Iron Working Processes
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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 -
Calcium-Looping Performance of Steel and Blast Furnace Slags for Thermochemical Energy Storage in Concentrated Solar Power Plants
View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by idUS. Depósito de Investigación Universidad de Sevilla Calcium-Looping performance of steel and blast furnace slags for Thermochemical Energy Storage in Concentrated Solar Power plants Jose Manuel Valverde a*, Juan Miranda-Pizarroa,c, Antonio Perejónb,c, Pedro E. Sánchez-Jiménezc, Luis A. Pérez-Maquedac aFacultad de Fisica, Universidad de Sevilla, Avenida Reina Mercedes s/n, 41012 Sevilla, Spain. bDepartamento de Química Inorgánica, Facultad de Química, Universidad de Sevilla, C. Prof. García González 1, Sevilla 41071, Spain. cInstituto de Ciencia de Materiales de Sevilla (C.S.I.C. - Universidad de Sevilla). C. Américo Vespucio 49, Sevilla 41092, Spain. Abstract The Calcium Looping (CaL) process, based on the carbonation/calcination of CaO, has been proposed as a feasible technology for Thermochemical Energy Storage (TCES) in Concentrated Solar Power (CSP) plants. The CaL process usually employs limestone as CaO precursor for its very low cost, non-toxicity, abundance and wide geographical distribution. However, the multicycle activity of limestone derived CaO under relevant CaL conditions for TCES in CSP plants can be severely limited by pore plugging. In this work, the alternative use of calcium-rich steel and blast furnace slags after treatment with acetic acid is investigated. A main observation is that the calcination temperature to regenerate the CaO is significantly reduced as compared to limestone. Furthermore, the multicycle activity of some of the slags tested at relevant CaL conditions for TCES remains high and stable if the treated samples are subjected to filtration. This process serves to remove silica grains, which helps decrease the porosity of the CaO resulting from calcination thus mitigating pore plugging. -
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. -
Effects of Copper on the Cupellation of Silver
Scholars' Mine Bachelors Theses Student Theses and Dissertations 1908 Effects of copper on the cupellation of silver Charles A. Baker Miles Sedivy Follow this and additional works at: https://scholarsmine.mst.edu/bachelors_theses Part of the Mining Engineering Commons Department: Mining Engineering Recommended Citation Baker, Charles A. and Sedivy, Miles, "Effects of copper on the cupellation of silver" (1908). Bachelors Theses. 240. https://scholarsmine.mst.edu/bachelors_theses/240 This Thesis - Open Access is brought to you for free and open access by Scholars' Mine. It has been accepted for inclusion in Bachelors Theses by an authorized administrator of Scholars' Mine. This work is protected by U. S. Copyright Law. Unauthorized use including reproduction for redistribution requires the permission of the copyright holder. For more information, please contact [email protected]. bl.':~M J1IJ!(JWI.'.~1.. ""'~tlION T ,~~. ][VI'ECTS Ol~ COPP}1~H OU TIm CUPlilJJJAT Ion OF SI J~VER • Charles A. Baker Miles Sedivy. MSM til~ t~lCrlt. \lYj,M.cmloi\l (1) ::.:.. :.. : -~..-. : ...... "' .. " : .. ~ --- The ob~iect of this work is to rind--t-he effec't o~ coppa- in - .. = : : .... : - - .. tbe cupellation of silver. - .. Our Method of attack was: 1st. To find the effect of varying the amount of copper with constant lead and constant temperature. 2nd. Effect in cupel"' ation of varying the temperature and the lead in the presence of a constant amount of copper. 3rd. To detecnine the rate at which the copper is removed during cupellation. R.W.Lodge in his book on Assaying states,"If a lead button contains much copper,CuO will be formed with the PbO and this,when absorbed by the cupel,seems to take silver with it into the cupe1.· 2 ~ a.... -
Enhancing the Flotation Recovery of Copper Minerals in Smelter Slags
Heliyon 6 (2020) e03135 Contents lists available at ScienceDirect Heliyon journal homepage: www.cell.com/heliyon Research article Enhancing the flotation recovery of copper minerals in smelter slags from Namibia prior to disposal V. Sibanda a, E. Sipunga a, G. Danha b, T.A. Mamvura b,* a School of Chemical and Metallurgical Engineering, University of the Witwatersrand, Johannesburg, Private Bag 3, Wits, 2050, South Africa b Department of Chemical, Materials and Metallurgical Engineering, Faculty of Engineering and Technology, Botswana International University of Science and Technology, Plot 10071, Boseja Ward, Private Bag 16, Palapye, Botswana ARTICLE INFO ABSTRACT Keywords: Namibia Custom Smelters (NCS) process a range of copper concentrates in their three furnaces, namely; top Metallurgical engineering submerged lance, copper converter and reverberatory furnaces, in order to produce mattes and fayalitic slags. The Materials characterization copper content of the slags range between 0.8 to 5 wt. % and this is considered too high for disposal to the Degradation environment. Currently, the slags are sent to a milling and flotation plant for liberation and recovery of residual Metallurgical process copper. The copper recoveries realized in the plant are much lower than expected and it has been postulated that Metallurgy fi fl fi Materials property some copper minerals may be occurring in forms that are more dif cult to oat like oxides or ne disseminations Top submerged lance in the gangue matrix. Mineralogical analysis of the slag samples was done using X-Ray Diffraction (XRD) and Converter slag Scanning Electron Microscopy (SEM) techniques. The analysis did not reveal the presence of copper oxide min- Reverbetory furnace slag erals, however most scans showed copper sulphide minerals as free grains and some finely disseminated in Copper recovery fayalite gangue. -
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. -
Xstrata Technology Update Edition 13 – April 2012 Building Plants That Work
