WO2024108653A1 - Plasma lithium supplementing device and method for positive electrode material for lithium battery - Google Patents
Plasma lithium supplementing device and method for positive electrode material for lithium battery Download PDFInfo
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- WO2024108653A1 WO2024108653A1 PCT/CN2022/137050 CN2022137050W WO2024108653A1 WO 2024108653 A1 WO2024108653 A1 WO 2024108653A1 CN 2022137050 W CN2022137050 W CN 2022137050W WO 2024108653 A1 WO2024108653 A1 WO 2024108653A1
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- lithium
- plasma
- positive electrode
- electrode material
- atmospheric pressure
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- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 77
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 title claims abstract description 76
- 239000007774 positive electrode material Substances 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 33
- 230000001502 supplementing effect Effects 0.000 title abstract 5
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims abstract description 35
- 229910001416 lithium ion Inorganic materials 0.000 claims abstract description 33
- 238000000137 annealing Methods 0.000 claims abstract description 19
- 238000001035 drying Methods 0.000 claims abstract description 16
- 239000002699 waste material Substances 0.000 claims abstract description 8
- 238000000678 plasma activation Methods 0.000 claims abstract description 7
- 238000010438 heat treatment Methods 0.000 claims abstract description 4
- 238000004140 cleaning Methods 0.000 claims abstract description 3
- 239000011343 solid material Substances 0.000 claims abstract description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 20
- GELKBWJHTRAYNV-UHFFFAOYSA-K lithium iron phosphate Chemical compound [Li+].[Fe+2].[O-]P([O-])([O-])=O GELKBWJHTRAYNV-UHFFFAOYSA-K 0.000 claims description 20
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims description 18
- 230000009469 supplementation Effects 0.000 claims description 13
- 229910000625 lithium cobalt oxide Inorganic materials 0.000 claims description 12
- BFZPBUKRYWOWDV-UHFFFAOYSA-N lithium;oxido(oxo)cobalt Chemical compound [Li+].[O-][Co]=O BFZPBUKRYWOWDV-UHFFFAOYSA-N 0.000 claims description 12
- 239000002904 solvent Substances 0.000 claims description 11
- FBDMTTNVIIVBKI-UHFFFAOYSA-N [O-2].[Mn+2].[Co+2].[Ni+2].[Li+] Chemical compound [O-2].[Mn+2].[Co+2].[Ni+2].[Li+] FBDMTTNVIIVBKI-UHFFFAOYSA-N 0.000 claims description 10
- 229910052786 argon Inorganic materials 0.000 claims description 10
- IIPYXGDZVMZOAP-UHFFFAOYSA-N lithium nitrate Chemical compound [Li+].[O-][N+]([O-])=O IIPYXGDZVMZOAP-UHFFFAOYSA-N 0.000 claims description 10
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 9
- 238000005188 flotation Methods 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims description 9
- DVATZODUVBMYHN-UHFFFAOYSA-K lithium;iron(2+);manganese(2+);phosphate Chemical compound [Li+].[Mn+2].[Fe+2].[O-]P([O-])([O-])=O DVATZODUVBMYHN-UHFFFAOYSA-K 0.000 claims description 9
- 229910000572 Lithium Nickel Cobalt Manganese Oxide (NCM) Inorganic materials 0.000 claims description 8
- 239000012535 impurity Substances 0.000 claims description 8
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims description 8
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- NDPGDHBNXZOBJS-UHFFFAOYSA-N aluminum lithium cobalt(2+) nickel(2+) oxygen(2-) Chemical compound [Li+].[O--].[O--].[O--].[O--].[Al+3].[Co++].[Ni++] NDPGDHBNXZOBJS-UHFFFAOYSA-N 0.000 claims description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- 230000004888 barrier function Effects 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 238000009832 plasma treatment Methods 0.000 claims description 6
- 239000010406 cathode material Substances 0.000 claims description 5
- 229910002102 lithium manganese oxide Inorganic materials 0.000 claims description 5
- INHCSSUBVCNVSK-UHFFFAOYSA-L lithium sulfate Inorganic materials [Li+].[Li+].[O-]S([O-])(=O)=O INHCSSUBVCNVSK-UHFFFAOYSA-L 0.000 claims description 5
- VLXXBCXTUVRROQ-UHFFFAOYSA-N lithium;oxido-oxo-(oxomanganiooxy)manganese Chemical compound [Li+].[O-][Mn](=O)O[Mn]=O VLXXBCXTUVRROQ-UHFFFAOYSA-N 0.000 claims description 5
- 239000003495 polar organic solvent Substances 0.000 claims description 5
- RBTVSNLYYIMMKS-UHFFFAOYSA-N tert-butyl 3-aminoazetidine-1-carboxylate;hydrochloride Chemical compound Cl.CC(C)(C)OC(=O)N1CC(N)C1 RBTVSNLYYIMMKS-UHFFFAOYSA-N 0.000 claims description 5
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 claims description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 4
- 229910001386 lithium phosphate Inorganic materials 0.000 claims description 4
- 239000001301 oxygen Substances 0.000 claims description 4
- 229910052760 oxygen Inorganic materials 0.000 claims description 4
- TWQULNDIKKJZPH-UHFFFAOYSA-K trilithium;phosphate Chemical compound [Li+].[Li+].[Li+].[O-]P([O-])([O-])=O TWQULNDIKKJZPH-UHFFFAOYSA-K 0.000 claims description 4
- 239000003570 air Substances 0.000 claims description 3
- 239000001307 helium Substances 0.000 claims description 3
- 229910052734 helium Inorganic materials 0.000 claims description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- 239000003960 organic solvent Substances 0.000 claims description 3
- CYSGHNMQYZDMIA-UHFFFAOYSA-N 1,3-Dimethyl-2-imidazolidinon Chemical compound CN1CCN(C)C1=O CYSGHNMQYZDMIA-UHFFFAOYSA-N 0.000 claims description 2
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 2
- 238000001994 activation Methods 0.000 claims description 2
- 230000004913 activation Effects 0.000 claims description 2
- 239000002244 precipitate Substances 0.000 claims description 2
- 230000001376 precipitating effect Effects 0.000 claims description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 2
- 230000008439 repair process Effects 0.000 abstract description 7
- 230000008569 process Effects 0.000 abstract description 3
- 230000008929 regeneration Effects 0.000 abstract description 3
- 238000011069 regeneration method Methods 0.000 abstract description 3
- 230000003213 activating effect Effects 0.000 abstract 1
- 239000000463 material Substances 0.000 description 18
- 239000000243 solution Substances 0.000 description 17
- 208000028659 discharge Diseases 0.000 description 15
- 239000000843 powder Substances 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 5
- 238000007599 discharging Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000007773 negative electrode material Substances 0.000 description 3
- FLAFBICRVKZSCF-UHFFFAOYSA-N [Li].[Co]=O.[Li] Chemical compound [Li].[Co]=O.[Li] FLAFBICRVKZSCF-UHFFFAOYSA-N 0.000 description 2
- IDSMHEZTLOUMLM-UHFFFAOYSA-N [Li].[O].[Co] Chemical class [Li].[O].[Co] IDSMHEZTLOUMLM-UHFFFAOYSA-N 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 1
- 101000827703 Homo sapiens Polyphosphoinositide phosphatase Proteins 0.000 description 1
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 1
- VEQPNABPJHWNSG-UHFFFAOYSA-N Nickel(2+) Chemical compound [Ni+2] VEQPNABPJHWNSG-UHFFFAOYSA-N 0.000 description 1
- 102100023591 Polyphosphoinositide phosphatase Human genes 0.000 description 1
