Extraction of a Low Grade Zinc Ore Using Gravity and Froth Flotation Methods
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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. -
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. -
Corrosion of Refractories in Lead Smelting Reactors
CORROSION OF REFRACTORIES IN LEAD SMELTING REACTORS By LINGXUAN WEI B.Sc, Wuhan University of Science & Technology, China 1986 M.Sc, University of Science & Technology Beijing, China 1997 A THESIS SUBMITTED IN PARTIAL FULFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF MASTER OF APPLIED SCIENCE in THE FACULTY OF GRADUATE STUDIES DEPARTMENT OF METALS AND MATERIALS ENGINEERING We accept this thesis as conforming to the required standard THE UNIVERSITY OF BRITISH .UMB1A DECEMBER 2000 ©Lingxuan Wei, ZO0O UBC Special Collections - Thesis Authorisation Form http://www.library.ubc.ca/spcoll/thesauth.html In presenting this thesis in partial fulfilment of the requirements for an advanced degree at the University of British Columbia, I agree that the Library shall make it freely available for reference and study. I further agree that permission for extensive copying of this thesis for scholarly purposes may be granted by the head of my department or by his or her representatives. It is understood that copying or publication of this thesis for financial gain shall not be allowed without my written permission. v 3 The University of British Columbia Vancouver, Canada Date lof 1 3/19/01 2:36 PM ABSTRACT Corrosion of refractories by slag is a complex phenomenon which, depending on the particular system, involves many processes, such as chemical wear (corrosion) and physical or mechanical wear (erosion), which may act synergistically. No single model can explain all cases of corrosion nor can it explain all corrosion mechanisms of a particular refractory in different environments, but the knowledge of the microstructure combined with the chemistry of the systems are necessary to understand the corrosion mechanism of a refractory material. -
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 -
Hg on Periodic Table
Hg On Periodic Table Cameron never westernize any stairs carnalize externally, is Thomas unlovely and muddled enough? gloomingPeridermal backstage, Aubert regales: uncontrolled he globe-trots and coequal. his costrels contentiously and impassively. Martie buck her How is left over the california, on hg could melt quickly by electronic strain gauge sensors have very fine flakes of Mercury than the chemical element with symbol Hg and atomic no 0 Mercury was a transition metal A transition metal is feast of the elements found between Groups. Mercury news a naturally occurring element found an air, corps and soil. This website under most abundant elements into minamata bay, or out that immediately contained in a product can cause damage, as a highly poisonous. Starship like the plane? Mercury compound thimerosal is used to our wonder leave you. It has been shown significantly more about a periodic table is liquid form alloys, switches like from countries are kidneys damage a periodic table live in terms are there is. Mercury chemical symbol Hg is an liquid metallic element that historically was used in many medicines but has now restricted due for legitimate concerns about. Cinnabar was rubbed together with policy in paper clay dish. Glad you liked this one, Jordan! Some forms of tame are particularly potent poisons. Why take some elements on the Periodic Table represented by letters that have only clear connection to their names? Mif signatures in antiseptics, facts about being replaced by where did you think about chemical sedimentation may also. Doesn't the periodic table define it Not got is overcome an element. -
A Study on Reduction of Copper Smelting Slag by Carbon for Recycling Into Metal Values and Cement Raw Material
