Modelling of an autoclave used for high pressure sulphuric acid/oxygen leaching of first stage leach residue. Part 1: Model development
•Discussion of different leaching reactor modelling approaches.•Overview of base metal refinery pressure leaching process and leaching chemistry.•Steady state and dynamic model developed to predict pressure leaching performance. Pressure leaching of the first stage leach residue in Base Metal Refine...
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Veröffentlicht in: | Minerals engineering 2013-11, Vol.53, p.220-227 |
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creator | Dorfling, C. Akdogan, G. Bradshaw, S.M. Eksteen, J.J. |
description | •Discussion of different leaching reactor modelling approaches.•Overview of base metal refinery pressure leaching process and leaching chemistry.•Steady state and dynamic model developed to predict pressure leaching performance.
Pressure leaching of the first stage leach residue in Base Metal Refinery (BMR) circuits aims to achieve high base metal dissolution with minimal precious metal leaching. Optimum autoclave operation is challenging because of the complex leaching chemistry, varying mineralogy of the feed material, and interaction between the different process variables. This research involved the modelling of the pressure leaching stages with flash recycle cooling at a typical BMR. The steady state solution employed the sequential modular approach in MATLAB, while the dynamic simulation involved the simultaneous solution of a set of differential equations, derived from mass and energy balances, in MATLAB. Part I of this communication presents a discussion of the Western Platinum Ltd. BMR process, an overview of relevant literature, and the strategies followed to develop both a steady state model and a dynamic model. Part II of this communication discusses the application of the models. |
doi_str_mv | 10.1016/j.mineng.2013.03.005 |
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Pressure leaching of the first stage leach residue in Base Metal Refinery (BMR) circuits aims to achieve high base metal dissolution with minimal precious metal leaching. Optimum autoclave operation is challenging because of the complex leaching chemistry, varying mineralogy of the feed material, and interaction between the different process variables. This research involved the modelling of the pressure leaching stages with flash recycle cooling at a typical BMR. The steady state solution employed the sequential modular approach in MATLAB, while the dynamic simulation involved the simultaneous solution of a set of differential equations, derived from mass and energy balances, in MATLAB. Part I of this communication presents a discussion of the Western Platinum Ltd. BMR process, an overview of relevant literature, and the strategies followed to develop both a steady state model and a dynamic model. Part II of this communication discusses the application of the models.</description><identifier>ISSN: 0892-6875</identifier><identifier>EISSN: 1872-9444</identifier><identifier>DOI: 10.1016/j.mineng.2013.03.005</identifier><language>eng</language><publisher>Elsevier Ltd</publisher><subject>Autoclaving ; Base metal ; Hydrometallurgy ; Leaching ; Mathematical models ; Matlab ; Modelling ; Precious metal ores ; Pressure leaching ; Residues</subject><ispartof>Minerals engineering, 2013-11, Vol.53, p.220-227</ispartof><rights>2013 Elsevier Ltd</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c339t-af60f0addbda4756e75c60d32c3b736ece109741eda0a29824a8a05c6eda182c3</citedby><cites>FETCH-LOGICAL-c339t-af60f0addbda4756e75c60d32c3b736ece109741eda0a29824a8a05c6eda182c3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.mineng.2013.03.005$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3549,27923,27924,45994</link.rule.ids></links><search><creatorcontrib>Dorfling, C.</creatorcontrib><creatorcontrib>Akdogan, G.</creatorcontrib><creatorcontrib>Bradshaw, S.M.</creatorcontrib><creatorcontrib>Eksteen, J.J.</creatorcontrib><title>Modelling of an autoclave used for high pressure sulphuric acid/oxygen leaching of first stage leach residue. Part 1: Model development</title><title>Minerals engineering</title><description>•Discussion of different leaching reactor modelling approaches.•Overview of base metal refinery pressure leaching process and leaching chemistry.•Steady state and dynamic model developed to predict pressure leaching performance.
