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By Luis Henrique Torres Dantas, Maycon Athayde, Rossano Augusto Pilon Nunes

The objective of this work is to evaluate the physical quality achieved in the iron ore pellets and the temperature profile in the pellet bed by applying an inversion in the flow during the cooling. The firing of pellets requires a minimum residence time in the sintering temperatures of the hematite grains [1]. The applied concept aims at raising this time to pellets located at the bottom of the bed which would provide an improvement in the physical quality of the product. The tests were carried out in a pot-grate type oven and the samples of fired pellets were divided into three aliquots according to the loading position of the pot termed top, middle and bottom, the pellets were sieved and subjected to physical tests and the compared to conventional indurating flow with the same ores and inputs. It was possible to show an increase of 7 to 8% in the compressive strength of the medium and bottom layers, maintaining the top layer results. The objectives of the research were achieved and the tests will be extended to assess the impacts on the mass and energy balance of the indurating machine and its components.

Oct 1, 2019

In recent years there have been many changes in mine ownership due to the on-going rationalisation towards larger mining companies. Larger companies inevitably find it hard to manage small mining operations and in many cases smaller mines do not fit corporate resource, production and profit criteria. Smaller companies are more suited to managing these medium or small scale mines and are tendering for the purchase or lease of mines that larger companies wish to dispose of. In addition to these factors there has also been a trend (especially in Western Australia) for mines to continue operating at ever increasing depths. This in turn has led to more mines operating in high stress environments and experiencing damaging seismicity. Assessing the viability of seismically active mines from a takeover or purchase point of view should involve analysing the risk profile of every aspect on mining that could be affected by adverse seismicity. This includes assessing current and alternative mining methods, mine designs, support systems, extraction sequencing, monitoring and blasting. This paper includes discussion on items that need to be assessed when considering the purchase of seismically active mines, with experience gained from some recent studies in Western Australia. In these cases it was apparent that quantification of previous seismic history on itÆs own was a totally inadequate method of assessing minewide seismic risk potential. A more holistic approach is required, taking into account all aspects of relevant data, all the minewide effects of seismic activity and all possible means of mitigating those effects.

Jan 1, 2002

By I. M. Ahmed, R. S. Hassan, M. I. Aly

Extraction and separation of La, Sm and Dy ions from acidic sulfate-phosphate solutions was investigated using a cation exchange extractant, bis(2,4,4-trimethylpentyl) phosphinic acid, CYANEX 272, in kerosene. The influence of shaking time, equilibrium pH, extractant, sulfate and phosphate ion concentrations, diluent type and temperature was studied. The extraction was found to be pH-dependent, and increasing the phosphate ion concentration inhibited the extraction which was found to be endothermic. The stoichiometry of the extracted metal species was found to be MOH.H2OHSO4H2A.A2. Aliphatic diluents were found to enhance the extraction compared to aromatic diluents. The results showed that there was a separation mode between the metal ions when varying the hydrogen ion and sulfate ion concentrations, under the used experimental conditions. The investigated process was used for the recovery of La, Sm and Dy from the acid solution resulting from the leaching of low-grade monazite.

By F. F. Poland

The purpose of this paper is to describe a new process for the refining of secondary copper-base metals and a specially designed high-temperature electric-resistor furnace used in the process for the distillation of zinc from these metals. The process was used for the conversion of nickel silver to cupronickel and to recover the zinc content in metallic form. It also proved applicable and economical for the treatment of scrap brass for separating and reclaiming the copper and zinc. The relatively large furnace developed for the distillation of zinc is described in detail, for it made economically possiblc the direct recovery of metallic zinc from scrap brass, which is a new step in the processing of such material. Considerable interest has been shown in the utilization of the distillation furnace for other metallurgical processes, where it is of advantage to operate in a controlled neutral or reducing atmosphere, or to avoid having the processed metal in contact with refractories other than carbon, or to operate at temperatures between 3000 and 4000°F. Purpose of Development It was recognized early in the war effort that nickel would become a critical metal. therefore all nickel stock and alloys containing relatively high percentages of nickel were frozen immediately. Among these alloys were considerable quantities of various grades of nickel silver, an alloy containing copper, nickel, zinc, and in some grades lead, also minor amounts of iron, manganese and other constituents. At the time there was no existing plant or process to eliminate the zinc, lead, and minor constituents so as to convert this metal to cupronickel, one of the important alloys needed by the U. S. Navy for condenser parts. Therefore the Bureau of Industrial Conservation of the War Production Board requested the executives of the leading nonferrous metal companies to have their metallurgical staffs study the problem of converting this metal to cupronickel conforming to U. S. Navy Specification 44T40. The composition specified therein is as follows: nickel, 29 to 32 per cent; zinc, 1.00; iron, 0.00 to 0.60; lead, 0.05; tin, 1.20; manganese, 0.00 to 1.00; total of other elemcnts (maximum). 0.50; copper, remainder. The problem in converting these alloys to cupronickel was the elimination of zinc, lead, iron, manganese, and other elements without appreciable loss of nickel to slags or other by-products. Revere Copper and Brass Incorporated, through its Research and Development Department, undertook to solve this problem. A Government-owned plant was built at Rome, N. Y., and there the conversion was made successfully.

