CN112342383B - Method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste - Google Patents
Method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste Download PDFInfo
- Publication number
- CN112342383B CN112342383B CN202010980593.8A CN202010980593A CN112342383B CN 112342383 B CN112342383 B CN 112342383B CN 202010980593 A CN202010980593 A CN 202010980593A CN 112342383 B CN112342383 B CN 112342383B
- Authority
- CN
- China
- Prior art keywords
- cobalt
- manganese
- nickel
- reaction
- lithium
- 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.)
- Active
Links
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 title claims abstract description 94
- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 73
- 239000011572 manganese Substances 0.000 title claims abstract description 69
- 239000002699 waste material Substances 0.000 title claims abstract description 66
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 title claims abstract description 65
- 229910052759 nickel Inorganic materials 0.000 title claims abstract description 55
- 229910052748 manganese Inorganic materials 0.000 title claims abstract description 54
- 238000000034 method Methods 0.000 title claims abstract description 42
- 229910017052 cobalt Inorganic materials 0.000 title claims abstract description 33
- 239000010941 cobalt Substances 0.000 title claims abstract description 33
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 title claims abstract description 33
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 238000006243 chemical reaction Methods 0.000 claims abstract description 104
- 239000000243 solution Substances 0.000 claims abstract description 78
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims abstract description 74
- KFDQGLPGKXUTMZ-UHFFFAOYSA-N [Mn].[Co].[Ni] Chemical compound [Mn].[Co].[Ni] KFDQGLPGKXUTMZ-UHFFFAOYSA-N 0.000 claims abstract description 62
- 239000002002 slurry Substances 0.000 claims abstract description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 39
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims abstract description 37
- 239000012045 crude solution Substances 0.000 claims abstract description 24
- 239000003153 chemical reaction reagent Substances 0.000 claims abstract description 21
- 239000011259 mixed solution Substances 0.000 claims abstract description 21
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 19
- 230000032683 aging Effects 0.000 claims abstract description 14
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 14
- 238000001556 precipitation Methods 0.000 claims abstract description 14
- 239000003513 alkali Substances 0.000 claims abstract description 13
- 238000002360 preparation method Methods 0.000 claims abstract description 12
- 150000003839 salts Chemical class 0.000 claims abstract description 10
- 239000012445 acidic reagent Substances 0.000 claims abstract description 6
- 238000003756 stirring Methods 0.000 claims description 71
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 37
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 30
- 239000007787 solid Substances 0.000 claims description 27
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 26
- 238000004537 pulping Methods 0.000 claims description 24
- -1 phosphate radical ions Chemical class 0.000 claims description 23
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 18
- 239000002253 acid Substances 0.000 claims description 17
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims description 16
- 238000005406 washing Methods 0.000 claims description 16
- 229910052739 hydrogen Inorganic materials 0.000 claims description 10
- 239000001257 hydrogen Substances 0.000 claims description 10
- 229910052742 iron Inorganic materials 0.000 claims description 10
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 9
- 229910001437 manganese ion Inorganic materials 0.000 claims description 9
- 229910017604 nitric acid Inorganic materials 0.000 claims description 9
- 229910052708 sodium Inorganic materials 0.000 claims description 4
- 229910019142 PO4 Inorganic materials 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 239000010452 phosphate Substances 0.000 claims description 3
- 239000002893 slag Substances 0.000 claims description 3
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical class [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 claims description 2
- 229910018661 Ni(OH) Inorganic materials 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 238000011084 recovery Methods 0.000 abstract description 15
- 238000001914 filtration Methods 0.000 description 28
- 239000012535 impurity Substances 0.000 description 24
- 238000002386 leaching Methods 0.000 description 17
- 230000001376 precipitating effect Effects 0.000 description 14
- 230000000052 comparative effect Effects 0.000 description 13
- 230000008569 process Effects 0.000 description 12
- 239000011734 sodium Substances 0.000 description 11
- 239000002244 precipitate Substances 0.000 description 10
- 238000000926 separation method Methods 0.000 description 9
- 239000003795 chemical substances by application Substances 0.000 description 7
- 150000002500 ions Chemical class 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000011230 binding agent Substances 0.000 description 6
- 238000000605 extraction Methods 0.000 description 6
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 5
- YUCQNFPMKWVCCP-UHFFFAOYSA-H cobalt(2+) manganese(2+) nickel(2+) diphosphate Chemical compound P(=O)([O-])([O-])[O-].[Ni+2].[Co+2].[Mn+2].P(=O)([O-])([O-])[O-] YUCQNFPMKWVCCP-UHFFFAOYSA-H 0.000 description 5
- 239000013078 crystal Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 229910001416 lithium ion Inorganic materials 0.000 description 4
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 238000005649 metathesis reaction Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910013716 LiNi Inorganic materials 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 239000011149 active material Substances 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- CPSYWNLKRDURMG-UHFFFAOYSA-L hydron;manganese(2+);phosphate Chemical compound [Mn+2].OP([O-])([O-])=O CPSYWNLKRDURMG-UHFFFAOYSA-L 0.000 description 2
- 150000002505 iron Chemical class 0.000 description 2
- 229910003002 lithium salt Inorganic materials 0.000 description 2
- 159000000002 lithium salts Chemical class 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 229910052723 transition metal Inorganic materials 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229910018119 Li 3 PO 4 Inorganic materials 0.000 description 1
- MKYBYDHXWVHEJW-UHFFFAOYSA-N N-[1-oxo-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propan-2-yl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(C(C)NC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 MKYBYDHXWVHEJW-UHFFFAOYSA-N 0.000 description 1
- 229910018060 Ni-Co-Mn Inorganic materials 0.000 description 1
- 229910018209 Ni—Co—Mn Inorganic materials 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- SOXUFMZTHZXOGC-UHFFFAOYSA-N [Li].[Mn].[Co].[Ni] Chemical compound [Li].[Mn].[Co].[Ni] SOXUFMZTHZXOGC-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000010405 anode material Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 229910000152 cobalt phosphate Inorganic materials 0.000 description 1
- ZBDSFTZNNQNSQM-UHFFFAOYSA-H cobalt(2+);diphosphate Chemical compound [Co+2].[Co+2].[Co+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O ZBDSFTZNNQNSQM-UHFFFAOYSA-H 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000009854 hydrometallurgy Methods 0.000 description 1
- 229910000398 iron phosphate Inorganic materials 0.000 description 1
- WBJZTOZJJYAKHQ-UHFFFAOYSA-K iron(3+) phosphate Chemical compound [Fe+3].[O-]P([O-])([O-])=O WBJZTOZJJYAKHQ-UHFFFAOYSA-K 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910000159 nickel phosphate Inorganic materials 0.000 description 1
- JOCJYBPHESYFOK-UHFFFAOYSA-K nickel(3+);phosphate Chemical compound [Ni+3].[O-]P([O-])([O-])=O JOCJYBPHESYFOK-UHFFFAOYSA-K 0.000 description 1
- 239000012074 organic phase Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000009210 therapy by ultrasound Methods 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 239000002351 wastewater Substances 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
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/006—Wet processes
- C22B7/007—Wet processes by acid leaching
-
- 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
- C22B23/0453—Treatment or purification of solutions, e.g. obtained by leaching
- C22B23/0461—Treatment or purification of solutions, e.g. obtained by leaching by chemical methods
-
- 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
- C22B26/00—Obtaining alkali, alkaline earth metals or magnesium
- C22B26/10—Obtaining alkali metals
- C22B26/12—Obtaining lithium
-
- 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
-
- 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
- C22B3/44—Treatment or purification of solutions, e.g. obtained by leaching by chemical processes
-
- 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
- C22B47/00—Obtaining manganese
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/54—Reclaiming serviceable parts of waste accumulators
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/84—Recycling of batteries or fuel cells
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Geochemistry & Mineralogy (AREA)
- Electrochemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention belongs to the technical field of lithium battery recovery, and discloses a method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste, which specifically comprises the following steps: (1) preparation of lithium-containing solution: adding water into the ternary waste to prepare slurry, adding a phosphoric acid mixed solution to adjust the pH of the slurry to be less than 4 after the slurry is prepared, then adding a reducing agent to carry out reaction, adding an alkali reagent A to adjust the pH to 7.0-11.0 after the reaction is completed, and then separating to obtain a lithium-containing solution and filter residue A; (2) preparing a nickel-cobalt-manganese refined solution: and (2) adding water into the filter residue A obtained in the step (1) to prepare slurry, adding ferric salt to perform double decomposition reaction after the slurry is prepared, adding an acid reagent to adjust the pH value of the system to 1.9-2.0 after the reaction is completed, aging and separating to obtain a nickel-cobalt-manganese crude solution and a filter residue B, continuously adding an alkali reagent B into the nickel-cobalt-manganese crude solution to adjust the pH value to 4.0-5.0 to perform precipitation, and separating to obtain a nickel-cobalt-manganese refined solution and a filter residue C.
