Chromium 2016
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Impurity Control in Copper Metallurgical Plants with Special Focus on Arsenic Oct 2018 17
Impurity Control in Copper Metallurgical Plants with Special Focus on Arsenic Oct 2018 17, George P. Demopoulos* Department of Mining and Materials Engineering, McGill University *[email protected] https://www.mcgill.ca/materials/people/faculty/george-p- Seminar Impurity JOGMEC demopoulos P1resented at the Int’l Seminar on Impurities in Copper 1 Raw Materials, Tokyo, Japan, October 2018 Towards Sustainable Metallurgical Processes • Impurity control- a must in making the Copper metallurgical industry sustainable! • Development of sustainable processes means Oct Oct 2018 17, innovation • Meet economic and environmental goals simultaneously • Innovation needs research collaborations Seminar Impurity JOGMEC • This series of seminars is an excellent initiative… 2 Sustainability Aspects of Impurity Control Technologies-1 • Consider deportment of impurities throughout the whole process flowsheet for best intervention strategy Oct Oct 2018 17, • Work towards clean impurity-specific separation approaches to minimize valuable metal loss, reagent usage, or intro of new pollutants: SX (residual organics?), IX, Molecular Recognition Technology (MRT), magnetic resins, selective precipitation, Sorption/Adsorption etc. Seminar Impurity JOGMEC • Equally important to get enrichment-concentration to 3 facilitate economic recovery and/or disposal Sustainability Aspects of Impurity Control Technologies-2 • Consider recovery if there is demand of the impurity as by-product; Oct 2018 17, Example: Se, Te, Sb, Bi in Cu industry: Can be sold as feedstock -
Ore Processing in Fluidized Bed Technologies Overview • Fundamentals in Fluidized Bed Technology
Ore processing in fluidized bed technologies Overview • Fundamentals in fluidized bed technology. • Outotec‘s experience in fluidized bed technologies. • CFB/FB applications for iron containing ores. • CFB aplications for alumina calcination. • Technology and project development. © Outotec – All rights reserved Fluidized bed systems - fundamentals Bubbling Circulating Transport or flash fluidized bed fluidized bed reactor (FR) (FB) (CFB) • In a fluidized bed particles are held suspended by the upward. • Increasing gas velocities will create different flow regimes. • The highest slip velocity is reached in CFB, leading to high mass & heat transfer rates. • Outotec has applied CFB, FB, AFB and FR for treatment of different fine ores. Annular fluidized bed (AFB) © Outotec – All rights reserved Circulating fluidized bed advantages • High mass & heat transfer CFB Uniform temperature, low energy consumption. • Direct processing of fines Fuel NG Minimum fines losses and accretions. • High productivity GasAir Minimum plant downtime & low GasAir specific investment costs. • No heavy rotating equipment Easy and flexible control, low operation & maintenance costs. • Easy and exact control of temperature and retention time. • Direct combustion of natural gas in the CFB furnace. Circulating fluidized bed © Outotec – All rights reserved Outotec‘s experience in fluidized bed technologies CFB applications Rio Tinto Alcan Gove 3 CFB calciners. HBI Circored plant Trinidad. Capacity 0.5 million t/a 6 © Outotec – All rights reserved CFB applications Outotec‘s fluidized bed applications 7 © Outotec – All rights reserved CFB applications – iron ore processing • Outotec has built CFB plants for preheating, roasting and hydrogen based reduction of iron ores. • In the case of iron ore preheating & calcination, the target is to remove LOI and to preheat the ore for down stream processes (e.g. -
Investor Presentation
