WO2023236573A1 - Procédé de préparation de feuille d'électrode basse tension de volume spécifique élevé pour électronique d'automobile - Google Patents
Procédé de préparation de feuille d'électrode basse tension de volume spécifique élevé pour électronique d'automobile Download PDFInfo
- Publication number
- WO2023236573A1 WO2023236573A1 PCT/CN2023/075328 CN2023075328W WO2023236573A1 WO 2023236573 A1 WO2023236573 A1 WO 2023236573A1 CN 2023075328 W CN2023075328 W CN 2023075328W WO 2023236573 A1 WO2023236573 A1 WO 2023236573A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- foil
- formation
- controlled
- minutes
- dip
- Prior art date
Links
- 239000011888 foil Substances 0.000 title claims abstract description 195
- 238000000034 method Methods 0.000 title claims abstract description 20
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 130
- 238000011282 treatment Methods 0.000 claims abstract description 31
- 229910019142 PO4 Inorganic materials 0.000 claims abstract description 17
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims abstract description 16
- 239000010452 phosphate Substances 0.000 claims abstract description 16
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 10
- 239000000126 substance Substances 0.000 claims description 29
- 238000012805 post-processing Methods 0.000 claims description 27
- 238000005406 washing Methods 0.000 claims description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 26
- 238000004140 cleaning Methods 0.000 claims description 24
- 239000011259 mixed solution Substances 0.000 claims description 24
- 239000002253 acid Substances 0.000 claims description 22
- 239000007864 aqueous solution Substances 0.000 claims description 22
- 238000007605 air drying Methods 0.000 claims description 20
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims description 19
- 229910052921 ammonium sulfate Inorganic materials 0.000 claims description 19
- 235000011130 ammonium sulphate Nutrition 0.000 claims description 19
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 claims description 19
- 235000019982 sodium hexametaphosphate Nutrition 0.000 claims description 19
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 claims description 19
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 18
- 239000000243 solution Substances 0.000 claims description 17
- NVIFVTYDZMXWGX-UHFFFAOYSA-N sodium metaborate Chemical compound [Na+].[O-]B=O NVIFVTYDZMXWGX-UHFFFAOYSA-N 0.000 claims description 16
- 239000000203 mixture Substances 0.000 claims description 14
- 238000002360 preparation method Methods 0.000 claims description 13
- BTBUEUYNUDRHOZ-UHFFFAOYSA-N Borate Chemical compound [O-]B([O-])[O-] BTBUEUYNUDRHOZ-UHFFFAOYSA-N 0.000 claims description 11
- 238000001035 drying Methods 0.000 claims description 10
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 9
- -1 amine salt Chemical class 0.000 claims description 8
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical group [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 claims description 7
- 230000001590 oxidative effect Effects 0.000 claims description 7
- 235000019333 sodium laurylsulphate Nutrition 0.000 claims description 7
- 238000010981 drying operation Methods 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 6
- XBPCUCUWBYBCDP-UHFFFAOYSA-N Dicyclohexylamine Chemical class C1CCCCC1NC1CCCCC1 XBPCUCUWBYBCDP-UHFFFAOYSA-N 0.000 claims description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 5
- 150000003242 quaternary ammonium salts Chemical class 0.000 claims description 5
- 229910021538 borax Inorganic materials 0.000 claims description 4
- LQZZUXJYWNFBMV-UHFFFAOYSA-N dodecan-1-ol Chemical compound CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 claims description 4
- 239000004328 sodium tetraborate Substances 0.000 claims description 4
- 235000010339 sodium tetraborate Nutrition 0.000 claims description 4
- 239000005696 Diammonium phosphate Substances 0.000 claims description 3
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 claims description 3
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 claims description 3
- 229910000388 diammonium phosphate Inorganic materials 0.000 claims description 3
- 235000019838 diammonium phosphate Nutrition 0.000 claims description 3
- XHFGWHUWQXTGAT-UHFFFAOYSA-N dimethylamine hydrochloride Natural products CNC(C)C XHFGWHUWQXTGAT-UHFFFAOYSA-N 0.000 claims description 3
- IQDGSYLLQPDQDV-UHFFFAOYSA-N dimethylazanium;chloride Chemical compound Cl.CNC IQDGSYLLQPDQDV-UHFFFAOYSA-N 0.000 claims description 3
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 claims description 3
- XJWSAJYUBXQQDR-UHFFFAOYSA-M dodecyltrimethylammonium bromide Chemical compound [Br-].CCCCCCCCCCCC[N+](C)(C)C XJWSAJYUBXQQDR-UHFFFAOYSA-M 0.000 claims description 3
- 238000005554 pickling Methods 0.000 claims description 3
- BTSZTGGZJQFALU-UHFFFAOYSA-N piroctone olamine Chemical compound NCCO.CC(C)(C)CC(C)CC1=CC(C)=CC(=O)N1O BTSZTGGZJQFALU-UHFFFAOYSA-N 0.000 claims description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 2
- HNDVDQJCIGZPNO-UHFFFAOYSA-N histidine Natural products OC(=O)C(N)CC1=CN=CN1 HNDVDQJCIGZPNO-UHFFFAOYSA-N 0.000 claims description 2
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 claims description 2
- 229910017604 nitric acid Inorganic materials 0.000 claims description 2
- 239000012266 salt solution Substances 0.000 claims description 2
- 238000003786 synthesis reaction Methods 0.000 claims description 2
- WGQKYBSKWIADBV-UHFFFAOYSA-N aminomethyl benzene Natural products NCC1=CC=CC=C1 WGQKYBSKWIADBV-UHFFFAOYSA-N 0.000 claims 1
- 150000003839 salts Chemical class 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 7
- 238000009835 boiling Methods 0.000 abstract description 6
