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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. -
Unusual Silicate Mineralization in Fumarolic Sublimates of the Tolbachik Volcano, Kamchatka, Russia – Part 2: Tectosilicates
Eur. J. Mineral., 32, 121–136, 2020 https://doi.org/10.5194/ejm-32-121-2020 © Author(s) 2020. This work is distributed under the Creative Commons Attribution 4.0 License. Unusual silicate mineralization in fumarolic sublimates of the Tolbachik volcano, Kamchatka, Russia – Part 2: Tectosilicates Nadezhda V. Shchipalkina1, Igor V. Pekov1, Natalia N. Koshlyakova1, Sergey N. Britvin2,3, Natalia V. Zubkova1, Dmitry A. Varlamov4, and Eugeny G. Sidorov5 1Faculty of Geology, Moscow State University, Vorobievy Gory, 119991 Moscow, Russia 2Department of Crystallography, St Petersburg State University, University Embankment 7/9, 199034 St. Petersburg, Russia 3Kola Science Center of Russian Academy of Sciences, Fersman Str. 14, 184200 Apatity, Russia 4Institute of Experimental Mineralogy, Russian Academy of Sciences, Akademika Osypyana ul., 4, 142432 Chernogolovka, Russia 5Institute of Volcanology and Seismology, Far Eastern Branch of Russian Academy of Sciences, Piip Boulevard 9, 683006 Petropavlovsk-Kamchatsky, Russia Correspondence: Nadezhda V. Shchipalkina ([email protected]) Received: 19 June 2019 – Accepted: 1 November 2019 – Published: 29 January 2020 Abstract. This second of two companion articles devoted to silicate mineralization in fumaroles of the Tol- bachik volcano (Kamchatka, Russia) reports data on chemistry, crystal chemistry and occurrence of tectosil- icates: sanidine, anorthoclase, ferrisanidine, albite, anorthite, barium feldspar, leucite, nepheline, kalsilite, so- dalite and hauyne. Chemical and genetic features of fumarolic silicates are also summarized and discussed. These minerals are typically enriched with “ore” elements (As, Cu, Zn, Sn, Mo, W). Significant admixture of 5C As (up to 36 wt % As2O5 in sanidine) substituting Si is the most characteristic. Hauyne contains up to 4.2 wt % MoO3 and up to 1.7 wt % WO3. -
Iron Recovery from Bauxite Tailings Red Mud by Thermal Reduction with Blast Furnace Sludge
applied sciences Article Iron Recovery from Bauxite Tailings Red Mud by Thermal Reduction with Blast Furnace Sludge Davide Mombelli * , Silvia Barella , Andrea Gruttadauria and Carlo Mapelli Dipartimento di Meccanica, Politecnico di Milano, via La Masa 1, Milano 20156, Italy; [email protected] (S.B.); [email protected] (A.G.); [email protected] (C.M.) * Correspondence: [email protected]; Tel.: +39-02-2399-8660 Received: 26 September 2019; Accepted: 9 November 2019; Published: 15 November 2019 Abstract: More than 100 million tons of red mud were produced annually in the world over the short time range from 2011 to 2018. Red mud represents one of the metallurgical by-products more difficult to dispose of due to the high alkalinity (pH 10–13) and storage techniques issues. Up to now, economically viable commercial processes for the recovery and the reuse of these waste were not available. Due to the high content of iron oxide (30–60% wt.) red mud ranks as a potential raw material for the production of iron through a direct route. In this work, a novel process at the laboratory scale to produce iron sponge ( 1300 C) or cast iron (> 1300 C) using blast furnace ≤ ◦ ◦ sludge as a reducing agent is presented. Red mud-reducing agent mixes were reduced in a muffle furnace at 1200, 1300, and 1500 ◦C for 15 min. Pure graphite and blast furnace sludges were used as reducing agents with different equivalent carbon concentrations. The results confirmed the blast furnace sludge as a suitable reducing agent to recover the iron fraction contained in the red mud. -
PRODUCTION and REFINING of METALS (Electrolytic C25); PRETREATMENT of RAW MATERIALS
C22B PRODUCTION AND REFINING OF METALS (electrolytic C25); PRETREATMENT OF RAW MATERIALS Definition statement This subclass/group covers: Metallurgical or chemical processes for producing or recovering metals from metal compounds, ores, waste or scrap metal and for refining metal. Included in this subclass are processes drawn to: the production of metal by smelting, roasting or furnace method; the extraction of metal compounds from ore and concentrates by wet processes; electrochemical treatment of ores and metallurgical products for obtaining metals or alloys; apparatus thereof; preliminary treatment of ores, concentrates and scrap; general process for refining or remelting metals; apparatus for electroslag or arc remelting of metals; obtaining specific metals; consolidating metalliferous charges or treating agents that are subsequently used in other processes of this subclass, by agglomerating, compacting, indurating or sintering. Relationship between large subject matter areas This subclass covers the treatment, e.g. decarburization, of metallferrous material for purposes of refining. C21C, C21D and C22F provide decarburization of metal for modifying the physical structure of ferrous and nonferrous metals or alloys, respectively. C22B also possesses groups for obtaining metals including obtaining metals by chemical processes, and obtaining metal compounds by metallurgical processes. Thus, for example, group C22B 11/00 covers the production of silver by reduction of ammoniacal silver oxide in solution, and group C22B 25/00 covers the -
