CN113707931A - High-rate rapid charging and discharging aluminum ion battery and preparation method thereof - Google Patents
High-rate rapid charging and discharging aluminum ion battery and preparation method thereof Download PDFInfo
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- CN113707931A CN113707931A CN202111008025.2A CN202111008025A CN113707931A CN 113707931 A CN113707931 A CN 113707931A CN 202111008025 A CN202111008025 A CN 202111008025A CN 113707931 A CN113707931 A CN 113707931A
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- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 45
- 238000007599 discharging Methods 0.000 title claims abstract description 14
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- 239000000919 ceramic Substances 0.000 claims abstract description 16
- 239000003792 electrolyte Substances 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims abstract description 6
- 238000007789 sealing Methods 0.000 claims abstract description 5
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical group Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims description 28
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 27
- -1 aluminum ion Chemical class 0.000 claims description 25
- 238000000576 coating method Methods 0.000 claims description 24
- 239000011248 coating agent Substances 0.000 claims description 22
- 229910052799 carbon Inorganic materials 0.000 claims description 19
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 15
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 14
- 239000011888 foil Substances 0.000 claims description 12
- TZIHFWKZFHZASV-UHFFFAOYSA-N methyl formate Chemical group COC=O TZIHFWKZFHZASV-UHFFFAOYSA-N 0.000 claims description 12
- 238000002156 mixing Methods 0.000 claims description 12
- 239000011148 porous material Substances 0.000 claims description 10
- FQERWQCDIIMLHB-UHFFFAOYSA-N 1-ethyl-3-methyl-1,2-dihydroimidazol-1-ium;chloride Chemical compound [Cl-].CC[NH+]1CN(C)C=C1 FQERWQCDIIMLHB-UHFFFAOYSA-N 0.000 claims description 8
- 238000005096 rolling process Methods 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 7
- OIFBSDVPJOWBCH-UHFFFAOYSA-N Diethyl carbonate Chemical compound CCOC(=O)OCC OIFBSDVPJOWBCH-UHFFFAOYSA-N 0.000 claims description 6
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 6
- 239000006258 conductive agent Substances 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- 239000011230 binding agent Substances 0.000 claims description 5
- WWFKDEYBOOGHKL-UHFFFAOYSA-N 1-ethyl-3-methyl-1,2-dihydroimidazol-1-ium;bromide Chemical compound Br.CCN1CN(C)C=C1 WWFKDEYBOOGHKL-UHFFFAOYSA-N 0.000 claims description 4
- XMWRBQBLMFGWIX-UHFFFAOYSA-N C60 fullerene Chemical compound C12=C3C(C4=C56)=C7C8=C5C5=C9C%10=C6C6=C4C1=C1C4=C6C6=C%10C%10=C9C9=C%11C5=C8C5=C8C7=C3C3=C7C2=C1C1=C2C4=C6C4=C%10C6=C9C9=C%11C5=C5C8=C3C3=C7C1=C1C2=C4C6=C2C9=C5C3=C12 XMWRBQBLMFGWIX-UHFFFAOYSA-N 0.000 claims description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 4
- 239000011149 active material Substances 0.000 claims description 4
- 150000001350 alkyl halides Chemical class 0.000 claims description 4
- 239000006256 anode slurry Substances 0.000 claims description 4
- 229950005499 carbon tetrachloride Drugs 0.000 claims description 4
- 150000001733 carboxylic acid esters Chemical class 0.000 claims description 4
- 239000002131 composite material Substances 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 4
- 229910003472 fullerene Inorganic materials 0.000 claims description 4
- 229910021389 graphene Inorganic materials 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- 239000002994 raw material Substances 0.000 claims description 3
- HNAGHMKIPMKKBB-UHFFFAOYSA-N 1-benzylpyrrolidine-3-carboxamide Chemical compound C1C(C(=O)N)CCN1CC1=CC=CC=C1 HNAGHMKIPMKKBB-UHFFFAOYSA-N 0.000 claims description 2
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims description 2
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 2
- JGFBQFKZKSSODQ-UHFFFAOYSA-N Isothiocyanatocyclopropane Chemical compound S=C=NC1CC1 JGFBQFKZKSSODQ-UHFFFAOYSA-N 0.000 claims description 2
