“Optimization in the Treatment of Spent Pot Lining - a Hazardous Waste Made Safe”

Total Page:16

File Type:pdf, Size:1020Kb

“Optimization in the Treatment of Spent Pot Lining - a Hazardous Waste Made Safe” A M.TECH THESIS ON “optimization in the treatment of Spent pot Lining - A Hazardous Waste Made Safe” MASTER OF TECHNOLOGY IN Chemical Engineering SUBMITTED BY Pankaj D. Indurkar Roll No. 212CH1074 Under the Supervision of Prof. Pradip Rath NATIONAL INSTITUTE OF TECHNOLOGY, ROURKELA 2013-2014 DEPARTMENT OF CHEMICAL ENGINEERING NATIONAL INSTITUTE OF TECHNOLOGY, ROURKELA CERTIFICATE This is to certify that the Project report entitled, “Optimization in the treatment of Spent Pot Lining - A Hazardous Waste Made Safe” submitted by Pankaj D. Indurkar, Roll No. 212CH1074 for the award of the Master of Technology Degree in Chemical Engineering at National Institute of Technology, Rourkela is prepared by him under my supervision and guidance. Date: Prof. Pradip Rath (Supervisor) ACKNOWLEDGEMENT I feel great pleasure in expressing my deepest sense of gratitude and sincere thanks to my guide Prof. Pradip Rath for his valuable guidance and grandeur during the project work, which it would have been very difficult task. I have no words to express my sincere thanks for valuable guidance, extreme assistance and cooperation extended to all the Teaching Staff Members of my Department. This acknowledgement would be incomplete without expressing my special thanks to Prof. R. K. Singh Head of Chemical Department for his support during the work. Last but not least I would like to thanks all the Non-Teaching staff members of the department and my colleague‘s friends those who helped me directly or indirectly for completing of this seminar successfully. Date: Mr. Pankaj D. Indurkar Roll No. 212CH1074 CONTENTS List of figure List of table Abbreviations Abstract Page No. CHAPTER 1: INTRODUCTION 1 1.1 Some facts about Aluminium 1 1.2 Spent Pot Lining (SPL) 2 1.3 Manufacture of Pure Alumina 2 1.4 Electrolysis of Alumina 3 1.5 Chemistry 5 1.6 Spent Pot Liner Waste Challenges 6 1.7 Objective of the project 7 1.7.1 Specific objective 7 CHAPTER 2: LITERATURE REVIEW 8 2.1 Thermal processes 9 2.2 Chemical processes 10 2.3 Rio Tinto Alcan—LCL&L Process 11 2.4 Alternate Processes to Primary Aluminium Smelting (Emerging Technologies) 12 2.5 Industrial use of SPL 13 2.5.1 Cement kiln 13 2.5.2 Pig iron and steel 14 2.5.3 Mineral Wool 14 2.5.4 Co-Processing SPL with Salt Slags 14 2.5.5 Ferro Alloys 15 2.5.6 Special products of 2nd cut 15 CHAPTER 3: MATERIALS AND METHODS 16 3.1 Materials 16 3.1.1 Instruments and its purpose 16 3.1.2 Chemicals used 17 3.2 Methods 17 3.2.1 Collection of sample 17 3.2.2 Experimental design 18 3.2.2.1 Definition of Experiment design 18 3.2.2.2 Objective of experimental designing 18 3.2.3 Conventional approach of optimization 18 3.2.4 Design of experiments by Taguchi method for optimization 18 3.2.4 Design of experiment by Response Surface Methodology 19 3.2.5 Leaching experiments 20 3.2.5.1 Cryolite precipitation 20 3.3 Characterization of spent pot liner 21 3.3.1 Thermo gravimetric Analysis (TGA) / DSC 21 3.3.2 XRD analysis 21 3.3.3 Ultimate and Proximate analysis 21 3.3.3.1 Moisture content 21 3.3.3.2 Volatile matter 22 3.3.3.3 Fixed carbon content 22 3.3.4 SEM-EDX analysis 22 3.3.5 Calorific value analysis 22 CHAPTER 4: RESULTS AND DISCUSSION 23 PART 1 4.1 Taguchi optimization of NaOH fallowed by HClO4 23 4.1.1 Treatment of sample 23 4.1.2 Alkali leaching 23 4.1.3 Acid leaching 23 4.1.4 Analysis of the S/N ratio 25 4.1.5 Analysis of variance 