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By Leandro Ramos Rodrigues, Jorge Emil João da Penha Júnior, Sérgio Valle Júnior

Esse artigo apresenta a estratégia adotada pela ArcelorMittal Tubarão referente extração de dados de pesagens realizadas pelas pás carregadeiras de forma automática. Para isto, foi desenvolvido um hardware que coleta e envia os dados por meio de uma comunicação de dados 3G/4G para o ambiente de nuvem da Microsoft por meio do produto Microsoft Azure IoT Hub, após isto os dados são enviados para o sistema de balanças rodoviárias da ArcelorMittal Tubarão. A Implantação da solução trouxe uma redução de 17% do tempo do recurso da contratada e 9% do tempo do recurso próprio, além de aumentar a confiabilidade do processo de consolidação dos dados de pesagem das pás carregadeiras.

Oct 1, 2019

By Ismael Nogueira Rabelo de Melo

A adição de Fe-Nb em ligas com alto teor de carbono apresenta baixas taxas de dissolução devido à formação de uma camada carburada na superfície, exigindo longos tempos para dissolução dos carbonetos NbC no banho. Foi avaliada a eficiência da dissolução de Fe-Nb em pó pelo processo de simples adição em uma liga de Ferro Fundido Branco com Alto Teor de Cromo. No processo foram obtidas eficiências de dissolução em torno de 90% e os carbonetos NbC apresentaram em formas finas e em aglomerados.

Oct 30, 2017

By Eduardo Cabral

A nova política de resíduos sólidos, imagem positiva da empresa, utilização consciente de recursos com a consequente redução de custos e preservação do meio ambiente têm levado as minerações e siderúrgicas a adotar uma gestão responsável com relação aos seus coprodutos. Em consequência, esses coprodutos (escorias e lamas da mineração, lamas de aciaria, pós da sinterização, calcinação, coqueria, carepas e outros resíduos da siderúrgica) estão sendo economicamente reintroduzidos no processo produtivo. Esse trabalho pretende fazer um resumo de possíveis tratamentos que esses materiais podem sofrer, como umectação, aglomeração, briquetagem, granulação, pelotização ou extrusão.

Aug 16, 2017

By Éric José de Souza Baeta

Maximizar a produtividade com o mínimo de perdas e sem interferir nas operações unitárias adjacentes é um dos grandes desafios existentes nas usinas de beneficiamento de minério em geral. O presente artigo tem como objetivo mostrar um caso prático de implementação de uma estratégia de controle do tipo preferencial, considerando restrições de processo, com o objetivo de obter ganho de produtividade e redução de perdas. Serão abordados aspectos práticos da implementação e resultados reais obtidos em uma das etapas do processo de uma usina de beneficiamento da Vale.

Aug 16, 2017

By J. S. Hu

FTIR spectroscopy has been used for the characterization of adsorbed oleate at the fluorite surface. It has been found that modest changes in the adsorption density at high temperature and high oxygen potential do not provide a satisfactory explanation for the significant increase in the hydrophobic character of the system under similar conditions. Rather, FTIR spectroscopic measurements suggest that chemical interaction between adsorbed oleyl groups occurs at high temperature and/or oxygen potential and accounts for the increased hydrophobicity. Specifically, the intensity of the =CH bond of the adsorbed oleate diminishes at high temperature and/or high oxygen potential. Such a phenomenon was not observed in control tests with the calcium oleate soap. For extensive reaction at the fluorite surface, the presence of a new surface species has been identified. These results indicate that the fluorite surface catalyzes an oxidation and/or polymerization reaction between adsorbed oleyl groups which results in a more hydrophobic structure at the fluorite surface.