xstrata technology update Edition 13 – April 2012 Building plants that work You have to get a lot of things it takes another operator to get them right to build a plant that works. right. Someone who has lived through the problems, had to do the maintenance, operated during a midnight power Of course the big picture must be right – doing the right project, in the right place, failure, cleaned up the spill. Someone at the right time. who has “closed the loop” on previous designs; lived with previous decisions After that, the devil is in the detail. You and improved them, over and over. need a sound design, good execution, good commissioning, and ongoing This is why Xstrata Technology provides support after commissioning. You need a technology “package”. Just as a car to operate and maintain your plant in is more than an engine, technology is the long run, long after the construction more than a single piece of equipment. company has left. That’s when all the Technology is a system. All the elements “little” details become important – how of the system have to work with each easy is it to operate, how good is the other and with the people in the plant. maintenance access, what happens in We want our cars designed by people a power failure, where are the spillage who love cars and driving. So should points and how do we clean them our plants be designed by people with up? Are the instruments reliable and experience and passion to make each is the process control strategy robust one work better than the last. -
Characterization and Recovery of Copper from Smelting Slag
CHARACTERIZATION AND RECOVERY OF COPPER FROM SMELTING SLAG A. P. GABRIEL*, L. R. SANTOS*, A.C. KASPER*, H. M. VEIT* * Materials Engineering Department, Engineering School, Universidade Federal do Rio Grande do Sul (UFRGS), Porto Alegre, Brazi SUMMARY: 1. INTRODUCTION. 2. EXPERIMENTAL. 2.1 Hazardousness test. 2.2 Chemical and mineralogical characterization. 2.3 Leaching 3. RESULTS AND DISCUSSION 3.1 Hazardousness Test. 3.2 Chemical and mineralogical characterization. 3.3 Leaching. 4. CONCLUSION. REFERENCES. 1. INTRODUCTION The generation of industrial solid waste constitutes an environmental problem that requires efforts for adequate disposal. Currently, in Brazil, solid waste management is standardized, with a classification determining the management according to its hazardous characteristics. ABNT NBR 10004 is a Brazilian Standard to solid waste and classifies its as: Class I (hazardous), Class II - A (non - hazardous and non - inert) and Class II - B (non - hazardous and inert) according to the concentration of elements that have potential risks to the environment and public health (ABNT NBR 10,004, 2004) A process with a large generation of wastes is the production of copper. Several studies in the last decades investigated routes to recovery copper and other metals of interest from the slag (solid waste from the foundry). In the case of primary production, the slag has copper contents between 0.5 and 2% and the volume generated is twice the refined metal (Schlesinger et al., 2011) In addition to primary copper production, there is a significant rate of the copper production from scrap/waste metal. Secondary copper production in Brazil in 2014 reached 23,600 tons, representing around 9% of domestic production. -
REFERENCE GUIDE to Treatment Technologies for Mining-Influenced Water
REFERENCE GUIDE to Treatment Technologies for Mining-Influenced Water March 2014 U.S. Environmental Protection Agency Office of Superfund Remediation and Technology Innovation EPA 542-R-14-001 Contents Contents .......................................................................................................................................... 2 Acronyms and Abbreviations ......................................................................................................... 5 Notice and Disclaimer..................................................................................................................... 7 Introduction ..................................................................................................................................... 8 Methodology ................................................................................................................................... 9 Passive Technologies Technology: Anoxic Limestone Drains ........................................................................................ 11 Technology: Successive Alkalinity Producing Systems (SAPS).................................................. 16 Technology: Aluminator© ............................................................................................................ 19 Technology: Constructed Wetlands .............................................................................................. 23 Technology: Biochemical Reactors ............................................................................................. -
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]. -
Lecture 12 Converter Steelmaking Practice & Combined Blowing
Lecture 12 Converter Steelmaking Practice & combined blowing Contents: Refining of hot metal Composition and temperature during the blow Physico-chemical interactions Developments in Top blown steelmaking practice Concept of bottom stirring in top blowing Top blowing attributes Characteristic feature of converter steelmaking Environmental issues in oxygen steelmaking Causes of high turnover rates of BOF Key words: Top blown steelmaking, combined blowing, bottom stirring, hot metal refining Refining of hot metal After the previous heat is tapped and slag is drained, lining is inspected. Scrap and hot metal are charged. Converter is tilted into the vertical position and the lance is lowered in the vessel to start the blowing. Selection of the starting lance distance is such that the concentration of the force at the bath level should not cause ejection of tiny iron particles (sparking) and at the same time maximum bath surface area is covered by the oxygen jet. The starting lance distance(Xi) for specific oxygen blowing Nm 3 3 rate ton ×min can be calculated by 1.04 Xi = 0.541(db) db is bath diameter in meter. For 150 Tons converter, db = 4.87 m and Xi = 2.8 m, when oxygen flow rate in approximately 450 Nm3/min. Initially oxygen is blown soft by keeping lance distance higher to promote slag formation and to avoid ejection of small particles, because hot metal is not covered by slag. Lime may be added either at the beginning of the blow or in portion during the blow. Oxygen is blown for nearly 15-20 minutes by progressively decreasing the lance distance such that slag foaming remains under control and oxidation reactions occur uninterruptedly.