27 4.2 Classical approach of optimization for NaOH fallowed by HClO4 28 4.2.1 Effect of alkali concentration 28 4.2.2 Effect of acid concentration 29 4.2.3 Effect of L/S ratio 30 4.2.4 Effect of temperature 31 4.2.5 Cryolite precipitation 32 4.3 Characterization of raw and treated sample 33 4.3.1 Thermo gravimetric Analysis/DSC 33 4.3.2 XRD analysis 35 4.3.3 Ultimate and Proximate analysis 35 4.3.4 Particle size analysis by DLS 36 4.3.5 SEM- EDX analysis 37 4.3.6 Calorific value analysis 41 4.4 Response Surface Methodology of NaOH fallowed by HClO4 41 4.4.1 Analysis of variance 44 4.4.2 Contour Plot and Surface plot 46 4.4.3 Residual plot 58 PART 2 4.5 Taguchi optimization of NaOH fallowed by H2SO4 49 4.5.1 Analysis of the S/N ratio 50 4.5.2 Analysis of variance 51 4.6 Classical approach of optimization of NaOH fallowed by H2SO4 52 4.6.1 Effect of alkali concentration 52 4.6.2 Effect of acid concentration 53 4.6.3 Optimization of L/S 53 4.6.4 Optimization of temperature 54 4.6.5 XRD analysis 55 4.6.6 Cryolite precipitation 56 4.6.7 Proximate analysis 58 4.6.8 Calorific value analysis 58 CHAPTER 5: CONCLUSION 59 5.1 Future recommendations 60 CHAPTER 6: REFERENCES 61 LIST OF FIGURES Figure No. Figure caption Page no. Figure 1.1 Flow sheet of the Bayer process 2 Figure 1.2 Hall-Heroult Cell With process Flow Diagram 4 Figure 2.1 Spent pot linings 9 Figure 2.2 Rio Tinto Alcan—LCL&L simplified flow sheet. 11 Figure 4.1 Main effect plot for SN ratios 26 Figure 4.2 Contour plot of leaching percentage vs. alkali content, temperature 26 Figure 4.3 Contour plot of leaching percentage vs. L/S ratio, alkali concentration 27 Figure 4.4 Influence of alkali concentration on leaching percentage 29 Figure 4.5 Influence of acid concentration on leaching percentage 30 Figure 4.6 Influence of L/S on leaching percentage 31 Figure 4.7 Influence of temperature on leaching percentage 32 Figure 4.8 XRD analysis of fluoride precipitation at pH value of 9.5 32 Figure 4.9 XRD analysis of fluoride precipitation at pH value of 4.5 33 Figure 4.10 TGA under N2 flow 34 Figure 4.11 TGA under O2 flow 34 Figure 4.12 XRD analysis of Raw SPL, Treated SPL with NaOH and treated SPL 35 with NaOH fallowed by HClO4 Figure 4.13 Particle size analysis of raw SPL 36 Figure 4.14 SEM-EDX images of raw SPL 37 Figure 4.15 SEM-EDX images of water wash SPL 38 Figure 4.16 SEM images Raw SPL sample burned at 7500C for 1.5h and at 800 0C 39 Figure 4.17 SEM images of alkali treatment SPL at 1.5 M NaOH 40 Figure 4.18 SEM images of alkali followed by acid treatment SPL1.5 40 MNaOH+2.5M HCLO4 Figure 4.19 Contour plot of leaching percentage vs acid concentration L/S ratio & 46 Contour plot of leaching percentage vs alkali concentration, temperature Figure 4.20 Surface plot for leaching percentage vs acid concentration, alkali 47 concentration & Surface plot for leaching percentage vs acid concentration, L/S ratio Fgure 4.21 Surface plot for leaching percentage vs acid concentration, 47 temperature Figure 4.22 Residual plot for leaching percentage 48 Figure 4.23 Main effect plot for SN ratio 51 Figure 4.24 Effect of alkali concentration on leaching percentage 52 Figure 4.25 Influence of acid concentration on leaching percentage 53 Figure 4.26 Influence of L/S on leaching percentage 54 Figure 4.27 Influence of temperature on leaching percentage 55 Figure 4.28 XRD analysis of raw SPL, Alkali treated SPL, and treated SPL with 56 NaOH Fallowed by H2SO4 samples Figure 4.29 XRD analysis of fluoride precipitation at pH value of 9.5 57 Figure 4.30 XRD analysis of fluoride precipitation at pH value