Factors affecting the leachability of Ni/Co/Cu slags at high temperature
An oxidative pressure acid leaching process was investigated for the extraction of Ni/Co/Cu/Zn metal values from base metal smelter slags. The process is applicable to smelting furnace dump slags, as well as to mid-stream converter slags. In addition to the economical advantages, extracting the base...
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description | An oxidative pressure acid leaching process was investigated for the extraction of Ni/Co/Cu/Zn metal values from base metal smelter slags. The process is applicable to smelting furnace dump slags, as well as to mid-stream converter slags. In addition to the economical advantages, extracting the base metal values from the dump slags produces an environmentally benign residue. To produce high level of extraction for the metal values, it is necessary to have the slag in crystalline structure. This, in turn, requires cooling the molten smelter slags sufficiently slowly during solidification. It was shown that if the same slags are quenched in water thereby producing an amorphous structure, the resulting metal extractions are substantially lower. The role of oxygen in the leaching reactions was also tested. The presence of oxygen is necessary for successful leaching of the metal values. After fine grinding, the slags were subjected to pressure acid leaching at 250 °C with an oxygen overpressure of 520 kPa. Sulfuric acid at a typical 0.3 acid to slag ratio was employed. Extractions higher than 90% of each of the nickel, cobalt, copper and zinc were achieved. Operating at 250 °C ensures that the concentration of Fe and Al impurity metals in leached solution remains very low. It was finally found that for high concentrations of divalent metals (Ni
+
Co
+
Cu
+
Mg) in the slag, a much higher quantity of sulfuric acid than the stoichiometric value is required. The latter is due to the drop of hydrogen ion concentration due to bisulphate formation. |
doi_str_mv | 10.1016/j.hydromet.2006.07.007 |
format | Article |
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+
Co
+
Cu
+
Mg) in the slag, a much higher quantity of sulfuric acid than the stoichiometric value is required. The latter is due to the drop of hydrogen ion concentration due to bisulphate formation.</description><identifier>ISSN: 0304-386X</identifier><identifier>EISSN: 1879-1158</identifier><identifier>DOI: 10.1016/j.hydromet.2006.07.007</identifier><identifier>CODEN: HYDRDA</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Applied sciences ; Cobalt ; Converter slag ; Copper ; Crystallinity ; Dump slag ; Exact sciences and technology ; Fayalite ; Metals. Metallurgy ; Nickel ; Oxidative pressure leaching ; Production of metals ; Sulfuric acid ; Zinc</subject><ispartof>Hydrometallurgy, 2007, Vol.85 (1), p.42-52</ispartof><rights>2006 Elsevier B.V.</rights><rights>2007 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c373t-4cd4bbc7a00c27ef16be217747550a6250066650534a64f589f476706d3a75ed3</citedby><cites>FETCH-LOGICAL-c373t-4cd4bbc7a00c27ef16be217747550a6250066650534a64f589f476706d3a75ed3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.hydromet.2006.07.007$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,4024,27923,27924,27925,45995</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=18446939$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Baghalha, M.</creatorcontrib><creatorcontrib>Papangelakis, V.G.</creatorcontrib><creatorcontrib>Curlook, W.</creatorcontrib><title>Factors affecting the leachability of Ni/Co/Cu slags at high temperature</title><title>Hydrometallurgy</title><description>An oxidative pressure acid leaching process was investigated for the extraction of Ni/Co/Cu/Zn metal values from base metal smelter slags. The process is applicable to smelting furnace dump slags, as well as to mid-stream converter slags. In addition to the economical advantages, extracting the base metal values from the dump slags produces an environmentally benign residue. To produce high level of extraction for the metal values, it is necessary to have the slag in crystalline structure. This, in turn, requires cooling the molten smelter slags sufficiently slowly during solidification. It was shown that if the same slags are quenched in water thereby producing an amorphous structure, the resulting metal extractions are substantially lower. The role of oxygen in the leaching reactions was also tested. The presence of oxygen is necessary for successful leaching of the metal values. After fine grinding, the slags were subjected to pressure acid leaching at 250 °C with an oxygen overpressure of 520 kPa. Sulfuric acid at a typical 0.3 acid to slag ratio was employed. Extractions higher than 90% of each of the nickel, cobalt, copper and zinc were achieved. Operating at 250 °C ensures that the concentration of Fe and Al impurity metals in leached solution remains very low. It was finally found that for high concentrations of divalent metals (Ni
+
Co
+
Cu
+