Description
Technical Field
The invention relates to the technical field of lithium battery recovery, in particular to a method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste.
Background
With the rapid development of electric vehicles and large-scale energy storage markets, the sales volume of lithium ion batteries is rapidly increased, and the quantity of waste lithium ion batteries is increased day by day. The ternary positive lithium ion battery contains valuable metals such as nickel, cobalt, manganese, lithium and the like, and has high recovery value. In the hydrometallurgy technology, after the anode material of the waste lithium ion battery is leached, valuable metal elements exist in a leaching solution in an ionic state, and if the valuable metal elements are further recycled, different valuable metals such as nickel, cobalt, manganese, lithium and the like need to be selectively separated.
The prior technology for separating nickel, cobalt, manganese and lithium from ternary waste materials is as follows: reducing and leaching the ternary waste to obtain sulfate solutions of four metal elements of nickel, cobalt, manganese and lithium, extracting the three elements of nickel, cobalt and manganese at one time by taking P204 or P507 as an extracting agent and 260# solvent oil as a diluent, and performing back extraction by adopting a sulfuric acid solution to obtain a sulfate solution containing the three elements of nickel, cobalt and manganese, thereby realizing the separation of nickel, cobalt and manganese from the lithium element. However, the extraction process is complicated, the efficiency is low, a large amount of extraction reagents are needed, the price is high, the waste salt is large, the environment is easily polluted, the organic solvent is easy to volatilize, the operation condition is poor, and meanwhile, the lithium-containing solution obtained by the separation technology has high sodium content and is difficult to be directly used for preparing high-purity lithium salt products.
Therefore, further development of a low-cost, green, high-efficiency and industrialized nickel-cobalt-manganese and lithium separation technology is a problem to be solved in the field of valuable metal recovery in the current ternary waste.
Disclosure of Invention
In order to overcome the defects of the prior art, the invention aims to provide the method for separating and recovering nickel, cobalt, manganese and lithium from the ternary waste material, which has the advantages of simple process, environmental protection and high efficiency.
In order to achieve the purpose, the invention adopts the following technical scheme:
a method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste comprises the following steps:
(1) preparation of lithium-containing solution: adding water into the ternary waste to prepare slurry, adding a phosphoric acid mixed solution to adjust the pH of the slurry to be less than 4 after the slurry is prepared, then adding a reducing agent to carry out reaction, adding an alkali reagent A to adjust the pH to 7.0-11.0 after the reaction is completed, and then separating to obtain a lithium-containing solution and filter residue A;
(2) preparing a nickel-cobalt-manganese refined solution: and (2) adding water into the filter residue A obtained in the step (1) to prepare slurry, adding ferric salt to perform double decomposition reaction after the slurry is prepared, adding an acid reagent to adjust the pH value of the system to 1.9-2.0 after the reaction is completed, aging and separating to obtain a nickel-cobalt-manganese crude solution and a filter residue B, continuously adding an alkali reagent B into the nickel-cobalt-manganese crude solution to adjust the pH value to 4.0-5.0 to perform precipitation, and separating to obtain a nickel-cobalt-manganese refined solution and a filter residue C.
Preferably, the liquid-solid ratio of the ternary waste to water in the step (1) is 1.5: 1-10: 1.
Preferably, the pulping in the step (1) can be carried out in a stirring mode, and the stirring is carried out at a stirring speed of 120-900 r/min for 0.5-2 h.
Preferably, the phosphoric acid mixed solution in the step (1) may be obtained by mixing phosphoric acid and at least one of sulfuric acid, hydrochloric acid, nitric acid, and the like.
Preferably, PO is contained in the phosphoric acid mixed solution 4 3- The molar concentration of the ions is 1-4 mol/L; h in the phosphoric acid mixed solution + The total molar concentration of the ions is 2-6 mol/L.
Preferably, the reducing agent in step (1) may include Na 2 S、Na 2 SO 3 、Na 2 S 2 O 3 、H 2 O 2 And the like.
Preferably, the adding amount of the phosphoric acid mixed solution in the step (1) is 1.0-1.05 times of the total reaction equivalent of the phosphate radical ions and the nickel-cobalt-manganese ions, and is calculated by taking hydrogen ions as 1.0-1.1 times of the reaction equivalent; the addition amount of the reducing agent is 1.0-2.0 times of the reaction equivalent.
Preferably, the reaction in the step (1) is carried out for 1-5 hours at the reaction temperature of 50-80 ℃ and the stirring speed of 120-900 r/min.
Preferably, the alkali agent A in step (1) may comprise NaOH, KOH, NH 4 At least one of OH, LiOH and the like.
Preferably, the separation in step (1) can be carried out by conventional procedures such as filtration and centrifugation.
Further, the lithium-containing solution obtained in the step (1) can be used for producing lithium salt, and the obtained filter residue A is mixed solid of nickel-cobalt-manganese phosphate, carbon powder, binder and the like.
Preferably, the liquid-solid ratio of the filter residue A to water in the pulping process in the step (2) is 1.5: 1-10: 1.
