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By David D. Rabb

Leaching or solution mining, a relatively simple and economical process for beneficiating metallic ores, is likely to find increasing application in the treatment of low-grade ores that are impractical to mine by any other means. This process may be carried out in two different ways: 1. Dump leaching, where the ore is moved from its original location to be leached at another site. 2. In situ leaching, where the ore is leached in place by introducing the leach solution at the top, letting it flow down through the ore under gravity, and then recovering it plus the dissolved metals it contains.

Jan 1, 1969

By Ferdinand S. Ruttmann

There is now in use at the mines of the Chateaugay Ore and Iron Co., at Lyon Mountain, New York, an ore-concentrating machine or jig, which, in view of the increasing attention given to the subject of concentrating lean ores of iron, seems worthy of notice. This Conkling Jig, as it is called, is not entirely unknown, having been used at several places with more or less success; but as yet, I believe, no drawings of it or records of its work have found a place in print. Although the jig will be found to be merely an adaptation of old forms, there are several points which deserve attention, particularly the method of central discharge, of freeing the bearings from grit, and the rotation of the sieve or screen. The ore-body at Lyon Mountain consists of a bed of rather compact, granular magnetite, occurring in a gueiss formation. The side walls of the ore-body are not sharply defined, the ore 011 either side becoming gradually poorer as the distance from the central point of the body increases. It is this lean ore, which, before the introduction of the jigs, was thrown away as waste, that is now concentrated. The material treated conseqnently consists of magnetite, intermixed with the component parts of gneiss, viz. quartz, felspar, hornblende, and mica. Grains of trap also form part of this material. These come from dykes of trap, which cross the ore-body at intervals. The ore which is to be concentrated usually contains from 30 to 40 per cent. of metallic iron. It is first crushed to the size of two inches, or less, by two large Blake crushers. The material from these crushers passes by a shute lined with screens, having holes 2 inches in diameter, to a second set of four crushers, set so as to close to one inch. The product from this set of crushers, together with that which passes through the screens in the shute, is then taken by an elevator to the top of the mill, and passed through a revolving screen, perforated with ) inch holes. The ore which passes through the screen goes to the jig-hoppers ; that which passes over goes to a third

Jan 1, 1888

By P. G. Bennett

The Bureau of Mines developed a process using ion exchange to recover cobalt from spent copper leach solutions. A preliminary economic evaluation of the process indicated that about one-third of the capital cost was attributed to the total resin inventory, and one-third of the operating cost was required for reagents to remove iron from the ion-exchange eluates. An agitated Pachuca elution system was investigated in place of a fixed-bed elution system. The Pachuca system reduced the resin inventory by 27 pet when compared with the fixed-bed elution system. Processing fresh spent copper leach solution reduced the resin inventory by 20 pct and resin iron loading by 80 pct. Reagent requirements for removing iron from the eluates were decreased because less iron was extracted. The Pachuca system, along with processing fresh spent copper leach solution, reduced the total resin inventory by 47 pct. A revised cost evaluation of the cobalt recovery process was obtained to determine the effects of these process modifIcations. The estimated total capital cost for a plant processing 10,000 gpm of spent copper leach solution containing 26 ppm Co was $23.1 million. With credits for nickel, zinc, and copper byproducts, the estimated net operating cost was $5.10/lb of cobalt.

Jan 1, 1988

By Ana Carolina Abrantes de Souza

O objetivo deste trabalho foi a obtenção de microestruturas diferenciadas, em um aço baixo carbono com microadição de Molibdênio e Nióbio laminado a quente, após submetê-lo a diferentes meios de resfriamento antes e após a temperatura de interrupção de 600°C (que simulava a temperatura de bobinamento). A evolução microestrutural e mecânica foi avaliada com o auxílio de técnicas de microscopia óptica e microscopia eletrônica de varredura, testes de dureza Vickers e tração uniaxial, somado a determinação das temperaturas de transformação de fase em um analisador termomecânico (TMA). De acordo com os resultados, meios de resfriamentos mais severos foram mais efetivos em proporcionar um aumento da resistência mecânica associado a decréscimo da ductilidade pela formação de fases mais dura e aumento da acicularidade da ferrita.

