WO2022237110A1 - 氟掺杂锂正极材料及其制备方法和应用 - Google Patents
氟掺杂锂正极材料及其制备方法和应用 Download PDFInfo
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- fluorine
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- lithium
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- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 66
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 title claims abstract description 57
- 238000002360 preparation method Methods 0.000 title claims abstract description 38
- 239000007774 positive electrode material Substances 0.000 title claims abstract description 36
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000001301 oxygen Substances 0.000 claims abstract description 50
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 50
- 239000007789 gas Substances 0.000 claims abstract description 30
- 238000001354 calcination Methods 0.000 claims abstract description 29
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims abstract description 20
- 229910001416 lithium ion Inorganic materials 0.000 claims abstract description 20
- 239000013067 intermediate product Substances 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 238000002156 mixing Methods 0.000 claims abstract description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 103
- 239000011572 manganese Substances 0.000 claims description 49
- 229910017855 NH 4 F Inorganic materials 0.000 claims description 35
- 239000002243 precursor Substances 0.000 claims description 24
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims description 17
- 238000003756 stirring Methods 0.000 claims description 15
- 239000007864 aqueous solution Substances 0.000 claims description 14
- 239000003792 electrolyte Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 11
- 239000002245 particle Substances 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 8
- 150000002642 lithium compounds Chemical class 0.000 claims description 7
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 claims description 6
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 5
- 229910052748 manganese Inorganic materials 0.000 claims description 5
- 229910052759 nickel Inorganic materials 0.000 claims description 5
- 150000001875 compounds Chemical class 0.000 claims description 4
- 239000007773 negative electrode material Substances 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 4
- XIXADJRWDQXREU-UHFFFAOYSA-M lithium acetate Chemical compound [Li+].CC([O-])=O XIXADJRWDQXREU-UHFFFAOYSA-M 0.000 claims description 3
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 claims description 3
- 229910052808 lithium carbonate Inorganic materials 0.000 claims description 3
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 abstract description 29
- 229910052731 fluorine Inorganic materials 0.000 abstract description 29
- 239000011737 fluorine Substances 0.000 abstract description 29
- 239000000463 material Substances 0.000 abstract description 25
- LDDQLRUQCUTJBB-UHFFFAOYSA-N ammonium fluoride Chemical compound [NH4+].[F-] LDDQLRUQCUTJBB-UHFFFAOYSA-N 0.000 abstract 1
- 230000001351 cycling effect Effects 0.000 abstract 1
- 239000010406 cathode material Substances 0.000 description 19
- 230000000694 effects Effects 0.000 description 12
- 229910018327 Ni0.25 Mn0.75 Inorganic materials 0.000 description 9
- 239000000243 solution Substances 0.000 description 7
- 229910018068 Li 2 O Inorganic materials 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 230000007062 hydrolysis Effects 0.000 description 5
- 238000006460 hydrolysis reaction Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 4
- 238000007599 discharging Methods 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 229910003002 lithium salt Inorganic materials 0.000 description 4
- 159000000002 lithium salts Chemical class 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000012512 characterization method Methods 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- OIFBSDVPJOWBCH-UHFFFAOYSA-N Diethyl carbonate Chemical compound CCOC(=O)OCC OIFBSDVPJOWBCH-UHFFFAOYSA-N 0.000 description 2
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 238000000967 suction filtration Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910009055 Li1.2Ni0.2Mn0.6O2 Inorganic materials 0.000 description 1
- 229910001290 LiPF6 Inorganic materials 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G53/00—Compounds of nickel
- C01G53/40—Nickelates
- C01G53/42—Nickelates containing alkali metals, e.g. LiNiO2
- C01G53/44—Nickelates containing alkali metals, e.g. LiNiO2 containing manganese
- C01G53/50—Nickelates containing alkali metals, e.g. LiNiO2 containing manganese of the type [MnO2]n-, e.g. Li(NixMn1-x)O2, Li(MyNixMn1-x-y)O2
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G53/00—Compounds of nickel
- C01G53/40—Nickelates
- C01G53/42—Nickelates containing alkali metals, e.g. LiNiO2
- C01G53/44—Nickelates containing alkali metals, e.g. LiNiO2 containing 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
- H01M10/05—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
- H01M4/36—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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/50—Solid solutions
- C01P2002/52—Solid solutions containing elements as dopants
- C01P2002/54—Solid solutions containing elements as dopants one element only
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/03—Particle morphology depicted by an image obtained by SEM
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/40—Electric properties
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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
- H01M2004/021—Physical characteristics, e.g. porosity, surface area
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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
- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/028—Positive electrodes
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- 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 invention relates to the technical field of lithium ion batteries, in particular to a fluorine-doped lithium positive electrode material and a preparation method and application thereof.