of 4.5 57 LIST OF TABLES Table no. Table caption Page no. Table 2.1 SPL typical components and concentration 8 Table 3.1 Instrument and its purpose 16 Table 3.2 Taguchi 4 factors 4 levels 19 Table 3.3 Ranges of experimental parameters 20 Table 4.1 Taguchi design of NaOH fallowed by HClO4 24 Table 4.2 Response Table for Signal to Noise Ratios 25 Table 4.3 Analysis of variance of SN ratio 28 Table 4.4 Proximate analysis of SPL samples 35 Table 4.5 Ultimate analysis of SPL samples 36 Table 4.6 Calorific values of Samples 41 Table 4.7 The central composite design with four independent variables 42 and experimental leaching percentage Table 4.8 Regression coefficient, p or probability for leaching percentage 43 Table 4.9 ANOVA for leaching percentage using Adjusted Sum of 45 Squares (SS) for tests Table 4.10 Taguchi design of NaOH fallowed by H2SO4 52 Table 4.11 Response Table for Signal to Noise Ratios 50 Table 4.12 Analysis of variance for SN ratio 52 Table 4.13 Proximate analysis of SPL samples 58 Table 4.14 Calorific value of raw SPL to treated SPL with H2SO4 58 ABBREVIATIONS SPL- Spent Pot Liner ANOVA-Analysis of Variance CHNS-Carbon, Hydrogen, Nitrogen, Sulfur L/S Ratio- Liquid to Solid Ratio RSM- Response Surface Methodology SEM- Scanning Electron Microscope EDX- Energy Dispersive X-ray TGA- Thermo-Gravimetric Analysis XRD- X-ray Diffraction GCV- Gross Calorific Value DSC- Differential scanning calorimetry LIST OF SYMBOLS x1 - Acid concentration x2 - Alkali concentration x3 - L/S ratio x4 - Temperature S- Response variable R2 - amount of variation in the observed response values ABSTRACT The increase in demand of aluminium leads to production of more Spent Pot Lining as well as more environmental problems.
Recommended publications
  • Equilibrium Gasification of Spent Pot Lining from the Aluminum Industry
    Equilibrium Gasification of Spent Pot lining from the Aluminum Industry Isam Janajreh1, Khadije Elkadi1, Olawale Makanjuola1, Sherien El-Agroudy2 1Khalifa University of Science and Technology, Mechanical Engineering Department, Abu Dhabi, UAE 1AinShams University, Environment Engineering Department, Cairo, Egypt 2Sharjeh University, Sustainable and Renewable Energy Department, Sharjah, UAE Abstract: The notion of reuse, recycle and reduce is suited for almost all streams of solid waste; including municipal solid waste as well as many streams of industrial wastes. Spent potlining (SPL) is a poisonous and potentially explosive solid waste from aluminum industry that defies this general consensus, being hazardous to reuse, non-recyclable, and increasing with over 2Mt annually. In this work, the technical feasibility of gasification of SPL through equilibrium modeling following different levels of treatment (water washed-WWSPL, acid treated-ATSPL, fully treated-FTSPL) is pursued. The model considers 12 species (CO, H2, CH4, N2, NH3, H2S, COS, H2O and Ash) including the molar ratio of the moderator (H2O) and the oxidizer (O2) to that of the SPL. The process metrics are assessed via the produced syngas fraction (CO and H2), gasification efficiency (GE) and in comparison/validation to the gasification of a baseline bituminous coal. The SPL results for each of the WWSPL, ATSPL, FTSPL, respectively, revealed GE of 40%, 65%, and 75% with corresponding syngas (CO & H2) molar fractions at 0.804 & 0.178, 0.769 & 0.159, and 0.730 & 0.218 at temperatures of 1450 oC, 1100 oC, and 1150 oC. These results suggest the potential and feasibility of gasifying only the treated SPL. Keywords: Spent potlining; Aluminum waste; Gasification; Syngas 1.
