CN1135533A - Method for recovering cobalt - Google Patents
Method for recovering cobalt Download PDFInfo
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- CN1135533A CN1135533A CN96100369A CN96100369A CN1135533A CN 1135533 A CN1135533 A CN 1135533A CN 96100369 A CN96100369 A CN 96100369A CN 96100369 A CN96100369 A CN 96100369A CN 1135533 A CN1135533 A CN 1135533A
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- cobalt
- organic phase
- ammonia
- back extraction
- extraction
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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
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- Manufacture And Refinement Of Metals (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The simple and effective method recovering cobalt from organic phase is characterized by mixing ammonia-ammonium carbonate aqueous solution and organic phase carrying cobalt to reextract the cobalt from them. The cobalt can be directly reextracted in the form of precipitation, also can be reextracted to water phase, then heated, the ammonia and carbon dioxide are evaporated, so that the cobalt compound can be deposited out. The recovered cobalt compound deposit can be roasted into cobalt oxide product or made into metal cobalt powder by using hydrogen reduction process or made into cathode cobalt by using electrodeposition process.
Description
The invention belongs to the recovery method of cobalt, particularly belong to from the method for organic phase back extraction cobalt.
Cobalt is widely used in aspects such as catalyzer, magneticsubstance, glass-ceramic pigment, various specific alloy and high temperature material.From various primary raw materialss and metallurgical byproduct or secondary resource, extract cobalt, need, particularly carry out just preparing high-purity cobalt oxide or other cobalt products after the nickel cobalt separates through purifying.Solvent extration is adopted in the purification of cobalt usually, makes extraction agent with organo phosphorous compounds, aminated compounds and fatty acid etc., realizes cobalt and other separate impurities.Wherein (2-ethylhexyl phosphoric acid (D2EHPA) and quaternary ammonium salt such as tri-n-octyl methyl ammonium chloride (Aliquat336) are the most frequently used cobalt extraction agent for organo phosphorous compounds such as 2-ethylhexyl phosphonic acid 2-ethylhexyl monoesters (M2EHPA), two.
From the organic phase of load cobalt, reclaim cobalt, traditional method is with the cobalt in the mineral acid back extraction organic phase, for example use sulfuric acid back extraction cobalt, again galvanic deposit cobalt (M.Ando, M.Takabashi and T.Gata from strip liquor, Separation ofCobalt from Nickel in NMC Process, Presented at the3rd International Symposium on Hydrometallurgy, March6-10,1983, Atlanta, USA); Or, from strip liquor, be settled out cobalt oxalate with oxalic acid again with hydrochloric acid back extraction cobalt, at last cobalt oxalate is sintered into cobalt oxide powder (Huang Qixing, Wang Lichuan, Zhu Dingyuan, " metallurgy of nickel ", China Science Tech Publishing House, 1990, Beijing).This class stripping method all will use the acid of higher concentration, especially when preparing cobalt oxide thus, also needs with the expensive like this reagent precipitate cobalt from strip liquor of oxalic acid, so that the production cost height.And the precipitation cobalt oxalate need be heated, and the organic phase behind the back extraction cobalt needs again with just returning extraction loop, complex operation after alkali or the ammonia saponification.
The objective of the invention is to provide a kind of economy, easy, effectively reclaim the cobalt novel method, preparation purity very high cobalt oxide or other cobalt products from organic phase.Novel method is back extraction cobalt from organic phase effectively, can easyly precipitate the cobalt of back extraction economically again and need not add any other reagent.The cobalt compound that is settled out can directly be sintered into high-purity cobalt oxide product, perhaps is processed into the cobalt metal with other known methods.For example make metal cobalt powder or electrodip process production negative electrode cobalt with hydrogen reduction method.