Investor presentation September 2020 Forward looking statements It should be noted that certain statements herein which are not historical facts, including, without limitation, those regarding expectations for general economic development and the market situation, expectations for customer industry profitability and investment willingness, expectations for company growth, development and profitability and the realization of synergy benefits and cost savings, and statements preceded by ”expects”, ”estimates”, ”forecasts” or similar expressions, are forward looking statements. These statements are based on current decisions and plans and currently known factors. They involve risks and uncertainties which may cause the actual results to materially differ from the results currently expected by the company. Such factors include, but are not limited to: 1) general economic conditions, including fluctuations in exchange rates and interest levels which influence the operating environment and profitability of customers and thereby the orders received by the company and their margins 2) the competitive situation, especially significant technological solutions developed by competitors 3) the company’s own operating conditions, such as the success of production, product development and project management and their continuous development and improvement 4) the success of pending and future acquisitions and restructuring. August 5, 2020 2 Metso Outotec in brief Metso Outotec is a frontrunner in sustainable technologies, end-to- end solutions and services for the aggregates, minerals processing, 4.2 50+ metals refining and recycling billion euro countries with industries globally. sales* presence By improving our customers’ energy and water efficiency, increasing their productivity and reducing environmental risks with our process 15,000+ 150 years of and product expertise, we are the employees, 80+ expertise in mining partner for positive change. -
Metso Outotec's Magazine for Mining & Aggregates Customers >> Issue 1, 2021
resultsMetso Outotec’s magazine for mining & aggregates customers >> Issue 1, 2021 Partner for positive change 1 results - mining + aggregates In this issue Metso Outotec in brief............................................................................................................... 4 Our businesses............................................................................................................................. 5 Our offerings - Aggregates / Mining / Metals refining.............................................. 6 Our strengths................................................................................................................................ 9 Our services................................................................................................................................... 10 Our customers : Our references............................................................................................. 12 Products / solutions.................................................................................................................... 26 Dear Customers, News updates............................................................................................................................... 44 I hope that you and your families are keeping safe and business is also improving. In these uncertain times, we need sharper focus on delivery & service capabilities to ensure business continuity for our customers. Therefore, we have ensured that our operations continue to deliver despite current challenges, -
Hydrometallurgical Precious Metals Process
Hydrometallurgical Precious Metals Process The Metso Outotec Hydrometallurgical Precious Metals Benefits Process is the result of decades of experience and • High direct recovery and high end-product continuous development in precious metals processing quality with low inventories technology. It offers high direct recoveries with low • Short processing time • Highly automated process enables stable inventories. The cost-effective, modular approach end-product quality and smooth operation comprises leaching, filtration, and precipitation steps, • Modular approach is both flexible and and can be adapted for a variety of applications, cost-efficient including processing of anode slimes or other residues • Recovered impurities can be sold as by-products instead of disposed of containing precious metals. • Low environmental impact with no flue dust or slag generation The Metso Outotec Hydrometallurgical Precious Metals Process Production of precious metals from anode TROF or Kaldo Furnace. The modular approach makes it A flexible, safe, and cost-effective process slimes or secondary raw materials possible to integrate the Metso Outotec process with your In the Metso Outotec Hydrometallurgical Precious Metals Originally developed for the treatment of copper existing process equipment. Process, slime