- 101100233916 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) KAR5 gene Proteins 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- -1 activated nickel cobalt aluminum lithium Chemical class 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- ACKHWUITNXEGEP-UHFFFAOYSA-N aluminum cobalt(2+) nickel(2+) oxygen(2-) Chemical compound [O-2].[Al+3].[Co+2].[Ni+2] ACKHWUITNXEGEP-UHFFFAOYSA-N 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- CXULZQWIHKYPTP-UHFFFAOYSA-N cobalt(2+) manganese(2+) nickel(2+) oxygen(2-) Chemical compound [O--].[O--].[O--].[Mn++].[Co++].[Ni++] CXULZQWIHKYPTP-UHFFFAOYSA-N 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- SLWMIXZPRPWLRQ-UHFFFAOYSA-M lithium;n,n-dimethylformamide;chloride Chemical compound [Li+].[Cl-].CN(C)C=O SLWMIXZPRPWLRQ-UHFFFAOYSA-M 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 229910001453 nickel ion Inorganic materials 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000010926 waste battery Substances 0.000 description 1
Images
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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/4235—Safety or regulating additives or arrangements in electrodes, separators or electrolyte
-
- 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
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
-
- 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
- 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 invention belongs to the field of recycling metal materials in waste batteries, and specifically relates to a plasma lithium replenishment system and method for positive electrode materials for lithium batteries.
- lithium batteries consume lithium ions in the positive electrode, resulting in irreversible capacity loss.
- the consumed lithium ions can be replenished by lithium replenishment methods, thereby increasing the capacity of lithium-ion batteries.
- lithium metal, negative electrode materials and non-aqueous solvents are mixed to form a slurry and coated on the current collector, so that lithium diffuses into the active material to replenish lithium; metal lithium foil is used to bond the negative electrode for composite, and after the battery is filled with liquid, the metal lithium and the negative electrode react and embed into the negative electrode material for lithium replenishment.
- Chinese patent CN201911413503.0 discloses a liquid phase lithium replenishment method for positive and negative electrode materials of lithium batteries, and CN202210050429.6 also discloses a lithium battery lithium replenishment and manufacturing method. However, these methods are relatively complicated and are not suitable for lithium replenishment of waste lithium batteries.
- the prior art does not solve the problem of fast and efficient lithium replenishment of lithium battery positive electrode materials.
- the purpose of the present invention is to propose a technical solution for replenishing lithium of waste lithium battery positive electrode materials using low-temperature plasma technology, especially atmospheric pressure plasma.
- the purpose of the present invention is to use atmospheric pressure plasma technology to replenish lithium for waste lithium battery positive electrode materials, replenish consumed lithium ions, thereby increasing the capacity of lithium ion batteries and achieving regeneration of waste lithium battery positive electrode materials.
- One aspect of the present invention provides a lithium replenishing device for lithium battery positive electrode materials, which includes a low-temperature plasma activation device, a container containing a lithium ion solution, an atmospheric pressure plasma generating device, a heating and drying device, and an annealing device.
- the atmospheric pressure plasma generating device is selected from a dielectric barrier discharge plasma generating device, a plasma jet plasma generating device, and a surface discharge plasma generating device.
- the atmospheric pressure plasma generating device comprises a gas source used for discharge, and the gas of the gas source is a combination of one or more of air, argon, helium, and nitrogen.
- the low-temperature plasma activation device is a low-pressure low-temperature plasma or atmospheric pressure plasma generating device.
- the low-temperature plasma activation device is selected from a jet plasma generator, a low-pressure air plasma generator, a low-pressure oxygen plasma generator, an atmospheric pressure argon plasma generator, and an atmospheric pressure argon plasma jet generator.
- the lithium ion solution is a solution containing at least one of lithium chloride, lithium hydroxide, lithium sulfate, lithium nitrate, lithium bromide, and lithium phosphate.
- the solvent in the solution is water or an organic solvent that can dissolve lithium ion salts.
- the drying device can provide a drying temperature of 50-200°C.
- the annealing device can provide an annealing temperature of 400-1000°C.
- the positive electrode of the lithium-ion battery is selected from at least one of lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, lithium iron phosphate, lithium manganese iron phosphate, lithium cobalt oxide or lithium manganese oxide.
- the lithium replenishing device further comprises a flotation device, wherein the flotation device comprises a solvent capable of suspending carbon impurities and precipitating positive electrode materials, and the positive electrode materials are selected from lithium iron phosphate and lithium manganese iron phosphate.
- Another aspect of the present invention provides a method for replenishing lithium of a positive electrode material of a lithium battery, the method comprising the following steps:
- the method does not include a step of heating the solution containing lithium ions.
- the lithium ions in the solution containing lithium ions come from at least one of lithium chloride, lithium hydroxide, lithium sulfate, lithium nitrate, lithium bromide, and lithium phosphate.
- the concentration of lithium ions in the solution containing lithium ions is 0.1-2 mol/L
- the solvent in the solution containing lithium ions is selected from water and a polar organic solvent
- the polar organic solvent is selected from at least one of formamide, N,N-dimethylformamide, N-methylpyrrolidone, 1,3-dimethyl-2-imidazolidinone and tetrahydrofuran.
- the solution containing lithium ions does not contain other chemical reagents.
- the other chemical reagents are selected from acidic compounds, alkaline compounds, catalysts, activators, and surfactants.
- the positive electrode material of the lithium-ion battery is selected from at least one of lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, lithium iron phosphate, lithium manganese iron phosphate, lithium cobalt oxide or lithium manganese oxide.
- the positive electrode of the lithium-ion battery is a waste positive electrode of a lithium-ion battery that has been used for a period of time.
- step S1) the plasma cleaning activation time is 1-10 min to obtain an activated positive electrode material.