Method provided by the invention is to mix with the load cobalt organic phase that contains extraction agent or mix and back extraction cobalt wherein with ammonia-ammonium carbonate solution.The cobalt of back extraction or change water over to directly with the precipitation forms back extraction perhaps steams ammonia and carbonic acid gas by water through heating and is precipitated out from strip liquor.The cobalt compound precipitation that obtains under two kinds of situations all can directly be calcined and be obtained the cobalt oxide product, perhaps is processed into the cobalt metal with other currently known methodss.For example make metal cobalt powder or electrodip process production negative electrode cobalt with hydrogen reduction method.Ammonia and all recyclable additional strip liquor of carbonic acid gas that ammonia that produces during calcining and carbonic acid gas and strip liquor heating steam.Whole in theory back extraction prepares the cobalt oxide process and does not consume ammonia-volatile salt reverse-extraction agent.Strip liquor can replenish and return the back extraction operation behind ammonia and the carbonic acid gas and use behind the wherein sedimentary cobalt compound of Separation and Recovery.Organic extractant behind the back extraction cobalt can directly return cobalt extraction loop, need not be again with carbon or ammonia saponification.The concentration 0-10mol/L of ammonia, volatile salt concentration 0.1-6mol/L.
Stripping method provided by the invention is applicable to all kinds of SOLVENTS extraction system of cobalt, comprises the organic solution of organophosphorus compound, aminated compounds, fatty acid extraction agent etc.Here the extraction agent of enumerating is not the restriction to extraction agent just as an example.
With compare with the method for mineral acid back extraction cobalt in the existing solvent extraction, the present invention has the following advantages:
Simplified operation.Desire to precipitate into cobalt oxalate after the hydrochloric acid back extraction so that when being sintered into the cobalt oxide product, the cobalt strip liquor need pass through oxalic acid back extraction operation.The present invention can be combined into an operation with cobalt back extraction and cobalt precipitation, makes cobalt directly with the precipitation forms back extraction.
Reduced cost.During with the mineral acid back extraction, acid promptly is consumed, and extraction agent the time spent also need add in alkali or the ammonia and the proton of extraction agent again.And method of the present invention, the recyclable usefulness again of reverse-extraction agent ammonia-volatile salt does not consume when back extraction in theory.Simultaneously, from the solution of hydrochloric acid back extraction cobalt, precipitate the oxalic acid that cobalt oxalate need add the comparison costliness.Method of the present invention does not need to add any other reagent beyond the reverse-extraction agent, can direct back extraction become precipitation, or the strip liquor heating is boiled off the cobaltous dihydroxycarbonate precipitation that obtains behind ammonia and the carbonic acid gas, thereby has saved reagent, has reduced cost.
Embodiment 1:
Prepare cobalt oxide with method of the present invention from the load organic phases of solvent extraction and separation nickel cobalt.Organic phase is the 20v% kerosin of 2-ethylhexyl phosphonic acid 2-ethylhexyl monoesters (M2EHPA), and its cobalt lifting capacity is 12g/L.Load organic phases with contain 0.5mol/L ammonia, the aqueous solution of 0.5mol/L volatile salt mixes 30min, directly back extraction obtains the cobalt compound precipitation.After telling organic phase, filter water, filter cake washing, drying are calcined 3h down at 600 ℃ then, obtain the cobalt oxide product, and its cobalt contents and impurity component all meet the cobalt oxide product standard, as table 1.
The cobalt oxide main chemical compositions (%) that table 1 is produced
Co Ni Fe Cu Mn Pb
72 0.01 0.042?0.01?＜0.01?0.006
Ca Mg Na S
0.013?0.027?0.005?0.029
Embodiment 2:
With method of the present invention back extraction cobalt from the organic phase of load 10g/L Co.Organic phase is 0.8 mol/L Aliquat, 336 kerosins, and under the back extraction condition of embodiment 1, the cobalt back extraction ratio can reach more than 99%.After the heating strip liquor boils off ammonia and carbonic acid gas, the cobalt compound precipitation sulfuric acid dissolution that obtains.Solution is packed in the autoclave, depresses reduction at 150-200 ℃ and 2-6MPa hydrogen branch and obtains cobalt metal powder.Its main chemical compositions sees Table 2.
