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By Raphael Lemos

Durante o ano de 2008 foram observados diversos “Gap’s” no processo de lubrificação, tais como: alto consumo de graxa, lubrificação em excesso, degradação de sistemas centralizados, ausência de procedimentos, mão-de-obra sem o conhecimento adequado, entre outros. Dessa forma, o processo de lubrificação foi separado em cinco grandes grupos de atuação, sendo eles: seleção de lubrificantes, gestão do processo de lubrificação, sistemas centralizados, contaminações e vazamentos. Foram aplicadas as ferramentas do MASP (Método de análise e solução de problemas) sendo a primeira delas o "Brainstorming", nos valendo das observações realizadas no Laminador de tiras a quente nº 2. Em sequência foi definido e implantado o plano de ação. Os resultados obtidos após as ações foram: a redução do tempo de parada associada a problemas de lubrificação dos equipamentos do LTQ#2, redução média de consumo de graxa no laminador de - 6.277 kg/mês, quando comparamos a média de consumo do período de Novembro de 2010 a Outubro de 2013, frente ao consumo atual no período de Novembro de 2013 a Outubro de 2014, totalizando uma redução média de aproximadamente - 75.321 kg nos últimos 12 meses.

Aug 16, 2017

By Izabelle Lannes Salgueiro Ferreira

O presente trabalho tem o objetivo de mostrar como sistemas especialistas melhoram a gestão da qualidade e processos ao trabalhar com grandes massas de dados, que são gerados continuamente pelos processos produtivos de laminação a quente.

Aug 17, 2017

By Karl Kristian Bagger

A construção naval sofreu nos últimos 40 anos várias mudanças de acordo com os diferentes cenários econômicos. O Brasil neste setor chegou a ocupar o segundo lugar na produção mundial, foi fortemente afetado pela crise recente. Diante desta conjuntura as empresas tem que otimizar seus processos visando um aumento na produtividade para se manter competitivas. A atividade da construção naval é complexa, tem várias etapas que geram interferências que muitas vezes impossibilitam trabalhos em paralelo. As chapas de aço que constituem as partes principais da embarcação, as estruturais, devem passar por um tratamento de preparação da superfície que inclui a sua pintura e proteção anticorrosiva, este é um dos processos mais críticos. Esta etapa além de demandar serviços muito especializados há ainda um aspecto agravante o ambiente confinado, que expõe os operários executantes a condições ergonômicas desfavoráveis proporcionando um rendimento baixo afetando diretamente a produtividade do processo. Este estudo realizou uma analise do processo e propôs as alterações nas etapas de fabricação eliminando os problemas proporcionando melhores condições de trabalho dessa forma minimizando o impactos ergonômicos, proporcionando redução de custo e aumento da produtividade.

Oct 30, 2017

By Artur Frederico Fonseca da Cruz

Com a necessidade urgente e constante de aumento da competitividade no cenário atual da mineração, mostra-se fundamental o desenvolvimento constante de novos parâmetros de processo combinados a uma estratégia de manutenção focada não só na disponibilidade dos ativos, e sim no desempenho dos equipamentos. No que tange ao processo de pelotização neste trabalho foi dado foco especificamente na configuração de perfis de queima no forno de grelha móvel, onde foram testados quatro perfis e fixado o perfil nº 04 otimizado via sistema de otimização de processo para níveis de produções diferentes, equilibrando qualidade e consumo específico de gás natural, no período anterior e posterior à parada fria. A partir daí foram analisados parâmetros de qualidade, produção e processo, comparando-os entre antes e após a parada fria. Foram registradas melhoras nos índices de qualidade e redução de aproximadamente 13,50% do consumo específico de gás natural e 10,80% de redução no consumo específico de energia elétrica de ventiladores por níveis de produção.

