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By Oscar Delgado Venero

Dado el alto potencial económico de los metales preciosos que genera Centromin Perú, el yacimiento minero elaboró un programa de investigación para la recuperación del oro y la plata, a partir de minerales marginales, relaves y productos intermedios de fundición. Durante el desarrollo de este programa, se utilizó el proceso de lixiviación en botaderos la extracción de plata para la extracción de los minerales piríticos de Cerro de Pasco, obteniendo resultados óptimos. Por tal motivo, el presente texto señala el proceso de lixiviación en botaderos que Centromin decide implementar en una planta industrial, utilizando como lixiviante el sistema de Nac1-H2 SO4 y la chatarra de fierro como agente de cementación.

Nov 24, 1986

By Roberto Heredia Zavala

"El presente texto señala la posibilidad de interconexión de dos sistemas generadores de energía eléctrica, en donde la zona de influencia, carece notoriamente de agua potable para atender el consumo doméstico e industrial impuesto por el desarrollo de esta. Asimismo, La integración de los sistemas de generación de electricidad sería para el reemplazo del calor de los hornos con hidroelectricidad, haciendo así que el calor reemplazado se utilice en la desalinización de agua de mar y en consecuencia permita ia disponibilidad de agua potable para consumo doméstico e industrial. "

Mar 1, 1967

Mining education has received almost continuous discussion since its inception and most people engaged in the mining industry and in mining education feel at some time the urge and necessity to express their views. This paper is not a comprehensive survey of past and present practices and accepted principles, but a personal opinion of the form mining education should take at university level. It is expressed because of a dissatisfaction with the existing courses offered to students. It is hoped to provoke discussionand bring forth guidance to those engaged in mining education. After all, students spend four or five years at a university and it is desirable that the graduate should be something more than just those many years older at the end of his course.POST GRADUATE EMPLOYMENTThe first problem confronting the university should, be to discover what the mining industry wants and expects or graduates. This must influence the university course and yet universities have done little to seek this information, and if suggestions have been offered by industry; universities appear to have made little use of them. University mining curricula are basically what they were 50, 100 and even 200 years ago. (See Appendix.) Whether this reflects the unchanging problems of mining the wisdom of early professors, the conservatism of subsequent professors or inability to apprectate necessity for changes, is debatable.Unfortunately there is no uniformity in the type of employment offered to new graduates: Some mining...

Jan 1, 1959

By M. Y. Solar, W. G. Davenport

Most of the recent growth in nickel demand has been for the production of stainless steels and virtually all of it has been satisfied by new ferronickel and nickel pig iron projects. But "good" laterite resources are more and more difficult to find: Ni grades are decreasing while Fe contents are increasing and SiO2/MgO ratios vary from 1 to 3 and even higher if limonites are included. Predicting the smelting behaviour of such ores requires a more fundamental understanding of the thermodynamics of these systems in commercial operations. One valid question is thus whether these furnaces are at thermodynamic equilibrium or not. The present paper investigates this question, compares calculated and measured O2 partial pressures and mechanical/chemical slag loss ratios and concludes that ferronickel furnaces are not at thermodynamic equilibrium. This departure from expectation is actually to the operators’ advantage: the targeted ferronickel grades can be obtained at lower reduction potentials than calculated from pure thermodynamics.

Jan 1, 2014

By Milson de Andrade Júnior

A central termoelétrica número 1 (CTE#1) da Companhia Siderúrgica Nacional possui duas caldeiras em operação denominadas 8 e 9 com capacidade total de produção de vapor de 200 Toneladas por hora. Estas caldeiras fornecem vapor para os turbo geradores e turbo sopradores da CTE#1, além de vapor de processo para a Usina Presidente Vargas (UPV). As caldeiras entraram em operação em 1982/83 e seus sistemas de controle e instrumentação eram totalmente pneumáticos. Ao longo do tempo foi surgindo dificuldades para reposição e manutenção dos componentes pneumáticos, motivo pelo qual se iniciaram os estudos para substituição deste sistema. Em 2009 teve início um projeto para substituição do controle pneumático por um controle microprocessado feito por PLC redundante trabalhando com um supervisório scada e para substituição das malhas de instrumentação pneumática por instrumentação em rede fieldbus. A substituição completa dos componentes pneumáticos foi concluída em 2012. O novo sistema implantado trouxe diversas melhorias na performance, confiabilidade, segurança operacional e ergonomia. Este trabalho apresenta as causas que motivaram o projeto em questão, a metodologia utilizada para a sua implantação e os resultados alcançados com a aplicação de tecnologia moderna para controle e instrumentação de caldeiras.