Jul 30, 2018

By Richard A. Pomeroy

This mine, known also as the A very Mine, is situated on Petite Anse Island, Iberia Parish, Louisiana. The island is about four miles from Vermillion Bay, an arm of the Gulf of Mexico, and is one of four islands or hills surrounded by the sea-marsh, as shown in the accompanying map. (Fig. 1.) A fifth, Joe Jefferson's Island, or hill, is some distance from the sea-marsh. These five islands: Belle Isle, Cote Blanche,Grand Cote, Petite Anse and Jefferson, appear to be the tops of submerged hills, and occupy a line having nearly a northwest trend. To the north are a series of hillocks that extend at intervals to the hills of Northern Louisiana, which in turn appear to run into the Ozarks of Arkansas. Near the mine there is sandstone, also a thick vein of lignite. Bones of the mastodon have been

Jan 1, 1889

By Mack JF

A metallurgical evaluation of the Argyle Kimberlite No. 1 (AKl) orebody has been carried out using a 40 tonnes per hour pilot plant. Pilot plant results, together with laboratory investigations provided a basis for the determination of process design criteria for a major treatment plant. Various sampling programmes were carried out to determine specific aspects in the evaluation of diamond liberation. Treatment parameters such as the top crush size, recrush size and the bottom cut-off size were investigated. A description of the pilot plant is given together with the design criteria for a 3 million tonne per annum treatment plant

Jan 1, 1984

By K. Hori

In this study, the determination of optimal conditions for jig separation has been investigated with a TACUB jig separator. The TACUB jig, from which a Batac jig originated, is a useful gravity separator that is effective to separate crushed solid wastes as well as coarse ores. A mixture of crushed polyethylene (specific gravity 1.3) and polyvinyl chloride (specific gravity 1.5) was separated by a batch TACUB jig by varying the frequency (wavelength) and the amplitude (pulse stroke length). It was found that the sample particle layer in the separation chamber was fluidized without turbulence by the rising water pulse resulting in the separation. However, a too strong water pulse reduced the efficiency of the separation of the particles. The results indicate that the specific velocity of the rising water is necessary to fluidize the particle layer without turbulence to separate the particles. The expansion ratios of the thickness of the particle layer in rising flows were measured in a cylindrical column. The pressure losses by the particle layer were calculated from the expansion ratios and the velocity of the rising flows by Ergun?s equation. The curve of the pressure loss vs. the velocity of rising flow showed a maximum point corresponded to the point of fluidization. The velocity of a rising flow on the point of fluidization provided the optimal separation condition.

Jan 1, 2014

By M. Katzer

The effect of selective dispersants as wet grinding aids for ores is demonstrated on laboratory scale batch and continuous grinding equipment. A complete characterization of behavior is performed on a given ore to demonstrate correlations involving torque, % solids, net production rate, and slurry weight and volume loading. The relationship between such laboratory data and industrial scale testing results is very consistent.

Jan 1, 1979

By Y. Zhen, N. Topliffe, G. Shou

The typical service life for a long distance slurry pipeline is15 to 25 years. Determination of wear rate for a pipeline could have a high economic impact on the pipeline project. Wear is a combination of chemical corrosion and mechanical abrasion. The contribution of each factor has to be determined project by project. Normally, chemical corrosion dominates the pipe wear in fine slurry pipelines. These pipelines have been designed with a velocity between 1.5 m/s and 2.5 m/s. Solids are suspended with high homogeneity across the pipeline section. Bottom wear is not much greater than the top wear and not sensitive to velocity. The wear pattern in the pipeline transporting medium coarse solids, such as milled ore and tailings, is different. Wear concentrates on the bottom of pipeline and the outer bends, and is more sensitive to flow velocity. Wear distribution along the pipelines is similar.

Jan 1, 2007

By Fabiana da Silva Santos

O presente estudo fez uso de uma liga de NiTi, rica em Ni, elaborada em um forno de fusão por indução a vácuo - VIM e posteriormente refundida em fornos de arco elétrico com eletrodo não consumível de tungstênio – VAR. Com base nos resultados de Calorimetria Diferencial de Varredura (DSC), Difração de Raios-X (DRX) e Microscopia Eletrônica de Varredura (MEV) / Espectroscopia de Energia Dispersiva de Raios-X (EDS), foi possível observar a heterogeneidade composicional/ típica de fundido por processo convencionais, as inclusões de TiC e Ti4Ni2O provenientes da fusão no forno VIM, e o refinamento microestrutural e manutenção da sua composição original com uso de cadinho de cobre e câmara/atmosfera dos fornos VAR.

Oct 30, 2017

By G. C. Stone

AS the term "hardness" is used with many different meanings, it should be understood that it here means resistance to deformation by compression. It was determined by measuring the pressure, in pounds per square inch, necessary to reduce by 20 per cent., the length of cylinders 1 in. (25 mm.) in diameter by 2.6 in. (66 mm.) long. The tests were made at Columbia University on an Olsen 400,000-lb. machine, the load being applied at a constant rate of speed 0.0319 in. per min. The results were obtained by Messrs. Rigg and Williams, and some of them were given in a paper read at the Sixteenth Annual Meeting of the American Society for Testing Materials, in June, 1913. The remainder of the results were obtained in subsequent experiments by the same authors. In all cases, the results given are the averages of three or more closely concordant tests. All of the spelters tested were of standard commercial grades and all were of compositions making them good deliveries. The accompanying table gives the results arranged in the order of increasing hardness:

