Processing oxidic waste of lead-acid batteries in order to recover lead
The main process parameters have been investigated with a relatively new method for lead recovery from oxidic paste. The method consisting in leaching with NaOH and is also useful for processing other secondary resources (volatile dusts resulted from metallurgical extraction of lead from primary res...
Gespeichert in:
Veröffentlicht in: | Asia-Pacific journal of chemical engineering 2015-01, Vol.10 (1), p.125-132 |
---|---|
Hauptverfasser: | , , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 132 |
---|---|
container_issue | 1 |
container_start_page | 125 |
container_title | Asia-Pacific journal of chemical engineering |
container_volume | 10 |
creator | Buzatu, Traian Petrescu, Mircea Ionut Ghica, Valeriu Gabriel Buzatu, Mihai Iacob, Gheorghe |
description | The main process parameters have been investigated with a relatively new method for lead recovery from oxidic paste. The method consisting in leaching with NaOH and is also useful for processing other secondary resources (volatile dusts resulted from metallurgical extraction of lead from primary resources). The chemical analysis and X‐ray diffraction have attested that the oxidic paste resulted from the dismantling of spent lead‐acid batteries has a content of 70–73% Pb, mainly as anglesite (around 38% PbSO4) and lanarkite (about 36% Pb2SO5). Experiments have been carried out through leaching with NaOH of the industrial paste out of spent car batteries as well as for the pure substances. The experiments were conducted at temperatures of 40, 60 and 80 °C, at various solid/liquid ratios (S : L = 1 : 10; 1 : 30 and 1 : 50) and different molarities for the NaOH solutions (2, 4, 6 and 8 M). The reaction time was 1 h for the leaching of the pure substances and 2 h for the leaching of the industrial pastes. An extraction efficiency of 92% Pb was obtained with a leaching solution of 6 M NaOH, at 60 °C, for 2 h and S/L ratios of 1 : 20–1 : 30. The efficiency may be increased up to 97% Pb only when the leaching process is carried out in two steps. © 2014 Curtin University of Technology and John Wiley & Sons, Ltd. |
doi_str_mv | 10.1002/apj.1854 |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_1669844926</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>1669844926</sourcerecordid><originalsourceid>FETCH-LOGICAL-c3734-82fd840923f22064c5eb7357553eee514033368d95a3d1a9bf9d2cd422161d1c3</originalsourceid><addsrcrecordid>eNp10M1OAjEUhuHGaCKiiZfQpZvR_s_MkhAFDeLEaFw2pT1jigPFdhC4eyEYjAtX51s8OYsXoUtKrikh7MYspte0kOIIdWjJWcao4MeHzeUpOktpSogUTIkOGlQxWEjJz99xWHvnLV6Z1AIONW7AuMxY7_DEtC1EDwn7OQ7RQcRtwBFs-NrOnTtHJ7VpElz83C56vbt96Q-z0dPgvt8bZZbnXGQFq10hSMl4zRhRwkqY5FzmUnIAkFQQzrkqXCkNd9SUk7p0zDrBGFXUUcu76Gr_dxHD5xJSq2c-WWgaM4ewTJoqVRZClEz9UhtDShFqvYh-ZuJGU6J3rfS2ld612tJsT1e-gc2_Tveqh7_eb1OtD97ED61ynkv9Nh5o3h9Xw0o-6mf-DcNeeCs</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1669844926</pqid></control><display><type>article</type><title>Processing oxidic waste of lead-acid batteries in order to recover lead</title><source>Wiley Online Library All Journals</source><creator>Buzatu, Traian ; Petrescu, Mircea Ionut ; Ghica, Valeriu Gabriel ; Buzatu, Mihai ; Iacob, Gheorghe</creator><creatorcontrib>Buzatu, Traian ; Petrescu, Mircea Ionut ; Ghica, Valeriu Gabriel ; Buzatu, Mihai ; Iacob, Gheorghe</creatorcontrib><description>The main process parameters have been investigated with a relatively new method for lead recovery from oxidic paste. The method consisting in leaching with NaOH and is also useful for processing other secondary resources (volatile dusts resulted from metallurgical extraction of lead from primary resources). The chemical analysis and X‐ray diffraction have attested that the oxidic paste resulted from the dismantling of spent lead‐acid batteries has a content of 70–73% Pb, mainly as anglesite (around 38% PbSO4) and lanarkite (about 36% Pb2SO5). Experiments have been carried out through leaching with NaOH of the industrial paste out of spent car batteries as well as for the pure substances. The experiments were conducted at temperatures of 40, 60 and 80 °C, at various solid/liquid ratios (S : L = 1 : 10; 1 : 30 and 1 : 50) and different molarities for the NaOH solutions (2, 4, 6 and 8 M). The reaction time was 1 h for the leaching of the pure substances and 2 h for the leaching of the industrial pastes. An extraction efficiency of 92% Pb was obtained with a leaching solution of 6 M NaOH, at 60 °C, for 2 h and S/L ratios of 1 : 20–1 : 30. The efficiency may be increased up to 97% Pb only when the leaching process is carried out in two steps. © 2014 Curtin University of Technology and John Wiley & Sons, Ltd.