CN116903050A - A preparation method of aluminum nickel manganese magnesium doped with cobalt tetroxide - Google Patents
A preparation method of aluminum nickel manganese magnesium doped with cobalt tetroxide Download PDFInfo
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- -1 aluminum nickel manganese magnesium Chemical compound 0.000 title claims abstract description 50
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 229910017052 cobalt Inorganic materials 0.000 title claims description 52
- 239000010941 cobalt Substances 0.000 title claims description 52
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 title claims description 52
- 238000006243 chemical reaction Methods 0.000 claims abstract description 29
- 239000011259 mixed solution Substances 0.000 claims abstract description 16
- 239000002243 precursor Substances 0.000 claims abstract description 12
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims abstract description 9
- 150000001868 cobalt Chemical class 0.000 claims abstract description 9
- 238000001354 calcination Methods 0.000 claims abstract description 8
- 159000000003 magnesium salts Chemical class 0.000 claims abstract description 7
- 150000002696 manganese Chemical class 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims abstract description 7
- 150000002815 nickel Chemical class 0.000 claims abstract description 7
- 239000008139 complexing agent Substances 0.000 claims abstract description 5
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 18
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 claims description 18
- 235000012538 ammonium bicarbonate Nutrition 0.000 claims description 18
- 239000001099 ammonium carbonate Substances 0.000 claims description 18
- 229910052782 aluminium Inorganic materials 0.000 claims description 14
- 239000002245 particle Substances 0.000 claims description 14
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 10
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims description 8
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims description 6
- 229910021529 ammonia Inorganic materials 0.000 claims description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims description 6
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 claims description 6
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 4
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 4
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims description 4
- YIXJRHPUWRPCBB-UHFFFAOYSA-N magnesium nitrate Chemical compound [Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O YIXJRHPUWRPCBB-UHFFFAOYSA-N 0.000 claims description 4
- 229910052943 magnesium sulfate Inorganic materials 0.000 claims description 4
- 235000019341 magnesium sulphate Nutrition 0.000 claims description 4
- 229940099596 manganese sulfate Drugs 0.000 claims description 4
- 239000011702 manganese sulphate Substances 0.000 claims description 4
- 235000007079 manganese sulphate Nutrition 0.000 claims description 4
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 claims description 4
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 claims description 4
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 3
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 claims description 2
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 claims description 2
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 claims description 2
- 229910021380 Manganese Chloride Inorganic materials 0.000 claims description 2
- GLFNIEUTAYBVOC-UHFFFAOYSA-L Manganese chloride Chemical compound Cl[Mn]Cl GLFNIEUTAYBVOC-UHFFFAOYSA-L 0.000 claims description 2
- VEQPNABPJHWNSG-UHFFFAOYSA-N Nickel(2+) Chemical compound [Ni+2] VEQPNABPJHWNSG-UHFFFAOYSA-N 0.000 claims description 2
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 claims description 2
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 claims description 2
- 229910001429 cobalt ion Inorganic materials 0.000 claims description 2
- 229910001981 cobalt nitrate Inorganic materials 0.000 claims description 2
- 229910000361 cobalt sulfate Inorganic materials 0.000 claims description 2
- 229940044175 cobalt sulfate Drugs 0.000 claims description 2
- XLJKHNWPARRRJB-UHFFFAOYSA-N cobalt(2+) Chemical compound [Co+2] XLJKHNWPARRRJB-UHFFFAOYSA-N 0.000 claims description 2
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 claims description 2
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 2
- 229910001425 magnesium ion Inorganic materials 0.000 claims description 2
- KBMLJKBBKGNETC-UHFFFAOYSA-N magnesium manganese Chemical compound [Mg].[Mn] KBMLJKBBKGNETC-UHFFFAOYSA-N 0.000 claims description 2
- 239000011565 manganese chloride Substances 0.000 claims description 2
- 235000002867 manganese chloride Nutrition 0.000 claims description 2
- 229940099607 manganese chloride Drugs 0.000 claims description 2
- 229910001437 manganese ion Inorganic materials 0.000 claims description 2
- MIVBAHRSNUNMPP-UHFFFAOYSA-N manganese(2+);dinitrate Chemical compound [Mn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MIVBAHRSNUNMPP-UHFFFAOYSA-N 0.000 claims description 2
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 claims description 2
- 229910001453 nickel ion Inorganic materials 0.000 claims description 2
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 claims description 2
- 230000001376 precipitating effect Effects 0.000 claims description 2
- 235000017557 sodium bicarbonate Nutrition 0.000 claims description 2
- 229910000030 sodium bicarbonate Inorganic materials 0.000 claims description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 2
