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By R. E. Lund

The design, operation, and performance of an integrated pilot plant for recovering zinc and copper from a complex sulfide ore are described. Metallurgical processing comprised selective sulfate roasting in a fluid bed, leaching in a weak sulfuring acid solution, recovering copper by cementation with scrap iron, air oxidation to remove soluble iron, more-or-less conventional purification for removal of impurities deleterious to zinc electrolysis, recovering zinc by electrolyzing solutions, and recycling spent electrolyte to the sulfating roaster. The effects of several feed preparation and roasting variables on the sulfation response of zinc, copper, and iron are set forth, together with the electrolyzing characteristics of the zinc solutions.

Jan 1, 1962

By Felipe da Silva Siqueira, Mariana Sizenando Lyrio, Aline Cristine Lemos Duarte, Weslley Luiz da Silva Assis, Harison da Silva Ventura, André Luiz Moraes Alves, Paulo Rangel Rios

A nucleação nos contornos de grão é um fenômeno muito recorrente em materiais metálicos. Essa situação foi tratada por diversos autores como Cahn e Rios e Villa, usando a abordagem de nucleação em planos e linhas aleatórias. Neste trabalho estudou-se a nucleação nos contornos do polígono de Poisson-Voronoi e de uma matriz hexagonal em 2-d com métodos analíticos e simulação computacional. Utilizou-se uma equação baseada no método de Cahn para nucleação nos contornos de grão. Para nucleação nos contornos do polígono de Voronoi a equação não mostrou adequação total com os resultados simulados para dois tipos diferentes de casos, já para os contornos da matriz hexagonal, notou-se que quanto maior a quantidade de pontos sorteados na matriz, mais os resultados simulados concordaram com a equação proposta.

Nov 13, 2019

By Lucas Xavier Soares de Souza

No contexto de eficiência energética nos setores automobilístico e aeronáutico, a redução de peso em estruturas assume um papel importante. Como alternativa para isso, as espumas metálicas, mais especificamente, as espumas de magnésio e de ligas de magnésio, surgem com grande potencial. Isso se deve, primeiramente, às propriedades desse elemento químico, que é o mais leve entre os metais estruturais. Já a estrutura em forma de espuma aparece como fator capaz de potencializar as propriedades desse elemento. Um dos processos para produção de espumas de magnésio é a metalurgia do pó e uma das etapas desse processo é a compactação dos pós. Busca-se com este trabalho, avaliar a densidade relativa de amostras que foram compactadas a partir da prensagem uniaxial a frio de pós da liga de magnésio AZ91 com hidreto de titânio. Foi verificado que para uma mesma pressão, variando a granulometria da liga AZ91 e a quantidade de hidreto, a variação nas densidades relativas é desprezível. A partir das curvas obtidas nos ensaios de compactação foi possível verificar que na faixa de 130 a 230 MPa ocorreu deformação plástica dos pós de forma gradual e foi possível constatar que a partir de 300MPa não ocorre variação significativa da densidade relativa com o aumento da pressão.

Oct 30, 2017

By César Jaime Fernández

El presente texto señala la función de la empresa privada en el desarrollo minero del Perú a través de dar a conocer los conceptos fundamentales que esto implica y asi determinar el crecimiento minero que convenga al país. Asimismo se revisa la evolución del hombre en la actividad económica, la empresa y los sistemas económicos, la empresa privada, la evolución en el Perú, la reforma de la empresa privada en el Perú y la responsabilidad social de las empresas en torno a la realidad peruana y el desarrollo de la confianza de parte de la comunidad en la inversión privada futura.

Nov 20, 1978

By Luis Alva Florián

El presente trabajo resume los logros obtenidos en la unidad minera San Rafael de Minsur, señala los parámetros actuales de perforación y voladura en tajeos y frentes, así como el carguío en el transporte a través de un estudio comparativo entre rendimientos y costos con los sistemas operacionales.

