CN105336947A - Lithium manganese phosphate chloride electrode material and preparation method thereof - Google Patents
Lithium manganese phosphate chloride electrode material and preparation method thereof Download PDFInfo
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- CN105336947A CN105336947A CN201510625593.5A CN201510625593A CN105336947A CN 105336947 A CN105336947 A CN 105336947A CN 201510625593 A CN201510625593 A CN 201510625593A CN 105336947 A CN105336947 A CN 105336947A
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- chlorophosphate
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- 239000007772 electrode material Substances 0.000 title claims abstract description 28
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- VIXUABYKEZCHNT-UHFFFAOYSA-K lithium hydrogen phosphate manganese(2+) chloride Chemical compound [Cl-].[Mn+2].[Li+].P(=O)([O-])([O-])O VIXUABYKEZCHNT-UHFFFAOYSA-K 0.000 title 1
- 229910052744 lithium Inorganic materials 0.000 claims abstract description 43
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims abstract description 38
- 239000011572 manganese Substances 0.000 claims abstract description 26
- 239000002245 particle Substances 0.000 claims abstract description 21
- -1 lithium manganese chlorophosphate Chemical compound 0.000 claims abstract description 18
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910052748 manganese Inorganic materials 0.000 claims abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 12
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 11
- 239000011574 phosphorus Substances 0.000 claims abstract description 11
- 150000001450 anions Chemical class 0.000 claims abstract description 10
- 239000002994 raw material Substances 0.000 claims abstract description 7
- 150000007524 organic acids Chemical group 0.000 claims abstract description 6
- 239000000843 powder Substances 0.000 claims description 34
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- 229910000388 diammonium phosphate Inorganic materials 0.000 claims description 14
- 235000019838 diammonium phosphate Nutrition 0.000 claims description 14
- XIXADJRWDQXREU-UHFFFAOYSA-M lithium acetate Chemical compound [Li+].CC([O-])=O XIXADJRWDQXREU-UHFFFAOYSA-M 0.000 claims description 12
- 239000002002 slurry Substances 0.000 claims description 9
- 229910019142 PO4 Inorganic materials 0.000 claims description 8
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 8
- 239000010452 phosphate Substances 0.000 claims description 8
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 7
- 239000008103 glucose Substances 0.000 claims description 7
- 230000001681 protective effect Effects 0.000 claims description 7
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 5
- 239000000460 chlorine Substances 0.000 claims description 5
- XKPJKVVZOOEMPK-UHFFFAOYSA-M lithium;formate Chemical compound [Li+].[O-]C=O XKPJKVVZOOEMPK-UHFFFAOYSA-M 0.000 claims description 5
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 5
- YNQRWVCLAIUHHI-UHFFFAOYSA-L dilithium;oxalate Chemical compound [Li+].[Li+].[O-]C(=O)C([O-])=O YNQRWVCLAIUHHI-UHFFFAOYSA-L 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 4
- 229940071264 lithium citrate Drugs 0.000 claims description 4
- WJSIUCDMWSDDCE-UHFFFAOYSA-K lithium citrate (anhydrous) Chemical compound [Li+].[Li+].[Li+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O WJSIUCDMWSDDCE-UHFFFAOYSA-K 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 claims description 3
- 229910052786 argon Inorganic materials 0.000 claims description 3
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims 1
- 239000004094 surface-active agent Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 8
- 238000001354 calcination Methods 0.000 abstract description 7
- ITVPBBDAZKBMRP-UHFFFAOYSA-N chloro-dioxido-oxo-$l^{5}-phosphane;hydron Chemical compound OP(O)(Cl)=O ITVPBBDAZKBMRP-UHFFFAOYSA-N 0.000 abstract description 7
- 238000004146 energy storage Methods 0.000 abstract description 3
- GELKBWJHTRAYNV-UHFFFAOYSA-K lithium iron phosphate Chemical compound [Li+].[Fe+2].[O-]P([O-])([O-])=O GELKBWJHTRAYNV-UHFFFAOYSA-K 0.000 abstract description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 abstract 1
- 239000011261 inert gas Substances 0.000 abstract 1
- 150000002641 lithium Chemical class 0.000 abstract 1
- 238000003746 solid phase reaction Methods 0.000 abstract 1