- 235000017550 sodium carbonate Nutrition 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 239000000243 solution Substances 0.000 abstract description 19
- UBEWDCMIDFGDOO-UHFFFAOYSA-N cobalt(2+);cobalt(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[O-2].[Co+2].[Co+3].[Co+3] UBEWDCMIDFGDOO-UHFFFAOYSA-N 0.000 abstract description 17
- 239000000463 material Substances 0.000 abstract description 17
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 abstract description 6
- 229910001416 lithium ion Inorganic materials 0.000 abstract description 6
- 230000005012 migration Effects 0.000 abstract description 3
- 238000013508 migration Methods 0.000 abstract description 3
- 230000008569 process Effects 0.000 abstract description 3
- 230000002195 synergetic effect Effects 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 1
- 239000012716 precipitator Substances 0.000 abstract 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 18
- 229910000625 lithium cobalt oxide Inorganic materials 0.000 description 13
- BFZPBUKRYWOWDV-UHFFFAOYSA-N lithium;oxido(oxo)cobalt Chemical compound [Li+].[O-][Co]=O BFZPBUKRYWOWDV-UHFFFAOYSA-N 0.000 description 13
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 12
- 229910021446 cobalt carbonate Inorganic materials 0.000 description 12
- ZOTKGJBKKKVBJZ-UHFFFAOYSA-L cobalt(2+);carbonate Chemical compound [Co+2].[O-]C([O-])=O ZOTKGJBKKKVBJZ-UHFFFAOYSA-L 0.000 description 12
- 239000011777 magnesium Substances 0.000 description 12
- 229910052749 magnesium Inorganic materials 0.000 description 12
- 239000012266 salt solution Substances 0.000 description 12
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 10
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 9
- 238000010586 diagram Methods 0.000 description 9
- 229910052759 nickel Inorganic materials 0.000 description 9
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 8
- 235000011114 ammonium hydroxide Nutrition 0.000 description 8
- 239000011572 manganese Substances 0.000 description 7
- 229910052748 manganese Inorganic materials 0.000 description 7
- BLJNPOIVYYWHMA-UHFFFAOYSA-N alumane;cobalt Chemical compound [AlH3].[Co] BLJNPOIVYYWHMA-UHFFFAOYSA-N 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000013078 crystal Substances 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 4
- 230000014759 maintenance of location Effects 0.000 description 4
- 238000011056 performance test Methods 0.000 description 4
- 239000010406 cathode material Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 2
- 238000001493 electron microscopy Methods 0.000 description 2
- 238000004626 scanning electron microscopy Methods 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- ZAUUZASCMSWKGX-UHFFFAOYSA-N manganese nickel Chemical compound [Mn].[Ni] ZAUUZASCMSWKGX-UHFFFAOYSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
Classifications
-
- 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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- Inorganic Compounds Of Heavy Metals (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
技术领域Technical field
本发明涉及电池材料制备技术领域,具体涉及一种铝镍锰镁掺杂四氧化三钴的制备方法。The invention relates to the technical field of battery material preparation, and specifically relates to a preparation method of aluminum, nickel, manganese and magnesium doped with cobalt tetroxide.
背景技术Background technique
随着3C产品的更新换代以及各种高端穿戴设备的推出,人们对锂离子电池的要求也越来越高,正极材料厂商常用大小颗粒混掺来提高正极的压实密度,进而提高锂离子电池的能量密度。四氧化三钴作为制备锂电池正极材料钴酸锂的重要前驱体,其各方面指标影响了钴酸锂正极材料及下游锂离子电池性能,现有的四氧化三钴所合成的钴酸锂材料结构在一定程度上增加了稳定性,但无法满足4.48V、4.5V等更高电压钴酸锂的需求。With the upgrading of 3C products and the launch of various high-end wearable devices, people's requirements for lithium-ion batteries are getting higher and higher. Cathode material manufacturers often mix large and small particles to increase the compaction density of the cathode, thereby improving the lithium-ion battery. energy density. Tricobalt tetroxide is an important precursor for preparing lithium cobalt oxide, a cathode material for lithium batteries. Its various indicators affect the performance of lithium cobalt oxide cathode materials and downstream lithium-ion batteries. The structure of the existing lithium cobalt oxide material synthesized by tricobalt tetroxide has increased to a certain extent. Improves stability, but cannot meet the needs of higher voltage lithium cobalt oxide such as 4.48V and 4.5V.
因此,亟需开发出一种四氧化三钴的制备方法能够解决目前的四氧化三钴所合成的钴酸锂材料结构无法满足4.48V、4.5V等更高电压钴酸锂的问题。Therefore, there is an urgent need to develop a preparation method of cobalt tetroxide that can solve the problem that the current lithium cobalt oxide material structure synthesized by cobalt tetroxide cannot meet the requirements of higher voltage lithium cobalt oxide such as 4.48V and 4.5V.
发明内容Contents of the invention
本发明旨在至少解决现有技术中存在的技术问题之一。为此,本发明提出一种四氧化三钴制备方法,通过多元掺杂,多种元素的协同效应,从而不仅提高材料结构的稳定性,还可以增加材料的电导率及提高锂离子充放电过程中的迁移效率,以本发明中的四氧化三钴所合成的钴酸锂材料能够满足4.48V、4.5V等更高电压钴酸锂的需求。The present invention aims to solve at least one of the technical problems existing in the prior art. To this end, the present invention proposes a preparation method of cobalt tetroxide. Through multi-element doping and the synergistic effect of multiple elements, it not only improves the stability of the material structure, but also increases the conductivity of the material and improves the migration of lithium ions during charge and discharge. Efficiency, the lithium cobalt oxide material synthesized with tricobalt tetroxide in the present invention can meet the demand for higher voltage lithium cobalt oxide such as 4.48V and 4.5V.