- 230000007547 defect Effects 0.000 abstract description 5
- 150000001412 amines Chemical class 0.000 abstract description 3
- 239000013078 crystal Substances 0.000 abstract description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 abstract description 3
- 230000008439 repair process Effects 0.000 abstract description 3
- 238000002791 soaking Methods 0.000 abstract description 2
- 238000005530 etching Methods 0.000 abstract 1
- 230000002035 prolonged effect Effects 0.000 abstract 1
- 235000021317 phosphate Nutrition 0.000 description 11
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 8
- VLTRZXGMWDSKGL-UHFFFAOYSA-N perchloric acid Chemical compound OCl(=O)(=O)=O VLTRZXGMWDSKGL-UHFFFAOYSA-N 0.000 description 8
- VFZWCTYGZWDQGK-UHFFFAOYSA-N n-benzylhexan-1-amine Chemical group CCCCCCNCC1=CC=CC=C1 VFZWCTYGZWDQGK-UHFFFAOYSA-N 0.000 description 6
- 239000003990 capacitor Substances 0.000 description 5
- 238000005457 optimization Methods 0.000 description 5
- 230000002378 acidificating effect Effects 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 4
- 238000011221 initial treatment Methods 0.000 description 4
- FLDCSPABIQBYKP-UHFFFAOYSA-N 5-chloro-1,2-dimethylbenzimidazole Chemical compound ClC1=CC=C2N(C)C(C)=NC2=C1 FLDCSPABIQBYKP-UHFFFAOYSA-N 0.000 description 3
- 239000001741 Ammonium adipate Substances 0.000 description 3
- 235000019293 ammonium adipate Nutrition 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 238000007598 dipping method Methods 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 3
- 229910001593 boehmite Inorganic materials 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 150000004682 monohydrates Chemical class 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- VPRYEZICHXRJIW-MERQFXBCSA-N (2S)-2-[bis[(2-methylpropan-2-yl)oxycarbonyl]amino]-3-(1H-imidazol-5-yl)propanoate dicyclohexylazanium Chemical compound C1(CCCCC1)[NH2+]C1CCCCC1.C(=O)(OC(C)(C)C)N([C@@H](CC1=CNC=N1)C(=O)[O-])C(=O)OC(C)(C)C VPRYEZICHXRJIW-MERQFXBCSA-N 0.000 description 1
- 229910017089 AlO(OH) Inorganic materials 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 150000001642 boronic acid derivatives Chemical class 0.000 description 1
- 238000010835 comparative analysis Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000007739 conversion coating Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- ODCCJTMPMUFERV-UHFFFAOYSA-N ditert-butyl carbonate Chemical group CC(C)(C)OC(=O)OC(C)(C)C ODCCJTMPMUFERV-UHFFFAOYSA-N 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000006855 networking Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/05—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
- C23C22/06—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/02—Anodisation
- C25D11/04—Anodisation of aluminium or alloys based thereon
- C25D11/06—Anodisation of aluminium or alloys based thereon characterised by the electrolytes used
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/05—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
- C23C22/06—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
- C23C22/07—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/73—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals characterised by the process
- C23C22/77—Controlling or regulating of the coating process
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/78—Pretreatment of the material to be coated
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/82—After-treatment
- C23C22/83—Chemical after-treatment
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/02—Anodisation
- C25D11/04—Anodisation of aluminium or alloys based thereon
- C25D11/12—Anodising more than once, e.g. in different baths
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/02—Anodisation
- C25D11/04—Anodisation of aluminium or alloys based thereon
- C25D11/16—Pretreatment, e.g. desmutting
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/02—Anodisation
- C25D11/04—Anodisation of aluminium or alloys based thereon
- C25D11/18—After-treatment, e.g. pore-sealing
- C25D11/24—Chemical after-treatment
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/042—Electrodes or formation of dielectric layers thereon characterised by the material
- H01G9/045—Electrodes or formation of dielectric layers thereon characterised by the material based on aluminium
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/048—Electrodes or formation of dielectric layers thereon characterised by their structure
- H01G9/055—Etched foil electrodes
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/60—Other road transportation technologies with climate change mitigation effect
- Y02T10/70—Energy storage systems for electromobility, e.g. batteries
Definitions
- the invention relates to the technical field of electrode foil manufacturing, in particular to a preparation method of high specific volume and low voltage electrode foil for automotive electronics.
- multi-stage formation of corroded foil is usually used to prepare electrode foil.
- the general operation steps are: four-stage formation, one-stage formation: 7% ammonium adipate, 1% borate, temperature 70°C, time 7 minutes , after washing with water, enter the secondary formation: 5% ammonium adipate, 1% borate, temperature 70°C, time 6 minutes, third-level formation: 3% ammonium adipate, 1% borate, temperature 70°C, time 8min, after washing with water, carry out four-stage formation: 5% phosphate, temperature 70°C, time 15min, the latter one: 1% phosphate, temperature 80°C, time 12min, after washing with water, enter 7% phosphoric acid solution, time 5min, after washing High temperature (450-500°C) treatment for 1.5min, the last two: 3% phosphate, temperature 70°C, time 5min, the last three: 1% phosphate, temperature 70°C, time 5.5min, wash with water and dry.
