Recovery of iron and aluminum from acid mine drainage by selective precipitation
The large volumes of sludge produced through the active treatment of acid mine drainage (AMD) require further processing and final disposal. AMD sludge typically contains a heterogeneous mixture of iron, aluminum, magnesium, and calcium oxides/hydroxides that are of little to no practical value. How...
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Veröffentlicht in: | Environmental engineering science 2005-11, Vol.22 (6), p.745-755 |
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description | The large volumes of sludge produced through the active treatment of acid mine drainage (AMD) require further processing and final disposal. AMD sludge typically contains a heterogeneous mixture of iron, aluminum, magnesium, and calcium oxides/hydroxides that are of little to no practical value. However, purified iron and aluminum hydroxides have potential commercial value. Based on the solubility of the major dissolved metals, a two-step selective precipitation process was developed to recover high purity iron and aluminum as separate hydroxide products through the manipulation of current AMD treatment operations. The recommended pH for iron precipitation was pH 3.5-4.0 with precipitate purity > 93.4% and iron recovery > 98.6%. AMD water after iron removal was used as source water for aluminum recovery. Aluminum precipitated best at pH 6.0-7.0 with aluminum recovery > 97.2% and precipitate purity > 92.1%. |
doi_str_mv | 10.1089/ees.2005.22.745 |
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AMD sludge typically contains a heterogeneous mixture of iron, aluminum, magnesium, and calcium oxides/hydroxides that are of little to no practical value. However, purified iron and aluminum hydroxides have potential commercial value. Based on the solubility of the major dissolved metals, a two-step selective precipitation process was developed to recover high purity iron and aluminum as separate hydroxide products through the manipulation of current AMD treatment operations. The recommended pH for iron precipitation was pH 3.5-4.0 with precipitate purity > 93.4% and iron recovery > 98.6%. AMD water after iron removal was used as source water for aluminum recovery. Aluminum precipitated best at pH 6.0-7.0 with aluminum recovery > 97.2% and precipitate purity > 92.1%.</description><identifier>ISSN: 1092-8758</identifier><identifier>EISSN: 1557-9018</identifier><identifier>DOI: 10.1089/ees.2005.22.745</identifier><language>eng</language><publisher>Larchmont, NY: Liebert</publisher><subject>Applied sciences ; Exact sciences and technology ; Pollution</subject><ispartof>Environmental engineering science, 2005-11, Vol.22 (6), p.745-755</ispartof><rights>2006 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c461t-8fedab60fe62ebc68026a5bc76469d307d788c866fc999111bab9f99cdc750d03</citedby><cites>FETCH-LOGICAL-c461t-8fedab60fe62ebc68026a5bc76469d307d788c866fc999111bab9f99cdc750d03</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,3029,27901,27902</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=17255123$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>XINCHAO WEI</creatorcontrib><creatorcontrib>VIADERO, Roger C</creatorcontrib><creatorcontrib>BUZBY, Karen M</creatorcontrib><title>Recovery of iron and aluminum from acid mine drainage by selective precipitation</title><title>Environmental engineering science</title><description>The large volumes of sludge produced through the active treatment of acid mine drainage (AMD) require further processing and final disposal. AMD sludge typically contains a heterogeneous mixture of iron, aluminum, magnesium, and calcium oxides/hydroxides that are of little to no practical value. However, purified iron and aluminum hydroxides have potential commercial value. Based on the solubility of the major dissolved metals, a two-step selective precipitation process was developed to recover high purity iron and aluminum as separate hydroxide products through the manipulation of current AMD treatment operations. The recommended pH for iron precipitation was pH 3.5-4.0 with precipitate purity > 93.4% and iron recovery > 98.6%. AMD water after iron removal was used as source water for aluminum recovery. Aluminum precipitated best at pH 6.0-7.0 with aluminum recovery > 97.2% and precipitate purity > 92.1%.