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By D. E. Healy

In 1989, an autogenous grinding task force was formed to study potential autogenous grinding circuits to replace the existing semi-autogenous grinding (SAG) at the National Steel Pellet Plant in Keewatin, MN. Pilot plant test work, performed by the Hanna Research Center (HRC), indicated that fully autogenous grinding with pebble extraction and crushing could be incorporated into the existing circuits. In 1990, one of the existing 10 grinding mills was converted for an in-plant test incorporating pebble crushing. Full-scale test work were conducted in 1990 and 1991. They verified the pilot plant projections with primary mill throughputs from the fully autogenous circuit using pebble crushing being greater than throughput of the existing SAG mill circuits. The plant produces 5 Mt/a (4.9 million ltpy) of iron ore pellets from 17.6 Mt (17.3 million It) of crude taconite. Crude ore is single-stage crushed by gyratory crushers. Primary grinding is performed by 10 semi-autogenous wet grinding mills. Secondary grinding is performed by five ball mills. Induration is with an Allis Chalmers grate-kiln pelletizing system. The primary grinding circuit consists of 108.2-m-diam x 5.5-m long (27 ft-diam x 18-ft) SAG mills. The mills are charged with 127 mm-diam (5 in.diam) steel grinding balls at from 3% to 5% by volume. Ball consumption rate is about 0.55 kg/t (1.25 lbs/lt) of crude ore feed to the mill. Each SAG mill is powered by two 2.6 MW (3500 hp) motors drawing 5450 kW (7300 hp) at 76% of critical speed. The mills are grate discharge with 16 mm (0.6 in.) slotted grate openings when new. The mill discharge is sized on a trommel screen having 4.5 mm (0.2 in.) openings. The plus 4.5 mm (+0.2 in.) oversize material is returned to the discharge end of the mill by a reverse screw auger located in the center of the trommel. The -4.5 mm (-0.2 in.) trommel screen undersize is pumped to magnetic cobbers.

Jan 1, 1992

By J. X. Zhang, F. S. Niu

"In order to accurately detect whether the collision occurs between particle and bubble in flotation process, a collision detection method of particle and bubble, which based on morphological image processing and Otsu method, is presented. First of all, it utilizes image pre-processing to optimize images, the target area and the background area are segmented by Otsu method. Then, particle and bubble are fitted to a circle combined with the least-square method. It’s convenient to obtain the coordinate information and radius. Finally, the position of all particles is extracted to an image, which achieves the particle tracking and avoids the complexity of the continuous frame image tracking.Experimental analysis shows that the relationship between the two ordinate difference d and the bubble radius r has a certain influence on the collision detection when the dripping particles are close to the bubble, when d>r, the detection accuracy is 92%;When d=1/2r, the detection accuracy is 97%;When d=0, the detection accuracy is 100%. The result indicates that this algorithm can detect the collision between particle and bubble quickly, and the working hours of manual test are saved effectively ,the best position of dripping particles close to the bubble which is taken with a CCD camera should be in the range of the particle and bubble’s ordinate difference less than half of the bubble radius.INTRODUCTIONFlotation is an important technical means to separate useful minerals from ores. The flotation process of ores and materials in the world is treated by flotation technology up to billions of tons every year, so the study of flotation process is particularly important. Raising the collision probability between mineral particles and bubbles in flotation process is one of the key factors to improve flotation separation efficiency[1]. The study indicates that[2-4] the collision probability between particles and bubbles is influenced by many factors, such as particle density, particle size bubble size, etc. The analysis of these influential factors requires a lot of experiments. Therefore, it is of great significance to design an accurate collision detection method for the research of this field."

Jan 1, 2018

CHEMICAL PRECIPITATION U.S. 4,067,789 - Removal of soluble manganous ions from a zinc sulfate solution formed by leaching roasted zinc sulfide ore with spent electrolyte. An excess of ammonium persulfate or like oxidant is added to the leach solution to convert manganese to insoluble, filterable gamma-manganese dioxide, and the precipitate separated from the solution by filtration. L. Harris and A. K. Hanson, Jr., assigned to Newmont Exploration Ltd. Jan. 10, 1978. 11 pp. (204-119). Filed: 5-3-76 (682.442). (Drawing on page 67.)

