Method for producing nickel chloride solution with noble-metal leaching agents as raw materials
The invention discloses a method for producing a nickel chloride solution with noble-metal leaching agents as raw materials. The method includes: the noble-meta leaching agents are taken as the raw materials, and requirement on final pH value of deironing noble-metal leaching agents is 3.5-4.0; duri...
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creator | ZHANG GUOYONG CHEN SHIQIANG XING XIAOZHONG CHEN SHENGWEI REN WEI MING JIANWEI |
description | The invention discloses a method for producing a nickel chloride solution with noble-metal leaching agents as raw materials. The method includes: the noble-meta leaching agents are taken as the raw materials, and requirement on final pH value of deironing noble-metal leaching agents is 3.5-4.0; during oxidation process of the deironing agents, reaction potential is controlled to be 450-550mv, chlorine feeding time is controlled to be 4-6 hours, and the pH value of the chlorine-fed solution is adjusted to 3.5-4.0; during extraction of P507, the volume ratio of an extracting agent P507 to a thinning agent of sulfonated kerosene is 1:3, the saponification rate of sodium soap is 70%, the volume ratio of extracted organic phase to water phase is 3:1, the extraction stage is grade 7, the phase ratio:O:A=4:1, and the extraction form is counter-current extraction. The method has the advantages that nickel of the noble-metal leaching agents is recycled, the qualified nickel chloride solution is produced, requirements |
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The method includes: the noble-meta leaching agents are taken as the raw materials, and requirement on final pH value of deironing noble-metal leaching agents is 3.5-4.0; during oxidation process of the deironing agents, reaction potential is controlled to be 450-550mv, chlorine feeding time is controlled to be 4-6 hours, and the pH value of the chlorine-fed solution is adjusted to 3.5-4.0; during extraction of P507, the volume ratio of an extracting agent P507 to a thinning agent of sulfonated kerosene is 1:3, the saponification rate of sodium soap is 70%, the volume ratio of extracted organic phase to water phase is 3:1, the extraction stage is grade 7, the phase ratio:O:A=4:1, and the extraction form is counter-current extraction. The method has the advantages that nickel of the noble-metal leaching agents is recycled, the qualified nickel chloride solution is produced, requirements</description><language>chi ; eng</language><subject>CHEMISTRY ; FERROUS OR NON-FERROUS ALLOYS ; METALLURGY ; PRETREATMENT OF RAW MATERIALS ; PRODUCTION AND REFINING OF METALS ; TREATMENT OF ALLOYS OR NON-FERROUS METALS</subject><creationdate>2017</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=20170125&DB=EPODOC&CC=CN&NR=106350686A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,776,881,25543,76293</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20170125&DB=EPODOC&CC=CN&NR=106350686A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>ZHANG GUOYONG</creatorcontrib><creatorcontrib>CHEN SHIQIANG</creatorcontrib><creatorcontrib>XING XIAOZHONG</creatorcontrib><creatorcontrib>CHEN SHENGWEI</creatorcontrib><creatorcontrib>REN WEI</creatorcontrib><creatorcontrib>MING JIANWEI</creatorcontrib><title>Method for producing nickel chloride solution with noble-metal leaching agents as raw materials</title><description>The invention discloses a method for producing a nickel chloride solution with noble-metal leaching agents as raw materials. The method includes: the noble-meta leaching agents are taken as the raw materials, and requirement on final pH value of deironing noble-metal leaching agents is 3.5-4.0; during oxidation process of the deironing agents, reaction potential is controlled to be 450-550mv, chlorine feeding time is controlled to be 4-6 hours, and the pH value of the chlorine-fed solution is adjusted to 3.5-4.0; during extraction of P507, the volume ratio of an extracting agent P507 to a thinning