Search Documents

By José Bacilio

Durante los siete meses de operación de la planta concentradora Mallay de Compañía de Minas Buenaventura S.A.A., surgió la necesidad de integrar nuevos equipos en los circuitos de molienda y flotación. En ese sentido, el presente trabajo describe la forma de optimizar las recuperaciones de valores y calidad de los concentrados a través del proceso de flotación de plomo, plata y zinc, queemplea como base de cálculo la producción obtenida entre los meses de julio a octubre del 2012, dado que en este período se estabilizan los parámetros de molienda, adición de reactivos y circuitos de flotación.

Sep 21, 2013

By Segundo Velásquez, Enrique Mego, Robert Montes

La pila de lixiviación de minera Coimolache, después de 11 años de operación, actualmente cuenta solo con espacio para cargar mineral en el lift 18 a 150 m. de la geomembrana de base. Esta altura restringe la recepción de leyes pregnant en la poza PLS a 31 días por la velocidad de percolación, que se ha determinado en 5 m/día, considerando una humedad retenida de 10%; sumado a ello la calidad del mineral acarreado de los tajos Ciénaga y Mirador presenta contenidos de fino de hasta 60% m-1/8 en promedio, que perjudican la percolación de la solución cianurada a través de la pila de mineral.

Sep 30, 2022

La voladura es la herramienta económica más efectiva para fragmentar y mover rocas. Sin embargo, no puede ser empleado cuando un patron de voladura mal diseñado, ya que se genera un descontrol sobre la energía liberada. En este sentido, el presente texto describe el empleo de la prospección fotogramétrica estéreo y los sistemas de prospección de pozos en una operación de voladura en la cantera brasileña Incopel.

Apr 1, 2013

By Marco Flores

El proceso de optimización se inicia desde chancado reduciendo la granulometría de un K80 de 6,500 a 5200 micrones, en el circuito de molienda se baja la carga circulante en el sistema de clasificación de 305% a 150% reemplazando los hidrociclones convencionales por zarandas de alta frecuencia, en el circuito de flotación de Pb se optimiza la celda unitaria, se utiliza el dióxido de carbono como modificador de pH y se incrementa el tiempo de flotación de Pb instalando celdas tanque de 20 m3 en reemplazo de las celdas Agitair 48. El proyecto supero las expectativas por lograr un incremento de la capacidad de tratamiento en 15%, mejorando la calidad de concentrados y las recuperaciones de Ag-Pb, Zn.

Sep 1, 2017

By Luis Vente

El presente texto describe las mejoras implementadas en el proceso Gold Mill de Minera Yanacocha luego de 3 años de operación desde marzo 2008 hasta la fecha. El desarrollo de diferentes diseños en los revestimientos del molino y parrillas de descarga, el incremento del porcentaje de bolas, las mejoras en la voladura, la reducción del set de chancadora primaria y las pequeñas ampliaciones en la planta incremetaron la capacidad de diseño de planta desde 5 Mtpa a 6 Mtpa. El incremento de tonelaje no afectó significativamente al producto de molienda y recuperación, pero traslada el cuello de botella a los espesadores donde ahora se los esfuerzos de incremento de capacidad.

Sep 12, 2011

By Adrián Del Carpio

Desde 1995 la planta de Lixiviación de Toquepala desarrolló un sistema de control automático para los procesos de extracción por solventes y electrodepositación. Sin embargo, con el desarrollo de la tecnología y las nuevas versiones de control, dicha plataforma se tornó arcaica. En ese sentido, el presente texto señala la modernización de los sistemas relacionados con el control y supervisión de las áreas de extracción por solventes, depositación electrolítica y áreas auxiliares. Como consecuencia de ello, se incrementó la operatividad, disponibilidad y fiabilidad con cero paradas por perturbaciones eléctricas, así como redujo el tiempo utilizado para el diagnóstico y solución de problemas.

Sep 12, 2011

By Víctor Enrique Zapata S

El presente trabajo señala los métodos adecuados para lograr una optimización en la evaluación, diseño de la implementación y el abastecimiento de los fluídos de las operaciones mineras. Para ello, se estudia el problema de cada sistema y se diseña las modificaciones que se requieran para satisfacer la demanda de los servicios correspondientes como el abastecimiento de agua, relleno hidráulico y aire de ventilación.

Nov 8, 1984

By Jesús Ylazaca

El presente trabajo describe el método de control de calidad del mineral o el denominado "Ore control", realizado en la unidad minera Yauli, cuya finalidad es maximizar el valor del mineral minado para lograr una mayor rentabilidad. En este sentido, el "ore control" es la gestión que optimiza las diferentes etapas de la exploración, explotación y concentración del mineral para lograr una buena calidad de producto (concentrados), a fin de satisfacer las necesidades del cliente. Los controles involucran a la Gerencia y el total de supervisores y trabajadores de operaciones, quienes deben ser proactivos ejecutando acciones preventivas más que correctivas.