- RJUFJBKOKNCXHH-UHFFFAOYSA-N Methyl propionate Chemical compound CCC(=O)OC RJUFJBKOKNCXHH-UHFFFAOYSA-N 0.000 claims description 2
- 239000002033 PVDF binder Substances 0.000 claims description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 claims description 2
- KXKVLQRXCPHEJC-UHFFFAOYSA-N acetic acid trimethyl ester Natural products COC(C)=O KXKVLQRXCPHEJC-UHFFFAOYSA-N 0.000 claims description 2
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 claims description 2
- 125000000217 alkyl group Chemical group 0.000 claims description 2
- 239000010405 anode material Substances 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims description 2
- 229910052794 bromium Inorganic materials 0.000 claims description 2
- OBNCKNCVKJNDBV-UHFFFAOYSA-N butanoic acid ethyl ester Natural products CCCC(=O)OCC OBNCKNCVKJNDBV-UHFFFAOYSA-N 0.000 claims description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 2
- PWLNAUNEAKQYLH-UHFFFAOYSA-N butyric acid octyl ester Natural products CCCCCCCCOC(=O)CCC PWLNAUNEAKQYLH-UHFFFAOYSA-N 0.000 claims description 2
- 239000006229 carbon black Substances 0.000 claims description 2
- 239000004917 carbon fiber Substances 0.000 claims description 2
- 239000002041 carbon nanotube Substances 0.000 claims description 2
- 229910021393 carbon nanotube Inorganic materials 0.000 claims description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 claims description 2
- 229910052801 chlorine Inorganic materials 0.000 claims description 2
- 239000000460 chlorine Substances 0.000 claims description 2
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical group COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 claims description 2
- 229940093499 ethyl acetate Drugs 0.000 claims description 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims description 2
- JBTWLSYIZRCDFO-UHFFFAOYSA-N ethyl methyl carbonate Chemical compound CCOC(=O)OC JBTWLSYIZRCDFO-UHFFFAOYSA-N 0.000 claims description 2
- 229910002804 graphite Inorganic materials 0.000 claims description 2
- 239000010439 graphite Substances 0.000 claims description 2
- 229910052736 halogen Inorganic materials 0.000 claims description 2
- 150000002367 halogens Chemical class 0.000 claims description 2
- 150000002460 imidazoles Chemical class 0.000 claims description 2
- 150000004693 imidazolium salts Chemical class 0.000 claims description 2
- 239000012535 impurity Substances 0.000 claims description 2
- 238000010030 laminating Methods 0.000 claims description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- 229940017219 methyl propionate Drugs 0.000 claims description 2
- 230000004048 modification Effects 0.000 claims description 2
- 238000012986 modification Methods 0.000 claims description 2
- 239000002808 molecular sieve Substances 0.000 claims description 2
- YKYONYBAUNKHLG-UHFFFAOYSA-N n-Propyl acetate Natural products CCCOC(C)=O YKYONYBAUNKHLG-UHFFFAOYSA-N 0.000 claims description 2
- UUIQMZJEGPQKFD-UHFFFAOYSA-N n-butyric acid methyl ester Natural products CCCC(=O)OC UUIQMZJEGPQKFD-UHFFFAOYSA-N 0.000 claims description 2
- 239000003960 organic solvent Substances 0.000 claims description 2
- 125000001147 pentyl group Chemical group C(CCCC)* 0.000 claims description 2
- 239000002985 plastic film Substances 0.000 claims description 2
- 229920006255 plastic film Polymers 0.000 claims description 2
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims description 2
- 229940090181 propyl acetate Drugs 0.000 claims description 2
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 2
- 238000000746 purification Methods 0.000 claims description 2
- 239000002002 slurry Substances 0.000 claims description 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 2
- 235000019812 sodium carboxymethyl cellulose Nutrition 0.000 claims description 2
- 229920001027 sodium carboxymethylcellulose Polymers 0.000 claims description 2
- 238000001179 sorption measurement Methods 0.000 claims description 2
- 229920003048 styrene butadiene rubber Polymers 0.000 claims description 2