    [Show full text]
  • Development of a Combined Leaching and Ion‑Exchange System for Valorisation of Spent Potlining Waste
    Waste and Biomass Valorization https://doi.org/10.1007/s12649-020-00954-1 ORIGINAL PAPER Development of a Combined Leaching and Ion‑Exchange System for Valorisation of Spent Potlining Waste Thomas J. Robshaw1 · Keith Bonser2 · Glyn Coxhill2 · Robert Dawson3 · Mark D. Ogden1 Received: 8 August 2019 / Accepted: 3 February 2020 © The Author(s) 2020 Abstract This work aims to contribute to addressing the global challenge of recycling and valorising spent potlining; a hazardous solid waste product of the aluminium smelting industry. This has been achieved using a simple two-step chemical leaching treat- ment of the waste, using dilute lixiviants, namely NaOH, H 2O2 and H 2SO4, and at ambient temperature. The potlining and resulting leachate were characterised by spectroscopy and microscopy to determine the success of the treatment, as well as the morphology and mineralogy of the solid waste. This confrmed that the potlining samples were a mixture of contaminated graphite and refractory materials, with high variability of composition. A large quantity of fuoride was solublised by the leaching process, as well as numerous metals, some of them toxic. The acidic and caustic leachates were combined and the aluminium and fuoride components were selectively extracted, using a modifed ion-exchange resin, in fxed-bed column experiments. The resin performed above expectations, based on previous studies, which used a simulant feed, extracting fuoride efciently from leachates of signifcantly diferent compositions. Finally, the fuoride and aluminium were coeluted from the column, using NaOH as the eluent, creating an enriched aqueous stream, relatively free from contaminants, from which recovery of synthetic cryolite can be attempted.
    [Show full text]
  • Highly Efficient Fluoride Extraction from Simulant Leachate of Spent Potlining Via La-Loaded Chelating Resin
    This is a repository copy of Highly efficient fluoride extraction from simulant leachate of spent potlining via La-loaded chelating resin. An equilibrium study. White Rose Research Online URL for this paper: http://eprints.whiterose.ac.uk/134730/ Version: Accepted Version Article: Robshaw, T.J., Tukra, S., Hammond, D. et al. (2 more authors) (2019) Highly efficient fluoride extraction from simulant leachate of spent potlining via La-loaded chelating resin. An equilibrium study. Journal of Hazardous Materials, 361. pp. 200-209. ISSN 0304-3894 https://doi.org/10.1016/j.jhazmat.2018.07.036 © 2018 Elsevier B.V. This is an author produced version of a paper subsequently published in Journal of Hazardous Materials. Uploaded in accordance with the publisher's self-archiving policy. Article available under the terms of the CC-BY-NC-ND licence (https://creativecommons.org/licenses/by-nc-nd/4.0/) Reuse This article is distributed under the terms of the Creative Commons Attribution-NonCommercial-NoDerivs (CC BY-NC-ND) licence. This licence only allows you to download this work and share it with others as long as you credit the authors, but you can’t change the article in any way or use it commercially. More information and the full terms of the licence here: https://creativecommons.org/licenses/ Takedown If you consider content in White Rose Research Online to be in breach of UK law, please notify us by emailing [email protected] including the URL of the record and the reason for the withdrawal request. [email protected] https://eprints.whiterose.ac.uk/ Highly Efficient Fluoride Extraction from Simulant Leachate of Spent Potlining via La-Loaded Chelating Resin.