- step S1) when the positive electrode material is lithium iron phosphate or lithium iron manganese phosphate, it also includes a step of further removing carbon impurities by flotation method.
- the flotation method is a method of dispersing the activated positive electrode material in a solvent to precipitate it, suspending carbon impurities in the solvent at the same time, and collecting the positive electrode material precipitate at the bottom.
- the solvent used is a mixed solvent of water and a polar organic solvent miscible with water in a volume ratio of 1:0.2-5.
- the low-temperature plasma in step S1) is low-pressure low-temperature plasma or atmospheric pressure plasma.
- step S3) is 1-30 min.
- the atmospheric pressure plasma may be produced by dielectric barrier discharge, plasma jet, or surface discharge.
- step S3 the drying temperature is 50-200° C., and the drying time is 0.2-24 h.
- the annealing temperature in step S3) is 400-1000°C.
- lithium iron phosphate or lithium iron manganese phosphate is annealed in an inert gas atmosphere at 400-800°C for 0.5-2 h; lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, lithium cobalt oxide, and lithium manganese oxide are annealed in an atmospheric environment at 700-950°C for 0.5-2 h.
- the present invention can achieve rapid lithium replenishment of the positive electrode material of the lithium battery at room temperature, and can complete the repair and regeneration of the positive electrode material of the lithium battery in combination with the annealing process.
- Figure 1 is an XRD diagram of the lithium cobalt oxide positive electrode material before and after lithium supplementation.
- Figure 2 is an XRD diagram of the nickel cobalt manganese oxide positive electrode material before and after lithium supplementation.
- FIG3 is an XRD diagram of the lithium iron phosphate positive electrode material before and after lithium supplementation.
- FIG4 is a charge and discharge diagram of a lithium iron phosphate button half-cell after plasma lithium supplementation.
- the discharge power of the plasma is not limited, because those skilled in the art can adjust the discharge power according to the generating device, gas and flow rate and the situation of the solution to be treated, and it is only necessary to ensure that the atmospheric pressure plasma acts on the solution containing the positive electrode material and lithium ions.
- functional group gases such as oxygen or water vapor can also be added during the generation of the atmospheric pressure plasma.
- the generation mode of the plasma, the generated gas pressure, the excitation power supply and other conditions can also be adjusted.
- the positive electrode material is a material obtained by stripping the current collector from the positive electrode sheet.
- the stripping means of the current collector may be existing methods, such as manual stripping, aqueous solution stripping (mainly the negative electrode sheet) or organic solvent stripping (mainly the positive electrode sheet).
- Example 1 Lithium battery positive electrode material lithium cobalt oxide lithium supplement
- the lithium supplementation method comprises the following steps:
- the repaired lithium cobalt oxide positive electrode material is obtained by discharging the material using air dielectric barrier discharge plasma for 10 min, then drying the material at 50° C. for 24 h, and annealing the material at 950° C. in an atmospheric environment for 0.5 h.
- Example 2 Lithium battery positive electrode material lithium cobalt oxide lithium supplement
- the lithium supplementation method comprises the following steps:
- the repaired lithium cobalt oxide positive electrode material is obtained by discharging the material using an argon plasma jet for 1 min, then drying the material at 80° C. for 10 h, and annealing the material at 700° C. for 2 h in an atmospheric environment in a ceramic crucible.
- Example 3 Lithium replenishment of lithium battery positive electrode material lithium nickel cobalt aluminum oxide
- the lithium supplementation method comprises the following steps:
- the repaired nickel cobalt aluminum oxide positive electrode material is obtained by performing discharge treatment using air surface discharge plasma for 20 min, then drying at 200° C. for 0.2 h, placing the material in a ceramic crucible and annealing at 850° C. in an atmospheric environment for 2 h.
- the capacity of the button half-cell assembled using the repair material was restored to 95% of commercial lithium nickel cobalt aluminum oxide.
- Example 4 Lithium replenishment of lithium nickel cobalt manganese oxide, a positive electrode material of lithium batteries
- the lithium supplementation method comprises the following steps:
- the repaired nickel cobalt manganese oxide lithium positive electrode material is obtained by discharging the material using an atmospheric pressure helium plasma jet for 15 min, drying the material at 70° C. for 10 h, and annealing the material at 850° C. for 1 h in an atmospheric environment in a ceramic crucible.
- the capacity of the button half-cell assembled using the repair material was restored to 98% of commercial lithium nickel cobalt manganese oxide.
- the XRD experimental results are shown in Figure 2. From the XRD results, it can be seen that the peak splitting at about 44 degrees of the original positive electrode material disappears after repair, but the peak splitting at about 37 degrees of the sample without plasma treatment is not obvious. The splitting degree of these two peaks represents the integrity of the layered structure. In addition, the ratio of the two peak intensities (003) and (104) represents the mixing of lithium ions and nickel ions. The larger the value, the smaller the mixing. The sample treated with plasma has a smaller mixing, indicating that lithium replenishment of the positive electrode material is achieved through plasma treatment.
- Example 5 Lithium supplementation of lithium iron phosphate, a positive electrode material of a lithium battery
- the lithium supplementation method comprises the following steps:
- the repaired lithium iron phosphate positive electrode material is obtained by discharging the material using an argon dielectric barrier discharge plasma for 10 min, then drying the material at 100° C. for 24 h, and annealing the material at 700° C. for 2 h in a graphite crucible in a nitrogen environment.
- the XRD experimental results are shown in Figure 3.
- the original lithium iron phosphate sample has impurities, and the impurities disappear completely after plasma treatment, indicating that plasma treatment can achieve lithium replenishment and repair of lithium iron phosphate.
- the charge and discharge results are shown in Figure 4.
- the discharge capacity of the original lithium iron phosphate decays to 110 mAh/g, and the discharge capacity of the plasma treated sample recovers to 158 mAh/g.
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- Manufacturing & Machinery (AREA)
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- Battery Electrode And Active Subsutance (AREA)
Abstract
The present invention provides a plasma lithium supplementing device and method for a positive electrode material for a lithium battery. The present application particularly discloses that the lithium supplementing device comprises a low-temperature plasma activation device, a container containing a lithium ion solution, an atmospheric pressure plasma generation device, a heating and drying device, and an annealing device. The present application further discloses that the lithium supplementing method comprises: S1) cleaning and activating a positive electrode material of a waste lithium battery by using low-temperature plasma; S2) placing the cleaned and activated positive electrode material in a solution containing lithium ions; and S3) treating the solution by using atmospheric pressure plasma, and then drying and annealing a solid material. According to the present invention, rapid lithium supplementing of the positive electrode material for the lithium battery is realized at normal temperature, and by combining the annealing process, repair and regeneration of the positive electrode material for the lithium battery can be completed.