- PUGUQINMNYINPK-UHFFFAOYSA-N tert-butyl 4-(2-chloroacetyl)piperazine-1-carboxylate Chemical compound CC(C)(C)OC(=O)N1CCN(C(=O)CCl)CC1 PUGUQINMNYINPK-UHFFFAOYSA-N 0.000 claims description 2
- 239000010936 titanium Substances 0.000 claims description 2
- 229910052719 titanium Inorganic materials 0.000 claims description 2
- NQPDZGIKBAWPEJ-UHFFFAOYSA-N valeric acid Chemical compound CCCCC(O)=O NQPDZGIKBAWPEJ-UHFFFAOYSA-N 0.000 claims description 2
- CYKMNKXPYXUVPR-UHFFFAOYSA-N [C].[Ti] Chemical compound [C].[Ti] CYKMNKXPYXUVPR-UHFFFAOYSA-N 0.000 claims 2
- 239000011883 electrode binding agent Substances 0.000 claims 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims 1
- 238000003825 pressing Methods 0.000 claims 1
- 230000008569 process Effects 0.000 abstract description 6
- 230000014759 maintenance of location Effects 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract description 2
- 150000002500 ions Chemical group 0.000 description 10
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000004200 deflagration Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000003446 memory effect Effects 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000003860 storage 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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/054—Accumulators with insertion or intercalation of metals other than lithium, e.g. with magnesium or aluminium
-
- 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
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
-
- 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
- H01M10/058—Construction or manufacture
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/431—Inorganic material
- H01M50/434—Ceramics
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/021—Physical characteristics, e.g. porosity, surface area
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Abstract
The invention discloses a high-rate rapid charging and discharging aluminum ion battery and a preparation method thereof. The aluminum ion battery comprises a positive plate, a negative plate, a ceramic diaphragm, electrolyte and a battery case, wherein the positive plate, the ceramic diaphragm, the negative plate and the ceramic diaphragm are sequentially and repeatedly laminated to form a dry battery core, and the aluminum ion battery is prepared by putting the dry battery core into the battery case, injecting the electrolyte, opening the dry battery core to form the dry battery core, sealing the dry battery core and dividing the dry battery core into the battery case. By optimizing the application of the optimized material and the process technology, the prepared aluminum ion battery can be rapidly charged at the rate of 6C and discharged at the rate of 1C, and the charge-discharge capacity retention rate is up to more than 90%.
Description
Technical Field
The invention belongs to the technical field of secondary ion battery processes, and relates to a high-rate rapid charging and discharging aluminum ion battery and a preparation method thereof.
Background
With the vigorous development of new energy industry, secondary ion batteries have been widely used in various fields because of their advantages of high energy density, high power density, long cycle life, no memory effect, low self-discharge rate, wide working temperature range, safety, reliability, environmental friendliness, etc.
At present, the process technology of commercial secondary ion batteries is relatively mature, the performances of rapid charge and discharge and the like are obviously optimized and improved, but the breakthrough is difficult to be made on the aspect of high-rate rapid charge and discharge performance, and particularly the high capacity retention rate is difficult to be realized on the aspect of rate discharge performance of more than 10C.
Under the background, the invention provides the high-rate rapid charging and discharging aluminum ion battery and the preparation method thereof to make up the defects of the prior art, thereby solving the problem of high-rate rapid discharging of the secondary ion battery.
