Extractive Metallurgy 3 Processing Operations and Routes
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A Review of Flotation Separation of Mg Carbonates (Dolomite and Magnesite)
minerals Review A Review of Flotation Separation of Mg Carbonates (Dolomite and Magnesite) Darius G. Wonyen 1,†, Varney Kromah 1,†, Borbor Gibson 1,† ID , Solomon Nah 1,† and Saeed Chehreh Chelgani 1,2,* ID 1 Department of Geology and Mining Engineering, Faculty of Engineering, University of Liberia, P.O. Box 9020 Monrovia, Liberia; [email protected] (D.G.W.); [email protected] (Y.K.); [email protected] (B.G.); [email protected] (S.N.) 2 Department of Electrical Engineering and Computer Science, University of Michigan, Ann Arbor, MI 48109, USA * Correspondence: [email protected]; Tel.: +1-41-6830-9356 † These authors contributed equally to the study. Received: 24 July 2018; Accepted: 13 August 2018; Published: 15 August 2018 Abstract: It is well documented that flotation has high economic viability for the beneficiation of valuable minerals when their main ore bodies contain magnesium (Mg) carbonates such as dolomite and magnesite. Flotation separation of Mg carbonates from their associated valuable minerals (AVMs) presents several challenges, and Mg carbonates have high levels of adverse effects on separation efficiency. These complexities can be attributed to various reasons: Mg carbonates are naturally hydrophilic, soluble, and exhibit similar surface characteristics as their AVMs. This study presents a compilation of various parameters, including zeta potential, pH, particle size, reagents (collectors, depressant, and modifiers), and bio-flotation, which were examined in several investigations into separating Mg carbonates from their AVMs by froth flotation. Keywords: dolomite; magnesite; flotation; bio-flotation 1. Introduction Magnesium (Mg) carbonates (salt-type minerals) are typical gangue phases associated with several valuable minerals, and have complicated processing [1,2]. -
Effects of Varied Process Parameters on Froth Flotation Efficiency: a Case Study of Itakpe Iron Ore
Nigerian Journal of Technology (NIJOTECH) Vol. 39, No. 3, July 2020, pp. 807 – 815 Copyright© Faculty of Engineering, University of Nigeria, Nsukka, Print ISSN: 0331-8443, Electronic ISSN: 2467-8821 www.nijotech.com http://dx.doi.org/10.4314/njt.v39i3.21 EFFECTS OF VARIED PROCESS PARAMETERS ON FROTH FLOTATION EFFICIENCY: A CASE STUDY OF ITAKPE IRON ORE S. Akande1, E. O. Ajaka2, O. O. Alabi3 and T. A. Olatunji4,* 1, 2, DEPARTMENT OF MINING ENGINEERING, FEDERAL UNIV. OF TECHNOLOGY, AKURE, ONDO STATE, NIGERIA 3, 4, DEPT. OF MET. & MATERIALS ENGINEERING, FEDERAL UNIV. OF TECHNOLOGY, AKURE, ONDO STATE, NIGERIA Email addresses: 1 [email protected], 2 [email protected], 3 [email protected], 4 [email protected] ABSTRACT The dire need for Itakpe iron ore concentrates of appreciable iron content meets for smelting operation necessitated this study. Core samples of the iron ore sourced from Itakpe, Kogi State, Nigeria were prepared for petrological analysis followed by chemical and particle size analyses. Froth flotation was done using different collectors at varying particle sizes and pH values. Characterization studies carried out revealed that Itakpe iron ore is a lean ore assaying 36.18% Fe2O3 and contains predominantly quartz, sillimanite, and haematite. Its liberation size lies favourably at 75 µm. Processing the ore by froth flotation yielded appreciable enrichment. Optimal recovery (~92%) was achieved using potassium amyl xanthate (PAX) at pH 11 for fine feed sizes (<125 µm) yielding iron concentrate assaying 67.66% Fe2O3. Thus, processing at this set-of- conditions is recommended for the industrial production of more enriched Itakpe iron ore concentrates. -
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. -
Table of Contents