根据本发明的第一方面实施例的一种铝镍锰镁掺杂四氧化三钴的制备方法,包括以下步骤:A method for preparing aluminum nickel manganese magnesium doped with cobalt tetroxide according to the first embodiment of the present invention includes the following steps:
S1:将铝盐、镁盐、镍盐、锰盐和钴盐混后得到混合溶液;S1: Mix aluminum salt, magnesium salt, nickel salt, manganese salt and cobalt salt to obtain a mixed solution;
S2:将步骤S1配制的混合溶液、沉淀剂和络合剂并流后通入含有底液的反应釜中于pH值为7.0~7.5,反应的温度为35~50℃下反应制得铝镍锰镁掺杂四氧化三钴前驱体;S2: The mixed solution, precipitant and complexing agent prepared in step S1 are flowed together and then passed into the reaction kettle containing the bottom liquid. The pH value is 7.0~7.5 and the reaction temperature is 35~50°C to prepare aluminum nickel. Manganese magnesium doped cobalt tetroxide precursor;
S3:将步骤S2制得的铝镍锰镁掺杂四氧化三钴前驱体煅烧后得到铝镍锰镁掺杂四氧化三钴。S3: Calcining the aluminum nickel manganese magnesium doped cobalt tetroxide precursor prepared in step S2 to obtain aluminum nickel manganese magnesium doped cobalt tetroxide.
根据本发明的第一方面的实施例至少具有以下有益效果:Embodiments according to the first aspect of the present invention have at least the following beneficial effects:
本发明中通过多元掺杂,多种元素的协同效应,从而不仅提高材料结构的稳定性,还可以增加材料的电导率及提高锂离子充放电过程中的迁移效率,其中铝提高了材料的结构稳定性,镁能形成柱状抑制相变,还能提高材料的电导率从而降低充放电过程中的阻抗,镍锰掺杂能使相变转为固溶行为,抑制相变,使得由铝镍锰镁掺杂四氧化三钴所制备的钴酸锂能满足更高电压需求。In the present invention, through multi-element doping, the synergistic effect of multiple elements not only improves the stability of the material structure, but also increases the conductivity of the material and improves the migration efficiency of lithium ions during the charge and discharge process. Among them, aluminum improves the structure of the material. Stability, magnesium can form columnar shapes to inhibit phase change, and can also increase the conductivity of the material to reduce the impedance during charge and discharge. Nickel-manganese doping can convert the phase change into solid solution behavior, inhibiting the phase change, making the material consist of aluminum, nickel, and manganese. Lithium cobalt oxide prepared by magnesium doping with cobalt tetraoxide can meet higher voltage requirements.
根据本发明的一些实施例,步骤S1中,所述钴盐包括氯化钴、硫酸钴、硝酸钴中的至少一种。According to some embodiments of the present invention, in step S1, the cobalt salt includes at least one of cobalt chloride, cobalt sulfate, and cobalt nitrate.
根据本发明的一些实施例,步骤S1中,所述混合溶液中,钴离子浓度为80~150g/L。According to some embodiments of the present invention, in step S1, the cobalt ion concentration in the mixed solution is 80-150g/L.
根据本发明的一些实施例,步骤S1中,所述混合溶液中,铝离子的浓度为0.5~2.2g/L。According to some embodiments of the present invention, in step S1, the concentration of aluminum ions in the mixed solution is 0.5-2.2g/L.
根据本发明的一些实施例,所述混合溶液中,镍离子的浓度为0.15~0.55g/L。According to some embodiments of the present invention, the concentration of nickel ions in the mixed solution is 0.15-0.55g/L.
根据本发明的一些实施例,所述混合溶液中,锰离子的浓度为0.1~0.63g/L。According to some embodiments of the present invention, the concentration of manganese ions in the mixed solution is 0.1-0.63g/L.
根据本发明的一些实施例,所述混合溶液中,镁离子的浓度为0.14~0.53g/L。According to some embodiments of the present invention, the concentration of magnesium ions in the mixed solution is 0.14-0.53g/L.
根据本发明的一些实施例,所述铝盐包括硫酸铝、氯化铝和硝酸铝中的至少一种。According to some embodiments of the present invention, the aluminum salt includes at least one of aluminum sulfate, aluminum chloride and aluminum nitrate.
根据本发明的一些实施例,所述镍盐包括硫酸镍、氯化镍和硝酸镍中的至少一种。According to some embodiments of the present invention, the nickel salt includes at least one of nickel sulfate, nickel chloride and nickel nitrate.
