CN101760628A - Thiosulfate gold extracting method taking diethylenetriamine as additive - Google Patents
Thiosulfate gold extracting method taking diethylenetriamine as additive Download PDFInfo
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- CN101760628A CN101760628A CN201010108631A CN201010108631A CN101760628A CN 101760628 A CN101760628 A CN 101760628A CN 201010108631 A CN201010108631 A CN 201010108631A CN 201010108631 A CN201010108631 A CN 201010108631A CN 101760628 A CN101760628 A CN 101760628A
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- Prior art keywords
- gold
- diethylenetriamine
- leaching
- additive
- copper
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- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 239000010931 gold Substances 0.000 title claims abstract description 44
- 229910052737 gold Inorganic materials 0.000 title claims abstract description 44
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 title claims abstract description 31
- 238000000034 method Methods 0.000 title claims abstract description 27
- 239000000654 additive Substances 0.000 title claims abstract description 21
- 230000000996 additive effect Effects 0.000 title claims abstract description 21
- DHCDFWKWKRSZHF-UHFFFAOYSA-N sulfurothioic S-acid Chemical compound OS(O)(=O)=S DHCDFWKWKRSZHF-UHFFFAOYSA-N 0.000 title abstract 4
- 238000002386 leaching Methods 0.000 claims abstract description 30
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 claims abstract description 26
- 150000002500 ions Chemical class 0.000 claims abstract description 11
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000001238 wet grinding Methods 0.000 claims abstract description 7
- DHCDFWKWKRSZHF-UHFFFAOYSA-L thiosulfate(2-) Chemical compound [O-]S([S-])(=O)=O DHCDFWKWKRSZHF-UHFFFAOYSA-L 0.000 claims description 20
- 238000013019 agitation Methods 0.000 claims description 6
- 229910021591 Copper(I) chloride Inorganic materials 0.000 claims description 3
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 claims description 3
- 239000011435 rock Substances 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 abstract description 5
- 239000000284 extract Substances 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract 1
- 231100000614 poison Toxicity 0.000 abstract 1
- 230000007096 poisonous effect Effects 0.000 abstract 1
- 238000011112 process operation Methods 0.000 abstract 1
- 238000003756 stirring Methods 0.000 abstract 1
- PODWXQQNRWNDGD-UHFFFAOYSA-L sodium thiosulfate pentahydrate Chemical compound O.O.O.O.O.[Na+].[Na+].[O-]S([S-])(=O)=O PODWXQQNRWNDGD-UHFFFAOYSA-L 0.000 description 12
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 6
- 239000003153 chemical reaction reagent Substances 0.000 description 6
- 239000010949 copper Substances 0.000 description 5
- XYXNTHIYBIDHGM-UHFFFAOYSA-N ammonium thiosulfate Chemical compound [NH4+].[NH4+].[O-]S([O-])(=O)=S XYXNTHIYBIDHGM-UHFFFAOYSA-N 0.000 description 4
- 238000013467 fragmentation Methods 0.000 description 4
- 238000006062 fragmentation reaction Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- KXZJHVJKXJLBKO-UHFFFAOYSA-N chembl1408157 Chemical compound N=1C2=CC=CC=C2C(C(=O)O)=CC=1C1=CC=C(O)C=C1 KXZJHVJKXJLBKO-UHFFFAOYSA-N 0.000 description 2
- -1 copper complex ion Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- XOCUXOWLYLLJLV-UHFFFAOYSA-N [O].[S] Chemical compound [O].[S] XOCUXOWLYLLJLV-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- QRJOYPHTNNOAOJ-UHFFFAOYSA-N copper gold Chemical compound [Cu].[Au] QRJOYPHTNNOAOJ-UHFFFAOYSA-N 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-O sulfonium Chemical compound [SH3+] RWSOTUBLDIXVET-UHFFFAOYSA-O 0.000 description 1
- NIAGBSSWEZDNMT-UHFFFAOYSA-M tetraoxidosulfate(.1-) Chemical compound [O]S([O-])(=O)=O NIAGBSSWEZDNMT-UHFFFAOYSA-M 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Images
Classifications
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- 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
- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention provides a thiosulfate gold extracting method taking diethylenetriamine as an additive, which is characgerized by comprising the following steps of: adding 0.03-3 mol/dm<3> of thiosulfate leaching agents to ore pulp which is subjected to wet grinding and has the mass concentration of 40 percent by water volume; then adding a diethylenetriamine and copper (II) coordination ion additive formed by 0.0015-0.09 mol/dm<3> of the diethylenetriamine and 0.0015-0.03 mol/dm<3> of copper (II) ions; regulating pH to 10-12; stirring and leaching for 6-24 hours so as to obtain gold-containing leaching liquor; and conventionally recovering the gold contained in the leaching liquor. The invention extracts the gold from ores by using the leaching liquor and has high gold leaching rate, extremely low thiosulfate consumption amount, high leaching speed, simple process operation and easy control, the simple components of the gold leaching liquor is beneficial to recovering the gold contained in the leaching liquor, the change of the pH has little influence on gold leaching and the whole gold extracting process has no poisonous wastes and can not pollute the environment.
