WO2013145849A1 - 活性炭に吸着された金及び銀の溶離方法及びそれを用いた金及び銀の回収方法 - Google Patents
活性炭に吸着された金及び銀の溶離方法及びそれを用いた金及び銀の回収方法 Download PDFInfo
- Publication number
- WO2013145849A1 WO2013145849A1 PCT/JP2013/052265 JP2013052265W WO2013145849A1 WO 2013145849 A1 WO2013145849 A1 WO 2013145849A1 JP 2013052265 W JP2013052265 W JP 2013052265W WO 2013145849 A1 WO2013145849 A1 WO 2013145849A1
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- WIPO (PCT)
- Prior art keywords
- silver
- activated carbon
- gold
- adsorbed
- eluting
- Prior art date
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 144
- 229910052709 silver Inorganic materials 0.000 title claims abstract description 88
- 239000004332 silver Substances 0.000 title claims abstract description 88
- 238000000034 method Methods 0.000 title claims abstract description 33
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 title claims description 82
- 229910052751 metal Inorganic materials 0.000 title abstract description 12
- 239000002184 metal Substances 0.000 title abstract description 12
- 239000007864 aqueous solution Substances 0.000 claims abstract description 13
- DHCDFWKWKRSZHF-UHFFFAOYSA-N sulfurothioic S-acid Chemical compound OS(O)(=O)=S DHCDFWKWKRSZHF-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000010931 gold Substances 0.000 claims description 88
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 82
- 229910052737 gold Inorganic materials 0.000 claims description 82
- 239000000243 solution Substances 0.000 claims description 24
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 claims description 9
- 235000019345 sodium thiosulphate Nutrition 0.000 claims description 9
- 238000010828 elution Methods 0.000 description 27
- 239000003480 eluent Substances 0.000 description 22
- DHCDFWKWKRSZHF-UHFFFAOYSA-L thiosulfate(2-) Chemical compound [O-]S([S-])(=O)=O DHCDFWKWKRSZHF-UHFFFAOYSA-L 0.000 description 20
- -1 thiosulfate ions Chemical class 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 6
- 239000011593 sulfur Substances 0.000 description 6
- 229910052717 sulfur Inorganic materials 0.000 description 6
- 235000013162 Cocos nucifera Nutrition 0.000 description 5
- 244000060011 Cocos nucifera Species 0.000 description 5
- 238000005259 measurement Methods 0.000 description 4
- 229910052946 acanthite Inorganic materials 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- XUARKZBEFFVFRG-UHFFFAOYSA-N silver sulfide Chemical compound [S-2].[Ag+].[Ag+] XUARKZBEFFVFRG-UHFFFAOYSA-N 0.000 description 2
- 229940056910 silver sulfide Drugs 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 229940006280 thiosulfate ion Drugs 0.000 description 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- DVRDHUBQLOKMHZ-UHFFFAOYSA-N chalcopyrite Chemical compound [S-2].[S-2].[Fe+2].[Cu+2] DVRDHUBQLOKMHZ-UHFFFAOYSA-N 0.000 description 1
- 229910052951 chalcopyrite Inorganic materials 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- FGRVOLIFQGXPCT-UHFFFAOYSA-L dipotassium;dioxido-oxo-sulfanylidene-$l^{6}-sulfane Chemical compound [K+].[K+].[O-]S([O-])(=O)=S FGRVOLIFQGXPCT-UHFFFAOYSA-L 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 229910052976 metal sulfide Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 1
- 229910052683 pyrite Inorganic materials 0.000 description 1
- 239000011028 pyrite Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
Images
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
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
- C22B3/22—Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
- C22B3/24—Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition by adsorption on solid substances, e.g. by extraction with solid resins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3416—Regenerating or reactivating of sorbents or filter aids comprising free carbon, e.g. activated carbon
-
- 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
- C22B11/04—Obtaining noble metals by wet processes
-
- 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
Definitions
- the present invention relates to a method for eluting gold and silver adsorbed on activated carbon and a method for recovering gold and silver using the same.
