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By J. Chipman, N. J. Grant, H. L. Bishop

In a recent review1 of the iron-oxide activity of simple open-hearth type slags containing lime, magnesia, silica, and iron oxide, it was established that activity values were lacking in the range of slag composition most interesting to open-hearth operators. That is, laboratory experimental results were not available for simple slag compositions having basicity ratios ranging from about 1.5 to 4.0 and iron-oxide concentrations ranging from about 10 to 30 pct. However, in order to estimate iron-oxide activities for the range of slag compositions of interest to open-hearth operators, activity values were calculated using ionic concepts of slags by following the treatment of Flood and Grjotheim.2 A study of these data indicated that the desired slag compositions were probably not obtained due to the limited solubility of the basic constituents lime and magnesia. Thus, it was decided to make additional heats equilibrating molten carbon-free iron with slags containing MnO, P2O5, and A12O3 in percentages commonly found in open-hearth refining slags, and to examine the liquid slag field over a greater composition range than that of the simple slags studied previously. The ranges of the constituents used in the present study are summarized as follows: Metal Pct 0 0.070-0.201 PctMn 0.005-0.142 Slag Pet CaO 24.45-41.90 Pct MgO 3.23- 9.21 Pct MnO 1.13- 9.62 Pct FeO 20.08-48.7 Pet Fe2o3 2.23-10.14 Pct SiO, 3.51-28.50 Pct P2O5 0.23- 3.65 Pct A12O3 0.43- 3.38 The experimental procedure consisted of equilibrating the slag and metal in an induction furnace provided with a carbon-arc slag heater as described previously by Winkler and chipman.3 The data obtained were used to establish both the iron-oxide activity values and the activity coefficients for FeO and MnO in the open-hearth type slags. RESULTS AND DISCUSSION I) Iron-Oxide Activity of Open-Hearth Type Slags—The iron-oxide activities of various iron-oxide contents of the open-hearth type slags, as calculated from the oxygen content of the metal by the method of Taylor and Chipman, 4 are plotted against the molar ratio of bases to acids in Fig. 1. The data represent slag-metal studies carried out in the temperature range 1530" to 1700°C. For the purpose of this study, the constituents CaO, MgO, and MnO are assumed equal on a molar basis in their effect on the iron-oxide activity; and, PO2,5 is calculated as an equivalent to SiO2 and A12O3 on a molar basis. The total iron content of the slag is calculated to FeO and is represented by the symbol (FeO) The points presented in Fig. 1 represent the results of this investigation for iron-oxide slags containing between 1 and 8 mol pct MnO and less than about 2 mol pct each of A12o3 and PO2,5 The curved lines shown in Fig. 1 represent the results of the summary1 of the iron-oxide activities of simple slags of the system (CaO + MgO) - SiOz - (FeO),. The solid portions of the curved lines represent experimental data, and the broken portions represent iron-oxide activities calculated from ionic concepts of slags. The iron-oxide values of the open-hearth type slags of this study are in good agreement with the values of the simple iron-oxide slag system. Only a slight modification is indicated. The results of this study suggest that the line for 20 mol pct (FeO), should be lowered slightly in the basicity range 1.5 to about 3.

Jan 1, 1959

By Antonio Augusto Gorni

O posicionamento de bobinas a quente com seu eixo na direção horizontal protege suas bordas, mas restringe sua área de apoio sobre o solo. Logo, é inevitável que a bobina sofra algum grau de ovalização pela ação de seu próprio peso, o qual se torna particularmente acentuado em algumas situações, como no caso de aços com médio e alto teor de carbono após bobinamento sob temperaturas relativamente altas. O objetivo desse trabalho foi identificar as possíveis contramedidas para minimizar o grau de ovalização das bobinas a quente. Foi constatado que a ocorrência desse problema é crítica para bobinas mais finas, com maior peso e com menor tensionamento entre as espiras, bem como quando seu bobinamento termina antes da transformação total da austenita, particularmente no caso de aços com alto carbono equivalente. Por outro lado, o posicionamento das bobinas em berços com ângulos otimizados contribui para minimizar a ovalização. A seleção das medidas a ser adotadas para reduzir esse problema deve ser ponderada caso a caso, pois elas podem eventualmente interferir com as características finais do produto solicitadas pelo cliente.

