proteção contendo 2% de N causou aumento de até 17,9 pontos percentuais na quantidade média de austenita na ZF. Adicionalmente, observou-se que os dois menores aportes provocaram a precipitação de fases secundárias na ZTA, com morfologia semelhante à nitreto de cromo.

Jan 16, 2018

By Paterson R. G, Compston W

The Mine granite at the Ardlethan tinfield is dated by Rb-Sr on a muscovite concentrate at not less than 417 &#177; 2.5 Ma (2s), consistent with the intrusion of this granitic body into folded Late Ordovician sediments. A combination of Rb-Sr and K-Ar evidence suggests a slightly younger age, 41O &#177; 2.5 Ma, both for the neighbouring Ardlethan Granite and for the hydrothermal alteration of the Mine granite, with which the tin is associated.On this basis, the somewhat high 206Pb/204Pb of two galena samples from within the hydrothermal alteration zone is best explained by an increase in U/Pb of order 10 per cent during a geochemical event in the Late Precambrian, in the rocks which eventually yielded the Pb to the mineralising fluid. This earlier event probably increased Th/U in these rocks as well, by as much as 5 per cent. If these reconstructions are valid, the lower-than-average U/Pb implied for the original Precambrian source rock bespeaks a mantle component of marginally greater proportion than for &quot;average orogene&quot;.

Jan 1, 1982

By G. Kolosay, J. Rajala, G. Deschênes, A. Romanov

ABSTRACT: The Kupol project, located in Far East Russia, treats a high-grade, free-milling ore containing 25.5 g/t Au, 298.3 g/t Ag, and 0.5% pyrite,with a P70of 53 microns. Most of the gold occurs as elec-trum and the silver is predominantly present in the forms of acanthite, stephanite, pyrargyrite, andproustite. The mill reached the design throughput of 3,000 tpd six months after start-up. AKnelson con-centratorrecovers10.4% gold and 0.5% silver. Leaching (14.5 hours pre-treatment and 116 hours cyanidation)of gravity tailings is performed with the CANMET Enhanced Leach Process (CELP),using only 490 ppm NaCN (cyanide consumption of 1.1 kg/t). The precious metals are recovered by counter-current decantation and the Merrill-Crowe process. Calcium hypochlorite destroyscyanide and thiocyanate. Overall, gold and silver recoveries for 2008 were 95.4% and 85.6%,respectively (2.8% and7.5% higher than targets). In the first eight months of 2009, gold and silver recoveries were 95.0% and82.6%, respectively. By August 2009, the mill processed 1.42 million tons of ore with production of 1.1 million ounces of gold and 11.3 million ounces of silver. CELP performance was not affected by changes in feed grade and ore mineralogy. Additional modifications to the leaching strategy allowed further reduction in cyanide consumption and effluent treatment costs.

Jan 1, 2011

By Helder Keitaro Arçari Ambo

Aços IF (Interstitial Free) são materiais com grande capacidade de serem conformados a frio, normalmente na forma de chapas, utilizados na indústria automobilística na fabricação de carrocerias de automóveis e outros componentes similares. Neste artigo foi realizado ensaio isotérmico de dupla deformação com objetivo de determinar a fração de amaciamento que ocorre no intervalo entre passes e o parâmetro de amaciamento4. O método para obter estes dados foi utilizando software da Instron em conjunto a maquina de torção e o forno de indução. Os resultados obtidos foram de grande importância no estudo para avaliar o comportamento do material quanto aos fenômenos metalúrgicos e termomecânicos envolvidos, ou seja, se ocorre recuperação, recristalização dinâmica entre outros processos de restauração do material quando submetido a forças externas em elevadas temperaturas.

Oct 30, 2017

By Torben Ulisses da Silva Carvalho

A lixiviação é um processo hidrometalúrgico que consiste na separação entre o metal e a ganga através da dissolução em meio aquoso do mineral contendo os metais de interesse. O presente trabalho utilizou o minério de cobre oxidado da Mina do Sossego, sendo lixiviado em escala laboratorial com diferentes períodos de tempo, utilizando o ácido sulfúrico como agente lixiviante. A partir desses ensaios foram construídas curvas contendo os teores do minério de interesse contidos no licor e no rejeito, além do cálculo da recuperação metalúrgica. Os resultados foram encontrados utilizando a técnica de titulometria. Houve notada variação dos teores encontrados, os quais aumentavam proporcionalmente com os períodos de lixiviação. Esse comportamento mostra a necessidade de um maior número de etapas nos determinados períodos de tempo para uma recuperação metalúrgica adequada.

Aug 16, 2017

By G. H. Wigton

THE oxidized ores of the Chief Consolidated Mining Co., in the Tintic mining district, have never yielded to metallurgical treatment by any standard method except smelting. These ores occur in comparatively small, irregular, siliceous replacements in limestone, and carry silver, lead, and gold as the principal valuable metals. But smelting methods. are unsatisfactory, as the lead smelters heavily penalize the large amount of silica in the ore, and the copper smelters do not pay for the lead in the ore; therefore, an alternative treatment method was sought. In 1916, a metallurgical research department was organized under; the direction of the writer. Many standard metallurgical methods were investigated but, on oxidized ore, none yielded extraction great enough to make its use feasible. During some chloridizing-roasting experiments in 1916, made in an assay muffle, the writer noted that large proportions of the silver, lead, and gold were volatilized from certain oxidized ores. The possibility of volatilizing the metals and collecting them in the form of a concentrated fume was then studied. But, as it was shown that satisfactory chloride-volatilization would be limited to a furnace feed with a high fusing temperature of the non-volatilizable constituents, and as the results obtained in a rotary kiln with the admixture of common salt with the ground ore were inferior to muffle tests, further volatilization experiments were discontinued until 1920. During this interval, an experimental sulfidizing and flotation plant was operated. After the cessation of attempts to float the oxidized minerals, chloride-volatilization experiments were resumed. The highly infusible flotation. tailing from the operation of the flotation mill was used for furnace feed. The first tests made on flotation tailing mixed with 10 per cent. common salt showed -nearly complete lead and gold volatilization but considerably less volatilization of silver than in muffle tests. In attempts to increase the silver extraction, the percentage salt in the furnace feed was varied, and it soon became apparent that the use of smaller percentages of salt raised the fusion temperature of the furnace charge and thus,

Jan 8, 1925