Jan 1, 1979

By M. G. Zabetakis

This publication describes an investigation conducted by the Federal Bureau of Mines regarding the cause of an explosion of a dephlegmator or fractionating column at the Cities Service Oil Company Refinery, Ponca City, Okla., January 22, 1959. The column was that used with the refinery's No.1 Dubbs Coker. The explosion caused the death of an employee of the refinery and resulted in extensive damage to the refinery and to nearby property. The Bureau's study of the explosion began January 26.

Jan 1, 1960

Pictured on these pages are the six RMCMI Scholarship Award Winners for the 1988-89 year followed by a brief profile. All winners were present as guests of the Institute at the June convention in Durango, Colorado to receive recognition at the Welcome Session Monday, June 26, 1989. Each state vice president served as the host for the collegiate winner. In addition to receiving a plaque from the Scholarship Chairman, Keith McGinnis, each winner receives $500.00 tuition credit for the coming academic year. As this is a continuing award, the winners from the previous year will receive another $500.00 for tuition credit in their senior year if they have maintained good academic standing and have been recommended by their university. Criteria for these awards to be made in the spring annually is (1) That the award be made to a sophomore student and used as tuition during the junior year. (2) That the recipient be both a U.S. citizen and a resident of the state involved. (3) That the recipient have good academic standing, be pursuing a degree in a mining related field and have an expressed interest in Western coal as a possible career path. The scholarship program includes curricula other than those in the mining departments, but in the engineering disciplines, such as geology, mineral processing and metallurgy. Contributions to this worthy project are tax deductible to each individual RMCMI member or his firm. Through annual donations of $100.00 or more, the Patrons of the Institute fund the scholarship program and the various vice presidents contribute the travel expenses to convention for these outstanding young collegiates. Donations to this worthwhile program may be made payable to RMCMI Scholarship and mailed to the RMCMI Office, 2700 Youngfield Street, Suite 100, Lakewood, CO 80215. Profiles of the 1989 Scholarship Winners follow. [ ] David P. Pelletier University of Arizona Tucson, Arizona David is a Mining Engineering major and graduated from Santa Fe High School in 1981. He served in the Sixth Marine Regiment, Second Marine Division of the United States Marine Corps from December 1982 thru December 1985. He is a student member of SME-AIME and has held the offices of treasurer, vice president and president. He works volunteer shifts at the University of Arizona San Xavier Mining Laboratory [ ] Johnny F. Blizzard Colorado School of Mines Golden, Colorado A high school graduate of Longmont, Colorado, Johnny carries a 3.968/4.000 at Mines, majoring in Mining Engineering with a minor in Metallurgy. His name has appeared on the Academic Dean's list for the past two years. He received the Robert M. & George R. Harris Scholarship during this past year. He is a student member of SME-AIMMP and an executive council member of CSM's chapter of AIME. Summertimes, Johnny works as a miner for Edger Mine in Idaho Springs, CO on an experimental project for USBM.

Jan 1, 1989

By M. E. Adam

This report describes the construction and testing of large (30 ft high by 55 ft wide) stopping and overcast structures in an oil shale mine. The work was undertaken to develop construction techniques and cost data, and to measure leakage rates on full scale structures in an oil shale mine. A design data base was developed by reviewing industry practice, oil shale industry plans, and technical literature. Alternate layouts for room and pillar mining were examined to find ways to reduce the size and number of ventilation control structures. Six full size stoppings and one overcast were built in the Colony Pilot Mine. Leakage rates were measured using both SF6 tracer gas techniques and the ?brattice window? method. The leakage was measured both before and after a full scale face blast. Blast air pressures were measured across two of the stoppings. Cost and leakage data were used to evaluate the projected overall performance of various combinations of the stoppings in a two-panel oil shale mine.