- the preparation process route is simple and the cost is low, the capacitance and boiling life of the prepared electrode foil are low, and the defective rate remains high.
- the reason is that the aluminum oxide crystal content in the oxide film on the surface of the electrode foil is low, and a large number of defects remain on the oxide film after chemical conversion treatment. Therefore, technicians are urgently needed to solve the above problems.
- the present invention relates to a preparation method of high specific volume low voltage electrode foil for automotive electronics, which includes the following steps:
- Multi-level formation including the following sub-steps:
- First-level formation immerse the corroded foil obtained in step S1 into a mixed solution containing 5-10wt% ammonium sulfate, 1-2wt% borate, and 0.5-1wt% amine salt, controlled at a temperature of 65-85°C. The formation is carried out at a voltage of 20 to 160V, and the time is controlled between 5 and 10 minutes, to produce a first-level formation foil;
- Secondary formation Dip the primary formation foil processed in step S22 into a mixed solution containing 3-7wt% ammonium sulfate and 1-2wt% borate at a temperature controlled at 65-85°C, 20-160V The formation is carried out under voltage and the time is controlled between 5 and 10 minutes to produce a secondary formation foil;
- Step S26 Intermediate treatment: Dip the tertiary chemical foil processed in step S25 into a quaternary ammonium salt solution with a temperature controlled at 40 to 60°C and 5 to 10 wt%, and the duration is controlled at 5 to 10 minutes;
- step S27 Four-stage formation: Dip the three-stage formation foil obtained in step S26 into a solution containing 5-7wt% phosphate at a temperature controlled at 65-85°C, and perform the formation at a voltage of 20-160V, and the duration is controlled at 15-15%. 20 minutes to make a fourth-stage chemical foil;
- Step S31 First-level post-processing: Dip the fourth-level chemical foil obtained in step S27 into a phosphate aqueous solution with a temperature controlled at 65-85°C and 1-5wt%, apply a voltage of 20-160V, and control the duration at 10-15 minutes. Made into primary treated foil;
- Step S33 Pickling treatment: Dip the first-level treated foil treated in step S32 into a mixed solution containing 7 to 10 wt% phosphoric acid and oxidizing acid, and the time is controlled to 5 to 10 minutes;
- step S34 Heat treatment: perform water washing and drying operations on the first-level treated foil obtained in step S33, and the drying temperature is controlled at 450 ⁇ 500°C, and the duration is controlled at 1 ⁇ 2 min;
- Secondary post-processing Dip the primary-processed foil obtained in step S34 into a phosphate aqueous solution with a temperature controlled at 65-85°C and 1-5wt%, apply a voltage of 20-160V, and control the duration at 5-10 minutes. Made into secondary treated foil;
- step S36 Third-level post-processing: Dip the secondary-processed foil obtained in step S35 into a phosphate aqueous solution with a temperature controlled at 65 to 85°C and 1 to 5 wt%, apply a voltage of 20 to 160 V, and control the duration to 5 to 10 minutes.
- a temperature controlled at 65 to 85°C and 1 to 5 wt% a temperature controlled at 65 to 85°C and 1 to 5 wt%
- apply a voltage of 20 to 160 V and control the duration to 5 to 10 minutes.
- step S37 Surface cleaning: Wash and air-dry the three-level treated foil obtained in step S36 to obtain a high specific volume low-voltage electrode foil.
- the borate is preferably any one of borax or sodium metaborate or a mixture thereof.
- the amine salt is preferably hexylbenzylamine salt, dicyclohexylamine salt, bis-tert-butoxycarbonylhistidine dicyclohexylamine salt, dimethylamine hydrochloride, and triethanolamine , any one of piroctone ethanolamine salts or their mixtures.
- the quaternary ammonium salt is preferably any one of sodium lauryl sulfate, dodecyl trimethyl ammonium bromide, ammonium lauryl alcohol ether sulfate or their combinations. mixture.
- the phosphate is preferably any one of diammonium phosphate, sodium hexametaphosphate, disodium hydrogen phosphate or a mixture thereof.
- the preparation method of high specific volume low-voltage electrode foil for automotive electronics has achieved at least the following beneficial effects:
- a constant density of current is applied to the formation bath liquid to ensure that the oxide film is stably and rapidly formed on the surface of the corroded foil. , and the distribution shape of the formed channels in different areas is more balanced;
- the voltage, temperature, time, and composition and ratio of the formation liquid used are adjusted so that the density of each layer of the formed oxide film becomes consistent, which is beneficial to improving the boiling properties of the electrode foil. life;
- step S21 adding amine treatment liquid during the first-level formation can improve the concentration of the oxide film.
- Figure 1 is a metallographic photograph of a shaped electrode foil prepared by conventional multi-stage formation as described in the background art.
- Figure 2 is a metallographic photograph of the shaped electrode foil prepared by the method in Example 1.
- Figure 3 is a metallographic photograph of the shaped electrode foil prepared by the method in Example 2.
- Figure 4 is a metallographic photograph of the shaped electrode foil prepared by the method in Example 3.
- Figure 5 is a metallographic photograph of the shaped electrode foil prepared by the method in Example 4.