is first leached in three sequential sulfuric acid electrorefining anode slime, the Metso Outotec leaching steps. The soluble copper and excess chlorides Hydrometallurgical Precious Metals Process can also be used The process ensures effective separation of impurities with are removed in copper recovery. The remaining copper and to process other raw materials containing precious metals, high recovery. Impurities can be converted into saleable most of the selenium, silver, and impurities are dissolved in including some secondary raw materials or lead anode products such as selenium, copper telluride, and lead sulfate pressure leaching. -
Pellet-Size Estimation of a Ferrochrome Pelletizer Circuit Using Computer Vision Techniques
Pellet-size estimation of a ferrochrome pelletizer circuit using Computer Vision techniques by Johannes Kasselman Rabie Thesis presented in partial fulfilment of the requirements for the Degree of MASTER OF ENGINEERING (EXTRACTIVE METALLURGICAL ENGINEERING) in the Faculty of Engineering at Stellenbosch University Supervisor Dr Lidia Auret March 2018 Stellenbosch University https://scholar.sun.ac.za DECLARATION By submitting this thesis electronically, I declare that the entirety of the work contained therein is my own, original work, that I am the sole author thereof (save to the extent explicitly otherwise stated), that reproduction and publication thereof by Stellenbosch University will not infringe any third party rights and that I have not previously in its entirety or in part submitted it for obtaining any qualification. Date: March 2018 Copyright © 2018 Stellenbosch University All rights reserved i Stellenbosch University https://scholar.sun.ac.za ABSTRACT Pellet-size estimation of a ferrochrome pelletizer circuit using Computer Vision techniques Rabie J.K., Auret L. Department of Process Engineering, University of Stellenbosch, Private Bag X1, Matieland 7602, South Africa. Thesis: M.Eng (Extractive Metallurgical Engineering) March 2018 Agglomerate pellet size plays an integral part in the safe and stable operation of a submerged arc furnace (SAF), and the efficiencies and yields achieved within the ferrochrome refining processes. For effective process control that ensures constant and optimal pellet size production, the continuous monitoring of pellet size distribution produced by the agglomeration circuit becomes imperative. Traditional size estimation methods tend to be labour intensive and time consuming, and cannot provide feedback in real time. The need therefore exists for automated, real time, and non-intrusive industrial size estimation systems. -
Nitrogen Compounds at Mines and Quarries I 226
VTT TECHNOLOGY NOL CH OG E Y T • • R E E C S N E E A Nitrogen compounds at mines and quarries I 226 R C 226 C Sources, behaviour and removal from mine and quarry S H • S H N waters – Literature study I G O I H S L I I V G • H S T Nitrogen compounds at mines and quarries Nitrogen compounds at mines and quarries ISBN 978-951-38-8320-1 (URL: http://www.vttresearch.com/impact/publications) ISSN-L 2242-1211 ISSN 2242-122X (Online) Sources, behaviour and removal from mine and quarry waters – Literature study VTT TECHNOLOGY 226 Nitrogen compounds at mines and quarries Sources, behaviour and removal from mine and quarry waters – Literature study Johannes Jermakka, Laura Wendling, Elina Sohlberg, Hanna Heinonen, Elina Merta, Jutta Laine-Ylijoki, Tommi Kaartinen & Ulla-Maija Mroueh VTT Technical Research Centre of Finland Ltd ISBN 978-951-38-8320-1 (URL: http://www.vttresearch.com/impact/publications) VTT Technology 226 ISSN-L 2242-1211 ISSN 2242-122X (Online) Copyright © VTT 2015 JULKAISIJA – UTGIVARE – PUBLISHER Teknologian tutkimuskeskus VTT Oy PL 1000 (Tekniikantie 4 A, Espoo) 02044 VTT Puh. 020 722 111, faksi 020 722 7001 Teknologiska forskningscentralen VTT Ab PB 1000 (Teknikvägen 4 A, Esbo) FI-02044 VTT Tfn +358 20 722 111, telefax +358 20 722 7001 VTT Technical Research Centre of Finland Ltd P.O. Box 1000 (Tekniikantie 4 A, Espoo) FI-02044 VTT, Finland Tel. +358 20 722 111, fax +358 20 722 7001 Cover image: Johannes Jermakka, VTT Abstract Nitrogen compounds at mines and quarries Sources, behaviour and removal from mine and quarry waters – Literature study Authors: Johannes Jermakka, Laura Wendling, Elina Sohlberg, Hanna Heinonen, Elina Merta, Jutta Laine-Ylijoki, Tommi Kaartinen and Ulla-Maija Mroueh Keywords: ammonia, nitrate, mine wastewater, treatment technology, nitrogen recovery, nitrogen sources, explosives Mining wastewaters can contain nitrogen from incomplete detonation of nitrogen rich explosives and from nitrogen containing chemicals used in enrichment pro- cesses. -
