PRODUCTION OF NICKEL POWDER FROM BASIC NICKEL CARBONATE
1388664 Recovering nickel SHERRITT GORDON MINES Ltd 13 June 1972 [30 June 1971] 27690/72 Heading C7D Ni powder is produced from a nickel and cobalt bearing aqueous ammoniacal (NH 4 ) 2 CO 3 liquor containing Cu and at least one of Zn, Mg, Mn by the following process. Sufficient Co is removed from th...
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creator | DONALD ROBERT WEIR WILLIE SEIBT |
description | 1388664 Recovering nickel SHERRITT GORDON MINES Ltd 13 June 1972 [30 June 1971] 27690/72 Heading C7D Ni powder is produced from a nickel and cobalt bearing aqueous ammoniacal (NH 4 ) 2 CO 3 liquor containing Cu and at least one of Zn, Mg, Mn by the following process. Sufficient Co is removed from the liquor to give a molar ratio of Ni : Co of 100-200, whereupon the liquor is heated to drive off NH 3 and CO 2 , leaving a basic carbonates precipitate. This precipitate is repulped with H 2 O to form a slurry which is reduced to Ni powder in a pressure vessel, e.g. an autoclave, with H 2 , which continues until the molar ratio of Ni : Co in the end solution is between 0À5 and 1À0, and the pH is between 2 and 3. The pH can be corrected by additions of NH 3 and sulphate ions. The end solution can then be stripped of Co and the other impurities, but a portion is recycled and used to repulp the slurry prior to reduction. Before reduction, the slurry is adjusted to contain between 40 and 150 g/l of nickel and sulphate ions and NH 3 . The liquor is initially obtained from leading Ni ores, e.g. laterite. The reduction is preferably carried out in the range 80‹-350‹C and 100-500 p.s.i., and a number of reductions can be carried out successively, with periodic removal of Ni powder. Any S present may be oxidized to sulphates if desired prior to reduction. |
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Sufficient Co is removed from the liquor to give a molar ratio of Ni : Co of 100-200, whereupon the liquor is heated to drive off NH 3 and CO 2 , leaving a basic carbonates precipitate. This precipitate is repulped with H 2 O to form a slurry which is reduced to Ni powder in a pressure vessel, e.g. an autoclave, with H 2 , which continues until the molar ratio of Ni : Co in the end solution is between 0À5 and 1À0, and the pH is between 2 and 3. The pH can be corrected by additions of NH 3 and sulphate ions. The end solution can then be stripped of Co and the other impurities, but a portion is recycled and used to repulp the slurry prior to reduction. Before reduction, the slurry is adjusted to contain between 40 and 150 g/l of nickel and sulphate ions and NH 3 . The liquor is initially obtained from leading Ni ores, e.g. laterite. The reduction is preferably carried out in the range 80‹-350‹C and 100-500 p.s.i., and a number of reductions can be carried out successively, with periodic removal of Ni powder. Any S present may be oxidized to sulphates if desired prior to reduction.</description><language>eng</language><subject>CASTING ; CHEMISTRY ; COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSESC01D OR C01F ; FERROUS OR NON-FERROUS ALLOYS ; INORGANIC CHEMISTRY ; MAKING METALLIC POWDER ; MANUFACTURE OF ARTICLES FROM METALLIC POWDER ; METALLURGY ; PERFORMING OPERATIONS ; POWDER METALLURGY ; PRETREATMENT OF RAW MATERIALS ; PRODUCTION AND REFINING OF METALS ; TRANSPORTING ; TREATMENT OF ALLOYS OR NON-FERROUS METALS ; WORKING METALLIC POWDER</subject><creationdate>1973</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19731129&DB=EPODOC&CC=AU&NR=4255072A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,776,881,25542,76289</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19731129&DB=EPODOC&CC=AU&NR=4255072A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>DONALD ROBERT WEIR</creatorcontrib><creatorcontrib>WILLIE SEIBT</creatorcontrib><title>PRODUCTION OF NICKEL POWDER FROM BASIC NICKEL CARBONATE</title><description>1388664 Recovering nickel SHERRITT GORDON MINES Ltd 13 June 1972 [30 June 1971] 27690/72 Heading C7D Ni powder is produced from a nickel and cobalt bearing aqueous ammoniacal (NH 4 ) 2 CO 3 liquor containing Cu and at least one of Zn, Mg, Mn by the following process. Sufficient Co is removed from the liquor to give a molar ratio of Ni : Co of 100-200, whereupon the liquor is heated to drive off NH 3 and CO 2 , leaving a basic carbonates precipitate. This precipitate is repulped with H 2 O to form a slurry which is reduced to Ni powder in a pressure vessel, e.g. an autoclave, with H 2 , which continues until the molar ratio of Ni : Co in the end solution is between 0À5 and 1À0, and the pH is between 2 and 3. The pH can be corrected by additions of NH 3 and sulphate ions. The end solution can then be stripped of Co and the other impurities, but a portion is recycled and used to repulp the slurry prior to reduction. Before reduction, the slurry is adjusted to contain between 40 and 150 g/l of nickel and sulphate ions and NH 3 . The liquor is initially obtained from leading Ni ores, e.g. laterite. The reduction is preferably carried out in the range 80‹-350‹C and 100-500 p.s.i., and a number of reductions can be carried out successively, with periodic removal of Ni powder. Any S present may be oxidized to sulphates if desired prior to reduction.