Aug 17, 2017

By Luis Alberto Sfalsin Passos

A aglomeração de minério de ferro para formação de pelotas é um processo dinâmico e seu controle é complexo. No controle manual o operador local é responsável pelos ajustes no processo e o tempo e a proporção de suas atuações dependem da percepção de cada um. Logo, o controle manual do processo é feito de forma individual e não padronizada e frequentemente não atende satisfatoriamente o controle da taxa de crescimento da pelota crua. Este artigo apresenta uma alternativa de controle automatizada, padronizada e otimizada da taxa de crescimento da pelota crua nos discos de pelotização. O “Sistema de Controle Avançado de Processo”, denominado SCAP, consiste em um controle multivariável baseado em ferramentas de controle convencionais e lógica nebulosa, que simula o pensamento humano nas tomadas decisão. As regras foram construídas e fundamentadas em conhecimentos previamente adquiridos por especialistas do processo. Verificou-se após a implantação um aumento do desempenho do processo produtivo. No âmbito das melhorias, destacam-se: redução de pelotas fora da especificação (granulometria), redução do consumo de insumos (agentes aglomerantes, gás natural, entre outros), melhoria na qualidade do produto final e aumento da produtividade.

Aug 1, 2018

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 Vander de Angeli

Em 2014 houve necessidade de substituição precoce de Caixas de refrigeração no Alto Forno devido a vazamentos provocados por defeitos de fundição ocasionando perda de produção. Após análise das falhas no componente, a oficina de fundição da ArcelorMittal Tubarão na busca contínua pela excelência na qualidade de seus produtos, propôs o desenvolvimento de um novo projeto de fundição visando atingimento de nível radiográfico = 3 nas caixas de refrigeração conforme critério de aceitação estabelecido na Norma ASTM E272. Para atingir o objetivo proposto foram inseridos no novo projeto itens para melhorar o processo de alimentação e solidificação do metal. Como resultado o novo projeto apresentou melhora significativa na qualidade do componente do sistema de insuflação de ar do Alto Forno atingindo níveis radiográficos que atendam as exigências da Norma.

Aug 16, 2017

By Guilherme Monteiro Garcia

O resfriamento contínuo de forma controlada garante propriedades mecânicas específicas nos aços. Este trabalho apresenta melhorias feitas em um sistema de controle de resfriamento em um laminador de tiras a quente. As melhorias apresentadas garantiram uma melhora na performance de 5% de forma a reduzir drasticamente o custo da não qualidade. As modificações visaram adaptar o sistema para uma nova realidade de grandes acelerações e desacelerações da tira no trem acabador visto o aumento da produtividade e a redução do uso da coil box.

Aug 17, 2017

By John J. Dunkley

Recent years have seen the increased use of hydrometallurgy in the smelting and refining of metals. However this is often used as a final refining step, following an initial pyrometallurgical smelting process. Huge amounts of material are produced as melts which have to be cast, comminuted, and taken up into solution or leached. A common method is to granulate the melt and then grind it. In the case of metallic melts this can be difficult or unfeasible due to the ductility of the granulated particles. Water atomisation is capable of replacing the granulation and grinding stages with a single process step that can process in excess of 30t/hour of melt into particles as fine as 50 microns. Applications in operation in Co, Cu, Ni, Ag, Au, Pt and Rh refining are discussed together with potential applications in copper smelting.

Jan 1, 2003

By John J. Dunkley

Recent years have seen the increased use of hydrometallurgy in the smelting and refining of metals. However this is often used as a final refining step, following an initial pyrometallurgical smelting process. Huge amounts of material are produced as melts which have to be cast, comminuted, and taken up into solution or leached. A common method is to granulate the melt and then grind it. In the case of metallic melts this can be difficult or unfeasible due to the ductility of the granulated particles. Water atomisation is capable of replacing the granulation and grinding stages with a single process step that can process in excess of 30tlhour of melt into particles as fine as 50 microns. Applications in operation in Co, Cu, Ni, Ag, Au, Pt and Rh refining are discussed together with potential applications in copper smelting.