Description
本发明属于废弃电池中金属材料循环利用领域,具体涉及一种锂电池用正极材料的等离子体补锂体系及方法。The present invention belongs to the field of recycling metal materials in waste batteries, and specifically relates to a plasma lithium replenishment system and method for positive electrode materials for lithium batteries.
锂电池在充放电过程中,会消耗正极中的锂离子,造成不可逆的容量损失。可以通过补锂的方法来对消耗掉的锂离子进行补充,从而提升锂离子电池的容量。例如,通过将锂金属、负极材料和非水溶剂混合形成浆料涂覆到集流体上,使得锂扩散到活性材料内部方式补锂;采用金属锂箔贴合负极进行复合,在电池注液后使金属锂和负极反应嵌入负极材料中进行补锂。中国专利CN201911413503.0公开了一种锂电池正负极材料液相补锂方法、CN202210050429.6也公开了一种锂电池补锂和制作方法等。然而,这些方法较为复杂,且不适合用于废旧锂电池的补锂。During the charging and discharging process, lithium batteries consume lithium ions in the positive electrode, resulting in irreversible capacity loss. The consumed lithium ions can be replenished by lithium replenishment methods, thereby increasing the capacity of lithium-ion batteries. For example, lithium metal, negative electrode materials and non-aqueous solvents are mixed to form a slurry and coated on the current collector, so that lithium diffuses into the active material to replenish lithium; metal lithium foil is used to bond the negative electrode for composite, and after the battery is filled with liquid, the metal lithium and the negative electrode react and embed into the negative electrode material for lithium replenishment. Chinese patent CN201911413503.0 discloses a liquid phase lithium replenishment method for positive and negative electrode materials of lithium batteries, and CN202210050429.6 also discloses a lithium battery lithium replenishment and manufacturing method. However, these methods are relatively complicated and are not suitable for lithium replenishment of waste lithium batteries.
现有技术没有解决锂电池正极材料快速高效补锂的问题。针对现有技术存在的问题,本发明的目的在于提出一种用低温等离子体技术,特别是大气压等离子体来对废旧锂电池正极材料进行补锂的技术方案。The prior art does not solve the problem of fast and efficient lithium replenishment of lithium battery positive electrode materials. In view of the problems existing in the prior art, the purpose of the present invention is to propose a technical solution for replenishing lithium of waste lithium battery positive electrode materials using low-temperature plasma technology, especially atmospheric pressure plasma.
本发明的目的在于利用大气压等离子体技术来对废旧锂电池正极材料进行补锂,对消耗掉的锂离子进行补充,从而提升锂离子电池的容量,实现废旧锂电池正极材料的再生。The purpose of the present invention is to use atmospheric pressure plasma technology to replenish lithium for waste lithium battery positive electrode materials, replenish consumed lithium ions, thereby increasing the capacity of lithium ion batteries and achieving regeneration of waste lithium battery positive electrode materials.
本发明一个方面提供了一种锂电池正极材料的补锂装置,其包括低温等离子体活化装置、包含锂离子溶液的容器、以及大气压等离子体发生装置、加温干燥装置以及退火装置。One aspect of the present invention provides a lithium replenishing device for lithium battery positive electrode materials, which includes a low-temperature plasma activation device, a container containing a lithium ion solution, an atmospheric pressure plasma generating device, a heating and drying device, and an annealing device.
进一步地,大气压等离子体发生装置选自采用介质阻挡放电等离子体发生装置、等离子体射流等离子体发生装置、沿面放电等离子体发生装置。Furthermore, the atmospheric pressure plasma generating device is selected from a dielectric barrier discharge plasma generating device, a plasma jet plasma generating device, and a surface discharge plasma generating device.
进一步地,大气压等离子体发生装置包含放电所使用气源,所述气源的气体为空气、氩气、氦气、氮气中的一种或多种的组合物。Furthermore, the atmospheric pressure plasma generating device comprises a gas source used for discharge, and the gas of the gas source is a combination of one or more of air, argon, helium, and nitrogen.
进一步地,低温等离子体活化装置为低气压低温等离子体或大气压等离子体发生装置。Furthermore, the low-temperature plasma activation device is a low-pressure low-temperature plasma or atmospheric pressure plasma generating device.
进一步地,低温等离子体活化装置选自射流等离子体发生装置、低气压空气等离子体发生装置、低气压氧气等离子体发生装置、大气压氩气等离子体发生装置、大气压氩气等离子体射流发生装置。Furthermore, the low-temperature plasma activation device is selected from a jet plasma generator, a low-pressure air plasma generator, a low-pressure oxygen plasma generator, an atmospheric pressure argon plasma generator, and an atmospheric pressure argon plasma jet generator.
进一步地,包含锂离子溶液为包含氯化锂、氢氧化锂、硫酸锂、硝酸锂、溴化锂、磷酸锂中至少一种的溶液,更进一步地,所述溶液中的溶剂为水或能够溶剂锂离子盐的有机溶剂。Furthermore, the lithium ion solution is a solution containing at least one of lithium chloride, lithium hydroxide, lithium sulfate, lithium nitrate, lithium bromide, and lithium phosphate. Furthermore, the solvent in the solution is water or an organic solvent that can dissolve lithium ion salts.
进一步地,干燥装置能够提供50-200 ℃的干燥温度。Furthermore, the drying device can provide a drying temperature of 50-200°C.
进一步地,所述退火装置能够提供400-1000℃的退火温度。Furthermore, the annealing device can provide an annealing temperature of 400-1000°C.
进一步地,锂离子电池正极选自以包含了镍钴锰酸锂、镍钴铝酸锂、磷酸铁锂、磷酸锰铁锂、钴酸锂或锰酸锂中的至少一种。Furthermore, the positive electrode of the lithium-ion battery is selected from at least one of lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, lithium iron phosphate, lithium manganese iron phosphate, lithium cobalt oxide or lithium manganese oxide.
进一步地,所述补锂装置还包含浮选装置,所述浮选装置中包含能够悬浮碳杂质,并沉淀正极材料的溶剂,所述的正极材料选自磷酸铁锂、磷酸锰铁锂。Furthermore, the lithium replenishing device further comprises a flotation device, wherein the flotation device comprises a solvent capable of suspending carbon impurities and precipitating positive electrode materials, and the positive electrode materials are selected from lithium iron phosphate and lithium manganese iron phosphate.
本发明另一个方面提供了一种锂电池正极材料的补锂方法,所述补锂方法包括以下步骤:Another aspect of the present invention provides a method for replenishing lithium of a positive electrode material of a lithium battery, the method comprising the following steps:
S1) 采用低温等离子体清洗活化废旧锂电池正极材料;S1) Using low-temperature plasma to clean and activate the cathode material of waste lithium batteries;
S2)
将清洗活化后的正极材料置于含有锂离子的溶液中,S2)
Put the cleaned and activated positive electrode material in a solution containing lithium ions.