Preprints (www.preprints.org) | NOT PEER-REVIEWED | Posted: 17 January 2020 doi:10.20944/preprints202001.0177.v1 Peer-reviewed version available at Sustainability 2020, 12, 1421; doi:10.3390/su12041421 Article A Study on Reduction of Copper Smelting Slag by Carbon for Recycling into Metal Values and Cement Raw Material Urtnasan Erdenebold and Jei-Pil Wang* Department of Metallurgical Engineering, School of Engineering, Pukyong National University, Busan 608- 739, Korea * Correspondence: [email protected]; Tel,: +82-51-629-6341 Abstract: Copper smelting slag is a solution of molten oxides created during the copper smelting and refining process, and about 1.5 million tons of copper slag is generated annually in Korea. Oxides in copper smelting slag include ferrous (FeO), ferric oxide (Fe2O3), silica (SiO2 from flux), alumina (AI2O3), calcia (CaO) and magnesia (MgO). Main oxides in copper slag, which iron oxide and silica, exist in the form of fayalite (2FeO·SiO2). Since the copper smelting slag contains high content of iron, and copper and zinc. Common applications of copper smelting slag are the value added products such as abrasive tools, roofing granules, road-base construction, railroad ballast, fine aggregate in concrete, etc., as well as the some studies have attempted to recover metal values from copper slag. This research was intended to recovery Fe-Cu alloy, raw material of zinc and produce reformed slag like a blast furnace slag for blast furnace slag cement from copper slag. As a results, it was confirmed that reduction smelting by carbon at temperatures above 1400°С is possible to recover pig iron containing copper from copper smelting slag, and CaO additives in the reduction smelting assist to reduce iron oxide in the fayalite and change the chemical and mineralogical composition of the slag. -
Nickel Laterite Smelting Processes and Some Examples of Recent Possible Modifications to the Conventional Route
metals Review Nickel Laterite Smelting Processes and Some Examples of Recent Possible Modifications to the Conventional Route Ender Keskinkilic Department of Metallurgical and Materials Engineering, Atilim University, 06830 Ankara, Turkey; [email protected]; Tel.: +90-533-302-9510 Received: 16 July 2019; Accepted: 1 September 2019; Published: 3 September 2019 Abstract: The treatment of laterites has been a research hotspot in extractive metallurgy over the past decades. Industrially, the pyrometallurgical treatment of laterites is mostly accomplished with a well-established method, namely, the rotary kiln–electric arc furnace (RKEF) process, which includes three main operations—calcination, prereduction, and smelting—followed by further refining for the removal of impurities from the raw ferro-nickel. As indicated in many studies of the RKEF process, the major downside of this method is its high energy consumption. Efforts have been made to lower this consumption. Furthermore, several new processes have been proposed. Among these, low-grade ferro-nickel production is regarded as the most widely and industrially used process after traditional RKEF operation. Although not widespread, other alternative processes of industrial scale have been generated since the start of the millennium. Recently, certain innovative processes have been tested either in the laboratory or at pilot-scale. In this paper, a literature review related to the smelting of laterites is made, and an emphasis on new processes and some examples of new developments in the RKEF process are presented. Keywords: laterite; smelting; RKEF process; low-grade ferro-nickel 1. Introduction According to a review published by Diaz et al., oxide-type nickel ores accounted for 64% of land-based nickel ores, but more than 60% of nickel production was based on the matte smelting of sulfide ores in 1988 [1]. -
Integral Management of Arsenical Sludge, Treatment and Recovery of By-Products of Acid Waters from Smelter Plants
