WO2024036906A1 - Lithium-ion battery positive electrode material and preparation method therefor - Google Patents
Lithium-ion battery positive electrode material and preparation method therefor Download PDFInfo
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- WO2024036906A1 WO2024036906A1 PCT/CN2023/077442 CN2023077442W WO2024036906A1 WO 2024036906 A1 WO2024036906 A1 WO 2024036906A1 CN 2023077442 W CN2023077442 W CN 2023077442W WO 2024036906 A1 WO2024036906 A1 WO 2024036906A1
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- Prior art keywords
- lithium
- manganese
- ferricyanide
- ion battery
- source
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- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 229910001416 lithium ion Inorganic materials 0.000 title claims abstract description 42
- 238000002360 preparation method Methods 0.000 title claims abstract description 21
- 239000007774 positive electrode material Substances 0.000 title claims abstract description 8
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims abstract description 101
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 61
- -1 potassium ferricyanide Chemical compound 0.000 claims abstract description 45
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 36
- 239000004642 Polyimide Substances 0.000 claims abstract description 34
- 229920001721 polyimide Polymers 0.000 claims abstract description 34
- 239000003945 anionic surfactant Substances 0.000 claims abstract description 30
- 229910052744 lithium Inorganic materials 0.000 claims abstract description 28
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 238000000034 method Methods 0.000 claims abstract description 22
- 238000006243 chemical reaction Methods 0.000 claims abstract description 15
- 238000000498 ball milling Methods 0.000 claims abstract description 9
- ISPYRSDWRDQNSW-UHFFFAOYSA-L manganese(II) sulfate monohydrate Chemical compound O.[Mn+2].[O-]S([O-])(=O)=O ISPYRSDWRDQNSW-UHFFFAOYSA-L 0.000 claims abstract description 9
- 239000001267 polyvinylpyrrolidone Substances 0.000 claims abstract description 9
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 claims abstract description 9
- 229920000036 polyvinylpyrrolidone Polymers 0.000 claims abstract description 9
- 238000003756 stirring Methods 0.000 claims abstract description 7
- 238000004448 titration Methods 0.000 claims abstract description 7
- 239000011572 manganese Substances 0.000 claims description 38
- 239000010406 cathode material Substances 0.000 claims description 32
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 13
- 229910052748 manganese Inorganic materials 0.000 claims description 9
- MQRWBMAEBQOWAF-UHFFFAOYSA-N acetic acid;nickel Chemical compound [Ni].CC(O)=O.CC(O)=O MQRWBMAEBQOWAF-UHFFFAOYSA-N 0.000 claims description 7
- XIXADJRWDQXREU-UHFFFAOYSA-M lithium acetate Chemical compound [Li+].CC([O-])=O XIXADJRWDQXREU-UHFFFAOYSA-M 0.000 claims description 7
- 229940078494 nickel acetate Drugs 0.000 claims description 7
- YAGKRVSRTSUGEY-UHFFFAOYSA-N ferricyanide Chemical compound [Fe+3].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] YAGKRVSRTSUGEY-UHFFFAOYSA-N 0.000 claims description 3
- 150000007942 carboxylates Chemical class 0.000 claims description 2
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 claims description 2
- 229910052808 lithium carbonate Inorganic materials 0.000 claims description 2
- 229910000008 nickel(II) carbonate Inorganic materials 0.000 claims description 2
- ZULUUIKRFGGGTL-UHFFFAOYSA-L nickel(ii) carbonate Chemical compound [Ni+2].[O-]C([O-])=O ZULUUIKRFGGGTL-UHFFFAOYSA-L 0.000 claims description 2
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 30
- 229910052742 iron Inorganic materials 0.000 abstract description 13
- 230000008569 process Effects 0.000 abstract description 10
- 230000008859 change Effects 0.000 abstract description 8
- 239000010410 layer Substances 0.000 abstract description 7
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 abstract description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 4
- 229910052799 carbon Inorganic materials 0.000 abstract description 4
- AHKZTVQIVOEVFO-UHFFFAOYSA-N oxide(2-) Chemical compound [O-2] AHKZTVQIVOEVFO-UHFFFAOYSA-N 0.000 abstract description 4
- 239000003792 electrolyte Substances 0.000 abstract description 3
- 238000005406 washing Methods 0.000 abstract description 2
- 230000032683 aging Effects 0.000 abstract 1
- 239000011247 coating layer Substances 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 238000001914 filtration Methods 0.000 abstract 1
- 230000035882 stress Effects 0.000 abstract 1
- 239000000047 product Substances 0.000 description 21
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 16
- 230000000052 comparative effect Effects 0.000 description 12
- 239000000203 mixture Substances 0.000 description 12
- 229910018663 Mn O Inorganic materials 0.000 description 11
- 229910003176 Mn-O Inorganic materials 0.000 description 11
- 239000002243 precursor Substances 0.000 description 11
- 239000012071 phase Substances 0.000 description 9
- 239000002994 raw material Substances 0.000 description 9
- 239000007795 chemical reaction product Substances 0.000 description 8
- 239000004094 surface-active agent Substances 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 239000002131 composite material Substances 0.000 description 6
- 239000006185 dispersion Substances 0.000 description 6
- 238000002156 mixing Methods 0.000 description 5
- 239000011268 mixed slurry Substances 0.000 description 4
- 229910007960 Li-Fe Inorganic materials 0.000 description 3
- 229910006564 Li—Fe Inorganic materials 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 3
- 229910017052 cobalt Inorganic materials 0.000 description 3
- 239000010941 cobalt Substances 0.000 description 3
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 3
- 125000001165 hydrophobic group Chemical group 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000002736 nonionic surfactant Substances 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 238000010532 solid phase synthesis reaction Methods 0.000 description 3
- VMSIYTPWZLSMOH-UHFFFAOYSA-N 2-(dodecoxymethyl)oxirane Chemical compound CCCCCCCCCCCCOCC1CO1 VMSIYTPWZLSMOH-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 2
- 229910000625 lithium cobalt oxide Inorganic materials 0.000 description 2
- BFZPBUKRYWOWDV-UHFFFAOYSA-N lithium;oxido(oxo)cobalt Chemical compound [Li+].[O-][Co]=O BFZPBUKRYWOWDV-UHFFFAOYSA-N 0.000 description 2
- 239000002086 nanomaterial Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- GPLRAVKSCUXZTP-UHFFFAOYSA-N diglycerol Chemical compound OCC(O)COCC(O)CO GPLRAVKSCUXZTP-UHFFFAOYSA-N 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 231100000086 high toxicity Toxicity 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002563 ionic surfactant Substances 0.000 description 1
- PVFSDGKDKFSOTB-UHFFFAOYSA-K iron(3+);triacetate Chemical compound [Fe+3].CC([O-])=O.CC([O-])=O.CC([O-])=O PVFSDGKDKFSOTB-UHFFFAOYSA-K 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229940071257 lithium acetate Drugs 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 229940071125 manganese acetate Drugs 0.000 description 1
- UOGMEBQRZBEZQT-UHFFFAOYSA-L manganese(2+);diacetate Chemical compound [Mn+2].CC([O-])=O.CC([O-])=O UOGMEBQRZBEZQT-UHFFFAOYSA-L 0.000 description 1
- SKHFIRJPDRRLST-UHFFFAOYSA-N manganese(2+);dicyanide Chemical compound [Mn+2].N#[C-].N#[C-] SKHFIRJPDRRLST-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- ONJQDTZCDSESIW-UHFFFAOYSA-N polidocanol Chemical compound CCCCCCCCCCCCOCCOCCOCCOCCOCCOCCOCCOCCOCCO ONJQDTZCDSESIW-UHFFFAOYSA-N 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/362—Composites
- H01M4/366—Composites as layered products
-
- 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
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/131—Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/139—Processes of manufacture
- H01M4/1391—Processes of manufacture of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
- H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
- H01M4/525—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/028—Positive electrodes
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the present application relates to the field of battery materials, and specifically to a lithium-ion battery cathode material and a preparation method thereof.