- Gold and silver are highly valuable metals, exist as simple particles in natural veins, and are contained in pyrite, chalcopyrite, and other metal sulfide ores as traces.
- the recovery method is disclosed in, for example, Patent Document 1 and is examined by a dry method and a wet method, respectively.
- a wet method gold or silver is dissolved in a liquid by leaching and then adsorbed on activated carbon.
- a method of recovering by burning the activated carbon or a method of recovering by eluting gold into a solution is performed.
- the present inventor conducted research to solve the above-mentioned problems. As a result, the gold and silver adsorbed on the activated carbon were eluted by using a thiosulfate aqueous solution maintained at a predetermined pH, thereby allowing the gold and silver to be eluted. It was found that it can be eluted efficiently.
- the present invention completed on the background of the above knowledge is adsorbed on activated carbon that elutes gold and silver using an aqueous thiosulfate solution maintained at a pH of less than 7 for activated carbon on which at least gold and silver are adsorbed. This is an elution method of gold and silver.
- the pH of the thiosulfate aqueous solution is maintained at 4 or more and less than 7.
- the aqueous thiosulfate solution is maintained at 20 to 90 ° C.
- the gold adsorbed on the activated carbon is selectively eluted by maintaining the thiosulfate aqueous solution at 60 to 90 ° C. To separate.
- the silver adsorbed on the activated carbon is selectively eluted by maintaining the thiosulfate aqueous solution at 20 to 50 ° C. To separate.
- the aqueous thiosulfate solution is an aqueous sodium thiosulfate solution.
- the present invention is a method for recovering gold and silver from an aqueous thiosulfate solution containing gold and silver obtained by the method for eluting gold and silver adsorbed on the activated carbon of the present invention.
- gold and silver adsorbed on activated carbon can be efficiently eluted.
- FIG. 3 is a graph showing the Au concentration in the liquid with respect to the elution time obtained in Example 1.
- FIG. 2 is a graph showing Ag concentration in liquid with respect to elution time obtained in Example 1.
- FIG. 4 is a graph showing the concentration of gold obtained in Example 2 in liquid.
- 3 is a graph showing the concentration of silver obtained in Example 2 in liquid.
- gold and silver are eluted using an aqueous thiosulfate solution kept at a pH of less than 7 with respect to activated carbon on which gold and silver are adsorbed.
- activated carbon such as coconut shell activated carbon and coke activated carbon, but any activated carbon may be used.
- At least gold and silver are adsorbed on the activated carbon used in the present invention.
- gold and silver are eluted and separated from the activated carbon.
- Each grade of gold and silver adsorbed on the activated carbon is not limited.
- an aqueous sodium thiosulfate solution maintained at a pH of less than 7 is used as an eluent.
- the thiosulfate include sodium thiosulfate, potassium thiosulfate and the like.
- sodium thiosulfate is effective for elution of gold and silver.
- sodium thiosulfate is less than pH 7, it is partially decomposed to produce sulfur.
- the aqueous thiosulfate solution elutes gold and silver in activated carbon, and precipitates the eluted silver as silver sulfide.
- the precipitated silver sulfide can be recovered from the eluent and treated with a chemical reduction method or the like to recover single silver.
- gold is eluted by a thiosulfate aqueous solution, it is a metal that does not form sulfides, so it remains eluted in the eluent. If necessary, gold can also be recovered from the eluent as a single gold using a chemical reduction method or a solvent extraction-electrolytic collection method.
- the concentration of thiosulfate ions can be 0.01 to 1.0 mol / L.
- the elution effect is saturated at a thiosulfate ion concentration of 0.5 mol / L.
- the amount of thiosulfuric acid required varies depending on the amount of gold or silver adsorbed on the activated carbon, but even if elution is insufficient as described above, gold or silver is not lost.
- Addition of a large excess of thiosulfuric acid inhibits elution by covering the surface of the activated carbon with sulfur, so the realistic thiosulfuric acid concentration is 0.01 to 0.5 mol / L.