Iron-Rich Bauxite and Bayer Red Muds Yingyi Zhang, Yuanhong Qi and Jiaxin Li
Chapter Aluminum Mineral Processing and Metallurgy: Iron-Rich Bauxite and Bayer Red Muds Yingyi Zhang, Yuanhong Qi and Jiaxin Li Abstract Bauxite is the main source for alumina production. With the rapid development of iron and steel industry and aluminum industry, high-quality iron ore and bauxite resources become increasingly tense. However, a lot of iron-rich bauxite and Bayer red mud resources have not been timely and effectively recycled, resulting in serious problems of environmental pollution and wastage of resources. The com- prehensive utilization of iron-rich bauxite and red mud is still a worldwide problem. The industrial stockpiling is not a fundamental way to solve the problems of iron- rich bauxite and red mud. As to the recovery of valuable metals from iron-rich bauxite and red mud, there are a lot of technical and cost problems, which are serious impediments to industrial development. Applying red mud as construction materials like cement, soil ameliorant applications face the problem of Na, Cr, As leaching into the environment. However, the high-temperature reduction, smelting and alkaline leaching process is a feasible method to recover iron and alumina from iron-rich bauxite and red mud. This chapter intends to provide the reader an overview on comprehensive utilization technology of the low-grade iron-rich bauxite and Bayer red mud sources. Keywords: bauxite, iron-rich bauxite, Bayer red mud, Bayer process, magnetic separation, reduction and smelting process 1. Introduction With 8.30%, aluminum is the third element in the earth’s crust after the oxygen and the silicon, and for that reason, aluminum minerals are abundant with more than 250 kinds. -
Lapis Lazuli
LAPIS LAZULI Among the world’s many gemstones, lapis lazuli, or “lapis” as it is familiarly known, has a distinction. Many scholars and archaeologists believe that it was the first gemstone ever mined in quantity. The oldest known lapis deposits, located in Afghanistan, have been systematically mined since about 4000 B.C. Few gemstones display color as rich as the deep, royal blue of fine lapis. Adding to its visual appeal, lapis often exhibits glittering, golden flecks of pyrite. When cut and polished into cabochons and set in gold, lapis gemstones have a distinctive beauty all their own. Understanding lapis lazuli, which is a rock, requires a basic understanding of lazurite, which is a mineral. Lazurite is the primary component of lapis lazuli and is also the cause of its blue color. Lazurite, or basic sodium calcium aluminum sulfate chlorosilicate (Na,Ca)8Si6Al6O24[(SO4),S,Cl,(OH)]2, is a tectosilicate or framework silicate that is made up of 13.5 percent sodium, 7.8 percent calcium, 15.8 percent aluminum, 16.3 percent silicon, 6.0 percent sulfur, 38.1 percent oxygen, and small percentages of chlorine and hydrogen. The color of pure lazurite is a deep azure. It crystallizes in the isometric (cubic) system, usually as dodecahedral and occasionally as cubic crystals, but most often occurs in massive form. Lazurite is usually opaque, has a dull-to-greasy luster, poor cleavage in six directions, a pale-blue streak, a Mohs hardness of 5.0-5.5, and a specific gravity of 2.4-2.5. Lazurite forms from high-grade, contact metamorphism of silica-poor marine limestone that contains available sulfur and chlorine. -
Extraction of Aluminium from Coal Fly Ash Using a Two-Step Acid Leach Process
EXTRACTION OF ALUMINIUM FROM COAL FLY ASH USING A TWO-STEP ACID LEACH PROCESS Alan Shemi A dissertation submitted to the faculty of Engineering and the Built Environment, University of Witwatersrand, Johannesburg, in fulfillment of the requirements for the degree of Master of Science in Engineering Extraction of Aluminium from CFA Alan Shemi DECLARATION I declare that this dissertation is my own unaided work. It is being submitted to the degree of Master of Science in Engineering to the University of the Witwatersrand, Johannesburg. It has not been submitted before for any other degree or examination in any other University. ---------------------------------- Alan Shemi 14th Day of May 2013 Page ii Extraction of Aluminium from CFA Alan Shemi ABSTRACT Hydrometallurgical extraction