Secure Fuels from Domestic Resources ______Profiles of Companies Engaged in Domestic Oil Shale and Tar Sands Resource and Technology Development
5th Edition Secure Fuels from Domestic Resources ______________________________________________________________________________ Profiles of Companies Engaged in Domestic Oil Shale and Tar Sands Resource and Technology Development Prepared by INTEK, Inc. For the U.S. Department of Energy • Office of Petroleum Reserves Naval Petroleum and Oil Shale Reserves Fifth Edition: September 2011 Note to Readers Regarding the Revised Edition (September 2011) This report was originally prepared for the U.S. Department of Energy in June 2007. The report and its contents have since been revised and updated to reflect changes and progress that have occurred in the domestic oil shale and tar sands industries since the first release and to include profiles of additional companies engaged in oil shale and tar sands resource and technology development. Each of the companies profiled in the original report has been extended the opportunity to update its profile to reflect progress, current activities and future plans. Acknowledgements This report was prepared by INTEK, Inc. for the U.S. Department of Energy, Office of Petroleum Reserves, Naval Petroleum and Oil Shale Reserves (DOE/NPOSR) as a part of the AOC Petroleum Support Services, LLC (AOC- PSS) Contract Number DE-FE0000175 (Task 30). Mr. Khosrow Biglarbigi of INTEK, Inc. served as the Project Manager. AOC-PSS and INTEK, Inc. wish to acknowledge the efforts of representatives of the companies that provided information, drafted revised or reviewed company profiles, or addressed technical issues associated with their companies, technologies, and project efforts. Special recognition is also due to those who directly performed the work on this report. Mr. Peter M. Crawford, Director at INTEK, Inc., served as the principal author of the report. -
Ferrochrome Waste Management - Addressing Current Gaps
Ferrochrome waste management - addressing current gaps SP du Preez orcid.org/ 0000-0001-5214-3693 Thesis submitted for the degree Doctor of Philosophy in Chemistry at the North-West University Promoter: Prof JP Beukes Co-promoter: Prof PG van Zyl Graduation May 2018 21220212 SOLEM DECLARATION I, Stephanus Petrus du Preez, declare herewith that the thesis entitled: Ferrochrome waste management - addressing current gaps, which I herewith submit to the North-West University (NWU) as completion of the requirement set for the Doctor in Philosophiae in Chemistry degree, is my own work, unless specifically indicated otherwise, has been text edited as required, and has not been submitted to any other tertiary institution other than the NWU. Signature of the candidate: University number: 21220212 Signed at Potchefstroom on 20 November 2017 SOLEMN DECLARATION i ACKNOWLEDGMENTS “A sluggard’s appetite is never filled, but the desires of the diligent are fully satisfied” Proverbs 12:4 God Almighty, thank you for the strength and perseverance to undertake each task that came across my path. Without your grace and love, I am nothing. I would sincerely like to thank and convey my most genuine gratitude towards the following people for their support, assistance and guidance during the past three years. They played a vital role in the completion of my thesis and helped me to grow both academically and as a person. My supervisor Prof Paul Beukes, and co-supervisor Dr Pieter van Zyl. I am endlessly thankful for your excellent guidance, patience, and the critical roles that both of you played in my personal and academical growth. -
International Strategic Minerals Inventory Summary Report-Chromium