S3)
利用大气压等离子体处理上述溶液,随后将固体材料进行干燥并退火。S3)
The solution is treated with atmospheric pressure plasma, and the solid material is then dried and annealed.
进一步地,不包含对含有锂离子的溶液中加热的步骤。Furthermore, the method does not include a step of heating the solution containing lithium ions.
进一步地,所述含有锂离子的溶液中的锂离子来自氯化锂、氢氧化锂、硫酸锂、硝酸锂、溴化锂、磷酸锂中的至少一种。Furthermore, the lithium ions in the solution containing lithium ions come from at least one of lithium chloride, lithium hydroxide, lithium sulfate, lithium nitrate, lithium bromide, and lithium phosphate.
进一步地,所述含有锂离子的溶液中的锂离子的浓度为0.1-2mol/LFurthermore, the concentration of lithium ions in the solution containing lithium ions is 0.1-2 mol/L
进一步地,所述含有锂离子的溶液中的溶剂选自水以及极性有机溶剂,所述极性有机溶剂选自甲酰胺、N,N-二甲基甲酰胺、N-甲基吡咯烷酮、1,3-二甲基-2-咪唑啉酮、四氢呋喃中的至少一种。Furthermore, the solvent in the solution containing lithium ions is selected from water and a polar organic solvent, and the polar organic solvent is selected from at least one of formamide, N,N-dimethylformamide, N-methylpyrrolidone, 1,3-dimethyl-2-imidazolidinone and tetrahydrofuran.
进一步地,所述含有锂离子的溶液不含有其他化学试剂。所述其他化学试剂选自酸性化合物、碱性化合物、催化剂、活化剂、表面活性剂。Furthermore, the solution containing lithium ions does not contain other chemical reagents. The other chemical reagents are selected from acidic compounds, alkaline compounds, catalysts, activators, and surfactants.
进一步地,锂离子电池正极材料选自以包含了镍钴锰酸锂、镍钴铝酸锂、磷酸铁锂、磷酸锰铁锂、钴酸锂或锰酸锂中的至少一种。Furthermore, the positive electrode material of the lithium-ion battery is selected from at least one of lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, lithium iron phosphate, lithium manganese iron phosphate, lithium cobalt oxide or lithium manganese oxide.
进一步地,所述锂离子电池正极为已经使用一段时间的废旧锂离子电池正极。Furthermore, the positive electrode of the lithium-ion battery is a waste positive electrode of a lithium-ion battery that has been used for a period of time.
进一步地,步骤S1)中等离子体清洗活化时间为1-10min,获得活化的正极材料。Furthermore, in step S1), the plasma cleaning activation time is 1-10 min to obtain an activated positive electrode material.
更进一步地,在步骤S1)中,当正极材料为磷酸铁锂或磷酸锰铁锂时,还包括进一步采用浮选法去除碳杂质的步骤。Furthermore, in step S1), when the positive electrode material is lithium iron phosphate or lithium iron manganese phosphate, it also includes a step of further removing carbon impurities by flotation method.
更进一步地,所述浮选法为通过将活化的正极材料分散在溶剂中使其沉淀,且能够同时将碳杂质悬浮在溶剂中,并收集底部正极材料沉淀的方法。在一些具体的实施方案中,采用的溶剂为水与能够与水互溶的极性有机溶剂以1:0.2-5的体积比进行混合的混合溶剂。Furthermore, the flotation method is a method of dispersing the activated positive electrode material in a solvent to precipitate it, suspending carbon impurities in the solvent at the same time, and collecting the positive electrode material precipitate at the bottom. In some specific embodiments, the solvent used is a mixed solvent of water and a polar organic solvent miscible with water in a volume ratio of 1:0.2-5.
进一步地,步骤S1)中的低温等离子体为低气压低温等离子体或大气压等离子体。Furthermore, the low-temperature plasma in step S1) is low-pressure low-temperature plasma or atmospheric pressure plasma.
进一步地,步骤S3)中的处理时间为1-30 min。Furthermore, the processing time in step S3) is 1-30 min.
进一步地,步骤S1)或S3)中大气压等离子体可以采用介质阻挡放电、等离子体射流、沿面放电。Furthermore, in step S1) or S3), the atmospheric pressure plasma may be produced by dielectric barrier discharge, plasma jet, or surface discharge.
进一步地,步骤S3)中干燥温度为50-200 ℃,干燥时间为0.2-24 h。Furthermore, in step S3), the drying temperature is 50-200° C., and the drying time is 0.2-24 h.
进一步地,步骤S3)中退火的温度为400-1000℃。在一些具体的实施方案中,根据正极材料分类,磷酸铁锂或磷酸锰铁锂为惰性气体氛围下,400~800 ℃,退火时间0.5~2
h;镍钴锰酸锂、镍钴铝酸锂、钴酸锂、锰酸锂为大气环境,700~950 ℃,退火时间为0.5~2 h。Further, the annealing temperature in step S3) is 400-1000°C. In some specific embodiments, according to the classification of the positive electrode material, lithium iron phosphate or lithium iron manganese phosphate is annealed in an inert gas atmosphere at 400-800°C for 0.5-2 h; lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, lithium cobalt oxide, and lithium manganese oxide are annealed in an atmospheric environment at 700-950°C for 0.5-2 h.
与现有技术相比,本发明在常温下实现锂电池正极材料的快速补锂,结合退火过程可完成锂电池正极材料的修复再生。Compared with the prior art, the present invention can achieve rapid lithium replenishment of the positive electrode material of the lithium battery at room temperature, and can complete the repair and regeneration of the positive electrode material of the lithium battery in combination with the annealing process.
图1为补锂前后的钴酸锂正极材料的XRD图。Figure 1 is an XRD diagram of the lithium cobalt oxide positive electrode material before and after lithium supplementation.
图2为补锂前后的镍钴锰酸锂正极材料的XRD图。Figure 2 is an XRD diagram of the nickel cobalt manganese oxide positive electrode material before and after lithium supplementation.
图3为补锂前后的磷酸铁锂正极材料的XRD图。FIG3 is an XRD diagram of the lithium iron phosphate positive electrode material before and after lithium supplementation.
图4 为等离子体补锂后的磷酸铁锂的扣式半电池充放电图。FIG4 is a charge and discharge diagram of a lithium iron phosphate button half-cell after plasma lithium supplementation.
为了使本发明的上述目的、特征和优点能够更加明显易懂,下面对本发明的具体实施方式做详细的说明,但不能理解为对本发明的可实施范围的限定。In order to make the above-mentioned objects, features and advantages of the present invention more obvious and understandable, the specific implementation modes of the present invention are described in detail below, but it should not be understood as limiting the applicable scope of the present invention.