- Lithium cobalt oxide is the earliest commercialized cathode material for lithium-ion batteries. It has high energy density and performance. However, due to the high toxicity of cobalt itself and low resource content, in order to reduce the cost of the material, nickel and manganese elements are used. Lithium cobalt oxide is doped and modified to reduce the relative content of cobalt element. At the same time, the three metal elements can have a synergistic effect, and the prepared ternary material can also produce good electrochemical performance.
- the prepared Li-Fe-Ni-Mn-O material has properties comparable to commercial ternary materials, and at the same time, the production cost is higher. Low, higher security.
- the introduction of iron element will directly cause the morphology of the ternary material to change, making it impossible to maintain a good layered structure, resulting in the inability to guarantee its electrochemical stability during use; at the same time, the iron element itself is also unstable to a certain extent. properties, impurities are prone to appear during the product preparation process, affecting product performance.
- the purpose of this application is to provide a preparation method for a lithium-ion battery cathode Li-Fe-Ni-Mn-O composite material with a layered structure.
- the preparation method uses ferricyanide with special morphology. Manganese oxide is used as the basic structure, and a cross-linked nitrogen-containing polymer polyimide and a specific surfactant are introduced to mix the precursors.
- Ni-Mn-O composite material the synthesis route of this material is simple, and the multi-layered sheet structure is conducive to electrolysis Full contact with the liquid can also effectively alleviate the stress caused by the volume change of the cathode material during the charge and discharge process; in addition, through the doping and stabilization of the nickel phase and the manganese phase, the iron phase in the material can be effectively stabilized in the oxide ion framework It maintains a higher valence state, and the nitrogen-containing coating carbon layer with high conductivity can achieve higher charge and discharge capacity.
- a method for preparing cathode materials for lithium-ion batteries including the following steps:
- the manganese ferricyanide obtained by the method has a special cubic nanostructure. At the same time, the structure is hollow inside. When it is combined with When the nickel source and lithium source contact and react, the reaction diffusion degree of lithium ions can be effectively improved.
- the cubic hollow nanostructure collapses due to stress and gradually transforms into The multi-layer flake structure layer fragments effectively increase the area of the product when in contact with the electrolyte and alleviate the volume change stress of the material during charge and discharge; in addition, the existing iron-doped Li-Fe-Ni-Mn-O or Li-Fe -The iron phase in the Co-Ni-Mn-O material is difficult to maintain a high valence state.
- the iron source is introduced in the form of manganese ferricyanide, and the iron phase can be made possible through the combination of manganese and nickel in the raw material. Effectively maintained in the oxide ion framework, the charge and discharge capacity of the overall material is effectively improved.
- the lithium source is usually introduced into the precursor by ball milling. Although this method is simple to operate, it can easily lead to a uniform mixture. The degree is poor and causes more loss of raw materials.
- the existing solutions mostly involve the introduction of organic solvents and some surface Surfactants serve as dispersants to alleviate particle agglomeration, but for components dissolved in the solvent, they will be lost as the solvent evaporates or is lost, while for insoluble components, they will still gradually disappear during the ball milling process. Staying at the bottom of the reaction vessel, the improvement in dispersion is limited.
- the preparation method of the product of this application uses polyimide as the intermediary.
- polyimide When water is used as the dispersed phase, polyimide can effectively cross-link or entrap each Li-Fe - Ni-Mn-O ternary cathode material precursor, and maintains good dispersion under the action of hydrophobic groups generated by anionic surfactants (because anionic surfactants easily generate hydrophobic groups in water, for water-soluble Polyimide can effectively cross-link precursor sources when dissolved in water. Oil-soluble polyimide can also be stably dispersed in water in the form of molecules under the action of hydrophobic groups. And enveloping each precursor source, both modes of action can effectively improve the dispersion of the precursor source during mixing). After high-temperature sintering, the polyimide is converted into a nitrogen-containing conductive carbon layer. In addition to playing a role in the material structure In addition to being protective, it can also effectively improve the conductivity of the overall material.
- the ratio of the moles of manganese sulfate monohydrate to the mass of polyvinylpyrrolidone in the solution A is (0.0025 ⁇ 0.0035) mol: (1 ⁇ 5)g, and the concentration of the solution A is 10 ⁇ 15g/L .
- the concentration of the potassium ferricyanide solution is 5-10 g/L.
- the Li-Fe-Ni-Mn-O composite material prepared through the above raw material ratio has a relatively high manganese element content, which can effectively improve the discharge capacity and cycle stability of the overall material.
- the nickel source is at least one of nickel acetate and nickel carbonate;
- the lithium source is at least one of lithium acetate and lithium carbonate.
- the anionic surfactant is a carboxylate anionic surfactant, a sulfonate anionic surfactant at least one of the sub-surfactants.
- Another object of the present application is to provide a lithium-ion battery cathode material prepared by the method for preparing a lithium-ion battery cathode material.
- the lithium-ion battery cathode material Li-Fe-Ni-Mn-O composite material prepared by the method described in this application constructs an ideal multi-layered structure through special raw material selection and synthesis process, which effectively ensures that the product can deintercalate lithium ions. Stable performance in the process.
- the iron phase in the obtained material has higher stability and the overall material purity is higher.
- due to the nitrogen The introduction of elements significantly improves the conductivity of the overall material.
- Another object of the present application is to provide a lithium-ion battery positive electrode sheet, which is prepared from the lithium-ion battery positive electrode material described in the present application.
- the beneficial effect of this application is that it provides a method for preparing a lithium-ion battery cathode material with a layered structure.
- the preparation method uses manganese ferricyanide with special morphology as the basic structure and introduces cross-linked nitrogen-containing materials.
- polymer polyimide and specific anionic surfactants as precursors, a Li-Fe-Ni-Mn-O composite material with a multi-layered sheet structure can be effectively obtained through a high-temperature solid phase method. This material has multiple properties.
- the lamellar structure is conducive to full contact with the electrolyte, and can also effectively alleviate the stress caused by the volume change of the cathode material during the charge and discharge process; in addition, the iron phase in the material can be effectively stabilized in the oxide ion framework and maintained
- the higher valence state, combined with the high conductivity nitrogen-containing carbon layer, can increase the charge and discharge capacity. higher.
- the resulting mixed slurry is dried at room temperature for 24 hours and then placed in an air atmosphere and kept at 850°C for 18 hours to obtain the lithium ion battery cathode material; wherein each mixture
- the materials of each example and comparative example were mixed with conductive carbon black and PVDF according to a mass ratio of 8:1:1, and an appropriate amount of NMP was added to adjust the slurry, and then coated
- the positive electrode piece was prepared by cutting it after drying on the aluminum foil. Lithium metal was used as the negative electrode piece and commercial polypropylene film was used as the separator to assemble the lithium ion button half battery. After the resulting battery was left to stand for 12 hours, it was heated for 2 to 2 hours at room temperature. 100 charge-discharge cycle tests were conducted under the condition of 4.5V voltage and 0.2C rate, then the rate was increased to 1C for 5 cycles, and finally returned to 0.2C for 5 cycles. The results are shown in Table 1.