Jan 1, 1986

By V. Barúa

El presente estudio revisa el panorama historiográfico sobre las etapas del minado de tajo abierto desde el pasado, presente hasta el futuro. En el pasado, la minera superficial a tajo abierto surgió para obtener principalmente materiales no metálicos de construcción, alcanzando su auge a partir de las últimas décadas del siglo pasado. Sin embargo, existieron algunos obstáculos en el desarrollo de su mecanización y tecnología que posteriormente fueron mejoradas. Posteriormente, existe una competencia por desarrollar equipos mecánicos de mayor capacidad y operación, como un interés por el advenimiento de nuevas tecnologías y uso de la investigación. Finalmente, el panorama sobre el futuro del minado a cielo abierto, presenta condiciones en las que no se asume nuevos progresos mecánicos ni mayores espectativas que en el pasado.

Nov 20, 1972

By Bruno Sampaio Jannuzzi, Klayton Sebastião Leopoldino, Rodrigo Jorge dos Santos Arruda, Sergio da Cunha Motta

Devido à necessidade de mitigar os riscos aos quais os empregados próprios e contratados ficavam expostos, durante o processo de peação de bobinas, em porões de navios, e também de reduzirmos os custos nessa operação, concluímos que deveríamos alterar o processo para aumentar a segurança dos trabalhadores, com a eliminação de materiais perfurocortantes, gerar redução do esforço físico, com a substituição de equipamentos e, consequentemente, obter redução de custos e ganho de produtividade, no embarque de bobinas de aço, em porões de navios, no Sepetiba Tecon - Porto de Itaguaí.

Oct 1, 2019

By Lorena Cristina Amorim Moura

O balanço de enxofre ao longo da cadeia de produção de aço é um problema muito discutido no setor siderúrgico, pois afeta a qualidade do produto final. Assim, este estudo tem como objetivo desenvolver uma metodologia de previsão de enxofre do coque, a partir de enxofre do carvão, com base na sua taxa de dessulfuração, obtida através do Índice de Inchamento Livre (FSI) em escala laboratorial. Estes resultados mostram boa correlação com o processo de fabricação de coque, permitindo a determinação do valor em uso em relação ao teor de S de cada carvão.

Oct 30, 2017

By Carlos Alberto Silva

A aplicação de lubrificação de tiras é um desafio para a maioria das empresas. Aplicações irregulares, não uniformes e excesso de óleo são problemas típicos encontrados quando se utiliza rolos de transferência ou tubos furados. Outros problemas como névoa, baixa eficiência de transferência e um ambiente de trabalho perigoso e insalubre são problemas comuns encontrados com equipamentos que utilizam a pulverização atomizada. O atual trabalho busca comparar os resultados da lubrificação de tiras obtidos com um equipamento de pulverização hidráulica da Spraying Systems frente ao antigo equipamento utilizado, atomizado.

Aug 16, 2017

By José Roberto de Olveira, Anna Paula Littig Berger, Caio Vaccari Silva, Victor Bridi Telles, Felipe Fardin Grillo, José Roberto de Oliveira

No presente trabalho foi proposto uma análise da eficiência de desfosforação de uma mistura padrão M1 e outras cinco misturas, onde foi realizada variação da massa de mistura adicionada ao sistema (60,70 e 80g), temperatura de trabalho (1350ºC e 1350ºC ajustada) e metodologia de adição. Os testes experimentais foram realizados a uma temperatura de 1400°C, com agitação de 450 RPM, em um forno de resistência. Para a análise das propriedades da escória, foram realizadas simulações através do software de termodinâmica computacional FactSage 7.2 e análises de imagens obtidas da superfície do cadinho ao final dos experimentos no software Quantikov. A mistura M1 apresentou melhor desempenho do que as misturas em todas as situações estudadas, sendo observado que melhores condições experimentais foram a utilização de 70g de mistura, a uma temperatura de 1400ºC, com a metodologia padrão de adição de toda a massa da mistura no início do experimento.

