Evaluation of Scale-Up Model for Flotation with Kristineberg Ore
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
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. -
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. -
Mercury and Mercury Compounds
United States Office of Air Quality EPA-454/R-97-012 Environmental Protection Planning And Standards Agency Research Triangle Park, NC 27711 December 1997 AIR EPA LOCATING AND ESTIMATING AIR EMISSIONS FROM SOURCES OF MERCURY AND MERCURY COMPOUNDS L & E EPA-454/R-97-012 Locating And Estimating Air Emissions From Sources of Mercury and Mercury Compounds Office of Air Quality Planning and Standards Office of Air and Radiation U.S. Environmental Protection Agency Research Triangle Park, NC 27711 December 1997 This report has been reviewed by the Office of Air Quality Planning and Standards, U.S. Environmental Protection Agency, and has been approved for publication. Mention of trade names and commercial products does not constitute endorsement or recommendation for use. EPA-454/R-97-012 TABLE OF CONTENTS Section Page EXECUTIVE SUMMARY ................................................ xi 1.0 PURPOSE OF DOCUMENT .............................................. 1-1 2.0 OVERVIEW OF DOCUMENT CONTENTS ................................. 2-1 3.0 BACKGROUND ........................................................ 3-1 3.1 NATURE OF THE POLLUTANT ..................................... 3-1 3.2 OVERVIEW OF PRODUCTION, USE, AND EMISSIONS ................. 3-1 3.2.1 Production .................................................. 3-1 3.2.2 End-Use .................................................... 3-3 3.2.3 Emissions ................................................... 3-6 4.0 EMISSIONS FROM MERCURY PRODUCTION ............................. 4-1 4.1 PRIMARY MERCURY -
Corrosion and Mercury Release from Dental Amalgam
Corrosion and Mercury Release from Dental Amalgam 1 Jaro Pleva, Ph.D. Abstract been presented, amalgam is still by far the most Corrosion attacks on twenty-two dental extensively used material for dental restorations.2 amalgam restorations after in vivo service have Since the investigations and warnings of the been studied by Scanning Electron Microscopy outstanding German chemist Alfred Stock, 1920- together with the Energy Dispersive X-Ray 19453 4 5 little epidemiological studies of mercury Technique, and by optical microscopy. From the release and its effects have been made. One of the measured depth and type of corrosion attack, possible reasons may be the very interdisciplinary estimates of released mercury amounts are made. character of the problem. For correct answer, The amalgam fillings have been obtained from specialist competence in the following fields is members of a group of 250 individuals, who required: materials science, suspected their health troubles potentially to be corrosion/electrochemistry, toxicology, chronic mercury poisoning from amalgam and medicine/diagnostics, physical biology, analytical were to have all amalgam fillings removed. Three chemistry. typical patient cases are presented. The common type of dental amalgam is an Model calculations of released mercury, based alloy containing typically in weight-%; 50 Hg, 35 on previously published measurements of Ag, 10 Sn, Cu, Zn. corrosion currents with and without abrasion are Reported types of amalgam degradation are also given. crevice corrosion,2 6 7 8 selective corrosion,9 The investigations show, that the long-term galvanic corrosion in contact with dissimilar release of mercury from a few amalgam fillings alloys10 11 and mechanical wear.12 33 Besides will often reach or exceed the recommended selective attack, stress corrosion has been limits for daily intake of mercury. -
NATURE MAY 6, 1944, Vol