    [Show full text]
  • Highly Efficient Fluoride Extraction from Simulant Leachate of Spent Potlining T Via La-Loaded Chelating Resin
    Journal of Hazardous Materials 361 (2019) 200–209 Contents lists available at ScienceDirect Journal of Hazardous Materials journal homepage: www.elsevier.com/locate/jhazmat Highly efficient fluoride extraction from simulant leachate of spent potlining T via La-loaded chelating resin. An equilibrium study ⁎ Thomas Robshawa, , Sudhir Tukrab, Deborah B. Hammondc, Graham J. Leggettc, Mark D. Ogdena a Separations and Nuclear Chemical Engineering Research (SNUCER), Department of Chemical & Biological Engineering, University of Sheffield, Sheffield, S1 3JD, United Kingdom b Bawtry Carbon International Ltd., Austerfield, Doncaster, DN10 6QT, United Kingdom c Department of Chemistry, University of Sheffield, Sheffield, S3 7HF, United Kingdom GRAPHICAL ABSTRACT ARTICLE INFO ABSTRACT Keywords: Spent potlining (SPL) hazardous waste is a potentially valuable source of fluoride, which may be recovered Spent potlining through chemical leaching and adsorption with a selective sorbent. For this purpose, the commercially available ® Purolite S950+ chelating resin Purolite S950+ was loaded with lanthanum ions, to create a novel ligand-exchange sorbent. The Chelating resin equilibrium fluoride uptake behaviour of the resin was thoroughly investigated, using NaF solution andasi- Fluoride uptake mulant leachate of SPL waste. The resin exhibited a large maximum defluoridation capacity of 187 ± 15 mg Lanthanum g−1 from NaF solution and 126 ± 10 mg g−1 from the leachate, with solution pH being strongly influential to uptake performance. Isotherm and spectral data indicated that both chemisorption and unexpected physisorp- tion processes were involved in the fluoride extraction and suggested that the major uptake mechanism differed in each matrix. The resin demonstrates significant potential in the recovery of fluoride from aqueous waste- streams.
    [Show full text]
  • Implementing Sustainability at Alcan Primary Metal - British Columbia
    IMPLEMENTING SUSTAINABILITY AT ALCAN PRIMARY METAL - BRITISH COLUMBIA Sheldon Shawn Zettler B.Sc., University of Winnipeg, 1990 B.Sc. Environmental Engineering, University of Guelph, 1995 Graduate Diploma, Business Administration, Simon Fraser University, 2003 PROJECT SUBMITTED IN PARTIAL FULFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF MASTER OF BUSINESS ADMINISTRATION In the Faculty of Business Administration Executive MBA O Shawn Zettler 2005 SIMON FRASER UNIVERSITY Fall 2005 All rights reserved. This work may not be reproduced in whole or in part, by photocopy or other means, without permission of the author. APPROVAL Name: Sheldon Shawn Zettler Degree: Master of Business Administration Title of Project: Implementing Sustainability at Alcan Primary Metal - British Columbia Supervisory Committee: Dr. Mark Selman, Senior Supervisor Executive Director, Learning Strategies Group, Faculty of Business Administration Dr. Mark Moore, Second Reader Lecturer, Faculty of Business Administration Date Approved: SIMON~~~~~mlibrary FRASER DECLARATION OF PARTIAL COPYRIGHT LICENCE The author, whose copyright is declared on the title page of this work, has granted to Simon Fraser University the right to lend this thesis, project or extended essay to users of the Simon Fraser University Library, and to make partial or single copies only for such users or in response to a request from the library of any other university, or other educational institution, on its own behalf or for one of its users. The author has further granted permission to Simon Fraser University to keep or make a digital copy for use in its circulating collection, and, without changing the content, to translate the thesislproject or extended essays, if technically possible, to any medium or format for the purpose of preservation of the digital work.
