Evolution of the Isamill™ Into Magnetite Processing
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From Base Metals and Back – Isamills and Their Advantages in African Base Metal Operations
The Southern African Institute of Mining and Metallurgy Base Metals Conference 2013 H. de Waal, K. Barns, and J. Monama From base metals and back – IsaMills and their advantages in African base metal operations H. de Waal, K. Barns, and J. Monama Xstrata IsaMill™ technology was developed from Netzsch Feinmahltechnik GmbH stirred milling technology in the early 1990s to bring about a step change in grinding efficiency that was required to make Xstrata’s fine-grained lead/zinc orebodies economic to process. From small-scale machines suited to ultrafine grinding, the IsaMill™ has developed into technology that is able to treat much larger tonnages, in coarser applications, while still achieving high energy efficiency, suited for coarser more standard regrind and mainstream grinding applications. The unique design of the IsaMillTM, combining high power intensity and effective internal classification, achieves high energy efficiency and tight product distribution which can be effectively scaled from laboratory scale to full-sized models. The use of fine ceramic media also leads to significant benefits in downstream flotation and leaching operations. These benefits are key drivers for the adoption of the technology into processing a diverse range of minerals worldwide, and offer major opportunities for power reduction and improved metallurgy for the African base metal operations. Keywords: IsaMill, regrind, energy efficiency, inert grinding. Introduction The development of the IsaMillTM, by MIM (now GlencoreXstrata) and Netzsch Feinmahltechnik GmbH, was initiated to enable the development of the fine-grained ore deposits at Mt Isa and McArthur River in Northern Australia. To liberate the valuable minerals and so produce a saleable concentrate this ultrafine-grained ore needed to be ground to a P80 of 7 μm. -
Orica's Flotation Reagents Increase Copper Recovery Rates, Resulting in a $2M Increase in Gross Revenue
Greater understanding, improved performance Orica’s flotation reagents increase copper recovery rates, resulting in a $2M increase in gross revenue WHO WAS THE CLIENT? combined with sodium isobutyl Xstrata Mount Isa Mines form one xanthate (SIBX). As a result, DSP 330 “The best flotation of the largest underground mining was chosen for plant trial. operations in the world. The plant trial supported the initial performance was The mines, based in North laboratory results, with copper achieved with the Queensland, produce both copper recovery improving by 3%. 50:50 addition ratio and zinc-lead-silver. Established Further laboratory testing and plant in 1924, 5,700 employees and trials conducted by Mount Isa Mines of DSP 330 and contractors today work across found an improvement in overall SIBX, with a copper Xstrata Mount Isa’s twin mining recovery of 3.5%. As a result, and processing streams. DSP 330 was adopted as specialty recovery of 92.4% for collector of choice when treating a head grade of 5.4% WHAT WERE THE CHALLENGES? slow cooled copper slag. Xstrata needed to improve copper and a cut-off copper recovery and called on Orica to WHAT WERE THE KEY grade of 24-25%.” identify and test collectors. OUTCOMES? Orica formulated a collector that would enhance milling and Pengfu Tan, Alberto Galvez, Lucya Yunus– Mount Isa Mines flotation of slow cooled copper slag. Identification of Ultimately, the process needed to achieve superior recovery of copper superior collector at a natural pH over a specific grind fineness. Xstrata’s key requirements were to: Optimised flotation • Identify superior collectors performance • Reduce reagent costs • Optimise flotation performance • Integrate improvements into 3.5% improvement existing operations in copper recovery HOW DID ORICA HELP? Orica developed a laboratory test work program using Xstrata’s current Reduction in performance as a benchmark. -
Optimisation of an Industrial Scale Ball Mill Using an Online Pulp and Ball
OPTIMISATION OF AN INDUSTRIALTown SCALE BALL MILL USING AN ONLINE PULP AND BALL LOADCape SENSOR of Thesis submitted in fulfilment of the degree of Master of Science University Pratish Keshav KSHPRA001 _______________ May 2013 Page | 1 The copyright of this thesis vests in the author. No quotation from it or information derived from it is to be published without full acknowledgementTown of the source. The thesis is to be used for private study or non- commercial research purposes only. Cape Published by the University ofof Cape Town (UCT) in terms of the non-exclusive license granted to UCT by the author. University ABSTRACT The secondary milling circuit at Waterval UG2 Concentrator had undergone a circuit change with the commissioning of the IsaMill, a horizontally stirred mill, in parallel with the secondary ball mill. The operation treats the PGM bearing UG2 ore type and produces a final concentrate enriched with PGM’s. The concept was to treat the finer silicate rich fraction in the IsaMill and the coarser chromite rich fraction through the ball mill. This circuit is typical of a UG2 plant in which maximum silicate with minimal chromite breakage is targeted. As a result of the circuit change an opportunity for optimisation around the industrial scale ball mill was considered for this study. Of concern in this study were new operating conditions for the mill in the changed circuit at which improved performance could be obtained. Another objective was to investigate if a difference in breakage response for the silicate and chromite fractions could be identified for different operating conditions in the ball mill. -