Sep 12, 2005

By Herly Alcázar

El presente trabajo describe el proceso de optimizacion en la fundición de precipitados de oro y plata en la refinería de la mina Pierina a través del control de los diversos parámetros que involucra dicho proceso. Para ello, se trabajó con composiciones ternarias cercanas al punto peritéctico y asi procesar adecuadamente el tipo de precipitado. Entre sus principales logros de optimización tenemos: el incremento de oro y plata, el rendimiento de los crisoles, la reducción de los costos por consumo de reactivos y el mantenimiento de la calidad del precipitado.

Sep 13, 2001

By Iván Turco

Las redes de distribución de energía eléctrica, compuestas por subestaciones, cables eléctricos de arrastre, conectores y accesorios, tienen la misma tecnología desde hace décadas. El presente trabajo muestra los excelentes resultados que obtuvimos frente a los problemas de salida de servicio y los tiempos extendidos en reconexión por fallas en los cables de arrastre y/o conectores con la finalidad de brindar la confiabilidad de alimentación de energía eléctrica a equipos movibles, asegurando la operatividad en campo, minimizando perdidas y maximizando la inversión en estos activos.

Sep 29, 2023

By Daniel Eduardo Parodi

Para acompañar el plan de aumento de producción de slabs de Siderar, fue necesario proyectar una nueva unidad separadora de aire para incrementar la generación de oxígeno, nitrógeno y argón. La premisa que direccionó este proyecto fue la integración y sinergia de la nueva unidad con el sistema de la Central Termoeléctrica y Altos Hornos, con el objetivo de salvar condicionamientos, obtener beneficios energéticos y aumentar la confiabilidad operativa. Como resultados de esta línea de trabajo se espera: Optimizar el aprovechamiento de gases de proceso, mejorando así el balance energético y la ecuación económica en la producción de los gases industriales; Mejorar el aspecto ambiental disminuyendo el quemado de gases en antorcha, reduciendo el consumo de combustibles fósiles y la compra de energía eléctrica; y aumentar la confiabilidad en el suministro de gases y del sistema de aire soplado a Altos Hornos.

Sep 25, 2017

By Omar Manfredo Herrera Terrazas

La voladura de rocas es una de las operaciones más relevantes dentro del proceso extractivo de minerales, cuyo objetivo es lograr un tamaño adecuado de roca, con un mínimo de daño en su entorno. Sin embargo, los resultados han sido adversos, incrementando los costos de operación. Por ello, el presente texto describe una metodología que basada en la exactitud del diseño de tiempos, optimiza los resultados de fragmentación en la mina Toquepala. Asímismo, incorpora la tecnología en su evaluación y desarrolla herramientas técnicas a objeto que permitan predecir el comportamiento de las variables que inciden en el desarrollo de las voladuras.

Sep 14, 2009

By Woodcock J. T

A sulphide ion selective electrode (ISE) is suitable for control of sodium sulphide additions in flotation because it has a rapid response to changeS in S2- concentrations, can indicate -low concentrations at differentpH values, suffers from few interferences, and is robust enou'gh to use in a pulp. Three sulphidization techniques were studied using the lSE electrode for measurement and/or control of S2- levels. Metallurgy was assessedfrom concentrate grades and copper recovery.With slug additions of sodium sulphide, sulphidizing conditions were poorly defined and reproducibility tended to be poor. Although acceptable metallurgy could be achieved by multiple additions, sodium sulphide consumption was high.Controlled potential sulphidization readily gave good metallurgy. The optimum potential of the lSE for sulphidizing was about -500 mV versus SCE, but depended on sulphidization and flotation times; suitable times were3 and 5 min respectively for three to five stages. Application of this technique to previously untested ores gave good metallurgy in a first test in spite of variation by a factor of three in the sodium sulphide requirements ofthe ores.Simultaneous sulphidization and flotation was satisfactory when conducted at an lSE potential of -450 mV versus SCE. Mixed cha!copyrite-oxide copper ores responded satisfactorily.Besides optimizing sulphidization conditions it is also necessary to optimize xanthate additions (e.g. by measuring xanthate residuals).