- the electrode foil is prepared with reference to the multi-stage formation method disclosed in the background art above.
- a method for preparing high specific volume low voltage electrode foil for automotive electronics which includes the following steps:
- Multi-level formation including the following sub-steps:
- First-level formation Immerse the corroded foil obtained in step S1 into a mixed solution containing 5wt% ammonium sulfate, 1wt% sodium metaborate, and 0.5wt% hexyl benzylamine salt, controlled at a temperature of 65 to 85°C, for 20 to The formation is carried out at a voltage of 160V and the time is controlled at 10 minutes to produce a first-level formation foil;
- step S22 Surface cleaning: perform water washing and air-drying operations on the primary chemical foil obtained in step S21 (the air-drying temperature does not exceed 20°C);
- Secondary formation Dip the primary formation foil processed in step S22 into a mixed solution containing 3wt% ammonium sulfate and 1wt% sodium metaborate at a temperature controlled at 65-85°C, and perform the formation at a voltage of 20-160V. , and the duration should be controlled at 10 minutes to make a secondary formation foil;
- step S24 Tertiary formation: Dip the secondary formation foil obtained in step S23 into a mixed solution containing 3wt% ammonium sulfate and 1wt% sodium metaborate at a temperature controlled at 65-85°C, and perform the formation at a voltage of 20-160V, and The time is controlled at 15 minutes to make a three-stage chemical foil;
- step S26 Intermediate treatment: Dip the tertiary chemical foil processed in step S25 into a 5wt% sodium dodecyl sulfate aqueous solution with a temperature controlled at 40-60°C, and the duration is controlled at 10 minutes;
- step S27 Four-stage formation: Dip the three-stage formation foil obtained in step S26 into a solution containing 5wt% sodium hexametaphosphate and controlled at a temperature of 65 to 85°C. The formation is carried out at a voltage of 20 to 160V, and the duration is controlled to 20 minutes. Made into quaternary formation foil;
- Step S31 First-level post-processing: Dip the fourth-level chemical foil obtained in step S27 into a 1wt% sodium hexametaphosphate aqueous solution with a temperature controlled at 65 to 85°C, apply a voltage of 20 to 160V, and control the time to 15 minutes to prepare Primary treatment foil;
- Acid dipping treatment Dip the first-level treated foil treated in step S32 into an acidic mixed solution containing 7wt% phosphoric acid:perchloric acid in a ratio of 1:1, and the duration is controlled to 6 minutes;
- step S34 Heat treatment: perform water washing and drying operations on the first-level treated foil obtained in step S33, and the drying temperature is controlled at 450 ⁇ 500°C, and the drying time is controlled at 1.5 minutes;
- Secondary post-processing Dip the primary-processed foil obtained in step S34 into a 1wt% sodium hexametaphosphate aqueous solution controlled at a temperature of 65 to 85°C, apply a voltage of 20 to 160V, and control the duration to 10 minutes to prepare secondary treatment foil;
- step S36 Third-level post-processing: Dip the secondary-processed foil obtained in step S35 into a 1wt% sodium hexametaphosphate aqueous solution with a temperature controlled at 65 to 85°C, apply a voltage of 20 to 160V, and control the duration to 10 minutes to prepare Tertiary treated foil;
- step S37 Surface cleaning: Wash and air-dry the three-level treated foil obtained in step S36 to obtain a high specific volume low-voltage electrode foil.
- a method for preparing high specific volume low voltage electrode foil for automotive electronics which includes the following steps:
- Multi-level formation including the following sub-steps:
- step S21 First-level formation: immerse the corroded foil obtained in step S1 into a mixed solution containing 8wt% ammonium sulfate, 1.5wt% sodium metaborate, and 0.7wt% hexyl benzylamine salt at a temperature of 65 to 85°C, 20 The formation is carried out at a voltage of ⁇ 160V, and the time is controlled at 10 minutes, to produce a first-level formation foil;
- step S22 Surface cleaning: perform water washing and air-drying operations on the primary chemical foil obtained in step S21 (the air-drying temperature does not exceed 20°C);
- Secondary formation Dip the primary formation foil processed in step S22 into a mixed solution containing 5wt% ammonium sulfate and 1.5wt% sodium metaborate, controlled at a temperature of 65 to 85°C, and carried out at a voltage of 20 to 160V. Formation, and the time should be controlled within 10 minutes, to produce a secondary formation foil;
- step S24 Tertiary formation: Dip the secondary formation foil obtained in step S23 into a mixed solution containing 4wt% ammonium sulfate and 1.5wt% sodium metaborate at a temperature controlled at 65-85°C, and perform the formation at a voltage of 20-160V. And the time is controlled at 15 minutes to make a three-stage chemical foil;
- step S26 Intermediate treatment: Dip the tertiary chemical foil processed in step S25 into an 8wt% sodium dodecyl sulfate aqueous solution with a temperature controlled at 40-60°C, and the duration is controlled at 10 minutes;
- step S27 Four-stage formation: Dip the three-stage formation foil obtained in step S26 into a solution containing 6wt% sodium hexametaphosphate at a temperature controlled at 65-85°C, and perform the formation at a voltage of 20-160V, and the duration is controlled at 20 minutes.
- a solution containing 6wt% sodium hexametaphosphate at a temperature controlled at 65-85°C and perform the formation at a voltage of 20-160V, and the duration is controlled at 20 minutes.