Grained Pyrite in the Mount Isa Copper System
Trace Element Variation of Coarse- Grained Pyrite in the Mount Isa Copper System Thesis submitted in accordance with the requirements of the University of Adelaide for an Honours Degree in Geology Shauna Maguire-Olstad November 2016 Shauna Maguire-Olstad Mt. Isa Coarse-grained Pyrite TRACE ELEMENT VARIATIONOF COARSE-GRAINED PYRITE IN THE MOUNT ISA COPPER SYSTEM MT.ISA COARSE-GRAINED PYRITE ABSTRACT The unique Mount Isa system, northwest Queensland, contains two world class deposits of copper and lead-zinc, which have a complex spatial relationship. The formation of the copper mineralization has long been debated, and occurs in a close spatial and temporal association with silica-dolomite alteration and coarse-grained pyrite (Pyrite 2). The geochemical characteristics of coarse-grained pyrite has not previously been studied and it is believed to hold valuable insight into the fluid evolution of the Mount Isa Copper System. Using LA-ICP-MS analysis, trace element variation of Pyrite 2 was investigated for numerous elements including Ag, As, Ba, Co, Cu, Mo, Ni, Pb and Zn across an explorative transect (drill hole 0406ED2), which passed through the alteration halo of the 1100 orebody. The trace element composition of Pyrite 2 was not consistent throughout the 0406ED2 transect and it does not appear to be controlled by host lithology. The analysis determined the Pyrite 2 grains formed during, or in close association with, the ore-mineral enriched hydrothermal fluid. Pyrite 2 data is consistent with the Mount Isa system having undergone multiple hydrothermal fluid events or from an evolving hydrothermal fluid. The trace element variation of Pyrite 2 is consistent with the currently established paragenesis and is indicative of the concurrent Cu, Pb and Zn mineralising system formed during protracted hydrothermal events. -
Challenges Related to the Processing of Fines in the Recovery of Platinum Group Minerals (Pgms)
minerals Review Challenges Related to the Processing of Fines in the Recovery of Platinum Group Minerals (PGMs) Kirsten C. Corin 1,* , Belinda J. McFadzean 1, Natalie J. Shackleton 2 and Cyril T. O’Connor 1 1 Centre for Minerals Research, Chemical Engineering Department, University of Cape Town, P Bag X3, Rondebosch, Cape Town 7700, South Africa; [email protected] (B.J.M.); [email protected] (C.T.O.) 2 Minerals Expertise Tech Pty Ltd., Germiston 2007, South Africa; [email protected] * Correspondence: [email protected] Abstract: In order to increase the recovery of PGMs by flotation, it is necessary to optimise the liberation of the key minerals in which the platinum group elements (PGEs) are contained which include sulphides, arsenides, tellurides, and ferroalloys among others, while at the same time ensuring the optimal depression of gangue minerals. In order to achieve this, comminution circuits usually consist of two or three stages of milling, in which the first stage is autogeneous, followed by ball milling. Further liberation is achieved in subsequent stages using ultra-fine grinding. Each comminution stage is followed by flotation in the so-called MF2 or MF3 circuits. While this staged process increases overall recoveries, overgrinding may occur, hence creating problems associated with fine particle flotation. This paper presents an overview of the mineralogy of most of the more significant PGM ores processed in South Africa and the various technologies used in comminution circuits. The paper then summarises the methodology used in flotation circuits to optimise recovery Citation: Corin, K.C.; McFadzean, of fine particles in terms of the collectors, depressants, and frothers used. -
Energy Efficiency Analysis of Copper Ore Ball Mill Drive Systems
energies Article Energy Efficiency Analysis of Copper Ore Ball Mill Drive Systems Piotr Bortnowski, Lech Gładysiewicz, Robert Król and Maksymilian Ozdoba * Department of Mining and Geodesy, Faculty of Geoengineering, Mining and Geology, Wroclaw University of Science and Technology, 50-421 Wroclaw, Poland; [email protected] (P.B.); [email protected] (L.G.); [email protected] (R.K.) * Correspondence: [email protected] Abstract: Milling is among the most energy-consuming technological stages of copper ore processing. It is performed in mills, which are machines of high rotational masses. The start of a mill filled to capacity requires appropriate solutions that mitigate the overloading. One method for increasing the energy efficiency of ball mills is to optimize their drive systems. This article looks at two variants of drive systems with efficiencies higher than the already existing solutions. The first variant is a low-speed synchronous motor with permanent magnets without a gearbox, and the second variant is an asynchronous high-efficiency motor with a gearbox and a fluid coupling. The energy performance analysis of the three solutions was based on the average energy consumption indicator per mass unit of the milled material and on the energy consumption per hour. The investigations required models of the drive systems and analyses with the use of the Monte Carlo methods. The highest energy efficiency is observed in the case of the solution based on the permanent magnet motor. However, the drive system with the high-speed motor offers a gentle start-up possibility owing to the fluid coupling. -