Disclosure of Invention
The invention provides a high-rate rapid charging and discharging aluminum ion battery and a preparation method thereof, which improve the ion storage space, the specific surface area, the pore volume and the number of pores of an active material of a positive plate, and increase the migration and transmission channels of ions, thereby enhancing the rapid and stable embedding/de-embedding of the ions, solving the problem of rapid high-rate charging and discharging of the battery, and simultaneously improving the energy density of the battery; the capacity retention rate of 10C/1C charge and discharge relative to 1C/1C charge and discharge reaches more than 90 percent.
The technical scheme adopted by the invention is as follows:
a high-rate rapid charge-discharge aluminum ion battery comprises a dry battery core, wherein the dry battery core comprises a positive plate, a negative plate and a ceramic diaphragm, and all parts are sequentially and repeatedly laminated to form the high-rate rapid charge-discharge aluminum ion battery; the aluminum ion battery is prepared by putting a dry battery core into a battery shell, injecting electrolyte, forming, sealing and grading.
The positive plate is prepared by uniformly coating dried positive material, conductive agent and binder into slurry on the front and back surfaces of the nano microporous superconducting carbon-coated titanium mesh with the reserved tabs to form a positive plate coating, and drying and rolling the positive plate to obtain the positive plate with the thickness of 0.1-0.5 mm.
The negative plate is a nano microporous aluminum foil and is obtained by rolling the aluminum foil with the reserved tab through nano needling, the thickness of the negative plate is 0.6-1 mm, and the aperture of the nano micropore is 30-100 nm.
The positive and negative both sides coating nanometer alumina coating of diaphragm to with the help of the vacuum baking oven solvent in removing the alumina coating obtains, and ceramic diaphragm thickness is 6 ~ 30um, and ceramic diaphragm's area is greater than the area of positive/negative pole piece.
The electrolyte is prepared by combining and mixing aluminum halide salt, imidazolium salt, alkyl halide, carbonate and/or carboxylic ester organic solvent; the aluminum halide salt is aluminum chloride and aluminum bromide; the imidazole salt is 1-methyl-3-ethyl imidazole chloride, 1-ethyl-3-methyl imidazole chloride, 1-methyl-3-ethyl imidazole bromide and 1-ethyl-3-methyl imidazole bromide; the alkyl halide is M-halogenated N alkyl, M is 1, 2, 3, 4, 5, …, N is methyl, ethyl, propyl, butyl, pentyl, …, and the halogen is chlorine or bromine; the carbonate is dimethyl carbonate, ethyl methyl carbonate and diethyl carbonate; the carboxylic ester is methyl formate, methyl acetate, ethyl acetate, propyl acetate, methyl propionate, methyl butyrate and ethyl butyrate.
The preparation method of the electrolyte comprises the following steps:
firstly, raw material treatment: baking and drying aluminum chloride and 1-ethyl-3-methylimidazole chloride respectively, and removing water; respectively passing tetrachloromethane, diethyl carbonate and methyl formate through a core filter, an adsorption column, a purification column and a molecular sieve to remove impurities and water;
mixing and dispersing: putting aluminum chloride and 1-ethyl-3-methylimidazole chloride into a tetrachloromethane solvent, mixing and stirring, and fully and uniformly dispersing to obtain an anhydrous aluminum chloride ion solution; the molar ratio of the aluminum ions to the chloride ions is 1: 3.5-4;
physical modification: mixing and stirring the anhydrous aluminum chloride ion solution, diethyl carbonate and methyl formate, and fully and uniformly dispersing to obtain the anhydrous aluminum chloride ion electrolyte with low viscosity and high fluidity; the concentration of aluminum chloride ions is 4-16 mol/L;
the active material of the positive plate is prepared by combining and mixing porous composite carbon, fullerene and graphene, wherein the mixing ratio is 30 percent to 60 percent to 10 percent; the porous composite carbon has a pore diameter of 20-50 nm and a specific surface area of 200-500 m2(ii)/g, pore volume greater than 95%; the specific surface area of the fullerene is 1000-1500 m2(ii)/g; the specific surface area of the graphene is 2000-3000 m2/g;
The positive electrode conductive agent is one or the combination of more than two of superconductive carbon black, conductive graphite, carbon fiber and carbon nano tube.