- 238000010671 solid-state reaction Methods 0.000 abstract 1
- 239000007921 spray Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 238000000498 ball milling Methods 0.000 description 12
- 230000006835 compression Effects 0.000 description 12
- 238000007906 compression Methods 0.000 description 12
- 238000003756 stirring Methods 0.000 description 12
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 10
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 9
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 9
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 6
- PQXKHYXIUOZZFA-UHFFFAOYSA-M lithium fluoride Chemical compound [Li+].[F-] PQXKHYXIUOZZFA-UHFFFAOYSA-M 0.000 description 6
- 239000000047 product Substances 0.000 description 5
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 4
- DWYMPOCYEZONEA-UHFFFAOYSA-L fluoridophosphate Chemical compound [O-]P([O-])(F)=O DWYMPOCYEZONEA-UHFFFAOYSA-L 0.000 description 4
- 229910001416 lithium ion Inorganic materials 0.000 description 4
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 3
- 235000019270 ammonium chloride Nutrition 0.000 description 3
- 229940071125 manganese acetate Drugs 0.000 description 3
- UOGMEBQRZBEZQT-UHFFFAOYSA-L manganese(2+);diacetate Chemical compound [Mn+2].CC([O-])=O.CC([O-])=O UOGMEBQRZBEZQT-UHFFFAOYSA-L 0.000 description 3
- 238000001694 spray drying Methods 0.000 description 3
- WBIQQQGBSDOWNP-UHFFFAOYSA-N 2-dodecylbenzenesulfonic acid Chemical compound CCCCCCCCCCCCC1=CC=CC=C1S(O)(=O)=O WBIQQQGBSDOWNP-UHFFFAOYSA-N 0.000 description 2
- BYMMIQCVDHHYGG-UHFFFAOYSA-N Cl.OP(O)(O)=O Chemical compound Cl.OP(O)(O)=O BYMMIQCVDHHYGG-UHFFFAOYSA-N 0.000 description 2
- LFVGISIMTYGQHF-UHFFFAOYSA-N ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 description 2
- 229910000387 ammonium dihydrogen phosphate Inorganic materials 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 229940060296 dodecylbenzenesulfonic acid Drugs 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 150000004679 hydroxides Chemical class 0.000 description 2
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 description 2
- 229910052808 lithium carbonate Inorganic materials 0.000 description 2
- AMWRITDGCCNYAT-UHFFFAOYSA-L manganese oxide Inorganic materials [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 2
- PPNAOCWZXJOHFK-UHFFFAOYSA-N manganese(2+);oxygen(2-) Chemical class [O-2].[Mn+2] PPNAOCWZXJOHFK-UHFFFAOYSA-N 0.000 description 2
- 235000019837 monoammonium phosphate Nutrition 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- CTIFKKWVNGEOBU-UHFFFAOYSA-N 2-hexadecylbenzenesulfonic acid Chemical compound CCCCCCCCCCCCCCCCC1=CC=CC=C1S(O)(=O)=O CTIFKKWVNGEOBU-UHFFFAOYSA-N 0.000 description 1
- DDFHBQSCUXNBSA-UHFFFAOYSA-N 5-(5-carboxythiophen-2-yl)thiophene-2-carboxylic acid Chemical compound S1C(C(=O)O)=CC=C1C1=CC=C(C(O)=O)S1 DDFHBQSCUXNBSA-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 229910010707 LiFePO 4 Inorganic materials 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- SRSXLGNVWSONIS-UHFFFAOYSA-N benzenesulfonic acid Chemical compound OS(=O)(=O)C1=CC=CC=C1 SRSXLGNVWSONIS-UHFFFAOYSA-N 0.000 description 1
- 229940092714 benzenesulfonic acid Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229940116007 ferrous phosphate Drugs 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 229910000398 iron phosphate Inorganic materials 0.000 description 1
- WBJZTOZJJYAKHQ-UHFFFAOYSA-K iron(3+) phosphate Chemical compound [Fe+3].[O-]P([O-])([O-])=O WBJZTOZJJYAKHQ-UHFFFAOYSA-K 0.000 description 1
- 229910000155 iron(II) phosphate Inorganic materials 0.000 description 1
- SDEKDNPYZOERBP-UHFFFAOYSA-H iron(ii) phosphate Chemical compound [Fe+2].[Fe+2].[Fe+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O SDEKDNPYZOERBP-UHFFFAOYSA-H 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003446 memory effect Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000011232 storage material Substances 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
-
- 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
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/5825—Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
-
- 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
-
- 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
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Crystallography & Structural Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Primary Cells (AREA)
