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Tin recovery from an electroplating sludge
Tin electroplating from a fluoroborate electrolyte produces sludge containing approximately 50% tin. It can be extracted by leaching the sludge with concentrated hydrochloric acid at room temperature for one month or by boiling in 10% HCl solution for two hours. Electrowinning from H 2SnCl 6 solutio...
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Published in: | Resources, conservation and recycling conservation and recycling, 1991, Vol.6 (1), p.61-69 |
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creator | Stefanowicz, Tadeusz Golik, Tomasz Napieralska-Zagozda, Stefania Osińska, Małgorzata |
description | Tin electroplating from a fluoroborate electrolyte produces sludge containing approximately 50% tin. It can be extracted by leaching the sludge with concentrated hydrochloric acid at room temperature for one month or by boiling in 10% HCl solution for two hours. Electrowinning from H
2SnCl
6 solution with a steel cathode and graphite anodes permits recovery of tin with 93% efficiency at tin concentrations in the electrolyte exceeding 50 g/l and a current density of 5 A/dm
2. The cell is covered with a box with air passing through two washers filled with 15–20% NaOH solution. Chlorine gas evolved at the anodes is adsorbed in washers; sodium hypochlorite, of more than 10% strength in solution, is yielded as a byproduct, with 80% efficiency. |
doi_str_mv | 10.1016/0921-3449(91)90006-A |
format | article |
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2SnCl
6 solution with a steel cathode and graphite anodes permits recovery of tin with 93% efficiency at tin concentrations in the electrolyte exceeding 50 g/l and a current density of 5 A/dm
2. The cell is covered with a box with air passing through two washers filled with 15–20% NaOH solution. Chlorine gas evolved at the anodes is adsorbed in washers; sodium hypochlorite, of more than 10% strength in solution, is yielded as a byproduct, with 80% efficiency.</description><identifier>ISSN: 0921-3449</identifier><identifier>EISSN: 1879-0658</identifier><identifier>DOI: 10.1016/0921-3449(91)90006-A</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Applied sciences ; Exact sciences and technology ; Other industrial wastes. Sewage sludge ; Pollution ; Wastes</subject><ispartof>Resources, conservation and recycling, 1991, Vol.6 (1), p.61-69</ispartof><rights>1991</rights><rights>1992 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c493t-abbcfabb94b4003e9fc87c30794cbe1333a55fd7fd3523275433d0658af4fc5a3</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/092134499190006A$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3482,4024,27923,27924,27925,45993</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=5103376$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Stefanowicz, Tadeusz</creatorcontrib><creatorcontrib>Golik, Tomasz</creatorcontrib><creatorcontrib>Napieralska-Zagozda, Stefania</creatorcontrib><creatorcontrib>Osińska, Małgorzata</creatorcontrib><title>Tin recovery from an electroplating sludge</title><title>Resources, conservation and recycling</title><description>Tin electroplating from a fluoroborate electrolyte produces sludge containing approximately 50% tin. It can be extracted by leaching the sludge with concentrated hydrochloric acid at room temperature for one month or by boiling in 10% HCl solution for two hours. Electrowinning from H
2SnCl
6 solution with a steel cathode and graphite anodes permits recovery of tin with 93% efficiency at tin concentrations in the electrolyte exceeding 50 g/l and a current density of 5 A/dm