Mg) in the slag, a much higher quantity of sulfuric acid than the stoichiometric value is required. The latter is due to the drop of hydrogen ion concentration due to bisulphate formation.</description><subject>Applied sciences</subject><subject>Cobalt</subject><subject>Converter slag</subject><subject>Copper</subject><subject>Crystallinity</subject><subject>Dump slag</subject><subject>Exact sciences and technology</subject><subject>Fayalite</subject><subject>Metals. Metallurgy</subject><subject>Nickel</subject><subject>Oxidative pressure leaching</subject><subject>Production of metals</subject><subject>Sulfuric acid</subject><subject>Zinc</subject><issn>0304-386X</issn><issn>1879-1158</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><recordid>eNqFkD1PwzAQhi0EEqXwF1AW2JKeY8dONlDFl1TBAhKb5TjnxlXaFNtF6r_HqCBGplue9967h5BLCgUFKmarot93flxjLEoAUYAsAOQRmdBaNjmlVX1MJsCA56wW76fkLIQVJJBJOiGP99rE0YdMW4smus0yiz1mA2rT69YNLu6z0WbPbjYfZ_NdFga9THDMerfss4jrLXoddx7PyYnVQ8CLnzklb_d3r_PHfPHy8DS_XeSGSRZzbjretkZqAFNKtFS0WFIpuawq0KKs0mFCVFAxrgW3Vd1YLoUE0TEtK-zYlFwf9m79-LHDENXaBYPDoDc47oIqGyZLyUUCxQE0fgzBo1Vb79ba7xUF9S1OrdSvOPUtToFUSVwKXv006GD0YL3eGBf-0jXnomFN4m4OHKZ3Px16FYzDjcHO-aRSdaP7r-oLlsGGaQ</recordid><startdate>2007</startdate><enddate>2007</enddate><creator>Baghalha, M.</creator><creator>Papangelakis, V.G.</creator><creator>Curlook, W.</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope></search><sort><creationdate>2007</creationdate><title>Factors affecting the leachability of Ni/Co/Cu slags at high temperature</title><author>Baghalha, M. ; Papangelakis, V.G. ; Curlook, W.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c373t-4cd4bbc7a00c27ef16be217747550a6250066650534a64f589f476706d3a75ed3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2007</creationdate><topic>Applied sciences</topic><topic>Cobalt</topic><topic>Converter slag</topic><topic>Copper</topic><topic>Crystallinity</topic><topic>Dump slag</topic><topic>Exact sciences and technology</topic><topic>Fayalite</topic><topic>Metals. Metallurgy</topic><topic>Nickel</topic><topic>Oxidative pressure leaching</topic><topic>Production of metals</topic><topic>Sulfuric acid</topic><topic>Zinc</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Baghalha, M.</creatorcontrib><creatorcontrib>Papangelakis, V.G.</creatorcontrib><creatorcontrib>Curlook, W.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aluminium Industry Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>Hydrometallurgy</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Baghalha, M.</au><au>Papangelakis, V.G.</au><au>Curlook, W.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Factors affecting the leachability of Ni/Co/Cu slags at high temperature</atitle><jtitle>Hydrometallurgy</jtitle><date>2007</date><risdate>2007</risdate><volume>85</volume><issue>1</issue><spage>42</spage><epage>52</epage><pages>42-52</pages><issn>0304-386X</issn><eissn>1879-1158</eissn><coden>HYDRDA</coden><abstract>An oxidative pressure acid leaching process was investigated for the extraction of Ni/Co/Cu/Zn metal values from base metal smelter slags. The process is applicable to smelting furnace dump slags, as well as to mid-stream converter slags. In addition to the economical advantages, extracting the base metal values from the dump slags produces an environmentally benign residue. To produce high level of extraction for the metal values, it is necessary to have the slag in crystalline structure. This, in turn, requires cooling the molten smelter slags sufficiently slowly during solidification. It was shown that if the same slags are quenched in water thereby producing an amorphous structure, the resulting metal extractions are substantially lower. The role of oxygen in the leaching reactions was also tested. The presence of oxygen is necessary for successful leaching of the metal values. After fine grinding, the slags were subjected to pressure acid leaching at 250 °C with an oxygen overpressure of 520 kPa. Sulfuric acid at a typical 0.3 acid to slag ratio was employed. Extractions higher than 90% of each of the nickel, cobalt, copper and zinc were achieved. Operating at 250 °C ensures that the concentration of Fe and Al impurity metals in leached solution remains very low. It was finally found that for high concentrations of divalent metals (Ni
+
Co
+
Cu
+
Mg) in the slag, a much higher quantity of sulfuric acid than the stoichiometric value is required. The latter is due to the drop of hydrogen ion concentration due to bisulphate formation.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.hydromet.2006.07.007</doi><tpages>11</tpages></addata></record> |
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subjects | Applied sciences Cobalt Converter slag Copper Crystallinity Dump slag Exact sciences and technology Fayalite Metals. Metallurgy Nickel Oxidative pressure leaching Production of metals Sulfuric acid Zinc |
title | Factors affecting the leachability of Ni/Co/Cu slags at high temperature |
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