- Example 1 From the comparison of the product performance of Example 1, Example 5 and Example 6, it can be seen that as the addition amount of polyimide and surfactant increases too much, the dispersion of each precursor of the product is better, and the nitrogen doping content It also becomes higher, but relatively speaking, it may cause each precursor to be completely separated from the water phase during the mixing process, and the degree of uniform mixing will become lower, and the cycle performance and rate performance of the product will also be affected.
- the product of Comparative Example 1 uses ordinary raw materials to prepare the product. Although surfactant and polyimide are finally introduced, the overall effect is poor, the product has poor cycle performance, low initial capacity and The rate performance is poor. Comparative Examples 2 and 3 did not introduce surfactant and polyimide respectively during the grinding and mixing process of the precursor.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Composite Materials (AREA)
- Manufacturing & Machinery (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
The present application relates to the field of battery materials, and disclosed thereby are a lithium-ion battery positive electrode material and a preparation method therefor. The preparation method comprises the following steps: (1) using water to prepare a solution A of manganese sulfate monohydrate and polyvinylpyrrolidone, adding a potassium ferricyanide solution into the solution A in a titration form, stirring, and reacting, and after the reaction is complete, aging, filtering, and washing to obtain manganese ferricyanide; and (2) using water to uniformly disperse the manganese ferricyanide, a nickel source, a lithium source, a polyimide, and an anionic surfactant, carrying out ball milling, then maintaining at 750-950° for 15-20 h, and obtaining the lithium-ion battery positive electrode material. The material has a multi-layer sheet-like structure that promotes sufficient contact with an electrolyte. The material may also effectively relieve the stress caused by the change in volume of the positive electrode material during charging and discharging processes. In addition, an iron phase in the material may be effectively stabilized in an oxide ion framework and maintain a high valence state, and the charge and discharge capacity may be improved when used in cooperation with a highly conductive nitrogen-containing carbon coating layer.
Description
本申请涉及电池材料领域,具体涉及一种锂离子电池正极材料及其制备方法。The present application relates to the field of battery materials, and specifically to a lithium-ion battery cathode material and a preparation method thereof.
钴酸锂是最早商业化的锂离子电池正极材料,其具有较高的能量密度和使用性能,但由于钴元素本身毒性高且资源含量少,为了降低材料的成本,人们以镍和锰元素进行钴酸锂的掺杂改性以减少钴元素的相对含量,同时三种金属元素可发生协同效应,制备的三元材料也能产生不错的电化学性能。Lithium cobalt oxide is the earliest commercialized cathode material for lithium-ion batteries. It has high energy density and performance. However, due to the high toxicity of cobalt itself and low resource content, in order to reduce the cost of the material, nickel and manganese elements are used. Lithium cobalt oxide is doped and modified to reduce the relative content of cobalt element. At the same time, the three metal elements can have a synergistic effect, and the prepared ternary material can also produce good electrochemical performance.
随着人们研究逐渐深入,人们开始采用铁元素完全代替三元材料中的钴元素,制备得到的Li-Fe-Ni-Mn-O材料具有与商业三元材料相媲美的性能,同时生产成本更低,安全性更高。然而,铁元素的引入会直接导致三元材料的形貌发生改变,无法维持良好的层状结构,导致无法保障其在使用过程中的电化学稳定性;同时铁元素本身也具有一定的不稳定性,在制备产品过程中容易出现杂相,影响产品性能。As people's research gradually deepens, people begin to use iron element to completely replace the cobalt element in ternary materials. The prepared Li-Fe-Ni-Mn-O material has properties comparable to commercial ternary materials, and at the same time, the production cost is higher. Low, higher security. However, the introduction of iron element will directly cause the morphology of the ternary material to change, making it impossible to maintain a good layered structure, resulting in the inability to guarantee its electrochemical stability during use; at the same time, the iron element itself is also unstable to a certain extent. properties, impurities are prone to appear during the product preparation process, affecting product performance.
发明内容Contents of the invention
以下是对本文详细描述的主题的概述。本概述并非是为了限制权利要求的保护范围。The following is an overview of the topics described in detail in this article. This summary is not intended to limit the scope of the claims.
基于现有技术的不足,本申请的目的在于提供了一种具有层状结构的锂离子电池正极Li-Fe-Ni-Mn-O复合材料的制备方法,该制备方法以特殊形貌的铁氰化锰作为基础结构,同时引入交联型含氮聚合物聚酰亚胺及特定的表面活性剂进行前驱体的混合,经高温固相法可以有效得到具有多层片状结构的Li-Fe-Ni-Mn-O复合材料,该材料合成路径简单,同时多层片状结构有利于电解
液的充分接触,也可有效缓解正极材料在充放电过程中的体积变化带来的应力;此外,通过镍相和锰相的掺杂稳定,材料中的铁相可有效稳定在氧化物离子框架中并保持较高的价态,配合高导电率的含氮包覆碳层可使充放电容量更高。Based on the shortcomings of the existing technology, the purpose of this application is to provide a preparation method for a lithium-ion battery cathode Li-Fe-Ni-Mn-O composite material with a layered structure. The preparation method uses ferricyanide with special morphology. Manganese oxide is used as the basic structure, and a cross-linked nitrogen-containing polymer polyimide and a specific surfactant are introduced to mix the precursors. Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe-Li-Fe from a multi-layer sheet-like structure can be obtained through a high-temperature solid-phase method. Ni-Mn-O composite material, the synthesis route of this material is simple, and the multi-layered sheet structure is conducive to electrolysis Full contact with the liquid can also effectively alleviate the stress caused by the volume change of the cathode material during the charge and discharge process; in addition, through the doping and stabilization of the nickel phase and the manganese phase, the iron phase in the material can be effectively stabilized in the oxide ion framework It maintains a higher valence state, and the nitrogen-containing coating carbon layer with high conductivity can achieve higher charge and discharge capacity.
为了达到上述目的,本申请采取的技术方案为:In order to achieve the above purpose, the technical solutions adopted by this application are:
一种锂离子电池正极材料的制备方法,包括以下步骤:A method for preparing cathode materials for lithium-ion batteries, including the following steps:
(1)将一水硫酸锰和聚乙烯吡咯烷酮用水配制溶液A,以滴定形式在溶液A中加入铁氰化钾溶液并搅拌反应,待反应完全后,陈化,过滤,洗涤,得铁氰化锰;(1) Prepare solution A with manganese sulfate monohydrate and polyvinylpyrrolidone with water. Add potassium ferricyanide solution to solution A in titration form and stir the reaction. After the reaction is complete, age, filter, and wash to obtain ferricyanide. manganese;
(2)将铁氰化锰、镍源、锂源、聚酰亚胺以及阴离子表面活性剂用水分散均匀并进行球磨处理,随后经750~950℃下保温15~20h,即得所述锂离子电池正极材料。(2) Disperse manganese ferricyanide, nickel source, lithium source, polyimide and anionic surfactant evenly with water and perform ball milling treatment, and then maintain the temperature at 750-950°C for 15-20 hours to obtain the lithium ions Battery cathode material.