Description
Technical field
The present invention relates to a kind of is the method for the thiosulfate gold extracting of additive with the diethylenetriamine, belongs to technical field of wet metallurgy.
Background technology
At present, it is to adopt cyanide process that gold extracts main, accounts for more than 80%.Yet sodium cyanide is hypertoxic chemical, and residual sodium cyanide and the toxic cyanide that produces in soaking golden process can cause serious environmental to be polluted in tailing dam, and some countries and regions have forbidden using prussiate in gold extracts for this reason.In addition, cyanide process also is difficult to complicated gold mines such as Treatment of Copper, carbon containing.
In recent years, in the alternative reagent of research prussiate, thiosulfate technique is considered to replace the method for the tool application prospect of cyanide process with its characteristics such as quick, nontoxic.Yet for golden speed is soaked in raising, investigator's employing mostly adds the leach liquor of the mixing solutions of copper (II) ion, ammoniacal liquor as the gold extraction in thiosulfate solution.Because of the existence of ammoniacal copper complex ion, thiosulphate consumption is sharply risen, and makes golden leach liquor complicated component, and the gold that enters in the leach liquor is difficult to efficient recovery again, cause reagent consume excessive, cost is too high, is difficult to realize suitability for industrialized production.
Many researchers adopts reagent such as adding sulfate radical, inferior sulfate radical and sulfonium ion again, and charge into nitrogen and reduce dissolved oxygen, change redox couple, or adopt no cuprammonium to have methods such as pressurization leaching down, carried out big quantity research to seek to reduce the method that reagent consumes, these methods have played certain effect really on control thiosulphate consumption, but but because of energy consumption height or complex manufacturing, are difficult to realize scale operation.
Summary of the invention
For solving Cu
2+-NH
3-S
2O
3 2-Mix problems such as gold leachate reagent consumption in soaking golden process is big, leaching system complexity, the invention provides a kind of employing diethylenetriamine and copper (II) ion formation diethylenetriamine and close the alternative Cu of copper (II) coordination ion
2+-NH
3-S
2O
3 2-The method of cuprammonium in the leaching system (II) coordination ion promptly is that leaching agent, diethylenetriamine and copper (II) ion formation diethylenetriamine closes the method that copper (II) coordination ion is an additive composition gold leachate with the thiosulphate.
Provided by the invention is that the thiosulfate gold extracting method of additive is finished by following technical proposal with the diethylenetriamine:
A. with ore reduction, wet-milling to fineness accounts for more than 90% for-200 orders, forms ore pulp;
B. regulate ore pulp mass concentration to 40%, press water meter, in ore pulp, add 0.03～3mol/dm
3The thiosulphate leaching agent, add 0.0015～0.09mol/dm again
3Diethylenetriamine and 0.0015～0.03mol/dm
3The diethylenetriamine that forms of copper (II) ion close copper (II) coordination ion additive, regulate pH to 10～12, agitation leach 6～24 hours, auriferous leach liquor, reclaim the gold in the leach liquor routinely.
Ore in the described a step is auriferous placer or rock ore deposit.
The preferred cupric of copper (II) ion (II) ionic CuSO in the described b step
4Solution or CuCl
2Solution, perhaps other cupric (II) ion solution.