Jan 1, 1949

By Tony Robles

"A new process is disclosed for the recovery of gold and/or silver values from activated carbon wherein they are adsorbed as cyanide complexes. A unique chemistry allows the new process to use mill process water containing an inexpensive, non-hazardous compound as the eluant. The new process has an elution period of 5 hours at 98°C. The gold in the eluant can be recovered by electrowinning or zinc precipitation. The new elution process is simple, reliable, and provides an eluted carbon that may not require thermal regeneration before reuse. Retrofitting the new process to existing processes such as Zadra, Anglo, and others will not require significant capital expenditures.IntroductionThe efficient and reliable elution process for gold/silver from activated carbon is a very important process in the gold mining industry. The most common techniques for elution of gold cyanide from activated carbon are the Zadra and Anglo procedures.Specialized elution techniques like the Micron and Acetonitrile processes have not been commercialized to significant extent probably due to relatively complex unit operations and expensive reagents.Important functions of the gold recovery circuit are:Efficiently recover gold/silver from the loaded carbon.Carbon is in good condition for reuse for optimum recovery.The pregnant solution is amenable to electrowinning or zinc precipitation to recover gold/silver from the solution.The whole process to be simple and short to reduce gold inventories.Present Elution ProcessesTable 1 shows some carbon elution processes that are available today. The two main elution processes used in the industry are: (1) the Zadra process, in which hot cyanide solution is circulated through an elution column and electrowinning cells; and (2) the Anglo American Research Laboratory (Anglo) process, consisting of a pretreatment step with caustic cyanide solution, followed by elution with deionized water."

Jan 1, 2000

By H. L. Bibbs, H. D. Snedden

"INTRODUCTION The use of beryllium and its alloys has increased rapidly during the last decade. Further expansion of its use is limited; in part, by lack of adequately developed ore reserves. The principal commercial beryllium mineral is beryl, which is found chiefly in pegmatites and produced for market as a byproduct of the mica and feldspar industries. The coarse beryl is mined selectively, sobbed and sorted by hand, and then sold without further beneficiation. The known reserves of coarse beryl are small. No method has been available for concentrating small disseminated beryl crystals, so ores of this type have not been mined or have been left on waste dumps. Disseminated ore in low-grade unmined areas and waste dumps on developed properties is a potential source of beryl, provided a method is developed for its beneficiation.Published literature on the concentration of beryl is lacking in detail or deals chiefly with tests on artificial mixtures of pure minerals, and procedures as given were not applicable to the beryl ores tested at the Salt Lake Station. The testing procedures described in this report are independent developments. By employing these procedures, beryl was satisfactorily con¬centrated from several run-of-mine and dump ores, although these ores wore low in grade and part of the contained beryl was finely crystalline and disseminated.Beryl, quartz, and feldspar, when ground to flotation sizes, are so alike in color and general appearance that they cannot he distinguished by visual observation. The progress of the work depended on rapid determination of the grade of test products by means of the petrographic microscope. Small samples of concentrates and tailings were often cut after each addition of reagents, dried, and examined under the microscope."

May 1, 1947

By I. Dymov, W. Phillips

A process has been evaluated, on a continuous pilot plant scale, to treat refractory gold arsenopyrite/pyrite concentrates. The process consisted of biological leaching to partially oxidise sulphides, followed by pressure leaching for complete sulphide oxidation and arsenic precipitation, followed by liquor neutralisation and cyanidation of the autoclave residue for gold recovery. This paper provides a brief description of the treatment flowsheet and discusses some of the main parameters and results of the process. During integrated pilot plant campaigns, it was confirmed that acceptable sulphide oxidation and gold extraction of 96-98% could be achieved by a two-stage oxidation with BIOX® (4 days total retention time) followed by PDX (40 minutes retention time at 220°C). Only partial arsenic precipitation was achieved in the autoclave, followed by complete precipitation by neutralization under atmospheric conditions. The overall process could be significantly simplified, and capital and operating costs reduced, with a flowsheet modification allowing all of the BIOX® liquor to bypass the autoclave directly to the neutralization circuit.