Oct 1, 2019

By Raphaella Hermont Fonseca Murta

O ensaio não destrutivo por ultrassom é amplamente utilizado para detectar e dimensionar descontinuidades no interior do material. A técnica TOFD (Time Of Flight Diffraction [do inglês]) foi a técnica ultrassônica utilizada. Entretanto, a classificação do tipo de descontinuidade, a partir dos sinais ultrassônicos obtidos durante uma inspeção requer um profissional altamente capacitado. Esta tarefa pode ser realizada por algoritmos de reconhecimento de padrões, capazes de processar rapidamente uma grande quantidade de dados. Nesse trabalho, foram simulados três tipos de descontinuidades em juntas soldadas: falta de penetração, poro e trinca, utilizando-se o Método dos Volumes Finitos (MVF). Em seguida, foi aplicado o método de reconhecimento de padrões K-vizinhos mais próximos (K-NN – K-nearest neighbors [do inglês]), para verificar como esses dados são separados. Esse trabalho é um passo inicial para o emprego de simulação numérica do ensaio ultrassônico para produzir sinais simulados e utilizá-los no treinamento de ferramentas de reconhecimento de padrão, a serem futuramente testados com sinais ultrassônicos experimentais. O K-NN classificou bem os sinais simulados. Conseguindo uma taxa média de acerto de aproximadamente 84%.

Oct 30, 2017

By Isabela Santana de Oliveira

O aço inoxidável 304L pode apresentar uma característica particular: transformações de fase induzidas por deformação, o efeito TRIP (Transformation Induced Plasticity) que possui embasamento na transformação martensítica. Neste trabalho propõe-se analisar o perfil de formação de martensita em corpos de prova submetidos a ensaio CLC (Curva Limite de Conformação), segundo o método Marciniak, nas regiões junto à trinca e distantes da mesma através de uma sonda portátil de um ferritoscópio. Utilizando técnicas de difração de Raios-X (DRX) e ensaios de dureza Vickers pode-se correlacionar a evolução microestrutural e valores de dureza nessas mesmas regiões ao grau de encruamento da austenita e a formação de martensita.

Aug 7, 2018

By R. L. Grayson

"Compliance standards for respirable dust, which are reduced because of high quart: concentrations, have become an industry-wide problem. Research on the physical and chemical character of quart-classified particles in respirable coal mine dusts indicates that they may exist in intermixed layers or may be coated by clay or coal material. The relative amount of intermixing varies with the coal seam being mined. If most of the quart: particles of a mine dust are ""pure,"" then the dust may have a high fibrogenic risk potential because of truly free silica and the compliance standard should be lowered. lf, however, quart: is locked inside another material matrix, or coated, a reduced compliance standard may not be appropriate.Although much research has been done on coal workers' pneumoconiosis (CWP) over the past decades, the etiologic agents of the disease still have not been pinpointed. The predominant methods of characterizing respirable coal mine dusts were bulk analysis techniques for determination of elemental and mineralogical concentrations, the results of which were used in statistical analyses to determine relationships between dust composition and the occurrence of CWP. These methods are incapable of finding the etiologic agents in the dust primarily because of complicated and confounding physiochemical factors, which may be discovered if the focus of characterization was done on a dust particle level.The SEM/EDXA-based research discussed here shows a significant difference in the number of ""pure"" quartz particles in respirable dusts collected from different mines. Some of the results have been reported previously (Grayson, Andre, and Simonyi, 1988). Concurrent research by other investigators (Wallace et al., 1989) demonstrates an SEM/EDXA-based methodology to pinpoint the location of the ""contaminating"" substance(s ) in a quartz-classified particle. The research of the European Economic Community has also begun analyses on the respirable-dust-particle level (Robock and Bauer, 1988).Since the compensatory and intangible costs of CWP are substantial in the United States, it is important that the etiologic agents be determined and then either controlled or neutralized in a cost-effective way. This line of research is especially important consid-ering the forecasted. near-term growth of coal production and the evolution of high productivity longwall panels (an immediate problem in compliance) and continuous mining sections ( a probable future problem).This need has been accentuated now that nearly all respirable dust samples submitted to MSHA are analyzed for free silica (Tomb, Parobeck, and Gem, 1986). Today a real problem exists in the coal industry, both underground and surface, because of high quartz levels in respirable dusts causing substantially reduced compliance standards (Murphy, 1989).The combined results of the respirable dust particle investigators indicate that conventional bulk sample analyses may not faithfully represent the amount of biologically available or active quartz in all mines with a high level (greater than 5% ) of quartz in the dust For example, some mine dusts might contain predominantly occluded (or coated) quartz particles where bulk analysis would result in anomalously high ""free silica"" measurements. The same result would occur when quartz particles are intermixed substantially with other minerals that can alter the surface of the composite particle away from a quartz-behaving character."