Jul 31, 2018

By A. Eccles

Phase designs are the foundation upon which all open pit mine sequence optimizations and budgets should be built. Unfortunately, at times, mine engineers skip the step of developing realistic pit phase designs - designs that include access ramps and mineable widths. Without mineable phase designs, their optimized schedules are based on theoretical pit shells or ?quick-and-dirty? plans with no ramps. The output from such optimizations is almost always overly optimistic. Without mineable designs, the production estimates are misleading, because they overestimate ore, and underestimate waste stripping requirements. Worse yet, when plans are not based on realistic phase designs, they can point to exactly the wrong decision in feasibility studies (i.e. ?go? when it should be ?no-go?). This paper discusses the importance and features of good pit phase design, and demonstrates the pitfalls of relying on optimized production sequences that are not based on properly designed pit phases.

Feb 27, 2013

By D. E. Calisaya, É. Poulin, A. Desbiens, R. del Villar, A. Riquelme

"A 15 cm diameter by 732 cm height, fully automated pilot column was installed in the Agnico-Eagle’s Laronde concentrator (Québec), for evaluating the performance of newly developed sensors and advanced process control algorithms. For eventual comparison purposes, the pilot column is continuously fed with the same slurry feeding the copper-circuit third cleaner column. It is equipped with electrical conductivity-based sensors for estimating the three variables used in the multi-variable control algorithm under evaluation: froth depth, fraction of wash water underneath the interface and gas hold-up. Froth depth is regulated using a PI controller while a predictive controller is formulated as the minimization of the tracking errors of gas hold-up and bias rate, keeping several operating constraints between their practical upper and lower limits. In particular, an unreachable high set point of gas hold-up can be selected in order to maximize the bubble surface area available for particle collection, while maintaining bias rate above a minimum value required for froth cleaning. The proposed strategy may indirectly help optimizing flotation column operation by using these secondary variables, without the implementation of a real-time optimization layer.INTRODUCTION Flotation columns have already been used for more than 30 years, mainly in cleaning stages, as a result of their froth washing capabilities. Despite their widespread usage, the measurement of some pertaining variables and their use for automatic control is rather scarce. Among the most important variables directly related to the process metallurgy (concentrate grade and recovery), froth depth (hf) is the only one normally monitored and controlled. Even though commercial sensors are available, gas hold-up (eg), a variable directly related to concentrate recovery, is seldom measured and never controlled. Another important variable, bias rate (Jb) responsible for concentrate cleaning, is simply not measured at all, as there is no commercial sensor available. Therefore, besides froth depth, continuous monitoring of process variables is limited to flow rates (gas, feed, tailings, wash water), i.e. to manipulated variables. Some new available sensors have been industrially tested, e.g. the Sonar-TracTM for eg (O'Keefe, Viega & Fernald, 2007) and the McGill hold-up sensor (Tavera & Escudero, 2002). Others, for bias rate and frother concentration, have been successfully validated at laboratory scale by Laval’s LOOP researchers (Maldonado, Desbiens, del Villar & Chirinos, 2008b; Maldonado, Desbiens, del Villar & Aguilera, 2010a). Some devices have been extensively used for monitoring bubble size and space distri-bution, e.g. McGill bubble viewer (Gomez & Finch, 2007) and others."