Preferably, the pulping in the step (2) is carried out by stirring, the stirring speed is 120-900 r/min, and the stirring time is 0.5-2 h.
Preferably, the ferric salt in step (2) may comprise FeCl 3 、Fe 2 (SO 4 ) 3 、Fe(NO 3 ) 3 And the like.
Preferably, the amount of the ferric iron salt added in the double decomposition reaction in the step (2) is 1.0-1.2 times of the reaction equivalent of the iron ions and the phosphate ions.
Preferably, the reaction temperature of the double decomposition reaction in the step (2) is 50-80 ℃, and the reaction time is 1-5 h.
Preferably, the double decomposition reaction process in the step (2) can be stirred at a stirring speed of 120-900 r/min.
Preferably, the acid reagent in step (2) may comprise HCl or H 2 SO 4 、HNO 3 And the like.
Preferably, the aging time in the step (2) is 0.5-2.0 h.
Preferably, the residue B in the step (2) can be washed with dilute acid, and the washing water obtained after washing the residue can be used for next pulping.
Preferably, the dilute acid may comprise at least one of dilute hydrochloric acid, dilute sulfuric acid, dilute nitric acid, and the like.
Preferably, in the slag washing process, the pH value of the system is controlled to be 2.0-4.0.
Preferably, the alkali agent B in step (2) may comprise NaOH or NH 4 OH、Ni(OH) 2 、Mn(OH) 2 、Co(OH) 2 And the like.
Preferably, the separation in step (2) can be carried out by conventional procedures such as filtration and centrifugation.
Compared with the prior art, the invention has the following advantages and technical effects:
(1) according to the technical scheme, the mixed phosphoric acid solution is adopted to selectively leach lithium in the ternary waste, and meanwhile, the characteristic that the precipitation tendency of iron phosphate is far stronger than that of nickel phosphate, cobalt phosphate and manganese phosphate is utilized, so that the nickel-cobalt-manganese element and the nickel-cobalt-manganese phosphate are separated from the filter residue and converted into the nickel-cobalt-manganese solution through a one-step method, and high-valued operation is achieved. The method for separating and recovering nickel, cobalt, manganese and lithium provided by the invention has the advantages of simple process, low cost, high recovery rate of nickel, cobalt, manganese and lithium, low equipment requirement, low control precision requirement, small waste salt amount, solid state, no need of evaporation and drying treatment and the like.
(2) According to the technical scheme, an extraction reagent is not needed, impurities of a lithium-containing solution and a nickel-cobalt-manganese solution which are recycled due to the introduction of an organic phase are avoided, COD (chemical oxygen demand) wastewater and sodium sulfate waste salt which are generated due to the use of a large amount of the extraction reagent are avoided, and the environmental pollution is reduced.
Drawings
FIG. 1 is a process flow diagram for separating and recovering nickel, cobalt, manganese and lithium from ternary waste in example 1 of the present invention.
Detailed Description
The present invention will be described in further detail with reference to the following detailed description and examples, but the embodiments of the present invention are not limited thereto. All the raw materials and reagents used in the present invention are commercially available raw materials and reagents, unless otherwise specified. In the examples, the components are used in g and mL in parts by mass.
Preparation of lithium-containing solution:
according to an embodiment of the invention, the ternary waste and water are pulped, leaching rates of elements in the ternary waste are increased along with the increase of the liquid-solid ratio, but the leaching rates are increased continuously after the liquid-solid ratio reaches a certain ratio, so that the leaching rates are not changed greatly, and therefore, in order to maintain a high leaching rate and save the use of reagents, the liquid-solid ratio of the ternary waste to the water is 1.5: 1-10: 1, and is preferably 4: 1-6: 1.
According to an embodiment of the invention, the ternary waste and water are uniformly mixed in a stirring manner in the pulping process of the ternary waste and water, wherein the stirring speed is 120-900 r/min, and the stirring time is 0.5-2 h. In order to better disperse the ternary waste in water, the slurry can be subjected to ultrasonic treatment and heating treatment, for example, the slurry is treated for 30-120 min at 50-60 ℃ under the condition of 500-1000W of ultrasonic power.
Further, the ternary waste material can be pretreated before pulping. The pretreatment may include the steps of: heating the ternary waste at 380-500 ℃ for 30-120 min. The binder is generally an organic high molecular compound, such as PDVF, which has stable structure and chemical properties and is insoluble in strong acid and strong base, so that an ash layer is easily formed in the process of carrying out acid leaching reaction on the ternary waste, and the leaching of valuable metals is not facilitated. The binder can be decomposed by adopting a high-temperature treatment mode, so that the nickel-cobalt-manganese-lithium active material is fully exposed, the dispersibility is improved, and the leaching rate is improved.
According to one embodiment of the invention, a phosphoric acid mixed solution is used in combination with a reductant to perform a selective leaching reaction on the ternary waste. The reducing agent may comprise Na 2 S、Na 2 SO 3 、Na 2 S 2 O 3 、H 2 O 2 And the like. The main active material in the ternary waste is LiNi 1-x-y Co x Mn y O 2 (x+y<1) Wherein the chemical valence of the transition metal elements Ni, Co and Mn is +2, +3 and +4, and Co is required to be added 3+ 、Mn 4+ Reduced to low valence and can be completely dissolved by acid. The phosphoric acid mixed solution is prepared by adding at least one of sulfuric acid, hydrochloric acid, nitric acid and the like into phosphoric acid. Among them, sulfuric acid, hydrochloric acid, nitric acid and the like are strong acids, and LiNi is easily converted 1-x- y Co x Mn y O 2 The Li, Ni, Co and Mn elements in the solution are leached into the solution in the form of metal ions, and simultaneously H is provided for a reaction system + And adjusting the pH of the reaction system<4; phosphoric acid mainly provides PO for reaction system 4 3+， And Ni 2+ 、Co 2+ 、Mn 2+ Phosphate precipitation is formed, and Li + And PO 4 3+ At pH<4 can not be precipitated under the condition of 4, exists in the solution in the form of ions, thereby realizing the selective leaching of the ternary waste material, and the elements of Ni, Co and MnAnd separating from Li element.
With H 2 O 2 As an example of the reducing agent, the reaction equation is as follows:
6LiMeO 2 +18H + +4PO 4 3- +3H 2 O 2 →6Li + +2(Me) 3 (PO 4 ) 2 ↓+12H 2 O+3O 2 ↑
wherein Me is Ni, Co, Mn.
According to one embodiment of the invention, the addition amount of the reducing agent is 1.0-2.0 times of the reaction equivalent, and the sufficient addition amount of the reducing agent aims to thoroughly reduce high-valence Co and Mn into low-valence Co and Mn and improve the dissolution rate of Co and Mn; the adding amount of the phosphoric acid mixed solution is 1.0-1.05 times of the reaction equivalent of phosphate ions, the total adding amount of hydrogen ions is 1.0-1.1 times of the reaction equivalent, and the sufficient adding amount of the acid mainly aims at completely precipitating Ni, Co and Mn and improving the separation efficiency.