根据本发明的一些实施例,所述锰盐包括硫酸锰、氯化锰和硝酸锰中的至少一种。According to some embodiments of the present invention, the manganese salt includes at least one of manganese sulfate, manganese chloride and manganese nitrate.
根据本发明的一些实施例,所述镁盐包括硫酸镁、氯化镁和硝酸镁中的至少一种。According to some embodiments of the present invention, the magnesium salt includes at least one of magnesium sulfate, magnesium chloride and magnesium nitrate.
根据本发明的一些实施例,所述沉淀剂包括碳酸氢铵、碳酸钠和碳酸氢钠中的至少一种。According to some embodiments of the present invention, the precipitating agent includes at least one of ammonium bicarbonate, sodium carbonate and sodium bicarbonate.
根据本发明的一些实施例,所述络合剂包括氨水、EDTA和柠檬酸中的至少一种。According to some embodiments of the present invention, the complexing agent includes at least one of ammonia, EDTA and citric acid.
根据本发明的一些实施例,步骤S2中,所述铝镍锰镁掺杂四氧化三钴前驱体的粒度为18~19μm。According to some embodiments of the present invention, in step S2, the particle size of the aluminum nickel manganese magnesium doped cobalt tetroxide precursor is 18 to 19 μm.
根据本发明的一些实施例,步骤S2中,所述反应的过程中包括搅拌反应。According to some embodiments of the present invention, in step S2, the reaction process includes a stirring reaction.
根据本发明的一些实施例,步骤S2中,所述搅拌的转速为200~400rpm。According to some embodiments of the present invention, in step S2, the stirring speed is 200 to 400 rpm.
根据本发明的一些优选地,实施例,步骤S2中,控制所述铝镍锰镁掺杂四氧化三钴前驱体的粒度为18~19μm的方法为每80h对反应釜进行分釜处理,晶种减半,对应流量、转速降低20%,直至160~260h四元素掺杂前驱体粒度达到18~19μm,停釜。According to some preferred embodiments of the present invention, in step S2, the method for controlling the particle size of the aluminum-nickel-manganese-magnesium-doped cobalt tetroxide precursor to be 18-19 μm is to separate the reaction kettle every 80 hours and reduce the seed crystal by half. , the corresponding flow rate and rotation speed are reduced by 20%, until the particle size of the four-element doping precursor reaches 18-19 μm in 160-260 hours, and the kettle is stopped.
根据本发明的一些实施例,步骤S3中,所述煅烧前还包括洗涤。According to some embodiments of the present invention, in step S3, washing is also included before the calcination.
根据本发明的一些实施例,步骤S3中,所述煅烧的温度为800~900℃;所述煅烧的时间为4~5h。According to some embodiments of the present invention, in step S3, the calcination temperature is 800-900°C; the calcination time is 4-5 hours.
本发明的其它特征和优点将在随后的说明书中阐述,并且,部分地从说明书中变得显而易见,或者通过实施本发明而了解。Additional features and advantages of the invention will be set forth in the description which follows, and in part will be apparent from the description, or may be learned by practice of the invention.
附图说明Description of the drawings
本发明的上述和/或附加的方面和优点从结合下面附图对实施例的描述中将变得明显和容易理解,其中:The above and/or additional aspects and advantages of the present invention will become apparent and readily understood from the description of the embodiments taken in conjunction with the following drawings, in which:
图1为实施例1所得的铝镍锰镁掺杂碳酸钴颗粒在3000倍扫描电镜(SEM)下的示意图;Figure 1 is a schematic diagram of aluminum nickel manganese magnesium doped cobalt carbonate particles obtained in Example 1 under a 3000x scanning electron microscope (SEM);
图2为实施例1所得的铝镍锰镁掺杂四氧化三钴在30000倍扫描电镜(SEM)下的示意图;Figure 2 is a schematic diagram of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 30,000x scanning electron microscope (SEM);
图3为实施例1所得的铝镍锰镁掺杂四氧化三钴在10000倍扫描电镜(SEM)下的示意图;Figure 3 is a schematic diagram of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 10000x scanning electron microscope (SEM);
图4为实施例1所得的铝镍锰镁掺杂四氧化三钴在5000倍扫描电镜(SEM)下的示意图;Figure 4 is a schematic diagram of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 5000x scanning electron microscope (SEM);
图5为实施例1所得的铝镍锰镁掺杂四氧化三钴在3000倍扫描电镜(SEM)下的示意图;Figure 5 is a schematic diagram of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 3000x scanning electron microscope (SEM);
图6为实施例1所得的铝镍锰镁掺杂四氧化三钴在1000倍扫描电镜(SEM)下的示意图;Figure 6 is a schematic diagram of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 1000x scanning electron microscope (SEM);
图7为实施例1所得的铝镍锰镁掺杂四氧化三钴在500倍扫描电镜(SEM)下的示意图。Figure 7 is a schematic diagram of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 500x scanning electron microscope (SEM).