Abstract
本发明公开了一种氯磷酸亚锰锂电极材料及其制备方法。该电极材料是一种表面包覆有碳膜的纳米至亚微米粒级的颗粒,化学式为Li2MnPO4·A。式中Mn为正二价,A是F-、Cl-、OH-中的一种或数种。这种锂电池电极材料采用固相反应法制备。将锰源、磷源、锂源、碳酸和阴离子源按化学计量比混合均匀,湿法球磨并喷雾干燥,在惰性气体保护下煅烧并冷却后,即得到所说的氯磷酸亚锰锂电极材料。原料中所含的有机酸根在煅烧时能使锰避免被氧化。本发明提供的氯磷酸亚锰锂在充放电容量和充放电速率等方面性能都明显优于现有的磷酸亚铁锂,为大功率用电器的蓄能提供了保障。The invention discloses a lithium manganese chlorophosphate electrode material and a preparation method thereof. The electrode material is a particle of nanometer to submicron size coated with a carbon film on the surface, and its chemical formula is Li 2 MnPO 4 ·A. In the formula, Mn is positive divalent, and A is one or more of F - , Cl - , OH - . This lithium battery electrode material is prepared by a solid-state reaction method. Manganese source, phosphorus source, lithium source, carbonic acid and anion source are mixed evenly according to the stoichiometric ratio, wet ball milled and spray dried, calcined and cooled under the protection of an inert gas, and the lithium manganous chlorophosphate electrode material is obtained . The organic acid groups contained in the raw materials can prevent manganese from being oxidized during calcination. The lithium manganous chlorophosphate provided by the invention is obviously superior to the existing lithium iron phosphate in terms of charge and discharge capacity and charge and discharge rate, and provides guarantee for energy storage of high-power electrical appliances.
Description
技术领域 technical field
本发明涉及一种氯磷酸亚锰锂电极材料及其制备方法。 The invention relates to a lithium manganous chlorophosphate electrode material and a preparation method thereof.
背景技术 Background technique
磷酸(亚)铁锂是目前应用最广的锂电池电极材料,和其它类型的锂电池电极材料相比,它具有安全性高,使用寿命长,高温性能好,无记忆效应,重量轻,环保等优点。但也存在低温性能差、大功率充放电性能欠佳、能量密度低等缺点,因此目前还不能用作电动汽车等大功率用电器的蓄能材料。 Lithium (sub)iron phosphate is currently the most widely used lithium battery electrode material. Compared with other types of lithium battery electrode materials, it has high safety, long service life, good high temperature performance, no memory effect, light weight, and environmental protection. Etc. However, there are also disadvantages such as poor low-temperature performance, poor high-power charge and discharge performance, and low energy density. Therefore, it cannot be used as an energy storage material for high-power electrical appliances such as electric vehicles.
本发明尝试提供一种能量密度高于磷酸亚铁锂的锂电池电极材料。 The present invention attempts to provide a lithium battery electrode material with higher energy density than lithium iron phosphate.
发明内容 Contents of the invention
本发明的目的是提供一种氯磷酸亚锰锂电极材料及其制备方法。 The object of the present invention is to provide a lithium manganese chlorophosphate electrode material and a preparation method thereof.
一种氯磷酸亚锰锂电极材料,它是一种表面包覆有碳膜的纳米至亚微米粒级的颗粒,分子式为:Li2MnPO4·A,式中Mn为正二价,A为阴离子,是F-、Cl-、OH-中的一种或数种。 A lithium manganese chlorophosphate electrode material, which is a nano-to-submicron particle coated with a carbon film on the surface, the molecular formula is: Li 2 MnPO 4 ·A, where Mn is positive divalent, A is anion , is one or more of F - , Cl - , OH - .
一种氯磷酸亚锰锂电极材料的制备方法的步骤如下: The steps of a preparation method of lithium manganous chlorophosphate electrode material are as follows:
1)将锰源、磷源、锂源和阴离子源按照分子式给定的化学计量比混合混匀,再加相当于锰源、磷源、锂源总重量0.1%至1%的碳源,全部原料总重3至5倍的水,球磨1至3小时,制成均匀的矿浆; 1) Mix the manganese source, phosphorus source, lithium source and anion source according to the stoichiometric ratio given by the molecular formula, and add a carbon source equivalent to 0.1% to 1% of the total weight of the manganese source, phosphorus source, and lithium source. Water 3 to 5 times the total weight of raw materials, ball milled for 1 to 3 hours to make a uniform slurry;
所述的锰源是二价锰的氧化物、氢氧化物和盐类化合物中的一种或数种;所述的磷源是磷酸氢铵、磷酸氢二铵中的一种;所述的锂源是乙酸锂、甲酸锂、柠檬酸锂、草酸锂的一种或数种;所述的阴离子源是锂、锰、铵的氯化物、氟化物、氢氧化物中的一种或数种;所述的碳源是水溶性有机酸、低粘度聚乙烯醇、葡萄糖中的一种或数种。 The manganese source is one or more of divalent manganese oxides, hydroxides and salt compounds; the phosphorus source is one of ammonium hydrogen phosphate and diammonium hydrogen phosphate; the The lithium source is one or more of lithium acetate, lithium formate, lithium citrate, and lithium oxalate; the anion source is one or more of lithium, manganese, and ammonium chloride, fluoride, and hydroxide ; The carbon source is one or more of water-soluble organic acids, low-viscosity polyvinyl alcohol, and glucose.