Jan 1, 2003

By Olaf Andersen

Crucible melt extraction yields short metal fibers with eqivalent diameters as low as 50 µm from almost arbitrary metals and alloys. Highly porous components can be made from such fibers by suitable deposition and sintering methods. This technology is being developed at the Dresden based Department of Powder Metallurgy and Composite Materials of the Fraunhofer Institute for Manufacturing and Advanced Materials (IFAM) and has been applied to gold alloys and iron-base alloys containing small additions of precious metals. From the manufactured gold fibers, sintered structures were made for decorative applications. Additionally, it was found that due to rapid solidification during the fiber formation, precious metals can be finely dispersed in ironchromium- aluminum (FeCrAl) and FeAl20 alloys. Good catalytic activity at elevated temperatures was found in compositions containing 3 wt.-% Ce and 0.5 wt.-% Pt.

Oct 1, 2003

By T. -M. Guo, M. J. Braun

"This paper presents an experimental and numerical study of melt flow near the solid-liquid interface and its effect on the interface curvature in a horizontal unidirectional solidification system with succinonitrile. Melt flow is introduced by increasing the ampoule channel thickness. Visualization techniques are employed to observe the flow field and the solid-liquid interface curvature. A numerical model is also developed to simulate the heat transfer, melt flow and phase change in the system. Quantitative information on the flow and temperature fields is generated. A good agreement is achieved between the experimental observations and model predictions. The results could be used for the study of the effect of the melt flow on interface morphology during solidification.IntroductionClassic unidirectional solidification experiments of transparent alloys are conducted with thin film samples sandwiched between two glass slides to investigate the development of interface morphology during solidification [1]. Samples with small channel thickness are usually used to suppress any melt flow due to natural convection and solidification in the channel would then be in the diffusive regime so that the solidification theory can be significantly simplified [2, 3]. Effects of melt flow, in particular due to natural convection, on solidification have also been studied extensively in those systems with large geometrical dimensions [4-6]. These studies indicate a strong effect of the melt flow on interface curvature during solidification [5, 6]. Only limited efforts were made to address the effect of the melt flow on interface morphology in horizontal unidirectional solidification, in particular for the cases when the channel thickness is not thin enough to suppress completely the natural convection [7]."

Jan 1, 2004

By Ian J. Graham

Brothers volcano, in the southern Kermadec Arc, is host to two hydrothermal vent fields with very different geology, permeability, vent fluid compositions and mineralogy (see de Ronde et al. and Ditchburn et al. this volume). The NW caldera site contains mineral deposits (sulfide chimneys and crusts), which are either Cu-rich (?magmatic?) or, more commonly, Zn-rich (?epithermal?). The lower cone site, in contrast, is characterized by native sulfur mounds and spires. It has been proposed (see de Ronde et al. this volume) that the metals, especially Cu and possibly also Au, enter the hydrothermal system via injection and degassing of magma and/or the dissolution of metal-rich glasses. They are then transported rapidly upwards via magmatic volatiles along long (c. 2.5 km), narrow (c. 300 m diameter) pipes, consistent with evidence of vent fluids forming at higher than hydrostatic pressures, at relatively shallow depths. The NW caldera and cone sites may represent stages along a continuum between magmatic-hydrothermal and water/rock-dominated end-members. In this context, investigation of melt inclusions in conjunction with other geochemical and petrological research was carried out to ascertain the metal transporting conditions that may have led to mineral deposition and ore formation. Sixteen melt inclusions in plagioclase were analyzed for their chemical compositions from a typical cone dacite sample using LA-ICPMS at the University of Tasmania. The inclusions are typically glassy and commonly occur with other inclusions such as apatite, clinopyroxene, zircon, magnetite, sulfides and/or low-density fluids (Fig. 1). Major (XRF) and trace element (ICPMS) analyses were performed on whole rock samples collected during the 2005 Shinkai 6500 expedition. Haase et al., (2006) has also reported EPMA glass analyses from cone dacites, which may be used for comparison (Table 1). [ ]

