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GB901573A - Improvements in or relating to the elution of gold-bearing ion-exchange resins - Google Patents

Improvements in or relating to the elution of gold-bearing ion-exchange resins

Info

Publication number
GB901573A
GB901573A GB34536/59A GB3453659A GB901573A GB 901573 A GB901573 A GB 901573A GB 34536/59 A GB34536/59 A GB 34536/59A GB 3453659 A GB3453659 A GB 3453659A GB 901573 A GB901573 A GB 901573A
Authority
GB
United Kingdom
Prior art keywords
cycle
resin
gold
fraction
solution
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
GB34536/59A
Inventor
Jack Davison
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.)
Consolidated Gold Fields of South Africa Ltd
Permutit Co Ltd
Original Assignee
Consolidated Gold Fields of South Africa Ltd
Permutit Co 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 Consolidated Gold Fields of South Africa Ltd, Permutit Co Ltd filed Critical Consolidated Gold Fields of South Africa Ltd
Priority to GB34536/59A priority Critical patent/GB901573A/en
Publication of GB901573A publication Critical patent/GB901573A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G7/00Compounds of gold
    • C01G7/003Preparation involving a liquid-liquid extraction, an adsorption or an ion-exchange
    • 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
    • C22B3/42Treatment or purification of solutions, e.g. obtained by leaching by ion-exchange extraction
    • 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)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Geology (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Environmental & Geological Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

Gold values are recovered from an ion-exchange resin containing gold, copper, and nickel by contacting the resin in a first step with an alkali metal cyanide solution, e.g. NaCN, to elute copper and nickel, and iron and zinc if present, in a second step with a mineral acid, e.g. H2SO4, to remove further copper and nickel, and in a third step with an alkaline solution of a thiocyanate, e.g. N H4CNS or NaCNS. The resin is obtained by passing a cyanide solution, obtained from the dressing of ore, through a predominantly weakly basic anion exchange resin, e.g. a polystyrene type, in the salt form. After the third step, the resin may be regenerated by mineral acid solution. The eluants in the first, second and fourth steps may be used in a number of fractions. In a succession of cycles of operation, the first fractions of the first and second steps of the first cycle are added to the original cyanide solution for gold leaching, while the second fraction becomes the first in the second cycle, the third becomes the second, and so on. The last fraction of the first step of the second cycle is a fresh cyanide solution, while the last fraction of the second step in the second cycle was the first fraction of the resin regeneration in the first cycle. The last fraction of the resin regeneration is a fresh acid solution. The gold is recovered from the eluate of the third step, e.g. by electrolysis, and the stripped eluate is used in the second cycle. Specification 901,572 is referred to.
GB34536/59A 1959-10-12 1959-10-12 Improvements in or relating to the elution of gold-bearing ion-exchange resins Expired GB901573A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB34536/59A GB901573A (en) 1959-10-12 1959-10-12 Improvements in or relating to the elution of gold-bearing ion-exchange resins

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB34536/59A GB901573A (en) 1959-10-12 1959-10-12 Improvements in or relating to the elution of gold-bearing ion-exchange resins

Publications (1)

Publication Number Publication Date
GB901573A true GB901573A (en) 1962-07-18

Family

ID=10366844

Family Applications (1)

Application Number Title Priority Date Filing Date
GB34536/59A Expired GB901573A (en) 1959-10-12 1959-10-12 Improvements in or relating to the elution of gold-bearing ion-exchange resins

Country Status (1)

Country Link
GB (1) GB901573A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5134169A (en) * 1988-12-19 1992-07-28 Mintek Gold selective ion exchange resins
WO1999032675A1 (en) * 1997-12-19 1999-07-01 Surini International Ltd. A process for recovering zinc values as complex zinc cyanide solution and use of the same for stripping copper from loaded anion exchange material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5134169A (en) * 1988-12-19 1992-07-28 Mintek Gold selective ion exchange resins
WO1999032675A1 (en) * 1997-12-19 1999-07-01 Surini International Ltd. A process for recovering zinc values as complex zinc cyanide solution and use of the same for stripping copper from loaded anion exchange material

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