Jan 1, 2004

By John V. Beall

Monotonous flood planes flanked either side of the road as we drove in the embassy car from the airport to downtown Seoul. We crossed the brown waters of the Hann River, meandering over mud flats. A great, gnarled tree bore beautiful fall colors of gold. "That is a Ginko Tree, the oldest living fossil, probably a hundred million years old;" said Jean W. Pressler. Compared to other cities of the Far East, the traffic in and around Seoul was sedate. Few motorcycles or bicycles, and little superfluous horn tooting. "This is the best season in Korea. We have long beautiful springs and falls," said Pressler, chief of the mining branch of USAID, and he continued with a briefing on the country.

Jan 8, 1969

Coal mining ceased at Strongman Mine this year after 70 years of production. Underground mining finished in 2003 and opencast methods began in 1998. During the life of the mine, 8 million tonnes of coal was extracted from two underground mines and 1.2 million tonnes removed through opencast methods. Strongman Mine is within the Grey Coal Fields; various seams have been extracted from the Rewanui Coal Measures. Coal extracted was predominantly of thermal or semi-soft specifications and characterised by low sulphur and low ash.   The area has steep topography, high rainfall (>3000 mm/yr) and is particularly exposed to westerly quarter winds. Strongman 1 and 2 underground mines are located in the steep, narrow valley which leads to the Strongman Opencast at the top of the valley. Subsidence from underground mining combined with spontaneous combustion, has resulted in an underground fire which has had substantial surface effects. Opencast mining in the steep topography resulted in several landslides at the perimeters of the site. These factors, along with water management, topsoil management and erosion control have added to the complexity of rehabilitating the site.   Rehabilitation of the site is well underway, including infrastructure removal, final landform creation and revegetation of the Strongman Opencast footprint (~45 hectares). Some innovative methods of rehabilitation have been trialled. Successful trials such as helicopter-seeding and moss hydro-seeding on highwalls are now routinely used along with traditional revegetation practices. 18 hectares disturbed land has been replanted with 88 000 seedlings, and another 200 000 seedlings are scheduled for planting over the three years. Fire management is an ongoing challenge; however thermal photography shows a steady decrease in hot areas which have been contained by grout curtains.   Mine closure is some time away and will occur after all standards set by Solid Energy and regulatory bodies are achieved.

Jan 1, 2006

By Ygor Pereira de Lima, Iana Costa Carvalho, Marcelo Henrique Prado da Silva, Talita Gama de Sousa, Andrey Mariano dos Santos, Paulo Davi Borges Esteves, Rodolfo da Silva Teixeira, Andersan dos Santos Paula

Durante muitos anos, as ligas convencionais foram base para o desenvolvimento de novos materiais metálicos, com propriedades melhores que as até então conhecidas. No entanto, na última década, as Ligas de Alta Entropia (LAE) trazem uma nova abordagem para a produção de materiais avançados, com excelentes propriedades e potencial para diversas aplicações. Em particular, as ligas do sistema Al-Co-Cr-Fe-Ni também se destacam por promoverem uma classe de LAE de baixa densidade e têm sido foco de inúmeros estudos no meio acadêmico atual. O presente artigo traz um estudo de otimização da preparação metalográfica da liga AlCo2Cr2FeNi2, a partir de 3 rotas diferentes de polimento e suas análises via microscopia eletrônica de varredura (MEV) e difração de Raios X (DRX). Além disso, foram avaliadas as modificações estruturais da liga em função de um tratamento térmico de solubilização (1050 ºC por 1 hora seguido de resfriamento em água). Os resultados das análises demonstraram a rota de polimento eletrolítico promissora para a caracterização da LAE em questão e a análise conjunta dos resultados de DRX e MEV, somado ao confronto com a literatura, permitiram identificar as fases presentes e suas modificações microestruturais em função do tratamento térmico.

Oct 24, 2019

By Aldo Henrique de Almeida Barbosa

Os modelos de tratamento de galvannealing, com encharque isotérmico após o aquecimento indutivo, permitem otimizar o aporte térmico para a formação de compostos intermetálicos Fe-Zn, o que contribui significativamente para a obtenção de revestimentos galvannealed-GA de elevada qualidade. Nesse estudo foi avaliado o efeito das condições de galvannealing na formação do revestimento GA sobre aços bake hardenable-BH. Foram realizadas, em escala de laboratório, simulações variandose o modelo de galvannealing, com ciclos isotérmicos e resfriamento imediatamente após o aquecimento indutivo, a temperatura de aquecimento, entre 525°C e 570°C, e o tempo de encharque, até 20 segundos. Em todas as simulações, além dos ciclos completos foram realizadas, também, interrupções do tratamento ao longo da etapa de encharque, através de resfriamento brusco das amostras, com o objetivo de se avaliar a microestrutura do revestimento ao longo de todo o tratamento. Para a caracterização dos revestimentos foram realizadas análises de composição química, microestrutura, perfil de composição ao longo da camada e de aderência. Os resultados permitiram determinar as características da formação do revestimento GA sobre os aços BH e estabelecer condições de galvannealing para o processamento desses aços, de forma a obter microestruturas otimizadas para as aplicações mais exigentes.