Jul 30, 2018

By Danielle Gonçalves Campos

Com o ensaio de RDI (Índice de Degradação sob Redução), pode-se determinar a geração de finos durante a redução da carga metálica no alto-forno, e com o RI (Índice de Redutibilidade) determina-se a capacidade do sínter em ceder oxigênio para o gás redutor. São ensaios de extrema importância, pois com o RDI é possível medir a degradação do sínter quando submetido a condições redutoras do alto-forno, e com o RI entende-se o grau de redução da carga metálica momentos antes do início de seu processo de amolecimento. Com a instalação deste forno no Laboratório de Redução da CSN, será possível correlacionar os componentes do sínter, e de outras cargas metálicas, avaliando suas influências no produto, e, consequentemente, em suas utilizações no alto-forno.

Aug 1, 2018

By Elaynne Rohem Peçanha

Com o objetivo de estudar a interação da hematita com biorreagente de flotação (Bacillus subtilis), foram realizados experimentos de ângulo de contato. Após a interação com o biorreagente, a superfície da hematita apresentou uma hidrofobicidade apresentando um valor de 46,0º. Os experimentos de potencial zeta mostraram uma interação acentuada entre o reagente e o mineral na faixa de pH alcalina com deslocamento do ponto isoelétrico da hematita. Ensaios de microflotação foram conduzidos em tubo de Hallimond modificado, em pH 6, com uma recuperação de, aproximadamente, 80%. As teorias DLVO e X-DLVO foram aplicadas para avaliar as energias de interação entre o reagente e os minerais. As duas teorias foram capazes de prever a interação que ocorre entre o biorreagente e a hematita. Os resultados evidenciaram o uso promissor do reagente na flotação direta de hematita.

Aug 17, 2017

By Marcilio do Carmo Silva

O circuito de flotação de Fábrica Nova é composto por três colunas de quatro metros de diâmetro e quinze de altura, equipadas com sparger’s tipo retrofit (misturadores), utilizando uma mistura de ar e polpa para geração de bolhas. As colunas operam em paralelo constituindo o estágio rougher. Os produtos gerados neste estágio são tratados em células convencionais (cleaner e scavenger). Com o empobrecimento do ROM proveniente da Mina de Fábrica Nova e conseqüente aumento de SiO2 na alimentação da flotação, fez-se necessário ajuste no circuito com o intuito de garantirmos qualidade competitiva do pellet feed de Fábrica Nova. Foram feitas alterações de rota do rejeito do estágio rougher, direcionando o mesmo para o rejeito final (no circuito padrão o mesmo alimentava o estágio scavenger). O rejeito do rougher e o rejeito do scavenger compõem o rejeito final da flotação. Um ajuste no percentual de sólidos da alimentação da flotação foi necessário para favorecer a coleta da sílica (saindo da ordem de 58-60% para 53-54%). Com esta manobra conseguimos retirar o excesso de SiO2 do circuito de flotação, possibilitando a geração de pellet feed com qualidade dentro dos padrões VALE.

Aug 8, 2018

By Ricardo Miranda Alé

Aços resistentes ao serviço ácido (sour service), com requisitos adicionais de alta resistência mecânica e tenacidade, têm sido especificados para aplicação em gasodutos do Pólo Pré-sal da Bacia de Santos. O desenvolvimento de aços que atendam a estes severos requisitos, visando à fabricação de tubos de elevada espessura, constitui um enorme desafio para o fabricante do aço. No presente trabalho, é apresentado o desenvolvimento do aço API 5L-X65 Sour Service para esse tipo de aplicação, onde são descritas as principais ações realizadas no processo de produção que permitiram o sucesso no desenvolvimento do produto, confirmado pelas excelentes propriedades obtidas nas chapas e nos tubos.