Jan 1, 2012

By A. C. Fieldner, W. A. Selvig

For purposes of coal classification it is desirable to know the composition and calorific value of the pure coal substance; that is, of the coal free from its ash-forming minerals. Two methods suggest themselves: (1) To free the coal from most of the ash-forming material previous to the analysis; and (2) to analyze the coal as received and calculate the analysis, with certain more or less arbitrary corrections, to the pure-coal basis. Calculation methods are obviously more apt to give correct results with low-ash than high-ash coals. With coals of unusually high ash it would appear preferable to remove, previous to the analysis, as much of the inorganic matter as possible, by float-and-sink or acid-treating methods. Effect of Ignition on Inorganic Constituents of Coal The need of corrections in calculating analysis to the pure-coal basis is due to the fact that the ash, as determined by ignition, is not the same, in either weight or composition, as the inorganic mineral matter in the coal. On ignition a number of changes occur in the coal such as loss of water of hydration of the shaly material, conversion of pyrite (FeS2) to ferric oxide (Fe203) with evolution of the sulfur as sulfur dioxide or possible fixation of more or less of the sulfur in the ash as calcium sulfate (CaSO4), and decomposition of calcite (CaC03) to calcium oxide (CaO). The amount of sulfur from pyrite which remains in the ash as calcium sulfate depends on the amount of calcite and pyrite in the coal. Certain coals high in both calcite and pyrite show relatively large amounts of sulfate sulfur in the coal ash. The determination of total carbon and hydrogen in coal includes, besides the organic carbon and hydrogen, the carbon of inorganic carbonates such as calcite, and the hydrogen of the water of composition of some of the ash-forming minerals. For detailed discussion of corrections proposed for calculations of coal analyses to the " pure "

Jan 1, 1930

Process Simulation and Plant Design of a Mineral Selective Magnetising Flash Roasting Plant Using Neutrons

Sep 13, 2010

THE machine from which the following results were obtained makes one of a row of seven at work in the Junction North, Concentration Mill at Broken Hill, New South Wales. It consists essentially of a belt for dressing purposes, which travels round two 12-in drums situated at either end of a wooden frame. This frame is supported on wooden legs, and the whole is affixed to two iron castings, one on either side of the frame. A to-and-fro motion is obtained from an eccentric shaft, which, together with the stationary end of the supporting legs, is carried by the iron castings. A belt drive to the forward drum provides a constant rate of travel to the dressing belt.The top half of the dressing belt is supported on 3-in rollers spaced about 12-in centres along the frame of the vanner. A fairly thick dressing belt is used, and no trouble whatever is experienced from the formation of gutters between the rollers.These belts are 28 ft 4 in long, 4 ft wide, 3-16 in thick, and are made of two-ply 32-oz duck, with a coating of rubber on either side. The surface available for dressing is about 10 ft 6 in x 3 ft 8 in- ie, about 38'5 square feet. The machine is driven atthe rate of 245 i-in strokes per minute, while the dressing belt travels at 15 feet per minute...

Jan 1, 1909

By Vicente Martínez Guerra

Producto de una de las operaciones realizadas en la Cerro de Pasco Corporation, se obtienen algunos elementos y subproductos químicos como el arseniato de calcio que ocupa el primer lugar en ventas en dicha compañía. Por ello, el objeto del presente texto describe el proceso y el uso de As2 O3 para la fabricación del arseniato de calcio en la planta de fundición de La Oroya, como su aplicación de insecticidad mineral en la agricultura. Dentro de este periodo, el elemento químico será recuperado en el cottrell de arsémico, de los humos provenientes de los hornos tostadores de los minerales de cobre, precipitando una concentración oscilante entre 40 a 45% con un contenido de cobre de 4%. donde el polvo sufre una tostación para así concentrar el cobre por sublimación del arsénico. Asimismo en este sistema de fabricación de arseniato, la liberación del As2 O5 del piroarsenIato de calcio se realiza por ataque con ácido sulfúrico, garantizando la pureza de este óxido en la precipitación final del proceso. En consecuencia, la aplicación del arseniato de calcio, como insectida inorgánico mineral protege el sistema ecológico, dado su bajo contenido de arsénico soluble en agua, al tiempo que se ajusta a las reglamentos oficiale vigentes del país.