The preferred Na of thiosulphate in the described b step
2S
2O
3Or (NH
4)
2S
2O
3, perhaps contain other salt of thiosulfate anion.
The pH regulator of described b step adopts conventional acid or alkali to regulate.
The present invention has following advantage and effect:
1, reagent consumption obviously reduces.Copper gold is adopted Cu
2+-NH
3-S
2O
3 2-The leaching system, handle ore thiosulphate consumption per ton up to 20～30kg, and adopt method provided by the invention, the thiosulphate consumption can be reduced to below the 5kg.
2, pH changes gold leaching influence little.Generally speaking, Cu
2+-NH
3-S
2O
3 2-The leaching system in, pH requires to be controlled at about 10, pH is too high, can cause gold leaching rate significantly to reduce, and in the method provided by the invention, pH was up to 12 o'clock, gold leaching rate and thiosulphate consumption all do not have big variation, need not the pH that leaches system is done accurate adjustment, are applicable to scale operation.
3, leaching velocity is fast, adopts method provided by the invention, and general gold mine can leach more than 85% through 6～24 hours, and sample ore adaptability is strong, can effectively handle cupric, carbon containing gold mine.
4, golden leach liquor component is simple, adopt method provided by the invention, because the consumption of thiosulphate is less, can not produce a large amount of polythionic acid roots and other oxygen sulfur compound, and the associated metal under the alkaline condition in the gold mine and other impurity (as Fe etc.) can not dissolve and enter golden leach liquor, help the recovery of gold in the golden leach liquor, the lean solution that reclaims gold also is easy to recycle.
Description of drawings
Fig. 1 is a process flow sheet of the present invention.
Embodiment
Below in conjunction with embodiment the present invention is described further.
Embodiment 1
A. auriferous rock ore deposit (this ore contains golden 2.78g/t, cupric 0.18%) 100kg is carried out fragmentation, wet-milling to ore fineness accounts for 90% for-200 orders, makes it to form ore pulp;
B. regulate ore pulp mass concentration to 40%, press water meter, in ore pulp, add Sulfothiorine to 0.03mol/dm
3As leaching agent, add diethylenetriamine again to 0.003mol/dm
3, CuSO
45H
2O to copper (II) ion be 0.0015mol/dm
3, make diethylenetriamine and copper (II) ion form the additive that diethylenetriamine closes copper (II) coordination ion, regulating pH routinely is 11, agitation leach 6 hours gets auriferous leach liquor, reclaims the gold in the leach liquor routinely.Wherein, the leaching yield of gold reaches 86.3%, and the consumption of Sulfothiorine is the 3.3kg/t ore.
With in the prior art with cuprammonium the Sulfothiorine consumption (21.5kg/t ore) during as additive compare, the consumption of its Sulfothiorine greatly reduces.
Embodiment 2
A. certain gold floatation concentrate ore (this ore contains golden 198.2g/t, cupric 23.1%) 50kg is carried out fragmentation, wet-milling to ore fineness accounts for 90% for-200 orders, forms ore pulp;
B. regulate ore pulp mass concentration to 40%, press water meter, in ore pulp, add leaching agent Sulfothiorine to 3mol/dm
3, add diethylenetriamine again to 0.03mol/dm
3, CuCl
2To copper (II) ion be 0.03mol/dm
3, make diethylenetriamine and copper (II) ion form the additive that diethylenetriamine closes copper (II) coordination ion, regulating pH is 12, agitation leach 24 hours gets auriferous leach liquor, reclaims the gold in the leach liquor routinely.Then, gold leaching rate reaches 88.5%, and the consumption of Sulfothiorine is the 4.65kg/t ore.
With in the prior art with cuprammonium the Sulfothiorine consumption (being the 29.6kg/t ore) during as additive compare, the consumption of its Sulfothiorine greatly reduces.