- Step S31 First-level post-processing: Dip the fourth-level chemical foil obtained in step S27 into a 3wt% sodium hexametaphosphate aqueous solution with a temperature controlled at 65 to 85°C, apply a voltage of 20 to 160V, and control the time to 15 minutes to prepare Primary treatment foil;
- step S33 Pickling treatment: Dip the first-level treated foil treated in step S32 into an acidic mixed solution containing 8wt% phosphoric acid:perchloric acid in a ratio of 1:1, and the time is controlled to 6 minutes;
- step S34 Heat treatment: perform water washing and drying operations on the first-level treated foil obtained in step S33, and the drying temperature is controlled at 450 ⁇ 500°C, and the drying time is controlled at 1.5 minutes;
- Secondary post-processing Dip the primary-processed foil obtained in step S34 into a 3wt% sodium hexametaphosphate aqueous solution with a temperature controlled at 65 to 85°C, apply a voltage of 20 to 160V, and control the duration to 10 minutes to prepare secondary treatment foil;
- step S36 Third-level post-processing: Dip the secondary-processed foil obtained in step S35 into a 3wt% sodium hexametaphosphate aqueous solution with a temperature controlled at 65 to 85°C, apply a voltage of 20 to 160V, and control the duration to 10 minutes to prepare Tertiary treated foil;
- step S37 Surface cleaning: Wash and air-dry the three-level treated foil obtained in step S36 to obtain a high specific volume low-voltage electrode foil.
- a method for preparing high specific volume low voltage electrode foil for automotive electronics which includes the following steps:
- Multi-level formation including the following sub-steps:
- step S21 First-level formation: immerse the corroded foil obtained in step S1 into a mixed solution containing 10wt% ammonium sulfate, 2wt% sodium metaborate, and 1wt% hexyl benzylamine salt at a temperature of 65 to 85°C, 20 to 160V Carry out formation under voltage and control the time to 10 minutes to make a first-level formation foil;
- step S22 Surface cleaning: perform water washing and air-drying operations on the primary chemical foil obtained in step S21 (the air-drying temperature does not exceed 20°C);
- Secondary formation Dip the primary formation foil processed in step S22 into a mixed solution containing 7wt% ammonium sulfate and 2wt% sodium metaborate at a temperature controlled at 65-85°C, and perform the formation at a voltage of 20-160V. , and the duration should be controlled at 10 minutes to make a secondary formation foil;
- step S26 Intermediate treatment: Dip the tertiary chemical foil processed in step S25 into a 10wt% sodium dodecyl sulfate aqueous solution with a temperature controlled at 40-60°C, and the duration is controlled at 10 minutes;
- step S27 Four-stage formation: Dip the three-stage formation foil obtained in step S26 into a solution containing 7wt% sodium hexametaphosphate at a temperature controlled at 65-85°C, and perform the formation at a voltage of 20-160V, and the duration is controlled at 20 minutes.
- a solution containing 7wt% sodium hexametaphosphate at a temperature controlled at 65-85°C and perform the formation at a voltage of 20-160V, and the duration is controlled at 20 minutes.
- Step S31 First-level post-processing: Dip the fourth-level chemical foil obtained in step S27 into a 5wt% sodium hexametaphosphate aqueous solution with a temperature controlled at 65 to 85°C, apply a voltage of 20 to 160V, and control the time to 15 minutes to prepare Primary treatment foil;
- Acid dipping treatment Dip the first-level treated foil treated in step S32 into an acidic mixed solution containing 10wt% phosphoric acid: perchloric acid in a ratio of 1:1, and the duration is controlled to 6 minutes;
- step S34 Heat treatment: perform water washing and drying operations on the first-level treated foil obtained in step S33, and the drying temperature is controlled at 450 ⁇ 500°C, and the drying time is controlled at 1.5 minutes;
- Secondary post-processing Dip the primary-processed foil obtained in step S34 into a 5wt% sodium hexametaphosphate aqueous solution with a temperature controlled at 65 to 85°C, apply a voltage of 20 to 160V, and control the duration to 10 minutes to prepare secondary treatment foil;
- step S36 Third-level post-processing: Dip the secondary-processed foil obtained in step S35 into a 5wt% sodium hexametaphosphate aqueous solution with a temperature controlled at 65 to 85°C, apply a voltage of 20 to 160V, and control the duration to 10 minutes to prepare Tertiary treated foil;
- step S37 Surface cleaning: Wash and air-dry the three-level treated foil obtained in step S36 to obtain a high specific volume low-voltage electrode foil.
- a method for preparing high specific volume low voltage electrode foil for automotive electronics which includes the following steps:
- Multi-level synthesis including the following sub-steps:
- First-level formation Immerse the corroded foil obtained in step S1 into a mixed solution containing 5wt% ammonium sulfate, 1wt% sodium metaborate, and 0.5wt% hexyl benzylamine salt, controlled at a temperature of 65 to 85°C, for 20 to The formation is carried out at a voltage of 160V and the time is controlled at 5 minutes to produce a first-level formation foil;
- step S22 Surface cleaning: perform water washing and air-drying operations on the primary chemical foil obtained in step S21 (the air-drying temperature does not exceed 20°C);
- Secondary formation Dip the primary formation foil processed in step S22 into a mixed solution containing 3wt% ammonium sulfate and 1wt% sodium metaborate at a temperature controlled at 65-85°C, and perform the formation at a voltage of 20-160V. , and the time should be controlled at 5 minutes to make a secondary formation foil;
- step S24 Tertiary formation: Dip the secondary formation foil obtained in step S23 into a mixed solution containing 3wt% ammonium sulfate and 1wt% sodium metaborate at a temperature controlled at 65-85°C, and perform the formation at a voltage of 20-160V, and The time is controlled at 7 minutes to produce a three-stage chemical foil;
- step S26 Intermediate treatment: Dip the tertiary chemical foil processed in step S25 into a 5wt% sodium dodecyl sulfate aqueous solution with a temperature controlled at 40-60°C, and the duration is controlled at 10 minutes;
- step S27 Four-stage formation: Dip the three-stage formation foil obtained in step S26 into a solution containing 5wt% sodium hexametaphosphate at a temperature controlled at 65-85°C, and perform the formation at a voltage of 20-160V, and the duration is controlled at 15 minutes.