本申请所述锂离子电池正极材料的制备方法中,通过所述方法得到的铁氰化锰除了作为铁源和锰源外,其具有特殊的立方纳米结构,同时该结构内部空心,当其与镍源及锂源接触反应时,可有效提升锂离子的反应扩散程度,而在最终Li-Fe-Ni-Mn-O复合材料烧结合成时,该立方空心纳米结构因应力发生崩塌,逐渐转化成多层片状结构层碎片,有效提升产品在电解液接触时的面积并缓解材料在充放电的体积变化应力;此外,现有铁掺杂的Li-Fe-Ni-Mn-O或Li-Fe-Co-Ni-Mn-O材料中铁相难以维持较高的价态,而本申请技术方案中以铁氰化锰的形式引入铁源,通过锰和原料中的镍元素的搭配使得铁相可有效保持在氧化物离子框架中,整体材料的充放电容量有效提升。In the preparation method of the lithium-ion battery cathode material described in the present application, in addition to being an iron source and a manganese source, the manganese ferricyanide obtained by the method has a special cubic nanostructure. At the same time, the structure is hollow inside. When it is combined with When the nickel source and lithium source contact and react, the reaction diffusion degree of lithium ions can be effectively improved. When the final Li-Fe-Ni-Mn-O composite material is sintered and synthesized, the cubic hollow nanostructure collapses due to stress and gradually transforms into The multi-layer flake structure layer fragments effectively increase the area of the product when in contact with the electrolyte and alleviate the volume change stress of the material during charge and discharge; in addition, the existing iron-doped Li-Fe-Ni-Mn-O or Li-Fe -The iron phase in the Co-Ni-Mn-O material is difficult to maintain a high valence state. However, in the technical solution of this application, the iron source is introduced in the form of manganese ferricyanide, and the iron phase can be made possible through the combination of manganese and nickel in the raw material. Effectively maintained in the oxide ion framework, the charge and discharge capacity of the overall material is effectively improved.
另一方面,由于传统固相法合成三元材料或Li-Fe-Ni-Mn-O材料的过程中锂源通常以球磨方法引入前驱体,这种方法虽然操作简单,但非常容易导致混合物均匀度差且造成较多原料损失。现有的解决办法多是引入有机溶剂及一些表
面活性剂作为分散剂缓解颗粒团聚,但是对于溶解于溶剂的组分,其会随着溶剂的挥发或损耗也随着发生损耗,而对于不溶解的组分,在球磨过程中其依然会逐渐停留在反应器皿底部,分散度提升有限,因此本申请产品的制备方法采用聚酰亚胺作为中介体,在水作为分散相的情况下,聚酰亚胺可有效交联或裹挟各Li-Fe-Ni-Mn-O三元正极材料前驱体,并在阴离子表面活性剂生成的憎水基团的作用下保持良好的分散性(由于阴离子表面活性剂在水中容易生成憎水基团,对于水溶性聚酰亚胺,其在水中溶解时可有效交联各前驱体源,而对于油溶性质的聚酰亚胺,在憎水基团的作用下,其也可以稳定以分子形式分散在水中并裹挟各前驱体源,两种作用方式均可有效提升前驱体源在混合时的分散性),在经过高温烧结后,聚酰亚胺转化为含氮导电碳层,除了起到材料结构的保护性外,还能有效提升整体材料的导电性。On the other hand, in the process of synthesizing ternary materials or Li-Fe-Ni-Mn-O materials using traditional solid-phase methods, the lithium source is usually introduced into the precursor by ball milling. Although this method is simple to operate, it can easily lead to a uniform mixture. The degree is poor and causes more loss of raw materials. The existing solutions mostly involve the introduction of organic solvents and some surface Surfactants serve as dispersants to alleviate particle agglomeration, but for components dissolved in the solvent, they will be lost as the solvent evaporates or is lost, while for insoluble components, they will still gradually disappear during the ball milling process. Staying at the bottom of the reaction vessel, the improvement in dispersion is limited. Therefore, the preparation method of the product of this application uses polyimide as the intermediary. When water is used as the dispersed phase, polyimide can effectively cross-link or entrap each Li-Fe - Ni-Mn-O ternary cathode material precursor, and maintains good dispersion under the action of hydrophobic groups generated by anionic surfactants (because anionic surfactants easily generate hydrophobic groups in water, for water-soluble Polyimide can effectively cross-link precursor sources when dissolved in water. Oil-soluble polyimide can also be stably dispersed in water in the form of molecules under the action of hydrophobic groups. And enveloping each precursor source, both modes of action can effectively improve the dispersion of the precursor source during mixing). After high-temperature sintering, the polyimide is converted into a nitrogen-containing conductive carbon layer. In addition to playing a role in the material structure In addition to being protective, it can also effectively improve the conductivity of the overall material.
可选地,所述溶液A中一水硫酸锰的摩尔与聚乙烯吡咯烷酮的质量之比为(0.0025~0.0035)mol:(1~5)g,所述溶液A的浓度为10~15g/L。Optionally, the ratio of the moles of manganese sulfate monohydrate to the mass of polyvinylpyrrolidone in the solution A is (0.0025~0.0035) mol: (1~5)g, and the concentration of the solution A is 10~15g/L .
可选地,所述铁氰化钾溶液的浓度为5~10g/L。Optionally, the concentration of the potassium ferricyanide solution is 5-10 g/L.
可选地,所述铁氰化锰中铁元素和锰元素之和与镍源中镍元素的摩尔比为n(Mn+Fe):n(Ni)=(9:1)~(8:2)。Optionally, the molar ratio of the sum of iron elements and manganese elements in the manganese ferricyanide to the nickel element in the nickel source is n(Mn+Fe): n(Ni)=(9:1)~(8:2) .
可选地,所述铁氰化锰、镍源中锰元素、铁元素、镍元素与锂源中锂元素的摩尔比为:n(Mn+Fe+Ni):n(Li)=1:(1~1.05)。Optionally, the molar ratio of manganese element, iron element, nickel element in the manganese ferricyanide, nickel source and lithium element in the lithium source is: n(Mn+Fe+Ni):n(Li)=1:( 1~1.05).
通过上述原料比例制备的Li-Fe-Ni-Mn-O复合材料锰元素含量占比较高,可有效提升整体材料的放电容量及循环稳定性。The Li-Fe-Ni-Mn-O composite material prepared through the above raw material ratio has a relatively high manganese element content, which can effectively improve the discharge capacity and cycle stability of the overall material.
可选地,所述镍源为醋酸镍、碳酸镍中的至少一种;所述锂源为醋酸锂、碳酸锂中的至少一种。Optionally, the nickel source is at least one of nickel acetate and nickel carbonate; the lithium source is at least one of lithium acetate and lithium carbonate.
可选地,所述阴离子表面活性剂为羧酸盐阴离子表面活性剂、磺酸盐阴离
子表面活性剂中的至少一种。Optionally, the anionic surfactant is a carboxylate anionic surfactant, a sulfonate anionic surfactant at least one of the sub-surfactants.
可选地,铁氰化锰、镍源、锂源、聚酰亚胺以及阴离子表面活性剂的质量之比为:m(铁氰化锰+镍源+锂源):m(聚酰亚胺):m(阴离子表面活性剂)=1:(0.4~0.6):(0.4~0.6)。Optionally, the mass ratio of manganese ferricyanide, nickel source, lithium source, polyimide and anionic surfactant is: m (manganese ferricyanide + nickel source + lithium source): m (polyimide ): m (anionic surfactant)=1: (0.4~0.6): (0.4~0.6).
聚酰亚胺以及阴离子表面活性剂的适量引入可以有效提升原料在分散过程中的分散性和均匀性,同时也不会造成原料可与水体体系完全分离,造成粘附在研磨壁的情况。The introduction of appropriate amounts of polyimide and anionic surfactants can effectively improve the dispersion and uniformity of the raw materials during the dispersion process. At the same time, it will not cause the raw materials to be completely separated from the water system and adhere to the grinding wall.
本申请的另一目的还在于提供所述锂离子电池正极材料的制备方法制备得到的锂离子电池正极材料。Another object of the present application is to provide a lithium-ion battery cathode material prepared by the method for preparing a lithium-ion battery cathode material.