Jan 1, 2010

By Knut H. Bech, Stein Tore Johansen

"The collision efficiency for small particles relative to 2D spherical bubbles in a developed turbulent flow field were calculated applying an adopted version of the CPD program FLUENT. The turbulence field was related to bubble size and fluid properties. The results were compared with analytical theory. The turbulence intensity was found to be the most important single parameter for collision efficiency. Effects of boundary layer thickness and particle diameter were discussed. IntroductionRemoval of inclusion particles from melted aluminium can be facilitated by means of a rotor system that supplies kinetic energy and gas bubbles to the floating metal. At the surface the inclusions adhere to the surface dross or slagg which is removed at regular intervals by the operators. When applying computational fluid dynamics (CFD) to model such a system, one experiences difficulties with the large range of turbulent length-scales encountered, from the large geometrical scales of the rotor and container, through the bubble size and down to the particle diameter. A mathematical model for the complete system will be both complex and require an extreme spatial resolution. Another way of dealing with the problem is to model the micro-scale phenomena separately and apply the results to create a model for the macroscopic system. In a previous work [12] we addressed these problems and developed a procedure for calculating turbulence enhanced flotation to bubbles. It was found that turbulence may have a profound effect on the collision rate of particles to idealized bubbles. In this study we recognize that only a fraction of the total turbulent kinetic energy generated by the rotor's work on the liquid metal may contribute to enhanced flotation. By using a model spectrum for the turbulence, the fraction of turbulent energy in eddies smaller than the bubble diameter is calculated. A twodimensional CFD model was then constructed to calculate the collision efficiency between particles and bubbles of various sizes."

Jan 1, 1999

By Edward Capillon

THE problem of scrap is probably of greater importance inn the production of gold, silver and other precious metal alloys than is the case for base metals and alloys. Remelting of gold and silver scrap in the shop is always a costly process because it involves losses by oxidation of the base metals in the alloy with a consequent increase in the percentage of precious metal. This is most marked in the case of alloys containing the low-boiling and easily oxidized metals zinc and cadmium. Since it is. not generally feasible to assay every shop remelt it follows that the possibilities of lost values are large. So-called rolled gold and silver plate is made by soldering or welding the precious metal alloys onto base, metal. Such plate when defective must be sent to the refinery to recover the gold and silver values, thereby involving additional expense in the form of refining charges. It is obvious therefore that gold and silver alloy scrap is an important item in manufacturing cost and must be reduced to a minimum. The amount of scrap resulting from poor metal will depend on a number of factors in the manufacturing operations, not least among which is the melting and casting practice. The notes which follow are a summary of experiments performed at various times to determine what variables in melting and casting are influential in the production of sound alloys.

Jan 1, 1930

By B. Larsen, S. Z. Nascimento, K. Fidje, J. P. M. Amaro, H. Gran

Safe and good operation of Søderberg electrodes is dependent upon high quality electrode paste coupled with correct electrode operating procedures. Good electrode performance depends further on proper melting and densification of the electrode paste. The melted paste should form a dense and viscous layer that prevents gasses from the baking process to move upwards. Both paste cylinders/blocks and briquettes can be used, but the procedures may differ between the various types of paste products. For briquette columns the formation of the important viscous layer is obtained through melting and densification of the briquettes. By basic rheological studies of electrode paste and by laboratory tests of briquette beds at isothermal conditions we have achieved a better understanding of the melting process. The effects of temperature gradients, pressure and friction between the briquettes and the electrode casing have also been evaluated qualitatively in pilot scale experiment and in industrial scale tests. The paper shows that melting and densification starts at a considerable lower temperature than the pitch softening temperature. It is concluded that the formation of a briquette electrode column depends on parameters as temperature, briquette column pressure and the friction. Operating conditions influencing the above parameters should be defined and established for each specific furnace operation. Such factors are e.g., charging and slipping procedures, column heating and electrical conditions.

Jan 1, 2004

By Gilberto Álvares da Silva

New elements have been inserted in NiTi lately, resulting in ternary alloys with specific characteristics beyond Shape Memory Effect and Superelasticity. Among all others alloying elements, the Ag additions itself gives potential antibacterial activity to that smart material. So on, the elaboration procedures of ternary NiTiAg alloys was studied in order to obtain a melting procedure to ensure further studies on this alloy. Microstructural and thermal analyses were used to evaluate the VAR-remelting production of NiTiAg with 4.0% wt silver content. The microstructure is composed by a NiTi matrix, pure Ag precipitates, and, scarcely, TiC inclusions. Heat treatments at high temperature could not dilute those Ag particles, but could lead to the precipitation of new ones. The silver element reduces the temperature of the martensitic transformation, yielding a material with superelastic behavior, beyond induces the R-phase on cooling stage of this alloy.