MILAF: INTEGRAL MANAGEMENT OF ARSENICAL SLUDGE, TREATMENT AND RECOVERY OF BY-PRODUCTS OF ACID WATERS FROM SMELTER PLANTS ULRIKE BROSCHEK, CECILIA VIDAL, LUIS BRAVO and GILDA ZUÑIGA Environmental Program, Fundación Chile Parque Antonio Rabat Sur 6165, Vitacura, Santiago, Chile; E-mail: [email protected] ABSTRACT Currently, the copper mining industry produces high amounts of sulfuric acid with low purity and high concentrations of arsenic and other metals. Most of these acid waters are neutralized in the copper smelting plants by using lime to raise the pH from 1 to 12 generating high amounts of arsenical sludge that has to be disposed on safety landfills because of its high toxicity. This has forced the mining companies to pay large sums of money for the disposal of significant volume of solid waste. Each copper smelting plant produces in average during this specific process more than 18,000 tons of arsenical sludge yearly, spending on the treatment and disposal stage more than US 2.8 million dollars per year where a 70 % of this cost corresponds to the disposal costs of the solid waste [1,2,3]. Different technologies for treating these acid wastewaters have been developed and patented worldwide. However, these treatments have focused on obtaining the separation of the arsenic from the effluent through physical-chemical precipitation using different basic components and cations that reacts with the contaminants and then precipitates in the solution [4]. These technologies have not been able to solve the problem because they are expensive, complex, not always efficient and still generates high amounts of arsenical sludge requiring high disposal costs; hence, mining companies have not implement them. -
Toxicological Profile for Zinc
TOXICOLOGICAL PROFILE FOR ZINC U.S. DEPARTMENT OF HEALTH AND HUMAN SERVICES Public Health Service Agency for Toxic Substances and Disease Registry August 2005 ZINC ii DISCLAIMER The use of company or product name(s) is for identification only and does not imply endorsement by the Agency for Toxic Substances and Disease Registry. ZINC iii UPDATE STATEMENT A Toxicological Profile for Zinc, Draft for Public Comment was released in September 2003. This edition supersedes any previously released draft or final profile. Toxicological profiles are revised and republished as necessary. For information regarding the update status of previously released profiles, contact ATSDR at: Agency for Toxic Substances and Disease Registry Division of Toxicology/Toxicology Information Branch 1600 Clifton Road NE Mailstop F-32 Atlanta, Georgia 30333 ZINC vi *Legislative Background The toxicological profiles are developed in response to the Superfund Amendments and Reauthorization Act (SARA) of 1986 (Public law 99-499) which amended the Comprehensive Environmental Response, Compensation, and Liability Act of 1980 (CERCLA or Superfund). This public law directed ATSDR to prepare toxicological profiles for hazardous substances most commonly found at facilities on the CERCLA National Priorities List and that pose the most significant potential threat to human health, as determined by ATSDR and the EPA. The availability of the revised priority list of 275 hazardous substances was announced in the Federal Register on November 17, 1997 (62 FR 61332). For prior versions of the list of substances, see Federal Register notices dated April 29, 1996 (61 FR 18744); April 17, 1987 (52 FR 12866); October 20, 1988 (53 FR 41280); October 26, 1989 (54 FR 43619); October 17, 1990 (55 FR 42067); October 17, 1991 (56 FR 52166); October 28, 1992 (57 FR 48801); and February 28, 1994 (59 FR 9486). -
National Emissions Standards for Hazardous Air Pollutants from Secondary Lead Smelting; Final Rules
Vol. 77 Thursday, No. 3 January 5, 2012 Part II Environmental Protection Agency 40 CFR Part 63 National Emissions Standards for Hazardous Air Pollutants From Secondary Lead Smelting; Final Rules VerDate Mar<15>2010 16:35 Jan 04, 2012 Jkt 226001 PO 00000 Frm 00001 Fmt 4717 Sfmt 4717 E:\FR\FM\05JAR2.SGM 05JAR2 mstockstill on DSK4VPTVN1PROD with RULES2 556 Federal Register / Vol. 77, No. 3 / Thursday, January 5, 2012 / Rules and Regulations ENVIRONMENTAL PROTECTION related to emissions during periods of the telephone number for the Air and AGENCY startup, shutdown, and malfunction. Radiation Docket and Information DATES: This final action is effective on Center is (202) 566–1742. 40 CFR Part 63 January 5, 2012. The incorporation by FOR FURTHER INFORMATION CONTACT: For [EPA–HQ–OAR–2011–0344; FRL–9610–9] reference of certain publications listed questions about this final action, contact in the rule is approved by the Director RIN 2060–AQ68 Mr. Nathan Topham, Office of Air of the Federal Register as of January 5, Quality Planning and Standards, Sector 2012. National Emissions Standards for Policies and Programs Division, U.S. ADDRESSES: Hazardous Air Pollutants From The EPA has established a Environmental Protection Agency, Secondary Lead Smelting docket for this action under Docket ID Research Triangle Park, NC 27711; No. EPA–HQ–OAR–2011–0344. All telephone number: (919) 541–0483; fax AGENCY: Environmental Protection documents in the docket are listed on number: (919) 541–3207; and email Agency (EPA). the http://www.regulations.gov Web address: [email protected]. For ACTION: Final rule. site. -