Jul 20, 1956

By J. A. McLennan, J. M. Ortiz

Nickel laterite deposits are typically formed from tropically weathered mafic-to-ultramafic complexes. The resulting nickel concentration is found within soil horizons and is mineable with regular dozer units. At the time of mining, digging elevations are needed at selective mining units (SMUs) or representative dozer regions (RDRs). Moreover, for mine planning, the costs due to dilution and lost ore require mining elevations to be specified. A conditional simulation approach is used to calculate “optimum” RDR mining elevations. Multiple realizations of the ore base surface are simulated. For a single bottom surface realization, dilution and lost ore costs are calculated over the entire vertical extent of each RDR. The optimum mining elevation is the elevation where the lowest summed cost of “accepting dilution” and “wasting ore” occurs. The reported RDR dilution is the cost of mining the volume of waste located below the bottom surface and above the optimum mining elevation. The reported RDR lost ore is the cost of not mining the volume of ore above the bottom surface and below the optimum mining elevation. For all ore bottom surface realizations, optimum RDR mining elevations and their associated dilution and lost ore costs are calculated and compiled to represent production uncertainty.

Jan 1, 2006

By Alberto Encinas

El presente texto describe el proyecto de explotación racional realizado en 1977 en la isla aurífera de Madre de Dios. El objetivo de este trabajo es justificar la adquisición de una retroexcavadora mediante un crédito del Banco Minero del Perú como una contribución al propuesto desarrollo de la minería aurífera.

May 1, 1978

By César Sotillo

"El presente texto describe el proceso de la industria del acero en México. La compañía fue fundada en el siglo XX y tiene sus altos hornos en Monterrey, capital del estado Nuevo León, donde se funden los minerales de fierro que provienen de los yacimientos del Cerro de Mercado, situado en la región central de Durango. El yacimiento consiste de cuerpos inclinados hacia el oeste y que tienen contactos bien definidos con la roca encajonante; Asimismo afloran cuatro cuerpos de mineral, de los cuales el más grande tiene cerca de 800 metros de longitud. El cuerpo mineral está dividido en dos partes por resbalamientos producidos por fallas en la porción occidental del valle; los mismos que junto con la erosión, han producido la peculiar topografía de esta parte del estado de Durango. "

May 1, 1953

I HAVE to thank the members of the Institute most cordially for the honour conferred upon me in selecting me President, which position my poor services have prevented my filling adequately. I have, therefore only been able to stumble through my year of office under the guiding direction of our esteemed Secretary. I fully appreciate the honour done to me; and, now that it is over, I can look back with pride and pleasure at having occupied the chair; but I am told that it remains for me to fill one of the requirements of our Institute and present you with what has been dignified by the name of a presidential address. My relief in complying with this is in the knowledge of its freedom from the usual discussion which appertains to papers presented by our worthy members. It has been usual in the past for the subject chosen to be specially connected with the work immediately engaging the attention of your president, and on this occasion I would like to break away from this time-honoured custom and engage your attention for a brief space on what is equally dear to us all namely, Ideals of the Profession. In doing so, the retort of Whistler to an art student gives me, I must admit, much misgiving, for, on being asked how he developed his artistic talents, replied that he painted what he saw, which produced the immediate reply, "Ah, but the tragedy will come when you see what...

Jan 1, 1909

By Hamed Khodadadi, Hamid Ghadiri

In this study, a fuzzy logic self-tuning PID controller based on an improved disturbance observer is designed for control of the ball mill grinding circuit. The ball mill grinding circuit has vast applications in the mining, metallurgy, chemistry, pharmacy, and research laboratories; however, this system has some challenges. The grinding circuit is a multivariable system in which the high interaction between loops, the variation of the system parameters with time, and time delay are some of the problems that pose a challenge. Since the controller parameters are determined offline in classic PID control, these gains are unchangeable and cannot overcome the mentioned challenges in this system. Hence, a fuzzy logic self-tuning PID controller, which is a combination of fuzzy logic and a conventional PID controller, is proposed to control the grinding system, especially in the presence of model mismatch and disturbances. In addition, in order to solve the system challenges, a multivariable control approach based on an improved disturbance observer is proposed to suppress the effects of the disturbances. The most important feature of the algorithm proposed in this paper as the combination of fuzzy logic self-tuning PID and improved disturbance observer is its ability to eliminate system interaction, attenuate internal and external disturbances, and compensate the effect of system uncertainty on the performance of the ball mill grinding circuit. Simulation results in the cases of the set-point change in particle size and circulating load in the presence of model mismatch and external disturbances confirmed the controller performance compared to other controllers.