Jan 1, 1978

By Alexandra Kozak, Rodrigo Costa, Bob Fukuhara

"The Jacobina project in Bahia, Brazil commenced operations in 2004 with a design capacity of 4,200 tpd. A project development plan to increase plant capacity to 6,500 tpd will be discussed. The project included an evaluation of the existing circuit and addressed bottlenecks in the crushing, milling, sedimentation, leaching and tailings transport. These circuits and the methodology used to provide higher capacity will be presented.INTRODUCTIONThe Jacobina mine is located in the state of Bahia in northeastern Brazil approximately 330 km northwest of the state capital city of Salvador and 9 km from the town of Jacobina. The Jacobina Mine (Figure 1) is owned by Jacobina Mineração e Comércio, a wholly owned subsidiary of Yamana Gold Inc.The gold mineralization of the Jacobina mine is hosted within quartz pebble conglomerate reefs of the Serra do Córrego Formation which together with the Rio do Ouro Formation forms the Serra do Jacobina mountain chain.The Serra do Jacobina mountains have been mined for gold since the late 17th century. Since the 1970’s, the Jacobina mine has been operated by Anglo American, Williams Resources Inc., Desert Sun Mining Inc. The mine is currently owned by Yamana Gold Inc.In December of 1998, operations at Jacobina were suspended and the property was placed under care and maintenance. Desert Sun Mining Inc. began exploring the property in 2002 and eventually purchased the Jacobina mine in 2003. In 2003, a feasibility study was completed that evaluated the economics of re-developing the mining operations and expanding gold production. In 2004, refurbishment and re-development of the mining operations began and the milling facility throughput capacity was expanded from 1.08 to 1.512 Mtpy (3,000 to 4,200 tpd). The milling operations were commissioned in the 1st quarter of 2005 and commercial production was declared 1 July 2005. In April 2006, Yamana Gold Inc. acquired the Jacobina mine through its acquisition of Desert Sun Mining Inc."

Jan 1, 2008

By D. Moradkhani

Copper metal has important role in the basic industrials, as if it did not exist, modern human life would not develop! Copper leaching, as the first step, is important step in copper production processes. In this research, efficient factors on the leaching have been investigated. For this reason, four efficient factors on leaching namely pH, liquid to solid ratio (L/S), temperature and time, as independent variables, were optimized using response surface (RSM) with D-optimal. A quadratic equation was used to create response and contours. According to the results from analysis of variance (ANOVA), the value of determination coefficient (R2=96.77%) indicates that the model was good fit. Optimum experiment condition also was found: pH of 1, L/S of 8.24, temperature of 26.06 ? and time of 43.64 min. At this condition, the maximum recovery of copper was equaled to 92/38 in which good desirability achieved.

Sep 1, 2012

By Jorge Cárdenas, Alejandro Luna

In mining simulation for fragmentation results prediction is of utmost importance to study feasibility, ensure safety, and estimate the correct use of resources in drilling an explosive to meet requirements and avoid excessive usage. One critical case is fragmentation prediction, developed through models. Developing a fragmentation model in a mining unit aims to control blasting results to align theoretical and real data and improve correlation. Therefore, it is essential to collect post-blast fragmentation data, organize it, and systematically process it to develop a suitable model that meets variable requirements. Using a robust system of equations, this model should generate the required results with minimal variability between simulation and actual results. Additionally, this model must be adaptive to reduce this variability. Studying the most known and used models in mining resulted in our work correlating Cunningham 2006, Swebrec, and CZM models. Thus, the Simfrag model was created, presenting a robust foundation and combining the most notable advantages of the aforementioned models.

Jan 21, 2025

By H. S. Rathor

NTPC (National Thermal Power Corporation), a multi-unit organization, is generating 26% of India’s total power. This power is produced from its 14 coal based stations and 7 gas based stations. NTPC is entering into the business of power-distribution, power-trading, setting up of coal mines and diversification in non-conventional energy sector as well. For achieving the goal of the country “Power for All” NTPC has taken a giant stride by entering into Hydro Power generation which is also the cheapest and the cleanest renewable source of energy. In its pursuit for excellence, 800 MW Koldam Hydro Power Project is NTPC’s first venture in hydro sector. In Koldam, hydropower potential will be harnessed by constructing a 163m high earth and rock fill dam in a narrow gorge at upstream end of Bhakra reservoir. The river diversion is envisaged through two parallel, 14m finished diameter ‘horseshoe’ tunnels of length 901m and 934m at village Kian on the right bank, where the river forms a 180° loop. The diversion tunnels are designed to accommodate a flood of 6500m3/sec, taking into account the maximum probable discharge of 200 years return period. The tunnels pass through dolomite and limestone rock formations. The excavation of tunnels was done with drill and blast method. The excavation was attempted from both inlet and outlet faces. During geological investigation a rock fault was located at the outlet area. The location of the fault was such that it was passing through the edge of the Tunnel-1portal and around 30m away from the face of the Tunnel-2 portal. The quality of the rock at Inlet was also poor. To save the portals from slips, excavation of the tunnels was planned to start after the completion of the open excavation and its support system both at inlet and outlet. The tunnel excavation at inlet was envisaged by approaching the tunnels’ portal by constructing a road through 540EL bench and meeting the inlet portals on the upstream end, which would have been ready by mid2003, only after completion of the open excavation and its support system. To save time and cost, it was felt necessary to modify the planning by starting the tunnel excavation simultaneously along with open works both at inlet and outlet. The excavation at the inlet face of the tunnels started in December 2002 after rerouting the approach road to inlet portals through haulage road on the downstream and similarly Tunnel-1 at the outlet was started in the low cover area before completion of open area works. Thus the tunnel—heading excavation was started nearly 06 months early with the change of methodology.