technologies provide a process route for resource recovery of valuable metals from both primary as well as secondary resources. In this study, the possibility of treating coal fly ash (CFA), a residue formed as a result of coal combustion in coal-fired power plants, was investigated. Eskom CFA contains significant amounts of alumina typically, 26-31%, in two dissimilar phases, namely amorphous and crystalline mullite, which may be processed separately. Due to its high silica content, however, CFA cannot be treated through the Bayer process route. Therefore, a leach-sinter-leach process was formulated that employed a two-step acid leach technique to extract alumina from CFA using sulphuric acid. In the preliminary test work, the effect of parameters on CFA leaching characteristics was investigated. From the experimental results, appropriate factor levels were found to be 6M acid concentration, 6 hours leaching time, 75°C temperature and 1:4 solid to liquid ratio. -
Recovery of Desilication Product in Alumina Industry
Recovery of Desilication Product in Alumina Industry Hasitha Indrajith de Silva B.Sc. Engineering (Honours) A thesis submitted for the degree of Doctor of Philosophy at The University of Queensland in 2013 School of Chemical Engineering Abstract Bayer process is used for the production of alumina from bauxite which contains siliceous minerals known as reactive silica. Reactive silica is also digested during the Bayer process, forming desilication product (DSP) which traps significant amount of sodium from the caustic soda used. DSP containing red mud is discarded to the bauxite residue storage areas causing alarming economic and environmental concerns to the alumina industry. Separation of DSP from red mud is a critical step to subsequent sodium recovery. Therefore, methods of separating DSP from red mud originated in a Western Australian alumina refinery were investigated in the present study. Red mud classified into five size classes was characterised using particle size measurement, material density, X-ray diffraction, X-ray photon spectroscopy, electron microscopy fitted with energy dispersive spectroscopy. Size separation alone resulted in an increase of DSP from ~7% to 12-14% in finer size classes of red mud. Since red mud contains more than 50% iron oxides, dissolution of these oxides would invariably result in an increase of DSP, therefore, several dissolution mechanisms of these oxides were investigated. Sodium Citrate-Bicarbonate-Dithionite (CBD) method resulted in an increase of DSP content from ~12 to 22%, while a comparative study was also carried out using deferroxiamine B (DFO-B) as the complexing agent. The use of ultrasonically assisted-CBD resulted in a significant improvement of iron dissolution from red mud. -
Phase Relations of the Hydroxyl Felspathoids in the System Naalsi0 -Naoh-H 0 4 2
THE HYDROXYL FELSPATHOIDS PHASE RELATIONS OF THE HYDROXYL FELSPATHOIDS IN THE SYSTE14 NaAlSiO4-NaOH-H 0 2 By PETER ASCROFT MACKENZIE ANDERSON, B.Se., M.Se. A Thesis Submitted to the Faculty of Graduate Studies in Partial Fulfilment of the Requirements for the Degree Doetor of Philosophy McMaster University May 1968 DOCTOR OF PHILOSOPHY (1968) McMASTER UNIVERSITY (Geology) Hamilton, Ontario TITLE: Phase Relations of the Hydroxyl Felspathoids in the System NaAlSi0 -NaOH-H 0 4 2 AUTHOR: Peter A.M. Anderson, B.Sc. (London University) M.Sc. (McMaster University) SUPERVISOR: Dr. B.J. Burley NUMBER OF PAGES: ix, 78 SCOPE AND CONTENTS: A stUdy was made of the phase relationships in the system NaAlSi0 -NaOH-H 0, at 15,000 p.s.i. and at 450°C, 520°C, 4 2 600°C and 700°C. The following phases were found and characterised: hydroxyl varieties of nosean, sodalite and cancrinite, with formulae approximating to 3NaA1Si04.NaOH.xH20, l6:.xbl.5, sodic nepheline and phase X, apparently a previously unreported phase, with composition approaching Na Al Si 0 • Approximate phase diagrams were deduced 4 2 2 9 for the four temperatures. i1 ACKNOWLEOOEMENTS The writer is very deeply indebted to Dr. B.J. Burley, without whose continued guidance and support, this investigation would have been quite impossible. Drs. C. Calvo and H.P. Schwarcz have also been generous with time and advice, throughout the project. The assist- ance of others, too numerous to mention individually, has been readily given and gratefully accepted; these include most of the members of the Department of Geology. -
CHANGING TECHNOLOGY Ln a CHANGING WORLD the CASE of EXTRACTIVE METALLURGY 1