By Hamed Khodadadi, Hamid Ghadiri

In this study, a fuzzy logic self-tuning PID controller based on an improved disturbance observer is designed for control of the ball mill grinding circuit. The ball mill grinding circuit has vast applications in the mining, metallurgy, chemistry, pharmacy, and research laboratories; however, this system has some challenges. The grinding circuit is a multivariable system in which the high interaction between loops, the variation of the system parameters with time, and time delay are some of the problems that pose a challenge. Since the controller parameters are determined offline in classic PID control, these gains are unchangeable and cannot overcome the mentioned challenges in this system. Hence, a fuzzy logic self-tuning PID controller, which is a combination of fuzzy logic and a conventional PID controller, is proposed to control the grinding system, especially in the presence of model mismatch and disturbances. In addition, in order to solve the system challenges, a multivariable control approach based on an improved disturbance observer is proposed to suppress the effects of the disturbances. The most important feature of the algorithm proposed in this paper as the combination of fuzzy logic self-tuning PID and improved disturbance observer is its ability to eliminate system interaction, attenuate internal and external disturbances, and compensate the effect of system uncertainty on the performance of the ball mill grinding circuit. Simulation results in the cases of the set-point change in particle size and circulating load in the presence of model mismatch and external disturbances confirmed the controller performance compared to other controllers.

By Léo Daiki Shinomiya

O trabalho apresenta estudos de cenários técnico e econômico para a implantação de uma pequena fábrica cerâmica, através do estudo de caso de uma prospecção de argila vermelha no interior do Pará. O estudo consistiu na execução de sondagem à trado (ST) na área, para cálculo volumétrico da reserva, e recolhimento de amostra para caracterizações em laboratório. A argila coletada foi submetida a análises do teor de umidade, química (Fluorescência de Raios-X) e mineralógica (Difratometria de Raios-X). Um cenário para uma empresa entre micro e pequena produtora de cerâmica foi estabelecido visando estimativas preliminares para um possível empreendimento. A análise de cenários levou a uma possibilidade de implementação de uma unidade fabril de cerâmica com capacidade produtiva de até 140 mil peças/mês. Restrições quanto ao tipo de produto desejado e a característica da argila prospectada devem ser consideradas, podendo ser necessário a mistura de argilas de base “gorda”, com maior quantidade de argilominerais.

Aug 17, 2017

By Manuel Álvarez Alvino

El presente trabajo señala el uso de las herramientas tecnológicas en los productos informáticos para controlar las operaciones mineras, dado que no existe un un producto concebido a la medida de cada operación ya que cada realidad es distinta de la otra, tanto en el detalle de la operación como en el aspecto administrativo. En este sentido, es importante la implementación de estos recursos, el control de la gestión, como en el de los estándares de los productos utilizados.

Jul 31, 2003

By Francisco Camus

El proceso de exploración en las campañas mineras es la primera fase del negocio y constituye una de los principales herramientas para su supervivencia, desarrollo y valorización de la industria. En este sentido, el presente texto señala la experiencia de Codelco en la exploración en Chile y su aplicación en Perú. Así, el conocimiento obtenido por Codelco realizado en el norte y centro de Chile, ha generado la formulación de modelos de exploración predictiva durantes los últimos diez años. Dichos modelos incorporaron el conocimiento logrado en el nivel de cada yacimiento individual, los entornos distritales y las franjas metalogénicas donde estos ocurren. En consecuencia, esta experiencia obtenida por Codelco y el reconocimiento de la continuidad en Chile, se extiende en el Perú y se presenta como una oportunidad de interés para el desarrollo de programas de exploración a futuro.

Sep 13, 2001