The Metallurgy of Antimony
Chemie der Erde 72 (2012) S4, 3–8 Contents lists available at SciVerse ScienceDirect Chemie der Erde journal homepage: www.elsevier.de/chemer The metallurgy of antimony Corby G. Anderson ∗ Kroll Institute for Extractive Metallurgy, George S. Ansell Department of Metallurgical and Materials Engineering, Colorado School of Mines, Golden, CO 80401, United States article info abstract Article history: Globally, the primary production of antimony is now isolated to a few countries and is dominated by Received 4 October 2011 China. As such it is currently deemed a critical and strategic material for modern society. The metallurgical Accepted 10 April 2012 principles utilized in antimony production are wide ranging. This paper will outline the mineral pro- cessing, pyrometallurgical, hydrometallurgical and electrometallurgical concepts used in the industrial Keywords: primary production of antimony. As well an overview of the occurrence, reserves, end uses, production, Antimony and quality will be provided. Stibnite © 2012 Elsevier GmbH. All rights reserved. Tetrahedrite Pyrometallurgy Hydrometallurgy Electrometallurgy Mineral processing Extractive metallurgy Production 1. Background bullets and armory. The start of mass production of automobiles gave a further boost to antimony, as it is a major constituent of Antimony is a silvery, white, brittle, crystalline solid that lead-acid batteries. The major use for antimony is now as a trioxide exhibits poor conductivity of electricity and heat. It has an atomic for flame-retardants. number of 51, an atomic weight of 122 and a density of 6.697 kg/m3 ◦ ◦ at 26 C. Antimony metal, also known as ‘regulus’, melts at 630 C 2. Occurrence and mineralogy and boils at 1380 ◦C. -
The Advanced Mining Technologies and Its Impact on the Australian Nonferrous Minerals Industry
Paper Title: PROVEN TECHNOLOGIES FROM XSTRATA AND THEIR APPLICATIONS FOR COPPER SMELTING AND REFINING IN CHINA Paper Presented at: Hainan Conference, China Authors: Mingwei Gao, Philip Arthur and Nigel Aslin, Xstrata Technology Date of Publication: 2004 For further information please contact us at [email protected] www.isasmelt.com PROVEN TECHNOLOGIES FROM XSTRATA AND THEIR APPLICATIONS FOR COPPER SMELTING AND REFINING IN CHINA Mingwei Gao, Philip Arthur and Nigel Aslin Xstrata Technology, Australia 1.0 INTRODUCTION The world’s non-ferrous industry has achieved significant improvements in efficiency in the last 20 years owing to the advanced technologies such as ISASMELT™ and ISA PROCESS that have been invented and developed at Mount Isa Mines in Australia,. A number of large nonferrous mining operations in the world are still in business today largely because of the commercial benefits that resulted from applying these technologies. ISASMELT and ISA PROCESS technologies are marketed worldwide by Xstrata Technology, a division of the Xstrata plc group of companies, which was formed upon Xstrata’s takeover of MIM Holdings Limited in mid 2003. Xstrata PLC is a diversified international mining company and has operations in Australia, the United Kingdom, Germany, Spain, South Africa, Chile, and Argentina with around 20,000 employees worldwide. Major products are copper, lead, zinc, silver, coal, ferrochrome, and ferrovanadium. In addition to these commodities, an integral part of the group is their independent process technology business – Xstrata Technology. Xstrata group companies have a long record of developing process technologies for in-house use and for sale to external clients. 2.0 ISASMELT™ TECHNOLOGY ISASMELT is a modern bath-smelting process for the production of non-ferrous metals.