本申请所述方法制备的锂离子电池正极材料Li-Fe-Ni-Mn-O复合材料通过特殊的原料选择及合成工艺构建出理想的多层层状结构,有效保障产品在进行锂离子脱嵌过程中的稳定性能,同时由于以铁氰化锰的形式引入铁源,以及采用含N聚合物作为辅助加工试剂,所得材料中的铁相稳定性较高且整体材料纯度较高,同时由于氮元素的引入使得整体材料的导电性也显著提升。The lithium-ion battery cathode material Li-Fe-Ni-Mn-O composite material prepared by the method described in this application constructs an ideal multi-layered structure through special raw material selection and synthesis process, which effectively ensures that the product can deintercalate lithium ions. Stable performance in the process. At the same time, due to the introduction of iron source in the form of manganese ferricyanide and the use of N-containing polymers as auxiliary processing reagents, the iron phase in the obtained material has higher stability and the overall material purity is higher. At the same time, due to the nitrogen The introduction of elements significantly improves the conductivity of the overall material.
本申请的再一目的还在于提供一种锂离子电池正极极片,所述正极极片由本申请所述锂离子电池正极材料制备得到。Another object of the present application is to provide a lithium-ion battery positive electrode sheet, which is prepared from the lithium-ion battery positive electrode material described in the present application.
本申请的有益效果在于,本申请提供了一种具有层状结构的锂离子电池正极材料的制备方法,该制备方法以特殊形貌的铁氰化锰作为基础结构,同时引入交联型含氮聚合物聚酰亚胺及特定的阴离子表面活性剂进行前驱体的混合,经高温固相法可以有效得到具有多层片状结构的Li-Fe-Ni-Mn-O复合材料,该材料具有多层片状结构,有利于和电解液充分接触,也可有效缓解正极材料在充放电过程中的体积变化带来的应力;此外,材料中的铁相可有效稳定在氧化物离子框架中并保持较高的价态,配合高导电率的含氮包覆碳层可使充放电容量
更高。The beneficial effect of this application is that it provides a method for preparing a lithium-ion battery cathode material with a layered structure. The preparation method uses manganese ferricyanide with special morphology as the basic structure and introduces cross-linked nitrogen-containing materials. By mixing polymer polyimide and specific anionic surfactants as precursors, a Li-Fe-Ni-Mn-O composite material with a multi-layered sheet structure can be effectively obtained through a high-temperature solid phase method. This material has multiple properties. The lamellar structure is conducive to full contact with the electrolyte, and can also effectively alleviate the stress caused by the volume change of the cathode material during the charge and discharge process; in addition, the iron phase in the material can be effectively stabilized in the oxide ion framework and maintained The higher valence state, combined with the high conductivity nitrogen-containing carbon layer, can increase the charge and discharge capacity. higher.
在阅读并理解了详细描述后,可以明白其他方面。Other aspects will become apparent after reading and understanding the detailed description.
为了更好地说明本申请的目的、技术方案和优点,下面将结合具体实施例及对比例对本申请作进一步说明,其目的在于详细地理解本申请的内容,而不是对本申请的限制。本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本申请的保护范围。本申请实施、对比例所设计的实验试剂、原料及仪器,除非特别说明,均为常用的普通试剂、原料及仪器。In order to better explain the purpose, technical solutions and advantages of the present application, the present application will be further described below in conjunction with specific embodiments and comparative examples. The purpose is to understand the content of the present application in detail, but not to limit the present application. All other embodiments obtained by those of ordinary skill in the art without creative efforts fall within the protection scope of this application. The experimental reagents, raw materials and instruments designed for the implementation and comparative examples of this application are all commonly used common reagents, raw materials and instruments unless otherwise specified.
实施例1Example 1
本申请所述锂离子电池正极材料及其制备方法的一种实施例,包括以下步骤:An embodiment of the lithium-ion battery cathode material and its preparation method described in the present application includes the following steps:
(1)将0.003mol一水硫酸锰和3g聚乙烯吡咯烷酮用水和少量乙醇配制浓度为12g/L的溶液A,以滴定形式在溶液A中加入12g/L铁氰化钾溶液并搅拌反应直至溶液浑浊度不再改变,待反应完全后,常温陈化24h,过滤,用水和乙醇分别洗涤,干燥后,得铁氰化锰;(1) Prepare solution A with a concentration of 12g/L by adding 0.003mol manganese sulfate monohydrate and 3g polyvinylpyrrolidone with water and a small amount of ethanol. Add 12g/L potassium ferricyanide solution to solution A in titration form and stir the reaction until the solution The turbidity will no longer change. After the reaction is complete, it is aged at room temperature for 24 hours, filtered, washed with water and ethanol respectively, and dried to obtain manganese ferricyanide;
(2)将铁氰化锰、醋酸镍、醋酸锂、聚酰亚胺以及阴离子表面活性剂十二烷基缩水甘油醚DEG(森菲达化工)置于球磨罐中,加入5倍质量的水分散均匀并采用行星式球磨仪以200rpm的速率进行球磨处理24h,所得混合浆料常温干燥24h后置入空气气氛中经850℃下保温18h,即得所述锂离子电池正极材料;其中各混合料中金属元素的根据理论反应产品化合式Li(Mn0.48Fe0.32Ni0.2)O2计算各元素比为n(Mn+Fe+Ni):n(Li)=1:1,n(Mn+Fe):n(Ni)=8:2;铁氰化锰、镍源、锂源、聚酰亚胺以及阴离子表面活性剂的质量之比为:m(铁氰化锰+镍源+锂源):m(聚酰亚胺):m(阴离子表面活性剂)=1g:0.5g:0.5g。
(2) Place manganese ferricyanide, nickel acetate, lithium acetate, polyimide and anionic surfactant dodecyl glycidyl ether DEG (Senfida Chemical) in a ball mill tank, and add 5 times the mass of water Disperse evenly and use a planetary ball mill to ball mill at a rate of 200 rpm for 24 hours. The resulting mixed slurry is dried at room temperature for 24 hours and then placed in an air atmosphere and kept at 850°C for 18 hours to obtain the lithium ion battery cathode material; wherein each mixture According to the theoretical reaction product formula of the metal elements in the material, Li(Mn 0.48 Fe 0.32 Ni 0.2 )O 2, the ratio of each element is calculated as n(Mn+Fe+Ni): n(Li)=1:1, n(Mn+Fe ): n (Ni) = 8:2; the mass ratio of manganese ferricyanide, nickel source, lithium source, polyimide and anionic surfactant is: m (manganese ferricyanide + nickel source + lithium source) :m (polyimide): m (anionic surfactant) = 1g: 0.5g: 0.5g.
实施例2Example 2
本实施例与实施例1的差别仅在于,各混合料中金属元素的根据理论反应产品化合式Li(Mn0.51Fe0.34Ni0.15)O2计算各元素比为n(Mn+Fe+Ni):n(Li)=1:1,n(Mn+Fe):n(Ni)=8.5:1.5。The only difference between this embodiment and Example 1 is that the ratio of each element in each mixture is calculated as n(Mn+Fe+Ni) based on the theoretical reaction product formula Li(Mn 0.51 Fe 0.34 Ni 0.15 )O 2 : n(Li)=1:1, n(Mn+Fe):n(Ni)=8.5:1.5.
实施例3Example 3
本实施例与实施例1的差别仅在于,各混合料中金属元素的根据理论反应产品化合式Li(Mn0.54Fe0.36Ni0.1)O2计算各元素比为n(Mn+Fe+Ni):n(Li)=1:1,n(Mn+Fe):n(Ni)=9:1。The only difference between this embodiment and Example 1 is that the ratio of each element of the metal elements in each mixture is n(Mn+Fe+Ni) calculated based on the theoretical reaction product formula Li(Mn 0.54 Fe 0.36 Ni 0.1 )O 2: n(Li)=1:1, n(Mn+Fe): n(Ni)=9:1.