在本发明的技术方案中,没有限定等离子体的放电功率,因为本领域技术人员可以根据发生装置、气体及流量以及待处理溶液的情况来进行调节放电功率,只需要确保大气压等离子体作用于含有正极材料和锂离子的溶液中即可。而且,为了加强反应效果,也可以在大气压等离子体产生过程中加入氧气或水蒸气等功能基团气体。同时,也可以在本发明的基础上,调节等离子体的产生方式、产生气压以及激发电源等条件。In the technical solution of the present invention, the discharge power of the plasma is not limited, because those skilled in the art can adjust the discharge power according to the generating device, gas and flow rate and the situation of the solution to be treated, and it is only necessary to ensure that the atmospheric pressure plasma acts on the solution containing the positive electrode material and lithium ions. Moreover, in order to enhance the reaction effect, functional group gases such as oxygen or water vapor can also be added during the generation of the atmospheric pressure plasma. At the same time, on the basis of the present invention, the generation mode of the plasma, the generated gas pressure, the excitation power supply and other conditions can also be adjusted.
在本发明中,正极材料为由正极极片剥离了集流体的材料,所述的集流体的剥离手段可以是现有的,例如人工剥离、水溶液剥离(主要是负极片)或者有机溶剂剥离(主要对象是正极片)。In the present invention, the positive electrode material is a material obtained by stripping the current collector from the positive electrode sheet. The stripping means of the current collector may be existing methods, such as manual stripping, aqueous solution stripping (mainly the negative electrode sheet) or organic solvent stripping (mainly the positive electrode sheet).
实施例 1锂电池正极材料钴酸锂的补锂
Example 1 Lithium battery positive electrode material lithium cobalt oxide lithium supplement
所述补锂方法包括以下步骤:The lithium supplementation method comprises the following steps:
S1)采用射流等离子体清洗活化钴酸锂电池正极材料5 min;S1) Using jet plasma to clean and activate the positive electrode material of lithium cobalt oxide battery for 5 min;
S2)将10g活化钴酸锂正极材料置于10 mL 0.2mol/L的氢氧化锂水溶液中;S2) placing 10 g of activated lithium cobalt oxide positive electrode material in 10 mL of 0.2 mol/L lithium hydroxide aqueous solution;
S3)利用空气介质阻挡放电等离子体进行放电处理10 min,随后50℃干燥24h,置于陶瓷坩埚中在大气环境950℃退火0.5h,即可获得修复的钴酸锂正极材料。S3) The repaired lithium cobalt oxide positive electrode material is obtained by discharging the material using air dielectric barrier discharge plasma for 10 min, then drying the material at 50° C. for 24 h, and annealing the material at 950° C. in an atmospheric environment for 0.5 h.
结果如图1所示,从XRD结果可以看出,未处理的正极材料位于18.5处的吸收峰在处理后消失,说明通过等离子体处理实现了正极材料的补锂。The results are shown in FIG1 . From the XRD results, it can be seen that the absorption peak of the untreated positive electrode material at 18.5 disappears after treatment, indicating that lithium replenishment of the positive electrode material is achieved through plasma treatment.
实施例 2锂电池正极材料钴酸锂的补锂
Example 2 Lithium battery positive electrode material lithium cobalt oxide lithium supplement
所述补锂方法包括以下步骤:The lithium supplementation method comprises the following steps:
S1)采用低气压空气等离子体清洗钴酸锂电池正极材料2 min;S1) Using low-pressure air plasma to clean the positive electrode material of lithium cobalt oxide battery for 2 min;
S2)将10g活化钴酸锂黑粉置于3 mL 2mol/L的氢氧化锂水溶液中形成泥状浆料;S2) placing 10 g of activated lithium cobalt oxide black powder in 3 mL of 2 mol/L lithium hydroxide aqueous solution to form a muddy slurry;
S3)利用氩气等离子体射流进行放电处理1 min,随后80℃干燥10h,置于陶瓷坩埚中在大气环境700℃退火2h,即可获得修复的钴酸锂正极材料。S3) The repaired lithium cobalt oxide positive electrode material is obtained by discharging the material using an argon plasma jet for 1 min, then drying the material at 80° C. for 10 h, and annealing the material at 700° C. for 2 h in an atmospheric environment in a ceramic crucible.
利用修复材料组装的扣式半电池容量恢复至商业钴酸锂的97%。The capacity of the button half-cell assembled using the repair material was restored to 97% of commercial lithium cobalt oxide.
实施例 3锂电池正极材料镍钴铝酸锂的补锂
Example 3 Lithium replenishment of lithium battery positive electrode material lithium nickel cobalt aluminum oxide
所述补锂方法包括以下步骤:The lithium supplementation method comprises the following steps:
S1)采用低气压氧气等离子体处理钴酸锂电池正极片1 min;S1) treating the positive electrode of the lithium cobalt oxide battery with low-pressure oxygen plasma for 1 min;
S2)将10g活化镍钴铝酸锂黑粉置于10 mL 1mol/L的硫酸锂水溶液中;S2) placing 10 g of activated nickel cobalt aluminum lithium black powder in 10 mL of 1 mol/L lithium sulfate aqueous solution;
S3)利用空气沿面放电等离子体进行放电处理20 min,随后200℃干燥0.2h,置于陶瓷坩埚中在大气环境850℃退火2h,即可获得修复的镍钴铝酸锂正极材料。S3) The repaired nickel cobalt aluminum oxide positive electrode material is obtained by performing discharge treatment using air surface discharge plasma for 20 min, then drying at 200° C. for 0.2 h, placing the material in a ceramic crucible and annealing at 850° C. in an atmospheric environment for 2 h.
利用修复材料组装的扣式半电池容量恢复至商业镍钴铝酸锂的95%。The capacity of the button half-cell assembled using the repair material was restored to 95% of commercial lithium nickel cobalt aluminum oxide.
实施例 4锂电池正极材料镍钴锰酸锂的补锂
Example 4: Lithium replenishment of lithium nickel cobalt manganese oxide, a positive electrode material of lithium batteries
所述补锂方法包括以下步骤:The lithium supplementation method comprises the following steps:
S1)采用大气压氩气等离子体处理镍钴锰酸锂2 min;S1) treating lithium nickel cobalt manganese oxide with atmospheric pressure argon plasma for 2 min;
S2)将10g活化镍钴锰酸锂黑粉置于10 mL 0.1mol/L的硝酸锂水溶液中;S2) placing 10 g of activated nickel cobalt lithium manganese oxide black powder in 10 mL of 0.1 mol/L lithium nitrate aqueous solution;
S3)利用大气压氦气等离子体射流进行放电处理15 min,随后70℃干燥10h,置于陶瓷坩埚中在大气环境850℃退火1h,即可获得修复的镍钴锰酸锂正极材料。S3) The repaired nickel cobalt manganese oxide lithium positive electrode material is obtained by discharging the material using an atmospheric pressure helium plasma jet for 15 min, drying the material at 70° C. for 10 h, and annealing the material at 850° C. for 1 h in an atmospheric environment in a ceramic crucible.