Aug 8, 2018

At Copper Refineries Pty. Ltd., Townsville, two reverberatory furnaces of 420 tonnes capacity are used to melt 210000 tonnes/year of copper for subsequent anode casting. When the refinery commenced production in1959, these furnaces were of 300 tonnes capacity. The original furnaces featured a silica brick hearth, magnesite and chrome magnesite side 'walls, and a sprung silica brick roof, but were unsatisfactory because of thelow refractory life and high costs. With continuous expansion in production and the incentive to increase furnace life and capacity the design of these furnaces has changed greatly since that time.The present furnaces feature all basic brick, a flat suspended basic brick roof, very extensive use of watercooled copper sections, and are of substantially increased (420 tonnes) capacity. Particular attention has been concentrated on high wear areas such as the taphole, side walls, and charging door jambs. Each furnace in its 24 h cycle, is charged, the copper melted, impurities skimmed off, metal "poled" prior to casting, and cast.The service condition during each of these operations is important in considering furnace refractory life.The improvements in operating practices and furnace 'construction which enabled the capacity of the furnaces to be increased are discussed. The life between major repairs to side walls has increased from 90 charges to300 charges.The scope for future improvement is considered and areas for development are suggested.

Jan 1, 1977

By Zhibao Li, Kunming Zhai, Yan Zhang

The hydration kinetics of MgO, namely magnesia or magnesium oxide, obtained by calcination of magnesite MgCO3 or synthetic MgCO3·3H2O has been studied. Nesquehonite (MgCO3·3H2O) was prepared by the reaction of MgCl2 with Na2CO3 in a mixed-suspension mixed-product removal (MSMPR) crystallizer at 40 °C. Three magnesium oxide samples were obtained by calcination of magnesite MgCO3 or synthetic MgCO3·3H2O in muffle furnace at 900, 1100 and 1300 °C for 3 h, respectively. The hydration experiments of MgO samples were investigated at 25, 35 and 45 °C for 24 h in a stirred batch reactor. The hydration results indicate that the rate and extent of hydration of magnesia decreased remarkably with hydration temperature and increased with decreasing calcination temperature at a constant hydration temperature. The whole hydration reaction of magnesia was supposed to experience the promotive period and declining period. An empirical kinetic model ( k t p -?ln(1-??) ??) and a modification of the classical shrinking core model for diffusion control ( k t b d -?-?3 2 ????1 [1 (1 ??) ] ) have been applied to fit the experimental data of hydration in two stages, respectively. The values of kinetic parameters ( p k and d k ) were obtained by regression analysis and the activation energy of the sample at 900 °C was estimated to be 34.23 kJ/mol. The comparison between MgO from calcination of synthetic MgCO3·3H2O and a commercial MgO used in silicon steel production was carried out, indicating that special silicon steel grade MgO can be obtained by calcination of MgCO3·3H2O below 900 °C.

Jan 1, 2014

By José Wilmar Calderón-Hernández

Aços inoxidáveis supermartensíticos (AISM) surgiram em meados dos anos 1990, após algumas empresas petroleiras e centros de pesquisa empreenderem projetos para desenvolver aços inoxidáveis com boa resistência mecânica e resistência à corrosão. A força motriz destes projetos foi a procura de aços inoxidáveis alternativos para os aços duplex e superduplex na extração de reservas de petróleo “offshore”, devido a seu alto custo e a problemas de produção naquela época. Os AISM são derivados dos aços martensíticos inoxidáveis convencionais, possuem menor teor de carbono, para permitir melhor soldabilidade e melhorar a resistência à corrosão, adição de níquel para evitar a presencia de ferrita delta (d) e adição de Mo, que também aumenta a resistência à corrosão. Através de ensaios de polarização potenciodinâmica foi avaliada a resistência à corrosão de um AISM 13Cr-5Ni-2Mo, denominado neste trabalho como AIS_2Mo, para três diferentes ambientes, NaCl, NaCl+CO2 e NaCl+H2S (soluções desaeradas). O material foi recebido como chapas laminadas a quente, as quais foram normalizadas a 1.050°C (½ hora/ar) e posteriormente revenidas a 600°C (2 horas/óleo). O melhor desempenho foi observado no eletrólito contendo apenas NaCl, com potencial de pite ao redor de 40 mV (ECS); o ambiente mais agressivo foi a mistura NaCl+H2S, com potencial de pite ao redor de -300mV (ECS), a mistura NaCl+CO2 teve potencial de pite intermediário, com valor 60 mV (ECS) abaixo do eletrólito contendo só NaCl.