    [Show full text]
  • Development of a Combined Leaching and Ion-Exchange System for Valorisation of Spent Potlining Waste
    Development of a combined leaching and ion-exchange system for valorisation of spent potlining waste Thomas J. Robshaw1*, Keith Bonser2, Glyn Coxhill2, Robert Dawson3 and Mark D. Ogden1 1Separations and Nuclear Chemical Engineering Research (SNUCER), Department of Chemical & Biological Engineering, University of Sheffield, Mappin Street, Sheffield, South Yorkshire, S1 3JD, United Kingdom 2Bawtry Carbon International Ltd., Austerfield, Doncaster, South Yorkshire, DN10 6QT, United Kingdom 3Department of Chemistry, University of Sheffield, Western Bank, Sheffield, South Yorkshire, S3 7HF, United Kingdom *+447534 304805, [email protected] Abstract This work aims to contribute to addressing the global challenge of recycling and valorising spent potlining; a hazardous solid waste product of the aluminium smelting industry. This has been achieved using a simple two-step chemical leaching treatment of the waste, using dilute lixiviants, namely NaOH, H2O2 and H2SO4, and at ambient temperature. The potlining and resulting leachate were characterised by spectroscopy and microscopy to determine the success of the treatment, as well as the morphology and mineralogy of the solid waste. The acidic and caustic leachates were combined and the fluoride component was selectively extracted, using a modified ion-exchange resin, in fixed-bed column experiments. Solid-state analysis confirmed that the potlining samples were a mixture of contaminated graphite and refractory materials. A large quantity of fluoride was solublised by the leaching process, as well as numerous metals, some of them toxic. In column-loading studies, the resin performed above expectations, based on previous studies, which used a simulant feed, extracting fluoride efficiently from leachates of significantly different compositions. Overall, the study accomplished several steps in the development of a fully-realised spent potlining treatment system.
    [Show full text]
  • United Nations Environment Programme)
    UNITED NATIONS SC UNEP/POPS/COP.3/INF/4 Distr.: General 13 April 2007 United Nations Environment Original: English Programme Conference of the Parties of the Stockholm Convention on Persistent Organic Pollutants Third meeting Dakar, 30 April–4 May 2007 Item 5 (h) of the provisional agenda* Matters for consideration or action by the Conference of the Parties: financial resources Draft guidelines on best available techniques and provisional guidance on best environmental practices relevant to Article 5 and Annex C∗∗ Note by the Secretariat As referenced in document UNEP/POPS/COP.3/7, the annex to the present note contains revised draft guidelines on best available techniques and best environmental practices relevant to Article 5 and Annex C of the Stockholm Convention on Persistent Organic Pollutants. The revised draft guidelines and provisional guidance have not been formally edited. * UNEP/POPS/COP.3/1. ∗∗ Stockholm Convention, Article 5 and Annex C; reports of the Conference of the Parties of the Stockholm Convention on Persistent Organic Pollutants on the work of its first meeting (UNEP/POPS/COP.1/31), Annex I, decisions SC-1/19 and SC-1/20 and on the work of its second meeting (UNEP/POPS/COP.2/30), Annex I, decision SC-2/4. REVISED DRAFT GUIDELINES ON BEST AVAILABLE TECHNIQUES AND PROVISIONAL GUIDANCE ON BEST ENVIRONMENTAL PRACTICES RELEVANT TO ARTICLE 5 AND ANNEX C OF THE STOCKHOLM CONVENTION ON PERSISTENT ORGANIC POLLUTANTS GENEVA, SWITZERLAND DECEMBER 2006 TABLE OF CONTENTS SECTION I : INTRODUCTION I. A PURPOSE I. B STRUCTURE OF DOCUMENT AND USING GUIDELINES AND GUIDANCE I. C CHEMICALS LISTED IN ANNEX C: DEFINITIONS, RISKS, TOXICITY I.