Aug 16, 2017

By Tcharllis João da Cunha Demartini

A produção de uma rocha artificial a partir da aglutinação de resíduos finos de mármore dolomítico pela resina epóxi pode ser uma alternativa viável do ponto de vista técnico, econômico e ecológico. O resíduo utilizado é proveniente do desdobramento de mármore dolomítico em teares de lâminas diamantadas e geralmente é descartado. Esta nova aplicação agrega valor ao resíduo, diminuindo o impacto ambiental gerado. O objetivo deste trabalho foi avaliar as propriedades físicas e mecânicas do mármore artificial produzido pela metodologia de vibro compressão à vácuo. Para isso, foram confeccionadas placas rochosas, em equipamento apropriado, com 85% em peso de partículas de resíduo e 15 % de sistema epoxídico DGEBA/TEPAc. As placas foram produzidas com uma pressão de compactação de 0,5 MPa, à temperatura de 90 °C por um período de 20 minutos. Posteriormente, as placas foram caracterizadas pelos ensaios de densidade, absorção de água, porosidade, resistência à flexão, resistência à compressão e microscopia eletrônica de varredura. Obteve-se um mármore artificial produzido pela técnica de vibro compressão a vácuo com absorção de água inferior a 0,06%, uma resistência à flexão de 33,93MPa e uma compressão uniaxial de 96,49MPa, confirmando uma boa adesão entre as partículas de resíduo e a resina epóxi.

Oct 30, 2017

By Hugo Candiotti

El presente texto describe la secuencia de los trabajos de exploración realizados en el yacimiento de Sipán desde el descubrimiento hasta la puesta en producción. Así también, señala las características geológicas, mineralógicas y geoquímicas del yacimiento que contribuyeron a la localización y formación del cuerpo mineralizado de oro.

Apr 26, 1999

By E. Ghali, W. Zhang, G. Gabra, N. Sorour, G. Houlachi

The additives polyacrylamide, 1-Butyl-3-methylimidazolium chloride, Tetra-butylammonium bromide, Benzalkonium chloride and chitin are evaluated during zinc electrolysis from synthetic acidic sulphate electrolyte containing Mn2+ ions, in absence and in presence of 0.0055 mg dm-3 of Sb3+ ions. Galvanostatic polarization tests for 2 hours at 50 mA cm-2 and 38oC were carried out to determine the cathodic and anodic potentials, and current efficiency of the deposited zinc. Potentiodynamic polarization and cyclic voltammetry tests have also been employed to study the electrochemical behavior of each additive on the zinc deposit on aluminum electrode. Results showed that, in presence of Sb3+, adding 1 to 3 mg of 1-Butyl-3-methylimidazolium chloride increases the cell voltage by ˜0-7 mV. Current efficiency is increased by ˜4.90-6.40%; power consumption is reduced by ˜147-173 kWh t-1 by adding 1-3 mg, respectively. However, in absence of Sb3+, cell voltage is decreased by ˜7-28 mV, current efficiency is increased by ˜0.70-1.50%; power consumption is reduced by ˜41-47 kWh t-1 by adding 1-3 mg. The effect of the other additives on cell voltage, current efficiency, lead content and morphology of zinc deposit has also been examined. Surface morphology and crystallographic orientation of the deposit was studied using scanning electron microscopic (SEM) and X-ray diffraction (XRD), respectively. The content of lead in the deposit has also been measured using inductively coupled plasma spectroscopy (ICP).

Jan 1, 2015

By M. D. Schlesinger

As part of the development of processes for producing synthetic fuels from coal, the Bureau of Mines prepared a special jet fuel in a pilot plant for evaluation by the Air Force. This jet fuel had all the required physical properties, including the important specifications of high heating value and high density. However, the finished fuel did not pass the stability test specified by the Air Force and conducted by the Southwest Research Institute in a high-temperature research coker. The cause for this instability is being investigated because pure compounds of the type identified in this fuel are known to be stable. The tar acid oil used was a 230° to 300° C. fraction of low-temperature tar obtained by carbonization of a West Virginia bituminous coal in the pilot plant of the Consolidation Coal Co. Both the desulfurization at 400° C. and saturation at 300" C. were done in the vapor phase at 2,500 p.s.i.g. After catalytic treatment and distillation the final jet fuel had a boiling range of 194° to 247° C., a net heating value of 18,420 B.t.u./lb. and a specific gravity of 0.8463 60° F./60° F. It also had u pour point below -62° C., and at 0° C. its viscosity was 4.5 cs. The oil was virtually all bicyclic, 41 pct. noncondensed and 56 pct. condensed.

