Search Documents

By K. Hanumantha Rao, A. Nayak, K. S. Narasimhan, S. N. Mahapatra

B.A. Hancock It is not at all surprising that causticized potato and potato derived amylopectin starch solutions performed much better than their parent starches. Some preparation is required to rupture the starch granules to effect the polymeric adsorption and interparticle bridging necessary for selective flocculation. In laboratory work comparing the deslime performance of causticized and autoclave cooked laboratory corn starch solution preparations, it was found that higher deslime weight rejections, with attendant proportionally greater iron unit losses, occurred with the causticized starch. These results may be specific to the ore involved but they do suggest that cooking and causticizing cause different starch granule rupture and/or starch breakdown, which have an effect on desliming response. I calculated from the data in the article that the slimes product grades were high - 24.3% and 20.3% Fe when 53.7% and 54.5% Fe concentrate products were obtained, respectively, in Table 4, and 21% Fe with a 62.6% Fe concentrate in Table 5 - using the natural tailings sample, which had a head of 34.3% Fe. It may be advisable for the authors to consider different starch preparations in future investigations. The combination of upgrading and selectivity results presented in Table 4 are not as good as the authors suggest. The authors' claim that a system has been developed to produce saleable concentrates from the Kudremukh tailings is quite disconcerting. There are many hurdles yet to be crossed before commercial application of selective flocculation becomes possible because differences between the very small-scale laboratory tests conducted and commercial application are rather large. Among the many differences are varying circuit feed grades that will occur from use of tailings, the apparent face that much lower tailings grades will be encountered in practice (it is much easier to achieve a high concentrate grade with reasonable recoveries using 34.3% Fe tailings as in the study rather than 25.3% Fe tailings grades that the plant apparently averages), the hydraulic nature of the thickeners used in operations compared to the static system used in laboratory tests, the different size distributions that will be obtained from a plant closed grinding-classification circuit, and differences in water used in a plant operation and the laboratory. The authors wrote that it was necessary to overgrind to be sure that the coarse gangue would not settle with the iron oxide floccules. This situation is likely to be exaggerated in commercial operations where it is assumed cyclones would be used for classification. Because cyclone classification is greatly influenced by particle densities, there will probably be an even greater difference in size between the iron and gangue particles in the plant, which would make the gangue slightly coarser still in relation to the iron. This would make the selective flocculation-desliming separations using the procedure employed by the authors even more difficult and, using the dispersant system the authors employed, greater overgrinding would be required. To grind finer to minimize the coarse gangue in the flocculated iron oxides is quite inefficient and appears not to broach the problem. The actual problem appears to be insufficient dispersion of the ground pulp. In this situation, addition of a dispersant would likely be required to attain a sufficiently high pulp dispersion level to efficiently effect a selective flocculation-desliming separation. Although the very coarse particles would still have a tendency to settle with the floccules, it probably would be found unnecessary to overgrind as much as indicated. Use of an optimum combination of dispersant and pH modifying reagents may also significantly improve the selectivity of desliming. Additionally, although it is possible that sufficient dispersion may be obtained by pH control alone in some situations, it is quite probable that added dispersity was obtained in the reported work from using distilled water. It is research experience that distilled water enhances dispersion. In commercial operations it may not be expected that sufficient dispersion will be obtained by pH control alone, unless the water used in the process is by nature quite dispersive. Overall, a change in the Kudremukh tailings dispersant scheme appears necessary where a dispersant is used in conjunction with a pH modifying reagent. With this change, different dispersion-flocculation responses will result that would have to be further evaluated. Therefore, it is still an open question whether an efficient and effective selective flocculation separation using Kudremukh tailings may be obtained that will produce saleable concentrates.

Jan 9, 1986

By Laurance L. Oden

The Bureau of Mines is developing nickel catalysts for converting synthesis gas derived from coal to synthetic natural gas. The present report describes the relationship between the composition of aluminum-nickel alloys in the composition range NiAl3 to Ni2Al3 equilibrated at 840° C and the properties of catalysts obtained from them. Methanation activity was determined in the temperature range of 300° to 360° C in a flowing gas stream containing 1 pct CO, 8 pct H2, and the remainder He. One part per million of H2S was added to the gas stream at 400° C to evaluate the susceptibility of catalysts to sulfur poisoning. The total surface area was measured by the adsorption of nitrogen at liquid nitrogen temperature, and the active surface area was measured by the adsorption of hydrogen at room temperature. Total surface area and active surface area were found to increase with increasing proportion of aluminum-saturated Ni2Al3 in the precursor alloy, but methanation activity and resistance to poisoning by H2S were nearly constant. However, the methanation activity of the catalyst prepared from stoichiometric Ni2Al3 was less than half that of the other catalysts.