The positive binder is one or the combination of more than two of polyvinylidene fluoride, styrene butadiene rubber and sodium carboxymethyl cellulose.
The nanometer micropore superconducting carbon-coated titanium mesh is obtained by coating a nanometer super conductive carbon coating on the surface of a high-porosity titanium mesh, not coating the titanium mesh on which a lug is reserved, and removing a solvent in the super conductive carbon coating by using a vacuum baking oven, wherein the thickness of the nanometer micropore superconducting carbon-coated titanium mesh is 6-20 mu m, and the pore diameter of the nanometer micropore is 30-100 nm.
The battery shell is square and is made of an aluminum-plastic film.
The high-rate rapid charging and discharging aluminum ion battery is safe and stable. The increase of the pore volume and the number of pores of the active material of the positive plate reduces the material volume drastic change effect caused by ion embedding and de-embedding in the charging and discharging process of the battery, improves the heat dissipation performance of the working process of the battery and further improves the safety and stability performance of the battery; the battery is completely matched without a heat dissipation cooling device in the using process, and fire, deflagration and explosion are basically avoided when the battery is impacted, extruded and needled by heavy objects.
In the application field of secondary ion batteries, in the market environment where lithium resources are in short supply and the price of lithium is high, the resources of aluminum and carbon are very rich, the processing is easier, and the cost advantage is very obvious, so that the raw material cost of the secondary ion battery is greatly reduced.
Detailed Description
The following describes specific embodiments of the present invention in detail with reference to the technical solutions.
A manufacturing method of a high-rate rapid charging and discharging aluminum ion battery comprises the following steps:
step 1, manufacturing a positive plate: preparing anode slurry from 85-98% by mass of an anode material, 1-10% by mass of a conductive agent and 1-15% by mass of a binder, uniformly coating the anode slurry on the front surface and the back surface of the nano microporous superconducting carbon-coated titanium mesh, and reserving a 5mm blank between the edges of the four directions of the anode coating plane and the edges of the nano microporous superconducting carbon-coated titanium mesh in the coating process; putting the anode plate into a vacuum baking oven, and baking the anode plate at 85 ℃ in a vacuum environment of-0.09 to-0.1 MPa to obtain an anode plate; rolling the positive plate to a compact state by using a calender, then putting the positive plate into a vacuum baking oven, and baking at 110 ℃ in a vacuum environment of-0.09 to-0.1 MPa to obtain the positive plate;
step 2, manufacturing the negative plate: rolling the aluminum foil with the thickness of 0.6-1 mm and reserved with the tabs by a nano-needle roller press, piercing the aluminum foil by a nano needle, and leaving a plurality of nano-micropores with the thickness of 30-100 nm on the aluminum foil to obtain a negative plate;
step 3, manufacturing the dry electric core: sequentially and repeatedly laminating the positive plate, the ceramic diaphragm, the negative plate and the ceramic diaphragm, wherein the reserved tab of the nano microporous superconducting carbon-coated titanium net of each positive plate is laminated and gathered, then wrapped by a metal sheet and welded to form a positive full tab, the reserved tab of the nano microporous aluminum foil of each negative plate is laminated and gathered, then wrapped by a metal sheet and welded to form a negative full tab, and the laminated outer surfaces in the positive/negative full tab direction and the reverse direction are wrapped by diaphragms to obtain a dry cell;
and step 4, assembling the battery: applying a certain pressure on a dry battery core at a certain temperature to enable the contact among the positive plate, the negative plate and the ceramic diaphragm to be more compact, then putting the dry battery core into a battery case, injecting electrolyte into the battery case, and obtaining the aluminum ion battery through formation, sealing and capacity grading.