Jan 1, 1919

By C. T. Young, J. L. Lytton

In recent investigations,1,2 the strength and thermal stability of dislocation substructures prepared by 5 to 25 pct room temperature tensile straining and recovery annealing at 120°, 160°, and 200°C have been studied in randomly oriented polycrystalline high purity aluminum. The techniques of transmission electron microscopy revealed that a major source of the strength and stability of dislocation substructures was the formation, during room temperature straining, of well-defined cells bounded by dislocation tangles which rearranged into nearly perfect dislocation networks during recovery, forming the boundaries of subgrains. The strength of such substructures increases with decreasing cell or subgrain size,2"6 and the formation of fine subgrain structures can provide thermally metastable strength at low temperatures and can favorably alter the course of primary creep at elevated temperatures.7'8 For maximum benefit, however, sub-grain growth should be reduced or eliminated. It was, therefore, decided to investigate the use of heterogeneous precipitation on dislocation networks as a means of imparting increased strength and thermal stability to subgrain structures through effective pinning. C.T. YOUNG, STUDENT MEMBER AIME, and J. L. LYTTON, Member

Jan 1, 1970

By Roger C. Ilsley

The $2.1 billion Milwaukee Water Pollution Abatement Program (MWAP) requires the construction of several miles of underground openings at depths up to 350 feet for the conveyance and storage of sewage and storm water overflows. The system will include approximately 27km (17 miles) of deep tunnels ranging from 3m (10 f t.) to 9m (30 f t.) in diameter, 26 shafts and a pumping station cavern. The facilities will be located primarily in Silurian Age dolomites of the Niagara Group. The rock is characterized as competent with vertical to sub-vertical orthogonal jointing and predominantly thin shale bedding planes. The site investigation was carried out incrementally, commencing on an area wide basis, becoming site specific as facility plans were developed. To achieve cost savings through uniformity and continuity, a computerized data bank was established. Software was developed during the initial stages of the program for the production of borehole logs, structure contour maps, geologic profiles and summaries of data for statistical evaluations. This paper discusses in general terms the collection, compilation and presentation of data necessary for the characterization of the rock mass.

Jan 1, 1984

By A. C. Dorenfeld

In most mineral enterprises, what is the progress, and shift in responsibilities, as the young engineer advances in the corporation? You are all familiar with the normal pattern-in mine production from level boss, to shift boss, to superintendent to manager; in milling from test engineer, to shift boss, to foreman, to superintendent and then manager; in engineering from surveying on to Chief Engineer; and all then aspire to the corporation presidency. Note the shift-from purely technical jobs, say in the first five to ten years in the profession, to administrative positions for 30 to 40 years. What is the average preparation given to mineral engineering students, who can look forward to about 30 years of administrative work? From the catalogs of 21 institutions, offering 36 curricula of four years length, in mining and/or metallurgy, requiring the equivalent of about 150 to 160 semesterhours for graduation, the following results were obtained: Average number of semester hours of economics, 3 hr. Range of requirements, 0 to 8 hr. Thirteen curricula do not require any economics. Accounting and business law, average: 1 semester hr, 26 curricula do not require business law or accounting.

Jan 2, 1955

By Oliver Bowles

Limestone is the most widely used of all racks and is essential to a great many industries, including tae building trades, highway construction, metallurgy, agriculture, end many chemical and manufacturing enterprises. It occurs in some form in every State and is produced in thousands of quarries. Production in 1930 exceeded 134,000,000 tons. It has more numerous and more diversified uses than any other rock. This paper is designed to furnish general information on the various branches of limestone quarrying and their economic importance. Brief reference is made to dimension stone, and a more complete discussion follows of the uses, requisite qualities, quarry methods, grid processes of preparation of crushed and broken limestone. Footnote references serve to guide the reader to more detailed information.

Jan 1, 1933

By Marcelo Moreira Furst Gonçalves

A qualidade superficial dos produtos lingotados continuamente está ligada diretamente aos estágios iniciais de solidificação do aço no molde. Nessa etapa do processo, os parâmetros e estratégias de oscilação são decisivos para a obtenção de produtos com qualidade superficial adequada. Assim, foi desenvolvido na Usiminas um sistema computadorizado para monitoramento dos parâmetros de oscilação do molde, de modo a fornecer subsídios para um melhor entendimento do processo. Este sistema monitora, em tempo real, o eixo vertical e as oscilações nos eixos horizontal e transversal, mesmo com baixas amplitudes. O sistema desenvolvido possibilita a obtenção dos dados com alta precisão, de forma totalmente automática e a realização de pós-tratamento de forma a se obterem valores relativos ao processo de lingotamento e funcionamento do molde.