    [Show full text]
  • 2019 Alcoa Sustainability Report
    2019 Alcoa Sustainability Report Alcoa Sustainability Performance 2019 0 0.2% employee and increase in contractor fatalities energy intensity Approximately 0.86 0.4% days away, increase in 73% restricted and transfer carbon dioxide of electricity consumed rate per 100 full-time equivalent by our smelters workers emissions was from renewable sources 6% reduction in bauxite residue land requirements per 1,000 metric tons of alumina produced since the 2015 baseline 0.97:1 7.7% ratio for increase in new active mining landfilled waste disturbance to 0.1% mine rehabilitation decline in net for the water consumption 2015 to 2019 period 15.5% of our global employees were US$6.0 women million in Alcoa Foundation community investments 95 US$8.8 score on the billion in 9,999 Corporate purchased employee volunteer hours Equality Index goods and in the community 2019 services 2 Table of Contents From the CEO ............................................................. 4 Improving Our Footprint .................................... 60 Climate Protection ..................................................... 61 Our Company .............................................................. 5 Energy ........................................................................... 65 Corporate Overview .....................................................6 Biodiversity and Mine Rehabilitation .................... 68 Governance, Ethics and Compliance .....................7 Tailings Management ................................................ 73 Legal Compliance .........................................................9
    [Show full text]
  • Fundamental and Applied Studies on Cyanide Formation in the Carbon
    FUNDAMENTAL AND APPLIED STUDIES ON CYANIDE FORMATION IN THE CARBON LINER OF AN INDUSTRIAL ALUMINIUM ELECTROLYTIC CELL by Bin Kiat YAP I A dissertation submitted in fulfilment of the requirements for the degree of Master of Science (Chemistry) THE UNIVERSITY OF TASMANIA HOBART, AUSTRALIA Date: July 1985 - i - ACKNOWLEDGEMENTS My a'ppreciation to my supervisor, Dr. Peter Smith, and to Dr. Barry 0' Grady for their suggestions and encouragement during the course of this project. Acknowledg~ment is also due to Tony Feest, John Osborne and other · members of staff of Development Services (Comalco Ltd., Bell Bay) for their interest and help in my work. Grateful acknowledgement ~ust also go to Comalco Aluminium (Bell Bay) Limited and Comalco Research Centre (Thomastown) for the facilities that enabled this project to be carried out. In addition, I would like to extend my thanks to Professor Barry Welch (University ~f Auckland, New Zealand) for the many suggestions and interest in my research. Sincere thanks are extended to Margare~ Pakura for her care and application in the typing of this thesis. Special thanks go to my wife, Edna, for her encouragement and understanding~ - ii - DECLARATION OF ORIGINALITY - This is to certify that the work presented in this thesis has not been.submitted previously to any other university or institution for a degree or award. &r~l BIN KIAT YAP - iii - ABSTRACT The objective of this study was to investigate the presence of cyanitle in the industrial ·aluminium electrolytic cell. Therefore, it was an aim of this investigation to identify the favoured regions of cyanide formation in potlining, and conduct parallel laboratory studies to determine some of the chemical factors likely to influence cyanide formation.