2)所得矿浆在150°C至260°C温度下喷雾干燥,得到干燥、粒度均匀的粉体; 2) The resulting pulp is spray-dried at a temperature of 150°C to 260°C to obtain dry powder with uniform particle size;
3)将粉体压制圆柱状或其它形状,在真空环境或保护气氛下550℃至850℃恒温2至6小时,冷却;所得产物为氯磷酸亚锰锂电极材料。 3) Press the powder into a cylindrical or other shape, keep the temperature at 550°C to 850°C for 2 to 6 hours in a vacuum environment or a protective atmosphere, and cool; the obtained product is lithium manganous phosphate electrode material.
所述的保护气氛是氮气或氩气的一种或数种。 The protective atmosphere is one or more of nitrogen or argon.
本发明提供的氯磷酸亚锰锂电极材料在充放电容量和充放电速率都得到了显著的提高,为大功率用电器的蓄能提供了保障。 The lithium manganous chlorophosphate electrode material provided by the invention has significantly improved charge and discharge capacity and charge and discharge rate, and provides guarantee for energy storage of high-power electrical appliances.
具体实施方式 detailed description
本发明提供的氯磷酸亚锰锂电极材料是一种表面包覆有碳膜的纳米至亚微米粒级的颗粒,分子式为:Li2MnPO4·A,式中Mn为正二价,A为阴离子,是F-、Cl-、OH-中的一种或数种。 The lithium manganese chlorophosphate electrode material provided by the present invention is a nanometer to submicron particle size coated with a carbon film on the surface, and its molecular formula is: Li 2 MnPO 4 ·A, where Mn is positive divalent, and A is an anion , is one or more of F - , Cl - , OH - .
Li2MnPO4·A是该电极材料的初始态(充电前状态),在对锂离子电池进行充电时,其分子中的Li离子进入电解质溶液,Mn也从正二价转为正四价,以保持分子结构的电中性。其饱和充电后的状态是MnPO4·A,式中Mn为正四价。和目前使用的磷酸亚铁锂相比,本发明提供的氯磷酸亚锰锂的摩尔活性锂离子含量提高了一倍,因此其充放电容量也将对应提高。 Li 2 MnPO 4 ·A is the initial state of the electrode material (state before charging). When charging the lithium-ion battery, Li ions in its molecules enter the electrolyte solution, and Mn also changes from positive divalent to positive tetravalent to maintain The electrical neutrality of the molecular structure. Its state after saturated charging is MnPO 4 ·A, where Mn is positive tetravalent. Compared with the currently used lithium ferrous phosphate, the molar active lithium ion content of the lithium manganese chlorophosphate provided by the present invention is doubled, so its charge and discharge capacity will also be correspondingly increased.
氯磷酸亚锰锂电极材料的制备方法的步骤如下: The steps of the preparation method of lithium manganous chlorophosphate electrode material are as follows:
1)将锰源、磷源、锂源和阴离子源按照分子式给定的化学计量比混合混匀,再加相当于锰源、磷源、锂源总重量0.1%至1%的碳源,全部原料总重3至5倍的水,球磨1至3小时,制成均匀的矿浆。原料混合后,会形成中间产物,也就是最终产物的前驱体,在研磨过程中,前驱体与溶液形成均匀的混合相。 1) Mix the manganese source, phosphorus source, lithium source and anion source according to the stoichiometric ratio given by the molecular formula, and add a carbon source equivalent to 0.1% to 1% of the total weight of the manganese source, phosphorus source, and lithium source. Water that is 3 to 5 times the total weight of raw materials is ball milled for 1 to 3 hours to make a uniform slurry. After the raw materials are mixed, an intermediate product is formed, which is the precursor of the final product. During the grinding process, the precursor and the solution form a homogeneous mixed phase.