- Lithium-rich manganese-based layered oxides are attracting more and more attention from researchers because of their high specific capacity over 250mAhg -1 , high operating cost at 4.8V, and high safety.
- LMROs lithium-rich manganese-based layered oxides
- lithium-rich materials generally have three major problems: 1. The initial coulombic efficiency is low due to the precipitation of lattice oxygen during charge and discharge; 2. The voltage decay is serious; 3. The rate performance is poor.
- the main purpose of the present invention is to provide a fluorine-doped lithium positive electrode material and its preparation method and application, so as to solve the problems of low first efficiency, poor cycle performance and rate performance of lithium-rich materials in the prior art.
- step S1 includes: step S1, under the first stirring, mix and react the aqueous solution of NH 4 F and Li x Ni y Mnz O 2 to obtain an intermediate product system.
- the mass ratio of NH 4 F to Li x Ni y Mnz O 2 in the aqueous solution of NH 4 F is 0.01 ⁇ 0.1:1, preferably 0.05 ⁇ 0.07:1.
- the speed of the above-mentioned first stirring is 300-2000 rpm, and the time is 1-10 min.
- the preparation method further includes: filtering the intermediate product system to obtain fluorine-modified Li x Ni y Mnz O 2 .
- the temperature of the above-mentioned first calcination is 400-800° C., and the time is 4-8 hours.
- volume content of oxygen in the first oxygen-containing gas is 10-100%.
- the above-mentioned first oxygen-containing gas is air.
- the flow rate of the first oxygen-containing gas is 5-10 L/min.
- the ratio of the molar weight of lithium in the lithiated compound to the sum of the molar weights of nickel and manganese in the Ni a Mn b CO 3 precursor is 1.4-1.6.
- the lithium compound is selected from one or more of lithium hydroxide, lithium carbonate, lithium chloride, and lithium acetate.
- Ni a Mn b CO 3 precursor has a particle size of 5-10 ⁇ m, and preferably the specific surface area of the Ni a Mn b CO 3 precursor is 20-120 m 2 /g.
- the bulk density of the above-mentioned Ni a Mn b CO 3 precursor is 1.4 ⁇ 2.5 g/cm 3 .
- the temperature of the above-mentioned second calcination is 750-850° C., and the time is 8-12 hours.
- volume content of oxygen in the second oxygen-containing gas is 10-100%.
- the flow rate of the second oxygen-containing gas is 5-10 L/min.
- the above-mentioned second oxygen-containing gas is air.
- a fluorine-doped lithium positive electrode material is provided, and the fluorine-doped lithium positive electrode material is prepared by any one of the above preparation methods.
- a lithium ion battery comprising an electrolyte, a positive electrode material and a negative electrode material, the positive electrode material includes a lithium positive electrode material, and the lithium positive electrode material is any one of the above-mentioned fluorine-doped lithium positive electrode materials.
- the above fluorine-modified Li x Ni y Mnz O 2 is first calcined to further infiltrate fluorine into the material to obtain a fluorine-doped lithium positive electrode material doped with fluorine. Due to the protection of fluorine, the material reduces the amount of free oxygen that enters the electrolyte during the first charging and discharging process when it is used as the positive electrode of lithium-ion batteries, and reduces the amount of lithium ions that are solidified into Li 2 O by free oxygen, thereby effectively improving the lithium ion battery. The first effect of ion batteries. At the same time, the cycle performance and rate performance of the battery are also improved compared with the lithium cathode material without F doping.