Jan 1, 1978

By Robert R. Walden, LeMont West

K ENTUCKY'S first acid-grade fluorspar flotation Kmill, shown in Fig. 1, was placed in operation Aug. 1, 1952, by the Pennsylvania Salt Manufacturing Co. at Mexico, Ky. During 1951 a critical shortage of acid-grade fluorspar developed and it became necessary for the company to produce part of its fluorspar requirements. In 1951 the company purchased the Crider and Lennen metallurgical fluorspar mill and an adjacent stockpile of tailing at Mexico, Ky. The tailing, assaying about 26 pct calcium fluoride, originated from log washer and jig mill concentrators in the area. As the mill did not have a fluorspar dryer or convenient rail facilities, the company leased the Burleson concentrator at Marion, Ky., where these facilities were available. At Marion, Ky., on the Illinois Central Railroad, dry acid-grade fluorspar is transported direct to the company's Calvert City, Ky., hydrofluoric acid plant. The Mexico flotation plant was reconditioned and designed to produce acid-grade fluorspar from the jig tailing stockpile. The new plant flowsheet is shown in Fig. 2. The ore feed, old tailing, which contains 10 pct of waste rock and coarse gravel assaying approximately 8 pct CaF,, is bound together by sticky clay

Jan 1, 1955

By W. W. Adams

The United States Bureau of Mines, in cooperation with the National Send and Gravel Association conducted a safety contest in 1929 Among producers of sand and gravel. Only 26 plants were enrolled, as the contest was late getting under way. It is hoped that a ranch larger number of plants will be represented in the safety competition of 1930. Two trophies, both of which were provided by Rock Products magazine, were awarded at the end of the contest; one trophy was given for the best safety record among plants working 100,000 or mare man-hours during the year and the other for the beat record among plants working less than 100,000 man-hours. The trophies were presented to representatives of the winning, companies on January 29, 1930, at the annual convention of the National Sand and Gravel Association at Memphis, Tenn.

Jan 1, 1930

By Rafael Fernandes Reis, Leonardo José Silva de Oliveira, Rodrigo Seara Martins

Alterações na cristalização dos pós fluxantes durante o processo, devido variações de composição química pelas reações metalúrgicas na interface metal/escória ou pela incorporação de compostos exógenos, afetam o fluxo de calor no molde de lingotamento contínuo. Um dos compostos importantes é o ZrO2, proveniente do desgaste da válvula submersa. A proposta do trabalho foi investigar o efeito deste composto, utilizando simulação laboratorial, na cristalização do pó fluxante e no fluxo de calor do molde. Os resultados demonstraram que quando há o incremento do teor de ZrO2 o fluxo de calor na região do menisco também se eleva. Tal efeito é crítico para formação de defeitos, uma vez que a região do menisco é crucial para a solidificação inicial do aço.

Oct 1, 2019

By Alexandra de Almeida Diego

O controle da transferência de calor é uma das principais funções que o fluxante exerce durante aplicação no molde de lingotamento contínuo. O fluxo de calor na interface placa / molde deve estar adequado aos parâmetros de processo e ao tipo de aço, caso contrário pode provocar preferencialmente alarmes de agarramento em aços baixo carbono e trincas longitudinais em aços médio carbono, podendo levar até ao breakout. Este trabalho tem o objetivo de caracterizar os filmes de escória aplicados em aços baixo (Filme BC) e médio carbono (Filme MC), ambos comerciais, utilizando as análises de Microscopia Eletrônica de Varredura (MEV) com Energia Dispersiva de raios-X (EDS) acoplado e Difratometria de raios-X (DRX). As diferenças entre os filmes de escórias foram discutidas e relacionadas aos dados presentes na literatura.