Table of Contents Preface ........................................... xi Chapter 1. Physical Extraction Operations .................... 1 1.1. Solid-solid and solid-fluid separation operations .............. 1 1.1.1. Flotation ................................... 1 1.1.2. Settling under gravity ........................... 3 1.1.3. Centrifugation ................................ 3 1.1.4. Filtration ................................... 4 1.2. Separation operations of the components of a fluid phase ........ 5 1.2.1. Condensation ................................ 5 1.2.2. Vacuum distillation ............................. 5 1.2.3. Liquation ................................... 6 1.2.4. Distillation .................................. 8 1.2.5. Extractive distillation ........................... 11 1.3. Bibliography ................................... 12 Chapter 2. Hydrometallurgical Operations .................... 15 2.1. Leaching and precipitation operations .................... 15 2.1.1. Leaching and precipitation reactors ................... 15 2.1.2. Continuous stirred tank reactor (CSTR) ................ 18 2.1.3. Models of leaching and precipitation operations ........... 20 2.1.4. Particle-size distribution (PSD) functions ............... 21 2.2. Reactor models based on particle residence time distribution functions ........................................ 24 2.2.1. Performance equations for a single CSTR ............... 24 2.2.2. Performance equations for multistage CSTRs ............. 28 2.3. Reactor models based on the population balance -
Occurrence and Extraction of Metals MODULE - 6 Chemistry of Elements
Occurrence and Extraction of Metals MODULE - 6 Chemistry of Elements 16 Notes OCCURRENCE AND EXTRACTION OF METALS Metals and their alloys are extensively used in our day-to-day life. They are used for making machines, railways, motor vehicles, bridges, buildings, agricultural tools, aircrafts, ships etc. Therefore, production of a variety of metals in large quantities is necessary for the economic growth of a country. Only a few metals such as gold, silver, mercury etc. occur in free state in nature. Most of the other metals, however, occur in the earth's crust in the combined form, i.e., as compounds with different anions such as oxides, sulphides, halides etc. In view of this, the study of recovery of metals from their ores is very important. In this lesson, you shall learn about some of the processes of extraction of metals from their ores, called metallurgical processes. OBJECTIVES After reading this lesson, you will be able to : z differentiate between minerals and ores; z recall the occurrence of metals in native form and in combined form as oxides, sulphides, carbonates and chlorides; z list the names and formulae of some common ores of Na, Al, Sn, Pb ,Ti, Fe, Cu, Ag and Zn; z list the occurrence of minerals of different metals in India; z list different steps involved in the extraction of metals; * An alloy is a material consisting of two or more metals, or a metal and a non-metal. For example, brass is an alloy of copper and zinc; steel is an alloy of iron and carbon. -
Mineral Engineering & Fuel Technology
MINERAL ENGINEERING & FUEL TECHNOLOGY (MME-203) 4th Semester B. Tech Dept. of Metallurgical and Materials Engineering V.S.S.university of Technology , Burla Sambalpur , odisha Person Name Designation Department involved And Email .id Course Gautam Assistant MME coordinator Behera professor [email protected] Course Co- Dinesh Assistant MME coordinator ku professor mishra , [email protected] Course Co- Avala Assistant MME coordinator Lava professor kumar [email protected] Goals of the subject 1-To impart knowledge about Mineral Processing [fundamental knowledge] 2-To teach you to “think” rather than “cook” 3-To encourage you to consider a career path in Mineral Processing Content Introduction to mineral processing(Engineering) Crushing and grinding Size separation methods Concentration methods Agglomeration techniques Fuel technology MODULE -I Introduction to mineral and mineral Engineering Mineral- a substance from which we get metal non metals or any valuables. Mineral Engineering ( branch of mme which deals with study of minerals and its processing )where the minerals is being processed to get a concentrate from which metals are extracted . Flow chat to show the relationship of mineral engineering with mining and extractive metallurgy engineering Subject covers Minerals definition MINERAL : Natural occur inorganic aggregate of metals and non metals . Or Inorganic compound having a definite chemical composition and crystal structure (atomic structure). Or minerals are the forms in which metals are found in the earth crust and as sea bed deposit depend on their reactivity with their environment, particular with oxygen , sulphur, and co2. Anything of economical value which is extracted from the earth. Characteristic of mineral 1-Minerals are homogeneous in physical and chemical composition. -