Jan 1, 1986

By E. Burdukova

Rheological measurements have found a wide array of applications in mineral processing research. Rheological properties of mineral suspensions are highly dependent on the mineral surface properties as described by DLVO theory, and the relationship between these properties and inter-particle interactions is well established. In this paper, rheological properties of mineral suspensions are used to study the differences in behaviour of isotropic talc and anisotropic zirconia minerals as a function of varying properties of the suspension medium, such as pH and polymer dosage, specifically carboxymethyl cellulose (CMC). It was found that the rheological tests when carried out in parallel with electrophoretic or point of zero charge measurements, clearly reveal differences between behaviour of the suspensions of isotropic and anisotropic minerals. These differences are further accentuated with the addition of carboxymethyl cellulose (CMC).

Jan 1, 2006

By Nancy Redhead

El buen funcionamiento de los equipos de una fábrica depende de la energía eléctrica. Si ocurriesen problemas con esta, se resuelven con tecnologías convencionales como la utilización de bancos de condensadores, filtros activos, UPS, estabilizadores de tensión y protectores de sobretensiones. Sin embargo, el riesgo de utilizarlas es que algunas veces son incompletas o no son compatibles. En ese sentido, el presente texto plantea una nueva tecnología utilizada en otros países que corrige los problemas eléctricos de forma completa y segura. Este un sistema automático completo de ahorro de energía y de la calidad de la onda eléctrica que está dotado de un microprocesador y analiza el voltaje, corriente, factor de potencia y armónicos. Asímismo, permite recuperar la energía perdida para luego filtrarla y devolverla a la red -al tiempo que se agrega una carga adicional sin necesidad de incrementar el tamaño de los transformadores o conductores.

Apr 1, 2013

By Jorge Black Florez

El presente texto describe la aplicación del programa de entrenamiento de seguridad para mineros en la Cerro de Pasco Corpotation. Este programa se basa en un estudio realizado entre los años 1956-1959, y consta de tres elementos: hacia quiénes va la instrucción, el tema a enseñar y la metodología a utilizar. La clasificación del personal según este programa, se divide en: obreros, supervisores y miembros de las cuadrillas de rescate minero. Los temas de instrucción son los tópicos generales para toda categoría de trabajador y los temas específicos de acuerdo a la naturaleza de las labores encomendadas. Finalmente se describe la práctica de los entrenamientos, la cual evidencia y reduce el índice de accidentes laborales, como estabiliza la productividad en la minera.

Jul 20, 1961

By R. H. Duthie

As at any other mine in Canada, grade control procedures are used at Steep Rock Iron Mines (1) in order to ensure that concentrator and pellet-plant operator s have a uniform feed so that they can manufacture a pellet to suit buyers' specifications and (2) to maximize ore recovery so that as little as possible finds its way to the waste dump or is downgraded by contamination. At Steep Rock, material grading 40% to 66 % Fe is considered ore. The ore may contain up to 10% sulphur. These ranges create six different stock pile types, with the possibility of more if large concentrations of arsenic are encountered. Although grading and mining techniques used to accomplish these ends are fairly standard, there is an appreciation and willingness by hourly and staff pit personnel to make grade control effective. This produces vertical and horizontal communication, which is necessary for success in this field. At Steep Rock, the waste-to-ore ratio is greater than at any other iron ore mine in Canada. Also, a high percentage of the ore mined is direct pellet feed. For these reasons, .grade control is very important.

Jan 1, 1977

By Robert A. Wilson

Los primeros pasos básicos para determinar los valores reales y los minerales concernientes, que son la base para las pruebas metalúrgicas, son presentados en este capítulo. A continuatión, eligiendo el proceso o los procesos indicados para el tratamiento de un mineral, son expuestos los temas. Todo esto es seguido por los procedimientos utilizados, el resultado de los cuales indicará la viabilidad para el tratamiento. Estas pruebas de procedimiento han sido desarrolladas, utilizadas y de probada efectividad en laboratorio con evaluaciones relativas al procesamiento de la planta. Los procedimientos especiales y poco comunes se encuentran fuera de la finalidad de este capítulo. La evaluatión de los resultados de las pruebas y su incorporatión dentro del flujograma preliminar y final para el diseno de la planta son temas igualmente expuestos. El valor de un flujograma, con balances de material y agua para el diseño de la planta, es asimismo mostrado.