Nov 24, 1993

Ion exchange (IX) has been in use for a long time, references to IX are made in The Bible, Exodus Chapter 15 vs. 22-25 ?and the waters were made sweet?.1, 2 Aristotle noted a reduction in the salt content of water when passed through certain types of sand, a phenomena probably associated with ion exchange characteristics of zeolites. Some major milestones in IX development include; ? ~ 1400 BC Moses ? ~ 330 BC Aristotle ? 1850 the discovery of the IX process3 ? 1909 Gans proposed zeolites for gold recovery ? 1935 sulfonated coals used for water softening ? 1939 copper recovery from Rayon Production ? 1940 The Rare Earth Project at Ames ? 1952 first South African U IX mine at West Rand (first SX of U using amines 1957) ? 1954 first U IX in USA at Shiprock Mine N.M. USA. ? Late 1950?s U IX over 50 fixed bed systems installed in North America ? 1950?s-1960?s FSU introduce U IX both fixed bed and RIP ? 1968 Gold IX (RIP) Muruntau Uzbekistan (CIL wasn?t commercialized until 1973) ? Mid 1970?s FSU & USA independently develop ISL combined with IX for U recovery ? 1978 Chinese Tungsten IX commercial Plant ? 1984 Uranium extraction from seawater ? 2004 Recovery of Gallium using hydroxyamic acid ligands ? Current ? Commercialization of IX for recovery of gold thiosulfate. Ion exchangers can be naturally occurring or synthetic; the majority of ion exchange materials in use today are synthetic resins based upon organic polymers such as polystyrene or methacrylate. Into more modern times the use of ion exchange for metal recovery was first proposed for the recovery of gold using zeolites in 1909.4 In 1939 copper was being recovered from the manufacturing of Rayon using ion exchange5 a development that continued applicability through to current times in the production/recovery of copper and nickel in ammoniacal leach processes. In early 1949 researchers at the Rohm & Haas Company discovered that hexavalent uranium existed as an ionic complex in sulfuric acid leach liquors, and that quaternary ammonium anion exchange resins exhibited a high selectivity for this ionic species6 The first commercial application of this technology went on-stream in October 1952 at the West Rand Consolidated Mines, Ltd operation in South Africa. 7 Ion Exchange has been applied for the recovery and purification of a range of metals;8 ? Uranium, Thorium and transuranic elements ? Rare Earths ? Gold, Silver and platinum group metals (PGM?s) ? Chromium, Copper, Zinc, Nickel, Cobalt ? Refractory Metals; Molybdate, Vanadate, Tungstate, Rhenium Mercury.

Feb 27, 2013

By André Nogueira

A etapa de flotação convencional do Concentrador 2 ocorre em um circuito com 13 tanques de flotação que recebem o produto dos ciclones limpadores (-0,15mm +0,030mm). O concentrado desta etapa contribui com aproximadamente 80% do volume de produção do concentrador. A necessidade da implantação do sistema de controle avançado de processos (SCAP) advém da alta heterogeneidade na alimentação do concentrador, uma vez que a Samarco não conta com pilha de homogeneização. O objetivo principal do projeto foi maximizar a recuperação metálica da flotação convencional e reduzir a variabilidade do teor de sílica no concentrado final. Aliado ao sistema de análise de imagem de espuma e ao analisador de sílica online, a ferramenta demostrou que, além de atingir os objetivos esperados, trouxe estabilização ao processo e padronização da operação.

Aug 16, 2017

Recovery of Rhenium from Mineral Raw Materials of Kazakhstan

Sep 13, 2010

By Marcela Alves Silva

Os aços inoxidáveis duplex - AID são ligas de Fe-Cr-Ni com no mínimo de 10,5% de Cr, promovendo uma película superficial aderente de Cr2O3, com proteção a corrosão e proporção microestrutural de austenita e ferrita próximas a 50%, potencializando as propriedades mecânicas e resistência à corrosão.Possuem boa soldabilidade, porém pode provocar um desbalanceamento microestrutural e a precipitação de fases deletérias, acarretando o declínio das propriedades, principalmente na zona afetada termicamente – ZTA. Desta forma o presente trabalho tem como objetivoavaliar à influência da energia de soldagem sobre a ZTA da junta soldada de AID, comparando soldas realizadas pelo processo TIG e FCAW levando em consideração o balanceamento das fases ferrita e austenita. Para tanto, foram realizadas soldas com parâmetros comumente utilizados nas indústrias em geral. As amostras apresentadas foram soldadas de acordo com o padrão da Thermon Indústria Mecânica, uma das colaboradoras deste projeto. Conclui-se que a comparação entre os dois processos distintos resultou em fatos já esperados, embasado na revisão bibliográfica, onde o corpo de prova soldado pelo processo TIG apresentou menor região propensa a fragilizações, menor ZTA. As frações de austenita e ferrita em cada corpo de prova foram similares nesta região.

Aug 17, 2017

By Gilbert A. Bonforte, Hugh P. Caspe, Tracy K. Lundin

The Narragansett Bay Commission (NBC) Combined Sewer Overflow Abatement Program is a major effort to address and mitigate discharges from combined sewer overflows in the Providence, Rhode Island area. The proposed system consists of three deep rock tunnel segments totaling 17.8 km (11.1 miles) in length that will provide 860,000 cu m (227 million gal) of storage at depths up to 99m (325 ft). This paper discusses 13.5 km (8.4 miles) of 6.64m (21.8 ft) finished diameter tunnel, four construction shafts, 19 dropshafts and one large diameter pump station shaft tapered from 1 5.2m (50 ft) at the surface to 27.4m (90 ft) at depth. All facilities are in preliminary design.