- the thiosulfate aqueous solution used for the eluent is kept at a pH of less than 7, preferably a pH of 4 or more and less than 7, and more preferably a pH of 4.5 or more and less than 6.
- elution temperature it is desirable to adjust the elution temperature with respect to the thiosulfate ion concentration.
- the decomposition of thiosulfate ions is accelerated by setting the temperature to 20 to 90 ° C.
- concentration of thiosulfate ions is low in order to prevent adsorption of sulfur onto activated carbon.
- it is closer to normal temperature it will become possible to selectively elute and separate silver from gold and silver adsorbed on the activated carbon. From such a viewpoint, it is more preferable to adjust the elution temperature to 20 to 50 ° C.
- a higher temperature is preferable, and specifically, 60 to 90 ° C. is more preferable.
- the remaining gold can be subsequently eluted from the activated carbon.
- activated carbon on which gold and silver are adsorbed is immersed in a thiosulfate aqueous solution (eluent) having a pH of less than 7 maintained at 20 to 50 ° C. to selectively elute silver.
- a thiosulfate aqueous solution eluent
- the supernatant of the eluent containing the eluted silver component is recovered.
- the eluent is heated and maintained at 60 to 90 ° C., and the remaining gold is eluted from the activated carbon and similarly recovered.
- money can be favorably isolate
- the remaining silver can be subsequently eluted from the activated carbon.
- activated carbon on which gold and silver are adsorbed is immersed in a thiosulfate aqueous solution (eluent) having a pH of less than 7 maintained at 60 to 90 ° C. to selectively elute gold.
- eluent a thiosulfate aqueous solution having a pH of less than 7 maintained at 60 to 90 ° C.
- the eluent is then cooled and held at 20-50 ° C., and the remaining silver is eluted from the activated carbon and recovered in the same manner.
- money can be favorably isolate
- the activated carbon of the present invention can be used repeatedly for adsorption of silver and gold even after elution of silver and gold, which is advantageous in terms of cost.
- gold and silver adsorbed on activated carbon can be efficiently eluted by a simple operation of setting pH using an aqueous thiosulfate solution as an eluent.
- Example 1 Activated carbon (coconut shell-derived activated carbon: coconut granular charcoal manufactured by Taihei Chemical Sangyo Co., Ltd.) adsorbed with gold from the leachate leached from the concentrate was prepared.
- the Au quality in the activated carbon was 9000 g / ton, and the Ag quality was 1400 g / ton.
- FIGS. 1 and 2 The results of the concentration of the obtained gold and silver in the liquid are shown in FIGS. 1 and 2, respectively.
- FIG. 1 it can be seen that when elution is performed at 80 ° C., gold is better eluted from activated carbon than silver.
- the Au concentration in the solution was 160 mg / L and the Ag concentration was ⁇ 1 mg / L after 6 hours of elution.
- Elution at 80 ° C. not only separated gold and silver, but also improved the elution rate of Au.
- FIG. 1 it can be seen that when elution is performed at 80 ° C., gold is better eluted from activated carbon than silver.
- the Au concentration in the solution was 160 mg / L and the Ag concentration was ⁇ 1 mg / L after 6 hours of elution.
- Elution at 80 ° C. not only separated gold and silver, but also improved the elution rate of Au.
- FIG. 1 it can be seen that when elution is performed at 80
- Example 2 Activated carbon (coconut shell-derived activated carbon: coconut granular charcoal manufactured by Taihei Chemical Sangyo Co., Ltd.) adsorbed with gold from the leachate leached from the concentrate was prepared.
- the Au quality in the activated carbon was 9000 g / ton, and the Ag quality was 1400 g / ton.