According to an embodiment of the present invention, after the reaction is completed, an alkaline reagent A is added to adjust the pH to 7.0-11.0, wherein the alkaline reagent B comprises NaOH, KOH, NH 4 At least one of OH, LiOH and the like, and the main purpose is to further completely precipitate nickel, cobalt and manganese phosphate and remove impurities from the system, and reduce impurities in the lithium-containing solution.
According to an embodiment of the invention, after the pH value of the alkali reagent A is adjusted to 7.0-11.0, a filtering operation is performed to obtain a lithium-containing solution and a filter residue A.
Preparing a nickel-cobalt-manganese refined solution:
according to an embodiment of the invention, filter residue A and water are pulped, the mass ratio of the filter residue A to the water in the pulping process is 1.5: 1-10: 1, pulping is carried out by stirring, the stirring speed is 120-900 r/min, and the stirring time is 0.5-2 h. The filter residue A is mixed solid of nickel cobalt manganese phosphate salt precipitate, carbon powder, binder and the like, and the pulping aims to fully disperse the nickel cobalt manganese phosphate salt precipitate in the solution and improve the reaction efficiency.
According to one embodiment of the present invention, the metathesis reaction is carried out after pulping by adding a ferric salt, which may include FeCl 3 、Fe 2 (SO 4 ) 3 、Fe(NO 3 ) 3 And the like. Using FePO 4 Much stronger precipitation tendency than Ni 3 (PO 4 ) 2 、Co 3 (PO 4 ) 2 、Mn 3 (PO 4 ) 2 The method is characterized in that Li, Ni and Co elements are replaced into ions from solid precipitates through double decomposition reaction and are dissolved in the solution, so that the Li, Ni and Co elements are separated from impurities such as carbon powder, a binder and the like, and a crude solution of nickel, cobalt and manganese and filter residue B are obtained.
The reaction equation for the metathesis reaction is as follows:
Me 3 (PO 4 ) 2 +2Fe 3+ +2H 2 O→FePO 4 ·2H 2 O↓+3Me 2+
wherein Me is Ni, Co or Mn.
According to an embodiment of the present invention, the amount of the trivalent iron salt added in the metathesis reaction is 1.0 to 1.2 times of the reaction equivalent. Adding a sufficient amount of a trivalent iron salt to effect Ni addition 3 (PO 4 ) 2 、Co 3 (PO 4 ) 2 、Mn 3 (PO 4 ) 2 The Ni, Co and Mn elements in the leaching solution are completely replaced, and the leaching efficiency is improved.
According to an embodiment of the present invention, after the double decomposition reaction is completed, an acid reagent is added to adjust the pH of the system to 1.9-2.0, and the system is aged for 0.5-2.0 h. The acid agent may include at least one of hydrochloric acid, sulfuric acid, nitric acid, and the like. During aging, FePO is reacted 4 ·2H 2 The small crystal grains of the O precipitate are gradually dissolved, the large crystal grains grow gradually, and the small crystal grains are adsorbed, occluded and occluded in FePO along with the dissolution of the small crystal grains 4 ·2H 2 Ni, Co and Mn ions in the O precipitation precipitate can be dissolved into the system again, thereby improving the recovery rate of Ni, Co and Mn and FePO 4 ·2H 2 Purity of O precipitated crystals.
According to an embodiment of the invention, the residue B is washed by dilute acid, and the washing water obtained after residue washing can be used for pulping the residue A next time. The dilute acid can be at least one of dilute sulfuric acid, dilute hydrochloric acid, dilute nitric acid and the like. The washing slagIn the process, the pH value of the system is controlled to be 2.0-4.0. Wherein the filter residue B is FePO 4 ·2H 2 Mixing solid of O precipitate and impurities such as carbon powder and binder, washing residue B with dilute strong acid to remove FePO in residue B 4 ·2H 2 Dissolving the O precipitate in washing water, reusing the O precipitate in pulping the filter residue A and water, and providing Fe for double decomposition reaction 3+ The reaction is carried out, so that the reagent is fully utilized, the reagent waste is reduced, and the cost is saved.
According to an embodiment of the present invention, the crude Ni-Co-Mn solution is precipitated by adding an alkali reagent to adjust the pH to 4.0-5.0. In the process of double decomposition reaction, in order to completely leach Ni, Co and Mn, excessive ferric salt is added, so that Fe also exists in the nickel-cobalt-manganese crude solution 3+ Thus adding an alkali agent to cause Fe 3+ Formation of Fe (OH) 3 (residue C) precipitation for impurity removal, since Fe (OH) 3 Much stronger precipitation tendency than Ni (OH) 2 、Co(OH) 2 、Mn(OH) 2 Therefore, under the condition that the pH value of the reaction system is 4.0-5.0, the added alkali reagent is preferentially mixed with Fe 3+ Formation of Fe (OH) 3 Precipitating, thereby obtaining the nickel-cobalt-manganese refined solution through filtering.
The following specific examples further illustrate the method for separating and recovering nickel, cobalt, manganese and lithium from the ternary waste material of the present invention, wherein the ternary waste material adopted in the examples comprises 7.2% of Li, 20.3% of Ni, 20.5% of Co and 19.0% of Mn.
Example 1: method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste
(1) Preparation of lithium-containing solution: stirring the ternary waste and water to prepare slurry with a liquid-solid ratio of 6:1, stirring for 1h at a stirring speed of 600r/min to obtain slurry, adding a phosphoric acid mixed solution (phosphoric acid is mixed with sulfuric acid, the adding amount of phosphate ions is controlled to be 1.05 times of the total reaction equivalent of the phosphate ions and the nickel-cobalt-manganese ions, and the total adding amount of hydrogen ions is 1.1 times of the reaction equivalent) into the slurry to adjust the pH of the system<4, continuing to add H 2 O 2 (H 2 O 2 The adding amount is 1.5 times of the reaction equivalent), and the stirring speed is 600r/min at the reaction temperature of 65 DEG CAnd (3) reacting for 3 hours, adding LiOH to adjust the pH of the system to 9.0 after the reaction is finished, further precipitating and removing impurities, and filtering to obtain a lithium-containing solution and filter residue A.
(2) Preparing a nickel-cobalt-manganese refined solution: adding water into the filter residue A obtained in the step (1) for pulping, wherein the liquid-solid ratio is 6:1, stirring for 1h at the stirring speed of 600r/min to obtain slurry, and then adding Fe into the slurry 2 (SO 4 ) 3 (Fe 2 (SO 4 ) 3 The adding amount is 1.1 times of the reaction equivalent of iron ions and phosphate ions) to carry out double decomposition reaction, the reaction is carried out for 3 hours under the conditions that the reaction temperature is 65 ℃ and the stirring speed is 600r/min, and then H is added 2 SO 4 Adjusting the pH value of the system to 1.9, aging for 1h, filtering to obtain a nickel-cobalt-manganese crude solution and a filter residue B, and then adding Mn (OH) into the nickel-cobalt-manganese crude solution 2 Adjusting the pH value of the system to 4.5, precipitating and removing impurities, and filtering to obtain a nickel-cobalt-manganese refined solution and filter residue C;
(3) slag washing: and (3) washing the filter residue B obtained in the step (2) with dilute sulfuric acid with the pH value of 3.0, and using washing water obtained after washing the filter residue for next pulping of the filter residue A and water.