实施例4Example 4
本实施例与实施例1的差别仅在于,各混合料中金属元素的根据理论反应产品化合式Li(Mn0.57Fe0.38Ni0.05)O2计算各元素比为n(Mn+Fe+Ni):n(Li)=1:1,n(Mn+Fe):n(Ni)=9.5:0.5。The only difference between this embodiment and Example 1 is that the ratio of each element in each mixture is calculated as n(Mn+Fe+Ni) based on the theoretical reaction product formula Li(Mn 0.57 Fe 0.38 Ni 0.05 )O 2 : n(Li)=1:1, n(Mn+Fe):n(Ni)=9.5:0.5.
实施例5Example 5
本实施例与实施例1的差别仅在于,铁氰化锰、镍源、锂源、聚酰亚胺以及阴离子表面活性剂的质量之比为:m(铁氰化锰+镍源+锂源):m(聚酰亚胺):m(阴离子表面活性剂)=1g:0.6g:0.6g。The only difference between this embodiment and Example 1 is that the mass ratio of manganese ferricyanide, nickel source, lithium source, polyimide and anionic surfactant is: m (manganese ferricyanide + nickel source + lithium source ): m (polyimide): m (anionic surfactant) = 1g: 0.6g: 0.6g.
实施例6Example 6
本实施例与实施例1的差别仅在于,铁氰化锰、镍源、锂源、聚酰亚胺以及阴离子表面活性剂的质量之比为:m(铁氰化锰+镍源+锂源):m(聚酰亚胺):m(阴离子表面活性剂)=1g:0.8g:0.8g。The only difference between this embodiment and Example 1 is that the mass ratio of manganese ferricyanide, nickel source, lithium source, polyimide and anionic surfactant is: m (manganese ferricyanide + nickel source + lithium source ): m (polyimide): m (anionic surfactant) = 1g: 0.8g: 0.8g.
对比例1Comparative example 1
一种锂离子电池正极材料及其制备方法,包括以下步骤:A lithium-ion battery cathode material and a preparation method thereof, including the following steps:
将醋酸铁、醋酸锰、醋酸镍、醋酸锂、聚酰亚胺以及阴离子表面活性剂十
二烷基甘油醚置于球磨罐中,加入5倍质量的水分散均匀并采用行星式球磨仪以200rpm的速率进行球磨处理24h,所得混合浆料常温干燥24h后置入空气气氛中经850℃下保温18h,即得所述锂离子电池正极材料;其中各混合料中金属元素的根据理论反应产品化合式Li(Mn0.48Fe0.32Ni0.2)O2计算各元素比为n(Mn+Fe+Ni):n(Li)=1:1,n(Mn+Fe):n(Ni)=8:2;铁源、锰源、镍源、锂源、聚酰亚胺以及阴离子表面活性剂的质量之比为:m(铁源+锰源+镍源+锂源):m(聚酰亚胺):m(阴离子表面活性剂)=1g:0.5g:0.5g。Combine iron acetate, manganese acetate, nickel acetate, lithium acetate, polyimide and anionic surfactants. Place the dialkyl glyceryl ether in a ball milling tank, add 5 times the mass of water to disperse evenly, and use a planetary ball mill to conduct ball milling at a rate of 200 rpm for 24 hours. The resulting mixed slurry is dried at room temperature for 24 hours and then placed in an air atmosphere and heated at 850°C. The lithium-ion battery cathode material is obtained by keeping it incubated for 18 hours; wherein the ratio of each element of the metal elements in each mixture is calculated based on the theoretical reaction product formula Li(Mn 0.48 Fe 0.32 Ni 0.2 )O 2 as n(Mn+Fe+ Ni): n(Li)=1:1, n(Mn+Fe): n(Ni)=8:2; iron source, manganese source, nickel source, lithium source, polyimide and anionic surfactant The mass ratio is: m (iron source + manganese source + nickel source + lithium source): m (polyimide): m (anionic surfactant) = 1g: 0.5g: 0.5g.
对比例2Comparative example 2
一种锂离子电池正极材料及其制备方法,包括以下步骤:A lithium-ion battery cathode material and a preparation method thereof, including the following steps:
(1)将0.003mol一水硫酸锰和3g聚乙烯吡咯烷酮用水和少量乙醇配制浓度为12g/L的溶液A,以滴定形式在溶液A中加入12g/L铁氰化钾溶液并搅拌反应直至溶液浑浊度不再改变,待反应完全后,常温陈化24h,过滤,用水和乙醇分别洗涤,干燥后,得铁氰化锰;(1) Prepare solution A with a concentration of 12g/L by adding 0.003mol manganese sulfate monohydrate and 3g polyvinylpyrrolidone with water and a small amount of ethanol. Add 12g/L potassium ferricyanide solution to solution A in titration form and stir the reaction until the solution The turbidity will no longer change. After the reaction is complete, it is aged at room temperature for 24 hours, filtered, washed with water and ethanol respectively, and dried to obtain manganese ferricyanide;
(2)将铁氰化锰、醋酸镍、醋酸锂、聚酰亚胺置于球磨罐中,加入5倍质量的水分散均匀并采用行星式球磨仪以200rpm的速率进行球磨处理24h,所得混合浆料常温干燥24h后置入空气气氛中经850℃下保温18h,即得所述锂离子电池正极材料;其中各混合料中金属元素的根据理论反应产品化合式Li(Mn0.48Fe0.32Ni0.2)O2计算各元素比为n(Mn+Fe+Ni):n(Li)=1:1,n(Mn+Fe):n(Ni)=8:2;铁氰化锰、镍源、锂源、聚酰亚胺的质量之比为:m(铁氰化锰+镍源+锂源):m(聚酰亚胺)=1g:0.5g。(2) Place manganese ferricyanide, nickel acetate, lithium acetate, and polyimide in a ball mill tank, add 5 times the mass of water to disperse evenly, and use a planetary ball mill to conduct ball milling at a rate of 200 rpm for 24 hours. The resulting mixture The slurry is dried at room temperature for 24 hours and then placed in an air atmosphere and kept at 850°C for 18 hours to obtain the lithium ion battery cathode material; the theoretical reaction product formula of the metal elements in each mixture is Li(Mn 0.48 Fe 0.32 Ni 0.2 )O 2 calculates the ratio of each element as n(Mn+Fe+Ni): n(Li)=1:1, n(Mn+Fe): n(Ni)=8:2; manganese ferricyanide, nickel source, The mass ratio of lithium source and polyimide is: m (manganese ferricyanide + nickel source + lithium source): m (polyimide) = 1g: 0.5g.