562 NATURE MAY 6, 1944, VoL. 153 If the number of young people leaving school and nineteenth century led to the emancipation of the college is much larger in recent years than at the lower classes and of women, and to increasing de beginning of the century, it would seem that this is mands for improved social status and better educa less marked in Switzerland than in certain other tion. Dr. Erb considers that, in Switzerland, the countries. For example, it is pointed out that, in exaggerated importance imputed to academic learn 1930-31, per 100,000 of population, Germany had 63 ing of the more showy or superficial type was par Abiturienten (holders of school-leaving certificates or ticularly marked, and was closely associated with equivalent) whereas Switzerland had only 34. Japan the growing soci»l prejudice for black-coated respect and Rumania in 1934 had more than six times as ability. Those who had not themselves attained many with academic training as in 1913. In the to this status were anxious and determined that their same period those of Holland increased by 146 per children should do so; and this delusion, says Dr. cent, of France 112 per cent, of Great Britain 83 per Erb, will continue until it is more generally realized cent, and of Switzerland 59 per cent. According to that the harder one studies the more certainly will Dr. Erb, the most disturbing aspect of this increase he miss the road to wealth. This may be often true, in quantity is the serious decline in quality : he but scarcely attains the dignity of a general thinks the standard, however measured, is definitely proposition ; and in any event strikes a slightly dis lower. -
Silver City Santa Rita Hurley
SCENIC TRIPS to the GEOLOGIC PAST SILVER CITY SANTA RITA HURLEY NEW MEXICO Scenic Trips to the Geologic Past Series: No. I - Santa Fe, New Mexico No. 2 - Taos-Red River - Eagle Nest, New Mexico, Circle Drive No. 3 - Roswell- Capitan - Ruidoso and Bottomless Lakes Park, New Mexico No. 4 - Southern Zuni Mountains, New Mexico No. 5 - Silver City-Santa Rita-Hurley, New Mexico Additional copies of these guidebooks are available, for 25 cents, from the New Mexico Bureau of Mines and Mineral Resources, Campus Station, Socorro, New Mexico. HO: FOR THE GOLD AND SILVER MINES OF NEW MEXICO Fortune hunters, capitalists, poor men, Sickly folks, all whose hearts are bowed down; And Ye who would live long, be rich, healthy, and Happy; Come to our sunny clime and see For Yourselves. Handbill -- 1883 Santa Rita Open Pit, 1959. Scenic Trips to the Geologic Past No. 5 SILVER CITY - SANTA RITA - HURLEY, NEW MEXICO by JOHN H. SCHILLING 1959 STATE BUREAU OF MINES AND MINERAL RESOURCES a division of NEW MEXICO INSTITUTE OF MINING AND TECHNOLOGY Socorro - New Mexico NEW MEXICO INSTITUTE OF MINING AND TECHNOLOGY E. J. Workman, President STATE BUREAU OF MINES AND MINERAL RESOURCES Alvin J. Thompson, Director THE REGENTS Members Ex Officio The Honorable John Burroughs ...............Governor of New Mexico Tom Wiley ……….…… ...........Superintendent of Public Instruction Appointed Members Holm 0. Bursum, Jr. ........................................................ Socorro Thomas M. Cramer.......................................................... Carlsbad Frank C. DiLuzio ...................................................... Albuquerque John N. Mathews, Jr. ....................................................... Socorro Richard A. Matuszeski .............................................. Albuquerque PREFACE Much of the work undertaken at the New Mexico Bureau of Mines and Mineral Resources is done to help the mineral industries -- the prospector, miner, geologist, oil man. -
Recovery of Phosphate Minerals from Plant Tailings Using Direct Froth Flotation
minerals Article Recovery of Phosphate Minerals from Plant Tailings Using Direct Froth Flotation Ashraf Alsafasfeh and Lana Alagha * Department of Mining & Nuclear Engineering, Missouri University of Science and Technology, Rolla, MO 65409, USA * Correspondence: [email protected]; Tel.: +1-573-341-6287; Fax: +1-573-341-6934 Received: 13 June 2017; Accepted: 9 August 2017; Published: 12 August 2017 Abstract: Wastes produced from the phosphate industry presents many challenges due to the high economic and environmental impacts involved with their disposal. However, the relative scarcity of high-grade phosphate ores has driven researchers to recover and recycle these valuable wastes (secondary sources). The goal of this study was to investigate the possibility of upgrading the P2O5 content in tailings produced from a phosphorous production plant using direct froth flotation. Characterization assays, including X-ray diffraction (XRD), scanning electron