Embodiment 3
A. certain gold ore ore (this ore contains golden 49.4g/t, cupric 2.4%) 80kg is carried out fragmentation, wet-milling to ore fineness accounts for 90% for-200 orders, forms ore pulp;
B. regulate ore pulp mass concentration to 40%, press water meter, in ore pulp, add leaching agent Sulfothiorine to 0.3mol/dm
3, add diethylenetriamine again to 0.0015mol/dm
3, CuSO
45H
2O to copper (II) ion be 0.015mol/dm
3, make diethylenetriamine and copper (II) ion form the additive that diethylenetriamine closes copper (II) coordination ion, regulating pH is 10, agitation leach 12 hours gets auriferous leach liquor, reclaims the gold in the leach liquor routinely.Then, the leaching yield of gold reaches 90.3%, and the consumption of Sulfothiorine is the 4.55kg/t ore.
With in the prior art with cuprammonium the Sulfothiorine consumption (being the 27.3kg/t ore) during as additive compare, the consumption of its Sulfothiorine greatly reduces.
Embodiment 4
A. will contain banket ore deposit (this ore contains golden 2.8g/t, cupric 0.31%, carbon containing 0.81%) 100kg and carry out fragmentation, wet-milling to ore fineness accounts for 90% for-200 orders, forms ore pulp;
B. regulate ore pulp mass concentration to 40%, press water meter, in ore pulp, add the leaching agent ammonium thiosulfate to 1.5mol/dm
3, add diethylenetriamine again to 0.09mol/dm
3, CuSO
45H
2O to copper (II) ion be 0.01mol/dm
3, make diethylenetriamine and copper (II) ion form the additive that diethylenetriamine closes copper (II) coordination ion, regulating pH is 11, agitation leach 12 hours must contain golden leach liquor, reclaims the gold in the leach liquor routinely.Then, the leaching yield of gold reaches 85.4%, and the consumption of ammonium thiosulfate is the 3.1kg/t ore.
With in the prior art with cuprammonium the ammonium thiosulfate consumption (being the 29.3kg/t ore) during as additive compare, the consumption of its ammonium thiosulfate greatly reduces.
Claims (4)
1. one kind is the thiosulfate gold extracting method of additive with the diethylenetriamine, it is characterized in that through the following step:
A. with ore reduction, wet-milling to fineness accounts for more than 90% for-200 orders, forms ore pulp;
B. regulate ore pulp mass concentration to 40%, press water meter, in ore pulp, add 0.03～3mol/dm
3The thiosulphate leaching agent, add 0.0015～0.09mol/dm again
3Diethylenetriamine and 0.0015～0.03mol/dm
3The diethylenetriamine that forms of copper (II) ion close copper (II) coordination ion additive, regulate pH to 10～12, agitation leach 6～24 hours, auriferous leach liquor, reclaim the gold in the leach liquor routinely.
2. according to claim 1 is the thiosulfate gold extracting method of additive with the diethylenetriamine, it is characterized in that the ore in the described a step is auriferous placer or rock ore deposit.
3. according to claim 1 is the thiosulfate gold extracting method of additive with the diethylenetriamine, it is characterized in that the preferred cupric of copper (II) ion (II) the ionic CuSO in the described b step
4Solution or CuCl
2Solution.