对比例3Comparative example 3
一种锂离子电池正极材料及其制备方法,包括以下步骤:A lithium-ion battery cathode material and a preparation method thereof, including the following steps:
(1)将0.003mol一水硫酸锰和3g聚乙烯吡咯烷酮用水和少量乙醇配制浓
度为12g/L的溶液A,以滴定形式在溶液A中加入12g/L铁氰化钾溶液并搅拌反应直至溶液浑浊度不再改变,待反应完全后,常温陈化24h,过滤,用水和乙醇分别洗涤,干燥后,得铁氰化锰;(1) Prepare a concentrated mixture of 0.003 mol manganese sulfate monohydrate and 3 g polyvinylpyrrolidone with water and a small amount of ethanol. For solution A with a concentration of 12g/L, add 12g/L potassium ferricyanide solution to solution A in titration form and stir the reaction until the turbidity of the solution no longer changes. After the reaction is complete, age it at room temperature for 24 hours, filter, and mix with water and After washing separately with ethanol and drying, manganese ferricyanide is obtained;
(2)将铁氰化锰、醋酸镍、醋酸锂、阴离子表面活性剂十二烷基缩水甘油醚置于球磨罐中,加入5倍质量的水分散均匀并采用行星式球磨仪以200rpm的速率进行球磨处理24h,所得混合浆料常温干燥24h后置入空气气氛中经850℃下保温18h,即得所述锂离子电池正极材料;其中各混合料中金属元素的根据理论反应产品化合式Li(Mn0.48Fe0.32Ni0.2)O2计算各元素比为n(Mn+Fe+Ni):n(Li)=1:1,n(Mn+Fe):n(Ni)=8:2;铁氰化锰、镍源、锂源、阴离子表面活性剂的质量之比为:m(铁氰化锰+镍源+锂源):m(阴离子表面活性剂)=1g:0.5g。(2) Place manganese ferricyanide, nickel acetate, lithium acetate, and anionic surfactant dodecyl glycidyl ether in a ball mill jar, add 5 times the mass of water to disperse evenly, and use a planetary ball mill at a rate of 200 rpm Perform ball milling treatment for 24 hours, dry the resulting mixed slurry at room temperature for 24 hours, then place it in an air atmosphere and keep it at 850°C for 18 hours to obtain the lithium-ion battery cathode material; wherein the theoretical reaction product formula of the metal elements in each mixture is Li (Mn 0.48 Fe 0.32 Ni 0.2 )O 2 The calculated ratio of each element is n(Mn+Fe+Ni): n(Li)=1:1, n(Mn+Fe): n(Ni)=8:2; iron The mass ratio of manganese cyanide, nickel source, lithium source and anionic surfactant is: m (manganese ferricyanide + nickel source + lithium source): m (anionic surfactant) = 1g: 0.5g.
对比例4Comparative example 4
本申请所述锂离子电池正极材料及其制备方法的一种实施例,包括以下步骤:An embodiment of the lithium-ion battery cathode material and its preparation method described in the present application includes the following steps:
(1)将0.003mol一水硫酸锰和3g聚乙烯吡咯烷酮用水和少量乙醇配制浓度为12g/L的溶液A,以滴定形式在溶液A中加入12g/L铁氰化钾溶液并搅拌反应直至溶液浑浊度不再改变,待反应完全后,常温陈化24h,过滤,用水和乙醇分别洗涤,干燥后,得铁氰化锰;(1) Prepare solution A with a concentration of 12g/L by adding 0.003mol manganese sulfate monohydrate and 3g polyvinylpyrrolidone with water and a small amount of ethanol. Add 12g/L potassium ferricyanide solution to solution A in titration form and stir the reaction until the solution The turbidity will no longer change. After the reaction is complete, it is aged at room temperature for 24 hours, filtered, washed with water and ethanol respectively, and dried to obtain manganese ferricyanide;
(2)将铁氰化锰、醋酸镍、醋酸锂、聚酰亚胺以及非离子表面活性剂AEO-9(岱旭化工)置于球磨罐中,加入5倍质量的水分散均匀并采用行星式球磨仪以200rpm的速率进行球磨处理24h,所得混合浆料常温干燥24h后置入空气气氛中经850℃下保温18h,即得所述锂离子电池正极材料;其中各混合料中金属元素的根据理论反应产品化合式Li(Mn0.48Fe0.32Ni0.2)O2计算各元素比为n
(Mn+Fe+Ni):n(Li)=1:1,n(Mn+Fe):n(Ni)=8:2;铁氰化锰、镍源、锂源、聚酰亚胺以及非离子表面活性剂的质量之比为:m(铁氰化锰+镍源+锂源):m(聚酰亚胺):m(非离子表面活性剂)=1g:0.5g:0.5g。(2) Place manganese ferricyanide, nickel acetate, lithium acetate, polyimide and nonionic surfactant AEO-9 (Daixu Chemical) in a ball mill tank, add 5 times the mass of water to disperse evenly and use a planetary The ball mill was ball milled at a speed of 200 rpm for 24 hours, and the resulting mixed slurry was dried at room temperature for 24 hours and then placed in an air atmosphere and kept at 850°C for 18 hours to obtain the lithium-ion battery cathode material; wherein the metal elements in each mixture were According to the theoretical reaction product formula Li(Mn 0.48 Fe 0.32 Ni 0.2 )O 2 , the ratio of each element is calculated as n (Mn+Fe+Ni): n(Li)=1:1, n(Mn+Fe): n(Ni)=8:2; manganese ferricyanide, nickel source, lithium source, polyimide and non- The mass ratio of ionic surfactants is: m (manganese ferricyanide + nickel source + lithium source): m (polyimide): m (nonionic surfactant) = 1g: 0.5g: 0.5g.
效果例1Effect example 1
为了验证本申请所述锂离子电池正极材料的电化学性能,将各实施例和对比例各材料与导电炭黑、PVDF按照质量比8:1:1混合并加入适量NMP调节制浆,涂覆在铝箔上经干燥后裁切制备得到正极极片,以锂金属为负极极片,商业聚丙烯膜为隔膜进行锂离子扣式半电池的组装,所得电池静置12h后,常温下在2~4.5V电压、0.2C倍率条件下进行100次充放电循环测试,随后提升倍率至1C循环5次,最终再回复至0.2C倍率循环5次,结果如表1所示。In order to verify the electrochemical performance of the lithium-ion battery cathode materials described in this application, the materials of each example and comparative example were mixed with conductive carbon black and PVDF according to a mass ratio of 8:1:1, and an appropriate amount of NMP was added to adjust the slurry, and then coated The positive electrode piece was prepared by cutting it after drying on the aluminum foil. Lithium metal was used as the negative electrode piece and commercial polypropylene film was used as the separator to assemble the lithium ion button half battery. After the resulting battery was left to stand for 12 hours, it was heated for 2 to 2 hours at room temperature. 100 charge-discharge cycle tests were conducted under the condition of 4.5V voltage and 0.2C rate, then the rate was increased to 1C for 5 cycles, and finally returned to 0.2C for 5 cycles. The results are shown in Table 1.