</description><identifier>ISSN: 1932-2135</identifier><identifier>EISSN: 1932-2143</identifier><identifier>DOI: 10.1002/apj.1854</identifier><language>eng</language><publisher>Blackwell Publishing Ltd</publisher><subject>aqueous solutions ; Concentration (composition) ; Diffraction ; dissolution ; Extraction ; Leaching ; Lead (metal) ; Lead acid batteries ; Pastes ; Process parameters ; Reaction time ; recycling ; waste</subject><ispartof>Asia-Pacific journal of chemical engineering, 2015-01, Vol.10 (1), p.125-132</ispartof><rights>2014 Curtin University of Technology and John Wiley & Sons, Ltd.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c3734-82fd840923f22064c5eb7357553eee514033368d95a3d1a9bf9d2cd422161d1c3</citedby><cites>FETCH-LOGICAL-c3734-82fd840923f22064c5eb7357553eee514033368d95a3d1a9bf9d2cd422161d1c3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fapj.1854$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fapj.1854$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,780,784,1417,27924,27925,45574,45575</link.rule.ids></links><search><creatorcontrib>Buzatu, Traian</creatorcontrib><creatorcontrib>Petrescu, Mircea Ionut</creatorcontrib><creatorcontrib>Ghica, Valeriu Gabriel</creatorcontrib><creatorcontrib>Buzatu, Mihai</creatorcontrib><creatorcontrib>Iacob, Gheorghe</creatorcontrib><title>Processing oxidic waste of lead-acid batteries in order to recover lead</title><title>Asia-Pacific journal of chemical engineering</title><addtitle>Asia-Pac. J. Chem. Eng</addtitle><description>The main process parameters have been investigated with a relatively new method for lead recovery from oxidic paste. The method consisting in leaching with NaOH and is also useful for processing other secondary resources (volatile dusts resulted from metallurgical extraction of lead from primary resources). The chemical analysis and X‐ray diffraction have attested that the oxidic paste resulted from the dismantling of spent lead‐acid batteries has a content of 70–73% Pb, mainly as anglesite (around 38% PbSO4) and lanarkite (about 36% Pb2SO5). Experiments have been carried out through leaching with NaOH of the industrial paste out of spent car batteries as well as for the pure substances. The experiments were conducted at temperatures of 40, 60 and 80 °C, at various solid/liquid ratios (S : L = 1 : 10; 1 : 30 and 1 : 50) and different molarities for the NaOH solutions (2, 4, 6 and 8 M). The reaction time was 1 h for the leaching of the pure substances and 2 h for the leaching of the industrial pastes. An extraction efficiency of 92% Pb was obtained with a leaching solution of 6 M NaOH, at 60 °C, for 2 h and S/L ratios of 1 : 20–1 : 30. The efficiency may be increased up to 97% Pb only when the leaching process is carried out in two steps. © 2014 Curtin University of Technology and John Wiley & Sons, Ltd.</description><subject>aqueous solutions</subject><subject>Concentration (composition)</subject><subject>Diffraction</subject><subject>dissolution</subject><subject>Extraction</subject><subject>Leaching</subject><subject>Lead (metal)</subject><subject>Lead acid batteries</subject><subject>Pastes</subject><subject>Process parameters</subject><subject>Reaction time</subject><subject>recycling</subject><subject>waste</subject><issn>1932-2135</issn><issn>1932-2143</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2015</creationdate><recordtype>article</recordtype><recordid>eNp10M1OAjEUhuHGaCKiiZfQpZvR_s_MkhAFDeLEaFw2pT1jigPFdhC4eyEYjAtX51s8OYsXoUtKrikh7MYspte0kOIIdWjJWcao4MeHzeUpOktpSogUTIkOGlQxWEjJz99xWHvnLV6Z1AIONW7AuMxY7_DEtC1EDwn7OQ7RQcRtwBFs-NrOnTtHJ7VpElz83C56vbt96Q-z0dPgvt8bZZbnXGQFq10hSMl4zRhRwkqY5FzmUnIAkFQQzrkqXCkNd9SUk7p0zDrBGFXUUcu76Gr_dxHD5xJSq2c-WWgaM4ewTJoqVRZClEz9UhtDShFqvYh-ZuJGU6J3rfS2ld612tJsT1e-gc2_Tveqh7_eb1OtD97ED61ynkv9Nh5o3h9Xw0o-6mf-DcNeeCs</recordid><startdate>201501</startdate><enddate>201501</enddate><creator>Buzatu, Traian</creator><creator>Petrescu, Mircea Ionut</creator><creator>Ghica, Valeriu Gabriel</creator><creator>Buzatu, Mihai</creator><creator>Iacob, Gheorghe</creator><general>Blackwell Publishing Ltd</general><scope>BSCLL</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SP</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>FR3</scope><scope>JG9</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>201501</creationdate><title>Processing