Jan 1, 1961

By Robson Gambeta

A CLE Brasil possui uma subestação de 230kV que apresentou sérios problemas de trincas e rachaduras nas estruturas de concreto após alguns anos. Em alguns pontos a ameaça de queda era real. Foi iniciado um estudo de patologia das estruturas de concreto, com uma empresa especializada em recuperação estrutural para conhecer as causas e recomendar a melhor terapia estrutural a ser realizada. Após o estudo, definiu-se a terapia adequada das estruturas. Esta atividade foi classificada como de grande risco e teve foco na segurança da equipe e operação do sistema, de modo que todo o serviço fosse executado sem quaisquer incidentes as pessoas, ao meio ambiente e ou interrupções de energia elétrica. Havia desafios como realizar manutenção nas proximidades da linha viva, serviços em altura com utilização de andaimes, período de chuvas e ventos, trocas de equipes e anomalias. As estruturas tratadas foram Pórticos com 17 metros de altura, postes e suportes para isoladores, TPs, TCs, Seccionadoras e Transformadores. A atividade durou 04 meses e contabilizou 5.752 horas de trabalho. Os resultados foram significativos e dentro do esperado, sem ocorrência de incidentes, prolongamento da vida útil e aumento considerável da segurança da equipe e do sistema de distribuição.

Jul 31, 2018

By W. W. Adams

[The s1xteeilth an.nual National Safety C mpeti t1on, concluc ted "by the Bureau of t4ine g, Un+ ~ed st tag' DepartIilent 0:1' the Interior, has jast been closed, and the results reveal t:'W.t. t_!e co~)eting comps.nies had fewer a.ccidents in proportion to the number. of !\1a..."1-h(J1J.l'~ :orkcd than in a:ny other yeex in the record of the contest. These annUk~l contestn are thus achieving the r purpose of promoting safety in tho minin induC'tr:r. ]

Jan 1, 1941

By George Joseph Malina

Contractor chose and Owner allowed concrete to be placed using the arch first principle while excavating the 35'-3" O.D. rock tunnel. The contract included excavating and lining 26,000 L.F. of rock tunnel to 33'-I.D. Concrete was placed at a rate of 90LF per working day using a movable bridge to allow batching, mixing and pumping of concrete adjacent to the tunnel form.

Jan 1, 1981

By Frederico Valadares de Andrade Resende

O uso de aglomerantes na pelotização é uma ciência que está em constante desenvolvimento de novos produtos, visando elevar o desempenho em suas aplicações, além da busca da redução e não incorporação de ganga ácida no produto final. Para tanto, a pelotização em parceria com fornecedores destes insumos está trabalhando em pesquisa para agregar cada vez mais valor nas pelotas de minério de ferro. Atualmente já ocorreram avanços na utilização da bentonita sódica superativada, com o desenvolvimento e aplicação em escala industrial, onde foi constatada vantagens em seu desempenho frente a outros tipos de aglomerantes. Porém, durante um maior período da utilização da bentonita sódica superativa em escala industrial, foram percebidas algumas influências não desejáveis no processo produtivo, as quais estavam interferindo diretamente no desempenho das plantas de pelotização que estavam utilizando tal aditivo em seu processo. Diante do exposto acima, foram estudadas possibilidades para adequação do produto, onde foi sugerida a alteração da formulação química promovendo uma redução do potencial de aglomeração do aditivo, alterando assim algumas características que estavam impossibilitando a utilização em escala industrial. Este trabalho apresenta a viabilidade da aplicação industrial da bentonita sódica superativada, após a reformulação desenvolvida em parceria com o fornecedor do produto, baseada em análises estatísticas dos resultados.

Aug 1, 2018

By Alex Salvador

El Comisionamiento de una planta concentradora es un proceso secuencial ordenado y adecuadamente organizado de pruebas de operación con carga, que permite llevar a los diferentes equipos a su capacidad de diseño. Consiste en un proceso de arranque de equipos, seguido de un incremento progresivo de tonelaje de acuerdo a los criterios y protocolos del fabricante.

Sep 29, 2023