- Fig. 1 shows the SEM image of the fluorine-doped lithium cathode material prepared in Example 2.
- FIG. 2 shows the SEM image of the fluorine-doped lithium cathode material prepared in Comparative Example 1.
- the lithium-rich materials in the prior art have low first efficiency, poor cycle performance and rate performance.
- the present application provides a fluorine-doped lithium positive electrode material and its preparation method and application.
- the material Due to the protection of fluorine, the material reduces the amount of free oxygen that enters the electrolyte during the first charging and discharging process when it is used as the positive electrode of lithium-ion batteries, and reduces the amount of lithium ions that are solidified into Li 2 O by free oxygen, thereby effectively improving the lithium ion battery.
- the first effect of ion batteries At the same time, the cycle performance and rate performance of the battery are also improved compared with the lithium cathode material without F doping.
- the hydrolysis of NH 4 F will produce hydrofluoric acid.
- the mass ratio of NH 4 F to Li x Ni y Mnz O 2 in the NH 4 F aqueous solution is preferably 0.01 ⁇ 0.1:1. Within the above raw material ratio range, it can further ensure that Li x Ni y Mnz O 2 is doped with more fluorine, and avoid the internal structure of the material from being corroded by HF acid, which will lead to performance degradation, especially when the ratio is 0.05-0.07:1 , the effect is particularly prominent.
- the above step S1 includes: step S1, under the first stirring, mixing and reacting an aqueous solution of NH 4 F and Li x Ni y Mnz O 2 to obtain an intermediate product system.
- step S1 under the first stirring, mixing and reacting an aqueous solution of NH 4 F and Li x Ni y Mnz O 2 to obtain an intermediate product system.
- the speed of the above-mentioned first stirring can be selected by those skilled in the art according to the needs in actual operation.
- the speed of the first stirring is preferably 300-2000 rpm and the time is 1-10 min.
- the preparation method further includes: filtering the intermediate product system , to obtain fluorine-modified Li x Ni y Mnz O 2 .
- the above-mentioned filtration methods can be selected from common filtration methods in the field, such as pressure filtration, suction filtration, centrifugal separation, etc., which will not be repeated here.
- the purpose of the first calcination is to allow fluorine to further penetrate into Li x Ni y Mnz O 2 to achieve a better doping effect.
- the temperature of the first calcination is 400-800°C, and the time is 4 ⁇ 8h.
- the infiltration of fluorine can be achieved relatively quickly and at the same time, it is ensured that the structural stability of the material will not be reduced due to the high sintering temperature.
- the volume content of oxygen in the first oxygen-containing gas is 10-100%, and preferably the first oxygen-containing gas is air.
- the flow rate of the first oxygen-containing gas is 5-10 L/min.
- the Li x Ni y MnzO used in the present application can be existing materials in the prior art or prepare the material by methods known in the prior art.
- the above-mentioned preparation method also includes Li x Ni y
- the content of nickel and manganese can be flexibly adjusted through the above preparation process.
- the ratio of the molar weight of lithium in the lithiated compound to the sum of the molar weights of nickel and manganese in the Ni a Mn b CO 3 precursor is 1.4 to 1.6, thereby further ensuring that the Li content in Li x Ni y Mnz O 2 is optimal within range.
- the lithium compound is selected from one or more of lithium hydroxide, lithium carbonate, lithium chloride, and lithium acetate.
- the particle size of the Ni a Mn b CO 3 precursor is 5-10 ⁇ m
- the specific surface area (BET) of the Ni a Mn b CO 3 precursor is preferably 20-120 m 2 /g
- the Ni a Mn b CO 3 precursor is preferably Bulk density (TD) is 1.4 ⁇ 2.5g/cm 3 .