agent of sulfonated kerosene is 1:3, the saponification rate of sodium soap is 70%, the volume ratio of extracted organic phase to water phase is 3:1, the extraction stage is grade 7, the phase ratio:O:A=4:1, and the extraction form is counter-current extraction. The method has the advantages that nickel of the noble-metal leaching agents is recycled, the qualified nickel chloride solution is produced, requirements</description><subject>CHEMISTRY</subject><subject>FERROUS OR NON-FERROUS ALLOYS</subject><subject>METALLURGY</subject><subject>PRETREATMENT OF RAW MATERIALS</subject><subject>PRODUCTION AND REFINING OF METALS</subject><subject>TREATMENT OF ALLOYS OR NON-FERROUS METALS</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2017</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqNy7EKwjAQgOEuDqK-w_kAhUoxuJaiuOjkXs7k2gSvuZJc6eur4AM4fcv_r4vuRurFQS8JpiRutiEOEIN9EYP1LCk4giw8a5AIS1APUZ5M5UiKDExo_XfBgaJmwAwJFxhRKQXkvC1W_Qfa_dwU-8v50V5LmqSjPKGlSNq190Nl6mNlTqap_2nenD09JQ</recordid><startdate>20170125</startdate><enddate>20170125</enddate><creator>ZHANG GUOYONG</creator><creator>CHEN SHIQIANG</creator><creator>XING XIAOZHONG</creator><creator>CHEN SHENGWEI</creator><creator>REN WEI</creator><creator>MING JIANWEI</creator><scope>EVB</scope></search><sort><creationdate>20170125</creationdate><title>Method for producing nickel chloride solution with noble-metal leaching agents as raw materials</title><author>ZHANG GUOYONG ; CHEN SHIQIANG ; XING XIAOZHONG ; CHEN SHENGWEI ; REN WEI ; MING JIANWEI</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_CN106350686A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>chi ; eng</language><creationdate>2017</creationdate><topic>CHEMISTRY</topic><topic>FERROUS OR NON-FERROUS ALLOYS</topic><topic>METALLURGY</topic><topic>PRETREATMENT OF RAW MATERIALS</topic><topic>PRODUCTION AND REFINING OF METALS</topic><topic>TREATMENT OF ALLOYS OR NON-FERROUS METALS</topic><toplevel>online_resources</toplevel><creatorcontrib>ZHANG GUOYONG</creatorcontrib><creatorcontrib>CHEN SHIQIANG</creatorcontrib><creatorcontrib>XING XIAOZHONG</creatorcontrib><creatorcontrib>CHEN SHENGWEI</creatorcontrib><creatorcontrib>REN WEI</creatorcontrib><creatorcontrib>MING JIANWEI</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>ZHANG GUOYONG</au><au>CHEN SHIQIANG</au><au>XING XIAOZHONG</au><au>CHEN SHENGWEI</au><au>REN WEI</au><au>MING JIANWEI</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Method for producing nickel chloride solution with noble-metal leaching agents as raw materials</title><date>2017-01-25</date><risdate>2017</risdate><abstract>The invention discloses a method for producing a nickel chloride solution with noble-metal leaching agents as raw materials. The method includes: the noble-meta leaching agents are taken as the raw materials, and requirement on final pH value of deironing noble-metal leaching agents is 3.5-4.0; during oxidation process of the deironing agents, reaction potential is controlled to be 450-550mv, chlorine feeding time is controlled to be 4-6 hours, and the pH value of the chlorine-fed solution is adjusted to 3.5-4.0; during extraction of P507, the volume ratio of an extracting agent P507 to a thinning agent of sulfonated kerosene is 1:3, the saponification rate of sodium soap is 70%, the volume ratio of extracted organic phase to water phase is 3:1, the extraction stage is grade 7, the phase ratio:O:A=4:1, and the extraction form is counter-current extraction. The method has the advantages that nickel of the noble-metal leaching agents is recycled, the qualified nickel chloride solution is produced, requirements</abstract><oa>free_for_read</oa></addata></record> |
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subjects | CHEMISTRY FERROUS OR NON-FERROUS ALLOYS METALLURGY PRETREATMENT OF RAW MATERIALS PRODUCTION AND REFINING OF METALS TREATMENT OF ALLOYS OR NON-FERROUS METALS |
title | Method for producing nickel chloride solution with noble-metal leaching agents as raw materials |
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