microscopy (SEM), X-ray fluorescence (XRF), and mineral liberation analysis (MLA), were first conducted to identify the mineralogical and morphological characteristics of tailings samples and grain properties to better understand the behavior of the flotation feed. Flotation experiments were conducted using Denver D-12 in a 1-L flotation cell in the presence of sodium silicate (dispersant) and sodium oleate (collector). Several parameters, such as the solids content of the flotation pulp, pulp pH and flotation time, were investigated to optimize the recovery and grade of the concentrate products. Results obtained from this study indicated that the P2O5 content in plant tailings could be upgraded from 21.57% to 28.4% at >73% recovery. Keywords: phosphate minerals; froth flotation; mineral liberation analysis; sodium silicate 1. -
Chemistry As a Tool for Historical Research: Identifying Paths of Historical Mercury Pollution in the Hispanic New World
Bull. Hist. Chem., VOLUME 37, Number 2 (2012) 61 CHEMISTRY AS A TOOL FOR HISTORICAL RESEARCH: IDENTIFYING PATHS OF HISTORICAL MERCURY POLLUTION IN THE HISPANIC NEW WORLD Saúl Guerrero, History Department, McGill University, Montreal, QC H3A 2T7, Canada, [email protected] Introduction silver ores to identify and quantify the different mercury loss vectors that resulted from the amalgamation process This article is the first of a series that explore the as practiced in the Hispanic New World. potential of chemistry as an efficient tool for historical research. Basic chemical principles such as the The Scale of Anthropogenic Emissions of stoichiometry of chemical reactions provide the historian Mercury in the New World with a powerful tool to judge the reliability of archival records and interpret better the historiography of events From 1521 to 1810 Spain produced nearly 69% of that relate directly to processes of production based the total world output of silver from its mines in New on chemical reactions. Chemical mass balances have Spain (present day Mexico) and in the Vice-Royalty of determined both revenue streams and environmental Peru (present day Peru and Bolivia). During this period consequences in the past. there was no other non-Hispanic major silver produc- A very appropriate case study to apply this ap- tion in the New World (2). The global economic impact proach is the first industrial scale chemical process to of these exports of silver to Europe and China during have caused a global economic impact. The application the Early Modern Era has received wide coverage in of mercury amalgamation to extract silver from the ores the historiography of this period (3). -
Metal Losses in Pyrometallurgical Operations - a Review
Advances in Colloid and Interface Science 255 (2018) 47–63 Contents lists available at ScienceDirect Advances in Colloid and Interface Science journal homepage: www.elsevier.com/locate/cis Historical perspective Metal losses in pyrometallurgical operations - A review Inge Bellemans a,⁎, Evelien De Wilde a,b, Nele Moelans c, Kim Verbeken a a Ghent University, Department of Materials, Textiles and Chemical Engineering, Technologiepark 903, B-9052, Zwijnaarde, Ghent, Belgium b Umicore R&D, Kasteelstraat 7, B-2250 Olen, Belgium c KU Leuven, Department of Materials Engineering, Kasteelpark Arenberg 44, bus 2450, B-3001, Heverlee, Leuven, Belgium article info abstract Article history: Nowadays, a higher demand on a lot of metals exists, but the quantity and purity of the ores decreases. The Received 24 October 2016 amount of scrap, on the other hand, increases and thus, recycling becomes more important. Besides recycling, Received in revised 4 August 2017 it is also necessary to improve and optimize existing processes in extractive and recycling metallurgy. One of Accepted 7 August 2017 the main difficulties of the overall-plant recovery are metal losses in slags, in both primary and secondary Available online 10 August 2017 metal production. In general, an increased understanding of the fundamental mechanisms governing these losses could help further improve production efficiencies. This review aims to summarize and evaluate the current sci- Keywords: fi Pyrometallurgy enti c knowledge concerning metal losses and pinpoints the knowledge gaps. Metal losses First, the industrial importance and impact of metal losses in slags will be illustrated by several examples from Slags both ferrous and non-ferrous industries. -