Pressure leaching of the first stage leach residue in Base Metal Refinery (BMR) circuits aims to achieve high base metal dissolution with minimal precious metal leaching. Optimum autoclave operation is challenging because of the complex leaching chemistry, varying mineralogy of the feed material, and interaction between the different process variables. This research involved the modelling of the pressure leaching stages with flash recycle cooling at a typical BMR. The steady state solution employed the sequential modular approach in MATLAB, while the dynamic simulation involved the simultaneous solution of a set of differential equations, derived from mass and energy balances, in MATLAB. Part I of this communication presents a discussion of the Western Platinum Ltd. BMR process, an overview of relevant literature, and the strategies followed to develop both a steady state model and a dynamic model. Part II of this communication discusses the application of the models.</description><subject>Autoclaving</subject><subject>Base metal</subject><subject>Hydrometallurgy</subject><subject>Leaching</subject><subject>Mathematical models</subject><subject>Matlab</subject><subject>Modelling</subject><subject>Precious metal ores</subject><subject>Pressure leaching</subject><subject>Residues</subject><issn>0892-6875</issn><issn>1872-9444</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2013</creationdate><recordtype>article</recordtype><recordid>eNp9kE9L5EAQxRtRcNT9Bnvo414Sq_O3swdBRHeFET3snpua7kqmh0w6dieDfgK_tq3xLBQUPH7vFfUY-ykgFSCqy126twMNXZqByFOIA-URWwlZZ0lTFMUxW4FssqSSdXnKzkLYQSRq2azY24Mz1Pd26LhrOQ4c58npHg_E50CGt87zre22fPQUwuyJh7kft7O3mqO25tK9vHY08J5Qb79SWuvDxMOEHS06j15rZkr5E_qJi9_88yo3dKDejXsapgt20mIf6MfXPmf_727_3fxN1o9_7m-u14nO82ZKsK2gBTRmY7Coy4rqUldg8kznmzqvSJOApi4EGQTMGpkVKBEiEwUhI3XOfi25o3fPM4VJ7W3QsQEcyM1BCQlSZBXkVUSLBdXeheCpVaO3e_SvSoD66F3t1NK7-uhdQRwoo-1qsVF842DJq6AtDZqM9aQnZZz9PuAd05aQQw</recordid><startdate>20131101</startdate><enddate>20131101</enddate><creator>Dorfling, C.</creator><creator>Akdogan, G.</creator><creator>Bradshaw, S.M.</creator><creator>Eksteen, J.J.</creator><general>Elsevier Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope></search><sort><creationdate>20131101</creationdate><title>Modelling of an autoclave used for high pressure sulphuric acid/oxygen leaching of first stage leach residue. Part 1: Model development</title><author>Dorfling, C. ; Akdogan, G. ; Bradshaw, S.M. ; Eksteen, J.J.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c339t-af60f0addbda4756e75c60d32c3b736ece109741eda0a29824a8a05c6eda182c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2013</creationdate><topic>Autoclaving</topic><topic>Base metal</topic><topic>Hydrometallurgy</topic><topic>Leaching</topic><topic>Mathematical models</topic><topic>Matlab</topic><topic>Modelling</topic><topic>Precious metal ores</topic><topic>Pressure leaching</topic><topic>Residues</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Dorfling, C.</creatorcontrib><creatorcontrib>Akdogan, G.</creatorcontrib><creatorcontrib>Bradshaw, S.M.</creatorcontrib><creatorcontrib>Eksteen, J.J.</creatorcontrib><collection>CrossRef</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>Minerals engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Dorfling, C.</au><au>Akdogan, G.</au><au>Bradshaw, S.M.</au><au>Eksteen, J.J.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Modelling of an autoclave used for high pressure sulphuric acid/oxygen leaching of first stage leach residue. Part 1: Model development</atitle><jtitle>Minerals engineering</jtitle><date>2013-11-01</date><risdate>2013</risdate><volume>53</volume><spage>220</spage><epage>227</epage><pages>220-227</pages><issn>0892-6875</issn><eissn>1872-9444</eissn><abstract>•Discussion of different leaching reactor modelling approaches.•Overview of base metal refinery pressure leaching process and leaching chemistry.•Steady state and dynamic model developed to predict pressure leaching performance.
Pressure leaching of the first stage leach residue in Base Metal Refinery (BMR) circuits aims to achieve high base metal dissolution with minimal precious metal leaching. Optimum autoclave operation is challenging because of the complex leaching chemistry, varying mineralogy of the feed material, and interaction between the different process variables. This research involved the modelling of the pressure leaching stages with flash recycle cooling at a typical BMR. The steady state solution employed the sequential modular approach in MATLAB, while the dynamic simulation involved the simultaneous solution of a set of differential equations, derived from mass and energy balances, in MATLAB. Part I of this communication presents a discussion of the Western Platinum Ltd. BMR process, an overview of relevant literature, and the strategies followed to develop both a steady state model and a dynamic model. Part II of this communication discusses the application of the models.</abstract><pub>Elsevier Ltd</pub><doi>10.1016/j.mineng.2013.03.005</doi><tpages>8</tpages></addata></record> |
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subjects | Autoclaving Base metal Hydrometallurgy Leaching Mathematical models Matlab Modelling Precious metal ores Pressure leaching Residues |
title | Modelling of an autoclave used for high pressure sulphuric acid/oxygen leaching of first stage leach residue. Part 1: Model development |
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