APPLICATION OF CYANEX272 TO Co/Ni SEPARATION
HU Fucheng
Abstract
HU Fucheng
Abstract
In order to completely separate cobalt from nickel,the process of cobalt extraction with Cyanex272 in solution derived from cobalt residue acid dissolving is investigated,and a commercial application is also described The cobalt extraction recovery is 98% with 3 min mixing time,and Co 2+ in solution reduces to 0 01g/L from 4 5g/L;the ratio of 〔Co〕/〔Ni〕 in the pregnant organic phase is up to 529 20 after 3 stages scrubbing The cobalt extractive recovery is over 99% by 3 stages extraction and scrubbing,the β Co/Ni is up to 2 50×10 5 The Co 2+ content in organic phase is below 0 020g/L with 2 stages stripping The C1 - content in refresh organic phase is eliminated completely by 2 stages scrubbing with deionized water,without accumulation in nickel electrolyte The cobalt extraction is not affected by calcium and magnesium existing in the solution In the commercial application,the A grade cobalt oxide is produced,and nickel sulfate solution meets the needs of A grade cathode nickel production by electrolysis
OpenAlex reports 3 citations for this work. Citation counts describe recorded attention and do not establish research quality.
A contribution statement is not available in the OpenAlex record.
Method details are not available in the OpenAlex metadata.
Findings are not separately available in the OpenAlex metadata.
Limitations are not available in the OpenAlex metadata.
Application details are not available in the OpenAlex metadata.
In order to completely separate cobalt from nickel,the process of cobalt extraction with Cyanex272 in solution derived from cobalt residue acid dissolving is investigated,and a commercial application is also described The cobalt extraction recovery is 98% with 3 min mixing time,and Co 2+ in solution reduces to 0 01g/L from 4 5g/L;the ratio of 〔Co〕/〔Ni〕 in the pregnant organic phase is up to 529 20 after 3 stages scrubbing The cobalt extractive recovery is over 99% by 3 stages extraction and scrubbing,the β Co/Ni is up to 2 50×10 5 The Co 2+ content in organic phase is below 0 020g/L with 2 stages stripping The C1 - content in refresh organic phase is eliminated completely by 2 stages scrubbing with deionized water,without accumulation in nickel electrolyte The cobalt extraction is not affected by calcium and magnesium existing in the solution In the commercial application,the A grade cobalt oxide is produced,and nickel sulfate solution meets the needs of A grade cathode nickel production by electrolysis
Key concepts: Cobalt, Data scrubbing, Nickel, Cobalt extraction techniques, Electrolysis, Stripping (fiber), Extraction (chemistry), Magnesium