- the Ni a Mn b CO 3 precursor within the above parameter range can prepare fluorine-doped lithium cathode materials with particle size and specific surface area that are easier to homogeneously coat.
- the temperature of the second calcination is preferably 750-850° C., and the time is 8-12 hours.
- the volume content of oxygen in the second oxygen-containing gas is preferably 10-100%, and the second oxygen-containing gas is preferably air.
- the flow rate of the second oxygen-containing gas is 5-10 L/min, so as to further improve the production rate and effect of Li x Ni y Mnz O 2 .
- a fluorine-doped lithium positive electrode material is provided, and the fluorine-doped lithium positive electrode material is prepared by any one of the above-mentioned preparation methods.
- the fluorine-doped lithium positive electrode material of the present application is doped with fluorine, and the stability of the bond formed by fluorine and metal is higher than that of oxygen and metal. Therefore, by doping fluorine, the oxygen in the material can be made
- the protection of fluorine reduces the free oxygen that leaves the material and enters the electrolyte during the charge and discharge process, especially reduces the amount of free oxygen that enters the electrolyte after the first charge and discharge. Less free oxygen will reduce the amount of lithium ions that are solidified by free oxygen and exist in the form of Li 2 O and cannot continue to participate in the electrochemical reaction, which will greatly increase the number of free lithium ions in the electrolyte, thereby effectively improving the performance of lithium-ion batteries. the first effect.
- the fluorine-doped lithium cathode material of the present application also improves the cycle performance and rate performance of the battery compared with the non-F-doped lithium cathode material.
- the fluorine content in the fluorine-doped lithium cathode material within the above range can better ensure the structural integrity of the material, thereby ensuring its advantages of high first efficiency, good cycle performance and rate performance.
- a lithium-ion battery including an electrolyte, a positive electrode material, and a negative electrode material
- the positive electrode material includes a lithium positive electrode material
- the lithium positive electrode material is any one of the above-mentioned fluorine-doped lithium positive electrodes
- the material or the fluorine-doped lithium positive electrode material prepared by any one of the above preparation methods.
- the material of this application reduces the amount of free oxygen that enters the electrolyte during the first charging and discharging process when it is used as the positive electrode of lithium-ion batteries, so that the amount of lithium ions that are solidified into Li 2 O by free oxygen decreases, thereby effectively improving the battery life.
- the first effect of lithium-ion batteries At the same time, the cycle performance and rate performance of the battery are also improved compared with the lithium cathode material without F doping.
- Example 1 The difference from Example 1 is that the calcination temperature in step 4) is 400°C.
- Example 1 The difference from Example 1 is that the calcination temperature in step 4) is 800°C.
- Example 1 The difference from Example 1 is that the calcination temperature in step 4) is 300°C.
- Example 1 The difference from Example 1 is that the calcination temperature in step 4) is 900°C.
- Example 1 The difference from Example 1 is that the calcination time in step 4) is 4h.
- Example 1 The difference from Example 1 is that the calcination time in step 4) is 8h.
- Example 1 The difference from Example 1 is that the calcination time in step 4) is 3h.
- Example 1 The difference from Example 1 is that the calcination time in step 4) is 9h.
- Example 1 The difference from Example 1 is that the air flow rate in step 4) is 5 L/min.
- Example 1 The difference from Example 1 is that the air flow rate in step 4) is 10 L/min.
- the prepared pole piece is assembled with CR2032 shell, the voltage window is 2-4.8V negative electrode material lithium metal, the electrolyte is conventional lithium-rich electrolyte: 1mol/L LiPF6, EC (ethylene carbonate): DEC (diethyl carbonate) volume ratio is 3:7.
- Table 1 shows the 0.1C discharge capacity, 1C discharge capacity, first effect and 50-week capacity retention rate of the above-mentioned examples and comparative examples.