Aug 8, 2018

By Guo Xian Jian

In this paper, the effects of matte grade, flux grain size, blast flowrate and blast O2 content on the process of silica flux melting in a copper converter were investigated. The results showed that the blast flowrate and the blast 02 content were not significant factors in the melting process. However, with an increase in grain size of flux and grade of matte, the amount of the flux molten decreased. The data on the melt rate of process correspond well with the mathematical model which simulates the chemical reactions occurring at the interface. The kinetic equations of melting are as follow:

Jan 1, 1996

By K. Krishnapisharody, S. Clark, M. Barati

Different gas purging methods to metallurgical baths have been applied to date, among which are top lancing and bottom blowing through tuyeres or porous plugs. Among these, the porous plug bottom blowing technique has shown higher efficiency in gas utilization than tuyeres and top blowing, due to smaller bubble size and lower liquid velocity. However, the studies related to bottom stirring of metallurgical baths are limited to slag-less or thin slag-covered melts. In particular, there is no examination of stirring ability in conditions similar to Falconbridge's Slag Make Converter, where the bath is covered with a thick slag layer and a stream of solids is charged on the bath from top. This study was undertaken to investigate the application of gas purging through a porous plug in stirring in and melting of the solid feeds. The spreading behaviour and melting time of a solid layer forming on a plume created by stirring were calculated using the existing models. The results show that formation of a thick solid layer, specifically in areas beyond the plume region is very likely. Nevertheless, the thickness of the layer and melting time do not appear unreasonably high. It is predicted that by proper controlling of gas flowrate and plug configurations, successful solid charging through the mouth can be practiced.

Jan 1, 2007

By T. W. Bossert

MELTING is the initial step in the fabricating of all aluminum and aluminum-alloy products. Its function may be considered as threefold: to improve the metal quality, to adjust the composition, and to change the form to that required for subsequent fabrication. Because the melting operation is generally somewhat removed from the final product fabrication, its importance is frequently overlooked. Melting equipment and melting procedures can reflect materially on fabricating procedures as well as on quality and cost of final product. The selection of equipment and the establishment and control of melting procedures, therefore, should be given careful consideration. It is the purpose of this paper to present the various factors that should be considered in establishing melting procedures and in selecting melting equipment. Certain of these are the result of the inherent characteristics of aluminum and can be treated rather specifically. Others depend on the particular production requirements and hence will have to be considered more generally. This paper is intended to cover only the melting of solids, as differentiated from fines, such as borings, turnings, and sawdust. The melting of fines, in many respects, is a subject that should be treated by itself, and practices for melting fines are by no means as standardized as are those for melting solids. The melting of fines is today the subject of considerable developmental interest; hence practices discussed today may soon be replaced by new or improved ones. CHARACTERISTICS OF THE METAL THAT AFFECT MELTING Aluminum and aluminum alloys possess several inherent characteristics that affect the melting problem. Of the physical properties, density, heat content, thermal conductivity, emissivity, and melting temperatures are important because of their effect on equipment design. A list of such properties for commercially pure aluminum is given in Table r, compared with similar properties for iron and copper. The low density of aluminum as well as of the aluminum alloys is of material advantage in the design of melting equipment, in that such equipment can be considerably lighter than similar equipment for handling the heavier metals. The density, however, particularly of the molten metal, is not greatly different from that of the oxides and other nonmetallic materials that develop or become part of the melt during the melting process. Separation of such nonmetallics is not as rapid a process as with some of the other metals, and consideration of this must be made in establishing melting procedures. Sufficient holding time to permit such materials to separate out and, in some cases, fluxing treatments to aid the separation, are required. Since some of these nonmetallics settle to the bottom of the melt, provision should also be

Jan 1, 1946