Jan 1, 1995

By G. S. Headley

At the Sullivan Mine, recent experience with sulphide fires, locally referred to as " hot muck", has necessitated extensive modifications to pillar mining design and operating procedures. Potentially hot pillars are now being designed and mined to prevent fires. Unusual safety hazards and difficulties are encountered in working with, and adjacent. to, existing pillar fires. Operating procedures developed for these conditions have proved successful for safe and continuing production. These changes have minimized the impact of hot ore on current operations and have promise for an improved future.

Jan 1, 1977

"El presente trabajo expone las pautas para la realización de un proyecto de fábrica de cemento, como los factores que influyen en su ubicación respecto al centro de distribución y el tipo de combustible que se emplea para la combustión. El impulso a la creación de una fábrica de cemento, se basa en la existencia de depósitos calcáreos, los cuales estratégicamente ubicados, permiten un mayor progreso económico del país y eliminan la limitación del suministro. Para tal fin, es necesario realizar un estudio económico del consumo considerando el período donde el abastecimiento y costo fueron normales. Otro estudio posible estriba en la comparación de la zona prevista de lde la fábrica con otras áreas de características económicas similares, basándose en la población, movimiento económico y otros elementos de comparación. Una vez determinada la zona, se fija el precio de la venta al público a través de tres elementos: precio de venta en fábrica, costo del transporte y la utilidad del distribuidor. Otros estudios a considerar son los basados en los yacimientos, los cuales complementan mejor la información de la instalación. Entre estos, tenemos a los estudios geológicos, levantamiento topográfico, muestreo sistemático, estudio químico de los minerales y pruebas térmicas y físicas de los productos. La ubicación de la fábrica dependerá si se decide instalar en el sitio de la cantera o en el mismo centro de distribución. Como estudio final, se prevee que la materia prima esté constituída por elementos que químicamente y mineralógicamente sean los más idóneos para así recurrir a materiales de complemento cuya dificultad o facilidad para mezclarlos íntimamente, determine el proceso a utilizarse. En consecuencia, la instalación de dicha manufactura, es el resultado del estudio global de las condiciones provistas en un zona, para así constituirse dentro de un mercado económicamente lucrativo. "

Jul 20, 1957

By Bern Klein

Motivation for Improved Energy Efficiency in Mining ? Canada potentially adopting Greenhouse Gas Emissions and Intensity Legislation in 2013 ? BC -Climate Action Plan and Energy Conservation Agreement in 2008 ? BC Energy Plan 2007 -BC Hydro is mandated to save 50% of new load growth ? TSM Initiative -Energy Management, Energy Reporting, Setting Energy Targets, GHG Management BC MOU for Energy Conservation Agreement -MEMPR, MABC, BC Hydro

May 1, 2010

By Eberhard Rother

El presente trabajo describe el trabajo de perforación y disparo realizado en la mina de Toquepala. Debido a la configuración del depósito, el yacimiento de Toquepala debe ser trabajado por tajadas verticales. El espaciamiento entre taladros varía por diversos factores como la naturaleza de la roca, la configuración del terreno (cresta y talud de los niveles) y las condiciones de operación. En ese sentido, los taladros son cargados diariamente, exceptuando solamente los huecos húmedos con agua. Por ello, se debe analizar el carguío de taladros con explosivo, disparos primarios, perforación y los disparos secundarios.

Nov 1, 1970

By Alvin Schallis

Of all the uses for dolomite that depend on its magnesia content, perhaps the most important is its use in basic refractories. The quantities of dolomite (including both that used as crude and that calcined before use) sold or used for refractory purposes by producers in the United States for 1920-41, inclusive, are shown in figure 1. As can be seen from the chart, the utilization of dolomite as a basic refractory is far from new; it was, in fact, the first basic refractory used extensively in open-hearth steel furnaces. After large deposits of magnesite were opened in Austria-Hungary, the use of dolomite in the open hearth declined somewhat, only to be actively revived during the World War of 1914 to 1918, when supplies from Austria were shut off. The use of dolomite as a refractory in the steel industry again declined slightly for a brief period after the Armistice, but subsequently its use has tended steadily to increase, latest statistics indicating that more dead-burned dolomite is used per ton of open-hearth steel now than during the World War of 1914 to 1918. Despite fluctuations in consumption, dolomite has continued to be by far the most widely used basic refractory material. The following table, showing the quantities of basic refractories consumed in the manufacture of steel, the principal outlet, indicates the relative importance of dolomite. The chief reason for the widespread use of dolomite as a basic refractory is its relatively low cost. Its abundance and the proximity of the deposits to the steel industry (see fig. 2) afford every incentive to enhance the desirable physical properties of dolomite refractories and to ameliorate certain of their less desirable characteristics. The present emergency, with its huge demands upon the steel industry, has lent further impetus to the work of improving dolomite refractories.