所述的锰源是二价锰的氧化物、氢氧化物和盐类化合物中的一种或数种;所述的磷源是磷酸氢铵、磷酸氢二铵中的一种;所述的锂源是乙酸锂、甲酸锂、柠檬酸锂、草酸锂的一种或数种,应避免直接使用碳酸锂,因为碳酸锂分解温度高,需要更高的煅烧温度,同时有可能造成产物烧结,降低其电化学性能;所述的阴离子源是锂、锰、铵的氯化物、氟化物、氢氧化物中的一种或数种;所述的碳源是水溶性有机酸、低粘度聚乙烯醇、葡萄糖中的一种或数种。 The manganese source is one or more of divalent manganese oxides, hydroxides and salt compounds; the phosphorus source is one of ammonium hydrogen phosphate and diammonium hydrogen phosphate; the The lithium source is one or several kinds of lithium acetate, lithium formate, lithium citrate, and lithium oxalate. The direct use of lithium carbonate should be avoided, because the decomposition temperature of lithium carbonate is high, which requires a higher calcination temperature, and may cause sintering of the product at the same time. reduce its electrochemical performance; the anion source is one or more of lithium, manganese, ammonium chloride, fluoride, and hydroxide; the carbon source is water-soluble organic acid, low-viscosity polyethylene One or more of alcohol and glucose.
2)所得矿浆在150°C至260°C温度下喷雾干燥,得到干燥、粒度均匀的粉体。 2) The obtained pulp is spray-dried at a temperature of 150°C to 260°C to obtain dry powder with uniform particle size.
喷雾干燥前应保持对矿浆进行持续搅拌,防止其沉淀分层;喷雾干燥能使物料快速脱水并烘干,得到成分均匀的粉体。 Before spray drying, the slurry should be continuously stirred to prevent its precipitation and stratification; spray drying can quickly dehydrate and dry the material to obtain a powder with uniform composition.
作为碳源加入的水溶性有机酸、低粘度聚乙烯醇、葡萄糖在喷雾干燥过程中起分散剂的作用,能抑制颗粒团聚。 Water-soluble organic acid, low-viscosity polyvinyl alcohol, and glucose added as carbon sources act as dispersants during the spray-drying process and can inhibit particle agglomeration.
3)将粉体压制圆柱状或其它形状,在真空环境或保护气氛下550℃至850℃恒温2至6小时,冷却;所得产物为氯磷酸亚锰锂电极材料。 3) Press the powder into a cylindrical or other shape, keep the temperature at 550°C to 850°C for 2 to 6 hours in a vacuum environment or a protective atmosphere, and cool; the obtained product is lithium manganous phosphate electrode material.
所述的保护气氛是氮气或氩气的一种或数种。保护气氛避免使用氢气等还原性气体,以免在产物中形成金属单质。 The protective atmosphere is one or more of nitrogen or argon. The protective atmosphere avoids the use of reducing gases such as hydrogen, so as not to form metal elements in the product.
煅烧前将粉体压制成型是为了压缩粉体的体积,同时也能赶出颗粒之间的的空气和氧气,保持粉体处于还原环境。煅烧过程的反应实例之一如: The purpose of compressing the powder before calcination is to compress the volume of the powder, and at the same time drive out the air and oxygen between the particles, and keep the powder in a reducing environment. One of the reaction examples of the calcination process is as follows:
Mn(CH3COO)2+LiCH3COO+(NH4)2HPO4+LiCl=Li2MnPO4Cl+3CO2+3CH4+2NH3(1) Mn(CH 3 COO) 2 +LiCH 3 COO+(NH 4 ) 2 HPO 4 +LiCl=Li 2 MnPO 4 Cl+3CO 2 +3CH 4 +2NH 3 (1)
在(1)式中醋酸锰提供锰源,醋酸锂提供部分锂,磷酸氢二铵提供磷,氯化锂提供氯和部分锂。 In formula (1), manganese acetate provides manganese source, lithium acetate provides part of lithium, diammonium hydrogen phosphate provides phosphorus, and lithium chloride provides chlorine and part of lithium.
在原料中,有机酸根起到了还原剂的作用,它们在煅烧分解的过程中释放的还原性气体使锰保持二价。在煅烧合成的过程中使变价元素保持为低价态是本发明的关键之一。 In the raw materials, the organic acid radicals act as reducing agents, and the reducing gas released during the calcination and decomposition process keeps the manganese divalent. It is one of the keys of the present invention to keep the variable-valence elements in a low-valence state during the calcination synthesis process.
在煅烧过程中,作为碳源加入的水溶性有机酸、低粘度聚乙烯醇、葡萄糖分解并炭化,碳膜和炭质微粒包覆在粉体颗粒表面并深入其内部,能有效降低颗粒之间的电阻率。 During the calcination process, the water-soluble organic acid, low-viscosity polyvinyl alcohol, and glucose added as carbon sources are decomposed and carbonized. resistivity.