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- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
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- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
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- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
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Abstract
Description
精鉱から金浸出した浸出液から金吸着した活性炭(ヤシ殻由来活性炭:太平化学産業社製ヤシコール 粒状炭)を準備した。活性炭中のAu品位は9000g/tonであり、Ag品位は1400g/tonであった。溶離液としては、pH=4の0.1Mチオ硫酸ナトリウム溶液を用いた。溶離液の温度は常温(20~30℃)及び80℃とした。この溶離液中に上述の活性炭を浸漬して攪拌した。試験開始から一時間毎にサンプリングを行い、溶離液中の金及び銀の濃度を測定した。測定はICP測定により行った。得られた金及び銀の液中濃度の結果を図1及び図2にそれぞれ示す。図1に示すように、80℃で溶離した場合、金が銀に対して活性炭からより多く良好に溶離していることがわかる。また、80℃で溶離した場合、溶離6時間で液中Au濃度は160mg/L、Ag濃度は<1mg/Lであった。80℃で溶離することにより、金及び銀を分離できるだけでなく、Auの溶離速度も向上した。一方、図2に示すように、常温で溶離した場合、銀が金に対して活性炭からより多く良好に溶離していることがわかる。また、常温で溶離した場合、溶離6時間で示した液中Au濃度20mg/Lが最大で後は再吸着しており、Ag濃度は最大25mg/Lを示して変化しなかった。銀に関しては活性炭中の銀を全量溶離したことになる。
精鉱から金浸出した浸出液から金吸着した活性炭(ヤシ殻由来活性炭:太平化学産業社製ヤシコール 粒状炭)を準備した。活性炭中のAu品位は9000g/tonであり、Ag品位は1400g/tonであった。溶離液としては、pH=4、6、8の0.1Mチオ硫酸ナトリウム溶液をそれぞれ用いた。溶離液の温度は80℃とした。この溶離液中に上述の活性炭を浸漬して攪拌した。試験開始から一時間毎にサンプリングを行い、溶離液中の金及び銀の濃度を測定した。測定はICP測定により行った。得られた金及び銀の液中濃度の結果を図3及び図4にそれぞれ示す。図3及び4に示すように、pHが8である溶離液で溶離した場合は、金及び銀のいずれも溶離が不良であった。
Claims (7)
- 少なくとも金及び銀が吸着した活性炭に対し、pH7未満に保持したチオ硫酸塩水溶液を用いて金と銀とを溶離させる活性炭に吸着された金及び銀の溶離方法。
- 前記チオ硫酸塩水溶液のpHが4以上7未満に保持されている請求項1に記載の活性炭に吸着された金及び銀の溶離方法。
- 前記チオ硫酸塩水溶液が20~90℃に保持されている請求項1又は2に記載の活性炭に吸着された金及び銀の溶離方法。
- 前記チオ硫酸塩水溶液を60~90℃に保持することで、前記活性炭に吸着した金を選択的に溶離して分離する請求項3に記載の活性炭に吸着された金及び銀の溶離方法。
- 前記チオ硫酸塩水溶液を20~50℃に保持することで、前記活性炭に吸着した銀を選択的に溶離して分離する請求項3に記載の活性炭に吸着された金及び銀の溶離方法。
- 前記チオ硫酸塩水溶液がチオ硫酸ナトリウム水溶液である請求項1~5のいずれかに記載の活性炭に吸着された金及び銀の溶離方法。
- 請求項1~6のいずれかに記載の活性炭に吸着された金及び銀の溶離方法で得られた金及び銀を含むチオ硫酸塩水溶液から金及び銀を回収する方法。
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2868296A CA2868296C (en) | 2012-03-30 | 2013-01-31 | Method of eluting gold and silver adsorbed on activated carbon and method of recovering gold and silver using the same |
AU2013201736A AU2013201736B2 (en) | 2011-11-16 | 2013-01-31 | Method of eluting gold and silver absorbed on activated carbon and method of recovering gold and silver using the same |
EP13769775.1A EP2832871A4 (en) | 2012-03-30 | 2013-01-31 | METHOD FOR ELIMINATING SILVER AND METALS ADDED BY ACTIVATED CARBON AND METHOD FOR RECOVERING SILVER AND OTHER METALS |
JP2014507477A JP5840764B2 (ja) | 2012-03-30 | 2013-01-31 | 活性炭に吸着された金及び銀の溶離方法及びそれを用いた金及び銀の回収方法 |
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JPPCT/JP2012/079857 | 2011-11-16 | ||
JP2012082295 | 2012-03-30 | ||
JP2012-082295 | 2012-03-30 | ||
JP2012079857 | 2012-11-16 |
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PCT/JP2013/052265 WO2013145849A1 (ja) | 2011-11-16 | 2013-01-31 | 活性炭に吸着された金及び銀の溶離方法及びそれを用いた金及び銀の回収方法 |