Jan 1, 1982

By Carlos Benavente

La actividad sísmica del Perú se origina en el proceso de convergencia de la Placa de Nazca bajo la Sudamericana, donde la geometría de la placa oceánica presenta dos tipos de segmentos, una que subduce con un ángulo de 30º hacia el este y la otra, de bajo ángulo o subducción plana. En esta perspectiva, el presente texto describe la estructura y cinemática de la Falla Purgatorio Mirave (FPM) ubicada en la vertiente pacífica de la Cordillera Occidental del sur del Perú, entre la ciudad de Tacna y Moquegua. Dicha falla tiene una longitud aproximada de 40 km al nivel, donde la placa oceánica subduce con un ángulo de 30º al este y el vector de convergencia es oblicuo en relación a la zona de contacto de las placas. Asimismo, la geometría de la costa afecta también la distribución de la deformación y la morfología resultante. La geometría, morfoestructura y cinemática de la estructura se puede dividir en tres segmentos: el segmento Este presenta una traza de falla rectilínea, morfoestructura bien conservada y el último movimiento de tipo inverso, el segmento central de traza rectilínea y escarpe de falla bien conservado, donde se observa el mayor desnivel de la FPM (3.5 m) y que afecta los depósitos cuaternarios, según las medidas de estrías en el plano de falla nos indica que el ultimo movimiento fue de tipo dextral. Finalmente, el segmento oeste presenta su parte más oriental una traza rectilínea para luego hacerse curvilínea y formar una geometría de tipo cola de caballo o echelón hacia su parte occidental, este segmento muestra evidencias deque su último movimiento es de tipo inverso, formando pliegues de propagación de falla que afectan depósitos cuaternarios.

Sep 14, 2009

By P J. Mienie

The Palaeo-Proterozoic Transvaal Supergroup in the Northern Cape Province of South Africa is host to the largest known resources of high-grade hematite ore on the Southern African continent. These ores are currently being exploited at Sishen and Beeshoek. Hematite occurances on the Sishen South exploration project (some 65 km south of Sishen mine), are at present the focus of an intensive investigation. At both the Sishen and Sishen South deposits, mineralisation is found within lithologies belonging to the Transvaal and Oliphantshoek Supergroups. The Transvaal Supergroup comprises a basal, carbonate platform sequence (the Campbell Rand Subgroup) overlain by thick units of banded iron-formation belonging to the Asbestos Hills Subgroup. The Asbestos Hills Subgroup is unconformably overlain by sedimentary rocks of the Gamagara Subgroup. The latter Subgroup has been correlated with the lowermost unit of the Oliphantshoek Supergroup. The Sishen and Sishen South deposits are located close to the western margin of the Kaapvaal craton and have been subjected to intensive, structural deformation. Both localities have undergone folding, faulting and thrusting. Early regional tectonism (2400 - 1700 Ma) played a critical role in the genesis and preservation of the ores from younger erosive events. At both deposits, four similar iron ore occurrences have been recognised. The ores have developed in specific depositional environments and hence display unique physical, chemical and metallurgical properties:The bulk of the high-grade hematite comprises laminated and massive ores, which are found in the upper parts of the Asbestos Hills Subgroup. The laminated and massive ores are best developed in basinal and pseudo-graben structures. Collapse breccia ores of medium- and lower-grade are preserved within deep palaeosinkholes. The sinkholes have developed within the dolomites of the Campbellrand Subgroup. Lower-grade conglomeratic and gritty ores constitute the remainder of the deposits. These ores are found in the overlying clastic succession of conglomerates, shales and quartzites belonging to the Gamagara Subgroup. Although, there are many stratigraphic and lithological similarities between the Sishen and Sishen South deposits, there are also important differences, which will impact on the profitable exploitation of the ores. The most striking contrast between the deposits is their size and geometry. Sishen mine is a single pit operation with an opencast mineable reserve of 895 Mt. The Sishen orebody is thicker, more continous and significantly larger than the Sishen South deposit. The Sishen South deposit has a potential opencast reserve of 228 Mt. It comprises a number of small and narrow, isolated orebodies, spread over an area of ¦64 km2 . There is a significant difference in grade between the deposits. On average the orebodies of the Sishen South deposit have a higher iron content (+0.25 per cent Fe), less potassium (- 0.090 per cent K2O) and less phosphorus (-0.019 per cent P). The Sishen South deposit has less interbedded shale in the laminated and massive ores. The footwall of these high-grade ores is a light-density, intrusive sill, compared to banded iron-formation at Sishen. With a proposed heavy-medium separation plant at Sishen South, the impact of dilution on product grades is expected to be less than that currently experienced at Sishen.