</description><subject>CASTING</subject><subject>CHEMISTRY</subject><subject>COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSESC01D OR C01F</subject><subject>FERROUS OR NON-FERROUS ALLOYS</subject><subject>INORGANIC CHEMISTRY</subject><subject>MAKING METALLIC POWDER</subject><subject>MANUFACTURE OF ARTICLES FROM METALLIC POWDER</subject><subject>METALLURGY</subject><subject>PERFORMING OPERATIONS</subject><subject>POWDER METALLURGY</subject><subject>PRETREATMENT OF RAW MATERIALS</subject><subject>PRODUCTION AND REFINING OF METALS</subject><subject>TRANSPORTING</subject><subject>TREATMENT OF ALLOYS OR NON-FERROUS METALS</subject><subject>WORKING METALLIC POWDER</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1973</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZDAPCPJ3CXUO8fT3U_B3U_DzdPZ29VEI8A93cQ1ScAvy91Vwcgz2dIZJODsGOfn7OYa48jCwpiXmFKfyQmluBnk31xBnD93Ugvz41OKCxOTUvNSSeMdQEyNTUwNzI0djwioAkOknNA</recordid><startdate>19731129</startdate><enddate>19731129</enddate><creator>DONALD ROBERT WEIR</creator><creator>WILLIE SEIBT</creator><scope>EVB</scope></search><sort><creationdate>19731129</creationdate><title>PRODUCTION OF NICKEL POWDER FROM BASIC NICKEL CARBONATE</title><author>DONALD ROBERT WEIR ; WILLIE SEIBT</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_AU4255072A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>1973</creationdate><topic>CASTING</topic><topic>CHEMISTRY</topic><topic>COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSESC01D OR C01F</topic><topic>FERROUS OR NON-FERROUS ALLOYS</topic><topic>INORGANIC CHEMISTRY</topic><topic>MAKING METALLIC POWDER</topic><topic>MANUFACTURE OF ARTICLES FROM METALLIC POWDER</topic><topic>METALLURGY</topic><topic>PERFORMING OPERATIONS</topic><topic>POWDER METALLURGY</topic><topic>PRETREATMENT OF RAW MATERIALS</topic><topic>PRODUCTION AND REFINING OF METALS</topic><topic>TRANSPORTING</topic><topic>TREATMENT OF ALLOYS OR NON-FERROUS METALS</topic><topic>WORKING METALLIC POWDER</topic><toplevel>online_resources</toplevel><creatorcontrib>DONALD ROBERT WEIR</creatorcontrib><creatorcontrib>WILLIE SEIBT</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>DONALD ROBERT WEIR</au><au>WILLIE SEIBT</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>PRODUCTION OF NICKEL POWDER FROM BASIC NICKEL CARBONATE</title><date>1973-11-29</date><risdate>1973</risdate><abstract>1388664 Recovering nickel SHERRITT GORDON MINES Ltd 13 June 1972 [30 June 1971] 27690/72 Heading C7D Ni powder is produced from a nickel and cobalt bearing aqueous ammoniacal (NH 4 ) 2 CO 3 liquor containing Cu and at least one of Zn, Mg, Mn by the following process. Sufficient Co is removed from the liquor to give a molar ratio of Ni : Co of 100-200, whereupon the liquor is heated to drive off NH 3 and CO 2 , leaving a basic carbonates precipitate. This precipitate is repulped with H 2 O to form a slurry which is reduced to Ni powder in a pressure vessel, e.g. an autoclave, with H 2 , which continues until the molar ratio of Ni : Co in the end solution is between 0À5 and 1À0, and the pH is between 2 and 3. The pH can be corrected by additions of NH 3 and sulphate ions. The end solution can then be stripped of Co and the other impurities, but a portion is recycled and used to repulp the slurry prior to reduction. Before reduction, the slurry is adjusted to contain between 40 and 150 g/l of nickel and sulphate ions and NH 3 . The liquor is initially obtained from leading Ni ores, e.g. laterite. The reduction is preferably carried out in the range 80‹-350‹C and 100-500 p.s.i., and a number of reductions can be carried out successively, with periodic removal of Ni powder. Any S present may be oxidized to sulphates if desired prior to reduction.</abstract><oa>free_for_read</oa></addata></record> |
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subjects | CASTING CHEMISTRY COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSESC01D OR C01F FERROUS OR NON-FERROUS ALLOYS INORGANIC CHEMISTRY MAKING METALLIC POWDER MANUFACTURE OF ARTICLES FROM METALLIC POWDER METALLURGY PERFORMING OPERATIONS POWDER METALLURGY PRETREATMENT OF RAW MATERIALS PRODUCTION AND REFINING OF METALS TRANSPORTING TREATMENT OF ALLOYS OR NON-FERROUS METALS WORKING METALLIC POWDER |
title | PRODUCTION OF NICKEL POWDER FROM BASIC NICKEL CARBONATE |
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