利用修复材料组装的扣式半电池容量恢复至商业镍钴锰酸锂的98%。The capacity of the button half-cell assembled using the repair material was restored to 98% of commercial lithium nickel cobalt manganese oxide.
XRD实验结果如图2所示,从XRD结果可以看出原始的正极材料44度左右的峰劈裂,经修复后劈裂消失,但是未经等离子体处理的样品37度左右的峰劈裂不明显,这两个峰的劈裂程度代表着层状结构的完整性,另外(003)和(104)两个峰强的比值代表着锂离子与镍离子的混排,值越大混排越小,经等离子体处理的样品混排较小,说明通过等离子体处理实现正极材料的补锂。The XRD experimental results are shown in Figure 2. From the XRD results, it can be seen that the peak splitting at about 44 degrees of the original positive electrode material disappears after repair, but the peak splitting at about 37 degrees of the sample without plasma treatment is not obvious. The splitting degree of these two peaks represents the integrity of the layered structure. In addition, the ratio of the two peak intensities (003) and (104) represents the mixing of lithium ions and nickel ions. The larger the value, the smaller the mixing. The sample treated with plasma has a smaller mixing, indicating that lithium replenishment of the positive electrode material is achieved through plasma treatment.
实施例 5锂电池正极材料磷酸铁锂的补锂
Example 5 Lithium supplementation of lithium iron phosphate, a positive electrode material of a lithium battery
所述补锂方法包括以下步骤:The lithium supplementation method comprises the following steps:
S1)采用大气压氩气等离子体射流处理磷酸铁锂黑粉2 min,采用水:N,N-二甲基甲酰胺为1:2 的混合溶液进行浮选,收集底部材料获得磷酸铁锂黑粉;S1) treating lithium iron phosphate black powder with an atmospheric pressure argon plasma jet for 2 min, flotation with a mixed solution of water: N,N-dimethylformamide in a ratio of 1:2, and collecting the bottom material to obtain lithium iron phosphate black powder;
S2)将10g活化磷酸铁锂黑粉置于10 mL 0.5mol/L的氯化锂N,N-二甲基甲酰胺溶液中;S2) placing 10 g of activated lithium iron phosphate black powder in 10 mL of 0.5 mol/L lithium chloride N,N-dimethylformamide solution;
S3)利用氩气介质阻挡放电等离子体进行放电处理10 min,随后100℃干燥24h,置于石墨坩埚中在氮气气环境700℃退火2h,即可获得修复的磷酸铁锂正极材料。S3) The repaired lithium iron phosphate positive electrode material is obtained by discharging the material using an argon dielectric barrier discharge plasma for 10 min, then drying the material at 100° C. for 24 h, and annealing the material at 700° C. for 2 h in a graphite crucible in a nitrogen environment.
性能恢复至商业磷酸铁锂的98%。The performance recovered to 98% of commercial lithium iron phosphate.
XRD实验结果如图3所示,原始磷酸铁锂样本有杂相出现,采用等离子体处理样本杂相完全消失,说明等离子体处理样本可实现磷酸铁锂的补锂和修复。充放电结果如图4所示,原始磷酸铁锂放电容量衰减至110 mAh/g,采用等离子体处理样本放电容量恢复至158 mAh/g。The XRD experimental results are shown in Figure 3. The original lithium iron phosphate sample has impurities, and the impurities disappear completely after plasma treatment, indicating that plasma treatment can achieve lithium replenishment and repair of lithium iron phosphate. The charge and discharge results are shown in Figure 4. The discharge capacity of the original lithium iron phosphate decays to 110 mAh/g, and the discharge capacity of the plasma treated sample recovers to 158 mAh/g.
Claims (10)
- 一种锂电池正极材料的补锂装置,其特征在于,其包括低温等离子体活化装置、包含锂离子溶液的容器、以及大气压等离子体发生装置、加温干燥装置以及退火装置;A lithium replenishing device for lithium battery positive electrode material, characterized in that it comprises a low-temperature plasma activation device, a container containing a lithium ion solution, an atmospheric pressure plasma generating device, a heating and drying device, and an annealing device;优选地,锂离子电池正极选自以包含了镍钴锰酸锂、镍钴铝酸锂、磷酸铁锂、磷酸锰铁锂、钴酸锂或锰酸锂中的至少一种。Preferably, the positive electrode of the lithium-ion battery is selected from at least one of lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, lithium iron phosphate, lithium manganese iron phosphate, lithium cobalt oxide or lithium manganese oxide.
- 根据权利要求1所述的补锂装置,其特征在于,低温等离子体活化装置为低气压低温等离子体或大气压等离子体发生装置;The lithium replenishment device according to claim 1, characterized in that the low-temperature plasma activation device is a low-pressure low-temperature plasma or atmospheric pressure plasma generating device;大气压等离子体发生装置选自采用介质阻挡放电等离子体发生装置、等离子体射流等离子体发生装置、沿面放电等离子体发生装置;The atmospheric pressure plasma generating device is selected from a dielectric barrier discharge plasma generating device, a plasma jet plasma generating device, and a surface discharge plasma generating device;优选地,大气压等离子体发生装置包含放电所使用气源,所述气源的气体为空气、氩气、氦气、氮气中的一种或多种的组合物。Preferably, the atmospheric pressure plasma generating device comprises a gas source used for discharge, and the gas of the gas source is a combination of one or more of air, argon, helium and nitrogen.优选地,低温等离子体活化装置选自射流等离子体发生装置、低气压空气等离子体发生装置、低气压氧气等离子体发生装置、大气压氩气等离子体发生装置、大气压氩气等离子体射流发生装置;Preferably, the low-temperature plasma activation device is selected from a jet plasma generator, a low-pressure air plasma generator, a low-pressure oxygen plasma generator, an atmospheric pressure argon plasma generator, and an atmospheric pressure argon plasma jet generator;优选地,所述补锂装置还包含浮选装置,所述浮选装置中包含能够悬浮碳杂质,并沉淀正极材料的溶剂,所述的正极材料选自磷酸铁锂、磷酸锰铁锂。Preferably, the lithium replenishing device further comprises a flotation device, wherein the flotation device comprises a solvent capable of suspending carbon impurities and precipitating positive electrode materials, and the positive electrode materials are selected from lithium iron phosphate and lithium manganese iron phosphate.