所得产物为氯磷酸亚锰锂,可用作锂电池电极材料。和以往使用的LiFePO4相比,本发明提供的Li2MnPO4·A活性锂离子摩尔密度增加了一倍,且制备工艺简单,原料来源广泛。 The obtained product is lithium manganese chlorophosphate, which can be used as electrode material of lithium battery. Compared with LiFePO 4 used in the past, the molar density of Li 2 MnPO 4 ·A active lithium ions provided by the invention is doubled, and the preparation process is simple and the source of raw materials is wide.
下面结合实施例对本发明作详细说明。 The present invention is described in detail below in conjunction with embodiment.
实施例1Example 1
1)称取乙酸锰19.67Kg,磷酸氢二铵10.57Kg,乙酸锂5.28Kg,氯化锂3.39Kg,加入100L水,0.2公斤葡萄糖,搅拌均匀倒入球磨机中,球磨1小时。 1) Weigh 19.67Kg of manganese acetate, 10.57Kg of diammonium hydrogen phosphate, 5.28Kg of lithium acetate, and 3.39Kg of lithium chloride, add 100L of water and 0.2 kg of glucose, stir evenly, pour into a ball mill, and mill for 1 hour.
2)球磨所得矿浆在150℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The pulp obtained from ball milling is spray-dried at 150°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下550℃煅烧6小时,冷却至室温即得到氯磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression die, put it into a closed calciner, calcinate at 550°C for 6 hours in a vacuum environment, and cool to room temperature to obtain lithium manganous phosphate chloride.
实施例2Example 2
1)称取MnO5.68Kg,磷酸氢二铵10.57Kg,乙酸锂5.28Kg,氟化锂2.07Kg,加入80L水,0.25公斤柠檬酸,搅拌均匀倒入球磨机中,球磨2小时。 1) Weigh 5.68Kg of MnO, 10.57Kg of diammonium hydrogen phosphate, 5.28Kg of lithium acetate, and 2.07Kg of lithium fluoride, add 80L of water, 0.25kg of citric acid, stir evenly, pour into a ball mill, and mill for 2 hours.
2)球磨所得矿浆在260℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The slurry obtained by ball milling is spray-dried at 260°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下850℃煅烧2小时,冷却至室温即得到氟磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression die, put it into a closed calciner, calcinate at 850°C for 2 hours in a vacuum environment, and cool to room temperature to obtain lithium manganous fluorophosphate.
实施例3Example 3
1)称取MnCl2·4H2O13Kg,磷酸氢二铵10.57Kg,乙酸锂5.28Kg,氢氧化锂3.35Kg,加入90L水,0.15公斤吐温-40,搅拌均匀倒入球磨机中,球磨3小时。 1) Weigh 13Kg of MnCl 2 4H 2 O, 10.57Kg of diammonium hydrogen phosphate, 5.28Kg of lithium acetate, 3.35Kg of lithium hydroxide, add 90L of water, 0.15kg of Tween-40, stir well and pour into a ball mill, and mill for 3 hours .
2)球磨所得矿浆在200℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The pulp obtained from ball milling is spray-dried at 200°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下600℃煅烧3小时,冷却至室温即得到羟基磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression die, put it into a closed calciner, calcinate at 600°C for 3 hours in a vacuum environment, and cool to room temperature to obtain lithium hydroxy manganous phosphate.
实施例4Example 4
1)称取Mn3(PO4)2·3H2O8.18Kg,磷酸氢二铵2.64Kg,乙酸锂3.94Kg,氯化锂2.54Kg,加入80L水,0.17公斤低粘度聚乙烯醇,搅拌均匀倒入球磨机中,球磨1小时。 1) Weigh Mn 3 (PO 4 ) 2 3H 2 O 8.18Kg, diammonium hydrogen phosphate 2.64Kg, lithium acetate 3.94Kg, lithium chloride 2.54Kg, add 80L water, 0.17kg low viscosity polyvinyl alcohol, stir well Pour into a ball mill and ball mill for 1 hour.
2)球磨所得矿浆在180℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The pulp obtained by ball milling is spray-dried at 180°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下700℃煅烧3小时,冷却至室温即得到氯磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression mold, put it into a closed calciner, and calcinate at 700°C for 3 hours in a vacuum environment, and cool to room temperature to obtain lithium manganous phosphate chloride.