Aug 16, 2017

El presente trabajo describe el sistema y los métodos para la extracción del oro en la planta de beneficio de Andaray Gold Mines, alcanzando una productividad óptima en el campo metalúrgico. La mina está situada en San Juan de Chorunga, provincia de Condesuyos, departamento de Arequipa, donde sus yacimientos mineralizados son de dos tipos: los yacimientos descompuestos que contienen limonita y oro libre, perteneciente a la mina Mercedes , y los de mineral piritoso aurífero, que comprenden chalcopirita y ojos de galena, perteneciente a la mina San Juan. El proceso de explotación se inicia con el transporte del mineral hasta su descarga en la parrilla de apertura. E mineral que no pase por la parrilla, se deriva a la chancadora durante 10 horas. Posteriormente pasa por la molienda para luego ser clasificado. Allí se adicionan los reactivos para la flotación y su análisis de malla. Producto de la flotación se obtiene el concentrado. El filtrado de los concentrados conlleva su envío a la molienda secundaria durante un período de seis horas. En este estado, la partícula de oro se encuentra limpia y en óptimas condiciones para la amalgamación y cianuración, donde el mercurio y la amalgama son exprimidos en una lona, destilándose, y se procede a la solución del oro, respectivamente. El método seguido es la agitación neumática, que suelta aire comprimido para la elevación del concentrado por el tubo elevador. Prosiguen los efectos de decantación, operación, control del cianuro y del alcali libre, precipitación, clarificación, limpieza y función de los precipitados. En el laboratorio se realiza el control de muestras del circuito de flotación, cianuración y de las barras, utilizando los métodos de soluciones de cianuro, ensayo de concentrados, minerales de mina, cabeza y relaves y ensayos de los precipitados. Finalmente, los cuadros de consumo de reactivos, mostrarán la eficacia del sistema y los resultados económicos de la planta de beneficio, como los costos, eficiencia de plata y mano de obra.

Jul 20, 1957

By Tiago Rafael Ferreira de Brito

O presente trabalho comparou o desempenho do fosfato de zinco e do microfosfato de zinco, ambos com tecnologia dry-in-place para verificação do comportamento destes revestimentos frente à conformação mecânica, por meio do ensaio de embutimento Erichsen, método Nakazima e curvas limite de conformação (CLC). Foram estudadas chapas de aço-carbono grau EM e grau EEP G4 eletrozincadas e fosfatizadas. As chapas foram fosfatizadas empregando-se dois banhos: fosfato de zinco e microfosfato de zinco, ambos com tecnologia dry-in-place. A caracterização da morfologia dos fosfatos estudados por microscopia eletrônica de varredura mostrou que as camadas de fosfato de zinco não apresentaram formação de cristais, quando aplicadas por roll coater e as análises por EDS comprovaram a presença do elemento fósforo. O ensaio de embutimento Erichsen somado aos resultados obtidos nas curvas CLC demonstraram que o microfosfato exibiu desempenho melhor em comparação ao fosfato. A diferença entre os dois tipos de fosfato foi mensurável e evidenciou que a tecnologia dry-in-place colaborou com a produção de camadas fosfatizadas adequadas para a lubrificação durante o processo de conformação mecânica.

Aug 16, 2017

By Jorge Alencastre Miranda

El presente artículo es un análisis dinámico estructural de una faja transportadora, (tipo Staker Radial) de una empresa minera a través de modelos conceptuales simplificados y programas computacionales.

Apr 1, 2016

By Jovanir Francisqueto

O objetivo deste trabalho foi implementar a célula de atendimento a prioridades dos clientes na ArcelorMittal Tubarão (Cockpit de Atendimento a Clientes), com foco na melhoria dos indicadores relacionados a entrega para clientes e visando reduzir a burocracia e barreiras organizacionais de forma a agilizar a tomada de decisão e consequentemente agilizar o fluxo dos pedidos prioritários na usina, desde a produção de aço até o despacho de produtos. O projeto foi implementado em etapas, com destaque para duas frentes, sendo uma de gestão da mudança, com a implementação do conceito de gestão por processos e em paralelo toda a implementação de infraestrutura sistêmica para suporte ao processo. Seis meses após o inicio do projeto a implementação do conceito de Gestão por Processo, de baixo custo e alto impacto no negócio trouxe uma evolução significativa nos indicadores de atendimento a cliente, com destaque para a consecução de atendimento aos pedidos prioritários que saltou de cerca de 30% para patamares acima dos 90%, assim como o lead time total de atendimento a pedidos que foi reduzido em cerca de 30%.

Aug 17, 2017

By Jack Eloranta

This paper documents the relationship between material handling and processing coete compared to blasting cost. The old adage, "The cheapest crushing is done in the pit", appears accurate in this c!ase study. Comparison of the accumulated cost of: powder, selected wear materials and electricity; indicate a strong. inverse correlation with powder factor (lbe powder/long ton of rock). In this case, the increased powder cost is more than offset by electrical savings alone.