图8为实施例2所得的铝镍锰镁掺杂碳酸钴颗粒在3000倍扫描电镜(SEM)下的示意图;Figure 8 is a schematic diagram of the aluminum nickel manganese magnesium doped cobalt carbonate particles obtained in Example 2 under a 3000x scanning electron microscope (SEM);
图9为实施例2所得的铝镍锰镁掺杂四氧化三钴在3000倍扫描电镜(SEM)下的示意图;Figure 9 is a schematic diagram of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 2 under a 3000x scanning electron microscope (SEM);
具体实施方式Detailed ways
下面详细描述本发明的实施例,所述实施例的示例在附图中示出,其中自始至终相同或类似的标号表示相同或类似的元件或具有相同或类似功能的元件。下面通过参考附图描述的实施例是示例性的,仅用于解释本发明,而不能理解为对本发明的限制。Embodiments of the present invention are described in detail below, examples of which are illustrated in the accompanying drawings, wherein the same or similar reference numerals throughout represent the same or similar elements or elements with the same or similar functions. The embodiments described below with reference to the drawings are exemplary and are only used to explain the present invention and cannot be understood as limiting the present invention.
实施例1Example 1
本实施例公开了一种铝镍锰镁掺杂四氧化三钴的制备方法,其过程包含以下步骤:This embodiment discloses a preparation method of aluminum nickel manganese magnesium doped with cobalt tetroxide. The process includes the following steps:
A1:配制钴铝镍锰镁混合盐溶液,其中钴盐为氯化钴,浓度为110g/L;铝盐为硫酸铝,铝离子浓度为1.46g/L;镍盐为硫酸镍,浓度为0.24g/L;锰盐为硫酸锰,浓度为0.19g/L;镁盐为硫酸镁,浓度为0.26g/L;A1: Prepare a mixed salt solution of cobalt, aluminum, nickel, manganese and magnesium. The cobalt salt is cobalt chloride with a concentration of 110g/L; the aluminum salt is aluminum sulfate with an aluminum ion concentration of 1.46g/L; the nickel salt is nickel sulfate with a concentration of 0.24 g/L; the manganese salt is manganese sulfate, with a concentration of 0.19g/L; the magnesium salt is magnesium sulfate, with a concentration of 0.26g/L;
A2:配制碳酸氢铵溶液,浓度为240g/L;氨水浓度为140g/L;A2: Prepare ammonium bicarbonate solution with a concentration of 240g/L; ammonia concentration is 140g/L;
A3:将钴铝镍锰镁混合盐溶液、碳酸氢铵溶液、氨水并流加入底液为130g/L碳酸氢铵溶液的反应釜中,底液加入量刚好没过反应釜底层搅拌桨,钴铝镍锰镁混合盐溶液进料为50mL/min,碳酸氢铵溶液进料为55mL/min,氨水进料为8mL/min,体系反应温度为40℃,体系反应pH为7.0~7.5,每80h对反应釜进行分釜处理,晶种减半,对应流量、转速降低20%,直至160~260h得到粒度为18~19μm的铝镍锰镁掺杂碳酸钴;A3: Add cobalt aluminum nickel manganese magnesium mixed salt solution, ammonium bicarbonate solution, and ammonia water into a reaction kettle whose bottom liquid is 130g/L ammonium bicarbonate solution in parallel flow. The amount of bottom liquid added just covers the bottom stirring paddle of the reaction kettle. Cobalt The feed of aluminum, nickel, manganese and magnesium mixed salt solution is 50mL/min, the feed of ammonium bicarbonate solution is 55mL/min, the feed of ammonia water is 8mL/min, the system reaction temperature is 40℃, the system reaction pH is 7.0~7.5, every 80h The reaction kettle is divided into kettles, the seed crystal is halved, and the corresponding flow rate and rotation speed are reduced by 20% until 160 to 260 hours to obtain aluminum nickel manganese magnesium doped cobalt carbonate with a particle size of 18 to 19 μm;
A4:将步骤A3中的铝镍锰镁掺杂碳酸钴洗涤至氯离子含量小于100ppm后,置于回转炉中800℃煅烧4h,获得铝镍锰镁掺杂四氧化三钴;A4: Wash the aluminum nickel manganese magnesium doped cobalt carbonate in step A3 until the chloride ion content is less than 100 ppm, then place it in a rotary furnace and calcine at 800°C for 4 hours to obtain aluminum nickel manganese magnesium doped cobalt tetroxide;
A5:取A4制得的铝镍锰镁掺杂四氧化三钴进行扫描电镜,电镜结果如图2~7所示。从图2中,可看出该材料呈现类球形,表面光滑,掺杂元素均一。其材料的主要理化指标如表1所示,四元素共掺杂四氧化三钴振实密度为2.12g/cm3,实际铝元素浓度为9018ppm、镍元素浓度为1109ppm、锰元素浓度为1264ppm、镁元素浓度为1366ppm;理化指标如表2所示。A5: Take the aluminum nickel manganese magnesium doped cobalt tetroxide prepared by A4 and conduct scanning electron microscopy. The electron microscopy results are shown in Figures 2 to 7. From Figure 2, it can be seen that the material has a spherical shape, a smooth surface, and uniform doping elements. The main physical and chemical indicators of the material are shown in Table 1. The tap density of the four-element co-doped cobalt tetroxide is 2.12g/cm 3 , the actual aluminum element concentration is 9018ppm, the nickel element concentration is 1109ppm, the manganese element concentration is 1264ppm, and the magnesium element concentration It is 1366ppm; the physical and chemical indicators are shown in Table 2.
