GB853323A - Process for the separation of nickel from solutions containing cobalt and nickel salts - Google Patents

Process for the separation of nickel from solutions containing cobalt and nickel salts

Info

Publication number
GB853323A
GB853323A GB1343558A GB1343558A GB853323A GB 853323 A GB853323 A GB 853323A GB 1343558 A GB1343558 A GB 1343558A GB 1343558 A GB1343558 A GB 1343558A GB 853323 A GB853323 A GB 853323A
Authority
GB
United Kingdom
Prior art keywords
nickel
copper
sulphide
arsenic
cobalt
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB1343558A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Societe dElectro Chimie dElectro Metallurgie et des Acieries Electriques Dugine SA SECEMAU
Original Assignee
Societe dElectro Chimie dElectro Metallurgie et des Acieries Electriques Dugine SA SECEMAU
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Societe dElectro Chimie dElectro Metallurgie et des Acieries Electriques Dugine SA SECEMAU filed Critical Societe dElectro Chimie dElectro Metallurgie et des Acieries Electriques Dugine SA SECEMAU
Publication of GB853323A publication Critical patent/GB853323A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/04Obtaining nickel or cobalt by wet processes
    • C22B23/0476Separation of nickel from cobalt
    • C22B23/0484Separation of nickel from cobalt in acidic type solutions
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/04Obtaining nickel or cobalt by wet processes
    • C22B23/0453Treatment or purification of solutions, e.g. obtained by leaching
    • C22B23/0461Treatment or purification of solutions, e.g. obtained by leaching by chemical methods
    • C22B23/0469Treatment or purification of solutions, e.g. obtained by leaching by chemical methods by chemical substitution, e.g. by cementation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Removal Of Specific Substances (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

Nickel is separated from an aqueous solution containing a mixture of cobalt and nickel salts by first precipitating the nickel by adding a metal more electronegative than nickel, for example iron, and also one or more metalloidic compounds formed between sulphur, selenium or tellurium on the one hand, and antimony or arsenic on the other. The separated nickel is then redissolved and the metalloidic compounds regenerated for further use. Copper may also be added in the first stage of the <PICT:0853323/III/1> process, either as a soluble salt, the amount of copper added being 0.3-2% by weight of the nickel, or as the sulphide, the copper being 10-25% by weight of the nickel. The first stage may be carried out at 50-100 DEG C. and at a pH of approximately 2.5. Suitable metalloidic compounds include arsenic and antimony sulphides, which may be naturally occurring, such as realgars, orpiments, and stibnites and may be employed in an amount 1-2 times by weight of the nickel present in the solution. Between 1 and 5 times the theoretically required amount of metal more electronegative than nickel may be employed, preferably between 1.1 and 1.3 times, and is preferably in a finely divided state. In an example, a solution of nickel and cobalt sulphate or chloride is heated to above 50 DEG C. with agitation, and copper is added, either as a soluble salt or as the sulphide, which may be added with the metalloidic compound. Arsenic trisulphide and iron are then added, preferably simultaneously, and the pH is maintained at about 2.5 by acid addition, for example hydrochloric acid. The suspended solids are then removed and washed. The cobalt-containing mother liquor remaining is practically free of nickel and copper. The solids are then treated to regenerate the arsenic trisulphide, for example by suspending in water and passing in chlorine until the nickel is substantially completely dissolved, removing the residue, acidifying and adding a sulphide, for example iron sulphide or preferably hydrogen sulphide, to precipitate arsenic and copper sulphides. This precipitate may be freed of copper by dissolving the arsenic sulphide in sodium sulphide solution and acidifying to reprecipitate. The filtrate obtained after the arsenic and copper sulphides have been precipitated is treated to eliminate cobalt and iron by oxidising with chlorine and precipitating ferric hydroxide by adding calcium carbonate to a pH of 3.0-3.5, and precipitating cobalt hydroxide, contaminated with a little nickel which may be recycled to the first stage of the process, by the simultaneous action of chlorine and sodium hydroxide as in Specification 795,410. The cobalt-containing mother liquor obtained after removing the suspended solids in the initial stage of the process may be freed from iron by precipitation as the hydroxide as indicated above. The accompanying flow sheets illustrates the process of the invention.
GB1343558A 1957-05-07 1958-04-28 Process for the separation of nickel from solutions containing cobalt and nickel salts Expired GB853323A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR853323X 1957-05-07

Publications (1)

Publication Number Publication Date
GB853323A true GB853323A (en) 1960-11-02

Family

ID=9327019

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1343558A Expired GB853323A (en) 1957-05-07 1958-04-28 Process for the separation of nickel from solutions containing cobalt and nickel salts

Country Status (3)

Country Link
US (1) US2960400A (en)
BE (1) BE566626A (en)
GB (1) GB853323A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3317312A (en) * 1967-05-02 Table i.xuptake o of a number of metals by various sulfides
US3322532A (en) * 1963-12-27 1967-05-30 Chemolimpex Process for recovering the metal content of middlings, slags, low-grade ores, and concentrates
FR1536922A (en) * 1964-11-25 1968-09-02 Republic Steel Corp Process for recovering nickel or metallic cobalt from solutions of salts of these two metals
US20110283831A1 (en) * 2008-06-20 2011-11-24 Eric Girvan Roche Process for the Recovery of Nickel and/or Cobalt from a Leach Solution

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL147433B (en) * 1948-07-12 Dresden Arzneimittel
BE493059A (en) * 1949-01-07
US2829965A (en) * 1956-05-15 1958-04-08 Electro Chimie Metal Process of eliminating nickel contained in solutions of mixed salts of cobalt and nickel

Also Published As

Publication number Publication date
US2960400A (en) 1960-11-15
BE566626A (en) 1900-01-01

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