- a solution containing 5wt% sodium hexametaphosphate at a temperature controlled at 65-85°C and perform the formation at a voltage of 20-160V, and the duration is controlled at 15 minutes.
- Step S31 First-level post-processing: Dip the fourth-level chemical foil obtained in step S27 into a 1wt% sodium hexametaphosphate aqueous solution with a temperature controlled at 65 to 85°C, apply a voltage of 20 to 160V, and control the time to 10 minutes to prepare Primary treatment foil;
- Acid dipping treatment Dip the first-level treated foil treated in step S32 into an acidic mixed solution containing 7wt% phosphoric acid:perchloric acid in a ratio of 1:1, and the duration is controlled to 6 minutes;
- step S34 Heat treatment: perform water washing and drying operations on the first-level treated foil obtained in step S33, and the drying temperature is controlled at 450 ⁇ 500°C, and the drying time is controlled at 1.5 minutes;
- Secondary post-processing Dip the primary-processed foil obtained in step S34 into a 1wt% sodium hexametaphosphate aqueous solution with a temperature controlled at 65 to 85°C, apply a voltage of 20 to 160V, and control the duration to 5 minutes to prepare secondary treatment foil;
- step S36 Third-level post-processing: Dip the secondary-processed foil obtained in step S35 into a 1wt% sodium hexametaphosphate aqueous solution controlled at a temperature of 65 to 85°C, apply a voltage of 20 to 160V, and control the duration to 5 minutes to prepare Tertiary treated foil;
- step S37 Surface cleaning: Wash and air-dry the three-level treated foil obtained in step S36 to obtain a high specific volume low-voltage electrode foil.
- Table 1 is a summary of the performance test results of the electrode foils obtained in Comparative Examples and Examples 1 to 4.
- Vfe the final voltage applied during the forming process of the unformed foil
- a constant density of current is applied to the formation bath liquid to ensure that the oxide film is stably and rapidly formed on the surface of the corroded foil. , and the distribution shape of the formed channels in different areas is more balanced;
- the voltage, temperature, time, and composition and ratio of the formation liquid used are adjusted so that the density of each layer of the formed oxide film becomes consistent, which is beneficial to improving the boiling properties of the electrode foil. life;
- step S21 adding amine treatment liquid during the first-level formation can improve the concentration of the oxide film.
- defects formed on the oxide film during chemical formation can be effectively and fully repaired, and can also be significantly improved. Improve the specific capacitance of aluminum electrode foil.
- the cathode Due to the presence of strong oxidizing acid, the cathode is
- borates such as borax and a mixture of sodium metaborate and borax can also be selected according to the actual situation;
- dicyclohexylamine salt or dicyclohexylamine salt or di-tert-butoxycarbonyl histidine dicyclohexylamine can also be selected according to the actual situation.
- Any one of amine salts such as dimethylamine hydrochloride, triethanolamine, piroctone ethanolamine salt, or mixtures thereof;
- dodecyltrimethylammonium bromide and lauryl alcohol ether can also be selected according to the actual situation. Any one of quaternary ammonium salts such as ammonium sulfate or their mixture;
- any one of the phosphates such as diammonium phosphate, disodium hydrogen phosphate or the like can also be selected according to the actual situation. Their mixture.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Electrochemistry (AREA)
- Power Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Chemical Treatment Of Metals (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Abstract