Jan 1, 1942

By Synthia N. McIntosh

The U.S. Bureau of Mines investigated the feasibility of using ammonium carbamate (NH2CO2NH4) leaching to recover manganese from steel plant slag. This investigation showed that treatment of the slag in hydrogen prior to leaching enhanced manganese extraction. Up to 80 pct of the manganese and 50 pct of the iron could be extracted from a silicon steel slag that had been pretreated in hydrogen at 700° C. Two 4-h leaching stages conducted at ambient temperature with a solution containing ammonia and carbon dioxide dissolved manganese and iron as their carbamate complexes. Heating the pregnant solution to 65° to 85° C decomposed the complexes and precipitated the metals as insoluble carbonate salts. Ammonium carbamate leaching of other slags from several steelmaking plants produced lower manganese extractions, which suggests that the method cannot be applied satisfactorily to all steelmaking slags

Jan 1, 2010

By B. Farouk, D. Apelian

"A numerical model has been developed to predict the temperature history of particles injected in a low pressure d.c. plasma jet. The temperature and velocity fields of the plasma jet are predicted as a free jet by solving the parabolized compressible Navier-Stokes equations using a spatial marching scheme. Particle trojectories and heat transfer characteristics are calculated using the predicted plasma jet temperature and velocity fields. Correction factors have been introduced to take into account non-continuum effects encountered in the low pressure environment. The plasma jet profiles as well as the particle/plasma interactions under different jet pressure ratios (from underexpanded to overexpanded) have been investigated.I. IntroductionIn the plasma spraying process a d.c. plasma jet is used as a heat source to melt and accelerate powder particles which subsequently impinge and solidify on a given substrate. During low pressure plasma deposition (LPPD) prooess, the plasma jet is expanded into a low pressure environment (40-80 Corr) which results in high plasma jet velocities with Mach numbers ranging from 2 to 3. Previous efforts to predict heat transfer and fluid flow in plasmas have made use of incompressible flow formulation employing turbulence models [1-3] for atmospheric plasma spraying. However, these theoretical calculations have been limited to the subsonic flow regime; hence, the compressibility effects and viscous heat dissipation were neglected. In the LPPD process, the plasma jet is operated at the supersonic flow regime, therefore, the compressibility effects and viscous heat dissipation are no longer negligible. This is the main motivation of this work.In addition, production of high quality dense deposits requires that a large fraction of the injected particles be in a molten state when they impact the substrate. An additional motivation for this work is that it is important to understand the plasma/particle heat and momentum transfer since these phenomena dictate both the particle thermal history and particle trajectory.Early computational works in supersonic nozzle field flow [4,5,6] consisted of patching methods that divided the flow field into an invisoid free stream and a viscous boundary and. mixing layers. Each was analyzed independently and coupled through appropriate boundary conditions. Later schemes [7,8] involved solving time-dependent, compressible Navier-Stokes equations over the entire computational domain. These schemes show a great promise in predicting flows with complex structure, and where the viscous effects became prevalent."

Jan 1, 1986

By Leland A. Yerkes

Refining aluminum from crude aluminum alloys by the subhalide reaction was investigated to develop a method of producing aluminum by means other than electrolysis of its oxide. The best materials and design for the apparatus and also optimum operating conditions, including temperature, pressure, vapor flow rate, and composition of alloy charge were studied. In the subhalide process, aluminum-trihalide vapor reacts with aluminum in the alloy under high temperature and low pressure, forming volatile aluminum monohalide which reverts to aluminum metal and aluminum trihalide on cooling. The only halide used in this investigation was aluminum trichloride. The crude aluminum-silicon alloys used as the principal raw material contained from 21.9 to 36 percent aluminum, and significant quantities of iron and titanium. These alloys were produced by direct electric smelting of clays. Graphite tubing that was heated by an induction coil proved to be satisfactory material for the laboratory reactor chamber, Enclosed in an insulated glass or quartz pipe, the reactor was used in both vertical and horizontal positions with various baffle and tray arrangements for directing the trihalide vapor both over and through the alloy. Aluminum trichloride vapor was generated in the sublimer at one end of the glass pipe, passed into the reactor where contact was made with the crude alloy, and aluminum monochloride gas was formed. When the gaseous mixture of aluminum monochloride and unreacted tri-chloride passed out of the reactor and entered the condenser, the gases were cooled to 900° C. or less, causing the monochloride to disproportionate into aluminum and aluminum trichloride vapor. The aluminum was deposited on the condenser walls while the aluminum trichloride vapor was carried out of the condenser and into the opposite end of the glass pipe where it solidified on the cooled copper coils.