实施例5Example 5
1)称取Mn(NO3)2·4H2O20Kg,磷酸氢二铵10.57Kg,乙酸锂5.28Kg,氯化锂3.39Kg,加入120L水,0.2公斤苯磺酸,搅拌均匀倒入球磨机中,球磨1小时。 1) Weigh Mn(NO 3 ) 2 4H 2 O20Kg, diammonium hydrogen phosphate 10.57Kg, lithium acetate 5.28Kg, lithium chloride 3.39Kg, add 120L water, 0.2 kg benzenesulfonic acid, stir well and pour into the ball mill, Ball mill for 1 hour.
2)球磨所得矿浆在160℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The pulp obtained by ball milling is spray-dried at 160°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下650℃煅烧2小时,冷却至室温即得到氯磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression mold, put it into a closed calciner, calcinate at 650°C for 2 hours in a vacuum environment, and cool to room temperature to obtain lithium manganous phosphate.
实施例6Example 6
1)称取MnO5.68Kg,磷酸二氢铵9.21Kg,甲酸锂5.69Kg,氢氧化锂1.91Kg,加入80L水,0.2公斤十二烷基苯磺酸,搅拌均匀倒入球磨机中,球磨2小时。 1) Weigh 5.68Kg of MnO, 9.21Kg of ammonium dihydrogen phosphate, 5.69Kg of lithium formate, 1.91Kg of lithium hydroxide, add 80L of water, 0.2 kg of dodecylbenzenesulfonic acid, stir well and pour into a ball mill, and ball mill for 2 hours .
2)球磨所得矿浆在260℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The pulp obtained by ball milling is spray-dried at 260°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下650℃煅烧2小时,冷却至室温即得到羟基磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression mold, put it into a closed calciner, calcinate at 650°C for 2 hours in a vacuum environment, and cool to room temperature to obtain lithium hydroxy manganous phosphate.
实施例7Example 7
1)称取MnCl2·4H2O13Kg,磷酸氢二铵10.57Kg,草酸锂8.15Kg,氟化锂2.07Kg,加入90L水,0.1公斤十六烷基苯磺酸,搅拌均匀倒入球磨机中,球磨3小时。 1) Weigh 13Kg of MnCl 2 4H 2 O, 10.57Kg of diammonium hydrogen phosphate, 8.15Kg of lithium oxalate, 2.07Kg of lithium fluoride, add 90L of water, 0.1 kg of cetylbenzenesulfonic acid, stir well and pour into the ball mill, Ball mill for 3 hours.
2)球磨所得矿浆在200℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The pulp obtained from ball milling is spray-dried at 200°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下850℃煅烧3小时,冷却至室温即得到氟磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression die, put it into a closed calciner, and calcinate at 850°C for 3 hours in a vacuum environment, and cool to room temperature to obtain lithium manganous fluorophosphate.
实施例8Example 8
1)称取Mn3(PO4)2·3H2O8.18Kg,磷酸氢二铵2.64Kg,柠檬酸锂33.84Kg,氯化铵3.21Kg,加入80L水,0.5公斤葡萄糖,搅拌均匀倒入球磨机中,球磨1小时。 1) Weigh Mn 3 (PO 4 ) 2 3H 2 O 8.18Kg, diammonium hydrogen phosphate 2.64Kg, lithium citrate 33.84Kg, ammonium chloride 3.21Kg, add 80L water, 0.5 kg glucose, stir well and pour into the ball mill , ball milled for 1 hour.
2)球磨所得矿浆在180℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The pulp obtained by ball milling is spray-dried at 180°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下650℃煅烧3小时,冷却至室温即得到氯磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression mold, put it into a closed calciner, calcinate at 650°C for 3 hours in a vacuum environment, and cool to room temperature to obtain lithium manganous chlorophosphate.
实施例9Example 9
1)称取乙酸锰19.67Kg,磷酸氢二铵10.57Kg,乙酸锂5.28Kg,氟化锂2.07Kg,加入90L水,0.5公斤柠檬酸,搅拌均匀倒入球磨机中,球磨2小时。 1) Weigh 19.67Kg of manganese acetate, 10.57Kg of diammonium hydrogen phosphate, 5.28Kg of lithium acetate, and 2.07Kg of lithium fluoride, add 90L of water, 0.5kg of citric acid, stir evenly, pour into a ball mill, and mill for 2 hours.
2)球磨所得矿浆在165℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The slurry obtained by ball milling is spray-dried at 165°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下850℃煅烧5小时,冷却至室温即得到氟磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression die, put it into a closed calciner, calcinate at 850°C for 5 hours in a vacuum environment, and cool to room temperature to obtain lithium manganous fluorophosphate.