FIG. 1 is a flow chart of the process for separating and recovering nickel, cobalt, manganese and lithium as ternary wastes in example 1.
Example 2: method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste
(1) Preparation of lithium-containing solution: stirring the ternary waste and water to prepare slurry with a liquid-solid ratio of 1.5:1, stirring for 0.5h at a stirring speed of 900r/min to obtain slurry, adding a phosphoric acid mixed solution (phosphoric acid is mixed with hydrochloric acid, the adding amount of phosphate ions is controlled to be 1.0 time of the total reaction equivalent of the phosphate ions and the nickel-cobalt-manganese ions, and the total adding amount of hydrogen ions is controlled to be 1.0 time of the reaction equivalent) into the slurry to adjust the pH of the system<4, continuing to add Na 2 S(Na 2 The adding amount of S is 1.0 time of the reaction equivalent), the reaction is carried out for 5 hours under the conditions that the reaction temperature is 80 ℃ and the stirring speed is 900r/min, NaOH is added after the reaction is finished to adjust the pH value of the system to be 11.0, the precipitation and the impurity removal are further carried out, and the lithium-containing solution and the filter residue A are obtained by filtering.
(2) Preparing a nickel-cobalt-manganese refined solution: adding water into the filter residue A obtained in the step (1) for pulping, wherein the liquid-solid ratio is 1.51, stirring for 0.5h at a stirring speed of 900r/min to obtain slurry, and adding FeCl into the slurry 3 (FeCl 3 The addition amount is 1.0 time of the reaction equivalent of iron ions and phosphate ions), carrying out double decomposition reaction, reacting for 5 hours at the reaction temperature of 80 ℃ and the stirring speed of 900r/min, then adding HCl to adjust the pH value of the system to be 2.0, aging for 2 hours, filtering to obtain a nickel-cobalt-manganese crude solution and a filter residue B, and then adding Co (OH) into the nickel-cobalt-manganese crude solution 2 And adjusting the pH value of the system to 4.0, precipitating, removing impurities, and filtering to obtain a nickel-cobalt-manganese refined solution and filter residue C.
Example 3: method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste
(1) Preparation of lithium-containing solution: stirring the ternary waste and water to prepare slurry with a liquid-solid ratio of 10:1, stirring for 2 hours at a stirring speed of 120r/min to obtain slurry, adding a phosphoric acid mixed solution (phosphoric acid is mixed with nitric acid, the adding amount of phosphate ions is controlled to be 1.03 times of the total reaction equivalent of the phosphate ions and the nickel-cobalt-manganese ions, and the total adding amount of hydrogen ions is controlled to be 1.05 times of the reaction equivalent) into the slurry to adjust the pH of the system<4, continuing to add Na 2 SO 3 (Na 2 SO 3 The adding amount is 2.0 times of the reaction equivalent), the reaction is carried out for 1 hour under the conditions that the reaction temperature is 50 ℃ and the stirring speed is 120r/min, and NH is added after the reaction is finished 4 And (4) regulating the pH value of the system to be 7.0 by OH, further precipitating and removing impurities, and filtering to obtain a lithium-containing solution and filter residue A.
(2) Preparing a nickel-cobalt-manganese refined solution: adding water into the filter residue A obtained in the step (1) for pulping, wherein the liquid-solid ratio is 10:1, stirring for 2 hours at a stirring speed of 120r/min to obtain slurry, and then adding Fe (NO) into the slurry 3 ) 3 (Fe(NO 3 ) 3 The addition amount is 1.05 times of the reaction equivalent of iron ions and phosphate ions) to carry out double decomposition reaction, the reaction is carried out for 1 hour under the conditions that the reaction temperature is 50 ℃ and the stirring speed is 900r/min, and then HNO is added 3 Adjusting the pH value of the system to 1.9, aging for 0.5h, filtering to obtain a nickel-cobalt-manganese crude solution and a filter residue B, and then adding Ni (OH) into the nickel-cobalt-manganese crude solution 2 And adjusting the pH value of the system to 5.0, precipitating, removing impurities, and filtering to obtain a nickel-cobalt-manganese refined solution and filter residue C.
Example 4: method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste
(1) Preparation of lithium-containing solution: pretreating ternary waste at 500 ℃ for 80min, stirring the ternary waste with water for pulping, wherein the liquid-solid ratio is 4:1, stirring the ternary waste at a stirring speed of 600r/min for 1h to obtain slurry, adding a phosphoric acid mixed solution (phosphoric acid is mixed with sulfuric acid, the adding amount of phosphate ions is controlled to be 1.05 times of the total reaction equivalent of the phosphate ions and the nickel-cobalt-manganese ions, and the total adding amount of hydrogen ions is controlled to be 1.1 times of the reaction equivalent) into the slurry to adjust the pH of the system<4, continuing to add H 2 O 2 (H 2 O 2 The adding amount is 1.5 times of the reaction equivalent), the reaction is carried out for 3 hours under the conditions that the reaction temperature is 65 ℃ and the stirring speed is 600r/min, KOH is added after the reaction is finished to adjust the pH value of the system to be 9.0, further precipitation and impurity removal are carried out, and the lithium-containing solution and the filter residue A are obtained by filtration.
(2) Preparing a nickel-cobalt-manganese refined solution: adding water into the filter residue A obtained in the step (1) for pulping, wherein the liquid-solid ratio is 6:1, stirring for 1h at the stirring speed of 600r/min to obtain slurry, and then adding Fe into the slurry 2 (SO 4 ) 3 (Fe 2 (SO 4 ) 3 The adding amount is 1.1 times of the reaction equivalent of iron ions and phosphate ions) to carry out double decomposition reaction, the reaction is carried out for 3 hours under the conditions that the reaction temperature is 65 ℃ and the stirring speed is 600r/min, and then H is added 2 SO 4 Adjusting the pH value of the system to 1.9, aging for 1h, filtering to obtain a nickel-cobalt-manganese crude solution and a filter residue B, and then adding NH into the nickel-cobalt-manganese crude solution 4 And (4) regulating the pH value of the system to be 4.5 by OH, precipitating, removing impurities, and filtering to obtain a nickel-cobalt-manganese refined solution and filter residue C.