U.S. GEOLOGICAL SURVEY CIRCULAR 93o-B International Strategic Minerals Inventory Summary Report-Chromium Prepared as a cooperative effort among earth science and mineral-resource agencies of Australia, Canada, the Federal Republic of Germany, the Republic of South Africa, and the United States of America Major geologic age units Million years Age before present Holocene QUATERNARY I- 0.1 Pleistocene u I- 2 Pliocene 5 N r- 5 Miocene 0z w r- 24 Oligocene TERTIARY u r- 38 Eocene I- 55 Paleocene 63 Late Cretaceous Cretaceous I- 96 u Early Cretaceous 5 N I- 138 0 Jurassic en w ~ f- 205 Triassic 240 Permian I- 290 Pennsylvanian Carboniferous r---330 Mississippian u - 5 I- 360 Devonian N 0 w I- ...J 410 <( Silurian Q.. r- 435 Ordovician r- 500 Cambrian -570 u Late Proterozoic 6 N 0 f-- 900 a: Middle Proterozoic w z 1- r- 1600 <( 0 a: a: Early Proterozoic 0.. CD 2500 ~ <( u z w <( a: w Q.. Iu a: <( International Strategic Minerals Inventory Summary Report-Chromium By John H. DeYoung, Jr., Michael P. lee, and Bruce R. lipin U. S. G E 0 L 0 G I C A L S U R V E Y C I R C U L A R 9 3 0-B Prepared as a cooperative effort among earth science and mineral-resource agencies of Australia, Canada, the Federal Republic of Germany, the Republic of South Africa, and the United States of America 1984 Department of the Interior WILLIAM P. CLARK, Secretary U.S. Geological Survey Dallas L. Peck, Director Library of Congress Catalog-card No. -
South Africanferroalloys Handbook 2013
HANDBOOK H1/2013 SOUTH AFRICANFERROALLOYS HANDBOOK 2013 DIRECTORATE: MINERAL ECONOMICS HANDBOOK H1/2013 SOUTH AFRICAN FERROALLOYS HANDBOOK 2013 DIRECTORATE: MINERAL ECONOMICS Compiled by: Ms K Ratshomo Email: ([email protected]) Picture on front cover Source: The BoshoekSmelter, North West Province www.meraferesources.co.za Issued by and obtainable from The Director: Mineral Economics, Trevenna Campus, 70 Meintjies Street, Arcadia, Pretoria 0001, Private Bag X59, Arcadia 0001 Telephone (012)444-3531, Telefax (012) 444-3134 Website: http://www.dmr.gov.za DEPARTMENT OF MINERAL RESOURCES Director-General Dr. T Ramontja MINERAL POLICY AND PROMOTION BRANCH Deputy Director-General Mr. M Mabuza MINERAL PROMOTION CHIEF DIRECTORATE Chief Director Ms. S Mohale DIRECTORATE MINERAL ECONOMICS Director: Mineral Economics Mr. TR Masetlana Deputy Director: Precious Metals and Minerals Ms. L Malebo and Ferrous Minerals THIS, THE FIRST EDITION, PUBLISHED IN 2013 ISBN: 978-0-621-42052-4 COPYRIGHT RESERVED DISCLAIMER Whereas the greatest care has been taken in the compilation of the contents of this publication, the Department of Mineral Resources does not hold itself responsible for any errors or omissions. TABLE OF CONTENTS Contents Page 1. INTRODUCTION .................................................................................................................1 2. SOUTH AFRICA’S FERROUS ALLOYS OVERVIEW ..........................................................1 3. FERROCHROME ................................................................................................................3 -
Ferrochrome (Fecr)
Ferrochrome (FeCr) Price range in 2020 2,78 €/kg Cr – 3,77 €/kg Cr for Low Carbon Ferrochrome 1,49 $/Ib Cr – 1,90 $/Ib Cr Formula FeCr CAS no. 11114-46-8 Description Ferrochrome, or Ferrochromium (FeCr) is a type of ferroalloy, that is, an alloy between chromium and iron, generally containing 50% to 70% chromium. It is produced in an energy intensive process in electric furnaces from chrome ore, iron ore and coal. FeCr is used in the production of stainless steel, special steel and castings. Ferrochrome is divided up in three main products which are Low Carbon FeCr, Medium Carbon FeCr and High Carbon FeCr. Physical Properties General The melting point and density of ferrochrome depends on its chrome and carbon content Abrasion good resistance to abrasion Corrosion good resistance to corrosion Gravity high specific gravity Magnetism high magnetism High carbon Medium carbon Low carbon DensityFeCr70 6,7-7,1 g/cm³ 0,242-0,257 Ib/in³ 7,1-7,3 g/cm³ 0,257-0,264 Ib/in³ 7,3-7,35 g/cm³ 0,264-0,266 Ib/in³ Melting 1350-1650 °C 2462-3002 °F 1360-1600 °C 2480-2912 °F 1580-1690 °C 2876-3074 °F pointFeCr70 Source: Volkert, G. & Frank, K.-D.: Die Metallurgie der Ferrolegierungen CO2 Footprint Scope 2 * Scope 3 ** Upstream emission factors - 5,987 tCo2 / tFeCr Source: worldsteel association Actually requested materials based on metalshub transactions Material Size Composition, as percentages by mass Designation Packaging Pallet name [mm] Cr C Si P S Low carbon Min. 10 65 - LCFeCr 65 1 mt big bags One way pallet grade Max.