Aug 8, 2018

By André de Albuquerque Vicente

Foram estudadas as camadas de óxidos formadas nas superfícies de um aço inoxidável austenítico laminado do tipo 22.12, após oxidação ao ar a 800, 900, 1000 e 1100 °C, dentro de um projeto que visava uma melhor compreensão da oxidação a altas temperaturas ao ar de aços inoxidáveis resistentes a altas temperaturas. Utilizou-se o aço inoxidável austenítico microligado ao cério (253 MA®), que é um aço projetado para trabalhos a altas temperaturas. Várias técnicas complementares de análise microestrutural foram utilizadas, tais como difração de raios X e microscopia eletrônica de varredura com EDS acoplado. Observou-se a formação de uma camada não protetora de óxidos de ferro (Fe2O3, Fe3O4 e FeO) e posterior formação de uma camada protetora mais espessa de crômia (Cr2O3). Mais internamente observou-se a formação de SiO2.

Oct 30, 2017

By Amanda de Angelis Vitoi

Neste trabalho foi estudado o efeito da adição de argônio à atmosfera de nitretação sob plasma sobre a resistência à corrosão do aço inoxidável austenítico AISI 316L. As nitretações foram realizadas em reator a plasma pulsado, a 420°C, por 6 h, adicionando-se 0%, 5% e 10% de argônio à mistura gasosa. Os resultados mostraram que a adição de 5% de argônio promove um aumento na espessura da camada de austenita expandida em relação ao material nitretado sem argônio. Com o aumento da concentração de argônio de 5 para 10%, no entanto, verificou-se a formação de camadas de austenita expandida mais finas e de baixa resistência à corrosão devido à presença de nitreto de cromo em sua estrutura.

Aug 8, 2018

By João Lucas Lautenschlager Cortez Alves

Foi implementado um modelo matemático transiente e tridimensional para prever os campos de temperatura e composição presentes no sólido e poça de fusão durante um processo de soldagem a arco. O modelo foi desenvolvido com base nas equações de conservação macroscópicas de calor, massa e espécies químicas, que foram solucionadas pelo método dos volumes finitos. Os resultados do modelo mostraram boa aderência com soluções analíticas. Foram apresentados os efeitos de mudança na velocidade e potência de soldagem na distribuição de temperatura obtida e no formato da poça de fusão para soldagem em uma chapa de liga Al-6,5%Cu.

Oct 30, 2017

By Euler De Souza

Backfilling in Canadian mines has been practised for close to 100 years and evidence anticipates the application of mine fill technology at an increasing rate during the foreseeable future. The evolution of backfill technology is closely related to the advancement of modern mining methods and the development of new backfill technology continues to evolve. The authors, after conducting extensive surveys of backfill practices in underground mines across Canada, have concluded that, because backfill operations employ large quantities of cement and experience large costs associated both with backfilling practice and cement use, opportunities exist for reducing backfill energy costs and enhancing the application of alternative cementing agents in backfill. Consequently, the authors have developed an alternate, equally effective and lower cost binder agent replacement for cement, and incorporated waste glass into the development of a lower cost backfill (glassfill). This paper presents the results of two design stages associated with the development of glassfill: strength development and flow performance. The advancement of this technology has reached a stage that should promote industrial implementation within the Canadian mining industry. A number of Canadian mining operations exhibit potential for plant optimization through possible binder source replacement, and might thus realize associated reductions in backfill and energy costs.