La présente invention concerne un procédé de préparation d'une feuille d'électrode basse tension de volume spécifique élevé pour l'électronique d'automobile. Le procédé comprend les étapes suivantes consistant à : tout d'abord, réaliser séquentiellement des opérations de formation de premier étage, de formation de deuxième étage, de formation de troisième étage et de formation quatrième étage sur une feuille de gravure, et ajuster respectivement la tension, la température, le temps et les composants et la proportion du liquide de formation utilisé pendant la réalisation d'une formation unique ; ajouter une solution de traitement d'amine pendant la formation du premier étage pour augmenter considérablement la teneur en cristaux d'oxyde d'aluminium dans un film d'oxyde formé ; puis tremper la feuille formée dans une solution de phosphate de multiples fois pour effectuer une opération de post-traitement de façon à réparer des points défectueux résiduels sur le film d'oxyde formé. De cette manière, non seulement la durée de vie à l'ébullition d'une feuille d'électrode peut être efficacement prolongée, mais une bonne base est également posée pour améliorer considérablement le volume spécifique électrique d'une feuille d'électrode en aluminium.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020237034833A KR20240009387A (ko) | 2022-06-07 | 2023-02-10 | 자동차 전자용 고비용량 저전압 전극 포일의 제조 방법 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210632100.0 | 2022-06-07 | ||
CN202210632100.0A CN114703526B (zh) | 2022-06-07 | 2022-06-07 | 一种汽车电子用高比容低压电极箔的制备方法 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2023236573A1 true WO2023236573A1 (fr) | 2023-12-14 |
Family
ID=82177640
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CN2023/075328 WO2023236573A1 (fr) | 2022-06-07 | 2023-02-10 | Procédé de préparation de feuille d'électrode basse tension de volume spécifique élevé pour électronique d'automobile |
Country Status (3)
Country | Link |
---|---|
KR (1) | KR20240009387A (fr) |
CN (1) | CN114703526B (fr) |
WO (1) | WO2023236573A1 (fr) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114703526B (zh) * | 2022-06-07 | 2022-11-01 | 南通海星电子股份有限公司 | 一种汽车电子用高比容低压电极箔的制备方法 |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006098445A1 (fr) * | 2005-03-17 | 2006-09-21 | Showa Denko K.K. | Procede pour produire un materiau en aluminium pour une electrode de condensateur electrolytique, ledit materiau, procede pour produire un materiau d’electrode de condensateur electrolytique, materiau d’anode pour un condensateur electrolytique en aluminium et condensateur electrolytique en aluminium |
CN1967752A (zh) * | 2006-11-06 | 2007-05-23 | 乳源瑶族自治县东阳光化成箔有限公司 | 一种铝电解电容器用低压阳极箔及其制造方法 |
CN101093751A (zh) * | 2006-11-17 | 2007-12-26 | 深圳清华大学研究院 | 高比容阴极箔的制备方法 |
CN101651049A (zh) * | 2009-06-24 | 2010-02-17 | 吴江飞乐天和电子材料有限公司 | 一种提高低压铝电解电容器电极箔比容的方法 |
US20100219079A1 (en) * | 2006-05-07 | 2010-09-02 | Synkera Technologies, Inc. | Methods for making membranes based on anodic aluminum oxide structures |
CN105097286A (zh) * | 2015-09-01 | 2015-11-25 | 广西贺州市桂东电子科技有限责任公司 | 一种超高压储能材料的腐蚀方法 |
CN108511195A (zh) * | 2018-03-19 | 2018-09-07 | 南通海星电子股份有限公司 | 一种提高中高压电极箔氧化膜质量的后处理方法 |
CN110760913A (zh) * | 2019-09-30 | 2020-02-07 | 东莞东阳光科研发有限公司 | 化成液、低压化成箔及其制备方法 |
CN111139508A (zh) * | 2019-01-23 | 2020-05-12 | 东莞东阳光科研发有限公司 | 化成液、化成方法及阳极箔 |
CN114007726A (zh) * | 2019-06-17 | 2022-02-01 | 纳诺佩克有限公司 | 用于医疗保健和生物技术的纳米多孔阳极氧化铝隔膜 |
CN114411157A (zh) * | 2021-12-31 | 2022-04-29 | 乳源县立东电子科技有限公司 | 一种铝箔残留氯离子的清洗方法及其应用 |
CN114703526A (zh) * | 2022-06-07 | 2022-07-05 | 南通海星电子股份有限公司 | 一种汽车电子用高比容低压电极箔的制备方法 |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008091358A (ja) * | 2006-09-29 | 2008-04-17 | Nichicon Corp | 固体電解コンデンサおよびその製造方法 |
CN101593628A (zh) * | 2008-05-26 | 2009-12-02 | 南通海一电子有限公司 | 低压用铝电解电容器电极箔的五级制造方法 |
CN101425383B (zh) * | 2008-07-24 | 2011-04-20 | 东莞市东阳光电容器有限公司 | 一种低压高介电铝电解电容器用化成箔的制造方法 |
CN109402700A (zh) * | 2018-11-01 | 2019-03-01 | 青海瑞合铝箔有限公司 | 一种改进的化成箔制造工艺 |