Jan 1, 2002

By Fernando Kameoka

Desde o final da década de 90, com o desenvolvimento de novos parâmetros industriais para a fabricação de produtos eletroeletrônicos criou-se o conceito de obsolescência programada. Como consequência deste comportamento mercadológico e novos parâmetros de consumo, o volume de resíduos de equipamentos eletroeletrônicos gerado pelo descarte indiscriminado de produtos ainda em condições de uso tem atingido patamares alarmantes, tornando-se assim um grave problema ambiental. Com a Política Nacional de Resíduos Sólidos, estudos sobre a logística reversa dos resíduos provenientes de equipamentos eletroeletrônicos revelam-se promissores devido à presença de metais com alto valor de mercado, o que viabiliza economicamente os processos de reciclagem destes resíduos. Quando se trata da recuperação de metais e de reagentes, as rotas envolvendo etapas hidrometalúrgicas oferecem um grande benefício em relação às soluções existentes devido à não liberação de gases tóxicos durante o processo. No entanto, para a recuperação de cobre e alguns metais nobres as rotas hidrometalúrgicas tradicionais têm-se mostrado ineficientes devido à presença de ferro nos resíduos. Por esta razão, este trabalho tem como objetivo realizar estudo cinético da lixiviação de ferro de forma seletiva para a recuperação de outros metais. Foi analisado o processo de lixiviação em ácido sulfúrico na concentração de 2M, variando tempo e temperatura, com o intuito de avaliar a extração seletiva do ferro e viabilizando assim os processos subsequentes de recuperação de cobre e metais nobres através de extração sólido-líquido ou líquido-líquido. Os resultados apontam para extrações de ferro em solução de ácido com índices de pureza acima de 95%.

Aug 16, 2017

By K. Fountain

In Novemeber of last year I visited a mica mine in Hunan Province, China. For nine months , we had been trying to sell Chinese mica to a customer in Belgium. Talking to the customer was like negotitating with a stone wall. The buyer refused to communicate any -thing other than his steadfast refusal to consider Chinese mica. He would not advise us what he wanted, what specifications or grades. He would give no indication if our price at market, or reasonable, or totally out to lunch. He would not even accept samples. It took no genius to guess that the mica buyer had at some time in the past bought a shipment of Chinese mica and had received a disaster. I invited the mica mine in Hunan in order to see for myself what could be done - without massive investment in equipment and instruments - to upgrade the quality of the mica for export. We had seen this type of customer reaction before. One disgruntled customer who had pur¬chased pigment grade barites direct from China ranted and raved about unreliable and inconsistent quality. It did no good to explain to him that China is a big country, with hundreds of mines scattered throughout many areas, each producing a different product. Our further explanation that Chinese export organizations also varied in degree and efficiency of customer service fell on deaf ears. Samples had no effect on his perception. Eventually we showed him photoraphs of two mountains of pigment grade barites. One lot was our sales of pigment barites to a major European minerals processor. Our Chinese barites stood proudly white and beautiful next to a hill of other material which now appeared at best mediocre and dull by comparison, and which the buyer had decided to reject after he received our Chinese barites. Finally the customer was sufficiently impressed to look seriously at our guaranteed specification and the outturn analysis performed by our other customer.