Jul 30, 2018

By Camila Luzia Lira Duarte

O processo de pelotização utiliza o combustível sólido com intuito de gerar energia térmica que será transferida para a pelota de forma a alcançar uma queima uniforme. Na usina de Vargem Grande normalmente o antracito é utilizado como combustível sólido. Com objetivo de testar diferentes fontes de combustível sólido, um teste industrial de com coque breeze substituindo o antracito foi realizado. Como o coque breeze possui menor teor de matéria volátil, cinzas ei maior teor de carbono fixo, o consumo de gás natural no forno pôde ser reduzido. Além disto, o coque breeze apresentou um perfil de combustão mais favorável à qualidade da pelota resultando em ganho nos resultados de compressão. Dessa forma, a viabilidade econômica e operacional da substituição do antracito pelo coque breeze foi positiva.

Aug 17, 2017

By John B. Gayle

[The coking time exerts a Considerable influence on the throughout of a coke oven, and for this reason a large number of papers dealing with the relation between coking tine and the different operating variables have been published. Although all of the factors known to ink influence the coking time have been studied, agreement leas not boon reached on several questions, 3/4/ and it appears worthwhile to evaluate any data that become available during investigations of the carbonizing properties of various oafs and coat blends, this report, therefore, includes a Study of the relation between coking lime and flue temperature and represents the second phase of overall investigation ion of factors influencing the coking time in slot-type ovens.]

Jan 1, 1956

By D. Harrington

The record of fatalities from mine explosions in the United States during the past 44 years has been the best in the history of the mining industry, despite the fact that the number of fatalities from this cause during the past fiscal year now is nearly double that of the previous year. During there 4 fiscal years, mine explosions have resulted in an average of 45.5 deaths per year, compared with an average of 153 deaths per year for the preceding 5 years; an average of 542 deaths per year for the 3 years 1907-1909, inclusive, and a yearly average of 265 deaths per year for the 20 years prior to 1929. Other types of mine accidents also have been reduced during this period, but not to the same degree or by as large a percentage as mine explosions. The fact that in this fiscal year ended June 30, 1937, electricity was responsible for 60 percent of the explosions and 85.5 percent of the fatalities resulting therefrom (see tables 3 and 4) is evidence that either mine operators are lax in providing proper electrical equipment or there is laxity in the upkeep and use of electricity in our mines and more particularly in our coal mines. Several large coal-producing States that in the Fast have had numerous disastrous explosions have been free from such disasters for continuous periods of as long as 8 years. The bituminous mines of Pennsylvania, one of the largest coal-producing States, give a good example of what can be done to prevent explosions. 'his State, with its large number of operating mines, many with very definite hazards from gas or dust or both, has had only two major explosions (resulting in 16 fatalities) during the past 7 years; this is a decidedly good record compared with any similar period in the past and when it is considered that during this period about 750,000,000 tons of coal have been produced. Other good records are: Tennessee, without a single fatality from explosions during the past 9 years; Alabama, with 6 fatalities during the past 7 years; Illinois, with no explosions during the past 4 years; and

Jan 1, 1938

By Priscila Graziela Melo Martins

O tamanho de grão austenítico é um parâmetro que influencia o desempenho de tratamentos térmicos em aços, assim como suas propriedades. Neste contexto, este trabalho investigou o uso de um reativo para ataque por imersão (240ml de água destilada, 2ml de HCl, 2g de ácido pícrico e 5 gotas de detergente neutro) para avaliar a influência da temperatura e do tempo de austenitização sobre o tamanho de grão austenítico de um aço ABNT1045 austenitizado nas temperaturas de 860ºC, 950ºC e 1100ºC por intervalos de tempo de 40, 90 e 180 minutos. As amostras austenitizadas foram temperadas em água, metalograficamente preparadas e atacadas com o reativo proposto com o objetivo de se revelar os antigos contornos de grãos austeníticos. Os tamanhos de grãos foram medidos com a utilização do software UMIAS de forma a possibilitar a determinação de distribuições estatísticas com quinhentas medidas para cada condição de tratamento. As amostras foram novamente preparadas e então atacadas com Nital 2%, sendo possível avaliar a influência do tamanho de grão austenítico sobre a morfologia da martensita. Pôde-se observar que, para o aço ABNT1045, a influência da temperatura de austenitização sobre o tamanho de grão austenítico é muito evidente e mais significativa do que a do tempo. Os valores de tamanho de grão se mostraram exponencialmente dependentes da temperatura, de forma que quanto maior o tamanho de grão austenítico, mais grosseira é a estrutura martensítica e menor é a dureza do material após a têmpera em água.

Aug 7, 2018