Jan 1, 1961

By W. M. Aubrey

The use of solid fuel in shaft furnaces to indurate iron ore pellets was originally considered a necessary evil, which the industry worked long and hard to eliminate. Since then changes have taken place in furnace design and operating practices that have led us to our suggestion that solid fuel additions could again be used. In essence, what has happened is that the developments which made it possible to operate without solid fuel have also created new operating conditions favorable to the effective use of solid fuel. Because these new conditions* were brought about in part by the desire to eliminate solid fuel and because the development was a gradual one, the industry failed to reassess its position and for years neglected the possibility of returning to solid fuel.

Jan 1, 1967

By A G. Cuison, B V. Andam

Three well-known copper and gold deposits in northern Luzon, Philippines are located in the Mankayan Mineral District. These are the Lepanto Copper-Gold Deposit, the Far Southeast Porphyry Copper Deposit and the newly discovered Victoria Gold Deposit. The latter discovery led LCMC to shift from a predominantly copper mine to a gold mine. The pre-Eocene Lepanto basement andesite and the middle Miocene Balili volcaniclastic sequence underlie the Mankayan Mineral District. They are intruded by tonalitic to gabbroic Bagon Intrusive followed by diorite-quartz diorite intrusions. Diatreme emplacement of late Miocene-early Pliocene Imbanguila dacite pyroclastics and porphyries took place much later. Faults in the district mostly form a conjugate fracture pattern dominated by north and northwest trending shears, east-west trending extensional fractures and few north-south trending fissures. Victoria is an epithermal gold-base metal rich quartz vein deposit. The veins occur along tensional structures and it is common to observe crustiform and banded features among the sulphides and gangue minerals. It is an open space infilling type of mineralisation. The Victoria vein systems are divided into zones based on continuity. In each zone are major veins and associated spits. Dacite pyroclastics and porphyries predominantly host the major veins with a few narrow veins hosted by the Balili volcaniclastics and the Lepanto metavolcanics. The veins generally trend east-northeast with 75 - 80 dips towards the south. The longest vein can be traced fairly continuously for a horizontal distance of about 600 metres. The vertical persistence of major veins exposed on three level drives has a range of 150 metres and can reach as much as 400 metres based on drill hole intercepts. The vein widths vary from two to eight metres. Right lateral movements of either the NW or NE shear faults could have produced the east trending tensional fractures. The development of ore shoot patterns was recognised and has been helpful to the mining operations. Cymoid loops with defined pinch and swell features are noted both laterally and vertically. Complementing the structural pattern is the distribution of gold values along veins where lateral and vertical continuity is also observed. Gold is associated with quartz, sphalerite, galena and chalcopyrite. In relatively high gold zones, the abundant sulphides are sphalerite and galena. In relatively high copper zones, there is an abundance of chalcopyrite and tetrahedrite. Galena is always associated with sphalerite but less in abundance. Chalcopyrite occurs either as separate bands from or associated with sphalerite-galena. Chalcopyrite and tetrahedrite appears contemporaneous with sphalerite and galena but in some portions the former cuts the latter sulphides. The predominant gangue minerals are quartz, carbonates and gypsum. Rhodochrosite is the predominant carbonate gangue. Few sulphides are found in the carbonates. Gypsum (anhydrite) is found cross-cutting early mineralisation. It carries very few sulphides. The alteration halos around veins are relatively narrow. In an outward sequence, the silicic alteration occurs very near the veins, followed by sericitic-argillic alteration then to propylitic zones. It is also common to observe veins bounded by propylitic alteration. Preliminary paragenetic studies show apparent three stages of mineralisation, the early-quartz (-gold) stage followed by a carbonate stage and a late-gypsum stage. The abundance of base metals relatively decreases towards the gypsum stage. The Victoria gold deposit could have some genetic associations with the Lepanto Cu-Au deposit and probably indirectly with the FSE porphyry system. It is relatively apparent that the Victoria quartz-gold-base metal veins could have occurred similarly as the quartz-gold roots overprinting the Lepanto enargite mineralisation. This overprinting signifies the waning stages of the entire hydrothermal system.

Jan 1, 1999