CN110016702B (zh) * | 2019-04-18 | 2020-12-11 | 内蒙古乌兰察布东阳光化成箔有限公司 | 一种铝电解电容器用超高压化成箔化成工艺 |
CN110055571B (zh) * | 2019-04-18 | 2020-05-22 | 宜都东阳光化成箔有限公司 | 一种提高铝电解电容器用中高压化成箔容量的预处理溶液及化成工艺 |
CN110219032B (zh) * | 2019-06-20 | 2020-10-13 | 新疆众和股份有限公司 | 一种超高电压铝电解电容器阳极箔的化成方法 |
CN113897651A (zh) * | 2021-08-23 | 2022-01-07 | 南通南辉电子材料股份有限公司 | 宽温、低阻抗、缩体、耐大纹波电流、长寿命的铝电解电容器用电极箔的制造方法 |
CN113862750A (zh) * | 2021-08-23 | 2021-12-31 | 南通南辉电子材料股份有限公司 | 电动汽车专用电容器用电极箔的制造方法 |
-
2022
- 2022-06-07 CN CN202210632100.0A patent/CN114703526B/zh active Active
-
2023
- 2023-02-10 KR KR1020237034833A patent/KR20240009387A/ko unknown
- 2023-02-10 WO PCT/CN2023/075328 patent/WO2023236573A1/fr unknown
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006098445A1 (fr) * | 2005-03-17 | 2006-09-21 | Showa Denko K.K. | Procede pour produire un materiau en aluminium pour une electrode de condensateur electrolytique, ledit materiau, procede pour produire un materiau d’electrode de condensateur electrolytique, materiau d’anode pour un condensateur electrolytique en aluminium et condensateur electrolytique en aluminium |
US20100219079A1 (en) * | 2006-05-07 | 2010-09-02 | Synkera Technologies, Inc. | Methods for making membranes based on anodic aluminum oxide structures |
CN1967752A (zh) * | 2006-11-06 | 2007-05-23 | 乳源瑶族自治县东阳光化成箔有限公司 | 一种铝电解电容器用低压阳极箔及其制造方法 |
CN101093751A (zh) * | 2006-11-17 | 2007-12-26 | 深圳清华大学研究院 | 高比容阴极箔的制备方法 |
CN101651049A (zh) * | 2009-06-24 | 2010-02-17 | 吴江飞乐天和电子材料有限公司 | 一种提高低压铝电解电容器电极箔比容的方法 |
CN105097286A (zh) * | 2015-09-01 | 2015-11-25 | 广西贺州市桂东电子科技有限责任公司 | 一种超高压储能材料的腐蚀方法 |
CN108511195A (zh) * | 2018-03-19 | 2018-09-07 | 南通海星电子股份有限公司 | 一种提高中高压电极箔氧化膜质量的后处理方法 |
CN111139508A (zh) * | 2019-01-23 | 2020-05-12 | 东莞东阳光科研发有限公司 | 化成液、化成方法及阳极箔 |
CN114007726A (zh) * | 2019-06-17 | 2022-02-01 | 纳诺佩克有限公司 | 用于医疗保健和生物技术的纳米多孔阳极氧化铝隔膜 |
CN110760913A (zh) * | 2019-09-30 | 2020-02-07 | 东莞东阳光科研发有限公司 | 化成液、低压化成箔及其制备方法 |
CN114411157A (zh) * | 2021-12-31 | 2022-04-29 | 乳源县立东电子科技有限公司 | 一种铝箔残留氯离子的清洗方法及其应用 |
CN114703526A (zh) * | 2022-06-07 | 2022-07-05 | 南通海星电子股份有限公司 | 一种汽车电子用高比容低压电极箔的制备方法 |
Also Published As
Publication number | Publication date |
---|---|
CN114703526A (zh) | 2022-07-05 |
KR20240009387A (ko) | 2024-01-22 |
CN114703526B (zh) | 2022-11-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2023236573A1 (fr) | Procédé de préparation de feuille d'électrode basse tension de volume spécifique élevé pour électronique d'automobile | |
CN110055571B (zh) | 一种提高铝电解电容器用中高压化成箔容量的预处理溶液及化成工艺 | |
CN109609991B (zh) | 化成箔、制备方法及其应用 | |
CN108456916B (zh) | 一种中高压电子铝箔的腐蚀方法 | |
KR102598338B1 (ko) | 자동차 전자용 나노 미세다공성 구조 알루미늄 전극박의 제조 방법 | |
CN112117129B (zh) | 一种高压高容低缺陷阳极箔的混酸化成工艺 | |
CN113502476B (zh) | 一种固态铝电解电容器用电极箔的制造方法 | |
CN101017735A (zh) | 阳极元件、制造该阳极元件的方法和固体电解质电容器 | |
CN109378218B (zh) | 一种高稳定性低压用铝电解电容器化成箔的制造方法 | |
CN100472680C (zh) | 固体电解电容器阴极制造方法 | |
KR20200066603A (ko) | 표면 실장 알루미늄 전해 커패시터용 전극박의 제조 방법 | |
WO2024027122A1 (fr) | Procédé de préparation d'une feuille frittée de poudre composite hautement diélectrique | |
CN109554746B (zh) | 一种高压高比容腐蚀箔的制造方法 | |
CN113436891A (zh) | 一种采用阳极氧化后的纳米凹坑来诱导中高压阳极箔均匀腐蚀发孔的方法 | |
CN111225997A (zh) | 铝箔及电极用铝部件 | |
JPH09275040A (ja) | 中高圧アルミニウム電解コンデンサ用電極箔の化成方法 | |
CN113862750A (zh) | 电动汽车专用电容器用电极箔的制造方法 | |
JP2000003835A (ja) | アルミニウム電解コンデンサ用電極箔の製造方法 | |
CN113322454A (zh) | 一种低压化成箔的化成方法及制得的低压化成箔 | |
JP6675996B2 (ja) | アルミニウム電解コンデンサ用電極の製造方法 | |
JPWO2004112065A1 (ja) | 電解コンデンサ電極用アルミニウム材の製造方法、電解コンデンサ電極用アルミニウム材、電解コンデンサ用電極材の製造方法およびアルミニウム電解コンデンサ | |
TWI443696B (zh) | 鋁電極之製造方法、其製備之鋁電極以及含該鋁電極之鋁電容器 | |
WO2003009321A1 (fr) | Feuille aluminium pour condensateur electrolytique | |
JP4308556B2 (ja) | 電解コンデンサ電極用アルミニウム材および電解コンデンサ電極材の製造方法並びに電解コンデンサ | |
JP3460418B2 (ja) | アルミ電解コンデンサ用電極箔の製造方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 23818741 Country of ref document: EP Kind code of ref document: A1 |