Table 2 hydrogen reduction metal powder main chemical compositions (%)
Co Ni Cu Fe Zn S
99.7 0.01 0.01 0.008?0.01 0.005
Claims (3)
1. the method for a back extraction cobalt from organic phase, it is characterized in that: mix with the load cobalt organic phase that contains extraction agent or mix with ammonia-ammonium carbonate solution, thereby change the cobalt in this organic phase over to water directly precipitation or be precipitated as cobalt compound through heating by water and reclaim.
2. as the method for claim 1 back extraction cobalt from organic phase, it is characterized in that described ammonia-ammonium carbonate solution, is the aqueous solution of ammonia and volatile salt, ammonia concentration 0-10mol/L wherein, volatile salt concentration 0.1-6mol/L.
3. as the method for claim 1 back extraction cobalt from organic phase, it is characterized in that described cobalt extraction agent is the organic solution of organo phosphorous compounds, aminated compounds and fatty acid extraction agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96100369A CN1101475C (en) | 1996-01-16 | 1996-01-16 | Method for recovering cobalt |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96100369A CN1101475C (en) | 1996-01-16 | 1996-01-16 | Method for recovering cobalt |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1135533A true CN1135533A (en) | 1996-11-13 |
| CN1101475C CN1101475C (en) | 2003-02-12 |
Family
ID=5116568
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96100369A Expired - Fee Related CN1101475C (en) | 1996-01-16 | 1996-01-16 | Method for recovering cobalt |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1101475C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8536381B2 (en) | 2008-09-12 | 2013-09-17 | Solvay Sa | Process for purifying hydrogen chloride |
| US8795536B2 (en) | 2008-01-31 | 2014-08-05 | Solvay (Societe Anonyme) | Process for degrading organic substances in an aqueous composition |
| US9309209B2 (en) | 2010-09-30 | 2016-04-12 | Solvay Sa | Derivative of epichlorohydrin of natural origin |
| US9663427B2 (en) | 2003-11-20 | 2017-05-30 | Solvay (Société Anonyme) | Process for producing epichlorohydrin |
| CN108360022A (en) * | 2018-05-02 | 2018-08-03 | 东北大学 | A kind of method that melten salt electriochemistry method recycles cobalt element in anode material of lithium battery |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ID827B (en) * | 1987-05-20 | 1996-07-25 | Meq Nickel Pty Ltd | SEPARATION AND REQUIREMENT OF NICKEL AND KOBAL BACK IN AMONIAC SYSTEMS |
| CA2134490C (en) * | 1993-10-29 | 2000-05-23 | John E. Fittock | Process for the preparation of a high purity cobalt intermediate |
| PH31603A (en) * | 1994-03-22 | 1998-11-03 | Goro Nickels S A | Process for the extraction and separation of nickel and/or cobalt. |
-
1996
- 1996-01-16 CN CN96100369A patent/CN1101475C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9663427B2 (en) | 2003-11-20 | 2017-05-30 | Solvay (Société Anonyme) | Process for producing epichlorohydrin |
| US8795536B2 (en) | 2008-01-31 | 2014-08-05 | Solvay (Societe Anonyme) | Process for degrading organic substances in an aqueous composition |
| US8536381B2 (en) | 2008-09-12 | 2013-09-17 | Solvay Sa | Process for purifying hydrogen chloride |
| US9309209B2 (en) | 2010-09-30 | 2016-04-12 | Solvay Sa | Derivative of epichlorohydrin of natural origin |
| CN108360022A (en) * | 2018-05-02 | 2018-08-03 | 东北大学 | A kind of method that melten salt electriochemistry method recycles cobalt element in anode material of lithium battery |
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| Publication number | Publication date |
|---|---|
| CN1101475C (en) | 2003-02-12 |
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