oxidic waste of lead-acid batteries in order to recover lead</title><author>Buzatu, Traian ; Petrescu, Mircea Ionut ; Ghica, Valeriu Gabriel ; Buzatu, Mihai ; Iacob, Gheorghe</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3734-82fd840923f22064c5eb7357553eee514033368d95a3d1a9bf9d2cd422161d1c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2015</creationdate><topic>aqueous solutions</topic><topic>Concentration (composition)</topic><topic>Diffraction</topic><topic>dissolution</topic><topic>Extraction</topic><topic>Leaching</topic><topic>Lead (metal)</topic><topic>Lead acid batteries</topic><topic>Pastes</topic><topic>Process parameters</topic><topic>Reaction time</topic><topic>recycling</topic><topic>waste</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Buzatu, Traian</creatorcontrib><creatorcontrib>Petrescu, Mircea Ionut</creatorcontrib><creatorcontrib>Ghica, Valeriu Gabriel</creatorcontrib><creatorcontrib>Buzatu, Mihai</creatorcontrib><creatorcontrib>Iacob, Gheorghe</creatorcontrib><collection>Istex</collection><collection>CrossRef</collection><collection>Electronics & Communications Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Materials Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Asia-Pacific journal of chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Buzatu, Traian</au><au>Petrescu, Mircea Ionut</au><au>Ghica, Valeriu Gabriel</au><au>Buzatu, Mihai</au><au>Iacob, Gheorghe</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Processing oxidic waste of lead-acid batteries in order to recover lead</atitle><jtitle>Asia-Pacific journal of chemical engineering</jtitle><addtitle>Asia-Pac. J. Chem. Eng</addtitle><date>2015-01</date><risdate>2015</risdate><volume>10</volume><issue>1</issue><spage>125</spage><epage>132</epage><pages>125-132</pages><issn>1932-2135</issn><eissn>1932-2143</eissn><abstract>The main process parameters have been investigated with a relatively new method for lead recovery from oxidic paste. The method consisting in leaching with NaOH and is also useful for processing other secondary resources (volatile dusts resulted from metallurgical extraction of lead from primary resources). The chemical analysis and X‐ray diffraction have attested that the oxidic paste resulted from the dismantling of spent lead‐acid batteries has a content of 70–73% Pb, mainly as anglesite (around 38% PbSO4) and lanarkite (about 36% Pb2SO5). Experiments have been carried out through leaching with NaOH of the industrial paste out of spent car batteries as well as for the pure substances. The experiments were conducted at temperatures of 40, 60 and 80 °C, at various solid/liquid ratios (S : L = 1 : 10; 1 : 30 and 1 : 50) and different molarities for the NaOH solutions (2, 4, 6 and 8 M). The reaction time was 1 h for the leaching of the pure substances and 2 h for the leaching of the industrial pastes. An extraction efficiency of 92% Pb was obtained with a leaching solution of 6 M NaOH, at 60 °C, for 2 h and S/L ratios of 1 : 20–1 : 30. The efficiency may be increased up to 97% Pb only when the leaching process is carried out in two steps. © 2014 Curtin University of Technology and John Wiley & Sons, Ltd.</abstract><pub>Blackwell Publishing Ltd</pub><doi>10.1002/apj.1854</doi><tpages>8</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 1932-2135 |
ispartof | Asia-Pacific journal of chemical engineering, 2015-01, Vol.10 (1), p.125-132 |
issn | 1932-2135 1932-2143 |
language | eng |
recordid | cdi_proquest_miscellaneous_1669844926 |
source | Wiley Online Library All Journals |
subjects | aqueous solutions Concentration (composition) Diffraction dissolution Extraction Leaching Lead (metal) Lead acid batteries Pastes Process parameters Reaction time recycling waste |
title | Processing oxidic waste of lead-acid batteries in order to recover lead |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-25T09%3A32%3A30IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Processing%20oxidic%20waste%20of%20lead-acid%20batteries%20in%20order%20to%20recover%20lead&rft.jtitle=Asia-Pacific%20journal%20of%20chemical%20engineering&rft.au=Buzatu,%20Traian&rft.date=2015-01&rft.volume=10&rft.issue=1&rft.spage=125&rft.epage=132&rft.pages=125-132&rft.issn=1932-2135&rft.eissn=1932-2143&rft_id=info:doi/10.1002/apj.1854&rft_dat=%3Cproquest_cross%3E1669844926%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=1669844926&rft_id=info:pmid/&rfr_iscdi=true |