Apr 1, 2005

By M. Prats

This paper presents a method for obtaining the correct values of the breakthrough sweep efficiency of the staggered line drive, taking into account the proper shape of the breakthrough streamline. Results obtained were different from those previously published, which were obtained by using an inexact shape of the breakrhrough streamline. INTRODUCTION In Section 9.31 of Muskat's' The Flow of Hotnogeticous Fluids Through Porous Media, it is stated that in a staggered line drive flood "the streamline of highest average velocity [is] the line of centers between input and output wells" (see Fig. I). Muskat used this concept to determine the relationship between the breakthrough sweep efficiency and the geometry of the staggered line drive pattern. Although it is clear from symmetry considerations that the breakthrough streamline passes through the midpoint between input and output wells, it is equally clear, as shown in Fig. 239 of Ref. 1, that the breakthrough streamline is not represented very well by the straight line joining the input and output wells. Therefore, it is desirable to determine the proper relationship between the breakthrough sweep efficiency and the pattern geometry by using the proper shape of the breakthrough streamline. METHOD OF SOLUTION It was found that the effect of the geometry of the staggered line drive on the breakthrough sweep efficiency can be investigated easily by making use of the method developed in Ref. 2. With this method, it can be shown that the general complex potential for the staggered line drive, which can be considered as a rectangular five-spot, is given in the coordinate system of Fig. 1, by O(z) = In cn(z\m) = +(x,y) + i $(x, y) . (1) where z = x + iy, +(x, y) is the potential distribution and $(x, y) is the stream function. The function cn (zm) is a Jacobian elliptic function of parameter m and has simple zeros at z,. = (2n + 1) K + 21iK and simple poles at z, = 2nK + (21 + 1)iK. Thus, the complex potential behaves like a(z) = ln(z - zr.) in the neighborhood of the production wells and behaves like a(z) = - ln(z - Z,) in the neighborhood of the injection wells. Since (z - z1.v) = rll.ei, we note that the potential + has the proper logarithmic behavior near the two wells, while the stream function $ varies with the angle, decreasing clockwise around the production well and increasing clockwise around the injection well. The functions K(m) and K'(tn), related by K(m) = K'(m,), where m + m, = 1, are known as the complete elliptic integrals of the first kind. By use of other properties of the Jacobian elliptic functions, the general stream function distribution for the staggered line drive can be obtained from Eq. 1: From the Jacobian elliptic function values, sn(0lm) = 0 dn(O(m) = cn(0jm) = 1, and f[K'(m)Iml = 03, it follows that the stream function given by Eq. 2 satisfies the proper symmetry conditions near a production well P located at [K(m), 01 and an injection well I located at [0, K' (m)]. That is, the line IOP in Fig. 1 is a streamline with value G (0. 0) = -0. and the straight lines connecting I and P to the point [K(m), K' (m)] is a streamline of value $[K(m), K' (m)] = -7/2. Similar symmetry conditions are obtained near other wells. It should be nuled that for m = m1, = 0.5, Eq. 2 reduces to the stream function distribution of the regular five-spot given in Ref. 7. SHAPE OF THE BREAKTHROUGH STREAMLINE It is apparent, from symmetry considerations, that the breakthrough streamline ($,) passes through the point [K(m)/2, K' (m)/2]. Its value there is so that the shape of the breakthrough streamline $,, is given by

Jan 1, 1957

By Akihiro Higashide, Roy H. Patten

The DOT Tunneling method combines two conventional earth pressure balance shield machines in an overlapping cylindrical arrangement. The method allows two tunnels to be driven simultaneously with mini¬mum cross sectional area. Two full size trials, one configured horizontally and one vertically stacked, were successfully completed employing the DOT method. The method was then utilized for the new transportation system. The goggle-shaped DOT machine, 9.36 m high by 15.86 m wide, is the largest earth pressure balance shield machine in the world. This paper includes a general description of the DOT tunneling method as well as a history of its development.