</description><subject>Applied sciences</subject><subject>Exact sciences and technology</subject><subject>Pollution</subject><issn>1092-8758</issn><issn>1557-9018</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2005</creationdate><recordtype>article</recordtype><recordid>eNqFkU1LxDAQhosouK6eveait3aTtPk6yuIXLCii55CmE4m0TU3ahf33dtkFj3uaGXje9zBPlt0SXBAs1QogFRRjVlBaiIqdZQvCmMgVJvJ83rGiuRRMXmZXKf1gTMqqJIvs_QNs2ELcoeCQj6FHpm-QaafO91OHXAwdMtY3aL4BNdH43nwDqncoQQt29FtAQwTrBz-a0Yf-Ortwpk1wc5zL7Ovp8XP9km_enl_XD5vcVpyMuXTQmJpjB5xCbbnElBtWW8ErrpoSi0ZIaSXnziqlCCG1qZVTyjZWMNzgcpndH3qHGH4nSKPufLLQtqaHMCVNFasEJdVpUGJVUiJPgkTMH6uoOg1WginJ942rA2hjSCmC00P0nYk7TbDeS9OzNL2XpinVs7Q5cXesNsma1kXTW5_-Y4IyRmhZ_gGBdZed</recordid><startdate>20051101</startdate><enddate>20051101</enddate><creator>XINCHAO WEI</creator><creator>VIADERO, Roger C</creator><creator>BUZBY, Karen M</creator><general>Liebert</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope><scope>7QH</scope><scope>7TV</scope><scope>7U6</scope><scope>7QF</scope><scope>8BQ</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>JG9</scope><scope>KR7</scope><scope>7TB</scope></search><sort><creationdate>20051101</creationdate><title>Recovery of iron and aluminum from acid mine drainage by selective precipitation</title><author>XINCHAO WEI ; VIADERO, Roger C ; BUZBY, Karen M</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c461t-8fedab60fe62ebc68026a5bc76469d307d788c866fc999111bab9f99cdc750d03</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2005</creationdate><topic>Applied sciences</topic><topic>Exact sciences and technology</topic><topic>Pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>XINCHAO WEI</creatorcontrib><creatorcontrib>VIADERO, Roger C</creatorcontrib><creatorcontrib>BUZBY, Karen M</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><collection>Aqualine</collection><collection>Pollution Abstracts</collection><collection>Sustainability Science Abstracts</collection><collection>Aluminium Industry Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Materials Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><jtitle>Environmental engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>XINCHAO WEI</au><au>VIADERO, Roger C</au><au>BUZBY, Karen M</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Recovery of iron and aluminum from acid mine drainage by selective precipitation</atitle><jtitle>Environmental engineering science</jtitle><date>2005-11-01</date><risdate>2005</risdate><volume>22</volume><issue>6</issue><spage>745</spage><epage>755</epage><pages>745-755</pages><issn>1092-8758</issn><eissn>1557-9018</eissn><abstract>The large volumes of sludge produced through the active treatment of acid mine drainage (AMD) require further processing and final disposal. AMD sludge typically contains a heterogeneous mixture of iron, aluminum, magnesium, and calcium oxides/hydroxides that are of little to no practical value. However, purified iron and aluminum hydroxides have potential commercial value. Based on the solubility of the major dissolved metals, a two-step selective precipitation process was developed to recover high purity iron and aluminum as separate hydroxide products through the manipulation of current AMD treatment operations. The recommended pH for iron precipitation was pH 3.5-4.0 with precipitate purity > 93.4% and iron recovery > 98.6%. AMD water after iron removal was used as source water for aluminum recovery. Aluminum precipitated best at pH 6.0-7.0 with aluminum recovery > 97.2% and precipitate purity > 92.1%.</abstract><cop>Larchmont, NY</cop><pub>Liebert</pub><doi>10.1089/ees.2005.22.745</doi><tpages>11</tpages></addata></record> |
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subjects | Applied sciences Exact sciences and technology Pollution |
title | Recovery of iron and aluminum from acid mine drainage by selective precipitation |
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