表1
Table 1
Table 1
从表1可以看出,各实施例所得产品在低倍率下的初始放电比容量均较高,可达到155mAh/g以上,而循环100次后的容量保持率也达到了80%以上,而当所述产品在经历大倍率循环,重新回到低倍率循环时,其放电比容量依然可观,最高可达到145mAh/g。从实施例1~4可知,随着产品中镍元素含量的降低,其循环稳定性有一定提升,但放电容量有所下降,基于综合性能考虑,产品中n(Mn+Fe):n(Ni)为9:1~8:2时性能较佳。从实施例1与实施例5、实施例6产品性能对比可知,随着聚酰亚胺和表面活性剂的添加量提升过多,产品各前驱体的分散性更好,且氮元素掺杂含量也变高,但相对而言可能导致各前驱体在混合过程中与水相完全分离,混合均匀的程度反而变低,产品的循环性能和倍率性能也会有所影响。相比之下,对比例1产品采用了普通的原料进行产品的制备,虽然最后也引入了表面活性剂和聚酰亚胺,但整体效果较差,产品的循环性能差,初始容量较低且倍率性能较差。对比例2和3在前驱体研磨混合的过程中分别没有引入表面活性剂和聚酰亚胺,相比于实施例1产品其循环性能和倍率性能显著变差,而对比例3产品的初始放电比容量较低,说明氮元素的掺杂缺失对于产品的初始容量也会有所影响。对比例4产品在制备过程中与实施例1的差别仅仅在于使用了不同种类的表面活性剂,显然其性能与不引入表面活性剂的对比例2产品相当,说明非离子表面活性剂并不能有效帮助各前驱体材料混合分散均匀,该助剂并不适用于本申请所述产品的制备工艺体系。It can be seen from Table 1 that the initial discharge specific capacity of the products obtained in each embodiment is relatively high at low rates, reaching more than 155mAh/g, and the capacity retention rate after 100 cycles also reaches more than 80%. When the product undergoes high-rate cycles and returns to low-rate cycles, its discharge specific capacity is still considerable, reaching a maximum of 145mAh/g. It can be seen from Examples 1 to 4 that as the nickel content in the product decreases, its cycle stability improves to a certain extent, but the discharge capacity decreases. Based on comprehensive performance considerations, n(Mn+Fe) in the product: n(Ni ) is 9:1 to 8:2, the performance is better. From the comparison of the product performance of Example 1, Example 5 and Example 6, it can be seen that as the addition amount of polyimide and surfactant increases too much, the dispersion of each precursor of the product is better, and the nitrogen doping content It also becomes higher, but relatively speaking, it may cause each precursor to be completely separated from the water phase during the mixing process, and the degree of uniform mixing will become lower, and the cycle performance and rate performance of the product will also be affected. In contrast, the product of Comparative Example 1 uses ordinary raw materials to prepare the product. Although surfactant and polyimide are finally introduced, the overall effect is poor, the product has poor cycle performance, low initial capacity and The rate performance is poor. Comparative Examples 2 and 3 did not introduce surfactant and polyimide respectively during the grinding and mixing process of the precursor. Compared with the product of Example 1, its cycle performance and rate performance were significantly worse, while the initial discharge of the product of Comparative Example 3 was The specific capacity is low, indicating that the lack of nitrogen doping will also have an impact on the initial capacity of the product. The difference between the product of Comparative Example 4 and that of Example 1 during the preparation process is only the use of different types of surfactants. Obviously, its performance is equivalent to that of the product of Comparative Example 2 without the introduction of surfactants, indicating that nonionic surfactants are not effective. Helps the precursor materials to be mixed and dispersed evenly. This additive is not suitable for the preparation process system of the product described in this application.
最后所应当说明的是,以上实施例仅用以说明本申请的技术方案而非对本申请保护范围的限制,尽管参照较佳实施例对本申请作了详细说明,本领域的普通技术人员应当理解,可以对本申请的技术方案进行修改或者等同替换,而
不脱离本申请技术方案的实质和范围。
Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present application and do not limit the protection scope of the present application. Although the present application has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that The technical solution of this application can be modified or equivalently replaced, and without departing from the essence and scope of the technical solution of this application.
Claims (10)
- 一种锂离子电池正极材料的制备方法,其中,包括以下步骤:A method for preparing cathode materials for lithium-ion batteries, which includes the following steps:(1)将一水硫酸锰和聚乙烯吡咯烷酮用水配制溶液A,以滴定形式在溶液A中加入铁氰化钾溶液并搅拌反应,待反应完全后,陈化,过滤,洗涤,得铁氰化锰;(1) Prepare solution A with manganese sulfate monohydrate and polyvinylpyrrolidone with water. Add potassium ferricyanide solution to solution A in titration form and stir the reaction. After the reaction is complete, age, filter, and wash to obtain ferricyanide. manganese;(2)将铁氰化锰、镍源、锂源、聚酰亚胺以及阴离子表面活性剂用水分散均匀并进行球磨处理,随后经750~950℃下保温15~20h,即得所述锂离子电池正极材料。(2) Disperse manganese ferricyanide, nickel source, lithium source, polyimide and anionic surfactant evenly with water and perform ball milling treatment, and then maintain the temperature at 750-950°C for 15-20 hours to obtain the lithium ions Battery cathode material.
- 如权利要求1所述锂离子电池正极材料的制备方法,其中,所述溶液A中一水硫酸锰的摩尔与聚乙烯吡咯烷酮的质量之比为(0.0025~0.0035)mol:(1~5)g,所述溶液A的浓度为10~15g/L。The preparation method of lithium ion battery cathode material according to claim 1, wherein the ratio of the moles of manganese sulfate monohydrate to the mass of polyvinylpyrrolidone in the solution A is (0.0025~0.0035) mol: (1~5) g , the concentration of solution A is 10-15g/L.
- 如权利要求1所述锂离子电池正极材料的制备方法,其中,所述铁氰化钾溶液的浓度为5~10g/L。The method for preparing a lithium-ion battery cathode material according to claim 1, wherein the concentration of the potassium ferricyanide solution is 5-10 g/L.
- 如权利要求1所述锂离子电池正极材料的制备方法,其中,所述铁氰化锰中铁元素和锰元素之和与镍源中镍元素的摩尔比为n(Mn+Fe):n(Ni)=(9:1)~(8:2)。The preparation method of lithium ion battery cathode material according to claim 1, wherein the molar ratio of the sum of iron element and manganese element in the manganese ferricyanide to the nickel element in the nickel source is n(Mn+Fe):n(Ni )=(9:1)~(8:2).
- 如权利要求1所述锂离子电池正极材料的制备方法,其中,所述铁氰化锰、镍源中锰元素、铁元素、镍元素与锂源中锂元素的摩尔比为:n(Mn+Fe+Ni):n(Li)=1:(1~1.05)。The preparation method of lithium ion battery cathode material according to claim 1, wherein the molar ratio of manganese element, iron element, nickel element in the manganese ferricyanide, nickel source and lithium element in the lithium source is: n(Mn+ Fe+Ni):n(Li)=1:(1~1.05).
- 如权利要求1所述锂离子电池正极材料的制备方法,其中,所述镍源为醋酸镍、碳酸镍中的至少一种;所述锂源为醋酸锂、碳酸锂中的至少一种。The method for preparing positive electrode materials for lithium ion batteries according to claim 1, wherein the nickel source is at least one of nickel acetate and nickel carbonate; and the lithium source is at least one of lithium acetate and lithium carbonate.
- 如权利要求1所述锂离子电池正极材料的制备方法,其中,所述阴离子表面活性剂为羧酸盐阴离子表面活性剂、磺酸盐阴离子表面活性剂中的至少一种。 The method for preparing positive electrode materials for lithium ion batteries according to claim 1, wherein the anionic surfactant is at least one of a carboxylate anionic surfactant and a sulfonate anionic surfactant.
- 如权利要求1所述锂离子电池正极材料的制备方法,其中,铁氰化锰、镍源、锂源、聚酰亚胺以及阴离子表面活性剂的质量之比为:m(铁氰化锰+镍源+锂源):m(聚酰亚胺):m(阴离子表面活性剂)=1:(0.4~0.6):(0.4~0.6)。The preparation method of lithium ion battery cathode material according to claim 1, wherein the mass ratio of manganese ferricyanide, nickel source, lithium source, polyimide and anionic surfactant is: m (manganese ferricyanide + Nickel source + lithium source): m (polyimide): m (anionic surfactant) = 1: (0.4~0.6): (0.4~0.6).
- 如权利要求1~8任一项所述锂离子电池正极材料的制备方法制备得到的锂离子电池正极材料。The lithium ion battery cathode material is prepared by the method for preparing a lithium ion battery cathode material according to any one of claims 1 to 8.
- 一种锂离子电池正极极片,其中,所述正极极片由权利要求9所述锂离子电池正极材料制备得到。 A lithium-ion battery positive electrode piece, wherein the positive electrode piece is prepared from the lithium-ion battery positive electrode material of claim 9.
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