Claims (8)
1. A high-rate rapid charge-discharge aluminum ion battery comprises a dry battery core, wherein the dry battery core comprises a positive plate, a ceramic diaphragm, a negative plate and a ceramic diaphragm, and all parts are sequentially and repeatedly laminated to form the high-rate rapid charge-discharge aluminum ion battery; the aluminum ion battery is prepared by putting a dry battery core into a battery shell, injecting electrolyte, opening, forming, sealing and grading; the method is characterized in that:
the positive plate is formed by uniformly coating dried positive material, conductive agent and binder into slurry on the front and back surfaces of the nano microporous superconducting carbon-coated titanium mesh with the reserved tabs to form a positive plate coating, and drying and rolling are carried out to obtain the positive plate with the integrated middle-surface density and middle-compacted density of the front and back materials, wherein the thickness of the positive plate is 0.1-0.5 mm;
the negative plate is a nano microporous aluminum foil and is prepared by rolling the aluminum foil with reserved lugs through nano needling, the thickness of the negative plate is 0.6-1 mm, and the aperture of the nano micropores is 30-100 nm;
coating the front surface and the back surface of the diaphragm with a nano aluminum oxide coating, and removing a solvent in the aluminum oxide coating by using a vacuum baking oven; the thickness of the ceramic diaphragm is 6-30 um, and the area of the ceramic diaphragm is larger than that of the positive/negative plate;
the electrolyte is prepared by combining and mixing aluminum halide salt, imidazolium salt, alkyl halide, carbonate and/or carboxylic ester organic solvent; the aluminum halide salt is aluminum chloride or aluminum bromide; the imidazole salt is one of 1-methyl-3-ethyl imidazole chloride, 1-ethyl-3-methyl imidazole chloride, 1-methyl-3-ethyl imidazole bromide and 1-ethyl-3-methyl imidazole bromide; the alkyl halide is M-halogenated N alkyl, wherein M is 1, 2, 3, 4, 5 and …, N is methyl, ethyl, propyl, butyl, pentyl and …, and halogen is chlorine or bromine; the carbonate is dimethyl carbonate, ethyl methyl carbonate and diethyl carbonate; the carboxylic ester is methyl formate, methyl acetate, ethyl acetate, propyl acetate, methyl propionate, methyl butyrate and ethyl butyrate.
2. The high-rate rapid charging and discharging aluminum ion battery as claimed in claim 1, wherein the active material of the positive plate is prepared by mixing porous composite carbon, fullerene and graphene, and the mixing ratio is 30% to 60% to 10%; the porous composite carbon has a pore diameter of 20-50 nm and a specific surface area of 200-500 m2(ii)/g, pore volume greater than 95%; the specific surface area of the fullerene is 1000-1500 m2(ii)/g; the specific surface area of the graphene is 2000-3000 m2/g。
3. The high-rate rapid charge-discharge aluminum ion battery according to claim 1 or 2, wherein the positive electrode conductive agent is one or a combination of two or more of superconducting carbon black, conductive graphite, carbon fiber and carbon nanotube.
4. The high-rate rapid charge-discharge aluminum ion battery according to claim 3, wherein the positive electrode binder is one or a combination of two or more of polyvinylidene fluoride, styrene butadiene rubber and sodium carboxymethylcellulose.
5. The high-rate rapid charging and discharging aluminum ion battery as claimed in claim 1, 2 or 4, wherein the nano-microporous superconducting carbon-titanium-coated mesh is obtained by coating a nano-super conductive carbon coating on the surface of a high-porosity titanium mesh, leaving no coating on the titanium mesh at the tab position, and removing the solvent in the super conductive carbon coating by means of a vacuum oven, wherein the thickness of the nano-microporous superconducting carbon-titanium-coated mesh is 6-20 μm, and the pore diameter of the nano-micropores is 30-100 nm.