实施例10Example 10
1)称取Mn3(PO4)2·3H2O8.18Kg,磷酸氢二铵2.64Kg,乙酸锂3.96Kg,氢氧化锂2.51Kg,加入100L水,0.15公斤吐温-40搅拌均匀倒入球磨机中,球磨3小时。 1) Weigh Mn 3 (PO 4 ) 2 3H 2 O 8.18Kg, diammonium hydrogen phosphate 2.64Kg, lithium acetate 3.96Kg, lithium hydroxide 2.51Kg, add 100L water, stir 0.15kg Tween-40 and pour into In a ball mill, ball mill for 3 hours.
2)球磨所得矿浆在190℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The slurry obtained by ball milling is spray-dried at 190°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下700℃煅烧4小时,冷却至室温即得到羟基磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression die, put it into a closed calciner, and calcinate it at 700°C for 4 hours in a vacuum environment, and cool it to room temperature to obtain lithium hydroxy manganous phosphate.
实施例11Example 11
1)称取MnO5.68Kg,磷酸二氢铵9.21Kg,甲酸锂11.38Kg,浓氨水8.4Kg,加入60L水,0.2公斤柠檬酸,搅拌均匀倒入球磨机中,球磨2小时。 1) Weigh 5.68Kg of MnO, 9.21Kg of ammonium dihydrogen phosphate, 11.38Kg of lithium formate, 8.4Kg of concentrated ammonia water, add 60L of water, 0.2 kg of citric acid, stir evenly, pour into a ball mill, and mill for 2 hours.
2)球磨所得矿浆在220℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The slurry obtained by ball milling is spray-dried at 220°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下600℃煅烧2小时,冷却至室温即得到羟基磷酸亚锰锂。 3) Press the powder into a cylindrical shape with a compression mold, put it into a closed calciner, calcinate at 600°C for 2 hours in a vacuum environment, and cool to room temperature to obtain lithium hydroxy manganous phosphate.
实施例12Example 12
1)称取Mn(NO3)2·4H2O20Kg,磷酸氢二铵10.57Kg,乙酸锂10.56Kg,氟化铵2.96Kg,加入120L水,0.04公斤十二烷基苯磺酸,搅拌均匀倒入球磨机中,球2小时。 1) Weigh Mn(NO 3 ) 2 4H 2 O20Kg, diammonium hydrogen phosphate 10.57Kg, lithium acetate 10.56Kg, ammonium fluoride 2.96Kg, add 120L water, 0.04kg dodecylbenzenesulfonic acid, stir evenly and pour Into the ball mill, the ball for 2 hours.
2)球磨所得矿浆在170℃下进行喷雾干燥,得到干燥且粒度均匀的粉体。 2) The slurry obtained by ball milling is spray-dried at 170°C to obtain dry powder with uniform particle size.
3)使用压模将粉体压制成圆柱形,放入密闭煅烧炉中,在真空环境下600℃煅烧4小时,冷却至室温即得到氟磷酸亚锰锂。 3) Press the powder into a cylindrical shape by using a compression die, put it into a closed calciner, and calcinate it at 600°C for 4 hours in a vacuum environment, and cool it to room temperature to obtain lithium manganous fluorophosphate.
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CN103022480A (en) * | 2011-09-21 | 2013-04-03 | 现代自动车株式会社 | Compositions and methods for manufacturing a cathode for lithium secondary battery |
CN103456954A (en) * | 2013-09-06 | 2013-12-18 | 四川一美能源科技有限公司 | Preparation method of active electrode material |
CN104584310A (en) * | 2012-08-16 | 2015-04-29 | 丰田自动车株式会社 | Lithium secondary battery and method for manufacturing same |
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CN1675785A (en) * | 2002-07-22 | 2005-09-28 | 威伦斯技术公司 | Method of synthesizing electrochemically active materials from a slurry of precursors |
CN101673819A (en) * | 2009-09-25 | 2010-03-17 | 清华大学 | Method for preparing manganese lithium phosphate/carbon composite material by manganese phosphate |
CN103022480A (en) * | 2011-09-21 | 2013-04-03 | 现代自动车株式会社 | Compositions and methods for manufacturing a cathode for lithium secondary battery |
CN104584310A (en) * | 2012-08-16 | 2015-04-29 | 丰田自动车株式会社 | Lithium secondary battery and method for manufacturing same |
CN103456954A (en) * | 2013-09-06 | 2013-12-18 | 四川一美能源科技有限公司 | Preparation method of active electrode material |
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