Jan 1, 1995

By W. K. Collins, C. L. Dahlin, D. C. Dahlin, W. K. O’Connor, G. E. Rush

Direct mineral carbonation has been investigated as a process to convert gaseous CO2 into a geologically stable final form. The process utilizes a slurry of water, with bicarbonate and salt additions, mixed with a mineral reactant, such as olivine (Mg2SiO4) or serpentine [Mg3Si2O5(OH)4]. Carbon dioxide is dissolved into this slurry, resulting in dissolution of the mineral and precipitation of magnesium carbonate (MgCO3). Optimum results have been achieved using heat pretreated serpentine feed material and high partial pressure of CO2 (PCO2). Specific conditions include: 155°C; P002=185 atm; 15% solids. Under these conditions, 78% conversion of the silicate to the carbonate was achieved in 30 minutes. Process mineralogy has been utilized to investigate the appropriate feed characteristics, identify the process products, and interpret the mineral dissolution and carbonate precipitation reaction paths.

Jan 1, 2001

By Ali Kazmi, Wern-ping N. Chen

A load rating procedure was performed to evaluate safe load capacity of the Port of Miami Tunnel (POMT), FDOT Tunnel No. 871071 SR 887. The rating procedure performed on a total of eleven stations beneath roadways and with fill depth less than the tunnel exterior diameter (42 ft). Calculations on tunnel sections passing beneath roadways were performed to evaluate the structural response of the sections subject to moving vehicular loads, dead load, and earth pressures. Ratings were performed in accordance with AASHTO and FDOT guidelines. The procedure considered two types of vehicles (HL-93 and FL-120) and two rating levels (Design level and Permit level). As part of HL-93 vehicle, Tandem load was also considered for rating, separately. For HL-93 and HL-93 Tandem, inventory and operating level ratings were performed. The results show rating factors are high. The minimum rating factor is 16.8 using Inventory truck HL-93. For Permit level using FDOT FL-120 truck the minimum rating factor is 6.9. As can be seen, rating factors are higher than comparable analysis for bridges. This paper explains how the procedure can be implemented for tunnels and evaluates the rating results.

Dec 1, 2022

By Gustavo Torres Málaga

Jul 20, 1955

By Bruna Iost Camacho

Inclusões não metálicas são impurezas presentes nos aços que corrompem, quando não moderadas, suas propriedades mecânicas e metalúrgicas. O tratamento de inclusões com ligas à base de cálcio é fortemente utilizado visando à produção de aços mais limpos e é fortemente induzido pela composição química e temperatura do aço. O objetivo geral deste trabalho será o estudo termodinâmico e experimental a respeito da modificação de inclusões não metálicas através do tratamento com cálcio, em aços de diferentes teores de enxofre. O presente trabalho utilizará como metodologia: i) obtenção de dados através de experimentos em forno resistivo para determinar os dados iniciais utilizados nas simulações; ii) estudo termodinâmico computacional através do software FactSage; iii) análise de inclusões via MEV/EDS e ASPEX-PSEM explorer. iv) comparação dos resultados obtidos nos dois meios de análise e também compará-las com os resultados obtidos via simulação. Para tanto, serão estabelecidas dife rentes temperaturas e concentrações de cálcio no banho e diferentes tempos de processo. Como resultado final, espera-se gerar um maior conhecimento que contribua para a compreensão dos fenômenos envolvidos em aços com maior teor de enxofre. Além disso, espera-se validar as técnicas e metodologia empregadas neste trabalho.

Aug 8, 2018

By C. Villachica

El molibdeno es un metal de alta cotización en el mercado puesto que se emplea en aleaciones de acero para la construcción de piezas y herramientas de alta duración. Sin embargo, este mercado de concentrados de molibdeno se rige a especificaciones referidas a impurezas y leyes mínimas de Mo, que limitan su recuperación por la relación de esta variable con el grado de los concentrados. Por ello, el presente texto describe un programa elaborado por el Departamento de investigaciones metalúrgicas de CENTROMIN-PERÚ que incrementa las recuperaciones de Mo y la calidad de los concentrados con técnicas de concentración en combinación con métodos hidro y/o pirometalúrgicos.

Oct 14, 1980

By O&apos, M. W. Neill

Mini-piles have been found to be a practical, technically correct remedial underpinning method. They can be constructed in limited access areas with very little disruption. Experience indicated that mini-piles installed using a down-the-hole soil displacement hammer would be particularly effective in the "bottomless" Beaumont Clay formations in the Houston, Texas, U.S.A. area. The University of Houston Foundation Testing Facility was ideally suited to perform tests on mini-piles. The availability of extensive geotechnical data and previous pile test results was invaluable in evaluating the mini-pile test data. As expected, the mini-pile test results were consistant with test results from large sized driven piles in the same soil formation.

