GB808909A - Improvements in or relating to the recovery of gold from aqueous cyanide liquors - Google Patents

Improvements in or relating to the recovery of gold from aqueous cyanide liquors

Info

Publication number
GB808909A
GB808909A GB36097/55A GB3609755A GB808909A GB 808909 A GB808909 A GB 808909A GB 36097/55 A GB36097/55 A GB 36097/55A GB 3609755 A GB3609755 A GB 3609755A GB 808909 A GB808909 A GB 808909A
Authority
GB
United Kingdom
Prior art keywords
gold
groups
nickel
silver
per cent
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
GB36097/55A
Inventor
Ronald Alfred Wells
Norman Frank Kember
John Aveston
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.)
National Research Development Corp UK
Original Assignee
National Research Development Corp UK
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 National Research Development Corp UK filed Critical National Research Development Corp UK
Priority to GB36097/55A priority Critical patent/GB808909A/en
Publication of GB808909A publication Critical patent/GB808909A/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)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (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 is recovered from gold-bearing aqueous cyanide liquors by contacting the liquor with an anion-exchange resin which is predominately weakly basic in character through the presence, at the majority of the ion-exchange positions, of primary, secondary or tertiary amine groups, but which also contains from 1 to 25 per cent of strongly basic (quaternary ammonium) groups, thereby absorbing the auro cyanide which may be recovered by subsequent elution. The weakly basic groups are preferably of the type -CH2NRR1, where R and R1 are hydrogen, methyl, ethyl or b -ethylamine, R and R1 being the same or different. The invention is particularly applicable to the recovery of gold from cyanide solutions containing also copper, nickel and iron. The adsorbed gold values may be removed by an alkali metal or ammonium thiocyanate solution which will simultaneously elute any cobalt, nickel or silver which has been taken up. The thiocyanate eluate may be subjected to electrolysis to deposit gold and any silver and the thiocyanate solution may thereafter be returned for elution of a further batch of resin. If zinc is present in the initial liquor it is taken up by the resin but may be eluted by means of a dilute hydrochloric acid solution prior to the elution of the gold. The anion exchange resins are preferably those derivable from cross-linked polystyrene by treatment with chloromethyl ether and treatment of the resulting product to aminate the -CH2Cl groups thereof. According to examples an aqueous cyanide solution containing iron, copper and nickel in addition to gold was brought into contact with a cross-link polystyrene resin containing 90 per cent of dimethylamine groups and 10 per cent of quaternary ammonium, -CH2N(CH3)3 + groups. The gold was preferentially absorbed. (2) An aqueous cyanide solution containing gold, silver, copper, nickel, cobalt, iron and also sodium thiocyanate was contacted with a cross-link polystyrene having dimethylamine groups and 8.5 per cent of quaternary ammonium groups whereby the gold was preferentially absorbed. The silver and nickel in such an initial liquor may be recovered by first treating the liquor with an anion-exchange resin having mainly dimethylamine groups and about 8 per cent of strong base groups, thereby removing the gold and then with an anion-exchange resin having 60 per cent dimethylamine groups and 40 per cent. strong base groups, the latter resin adsorbing nickel and silver. The nickel and silver may be recovered by elution of the latter resin with sodium thiocyanate, and the silver may be recovered from the eluate by electrodeposition. The nickel may then be removed from the stripped eluate by acidifying the solution and the thiocyanate solution resulting may be neutralized and re-used. Specification 808,910 is referred to.
GB36097/55A 1955-12-16 1955-12-16 Improvements in or relating to the recovery of gold from aqueous cyanide liquors Expired GB808909A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB36097/55A GB808909A (en) 1955-12-16 1955-12-16 Improvements in or relating to the recovery of gold from aqueous cyanide liquors

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB36097/55A GB808909A (en) 1955-12-16 1955-12-16 Improvements in or relating to the recovery of gold from aqueous cyanide liquors

Publications (1)

Publication Number Publication Date
GB808909A true GB808909A (en) 1959-02-11

Family

ID=10384918

Family Applications (1)

Application Number Title Priority Date Filing Date
GB36097/55A Expired GB808909A (en) 1955-12-16 1955-12-16 Improvements in or relating to the recovery of gold from aqueous cyanide liquors

Country Status (1)

Country Link
GB (1) GB808909A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0106327A2 (en) * 1982-10-14 1984-04-25 J.T. Baker Chemical Co. Selective separation of noble metals
CN113042113A (en) * 2021-03-22 2021-06-29 中国科学院广州能源研究所 Preparation method of macroporous weak base anion exchange resin special for gold extraction

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0106327A2 (en) * 1982-10-14 1984-04-25 J.T. Baker Chemical Co. Selective separation of noble metals
EP0106327A3 (en) * 1982-10-14 1984-11-14 J.T. Baker Chemical Co. Selective separation of noble metals
CN113042113A (en) * 2021-03-22 2021-06-29 中国科学院广州能源研究所 Preparation method of macroporous weak base anion exchange resin special for gold extraction

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