2. The cell is covered with a box with air passing through two washers filled with 15–20% NaOH solution. Chlorine gas evolved at the anodes is adsorbed in washers; sodium hypochlorite, of more than 10% strength in solution, is yielded as a byproduct, with 80% efficiency.</description><subject>Applied sciences</subject><subject>Exact sciences and technology</subject><subject>Other industrial wastes. Sewage sludge</subject><subject>Pollution</subject><subject>Wastes</subject><issn>0921-3449</issn><issn>1879-0658</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1991</creationdate><recordtype>article</recordtype><recordid>eNqFkU9LAzEQxYMoWKvfwMMeRFRYTXaSTXIRSvEfFLzUc8hmkxLZ7tZkW-i3N2tLj_Yyc_nNe8N7CF0T_EgwKZ-wLEgOlMo7Se4lxrjMJydoRASXOS6ZOEWjA3KOLmL8TgwICSP0MPdtFqzpNjZsMxe6ZabbzDbW9KFbNbr37SKLzbpe2Et05nQT7dV-j9HX68t8-p7PPt8-ppNZbqiEPtdVZVwaklY0uVjpjOAGMJfUVJYAgGbM1dzVwAooOKMA9fCldtQZpmGMbne6q9D9rG3s1dJHY5tGt7ZbR1VISQVPXsdBLgRN8kdBxgiIkh0FSUkIFBQnkO5AE7oYg3VqFfxSh60iWA2dqCFwNQSuJFF_nahJOrvZ6-todOOCbo2Ph1tGMAAvE_a8w2yKeeNtUNF42xpb-1RVr-rO_-_zC0X9nig</recordid><startdate>1991</startdate><enddate>1991</enddate><creator>Stefanowicz, Tadeusz</creator><creator>Golik, Tomasz</creator><creator>Napieralska-Zagozda, Stefania</creator><creator>Osińska, Małgorzata</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7T2</scope><scope>7TV</scope><scope>7U2</scope><scope>C1K</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope><scope>7TB</scope><scope>FR3</scope><scope>KR7</scope></search><sort><creationdate>1991</creationdate><title>Tin recovery from an electroplating sludge</title><author>Stefanowicz, Tadeusz ; Golik, Tomasz ; Napieralska-Zagozda, Stefania ; Osińska, Małgorzata</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c493t-abbcfabb94b4003e9fc87c30794cbe1333a55fd7fd3523275433d0658af4fc5a3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1991</creationdate><topic>Applied sciences</topic><topic>Exact sciences and technology</topic><topic>Other industrial wastes. Sewage sludge</topic><topic>Pollution</topic><topic>Wastes</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Stefanowicz, Tadeusz</creatorcontrib><creatorcontrib>Golik, Tomasz</creatorcontrib><creatorcontrib>Napieralska-Zagozda, Stefania</creatorcontrib><creatorcontrib>Osińska, Małgorzata</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Health and Safety Science Abstracts (Full archive)</collection><collection>Pollution Abstracts</collection><collection>Safety Science and Risk</collection><collection>Environmental Sciences and Pollution Management</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Resources, conservation and recycling</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Stefanowicz, Tadeusz</au><au>Golik, Tomasz</au><au>Napieralska-Zagozda, Stefania</au><au>Osińska, Małgorzata</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Tin recovery from an electroplating sludge</atitle><jtitle>Resources, conservation and recycling</jtitle><date>1991</date><risdate>1991</risdate><volume>6</volume><issue>1</issue><spage>61</spage><epage>69</epage><pages>61-69</pages><issn>0921-3449</issn><eissn>1879-0658</eissn><abstract>Tin electroplating from a fluoroborate electrolyte produces sludge containing approximately 50% tin. It can be extracted by leaching the sludge with concentrated hydrochloric acid at room temperature for one month or by boiling in 10% HCl solution for two hours. Electrowinning from H
2SnCl
6 solution with a steel cathode and graphite anodes permits recovery of tin with 93% efficiency at tin concentrations in the electrolyte exceeding 50 g/l and a current density of 5 A/dm
2. The cell is covered with a box with air passing through two washers filled with 15–20% NaOH solution. Chlorine gas evolved at the anodes is adsorbed in washers; sodium hypochlorite, of more than 10% strength in solution, is yielded as a byproduct, with 80% efficiency.</abstract><cop>Amsterdam</cop><cop>Oxford</cop><pub>Elsevier B.V</pub><doi>10.1016/0921-3449(91)90006-A</doi><tpages>9</tpages></addata></record> |
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source | Elsevier SD Backfile Environmental Sciences |
subjects | Applied sciences Exact sciences and technology Other industrial wastes. Sewage sludge Pollution Wastes |
title | Tin recovery from an electroplating sludge |
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