Jan 1, 1995

By D. Yu, Y. Thibault, D. Paktunc

"Prereduction and flux-aided direct reduction of chromite provide significant advantages in reducing energy consumption and greenhouse gas emissions during ferrochrome production. In this investigation, a comparative evaluation of the influences of several alkali fluxes was carried out based on experimental observations supplemented by advanced material characterization and thermodynamic predictions. Direct reduction of a chromite ore with alkali fluxes at 1300°C for 1 hour produced (Cr,Fe)7C3 type alloys with Cr/Fe mass ratios from 0.7 to 2.3. Among the alkali fluxes, reduction aided by NaOH resulted in a high degree (85%) of Cr metallization with the ferrochrome alloy being Cr4.2–4.6Fe2.4–2.8C3. The formation of liquid slag, which facilitated Cr metallization, was limited by the formation of NaAlO2 between 800 and 1300°C. This, in turn, restricted the collection and transport of the charged ionic Cr species (i.e. O2–) to graphite particles. Under the conditions studied, ferrochrome particles were often small and largely unliberated, which would make the physical recovery of ferrochrome challenging. At 1400°C, the amount of liquid slag increased, enabling the growth of alloy particles. Direct reduction of chromite aided by NaOH is promising as an alternative technology to conventional flux-based smelting in electric arc furnaces. IntroductionConventional smelting processes are energyintensive (Riekkola-Vanhanen, 1999) with the energy requirements greater than 4 MWh/t (Naiker and Riley, 2006; Beukes, van Zyl, and Neizel, 2015), and the greenhouse gas emissions can be significant, exceeding 10.5 t CO2 per ton Cr in ferrochrome produced (International Chromium Development Association, 2016). These include emissions occurring on-site (smelter), emissions due to electricity production, and emissions due to upstream processes. Overall energy requirements are influenced by the degree of prereduction and smelter charge temperature. Significant reduction in electricity consumption can be realized if the charge is prereduced before feeding to the submerged arc furnace (Niayesh and Fletcher, 1986). This consideration has led to the development of several prereduction technologies, with the most important example being the Premus process. In comparison to the conventional smelting processes, this prereduction process lowers the overall energy consumption and greenhouse gas emissions by about one-third (Naiker, 2007)."

Dec 1, 2018

By Ana Carolina Fernandes Reis

O objetivo do trabalho foi investigar a recuperação metalúrgica da flotação de sulfeto de ouro utilizando diferentes tamanhos de partículas, a partir de ensaios de moagem e flotação em bancada, visando analisar o melhor desempenho e seletividade do processo. O minério em estudo apresenta um teor médio de ouro de 5,28 ppm e 0,59% de S. Nos testes verificou-se uma correlação diretamente proporcional entre a recuperação mássica e metalúrgica, ambas mostraram-se inversamente proporcional a seletividade no concentrado. A granulometria com 90% passante na malha de 0,053mm obteve o melhor resultado de recuperação tanto do ouro como de sulfetos, em contra partida, apresentou o menor grau de seletividade.

Aug 16, 2017

By Kenneth G. Skinner, Hewitt Wilson, Thomas L. Hurst

Although chromite deposits occur in California , Oregon, Washington, Montana, Wyoming , Pennsylvania, Maryland , New Mexico , North Carolina, Alaska, and the Phillippine Islands , less than 1 percent of the ore used in the United States is obtained from these deposits . Most of the ore in peacetime has been supplied by imports from South Africa, New Caledonia, Turkey, and Cuba . The mineral chromite , the most important chromium ore , is an isometric spinel with an ideal composition of FeO Cr2O3 , but commercial chromite has the variable composition (Fe , Mg) Oʻ (Cr , Al , Fe) 203. Chromite has a black color , a specific gravity of 4.4 , and a hardness of 5.5 . In thin section the color is reddish -brown to black . Chromite occurs in dunite and pyroxenitic ultrabasic rocks , which are composed of iron- magnesium silicate minerals such as olivine , saxonite , serpentine , and enstatite . These are also the gangue minerals . Com mercial ore occurs at random in the country rock in kidney- or lens - shaped deposits , which have no apparent relationship to each other . Stringers , veins , and bands often cut the country rock without regard either to fracture or to other deposits . Some beach sands , such as those in southern Oregon, contain chromite .

Mar 1, 1943

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

Addicks, L Ambler, J O Anderson, F B Armstrong, T Allen, L M, Jr Arnold, C E Adams, C E Adams, R E Anderson, A J Booth, E L Bernhardt, D I Boyd, W S Browning, W C Blake, D E Black, T B Bergman, Julius Bowen, H P Beckett, P G Blickensdefer, F C Bond, Josiah Butler, P P Bondlas. Y

Jan 1, 1923