Comparative example 1:
(1) preparation of lithium-containing solution: stirring the ternary waste and water to prepare slurry with a liquid-solid ratio of 6:1, stirring for 1h at a stirring speed of 600r/min to obtain slurry, adding a phosphoric acid mixed solution (phosphoric acid is mixed with sulfuric acid, the adding amount of phosphate ions is controlled to be 1.2 times of the total reaction equivalent of the phosphate ions and the nickel-cobalt-manganese ions, and the total adding amount of hydrogen ions is controlled to be 1.5 times of the reaction equivalent) into the slurry to adjust the pH of the system<4, continuing to add H 2 O 2 (H 2 O 2 The addition amount is reverse1.5 times of the equivalent), reacting for 3 hours at the reaction temperature of 65 ℃ and the stirring speed of 600r/min, adding LiOH to adjust the pH of the system to 9.0 after the reaction is finished, further precipitating and removing impurities, and filtering to obtain a lithium-containing solution and filter residue A.
(2) Preparing a nickel-cobalt-manganese refined solution: adding water into the filter residue A obtained in the step (1) for pulping, wherein the liquid-solid ratio is 6:1, stirring for 1h at the stirring speed of 600r/min to obtain slurry, and then adding Fe into the slurry 2 (SO 4 ) 3 (Fe 2 (SO 4 ) 3 The adding amount is 1.1 times of the reaction equivalent of iron ions and phosphate ions) to carry out double decomposition reaction, the reaction is carried out for 3 hours under the conditions that the reaction temperature is 65 ℃ and the stirring speed is 600r/min, and then H is added 2 SO 4 Adjusting the pH value of the system to 1.9, aging for 1h, filtering to obtain a nickel-cobalt-manganese crude solution and a filter residue B, and then adding Mn (OH) into the nickel-cobalt-manganese crude solution 2 And adjusting the pH value of the system to 4.5, precipitating, removing impurities, and filtering to obtain a nickel-cobalt-manganese refined solution and filter residue C.
Comparative example 2:
(1) preparation of lithium-containing solution: stirring the ternary waste and water for pulping with the liquid-solid ratio of 6:1, stirring for 1h at the stirring speed of 600r/min to obtain slurry, adding a phosphoric acid mixed solution (phosphoric acid is mixed with sulfuric acid, the adding amount of phosphate ions is controlled to be 0.9 time of the total reaction equivalent of the phosphate ions and the nickel-cobalt-manganese ions, and the total adding amount of hydrogen ions is controlled to be 0.9 time of the reaction equivalent) into the slurry to adjust the pH of the system<4, continuing to add H 2 O 2 (H 2 O 2 The adding amount is 1.5 times of the reaction equivalent), the reaction is carried out for 3 hours under the conditions that the reaction temperature is 65 ℃ and the stirring speed is 600r/min, after the reaction is finished, LiOH is added to adjust the pH value of the system to be 9.0, the precipitation and the impurity removal are further carried out, and the lithium-containing solution and the filter residue A are obtained by filtration.
(2) Preparing a nickel-cobalt-manganese refined solution: adding water into the filter residue A obtained in the step (1) for pulping, wherein the liquid-solid ratio is 6:1, stirring for 1h at the stirring speed of 600r/min to obtain slurry, and then adding Fe into the slurry 2 (SO 4 ) 3 (Fe 2 (SO 4 ) 3 The addition amount is 1.1 times of the reaction equivalent of the iron ions and the phosphate ions) to carry out double decomposition reactionReacting at 65 deg.C under stirring speed of 600r/min for 3H, and adding H 2 SO 4 Adjusting the pH value of the system to 1.9, aging for 1h, filtering to obtain a nickel-cobalt-manganese crude solution and a filter residue B, and then adding Mn (OH) into the nickel-cobalt-manganese crude solution 2 And adjusting the pH value of the system to 4.5, precipitating, removing impurities, and filtering to obtain a nickel-cobalt-manganese refined solution and filter residue C.
Comparative example 3:
(1) preparation of lithium-containing solution: stirring the ternary waste and water to prepare slurry with a liquid-solid ratio of 6:1, stirring for 1h at a stirring speed of 600r/min to obtain slurry, adding a phosphoric acid mixed solution (phosphoric acid is mixed with sulfuric acid, the adding amount of phosphate ions is controlled to be 1.05 times of the total reaction equivalent of the phosphate ions and the nickel-cobalt-manganese ions, and the total adding amount of hydrogen ions is 1.1 times of the reaction equivalent) into the slurry to adjust the pH of the system<4, continuing to add H 2 O 2 (H 2 O 2 The adding amount is 3.0 times of the reaction equivalent), the reaction is carried out for 3 hours under the conditions that the reaction temperature is 65 ℃ and the stirring speed is 600r/min, after the reaction is finished, LiOH is added to adjust the pH value of the system to be 9.0, the precipitation and the impurity removal are further carried out, and the lithium-containing solution and the filter residue A are obtained by filtration.
(2) Preparing a nickel-cobalt-manganese refined solution: adding water into the filter residue A obtained in the step (1) for pulping, wherein the liquid-solid ratio is 6:1, stirring for 1h at the stirring speed of 600r/min to obtain slurry, and then adding Fe into the slurry 2 (SO 4 ) 3 (Fe 2 (SO 4 ) 3 The adding amount is 1.1 times of the reaction equivalent of iron ions and phosphate ions) to carry out double decomposition reaction, the reaction is carried out for 3 hours under the conditions that the reaction temperature is 65 ℃ and the stirring speed is 600r/min, and then H is added 2 SO 4 Adjusting the pH value of the system to 1.9, aging for 1h, filtering to obtain a nickel-cobalt-manganese crude solution and a filter residue B, and then adding Mn (OH) into the nickel-cobalt-manganese crude solution 2 And adjusting the pH value of the system to 4.5, precipitating, removing impurities, and filtering to obtain a nickel-cobalt-manganese refined solution and filter residue C.
Comparative example 4:
(1) preparation of lithium-containing solution: stirring the ternary waste and water to prepare slurry with a liquid-solid ratio of 6:1, stirring for 1h at a stirring speed of 600r/min to obtain slurry, and then adding a phosphoric acid solution into the slurryAdjusting the pH of the system<4, continuing to add H 2 O 2 (H 2 O 2 The adding amount is 1.5 times of the reaction equivalent), the reaction is carried out for 3 hours under the conditions that the reaction temperature is 65 ℃ and the stirring speed is 600r/min, after the reaction is finished, LiOH is added to adjust the pH value of the system to be 9.0, the precipitation and the impurity removal are further carried out, and the lithium-containing solution and the filter residue A are obtained by filtration.
(2) Preparing a nickel-cobalt-manganese refined solution: adding water into the filter residue A obtained in the step (1) for pulping, wherein the liquid-solid ratio is 6:1, stirring for 1h at the stirring speed of 600r/min to obtain slurry, and then adding Fe into the slurry 2 (SO 4 ) 3 (Fe 2 (SO 4 ) 3 The adding amount is 1.1 times of the reaction equivalent of iron ions and phosphate ions) to carry out double decomposition reaction, the reaction is carried out for 3 hours under the conditions that the reaction temperature is 65 ℃ and the stirring speed is 600r/min, and then H is added 2 SO 4 Adjusting the pH value of the system to 1.9, aging for 1h, filtering to obtain a nickel-cobalt-manganese crude solution and a filter residue B, and then adding Mn (OH) into the nickel-cobalt-manganese crude solution 2 And adjusting the pH value of the system to 4.5, precipitating, removing impurities, and filtering to obtain a nickel-cobalt-manganese refined solution and filter residue C.