- 根据权利要求1所述的补锂装置,其特征在于,包含锂离子溶液为包含氯化锂、氢氧化锂、硫酸锂、硝酸锂、溴化锂、磷酸锂中至少一种的溶液;The lithium replenishing device according to claim 1, characterized in that the lithium ion solution is a solution containing at least one of lithium chloride, lithium hydroxide, lithium sulfate, lithium nitrate, lithium bromide, and lithium phosphate;优选地,所述溶液中的溶剂为水或能够溶剂锂离子盐的有机溶剂。Preferably, the solvent in the solution is water or an organic solvent capable of dissolving lithium ion salts.
- 根据权利要求1所述的补锂装置,其特征在于,所述退火装置能够提供400-1000℃的退火温度。The lithium replenishing device according to claim 1 is characterized in that the annealing device can provide an annealing temperature of 400-1000°C.
- 一种锂电池正极材料的补锂方法,其特征在于,所述补锂方法包括以下步骤:A lithium replenishment method for a lithium battery positive electrode material, characterized in that the lithium replenishment method comprises the following steps:S1) 采用低温等离子体清洗活化废旧锂电池正极材料;S1) Using low-temperature plasma to clean and activate the cathode material of waste lithium batteries;S2) 将清洗活化后的正极材料置于含有锂离子的溶液中,S2) Put the cleaned and activated positive electrode material in a solution containing lithium ions.S3) 利用大气压等离子体处理上述溶液,随后将固体材料进行干燥并退火;S3) The solution is treated with atmospheric pressure plasma, followed by drying and annealing the solid material;优选地,锂离子电池正极材料选自以包含了镍钴锰酸锂、镍钴铝酸锂、磷酸铁锂、磷酸锰铁锂、钴酸锂或锰酸锂中的至少一种。Preferably, the positive electrode material of the lithium-ion battery is selected from at least one of lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, lithium iron phosphate, lithium manganese iron phosphate, lithium cobalt oxide or lithium manganese oxide.
- 权利要求5所述的补锂方法,其特征在于,所述含有锂离子的溶液中的锂离子来自氯化锂、氢氧化锂、硫酸锂、硝酸锂、溴化锂、磷酸锂中的至少一种;The lithium supplementation method according to claim 5, characterized in that the lithium ions in the solution containing lithium ions are from at least one of lithium chloride, lithium hydroxide, lithium sulfate, lithium nitrate, lithium bromide, and lithium phosphate;优选地,所述含有锂离子的溶液中的锂离子的浓度为0.1-2mol/L;Preferably, the concentration of lithium ions in the solution containing lithium ions is 0.1-2 mol/L;优选地,所述含有锂离子的溶液中的溶剂选自水以及极性有机溶剂,所述极性有机溶剂选自甲酰胺、N,N-二甲基甲酰胺、N-甲基吡咯烷酮、1,3-二甲基-2-咪唑啉酮、四氢呋喃中的至少一种。Preferably, the solvent in the solution containing lithium ions is selected from water and a polar organic solvent, and the polar organic solvent is selected from at least one of formamide, N,N-dimethylformamide, N-methylpyrrolidone, 1,3-dimethyl-2-imidazolidinone and tetrahydrofuran.
- 权利要求5所述的补锂方法,其特征在于,步骤S1)中的低温等离子体为低气压低温等离子体或大气压等离子体;The lithium supplementation method according to claim 5 is characterized in that the low-temperature plasma in step S1) is low-pressure low-temperature plasma or atmospheric pressure plasma;优选地,步骤S1)中等离子体清洗活化时间为1-10min,获得活化的正极材料;Preferably, in step S1), the plasma cleaning activation time is 1-10 min to obtain an activated positive electrode material;优选地,在步骤S1)中,当正极材料为磷酸铁锂或磷酸锰铁锂时,还包括进一步采用浮选法去除碳杂质的步骤;Preferably, in step S1), when the positive electrode material is lithium iron phosphate or lithium iron manganese phosphate, it also includes a step of further removing carbon impurities by flotation method;更优选地,所述浮选法为通过将活化的正极材料分散在溶剂中使其沉淀,且能够同时将碳杂质悬浮在溶剂中,并收集底部正极材料沉淀的方法。More preferably, the flotation method is a method of dispersing the activated cathode material in a solvent to precipitate the activated cathode material, suspending carbon impurities in the solvent at the same time, and collecting the cathode material precipitate at the bottom.
- 权利要求5所述的补锂方法,其特征在于,步骤S1)或S3)中大气压等离子体可以采用介质阻挡放电、等离子体射流、沿面放电;The lithium replenishment method according to claim 5 is characterized in that the atmospheric pressure plasma in step S1) or S3) can be dielectric barrier discharge, plasma jet, or surface discharge;优选地,步骤S3)中的大气压等离子体处理时间为1-30 min。Preferably, the atmospheric pressure plasma treatment time in step S3) is 1-30 min.
- 权利要求5所述的补锂方法,其特征在于,步骤S3)中干燥温度为50-200 ℃,干燥时间为0.1-24 h。The lithium supplementation method according to claim 5 is characterized in that in step S3), the drying temperature is 50-200°C and the drying time is 0.1-24 h.
- 权利要求5所述的补锂方法,其特征在于,步骤S3)中退火的温度为400-1000℃,退火时间为0.5-2小时。The lithium replenishing method according to claim 5 is characterized in that the annealing temperature in step S3) is 400-1000°C and the annealing time is 0.5-2 hours.
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CN114388923A (en) * | 2022-01-19 | 2022-04-22 | 四川欣联伍材料科技有限公司 | Method for repairing and regenerating waste lithium iron phosphate anode material and lithium iron phosphate anode material |
US20220223379A1 (en) * | 2021-01-11 | 2022-07-14 | 6K Inc. | Methods and systems for reclamation of li-ion cathode materials using microwave plasma processing |
CN114976334A (en) * | 2022-05-25 | 2022-08-30 | 中国科学院化学研究所 | Direct regeneration method of waste lithium ion battery anode material |
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CN107919508A (en) * | 2016-10-11 | 2018-04-17 | 中国科学院过程工程研究所 | A kind of method that positive electrode is remanufactured using waste and old lithium ion battery |
US20220223379A1 (en) * | 2021-01-11 | 2022-07-14 | 6K Inc. | Methods and systems for reclamation of li-ion cathode materials using microwave plasma processing |
CN114388923A (en) * | 2022-01-19 | 2022-04-22 | 四川欣联伍材料科技有限公司 | Method for repairing and regenerating waste lithium iron phosphate anode material and lithium iron phosphate anode material |
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