Extractive Metallurgy of Copper This Page Intentionally Left Blank Extractive Metallurgy of Copper
Extractive Metallurgy of Copper This page intentionally left blank Extractive Metallurgy of Copper Mark E. Schlesinger Matthew J. King Kathryn C. Sole William G. Davenport AMSTERDAM l BOSTON l HEIDELBERG l LONDON NEW YORK l OXFORD l PARIS l SAN DIEGO SAN FRANCISCO l SINGAPORE l SYDNEY l TOKYO Elsevier The Boulevard, Langford Lane, Kidlington, Oxford OX5 1GB, UK Radarweg 29, PO Box 211, 1000 AE Amsterdam, The Netherlands First edition 1976 Second edition 1980 Third edition 1994 Fourth edition 2002 Fifth Edition 2011 Copyright Ó 2011 Elsevier Ltd. All rights reserved. No part of this publication may be reproduced, stored in a retrieval system or transmitted in any form or by any means electronic, mechanical, photocopying, recording or otherwise without the prior written permission of the publisher Permissions may be sought directly from Elsevier’s Science & Technology Rights Department in Oxford, UK: phone (+44) (0) 1865 843830; fax (+44) (0) 1865 853333; email: permissions@ elsevier.com. Alternatively you can submit your request online by visiting the Elsevier web site at http://elsevier.com/locate/permissions, and selecting Obtaining permission to use Elsevier material Notice No responsibility is assumed by the publisher for any injury and/or damage to persons or property as a matter of products liability, negligence or otherwise, or from any use or operation of any methods, products, instructions or ideas contained in the material herein British Library Cataloguing in Publication Data A catalogue record for this book is available from the British Library Library of Congress Cataloging-in-Publication Data A catalog record for this book is available from the Library of Congress ISBN: 978-0-08-096789-9 For information on all Elsevier publications visit our web site at elsevierdirect.com Printed and bound in Great Britain 11 12 13 14 10 9 8 7 6 5 Photo credits: Secondary cover photograph shows anode casting furnace at Palabora Mining Company, South Africa. -
Slag Reprocessing: Magma Copper Company's San Manuel Facility
I' SLAG REPROCESSING: MAGMA COPPER COMPANY'S SAN MANUEL FACILITY DRAFT August 1993 Prepared by: U.S. Environmental Protection Agency Office of Solid Waste Special Waste Branch 401 M Street, S.W. Washington, D.C. 20460 Pyrite Flotation: Supenbr Mine DISCLAIMER AND ACKNOWLEDGEMENTS This document was prepared by the U.S. Environmental Protection Agency (EPA) with assistance from Science Applications International Corporation (SAIC) in partial fulfillment of EPA Contract No. 68- W0-0025,Work Assignment 209. Magma Copper Company submitted comments on an earlier draft of this report. EPA had amended the report where appropriate to reflect those comments. The mention of company or product names is not to be considered an endorsement by the U.S. Government or the U.S. Environmental Protection Agency (EPA). Draft I August 1993 Slag Reprocessing: San Manuel DISCLAIMER AND ACKNOWLEDGEMENTS This document was prepared by the U.S. Environmental Protection Agency (EPA) with assistance from Science Applications International Corporation (SAIC) in partial fulfillment of EPA Contract No. 68- W0-0025, Work Assignment 209. Magma Copper Company submitted comments on an earlier draft of this report. EPA has responded to those comments and changed the text where appropriate. The mention of company or product names is not to be considered an endorsement by the U.S.Government or the U.S. Environmental Protection Agency (EPA). Draft I August 1993 Slag Reprocessing: Son Munuti TABLE OF CONTENTS 1 .0 Introduction .................................................. 1 2 .0 Pollution PreventionNaste Minimization with Slag Reprocessing ................. 1 2.1 Slag Reprocessing .......................................... 4 2.2 costs .................................................. 9 2.3 Benefits ............................................... 10 2.4 Limitations ............................................