    [Show full text]
  • Considerations for Dealing with Spent Potlining Technical Paper for 11Th Australasian Aluminium Smelting Technology Conference
    Considerations for Dealing with Spent Potlining Technical Paper for 11th Australasian Aluminium Smelting Technology Conference Bernie J Cooper, Regain Technologies Pty Ltd, Australia Abstract The carbon cathode and refractory lining material that is removed from the electrolytic cells (or pots) used in primary aluminium smelting is known as spent potlining (SPL). SPL is hazardous waste material subject to close regulatory control in most jurisdictions and its disposal has proven to be a challenge for the aluminium industry. This paper sets out considerations for dealing with SPL. A review of the chemical reactions that take place during the typical operational life of the lining leads to an overview of the chemical composition of the resultant SPL material and its inherent hazards. Potential safety and environmental risks associated with the SPL hazards are discussed. Issues to be addressed in using SPL as input to downstream industrial processes are examined using cement manufacture as a case study. Life cycle analysis is used to support an approach to optimising the economic use of all of the SPL material thus ensuring its safe and effective disposal. Keywords: Spent potlining, Aluminium smelting, Hall-Heroult process, Fluoride, Cyanide, Hazardous waste.. Introduction Production of primary aluminium metal with the Hall-Heroult process involves electrolytic reduction of alumina in cells or pots. The electrolyte is made up of molten sodium aluminium fluoride (cryolite) and other additives and is contained in a carbon and refractory lining in a steel potshell. Over time, the effectiveness of the lining deteriorates and the lining of the pot is removed and replaced. The lining material that is removed from the pots is known as spent potlining (SPL).
    [Show full text]
  • Environmental Assessment: Spent Potlining Processing
    Weston Aluminium Pty Ltd 06-Sep-2016 Environmental Assessment: Spent Potlining Processing Modification to DA 86_04_01 & DA_10397 of 1995 AECOM Environmental Assessment: Spent Potlining Processing – DA 86_04_01 MOD 10 & DA_10397 MOD 8 Environmental Assessment: Spent Potlining Processing DA 86_04_01 MOD 10 & DA_10397 MOD 8 Client: Weston Aluminium Pty Ltd ABN: 91 075 245 108 Prepared by AECOM Australia Pty Ltd 17 Warabrook Boulevard, Warabrook NSW 2304, PO Box 73, Hunter Region MC NSW 2310, Australia T +61 2 4911 4900 F +61 2 4911 4999 www.aecom.com ABN 20 093 846 925 06-Sep-2016 Job No.: 60486360 AECOM in Australia and New Zealand is certified to the latest version of ISO9001, ISO14001, AS/NZS4801 and OHSAS18001. © AECOM Australia Pty Ltd (AECOM). All rights reserved. AECOM has prepared this document for the sole use of the Client and for a specific purpose, each as expressly stated in the document. No other party should rely on this document without the prior written consent of AECOM. AECOM undertakes no duty, nor accepts any responsibility, to any third party who may rely upon or use this document. This document has been prepared based on the Client’s description of its requirements and AECOM’s experience, having regard to assumptions that AECOM can reasonably be expected to make in accordance with sound professional principles. AECOM may also have relied upon information provided by the Client and other third parties to prepare this document, some of which may not have been verified. Subject to the above conditions, this document may be transmitted, reproduced or disseminated only in its entirety.
    [Show full text]
  • Spent Pot Lining Project (Feasibility of an Agreement Based Approach to Clear Stockpiles)
    Spent pot lining project (feasibility of an agreement based approach to clear stockpiles) Final national summary report October 2016 In association with: Spent pot lining project (feasibility of an agreement based approach to clear stockpiles) Final national summary report Client The Department of the Environment and Energy (DoEE) Client Contact Paul Starr Assistant Director Hazardous Waste Section Chemicals & Waste Branch Department of the Environment and Energy 02 6274 1909 / 0408 476 740 [email protected] Authors Paul Randell (REC), Geoff Latimer (Ascend Waste and Environment) Project Number: PREC063 Report Disclaimer This report has been prepared for DoEE in accordance with the terms and conditions of appointment dated 30/04/2016. Randell Environmental Consulting Pty Ltd (ABN 17 153 387 501) cannot accept any responsibility for any use of or reliance on the contents of this report by any third party. Randell Environmental Consulting Pty Ltd ABN 17 153 387 501 Woodend Victoria 3442 [email protected] Phone 0429 501 717 Contents Executive summary ................................................................................................................................ iv 1 Introduction ................................................................................................................................... 1 1.1 Project scope ........................................................................................................................... 1 1.2 Project background and context ............................................................................................
    [Show full text]