Mar 1, 1992

By W. F. Faragher

The principal equipment in the catalyst plants at Ludwigshafen-Oppau was inspected and is presented in the form of flow sheets for the manufacture of four of the principal catalysts. The equipment is in many cases of special design rather than stock items that was built by the company and modified in the coarse of the growth of the high-pressure synthesis of hydrocarbons in Germany. It is believed that if the manufacture of catalysts were to be undertaken elsewhere, the selection of equipment for the operations involved could be made successfully from the guidance furnished by this rather general report. Five additional catalysts are described, also. II. CATALYST 5058 FROM FRESH TUNGSTIC ACID In a supply tank of about 2,000 liters capacity, 500 kg. of tungstic acid (W03.H2O) that contains about 92-93 percent of W03 is dissolved at 60-70° C. in 1,500 liters of mother liquor. The solution is-effected by stirring for about 1-1/2 hours. The mother liquor is obtained from a previous, lot of catalyst and is first adjusted to a concentration of 13 percent 1H3 by passing in gaseous ammonia. The solution is allowed to stand without stirring for 1 hour, then is pumped into the saturating vessel through a cloth filter (three-quarters hr. to one hr.). The saturator is purged with H2S and thereafter the solution, which has been cooled to about 75° C., is heated in an atmosphere of hydrogen sulfide with stirring to about 70° C. This charge is slowly cooled to 50°, and then more rapidly to about 20° C. (time of cooling 6-7 hours).

Jan 1, 1946

[I-Institute of Metals Division PAUL D. MERICA, Chairman ZAY JEFFRIES, Vice-chairman W. M. CORSE, Secretary General Committee ROBERT J. ANDERSON H. C. JENNISON L. W. SPRING WILLIAN K. FRANK DAVID LEVINGER R. L. SUHL J. R. FREEMAN, JR. PAUL McKINNEY R. F. WOOD]

Jan 1, 1928

By Lenny Winkel

With the aim to develop a solar-driven process for the extraction of copper from sulfide concentrates research on the decomposition of copper sulfides under inert atmospheres has been initiated. Thermogravimetric measurements on chalcocite (CuzS) revealed that copper is formed already at 1823 K. Chalcopyrite (CuFeS2) also disintegrates at this temperature, although at a lower rate. Copper and iron have been identified in the solid residue. The results confirm the feasibility of copper extraction by direct decomposition of sulfides under atmospheric pressure. The decomposition under inert atmosphere prevents generation of SO2, it also alters the behavior of volatile impurities during decomposition of copper sulfide concentrates. Chemical eqUilibrium calculations for chalcopyrite contaminated with enargite (Cu3AsS4) have shown that the absence of an oxidic slag allows for a complete evaporation of arsenic and subsequent separation from intermediate sulfides. The need to better assess the potential of direct sulfide decomposition has prompted the development of an experimental setup for studying the decomposition reactions. The experiment has been devised such that data on the decomposition kinetics and on impurity removal can be obtained at temperatures up to 2500 K.

Jan 1, 2003

By Y. C. Kim

This paper describes the implementation aspect of a blast hole kriging system which has been developed for the purpose of daily ore-waste control in an open pit mine. The primary goal of blast hole kriging is to improve the ore-waste delineation procedure. A complete computer program package called Blast Hole Kriging (BHK) System was developed for IBM/PC AT or XT computer, using Fortran language and supplemented by a few Assembly language routines for bit-map manipulation. The emphasis of this paper is on the implementation aspect of the developed system. For this reason, the requirements for practical implementation and the system design considerations are discussed in the paper, as well as the main features of the University of Arizona's BHK System.