A6:将铝镍锰镁掺杂四氧化三钴烧制成钴酸锂测试电性能(4.55V)0.1C容量为181.7mAh/g,循环50周容量保持率为98.3%。A6: Al-nickel-manganese-magnesium doped with cobalt tetroxide was fired into lithium cobalt oxide. The electrical performance test (4.55V) at 0.1C was 181.7mAh/g, and the capacity retention rate after 50 cycles was 98.3%.
图1为实施例1所得的铝镍锰镁掺杂碳酸钴颗粒在3000倍扫描电镜(SEM)下的图;Figure 1 is a picture of the aluminum nickel manganese magnesium doped cobalt carbonate particles obtained in Example 1 under a 3000x scanning electron microscope (SEM);
图2为实施例1所得的铝镍锰镁掺杂四氧化三钴在30000倍扫描电镜(SEM)下的图;Figure 2 is a picture of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 30,000x scanning electron microscope (SEM);
图3为实施例1所得的铝镍锰镁掺杂四氧化三钴在10000倍扫描电镜(SEM)下的图;Figure 3 is a picture of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 10,000x scanning electron microscope (SEM);
图4为实施例1所得的铝镍锰镁掺杂四氧化三钴在5000倍扫描电镜(SEM)下的图;Figure 4 is a picture of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 5000x scanning electron microscope (SEM);
图5为实施例1所得的铝镍锰镁掺杂四氧化三钴在3000倍扫描电镜(SEM)下的图;Figure 5 is a picture of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 3000x scanning electron microscope (SEM);
图6为实施例1所得的铝镍锰镁掺杂四氧化三钴在1000倍扫描电镜(SEM)下的图;Figure 6 is a picture of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 1000x scanning electron microscope (SEM);
图7为实施例1所得的铝镍锰镁掺杂四氧化三钴在500倍扫描电镜(SEM)下的图。Figure 7 is a picture of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 1 under a 500x scanning electron microscope (SEM).
表1:铝镍锰镁掺杂四氧化三钴主要理化指标Table 1: Main physical and chemical indicators of aluminum, nickel, manganese and magnesium doped with cobalt tetroxide
实施例2Example 2
A1:配制钴铝镍锰镁混合盐溶液,其中钴盐为氯化钴,浓度为80g/L;铝盐为硫酸铝,铝离子浓度为0.943g/L;镍盐为硫酸镍,浓度为0.177g/L;锰盐为硫酸锰,浓度为0.266g/L;镁盐为硫酸镁,浓度为0.187g/L;A1: Prepare a mixed salt solution of cobalt, aluminum, nickel, manganese and magnesium. The cobalt salt is cobalt chloride with a concentration of 80g/L; the aluminum salt is aluminum sulfate with an aluminum ion concentration of 0.943g/L; the nickel salt is nickel sulfate with a concentration of 0.177 g/L; the manganese salt is manganese sulfate, with a concentration of 0.266g/L; the magnesium salt is magnesium sulfate, with a concentration of 0.187g/L;
A2:配制碳酸氢铵溶液,浓度为200g/L;氨水浓度为100g/L;A2: Prepare ammonium bicarbonate solution with a concentration of 200g/L; ammonia concentration is 100g/L;
A3:将钴铝镍锰镁混合盐溶液、碳酸氢铵溶液、氨水并流加入底液为100g/L碳酸氢铵溶液的反应釜中,底液加入量刚好没过反应釜底层搅拌桨,钴铝镍锰镁混合盐溶液进料为70mL/min,碳酸氢铵溶液进料为65mL/min,氨水进料为12mL/min,体系反应温度为40℃,体系反应pH为7.0~7.5,每80h对反应釜进行分釜处理,晶种减半,对应流量、转速降低20%,直至160~260h得到粒度为18~19μm的铝镍锰镁掺杂碳酸钴;A3: Add cobalt aluminum nickel manganese magnesium mixed salt solution, ammonium bicarbonate solution, and ammonia water into a reaction kettle whose bottom liquid is 100g/L ammonium bicarbonate solution. The amount of bottom liquid added just covers the bottom stirring paddle of the reaction kettle. Cobalt The feed of aluminum, nickel, manganese and magnesium mixed salt solution is 70mL/min, the feed of ammonium bicarbonate solution is 65mL/min, the feed of ammonia water is 12mL/min, the system reaction temperature is 40℃, the system reaction pH is 7.0~7.5, every 80h The reaction kettle is divided into kettles, the seed crystal is halved, and the corresponding flow rate and rotation speed are reduced by 20% until 160 to 260 hours to obtain aluminum nickel manganese magnesium doped cobalt carbonate with a particle size of 18 to 19 μm;
A4:将步骤A3中的铝镍锰镁掺杂碳酸钴洗涤至氯离子含量小于100ppm后,置于回转炉中800℃煅烧4h,获得铝镍锰镁掺杂四氧化三钴;A4: Wash the aluminum nickel manganese magnesium doped cobalt carbonate in step A3 until the chloride ion content is less than 100 ppm, then place it in a rotary furnace and calcine at 800°C for 4 hours to obtain aluminum nickel manganese magnesium doped cobalt tetroxide;
