GB959813A - A process for the extraction of a metal value or values - Google Patents

A process for the extraction of a metal value or values

Info

Publication number
GB959813A
GB959813A GB19802/61A GB1980261A GB959813A GB 959813 A GB959813 A GB 959813A GB 19802/61 A GB19802/61 A GB 19802/61A GB 1980261 A GB1980261 A GB 1980261A GB 959813 A GB959813 A GB 959813A
Authority
GB
United Kingdom
Prior art keywords
metal
solution
aqueous
ions
salts
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
GB19802/61A
Inventor
William Bernard Hawes
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.)
Shell Research Ltd
Original Assignee
Shell Research Ltd
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 Shell Research Ltd filed Critical Shell Research Ltd
Priority to GB19802/61A priority Critical patent/GB959813A/en
Publication of GB959813A publication Critical patent/GB959813A/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
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/26Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds
    • C22B3/32Carboxylic acids
    • 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

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Extraction Or Liquid Replacement (AREA)

Abstract

Metal values are extracted from aqueous media containing at least one metal salt (other than an alkali metal salt) in solution or suspension by contacting the aqueous medium with a solution of a Koch acid or a carboxylic acid obtained by caustic fusion from an oxo-alcohol, in an inert organic solvent substantially immiscible with the aqueous medium, the latter being extracted at a pH above or substantially at the pH of hydrolysis of an undesired metal salt or salts (and preferably not more than 0.5 of a pH unit below the pH of hydrolysis of the metal salt it is desired to extract). The extraction may be selective if the pH is suitably adjusted, the metal salts which have a pH of hydrolysis at or below the pH of the aqueous medium forming with the carboxylic acid salts insoluble in water but soluble in the organic solvent. Metal values are recovered from the inert solvent solution by treating it with aqueous acid media which form water-soluble salt of the metal, and, by using aqueous media of a suitable pH, metal salts may be selectively stripped from an organic solvent solution containing more than one metal carboxylate. The process of the invention may be carried out using normal techniques of co-current or counter-current liquid liquid extraction. Examples describe the extraction of (1) nickelous ion Ni2+ and cobaltous ion Co2+ are extracted from separate solutions containing nickel sulphate and cobalt sulphate respectively with Koch acids (prepared from a C8 to C18 mixture olefinic hydrocarbons derived from cracked raffinate olefines) in kerosene; (2) nickel ions and copper ions from a mixed solution of copper sulphate and nickel sulphate at pH 5.5; (3) cobalt ions and nickel ions from mixed solutions of cobalt sulphate and nickel sulphate at pH=7.4; (4) copper ions and cobalt ions from mixed solutions of copper sulphate and cobalt sulphate at pH=5.8; (5) cobalt ions from cobalt sulphate solution at pH=8.7 using a mixture of C7 to C20 carboxylic acids derived from sodium hydroxide fusion of oxo-alcohol residues. The recovery of the metal ions from the carboxylic acid salts thereof is accomplished by treating the organic solution with sulphuric acid and separating the aqueous layer. Specifications 743,597, 798,065, 871,278 and 883,143 are referred to.ALSO:Metal values are extracted from aqueous media containing at least one metal salt (other than an alkali metal salt) in solution or suspension by contacting the aqueous medium with a solution of a Koch acid or a carboxylic acid obtained by caustic fusion from an oxo-alcohol, in an inert organic solvent substantially immiscible with the aqueous medium, the latter being extracted at a pH above or substantially at the pH of hydrolysis of an undesired metal salt or salts. Suitably the concentration of any one metal salt in solution or suspension is from 0.01M to 1M, preferably 0.1M, and the pH of this aqueous medium not more than 0.5 of a pH unit below the pH of hydrolysis of the metal salt it is desired to extract. The concentration of carboxylic acid in the inert organic solvent is generally 0.5M to 2M, preferably 1M, and the solvent is generally kerosene or an aliphatic hydrocarbon containing a minor proportion of an aromatic hydrocarbon. According to an embodiment of the invention a metal value is selectively extracted from an aqueous solution containing at least two metal salts by contacting the aqueous medium at a certain pH value with a solution of the carboxylic acid in an inert organic solvent of the type described, when the metal salts which have a pH value of hydrolysis at or lower than the pH of the aqueous medium form with the carboxylic acid salts insoluble in water but soluble in the inert organic solvent. The carboxylic acids may be regenerated for re-use by treating the organic solvent solution of their metal salts with an aqueous acid forming water-soluble salts of the metals. Methods of extracting a metal ion from an aqueous solution containing several metal ions, which involves partial removal of undesired metal ions before forming the desired metal salt of the carboxylic acid, or the complete extraction into the inert organic solvent of all metal ions contained in the aqueous solution are disclosed. The process of the invention may be carried out using normal techniques of co-current or counter-current liquid extraction. Specifications 743,597, 798,065, 871,278 and 883,142 are referred to.
GB19802/61A 1961-06-01 1961-06-01 A process for the extraction of a metal value or values Expired GB959813A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB19802/61A GB959813A (en) 1961-06-01 1961-06-01 A process for the extraction of a metal value or values

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB19802/61A GB959813A (en) 1961-06-01 1961-06-01 A process for the extraction of a metal value or values

Publications (1)

Publication Number Publication Date
GB959813A true GB959813A (en) 1964-06-03

Family

ID=10135471

Family Applications (1)

Application Number Title Priority Date Filing Date
GB19802/61A Expired GB959813A (en) 1961-06-01 1961-06-01 A process for the extraction of a metal value or values

Country Status (1)

Country Link
GB (1) GB959813A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3950488A (en) * 1974-11-04 1976-04-13 Kennecott Copper Corporation Process for recovering copper from basic carbonate mixtures
US4120817A (en) * 1972-07-03 1978-10-17 Outokumpu Oy Extraction agent composition
US4200504A (en) * 1974-05-30 1980-04-29 Gunnar Thorsen Extraction and separation of metals from solids using liquid cation exchangers
FR2440995A1 (en) * 1978-11-09 1980-06-06 Nippon Mining Co PROCESS FOR SEPARATING AND RECOVERING COBALT BY EXTRACTION

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4120817A (en) * 1972-07-03 1978-10-17 Outokumpu Oy Extraction agent composition
US4200504A (en) * 1974-05-30 1980-04-29 Gunnar Thorsen Extraction and separation of metals from solids using liquid cation exchangers
US3950488A (en) * 1974-11-04 1976-04-13 Kennecott Copper Corporation Process for recovering copper from basic carbonate mixtures
FR2440995A1 (en) * 1978-11-09 1980-06-06 Nippon Mining Co PROCESS FOR SEPARATING AND RECOVERING COBALT BY EXTRACTION

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