6. The high-rate rapid charge-discharge aluminum ion battery according to claim 5, wherein the electrolyte is prepared by the following steps:
firstly, raw material treatment: baking and drying aluminum chloride and 1-ethyl-3-methylimidazole chloride respectively, and removing water; respectively passing tetrachloromethane, diethyl carbonate and methyl formate through a core filter, an adsorption column, a purification column and a molecular sieve to remove impurities and water;
mixing and dispersing: putting aluminum chloride and 1-ethyl-3-methylimidazole chloride into a tetrachloromethane solvent, mixing and stirring, and fully and uniformly dispersing to obtain an anhydrous aluminum chloride ion solution; the molar ratio of the aluminum ions to the chloride ions is 1: 3.5-4;
physical modification: mixing and stirring the anhydrous aluminum chloride ion solution, diethyl carbonate and methyl formate, and fully and uniformly dispersing to obtain the anhydrous aluminum chloride ion electrolyte with low viscosity and high fluidity; the concentration of aluminum chloride ions is 4-16 mol/L.
7. The battery can of claim 6, wherein the shape is square and the material is an aluminum plastic film.
8. The preparation method of the high-rate rapid charging and discharging aluminum ion battery as claimed in any one of claims 1 to 7, characterized by comprising the following steps:
A. manufacture of positive plate
Preparing anode slurry from 85-98% by mass of an anode material, 1-10% by mass of a conductive agent and 1-15% by mass of a binder, uniformly coating the anode slurry on the front surface and the back surface of the nano microporous superconducting carbon-coated titanium mesh, and reserving a 5mm blank between the edges of the four directions of the anode coating plane and the edges of the nano microporous superconducting carbon-coated titanium mesh in the coating process; putting the anode plate into a vacuum baking oven, and baking the anode plate at 85 ℃ in a vacuum environment of-0.09 to-0.1 MPa to obtain an anode plate; rolling the positive plate to a compact state by using a calender, then putting the positive plate into a vacuum baking oven, and baking at 110 ℃ in a vacuum environment of-0.09 to-0.1 MPa to obtain the positive plate;
B. manufacture of negative plate
Rolling the aluminum foil with the thickness of 0.6-1 mm and reserved with the tabs by a nano-needle roller press, piercing the aluminum foil by a nano needle, and leaving a plurality of nano-micropores with the thickness of 30-100 nm on the aluminum foil to obtain a negative plate;
C. dry cell fabrication
Sequentially and repeatedly laminating the positive plate, the ceramic diaphragm, the negative plate and the ceramic diaphragm, wherein the reserved tab of the nano microporous superconducting carbon-coated titanium net of each positive plate is laminated and gathered, then wrapped by a metal sheet and welded to form a positive full tab, the reserved tab of the nano microporous aluminum foil of each negative plate is laminated and gathered, then wrapped by a metal sheet and welded to form a negative full tab, and the laminated outer surfaces in the positive/negative full tab direction and the reverse direction are wrapped by diaphragms to obtain a dry cell;
D. battery assembly
And applying pressure to the dry cell to enable the contact among the positive plate, the negative plate and the ceramic diaphragm to be more compact, then putting the dry cell into a cell shell, injecting electrolyte into the cell shell, and performing opening formation, sealing and capacity grading to obtain the aluminum ion cell.
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CN108376795A (en) * | 2018-04-04 | 2018-08-07 | 天津大学 | A kind of no dendrite, powerful aluminium ion battery |
US20200287232A1 (en) * | 2019-03-08 | 2020-09-10 | Everon24, Inc. | Aqueous aluminum ion batteries, hybrid battery-capacitors, compositions of said batteries and battery-capacitors, and associated methods of manufacture and use |
CN112164828A (en) * | 2020-09-22 | 2021-01-01 | 同济大学 | Fibrous flexible aluminum ion battery and preparation method thereof |
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CN108376795A (en) * | 2018-04-04 | 2018-08-07 | 天津大学 | A kind of no dendrite, powerful aluminium ion battery |
US20200287232A1 (en) * | 2019-03-08 | 2020-09-10 | Everon24, Inc. | Aqueous aluminum ion batteries, hybrid battery-capacitors, compositions of said batteries and battery-capacitors, and associated methods of manufacture and use |
CN112164828A (en) * | 2020-09-22 | 2021-01-01 | 同济大学 | Fibrous flexible aluminum ion battery and preparation method thereof |
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