The lithium-containing solutions obtained in example 1, comparative example 2, and comparative example 3 and the residue a were subjected to content analysis of Li element, and the results are shown in table 1.
TABLE 1 Li content in Li-containing solution and residue A
| Example 1 (%) | Comparative example 1 (%) | Comparative example 2 (%) | Comparative example 3 (%) | |
| Lithium-containing solution | 21.4651 | 18.7736 | 17.2975 | 21.8142 |
| Residue A | 0.0147 | 0.2971 | 0.3882 | 0.0129 |
As can be seen from the data in Table 1, the phosphoric acid mixed solution of comparative example 1 was added in an excessive amount and PO was excessively added in comparison with example 1 4 3+ With Li + In the subsequent process of adjusting the pH value to 7.0-11.0 and removing impurities, PO is converted from an acidic condition to an alkaline condition 4 3+ With Li + Generation of Li 3 PO 4 Precipitating to reduce the content of Li in the lithium-containing solution and increase the content of Li in the filter residue A; ② compared with the embodiment 1, the phosphoric acid mixed solution of the comparative example 2 has insufficient addition amount, the Li element leaching amount in the ternary waste is reduced, thereby leading to the reduction of Li content in the Li-containing solution and the increase of Li content in the filter residue A, furthermore, because PO is adopted 4 3+ Insufficient, Ni, Co and Mn ions leached by acid are not completely precipitated, and the impurity content of Ni, Co and Mn in the lithium-containing solution is increased; ③ compared with the example 1, the reducing agent with the reaction equivalent of 3.0 times is added in the comparative example 3, but the Li content in the Li-containing solution is not increased significantly, furthermore, if the adding amount of the reducing agent is insufficient, the high-valence Co and Mn in the ternary waste material can not be reduced to low-valence completely, because the high-valence Co and Mn can not be leached by acid, the recovery rate of Co and Mn can be reduced, therefore, in order to save resources and ensure the recovery rate of Co and Mn, the reduction is controlled in the technical proposal of the inventionThe addition amount of the agent is 1.0-2.0 times of the reaction equivalent.
The lithium-containing solution and the nickel-cobalt-manganese refined solution prepared in examples 1 to 4 were subjected to Ni, Co, Mn, and Li content measurement, and the recovery rates of Ni, Co, Mn, and Li in the ternary wastes were calculated, and the results are shown in table 2.
TABLE 2 recovery of Ni, Co, Mn, Li from ternary wastes
As can be seen from the data in Table 2, in comparative example 4, the ternary waste is leached by using the single phosphoric acid, and the phosphoric acid is inorganic weak acid and has poor leaching effect on transition metals such as Ni, Co, Mn and the like, so that the leaching rate of Ni, Co, Mn and Li in the ternary waste is improved by using the phosphoric acid mixed strong acid as the leaching solution, and the leached Ni, Co and Mn ions can be mixed with PO 4 3- The formation of the nickel cobalt manganese phosphate precipitate is the premise of one-step separation and recovery of the nickel cobalt manganese solution in the technical scheme, thereby improving the recovery rate of Ni, Co and Mn.
As can be seen from the data of examples 1 to 4 in table 2, the recovery rates of Ni, Co, Mn, and Li in the technical scheme are high, the separation and recovery of nickel, cobalt, manganese, and lithium in the ternary waste can be well completed, and the technical problems of high cost and large environmental pollution caused by the separation and recovery by using an extraction agent in the prior art are solved.
The above embodiments are the best mode for carrying out the present invention, but the embodiments of the present invention are not limited to the above embodiments, and any other changes, modifications, substitutions, combinations, and simplifications which do not depart from the spirit and principle of the present invention should be regarded as equivalent substitutions and are included in the scope of the present invention.
Claims (8)
1. A method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste is characterized by comprising the following steps:
(1) preparation of lithium-containing solution: adding water into the ternary waste to prepare slurry, adding a phosphoric acid mixed solution to adjust the pH of the slurry to be less than 4 after the slurry is prepared, then adding a reducing agent to carry out reaction, adding an alkali reagent A to adjust the pH to 7.0-11.0 after the reaction is completed, and then separating to obtain a lithium-containing solution and filter residue A;
(2) preparing a nickel-cobalt-manganese refined solution: adding water into the filter residue A obtained in the step (1) to prepare slurry, adding ferric salt to perform double decomposition reaction after the slurry is prepared, adding an acid reagent to adjust the pH of the system to 1.9-2.0 after the reaction is completed, aging and separating to obtain a nickel-cobalt-manganese crude solution and a filter residue B, continuously adding an alkali reagent B into the nickel-cobalt-manganese crude solution to adjust the pH to 4.0-5.0 to perform precipitation, and separating to obtain a nickel-cobalt-manganese refined solution and a filter residue C;
the phosphoric acid mixed solution in the step (1) is obtained by mixing phosphoric acid and at least one of sulfuric acid, hydrochloric acid and nitric acid; the reducing agent comprises Na 2 S、Na 2 SO 3 、Na 2 S 2 O 3 、H 2 O 2 At least one of;
the adding amount of the phosphoric acid mixed solution in the step (1) is 1.0-1.05 times of the total reaction equivalent of the phosphate radical ions and the nickel-cobalt-manganese ions, and the adding amount is calculated by taking hydrogen ions as 1.0-1.1 times of the reaction equivalent; the addition amount of the reducing agent is 1.0-2.0 times of the reaction equivalent.
2. The method for separating and recovering nickel, cobalt, manganese and lithium in the ternary waste material as claimed in claim 1, wherein the method comprises the following steps: the liquid-solid ratio of the ternary waste to water in the step (1) is 1.5: 1-10: 1; the alkaline reagent A comprises NaOH, KOH and NH 4 At least one of OH and LiOH.
3. The method for separating and recovering nickel, cobalt, manganese and lithium in the ternary waste material as claimed in claim 1, wherein the method comprises the following steps: the reaction in the step (1) is carried out for 1-5 h under the conditions that the reaction temperature is 50-80 ℃ and the stirring speed is 120-900 r/min.
4. The method for separating and recovering nickel, cobalt, manganese and lithium in the ternary waste material as claimed in claim 1, wherein the method comprises the following steps: the ferric salt in the step (2) comprises FeCl 3 、Fe 2 (SO 4 ) 3 、Fe(NO 3 ) 3 At least one of; the addition amount of the ferric iron salt is calculated by 1.0-1.2 times of the reaction equivalent of iron ions and phosphate ions.
5. The method for separating and recovering nickel, cobalt, manganese and lithium in the ternary waste material as claimed in claim 1, wherein the method comprises the following steps: the reaction temperature of the double decomposition reaction in the step (2) is 50-80 ℃, and the reaction time is 1-5 h.