Jan 1, 1990

By Frank C. Stevens

Many changes have taken place in the "World Cement Market" since Joseph Aspdin discovered portland cement in the early 1800's. At the turn of the century, production of cement world wide was a few million tons; today, it is over one billion tons. By 1995, world production is estimated to reach 1.2 billion tons. Cement processing has changed from inefficient, small vertical kilns to large efficient, precalcining kilns, and large automated crushing, blending and grinding systems. Consequently the cost of production has declined in real terms, resulting in significant economic benefits to the general public. In addition, quality and uniformity of cement have increased, strengths have increased, and at least 25% fewer pounds of cement are needed for each cubic yard of concrete. Today, cement moves thousands of miles on the inland rivers and great lakes of the U. S., across Siberia and across the oceans of the world. The volume of cement moving more than a few hundred miles is almost 100 million tons, or 10% of world production. Today, on a per ton basis, it costs no more to move 40,000 tons of cement to the United States from the Western Pacific rim or from Europe than it does to truck cement 200 miles. For example, cement shipped by water from Spain costs $5.00 to $7.00 per ton compared to cement shipped by truck 200 miles at $16.00 per ton. This low cost water transportation has been a major factor for the increased movement of cement between countries. Table 1, Cement Production Summary-World, gives a global picture of production, export and import tonnages in recent years. Figure 1 is a graph showing CEMENT PRODUCTION SUMMARY WORLD WIDE.

Jan 1, 1987

By Frank A. Peters

This Bureau of Mines report is the second of a series of process evaluations planned to determine the relative processing costs of producing metallurgical-grade alumina from low-grade aluminous materials. Included in these evaluations are recommendations for additional research and development to improve the processes and to lower their costs. The design for each process is based on published work. The processes considered in this report are designed to extract alumina as aluminum chloride from calcined clay with 20 percent hydrochloric acid and to remove the silica residue by filtration. Iron is removed by one of the following processes: Isopropyl ether extraction, in which iron chloride is extracted before decomposing the aluminum chloride; gas precipitation, in which the aluminum chloride is precipitated with hydrogen chloride while leaving the iron chloride in solution; gas precipitation-isopropyl ether extraction, in which the aluminum chloride from precipitation is extracted with isopropyl ether, if necessary; caustic purification, in which a crude alumina is produced and then purified by a modified Bayer operation; or sinter purification, in which a crude alumina is produced and then purified by a lime-soda sinter operation. For plants producing 1,000 tons of alumina a day the estimated operating costs per ton of alumina are: [Isopropyl ether extraction process $ 65.09 Gas precipitation process 89.04 Gas precipitation-isopropyl ether extraction process 119.65 Caustic purification process 73.79 Sinter purification process 80.47] The estimated fixed capital costs per annual ton for these plants on a Marshall and Stevens chemical equipment basis of 240.0 are: [Isopropyl ether extraction process $229.03 Gas precipitation process 287.16 Gas precipitation-isopropyl ether extraction process 356.59 Caustic purification process 266.48 Sinter purification process 279.13]

Jan 1, 1962

Flotation works very well for particles that are typically in the range 20 to 150 µmin diameter, for base metal ores. In this range, it is possible to get quite high recoveries in conventional flotation machines. Outside this range, the recoveries decline progressively, whether it be with the very fine or the coarse end of the size spectrum. In this paper, the reasons for the drop-off in recovery are briefly reviewed, together with strategies for future work. Recent progress in the author's laboratory will be described. These include the Concorde Cell, which takes advantage of the high dissipation rates in the shock wave created when a gas-liquid mixture reaches supersonic velocities. The environment thus created is very beneficial for the flotation of ultrafines. For coarse particles, the reasons for the drop-off in recovery can be related to the highly turbulent nature of the pulp in a conventional flotation cell. To improve recovery, it is necessary to find a way of bringing particles and bubbles into contact in a quiescent environment. A new process for coarse particle flotation will be described, in which a fluidized bed is created in the flotation cell. The flow conditions are very gentle, and the high solids concentration leads to rapid rates of capture of the particles. Experimental results are presented. It is apparent that the maximum floatable size for coal and minerals can be increased by a factor often over the limits found in current practice. Advances

Jan 1, 2009