Regrinding and Fine Grinding Technology - the Facts and Myths
A review of regrinding and fine grinding technology - the facts and myths Dr Alex Jankovic, Metso Minerals Process Technology Asia-Pacific, [email protected] ABSTRACT Stirred milling technology is used extensively for fine grinding in the ceramic, paint and pharmaceutical industrials. It has been recently adopted by the mining industry. Specific conditions in the mining industry require somewhat different operation of this technology. However, the basic principles of operation are the same and the accumulated knowledge and experience developed in these other industries could be used to assist mining operations to get the most benefit from the stirred milling technology. This paper presents some of the important aspects of stirred milling operation discussed in the literature and not commonly known within the mining industry: grinding media motion, active grinding volume, wear of grinding media and energy transfer, stress intensity, scale-up issues and flow limitations. The intention is to introduce a “different perspective” of stirred milling technology, in particular highlighting its potential benefits and limitations. HISTORY Stirred milling technology may be regarded as relatively new in minerals processing, however it is a mature and extensively used technology in the ceramic, paint and pharmaceutical industries. The latest development of this technology is in the area of “Nano-grinding” for grinding down to nano-sizes. One may say that stirred mills used today in mining and minerals processing are equivalent to the early models of stirred mills used in parallel industries. The most commonly used stirred mills in mining and minerals processing are the VERTIMILL®, STIRRED MEDIA DETRITOR (SMD®) and ISAMILL® and a brief history of their development is given below. -
Isamill™ Technology Used in Efficient Grinding Circuits
1 IsaMill™ Technology Used in Efficient Grinding Circuits B.D. Burford1 and L.W. Clark2 High intensity stirred milling is now an industry accepted method to efficiently grind fine and coarse particles. In particular, the IsaMill™, which was invented for, and transformed the fine grinding industry, is now being included in many new comminution circuits in coarser applications. While comminution has always been regarded as important from a processing perspective, the pressure being applied by environmental concerns on all large scale power users, now make highly energy efficient processes more important than ever. The advantages that were developed in fine grinding in the early IsaMill™ installations have been carried over into coarse grinding applications. These advantages include a simple grinding circuit that operates in open circuit with a small footprint, the ability to offer sharp product size classification, as well as the use of inert media in a high energy intensive environment. This paper will examine the use of IsaMill™ technology in fine grinding (P80 below 15 micron), and examine the use of the technology in conventional grinding applications (P80 20 - 150 µm). Recent installations will be examined, including fine and coarse grinding applications, as well as the recent test work that was undertaken using an IsaMill™ in a primary grinding circuit, and the resulting circuit proposal for this site. While comminution has been relatively unchanged for the last century, the need to install energy efficient technology will promote further growth in IsaMill™ installations, and result in one of the biggest challenges to traditional comminution design. 1. Senior Process Engineer, Xstrata Technology, L4, 307 Queen Street, Brisbane 4000, Qld, Australia 2. -
The Effect of Regrinding Chemistry and Particle Breakage Mechanisms on Subsequent Cleaner Flotation Xumeng Chen Beng and Meng in Materials Engineering
The Effect of Regrinding Chemistry and Particle Breakage Mechanisms on Subsequent Cleaner Flotation Xumeng Chen BEng and MEng in Materials Engineering A thesis submitted for the degree of Doctor of Philosophy at The University of Queensland in November 2014 Sustainable Minerals Institute Julius Kruttschnitt Mineral Research Centre Abstract Regrinding rougher flotation concentrates is typically used to liberate valuable minerals from gangue prior to the cleaner separation stage in processing of low grade ores. Compared to the rougher flotation after primary grinding, it is usually more challenging to achieve a satisfactory performance in post-regrind cleaner flotation especially when fine particles are generated. One main factor which results in this reduction in flotation is the unsuitable particle surfaces produced after regrinding. However, this factor is not usually considered when designing and optimizing the regrinding process. Extensive studies have demonstrated that grinding chemistry can influence mineral floatability. However, earlier studies focused on primary grinding and rougher flotation rather than regrinding and cleaner flotation. In addition, different types of regrind mills are used in industry, and these provide different particle breakage mechanisms which may also influence mineral floatability. Therefore, the overall objective of this thesis study is to investigate the effects of regrinding chemistry and particle breakage mechanisms on the cleaner flotation. The implementation of regrinding in the copper and pyrite flotation circuits at Telfer gold mine was taken as a case study and four research areas were addressed with the objective of developing fundamental understanding to provide practical guidance for the plant operation. The four areas investigated are: 1. Effect of regrinding chemistry on copper activation of pyrite and its flotation; 2. -
Telfer Processing Plant Upgrade – the Implementation of Additional
Telfer Processing Plant Upgrade – The Implementation of Additional Cleaning Capacity and the Regrinding of Copper and Pyrite Concentrates D R Seaman1, F Burns2, B Adamson3, B A Seaman4 and P Manton5 ABSTRACT The Telfer concentrator, located in the Great Sandy Desert of Western Australia, consists of a dual train gold/copper operation processing ore from one underground and, currently, two open pit mines with differing mineralogy. The fl otation circuit of each train was designed to operate in several modes depending on the feed mineralogy. The majority of ore mined at Telfer is processed in a sequential mode where copper minerals are fi rst fl oated into a saleable copper concentrate followed by the fl otation of an auriferous pyrite concentrate which is treated in an on-site hydrometallurgical plant (carbon-in-leach (CIL)). Gold is recovered as a gravity product within the primary grinding circuit, to the copper concentrate, and to a lesser extent, the CIL circuit. Since Telfer was re-opened, with a new concentrator, in 2004, the processing plant has struggled with poor copper concentrate grades, partially due to the excessive entrainment of non-sulfi de gangue minerals in the copper fl otation circuit and, more recently, due to composite copper particles produced when processing ore from a supplementary satellite pit that has not previously been processed through the new Telfer concentrator. Gold recoveries in the CIL circuit have also been below industry standard. This paper presents the implementation of recent changes made to the circuit to address these performance issues. The reconfi guration of the circuit has involved the installation of the following major equipment items: two ISAMills™ in ultra-fi ne grinding applications (one in the copper circuit and one in the pyrite circuit), two Jameson Cells to improve fi ne gangue rejection and a bank of 5 × Outotec TC30s to recovery copper and gold from the reground pyrite stream. -
Comminution of Copper Ores with the Use of a High-Pressure Water Jet
energies Article Comminution of Copper Ores with the Use of a High-Pressure Water Jet Przemyslaw J. Borkowski Faculty of Geo Engineering Mining and Geology, Wroclaw University of Technology, 50-370 Wroclaw, Poland; [email protected] Received: 4 November 2020; Accepted: 27 November 2020; Published: 28 November 2020 Abstract: The article presents research on the comminution of copper ore in a self-constructed mill using high-pressure water jet energy to investigate the usefulness of such a method for comminuting copper ore. As a result, ore particles are obtained that are characterized by appropriate comminution and a significant increase in their specific surface, in turn allowing for potential further processing of the mineral. A comparative analysis of the efficiency of copper ore comminution, primarily taking into account the unit energy consumption and the efficiency of the milling process, clearly indicates that the energy absorption of hydro-jet material comminuting is lower than during mechanical grinding, e.g., in a planetary ball mill. The applicability of the technique depends on the brittle nature of the host rock, e.g., it is especially appropriate for sandstone and shale ores. Keywords: copper ore comminution; hydro-jet mill; high-pressure water jet 1. Introduction Shredding processes are widely used in various fields of raw material processing. Such procedures are carried out in order to lower the costs of maintaining the cutter discs used in Tunnel Boring Machines (TBM) operating in hard rock formations [1]. They are also used to obtain fine-grained particles, sometimes even nanoparticles [2] or those that have an increased specific surface, which can be especially useful in pharmaceuticals [3]. -
Xstrata Technology Update Edition 13 – April 2012 Building Plants That Work
xstrata technology update Edition 13 – April 2012 Building plants that work You have to get a lot of things it takes another operator to get them right to build a plant that works. right. Someone who has lived through the problems, had to do the maintenance, operated during a midnight power Of course the big picture must be right – doing the right project, in the right place, failure, cleaned up the spill. Someone at the right time. who has “closed the loop” on previous designs; lived with previous decisions After that, the devil is in the detail. You and improved them, over and over. need a sound design, good execution, good commissioning, and ongoing This is why Xstrata Technology provides support after commissioning. You need a technology “package”. Just as a car to operate and maintain your plant in is more than an engine, technology is the long run, long after the construction more than a single piece of equipment. company has left. That’s when all the Technology is a system. All the elements “little” details become important – how of the system have to work with each easy is it to operate, how good is the other and with the people in the plant. maintenance access, what happens in We want our cars designed by people a power failure, where are the spillage who love cars and driving. So should points and how do we clean them our plants be designed by people with up? Are the instruments reliable and experience and passion to make each is the process control strategy robust one work better than the last.