Jan 1, 2005

By Beatrice Pierre, Juan Carrasco

Altonorte began as a concentrate roasting operation in 1988 under the name of Refimet. In 1993, a copper smelter was built with a design capacity of 203,000 tonnes per annum of concentrate. Since 2001, many technological advances have been made in Altonorte, where the biggest Noranda Reactor in the world is installed being the first Noranda Reactor reaching above one million tonnes of copper concentrates processed per annum. In 2013, Altonorte was acquired by Glencore. Recently due to various new environmental regulations in Chile, Altonorte has evolved to new standards of operation in order to reach the vision of becoming a World Class Smelter. This paper describes the path followed to improve safety, environmental performance, process capacity, reliability, and productivity. The foundation for the growth and success in Altonorte is our People. Employee engagement and branding of our cultural journey is what allows Altonorte to face the future with the certainty of becoming a World Class Smelter. INTRODUCTION Altonorte is located in Antofagasta, the mining capital in the north of Chile and is the last smelter built in Chile practically completed with second hand equipment. The biggest technological change in Altonorte occurred during the phase 3 expansion in 2003, where the old Reverberatory furnace was shut down and replaced by the biggest Noranda Reactor installed in the world. The vessel measures 5.3 m × 26m. ºAdditionally, this project contemplated a new rotary dryer, three (3) new Peirce Smith converters, new anode furnaces and a new Acid plant. The nominal capacity was to treat 816.000 tons of new concentrate per year. In 2008, a new expansion phase was implemented where a new double absorption acid plant replaced the oldest acid plant. Bottlenecks such as blowing capacity and oxygen availability were solved installing a new air blower and a new contract was negotiated with our oxygen supplier to increase oxygen availability up to 683 tpd. This improvement defined the current nominal capacity of 1.100.000 ton of new concentrate per year. Current process description All concentrates are received by trucks directly from domestic mines or from the Antofagasta international port in cases of imported concentrates; the concentrate warehouse has a capacity of 25 kt where the blend is prepared to feed the smelter.

Jan 1, 2019

By Tiejun Chun, Gutian Mu, Jiaxin Li, Hongming Long, Zhengwei Yu, Ning Li

The basic characteristics of iron ore, including assimilation, fluidity, cohesive phase strength and the ability to produce calcium ferrite, are often used to evaluate the sintering properties of iron ore and guide the optimization of iron ore blending. Six kinds of common iron ore used in a steel company in China were selected in this work. The basic characteristics of the single iron ore and blended iron ores were studied, as well as the difference between weighted averages of basic characteristic index of single iron ores and the real value of basic characteristic index of blended iron ore under different ore blending ratios. The results shew that the liquid phase liquidity, cohesive phase strength and calcium ferrite formation ability had a significant linear positive correlation with SiO2 content. The weighted average of basic characteristic index of single iron ore cannot fully reflect the actual blended iron ore properties. The optimization of the blending ratio can be achieved through the detection of the basic characteristics of the mixed iron ore, combined with the basic characteristics of iron ores.

Mar 1, 2018

By B. J. Zhang

Conventional spirals are capable of providing excellent clean coal recovery, although at a relatively high ash content. Compound spirals, which provide two stages of spiral cleaning in a single taller unit, have been commercialized in recent years to improve upon the cleaning performance obtained from conventional spirals. The present study aimed at optimizing the performance obtained from a compound spiral for cleaning especially high sulfur fine and ultrafine coal. Industrial-scale spiral units were utilized for this study in a pilot-scale facility at the Illinois Coal Development Park. A statistically designed experimental program was conducted to optimize ash and sulfur cleaning performance of the compound spiral. It was found that significant cleaning of ultrafine coal (i.e., 150 microns × 45 microns and even 45 microns × 25 microns size coal) is achievable with the compound spiral. However, operating conditions for cleaning finer coal fractions (-150 microns size coal) have to be significantly different from those used to clean coarser coal fractions (+150 microns size coal). The sulfur rejection trends were different from ash separation efficiency trends in all size fractions except 45 microns × 25 microns. The probable error (Ep) and effective specific gravity of separation (SG50c) determined for the compound spiral cleaning of the overall particle size were as low as 0.07 and 1.62, respectively. However, the bypass of a small percentage of clean coal to the tailings stream of the compound spiral, may need further adjustment of the key process parameters.

Jan 1, 2014