Evaluation of Scale-Up Model for Flotation with Kristineberg Ore
Evaluation of Scale-up Model for Flotation with Kristineberg Ore Adam Isaksson Chemical Engineering, master's level 2018 Luleå University of Technology Department of Civil, Environmental and Natural Resources Engineering Evaluation of Scale-up Model for Flotation with Kristineberg Ore Adam Isaksson 2018 For degree of MASTER OF SCIENCE Luleå University of Technology Department of Civil, Environmental and Natural Resources Engineering Division of Minerals and Metallurgical Engineering Printed by Luleå University of Technology, Graphic Production 2018 Luleå 2018 www.ltu.se Preface As you may have figured out by now, this thesis is all about mineral processing and the extraction of metals. It was written as part of my studies at Luleå University of Technology, for a master’s degree in Chemical Engineering with specialisation Mineral and Metal Winning. There are many people I would like to thank for helping me out during all these years. First of all, my thanks go to supervisors Bertil Pålsson and Lisa Malm for the guidance in this project. Iris Wunderlich had a paramount role during sampling and has kindly delivered me data to this report, which would not have been finished without her support. I would also like to thank Boliden Mineral AB as a company. Partly for giving me the chance to write this thesis in the first place, but also for supporting us students during our years at LTU. Speaking of which, thanks to Olle Bertilsson for reading the report and giving me feedback. The people at the TMP laboratory deserves another mention. I am also very grateful for the financial support and generous scholarships from Jernkontoret these five years. -
Study on New Desilication Technology of High Silica Bauxite
2016 2nd International Conference on Sustainable Energy and Environmental Engineering (SEEE 2016) ISBN: 978-1-60595-408-0 Study on New Desilication Technology of High Silica Bauxite Hai-yun XIE 1, Chao DING 1, Peng-fei ZHANG 1,2 , Lu-zheng CHEN 1, and Xiong-TONG 1 1Faculty of Land Resource Engineering, Kunming University of Science and Technology, Kunming 650093, China 2State Key Laboratory of Complex Nonferrous Metal Resource Clean Utilization, Kunming 650093, China Keywords: High silicon bauxite, Desilication, Gravity separation, Froth flotation. Abstract: There are abundant diasporic bauxite resource in China. The gravity separation and flotation process are utilized for treating this kind of ore. When the ore grinding fineness is -200 mesh 80%, the qualified bauxite concentrate can be obtained, and it contains Al 2O3 71.62%, SiO 2 8.94%, and its Al 2O3 recovery rate is 75.43%, A/S is 8.02.Compared with single flotation process, it can be reduced for the dosage flotation reagent and the cost of mineral processing. Introduction China's bauxite resources are rich, the amount of resources of 1.914 billion, ranking the fifth in the world, but more than 80% are medium and low grade ore, Aluminum silicon ratio (A/S) between 4 to 7 of the bauxite accounted for 59.5%. These minerals can not meet the basic conditions for the production of alumina by Bayer process. (A/S>8) [1]. The vast majority of China's bauxite belong to high-alumina, high-silicon, fine-grained embedded diaspore-type bauxite, so the bauxite is difficult to concentrate. -
Flotation of Copper Sulphide from Copper Smelter Slag Using Multiple Collectors and Their Mixtures
International Journal of Mineral Processing 143 (2015) 43–49 Contents lists available at ScienceDirect International Journal of Mineral Processing journal homepage: www.elsevier.com/locate/ijminpro Flotation of copper sulphide from copper smelter slag using multiple collectors and their mixtures Subrata Roy a,⁎, Amlan Datta b, Sandeep Rehani c a Aditya Birla Science and Technology Company Ltd., Taloja, Maharashtra, India b Formerly with Aditya Birla Science and Technology Company Ltd., Taloja, Maharashtra, India. c Birla Copper, Dahej, Gujarat, India article info abstract Article history: Present work focuses on the differences in the performances obtained in the froth flotation of copper smelter Received 14 August 2014 slag with multiple collector viz. sodium iso-propyl xanthate (SIPX), sodium di-ethyl dithiophosphate (DTP) Received in revised form 11 February 2015 and alkyl hydroxamate at various dosages. Flotation tests were carried out using single collectors as well as var- Accepted 20 