4. according to claim 1 is the thiosulfate gold extracting method of additive with the diethylenetriamine, it is characterized in that the preferred Na of thiosulphate in the described b step
2S
2O
3Or (NH
4)
2S
2O
3
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101086317A CN101760628B (en) | 2010-02-10 | 2010-02-10 | Thiosulfate gold extracting method taking diethylenetriamine as additive |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101086317A CN101760628B (en) | 2010-02-10 | 2010-02-10 | Thiosulfate gold extracting method taking diethylenetriamine as additive |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101760628A true CN101760628A (en) | 2010-06-30 |
| CN101760628B CN101760628B (en) | 2012-10-31 |
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ID=42492007
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|---|---|---|---|
| CN2010101086317A Expired - Fee Related CN101760628B (en) | 2010-02-10 | 2010-02-10 | Thiosulfate gold extracting method taking diethylenetriamine as additive |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2966470A1 (en) * | 2010-10-25 | 2012-04-27 | Christian Queyroix | Treating gold ore to extract gold contained in ore, by placing ore having liquid and solid phases and then forming prepared ore from ore, placing etching solution comprising sodium thiosulfate, and mixing prepared ore with etching solution |
| CN103409623A (en) * | 2013-07-26 | 2013-11-27 | 中南大学 | Method for reducing consumption of thiosulfate in gold leaching system |
| CN104805285A (en) * | 2015-05-05 | 2015-07-29 | 中南大学 | Method for leaching gold by virtue of thiosulfate utilizing ammonium alcohol polyvinyl phosphate as additive |
| CN104862494A (en) * | 2015-05-05 | 2015-08-26 | 中南大学 | Gold leaching process from sulfide gold mine |
| CN105803220A (en) * | 2016-04-28 | 2016-07-27 | 长春黄金研究院 | Method for reducing thiosulfate consumption quantity |
| CN109852814A (en) * | 2019-02-25 | 2019-06-07 | 昆明理工大学 | A kind of thiosulfate gold extracting method elution process golden in modified gold loaded carbon |
| CN111471858A (en) * | 2020-06-15 | 2020-07-31 | 矿冶科技集团有限公司 | Thiosulfate gold leaching method and application |
| CN112501450A (en) * | 2020-10-28 | 2021-03-16 | 黄伟 | Gold extraction agent for treating high-sulfur high-arsenic gold ore and preparation method thereof |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109680163A (en) * | 2019-01-14 | 2019-04-26 | 东北大学 | A method of using triethanolamine as the Leaching of Gold Using Thiosulfate of additive |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5939034A (en) * | 1996-06-26 | 1999-08-17 | Henkel Corporation | Process for the recovery of precious metal values from aqueous ammoniacal thiosulfate leach solutions |
| CN101421426A (en) * | 2006-03-03 | 2009-04-29 | 鑫亚国际有限公司 | Process for extracting gold from gold-bearing ore |
-
2010
- 2010-02-10 CN CN2010101086317A patent/CN101760628B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5939034A (en) * | 1996-06-26 | 1999-08-17 | Henkel Corporation | Process for the recovery of precious metal values from aqueous ammoniacal thiosulfate leach solutions |
| CN101421426A (en) * | 2006-03-03 | 2009-04-29 | 鑫亚国际有限公司 | Process for extracting gold from gold-bearing ore |
Non-Patent Citations (1)
| Title |
|---|
| 《昆明理工大学硕士论文》 20081231 白成庆 硫代硫酸盐溶金机理研究 50-52 1-4 , 2 * |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2966470A1 (en) * | 2010-10-25 | 2012-04-27 | Christian Queyroix | Treating gold ore to extract gold contained in ore, by placing ore having liquid and solid phases and then forming prepared ore from ore, placing etching solution comprising sodium thiosulfate, and mixing prepared ore with etching solution |
| CN103409623A (en) * | 2013-07-26 | 2013-11-27 | 中南大学 | Method for reducing consumption of thiosulfate in gold leaching system |
| CN104805285A (en) * | 2015-05-05 | 2015-07-29 | 中南大学 | Method for leaching gold by virtue of thiosulfate utilizing ammonium alcohol polyvinyl phosphate as additive |
| CN104862494A (en) * | 2015-05-05 | 2015-08-26 | 中南大学 | Gold leaching process from sulfide gold mine |
| CN104805285B (en) * | 2015-05-05 | 2017-04-12 | 中南大学 | Method for leaching gold by virtue of thiosulfate utilizing ammonium alcohol polyvinyl phosphate as additive |
| CN105803220A (en) * | 2016-04-28 | 2016-07-27 | 长春黄金研究院 | Method for reducing thiosulfate consumption quantity |
| CN109852814A (en) * | 2019-02-25 | 2019-06-07 | 昆明理工大学 | A kind of thiosulfate gold extracting method elution process golden in modified gold loaded carbon |
| CN109852814B (en) * | 2019-02-25 | 2021-11-12 | 昆明理工大学 | Elution method of gold on modified gold-loaded carbon for thiosulfate gold extraction method |
| CN111471858A (en) * | 2020-06-15 | 2020-07-31 | 矿冶科技集团有限公司 | Thiosulfate gold leaching method and application |
| CN112501450A (en) * | 2020-10-28 | 2021-03-16 | 黄伟 | Gold extraction agent for treating high-sulfur high-arsenic gold ore and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101760628B (en) | 2012-10-31 |
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