A5:取A4制得的铝镍锰镁掺杂四氧化三钴进行扫描电镜,电镜结果如图7~9所示。从图8中,可看出该材料呈现类球形,表面光滑,掺杂元素均一。其材料的主要理化指标如表2所示,四元素共掺杂四氧化三钴振实密度为2.18g/cm3,实际铝元素浓度为7995ppm、镍元素浓度为1118ppm、锰元素浓度为2326ppm、镁元素浓度为1348ppm;理化指标如表2所示。A5: Take the aluminum nickel manganese magnesium doped cobalt tetroxide prepared by A4 and conduct scanning electron microscopy. The electron microscopy results are shown in Figures 7 to 9. From Figure 8, it can be seen that the material has a spherical shape, a smooth surface, and uniform doping elements. The main physical and chemical indicators of the material are shown in Table 2. The tap density of the four-element co-doped cobalt tetroxide is 2.18g/cm 3 , the actual aluminum element concentration is 7995ppm, the nickel element concentration is 1118ppm, the manganese element concentration is 2326ppm, and the magnesium element concentration is 1348ppm; the physical and chemical indicators are shown in Table 2.
A6:将铝镍锰镁掺杂四氧化三钴烧制成钴酸锂测试电性能(4.55V)0.1C容量为182.4mAh/g,循环50周容量保持率为97.6%。A6: Al-nickel-manganese-magnesium doped with cobalt tetroxide was fired into lithium cobalt oxide. The electrical performance test (4.55V) at 0.1C was 182.4mAh/g, and the capacity retention rate after 50 cycles was 97.6%.
图8为实施例2所得的铝镍锰镁掺杂碳酸钴颗粒在3000倍扫描电镜(SEM)下的图;Figure 8 is a picture of the aluminum nickel manganese magnesium doped cobalt carbonate particles obtained in Example 2 under a 3000x scanning electron microscope (SEM);
图9为实施例2所得的铝镍锰镁掺杂四氧化三钴在3000倍扫描电镜(SEM)下的图;Figure 9 is a picture of the aluminum nickel manganese magnesium doped cobalt tetroxide obtained in Example 2 under a 3000x scanning electron microscope (SEM);
表2:铝镍锰镁掺杂四氧化三钴主要理化指标Table 2: Main physical and chemical indicators of aluminum nickel manganese magnesium doped cobalt tetroxide
对比例1Comparative example 1
A1:配制钴铝混合盐溶液,其中钴盐为氯化钴,浓度为110g/L;铝盐为硫酸铝,铝离子浓度为1.46g/L;A1: Prepare a cobalt-aluminum mixed salt solution, in which the cobalt salt is cobalt chloride with a concentration of 110g/L; the aluminum salt is aluminum sulfate with an aluminum ion concentration of 1.46g/L;
A2:配制碳酸氢铵溶液,浓度为240g/L;氨水浓度为140g/L;A2: Prepare ammonium bicarbonate solution with a concentration of 240g/L; ammonia concentration is 140g/L;
A3:将钴铝混合盐溶液、碳酸氢铵溶液、氨水并流加入底液为130g/L碳酸氢铵溶液的反应釜中,底液加入量刚好没过反应釜底层搅拌桨,钴铝混合盐溶液进料为50mL/min,碳酸氢铵溶液进料为55mL/min,氨水进料为8mL/min,体系反应温度为40℃,体系反应pH为7.0~7.5,每80h对反应釜进行分釜处理,晶种减半,对应流量、转速降低20%,直至160~260h得到粒度为18~19μm的铝掺杂碳酸钴;A3: Add the cobalt-aluminum mixed salt solution, ammonium bicarbonate solution, and ammonia water into a reaction kettle whose bottom liquid is 130g/L ammonium bicarbonate solution in parallel flow. The amount of the bottom liquid added just covers the bottom stirring paddle of the reaction kettle. The cobalt-aluminum mixed salt solution The solution feed is 50mL/min, the ammonium bicarbonate solution feed is 55mL/min, the ammonia water feed is 8mL/min, the system reaction temperature is 40°C, the system reaction pH is 7.0~7.5, and the reaction kettle is separated every 80 hours. During the treatment, the seed crystal is halved, and the corresponding flow rate and rotation speed are reduced by 20% until 160 to 260 hours to obtain aluminum-doped cobalt carbonate with a particle size of 18 to 19 μm;
A4:将步骤A3中的铝掺杂碳酸钴洗涤至氯离子含量小于100ppm后,置于回转炉中800℃煅烧4h,获得振实密度为2.27g/cm3的铝掺杂四氧化三钴,铝掺杂四氧化三钴实际铝元素浓度为8957ppm;A4: Wash the aluminum-doped cobalt carbonate in step A3 until the chloride ion content is less than 100 ppm, then place it in a rotary furnace and calcine it at 800°C for 4 hours to obtain aluminum-doped cobalt tetroxide with a tap density of 2.27g/ cm3 . The actual aluminum element concentration of cobalt tetroxide is 8957ppm;
A5:将铝掺杂四氧化三钴烧制成钴酸锂测试电性能(4.55V)0.1C容量为179.6mAh/g,循环50周容量保持率为96.7%。A5: Aluminum-doped cobalt tetroxide is fired into lithium cobalt oxide. The electrical performance test (4.55V) at 0.1C is 179.6mAh/g, and the capacity retention rate after 50 cycles is 96.7%.