6. The method for separating and recovering nickel, cobalt, manganese and lithium in the ternary waste material as claimed in claim 1, wherein the method comprises the following steps: the acid reagent in the step (2) comprises HCl and H 2 SO 4 、HNO 3 At least one of; the aging time is 0.5-2.0 h.
7. The method for separating and recovering nickel, cobalt, manganese and lithium in the ternary waste material as claimed in claim 1, wherein the method comprises the following steps: washing the residue B in the step (2) by using dilute acid, and using washing water obtained after residue washing for pulping of the next residue A; the dilute acid comprises at least one of dilute hydrochloric acid, dilute sulfuric acid and dilute nitric acid; and in the slag washing process, the pH value of the system is 2.0-4.0.
8. The method for separating and recovering nickel, cobalt, manganese and lithium in the ternary waste material as claimed in claim 1, wherein the alkali reagent B in step (2) comprises NaOH and NH 4 OH、Ni(OH) 2 、Mn(OH) 2 、Co(OH) 2 At least one of (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010980593.8A CN112342383B (en) | 2020-09-17 | 2020-09-17 | Method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010980593.8A CN112342383B (en) | 2020-09-17 | 2020-09-17 | Method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN112342383A CN112342383A (en) | 2021-02-09 |
| CN112342383B true CN112342383B (en) | 2022-08-12 |
Family
ID=74357922
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010980593.8A Active CN112342383B (en) | 2020-09-17 | 2020-09-17 | Method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112342383B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114836620A (en) * | 2022-03-29 | 2022-08-02 | 上海电气集团股份有限公司 | Method for recycling lithium from waste battery |
| CN115747518A (en) * | 2022-12-09 | 2023-03-07 | 贵州红星电子材料有限公司 | Method for recovering nickel-cobalt-manganese-containing slag |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2014162982A (en) * | 2013-02-27 | 2014-09-08 | Jx Nippon Mining & Metals Corp | Method of separating and recovering metal from metal mixed solution |
| CN109473691A (en) * | 2018-09-29 | 2019-03-15 | 惠州亿纬锂能股份有限公司 | Waste and old ternary lithium battery selectively extraction recovery method |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5161361B1 (en) * | 2011-12-28 | 2013-03-13 | Ｊｘ日鉱日石金属株式会社 | Method for separating metal in mixed metal solution |
| CN106684485B (en) * | 2016-12-19 | 2020-04-21 | 天齐锂业股份有限公司 | Method for recycling waste lithium iron phosphate anode material by acid leaching method |
| CN110371943B (en) * | 2019-06-28 | 2021-03-09 | 湖南邦普循环科技有限公司 | Selective recovery process of nickel cobalt lithium manganate and lithium iron phosphate mixed waste |
| CN111082043A (en) * | 2019-11-26 | 2020-04-28 | 宁夏百川新材料有限公司 | Recycling method of waste nickel cobalt lithium manganate ternary battery positive electrode material |
| CN111270073A (en) * | 2020-02-03 | 2020-06-12 | 广东省稀有金属研究所 | Method for recovering valuable metals from leachate of waste lithium ion battery electrode material |
-
2020
- 2020-09-17 CN CN202010980593.8A patent/CN112342383B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2014162982A (en) * | 2013-02-27 | 2014-09-08 | Jx Nippon Mining & Metals Corp | Method of separating and recovering metal from metal mixed solution |
| CN109473691A (en) * | 2018-09-29 | 2019-03-15 | 惠州亿纬锂能股份有限公司 | Waste and old ternary lithium battery selectively extraction recovery method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN112342383A (en) | 2021-02-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN113912032B (en) | Method for recycling and preparing battery-grade lithium carbonate and ferric phosphate from waste lithium iron phosphate battery positive electrode powder | |
| WO2022161087A1 (en) | Method for separating nickel and iron from nickel-iron alloy and use | |
| CN111924817A (en) | Method for comprehensively utilizing waste lithium iron phosphate anode material | |
| CN111129632A (en) | Method for recycling anode and cathode mixed materials of waste ternary lithium ion battery | |
| CN109052492B (en) | Method for preparing ternary cathode material from laterite nickel ore nitric acid leaching solution | |
| CN106654205B (en) | Method for preparing ternary positive electrode material precursor by using waste lithium battery material | |
| CN112320780B (en) | Method for recycling iron phosphate waste | |
| CN108767353B (en) | Method for producing lithium-rich clean liquid from anode active material of waste lithium ion battery | |
| CN106848473A (en) | A kind of selective recovery method of lithium in waste lithium iron phosphate battery | |
| CN112342383B (en) | Method for separating and recovering nickel, cobalt, manganese and lithium in ternary waste | |
| CN113912033A (en) | Method for recycling anode and cathode mixed powder of waste lithium iron phosphate battery with pre-positioned lithium extraction | |
| CN115196609B (en) | Method for recovering iron phosphate from lithium iron phosphate lithium extraction slag and application thereof | |
| CN111471856A (en) | Method for one-step acid leaching of laterite-nickel ore and co-production of lithium iron phosphate positive active material | |
| CN115744864A (en) | Method for efficiently recycling and reusing waste lithium iron phosphate battery positive electrode material | |
| CN115747521A (en) | Method for recovering and preparing lithium carbonate from waste lithium ion battery positive electrode material | |
| CN112725621B (en) | Method for separating nickel, cobalt and manganese from waste lithium battery based on carbonate solid-phase conversion method | |
| CN113716539A (en) | Method for preparing iron phosphate precursor by using zinc hydrometallurgy high-iron solution | |
| CN115784188A (en) | Method for recycling and preparing battery-grade iron phosphate | |
| CN115535987B (en) | Method for recycling valuable elements from lithium iron manganese phosphate positive electrode waste | |
| CN115709979B (en) | Method for preparing battery-grade manganese iron phosphate by taking high-iron manganese ore as raw material | |
| CN115261605B (en) | Recovery method of lithium iron phosphate | |
| CN116675197B (en) | Method for preparing ferric phosphate from iron phosphate slag after lithium extraction from waste lithium iron phosphate anode powder | |
| CN114988382B (en) | Recovery method of waste lithium iron phosphate battery powder | |
| WO2023005031A1 (en) | Preparation method for nickel-cobalt-manganese ternary precursor material and lithium ion battery | |
| CN114976337A (en) | Comprehensive recovery method of scrapped lithium iron phosphate |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Separation and Recovery Method of Nickel, Cobalt, Manganese and Lithium in Ternary Waste Effective date of registration: 20230424 Granted publication date: 20220812 Pledgee: Huaxia Bank Co.,Ltd. Jingmen Branch Pledgor: Hubei Jinquan New Material Co.,Ltd. Registration number: Y2023980039070 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Granted publication date: 20220812 Pledgee: Huaxia Bank Co.,Ltd. Jingmen Branch Pledgor: Hubei Jinquan New Material Co.,Ltd. Registration number: Y2023980039070 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |