Half-Yearly Report 2012 Six Months Ended 30 June 2012 Xstrata Plc Half-Yearly Results 2012 | 1
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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. -
Heart of Gold Lesson Plan Year 7
Heart of Gold Lesson Plan Year 7 Lesson 1 Separation of Gold Curriculum Links: (ACSSU112) / Year 7 / Science / Science Understanding / Chemical Sciences (ACSSU222) / Year 7 / Science / Science Understanding / Earth and Space Sciences (ACSHE119) / Year 7 / Science / Science as a Human Endeavour / Nature and Development of Science (ACSHE121) / Year 7 / Science / Science as a Human Endeavour / Use and Influence of Science Background Information: It is actually quite unusual to find large nuggets of gold and most gold prospectors actually need to separate gold out from lots of other material. Depending on where the gold is found, this may be done by panning or through dry blowing. Each of these methods relies on the property of density. As gold has a very high density compared to the rock, soil and sediments it is contained in, it can be separated out by exploiting this property as it will fall to the bottom of mixtures that are allowed to settle out. The process of panning is used when small pieces of gold are found in creeks and rivers. It involves using a large shallow dish (pan) to scoop out some of the sediments in the riverbed and a small amount of water. You use a swirling motion with the pan tipped away from you and allow small amounts of the sediments and water to spill over the edge of the pan. When you have only a small amount of the sediments remaining in the pan, you will be able to see any gold particles that remain at the bottom of the pan. During the West Australian gold rush, most of the gold was being found in dry areas and water was a scarce commodity. -
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. -
Metal Extraction Processes for Electronic Waste and Existing Industrial Routes: a Review and Australian Perspective
Resources 2014, 3, 152-179; doi:10.3390/resources3010152 OPEN ACCESS resources ISSN 2079-9276 www.mdpi.com/journal/resources Review Metal Extraction Processes for Electronic Waste and Existing Industrial Routes: A Review and Australian Perspective Abdul Khaliq, Muhammad Akbar Rhamdhani *, Geoffrey Brooks and Syed Masood Faculty of Science, Engineering and Technology, Swinburne University of Technology, Hawthorn, VIC 3122, Australia; E-Mails: [email protected] (A.K.); [email protected] (G.B.); [email protected] (S.M.) * Author to whom correspondence should be addressed; E-Mail: [email protected]; Tel.: +61-3-9214-8528; Fax: +61-3-9214-8264. Received: 11 December 2013; in revised form: 24 January 2014 / Accepted: 5 February 2014 / Published: 19 February 2014 Abstract: The useful life of electrical and electronic equipment (EEE) has been shortened as a consequence of the advancement in technology and change in consumer patterns. This has resulted in the generation of large quantities of electronic waste (e-waste) that needs to be managed. The handling of e-waste including combustion in incinerators, disposing in landfill or exporting overseas is no longer permitted due to environmental pollution and global legislations. Additionally, the presence of precious metals (PMs) makes e-waste recycling attractive economically. In this paper, current metallurgical processes for the extraction of metals from e-waste, including existing industrial routes, are reviewed. In the first part of this paper, the definition, composition and classifications of e-wastes are described. In the second part, separation of metals from e-waste using mechanical processing, hydrometallurgical and pyrometallurgical routes are critically analyzed. -
Principles of Extractive Metallurgy Lectures Note
PRINCIPLES OF EXTRACTIVE METALLURGY B.TECH, 3RD SEMESTER LECTURES NOTE BY SAGAR NAYAK DR. KALI CHARAN SABAT DEPARTMENT OF METALLURGICAL AND MATERIALS ENGINEERING PARALA MAHARAJA ENGINEERING COLLEGE, BERHAMPUR DISCLAIMER This document does not claim any originality and cannot be used as a substitute for prescribed textbooks. The information presented here is merely a collection by the author for their respective teaching assignments as an additional tool for the teaching-learning process. Various sources as mentioned at the reference of the document as well as freely available material from internet were consulted for preparing this document. The ownership of the information lies with the respective author or institutions. Further, this document is not intended to be used for commercial purpose and the faculty is not accountable for any issues, legal or otherwise, arising out of use of this document. The committee faculty members make no representations or warranties with respect to the accuracy or completeness of the contents of this document and specifically disclaim any implied warranties of merchantability or fitness for a particular purpose. BPUT SYLLABUS PRINCIPLES OF EXTRACTIVE METALLURGY (3-1-0) MODULE I (14 HOURS) Unit processes in Pyro metallurgy: Calcination and roasting, sintering, smelting, converting, reduction, smelting-reduction, Metallothermic and hydrogen reduction; distillation and other physical and chemical refining methods: Fire refining, Zone refining, Liquation and Cupellation. Small problems related to pyro metallurgy. MODULE II (14 HOURS) Unit processes in Hydrometallurgy: Leaching practice: In situ leaching, Dump and heap leaching, Percolation leaching, Agitation leaching, Purification of leach liquor, Kinetics of Leaching; Bio- leaching: Recovery of metals from Leach liquor by Solvent Extraction, Ion exchange , Precipitation and Cementation process. -
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. -
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. -
Evolution of the Isamill™ Into Magnetite Processing
EVOLUTION OF THE ISAMILL™ INTO MAGNETITE PROCESSING Greg Rasmussen, Xstrata Technology Pty Ltd Tommy Do , Ernest Henry Mining Michael Larson, Xstrata Technology Pty Ltd Katie Barns, Xstrata Technology Pty Ltd Xstrata Technology • Mount Isa Mines (MIM), a large Australian mining company, was acquired by Xstrata in 2003 who then merged with Glencore in 2013 • MIM internal technology group was re-named Xstrata Technology (XT) and became an independent technology developer and supplier to the global minerals industry with 250 staff worldwide • The equipment and processes which are marketed by XT are developed in our own operations • XT offers full-package solutions including: • Equipment and processes • Engineering • Commissioning and Training • Dedicated after-market support IsaMill™ Technology Development ™ • Development of IsaMill driven by inability Broken Hill to efficiently treat fine grained orebodies • Late 1980s, Xstrata required 7µm grind for new Pb/Zn orebodies in Australia • Conventional mining technologies tested (1975-1990), but 0 40 micron − Too high power consumption to achieve target size McArthur River − Ball/tower mills ineffective below 20-30μm − Negative influence of steel grinding on flotation 0 40 micron IsaMill™ Technology Development A technology was found... • Horizontal Bead Mills − Used in industries other than mining (pharmaceuticals, paint, food, etc.) − Small, batch scale − Very expensive and exotic media types • Cross-over into mining required: − Much larger scale − Continuous operation − Ability to use cheap, -
Effects of Flux Materials on the Fire Assay of Oxide Gold Ores
Effects of Flux Materials on the Fire Assay of Oxide Gold Ores Haluk Ozden Basaran1, Ahmet Turan1,2*, Onuralp Yucel1 1Istanbul Technical University; Chemical Metallurgical Faculty, Department of Metallurgical and Materials Engineering; Maslak, Istanbul, 34469, Turkey 2Yalova University, Yalova Community College, 77100, Yalova, Turkey Abstract: Fire assay is the most accurate and widely used method for the determination of gold, silver and the PGM contents of ores and other solid materials. The technique has three steps; first step is the smelting of charge mixtures which consist of ground ore samples, acidic and basic fluxes, lead oxide and a carbon source. Isolation of precious metals which are collected in metallic lead phase as a result of the reduction of PbO is the second step and it is called cupellation. Obtained precious metals are analyzed by using wet analysis methods such as AAS (Atomic absorption spectrometry) and ICP (Inductively coupled plasma spectrometry) at the last stage. The aim of this study is the investigation of the effects of the acidic flux materials for the fire assay of oxide gold ores. Acidic fluxes, sodium borax decahydrate (Borax, Na2B4O7·10H2O) and quartz (SiO2), were individually and together added to the charge mixtures which contain oxide gold ore samples, sodium carbonate (Na2CO3) and lead oxide with flour as a carbon source. Acidic flux additions were performed in different amounts. Smelting stage of the experiments was conducted at 1100 °C in fire clay crucibles for a reaction time of 60 minutes by using a chamber furnace. After the cupellation step in the chamber furnace, gold containing beads were obtained. -
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. -
GOLDFAN West Perth, W.A
2nd Floor, 45 Richardson Street, West Perth, Western Australia 6005 P.O. Box 893, GOLDFAN West Perth, W.A. 6005 Tel: (09) 322 2788 LTD Fax: (09) 481 1669 (Inc. in WA.) ly NOTICE OF INTENT THREE MILE HILL PROJECT COOLGARDIE MINERAL FIEL) r'rt T%T) ).T 1 L - VOLUME 1 CONTENTS VOLUME I PAGE 1.0 GENERAL SUMMARY I 2.0 GENERAL INTRODUCTION 3 3.0 GENERAL AND ENVIRONMENTAL STATUS 4 3.1 LOCATION AND ACCESS 4 3.2 TENEMENT OWNERSHIP 4 3.2.1 Mine and Milisite Area 4 3.2.2 Borefield and Pipeline 4 3.3 PROSPECT HISTORY 4 3.3.1 Early Mining 4 3.3.2 Modern Day Activities 5 3.3.3 Goldfan Ltd Activities 5 3.4 ENVIRONMENTAL STATUS 5 3.4.1 Regional Setting 5 3.4.2 Geomorphology 6 3.4.3 Climate 6 3.4.4 Hydrology 7 3.4.4.1 Three Mile Hill 7 3.4.4.2 Roger Spring Borefield Area 7 3.4.5 Flora 8 3.4.6 Fauna 8 3.5 GEOLOGY AND RESOURCES 8 3.5.1 Sub-Regional Geology 8 3.5.2 Local Geology, Structure, Stratigraphy 9 3.5.3 Lithology and Host Unit Characteristics 9 3.5.4 Mineralisation 10 3.5.5 Mineral Resources io 4.0 MINING AND MINESITE REHABILITATION 12 4.1 MINING OBJECTIVE AND SCOPE 12 4.2 GEOTECHNICAL ASPECTS 12 4.3 OPEN PIT OPERATIONS 13 4.3.1 General Open Pit Scheme 13 4.3.2 Drill and Blast Operations 13 4.3.3 Final High Wall Reinforcement 14 4.3.4 Decline 14 4.3.5 Ore and Waste Haulage 14 4.3.6 Dust Suppression is 4.4 OVERBURDEN MANAGEMENT AND REHABILITATION 15 4.4.1 Topsoil Recovery and Storage 15 4.4.2 Overburden Dumping 15 4.4.3 Rehabilitation 15 F CONTENPS VOLUME I PAGE 5.0 ORE PROCESSING, WATER SUPPLY & TAILINGS 16 5.1 ORE PROCESSING 16 5.1.1 Crushing Circuit 16 5.1.2 Grind and Gravity Circuit 16 5.1.3 Flotation and Regrind Circuit 16 5.1.4 CIP General 17 5.1.5 Leach and Adsorption Circuit 17 5.1.6 Carbon Desorption and Re-Activation 17 5.1.7 Gold Room 18 5.2 PROCESS WATER BOREFIELD AND PIPELINE 18 5.2.1 Borefield 18 5.2.2 Pipeline 19 5,3 TAILINGS DISPOSAL DAMS 19 5.3.1 TD1 19 5.3.2.