CHANGING TECHNOLOGY lN A CHANGING WORLD THE CASE OF EXTRACTIVE METALLURGY 1 Fathi Habashi 2 ABSTRACT Smelting of ores for metal extraction is an ancient art in our civilization. New technology is being introduced, but forces of resistance are sometimes so strong to permit a radical change. While the iron and steel, zinc, aluminum, and gold industries are responding to change, the copper and nickel industries seem to be more conservative. Key words: iron, steel, copper, pressure hydrometallurgy, gold, alurninum, zinc, nickel, sulfur dioxide, elemental sulfur, sulfuric acid, pyrite, arsenopyrite. ' XVII Encontro Nacional de Tratamento de Minérios e Metalurgia Extrativa - I Simpósio sobre Química de Colóides- Aguas de Sao Pedro- SP, Brazil , August 23-26. 1998. :· Department of Mining and Metallurgy, Lavai University, Qut:bec City, Canada 49 INTRODUCTION Extractive metallurgy today is usually divided in two sectors: ferrous and nonferrous because of the large scale operations in the ferrous [1). Steel production in one year exceeds that of ali other metais combined in ten years. As a result, metallurgists in the nonferrous sector usually do not participate in the activities of iron and steel makers and vice versa. This is a pity because for sure one can leam from the other. ln fact, the copper industry adopted many technologies used first in iron and steel production. For example, when Bessemer invented the conventer in 1856 it was adopted in the copper industry ten years !ater, and when high grade massive copper sulfide ores were exhausted and metallurgists were obliged to treat low-grade ores, the puddling furnace was adapted in form of a reverberatory furnace to treat the flotation concentrates. -
A Chemical, Thermogravimetric and X-Ray Study of Cancrinite
A CHEMICAL, THERMOGRAVIMETRIC AND X-RAY STUDY OF CANCRINITE by 1 SHU-MEEI CHEN, B • Sc. A The sis Submitted to the School of Graduate Studies in Partial Fulfilment of the Requirements for the Degree Master of Science McMaster University September, 1970 STUDIES ON CANCRINITE MASTER OF SCIENCE (Ge ology) McMASTER UNIVERSITY Hamilton, Ontario. TITLE: A Chemical, Thermogravimetric and X-Ray Study of C ancrinite. AUTHOR: Shu-Meei Chen, B.Sc. (National Taiwan University) SUPER VISOR: Professor B. J. Burley NUMBER OF PAGES: 65, viii. SCOPE AND CONTENTS: Four specimens of natural cancrinite from Ontario we r e studied. Single crystal photog raphs were taken and non-Bragg reflections were observed. Changes in these reflections in samples heated to 410°, 600°, and 745°C "\Vere investigated. Phase changes in these heated cancrinites we re also studied. Suggestions have been n1ade as to the origin of the non-Bragg reflections. ii ACKNOWLEDGEMENTS The writer wishes to express her sincere appreciation to Professor B. J . Burley, her supervisor, for many discussions and c orrections of the manuscript. Thanks are also extended to Dr. H. D. Grundy for his help with taking precession photographs, to J. Muysson, who did the chemical analyses and to F. Tebay, who took care of the x -ray equipment. Financial support was provided by the Department of Geology, McMaster University, the National Re search Council and the Geological Survey of Canada. iii TABLE OF CONTENTS PAG:E CHAPTER 1 INTRODUCTION 1 CHAPTER 2 STUDIES ON PRECESSION PHOTOGRAPHS OF CANCRINITE -
VALUE ADDED METAL EXTRACTION from RED MUD Department Of
VALUE ADDED METAL EXTRACTION FROM RED MUD Thesis submitted in partial fulfilment of the requirements for the award of the degree of Master of Technology In Mechanical Engineering [Specialization: Steel Technology] Submitted by Ankur Pyasi Roll No. - 212MM2422 Department of Metallurgical and Materials Engineering National Institute of Technology Rourkela-769008 May 2014 National Institute of Technology Rourkela Certificate This is to certify that the thesis entitled “Value added metal extraction from red mud” submitted by Ankur pyasi in partial fulfilment of the requirement for the degree of “Master of Technology” in Mechanical Engineering with specialization in Steel technology, is a bonafide work carried out by him under our supervision and guidance. In our opinion, the work fulfils the requirement for which it is being submitted. Supervisor Prof. Smarajit sarkar Department of Metallurgical & Materials Engineering National Institute of Technology, Rourkela Rourkela – 769008 Email: [email protected] Acknowledgment I wish to express my sincere gratitude to my supervisor Prof. Smarajit sarkar, for giving me an opportunity to work on this project, for his guidance, encouragement and support throughout this work and my studies here at NIT Rourkela. His impressive knowledge, technical skills and human qualities have been a source of inspiration and a model for me to follow. I like to express my deep sense of respect and gratitude to Dr. B.Mishra, Dy. Director at DISIR Rajgangpur, Odisha for their useful suggestions and help rendered to me in carrying out this work. I am grateful to Prof. B C Roy, present Head of the Department of Metallurgical & Materials Engineering Department for providing facilities for smooth conduct of this work.