- the SEM characterization of the fluorine-doped lithium cathode material prepared in Example 2 is shown in FIG. 1
- the SEM characterization of the non-fluorine-doped lithium cathode material prepared in Comparative Example 1 is shown in FIG. 2 . It can be seen that the structure and surface physical properties of the lithium cathode material do not change significantly before and after fluorine doping, indicating that the method of the present application will not adversely affect the structure of the lithium cathode material.
- the material Due to the protection of fluorine, the material reduces the amount of free oxygen that enters the electrolyte during the first charging and discharging process when it is used as the positive electrode of lithium-ion batteries, and reduces the amount of lithium ions that are solidified into Li 2 O by free oxygen, thereby effectively improving the lithium ion battery.
- the first effect of ion batteries At the same time, the cycle performance and rate performance of the battery are also improved compared with the lithium cathode material without F doping.
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Abstract
Description
Claims (14)
- 一种氟掺杂锂正极材料的制备方法,其特征在于,所述制备方法包括:步骤S1,将NH 4F、Li xNi yMn zO 2和水混合反应,得到中间产物体系,所述中间产物体系包括氟改性的所述Li xNi yMn zO 2,所述NH 4F与所述Li xNi yMn zO 2质量比为0.05~0.07:1;步骤S2,在第一含氧气体中,对所述氟改性的所述Li xNi yMn zO 2进行第一煅烧,得到所述氟掺杂锂正极材料,所述第一含氧气体中氧气的体积含量为10~100%,其中x=1~1.3,y=0.1~0.9,z=0.1~0.9,x:(y+z)=1.4~1.6。
- 根据权利要求1所述的制备方法,其特征在于,所述步骤S1包括:步骤S1,在第一搅拌下,将NH 4F的水溶液和所述Li xNi yMn zO 2混合并发生所述反应,得到所述中间产物体系。
- 根据权利要求1所述的制备方法,其特征在于,在所述步骤S2之前,所述制备方法还包括:对所述中间产物体系进行过滤,得到所述氟改性的所述Li xNi yMn zO 2。
- 根据权利要求1所述的制备方法,其特征在于,所述第一煅烧的温度为400~800℃,时间为4~8h。
- 根据权利要求1至4中任一项所述的制备方法,其特征在于,所述第一含氧气体的流量为5~10L/min。
- 根据权利要求1所述的制备方法,其特征在于,所述第一含氧气体为空气。
- 根据权利要求1所述的制备方法,其特征在于,所述制备方法还包括所述Li xNi yMn zO 2的制备过程,所述制备过程包括:在第二含氧气体中,对包含Ni aMn bCO 3前驱体和锂化物的原料体系进行第二煅烧,得到所述Li xNi yMn zO 2,其中a=0.1~0.9,b=0.1~0.9,a+b=1。
- 根据权利要求7所述的制备方法,其特征在于,所述锂化物中的锂的摩尔量和所述Ni aMn bCO 3前驱体中的镍和锰摩尔量总和的比值为1.4~1.6。
- 根据权利要求7所述的制备方法,其特征在于,所述锂化物选自氢氧化锂、碳酸锂和氯化锂、醋酸锂中的一种或多种。
- 根据权利要求7至9中任一项所述的制备方法,其特征在于,所述Ni aMn bCO 3前驱体粒径为5~10μm,优选所述Ni aMn bCO 3前驱体的比表面积为20~120m 2/g,优选所述Ni aMn bCO 3前驱体的堆密度为1.4~2.5g/cm 3。
- 根据权利要求7所述的制备方法,其特征在于,所述第二煅烧的温度为750~850℃、时间为8~12h。
- 根据权利要求7或11所述的制备方法,其特征在于,所述第二含氧气体中氧气的体积含量为10~100%,优选所述第二含氧气体为空气,优选所述第二含氧气体的流量为5~10L/min。
- 一种氟掺杂锂正极材料,其特征在于,所述氟掺杂锂正极材料由权利要求1至12中任一项所述的制备方法制备得到。
- 一种锂离子电池,包含电解液、正极材料和负极材料,所述正极材料包含锂正极材料,其特征在于,所述锂正极材料为权利要求13所述的氟掺杂锂正极材料。
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