GB795790A - Improvements in or relating to the recovery of gold - Google Patents
Improvements in or relating to the recovery of goldInfo
- Publication number
- GB795790A GB795790A GB1171156A GB1171156A GB795790A GB 795790 A GB795790 A GB 795790A GB 1171156 A GB1171156 A GB 1171156A GB 1171156 A GB1171156 A GB 1171156A GB 795790 A GB795790 A GB 795790A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gold
- sulphuric
- iron
- hydrochloric acid
- mixture
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B23/00—Obtaining nickel or cobalt
- C22B23/04—Obtaining nickel or cobalt by wet processes
- C22B23/0407—Leaching processes
- C22B23/0415—Leaching processes with acids or salt solutions except ammonium salts solutions
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B11/00—Obtaining noble metals
- C22B11/06—Chloridising
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/04—Extraction of metal compounds from ores or concentrates by wet processes by leaching
- C22B3/06—Extraction of metal compounds from ores or concentrates by wet processes by leaching in inorganic acid solutions, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Metallurgy (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Environmental & Geological Engineering (AREA)
- Geology (AREA)
- Geochemistry & Mineralogy (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Gold is separated from arsenical and sulpharsenical ores, concentrates and residues and roasted materials, which may contain also cobalt and/or nickel and/or iron, by treatment with one or more strong mineral acids followed by treatment in the same medium with an oxidizing agent supplied as such or produced in situ, the redox potential of the medium being measured, and maintained during the oxidation treatment at such a value that the gold is oxidized and solubilized. Thereafter any solid residue is separated and gold recovered from the solution. Mineral acids referred to are a mixture of sulphuric and nitric acids, hydrochloric acid and sulphuric acid. Suitable oxidizing agents are chlorine (which may be produced in situ by the addition of aqueous hydrochloric acid or sodium chloride to a sulphuric acid mixture or the addition of sodium chlorate to a hydrochloric acid mixture) and sodium or calcium hypochlorites, and the salts may be added as aqueous solutions. It is preferred to employ a temperature of about 70 DEG C. and an acidity greater than normal. When using a mixture of sulphuric and nitric acids it may be necessary, e.g. when using chlorine as oxidizing agent, to remove some of the arsenious oxide before effecting solubilization of the gold: in this case the residue of metallic arsenides which remains insoluble may be separated from the liquid, arsenic removed therefrom by suitable means such as hot water washing, and the solids resuspended in the liquid for completion of the solubilization after restoration of the redox potential. If, however, hydrochloric acid or sodium chloride are used as oxidizing agents with sulphuric and nitric acids, the gold is solubilized before the arsenic is oxidized. After oxidation the liquor may be neutralized, e.g. with lime or calcium carbonate, with continuous maintenance of the redox potential above the level at which gold reprecipitates and with pH measurement. Thus with the solution from an ore containing iron and cobalt, and after obtaining an Fe/As ratio of about 1, the neutralization should continue until ferric arsenate is precipitated, then gold can be separated by adding sodium sulphide or iron or, as described in an example, by adsorption on charcoal. Any silver present may be recovered by passing the gold-free solution over copper or iron. In examples: (1) a roasted speiss containing cobalt, nickel, iron and arsenic was reacted at 90 DEG C. with hydrochloric acid and aqueous sodium chlorate added; and (2) smaltite containing cobalt, nickel and arsenic was reacted with a mixture of sulphuric and nitric acids and chlorine added as oxidizing agent. Specification 795,793 is referred to.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR795790X | 1955-04-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB795790A true GB795790A (en) | 1958-05-28 |
Family
ID=9234798
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB1171156A Expired GB795790A (en) | 1955-04-20 | 1956-04-17 | Improvements in or relating to the recovery of gold |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB795790A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013044380A1 (en) * | 2011-09-27 | 2013-04-04 | Nichromet Extraction Inc. | A method and a system for gold extraction with halogens |
| CN112725633A (en) * | 2021-02-07 | 2021-04-30 | 厦门海峡黄金珠宝产业园有限公司 | Negative pressure type gold chlorination and separation process |
| CN113528850A (en) * | 2021-07-26 | 2021-10-22 | 中南大学 | A kind of method of controlling potential to purify gold |
| CN116096930A (en) * | 2020-08-05 | 2023-05-09 | 罗伯特·博世有限公司 | Method and device for obtaining gold and/or silver and/or at least one platinum group metal |
-
1956
- 1956-04-17 GB GB1171156A patent/GB795790A/en not_active Expired
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013044380A1 (en) * | 2011-09-27 | 2013-04-04 | Nichromet Extraction Inc. | A method and a system for gold extraction with halogens |
| US9051626B2 (en) | 2011-09-27 | 2015-06-09 | Dundee, Technologies Durables Inc. | Method and a system for gold extraction with halogens |
| CN116096930A (en) * | 2020-08-05 | 2023-05-09 | 罗伯特·博世有限公司 | Method and device for obtaining gold and/or silver and/or at least one platinum group metal |
| CN112725633A (en) * | 2021-02-07 | 2021-04-30 | 厦门海峡黄金珠宝产业园有限公司 | Negative pressure type gold chlorination and separation process |
| CN112725633B (en) * | 2021-02-07 | 2022-04-26 | 厦门海峡黄金珠宝产业园有限公司 | Negative pressure type gold chlorination and separation process |
| CN113528850A (en) * | 2021-07-26 | 2021-10-22 | 中南大学 | A kind of method of controlling potential to purify gold |
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