对比例2Comparative example 2
A1:配制钴铝混合盐溶液,其中钴盐为氯化钴,浓度为80g/L;铝盐为硫酸铝,铝离子浓度为0.943g/L;A1: Prepare a cobalt-aluminum mixed salt solution, in which the cobalt salt is cobalt chloride with a concentration of 80g/L; the aluminum salt is aluminum sulfate with an aluminum ion concentration of 0.943g/L;
A2:配制碳酸氢铵溶液,浓度为200g/L;氨水浓度为100g/L;A2: Prepare ammonium bicarbonate solution with a concentration of 200g/L; ammonia concentration is 100g/L;
A3:将钴铝混合盐溶液、碳酸氢铵溶液、氨水并流加入底液为100g/L碳酸氢铵溶液的反应釜中,底液加入量刚好没过反应釜底层搅拌桨,钴铝混合盐溶液进料为70mL/min,碳酸氢铵溶液进料为65mL/min,氨水进料为12mL/min,体系反应温度为40℃,体系反应pH为7.0~7.5,每80h对反应釜进行分釜处理,晶种减半,对应流量、转速降低20%,直至160~260h得到粒度为18~19μm的铝掺杂碳酸钴;A3: Add the cobalt-aluminum mixed salt solution, ammonium bicarbonate solution, and ammonia water into a reaction kettle whose bottom liquid is 100g/L ammonium bicarbonate solution in parallel flows. The amount of the bottom liquid added just covers the bottom stirring paddle of the reaction kettle. The cobalt-aluminum mixed salt solution The solution feed is 70mL/min, the ammonium bicarbonate solution feed is 65mL/min, the ammonia water feed is 12mL/min, the system reaction temperature is 40°C, the system reaction pH is 7.0~7.5, and the reaction kettle is separated every 80 hours. During the treatment, the seed crystal is halved, and the corresponding flow rate and rotation speed are reduced by 20% until 160 to 260 hours to obtain aluminum-doped cobalt carbonate with a particle size of 18 to 19 μm;
A4:将步骤A3中的铝掺杂碳酸钴洗涤至氯离子含量小于100ppm后,置于回转炉中800℃煅烧4h,获得振实密度为2.19g/cm3的铝掺杂四氧化三钴,铝掺杂四氧化三钴实际铝元素浓度为7957ppm;A4: Wash the aluminum-doped cobalt carbonate in step A3 until the chloride ion content is less than 100 ppm, then place it in a rotary furnace and calcine it at 800°C for 4 hours to obtain aluminum-doped cobalt tetroxide with a tap density of 2.19g/ cm3 . The actual aluminum element concentration of cobalt tetroxide is 7957ppm;
A5:将铝掺杂四氧化三钴烧制成钴酸锂测试电性能(4.55V)0.1C容量为180.3mAh/g,循环50周容量保持率为94.5%。A5: Aluminum-doped cobalt tetroxide is fired into lithium cobalt oxide. The electrical performance test (4.55V) at 0.1C is 180.3mAh/g, and the capacity retention rate after 50 cycles is 94.5%.
上面结合附图对本发明实施例作了详细说明,但本发明不限于上述实施例,在所属技术领域普通技术人员所具备的知识范围内,还可以在不脱离本发明宗旨的前提下作出各种变化。The embodiments of the present invention have been described in detail above with reference to the accompanying drawings. However, the present invention is not limited to the above embodiments. Within the scope of knowledge possessed by those of ordinary skill in the art, various modifications can be made without departing from the purpose of the present invention. Variety.
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| CN110534719A (en) * | 2019-09-06 | 2019-12-03 | 衢州华友钴新材料有限公司 | A kind of preparation method of aluminum-magnesium-nickel-manganese spherical cobalt tetroxide |
| CN113562777A (en) * | 2021-09-27 | 2021-10-29 | 金驰能源材料有限公司 | Preparation method and application of multi-element doped cathode material precursor with low impurity content |
| CN115520903A (en) * | 2022-09-21 | 2022-12-27 | 青海泰丰先行锂能科技有限公司 | Preparation method and positive electrode material of doped tricobalt tetroxide with wide particle size distribution |
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