Jan 1, 1989

By Wesley Alves Quintão

O projeto criado e aqui apresentado teve por objetivo atender as necessidades da empresa em relação às metas de economia de energia e adequação ao mercado atual e para isso foi estudada uma maneira de gerar economia de gás com o desligamento de pilotos de ignição e também eliminar atrasos mecânicos no processo de acendimento, purga e estanqueidade do forno de reaquecimento Stein, através do uso de recursos da automação, eliminando dispositivos eletromecânicos garantindo velocidade de informação, economia comprovada de gás e maior confiabilidade no sistema de monitoramento do processo.

Aug 17, 2017

By T. B. Acton

There are two types of ore transportation systems in use at Newmont's Magma Copper Co. San Manuel mine in Arizona-rail-mounted, box-type rotary cars and the newer rail-mounted, bottom-dumping ASEA cars. Though the cost per car for the ASEA units greatly exceeds the cost per rotary car, the advantages of the ASEA units, including much faster dump times, have made the ASEA system a successful alternative at the San Manuel mine. The rotary system of ore transportation has been in use at San Manuel since production began in 1956. The system employs 7.9-m3 box-type cars to transport ore by rail to shaft pocket areas. A rotating dumping mechanism turns three cars at a time upside down to empty them, and returns them to an upright position. Trains of 15 cars each are dumped in about six minutes. Each 15-car train is pulled by an 18-t rated trolley locomotive. There are about 400 rotary cars in service at San Manuel and the system is used for the majority of ore haulage. This well-proven rotary method was instrumental in achieving the December 1977 world record of 272 Mt hoisted from an underground copper mine. Magma Copper Co. began using ASEA cars in late 1977. Designed by ASEA of Sweden, the cars are built for San Manuel by Kasper-Hall Manufacturing Co. in Tucson. The cars basic design feature is a hinged floor that opens at the side as the car is pulled through the dump. As it passes over the dump, a fifth wheel attached to the hinged floor (opposite the hinges) travels along a rail in the dump. This rail dips down into the pocket and then returns to track level. As the fifth wheel travels along the rail, the car floor opens, the car dumps, and the floor is then returned to track level. As the car is dumping, the body remains suspended over the pocket by wheel rollers attached to each side of the dump. Trains of 10 cars each are emptied in about 45-50 seconds. Each ASEA train is pulled by an 18-t rated trolley locomotive, adapted at San Manuel to allow it to pass through the ASEA dump. At minimal cost, "wings" are welded to each side of the locomotive. These wings suspend the locomotive over the pocket as the train passes through the dump. Advantages of the ASEA System Major design characteristics of the ASEA and rotary systems are shown in the accompanying table. The comparison points out some of the following advantages demonstrated by the ASEA system. • Faster dumping-An ASEA train dumps in 50 seconds, while a rotary train takes at least six minutes. There is no stopping or starting when dumping an ASEA train. The train enters the dump area, dumps, and leaves in one continuous motion-in contrast to rotary trains which must stop and start five times to dump. With the rotary system, three cars are spotted in the dump mechanism by remote control. When the cars are in place, the train operator activates the dump, the cars are turned over, and then returned to an upright position. This process is repeated until all 15 cars in the train are emptied.

Jan 4, 1980

By N. Wahl, D. M. Blackketter, R. Thornton

This paper evaluated using a water-filled abandoned mine (Orphan Boy) as a heat source for a 240- kW closed-loop heat pump with the goal of heating a 2,000-m2 building. The mine has a 245-m vertical shaft connected to a large stope by three horizontal cross-cut shafts. There is 1,250 x 106 L of water at a consistent temperature of 24-26° C that is available mostly in the stope. The only heat exchanger placement option is in the vertical shaft. Therefore, the focus was to model heat exchanger placement in the vertical shaft to determine the extent to which the systems will induce thermal currents between the stope and vertical shaft. Modeling of thermal currents, temperature profiles and heat contribution from the ground was done using finite difference and computational fluid dynamics. An optimal configuration was determined showing sufficient water movement and heat transfer will occur with a low water temperature in the shaft above 20° C. This project supports a U.S. Department of Energy (DOE) grant that will implement the full-scale system.

Jan 1, 2013