Jan 1, 1987

By Felipe Fardin Grillo

Neste trabalho foram elaboradas escórias de aluminato de cálcio para refino de aço e comparadas com uma mistura industrial contendo fluorita em sua composição. As escórias foram analisadas por meio do software ThermoCalc e testadas em um banho metálico de aço SAE 1020 a 1600oC. O experimento foi conduzido em um forno de dissiliceto de molibdênio, sob atmosfera de argônio. Foram retiradas amostras até 30 minutos de experimento. Os resultados obtidos indicam que é possível obter até 78,7% de eficiência na remoção do enxofre utilizando escórias de aluminato de cálcio com 83,22% de fase líquida, mostrando que estas escórias cumprem o mesmo papel de dessulfuração das escórias com fluorita.

Oct 30, 2017

By Bora Derin

This work deals with the recovery of valuable metals from the ancient copper smelting slags located in Küre-Turkey. In this process, copper and cobalt were recovered in metallic form and/or as their compounds, whereas iron was recovered as magnetic oxide or pigment. Abrasive grit material was produced using reduced final slag. The process stages involved carbothermal reduction in a DC arc furnace, granulation, leaching, chemical precipitation, selective sulfidizing roasting and product preparations. In this paper, the process stages were described as theoretically and experimentally whereas slag and products were characterized in detail.

Jan 1, 2003

By Giovanni Franco Sepúlveda

Dado que los procesos de planificación minera en los depósitos a cielo abierto en Colombia se realizaron a través de herramientas deterministas que excluyen la evaluación de riesgos y las incertidumbres del negocio minero, se plantea modelos alternativos de planificación minera que optimizen las condiciones de competitividad y productividad a través del uso de los algoritmos genéticos y su aplicación a los procesos de planificación minera para explotaciones a cielo abierto. Es decir, se busca realizar una aproximación al planteamiento minero estocástico desde dichos algoritmos genéticos y así mejorar la cadena productiva del proceso minero.

Mar 1, 2014

By Paul Eger

The use of wetlands to treat mine drainage has become increasingly common, particularly as more information is available on their operation and construction. However, the lifetime of each system is still, at best, an estimate. Treatment lifetime depends on the types of processes that provide the majority of the metal removal. Anaerobic systems (vertical flow systems) rely primarily on sulfate reducing bacteria, which reduce sulfate to sulfide and generate alkalinity. Metals can be precipitated as sulfides, and acidity is neutralized. These systems can remove over 90% of the metals and increase pH from around 4 to over 7. The bacteria will remain active as long as the system remains anaerobic and contains an adequate supply of sulfate and small chain organics. Although estimates of lifetime made on the total carbon in the system suggest that lifetime should exceed 20 years, data from field and laboratory studies show that the rate of sulfate reaction decreases with time, and that after several years rates decreased substantially. To maintain acceptable treatment, either additional organic material must be added or the total metal and acid load to the system would need to be reduced substantially. Aerobic systems (overland flow wetlands) can effectively remove metals from neutral mine drainage by reactions with organic material in the substrate. Over 90% of the copper and nickel have been removed in aerobic systems treating mine drainage in Minnesota. The primary removal processes in these systems include adsorption, ion exchange and complexation, which are finite; removal will cease unless new removal sites are generated. Two wetlands built in Minnesota have been successfully treating mine drainage for 12 years. At one of the wetlands, the annual production of new removal sites has been estimated to be equal to the annual metal input, and, as a result, metal removal should theoretically continue indefinitely.

Jan 1, 2005

Preparation of MgO Nano-Particles with Magnesite

Sep 13, 2010