Country Status (6)
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EP (1) | EP2832871A4 (ja) |
JP (1) | JP5840764B2 (ja) |
CA (1) | CA2868296C (ja) |
CL (1) | CL2014002592A1 (ja) |
PE (1) | PE20142416A1 (ja) |
WO (1) | WO2013145849A1 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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US10392679B2 (en) | 2014-12-26 | 2019-08-27 | Jx Nippon Mining & Metals Corporation | Method for recovering gold from activated carbon |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6145828A (ja) | 1984-05-14 | 1986-03-05 | ウインドメ−レル ウント ヘルシエル | パレツトをその上に載置された物品例えば大袋と共に積上げる装置 |
JPH05311258A (ja) * | 1992-03-16 | 1993-11-22 | Nikko Kinzoku Kk | 銅電解アノードスライムの湿式処理方法 |
JP2009057588A (ja) * | 2007-08-30 | 2009-03-19 | Kobe Steel Ltd | 金属含有物から金属を回収する方法、および金属回収装置 |
JP2011105969A (ja) * | 2009-11-13 | 2011-06-02 | Sumitomo Metal Mining Co Ltd | 含銅硫化物からの銀の回収方法 |
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Publication number | Priority date | Publication date | Assignee | Title |
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US4778519A (en) * | 1987-02-24 | 1988-10-18 | Batric Pesic | Recovery of precious metals from a thiourea leach |
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2013
- 2013-01-31 EP EP13769775.1A patent/EP2832871A4/en not_active Withdrawn
- 2013-01-31 CA CA2868296A patent/CA2868296C/en active Active
- 2013-01-31 JP JP2014507477A patent/JP5840764B2/ja active Active
- 2013-01-31 WO PCT/JP2013/052265 patent/WO2013145849A1/ja active Application Filing
- 2013-01-31 PE PE2014001509A patent/PE20142416A1/es active IP Right Grant
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- 2014-09-26 CL CL2014002592A patent/CL2014002592A1/es unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS6145828A (ja) | 1984-05-14 | 1986-03-05 | ウインドメ−レル ウント ヘルシエル | パレツトをその上に載置された物品例えば大袋と共に積上げる装置 |
JPH05311258A (ja) * | 1992-03-16 | 1993-11-22 | Nikko Kinzoku Kk | 銅電解アノードスライムの湿式処理方法 |
JP2009057588A (ja) * | 2007-08-30 | 2009-03-19 | Kobe Steel Ltd | 金属含有物から金属を回収する方法、および金属回収装置 |
JP2011105969A (ja) * | 2009-11-13 | 2011-06-02 | Sumitomo Metal Mining Co Ltd | 含銅硫化物からの銀の回収方法 |
Non-Patent Citations (1)
Title |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10392679B2 (en) | 2014-12-26 | 2019-08-27 | Jx Nippon Mining & Metals Corporation | Method for recovering gold from activated carbon |
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CA2868296C (en) | 2018-01-23 |
JPWO2013145849A1 (ja) | 2015-12-10 |
CL2014002592A1 (es) | 2015-01-16 |
CA2868296A1 (en) | 2013-10-03 |
PE20142416A1 (es) | 2015-01-21 |
EP2832871A4 (en) | 2015-12-09 |
EP2832871A1 (en) | 2015-02-04 |
JP5840764B2 (ja) | 2016-01-06 |
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