August 2015 ious mixtures of the two collectors at different but constant total molar concentrations. Flotation performances Available online 28 August 2015 were increased effectively by the combination of collectors. The findings show that a higher copper recovery (84.82%) was obtained when using a 40:160 g/t mixture of sodium iso-propyl xanthate (SIPX) with di-ethyl Keywords: Flotation dithiophosphate compared to 78.11% with the best single collector. Similar recovery improvement (83.07%) Copper slag was also observed by using a 160:40 g/t mixture of sodium iso-propyl xanthate (SIPX) with alkyl hydroxamate. Sodium isobutyl xanthate The results indicate that in both cases DTP and alkyl hydroxamate played important role as co-collector with SIPX Hydroxamate for the recovery of coarse interlocked copper bearing particles and has an important effect on the behaviour of Dithiophosphate the froth phase. -
Extractive Metallurgy & the Smelting of Bronze
Extractive Metallurgy & the Smelting of Bronze INTRODUCTION: Seven metals were in use before the invention of writing: gold, silver, copper, iron, mercury, tin & lead. Many of these are so scarce they couldn’t be used practically (like gold). Others are rarely found in their elemental form, instead found as minerals of carbonates, oxides, or sulfides. It is the elemental form of metals that we are familiar with when we speak of their shiny, malleable and conducting properties. As minerals or ores, metals exist in combination with other elements, often as brittle, non-conducting substances (image rocks, salts & crystals). To produce a metal in its elemental form from an ore requires a chemical transformation, a process of extractive metallurgy called smelting. The fundamental problem of smelting involves the chemical reduction of metallic compounds to elemental metals, with different compounds requiring different treatment conditions. Oxide or carbonate ores are heated with charcoal, which combines with the oxygen in the ore, to release carbon dioxide and produce the elemental metal. 2 Cu3(CO3)2(OH)2 + 3 C → 6 Cu + 7 CO2 + 2 H2O (1) SnO2 + C → Sn + CO2 (2) Copper was the earliest metal to come into common usage because its ores are fairly common, like that of malachite (Cu2CO3(OH)2), and because it can be smelted at moderate temperatures (see equation 2 above). It is a soft metal, however, which makes it of marginal value for tools and weapons. Tin forms an alloy with copper, called bronze, which is harder than either metal alone. By 3,000 BC bronze had become the dominant metal, so much so that its use defines the Bronze Age. -
Liquation Cracking in the Heat-Affected Zone of IN738 Superalloy Weld
metals Article Liquation Cracking in the Heat-Affected Zone of IN738 Superalloy Weld Kai-Cheng Chen 1, Tai-Cheng Chen 2,3 ID , Ren-Kae Shiue 3 ID and Leu-Wen Tsay 1,* ID 1 Institute of Materials Engineering, National Taiwan Ocean University, Keelung 20224, Taiwan; [email protected] 2 Nuclear Fuels and Materials Division, Institute of Nuclear Energy Research, Taoyuan 32546, Taiwan; [email protected] 3 Department of Materials Science and Engineering, National Taiwan University, Taipei 10617, Taiwan; [email protected] * Correspondence: [email protected]; Tel.: +886-2-24622192 (ext. 6405) Received: 7 May 2018; Accepted: 25 May 2018; Published: 27 May 2018 Abstract: The main scope of this study investigated the occurrence of liquation cracking in the heat-affected zone (HAZ) of IN738 superalloy weld, IN738 is widely used in gas turbine blades in land-based power plants. Microstructural examinations showed considerable amounts of γ’ uniformly precipitated in the γ matrix. Electron probe microanalysis (EPMA) maps showed the γ-γ’ colonies were rich in Al and Ti, but lean in other alloy elements. Moreover, the metal carbides (MC), fine borides (M3B2 and M5B3), η-Ni3Ti, σ (Cr-Co) and lamellar Ni7Zr2 intermetallic compounds could be found at the interdendritic boundaries. The fracture morphologies and the corresponding EPMA maps confirmed that the liquation cracking in the HAZ of the IN738 superalloy weld resulted from the presence of complex microconstituents at the interdendritic boundaries. Keywords: IN738 superalloy; welding; HAZ cracking; microconstituent 1. Introduction The superior tensile strength, creep and oxidation resistance at elevated temperature make Ni-base superalloys used extensively in industrial gas turbines [1].