CN101707141A - Method for manufacturing anodic foil of aluminum electrolytic capacitor - Google Patents
Method for manufacturing anodic foil of aluminum electrolytic capacitor Download PDFInfo
- Publication number
- CN101707141A CN101707141A CN200910114537A CN200910114537A CN101707141A CN 101707141 A CN101707141 A CN 101707141A CN 200910114537 A CN200910114537 A CN 200910114537A CN 200910114537 A CN200910114537 A CN 200910114537A CN 101707141 A CN101707141 A CN 101707141A
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- Prior art keywords
- treatment
- heat treatment
- phosphate
- change
- electrolytic capacitor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000011888 foil Substances 0.000 title claims abstract description 25
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 14
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 14
- 239000003990 capacitor Substances 0.000 title claims abstract description 14
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 13
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 12
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 4
- 238000005755 formation reaction Methods 0.000 claims abstract description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 28
- 238000000034 method Methods 0.000 claims description 21
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 14
- 238000005868 electrolysis reaction Methods 0.000 claims description 10
- NBIIXXVUZAFLBC-UHFFFAOYSA-L phosphate Chemical compound OP([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-L 0.000 claims description 9
- ABLZXFCXXLZCGV-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)=O ABLZXFCXXLZCGV-UHFFFAOYSA-N 0.000 claims description 7
- 238000005470 impregnation Methods 0.000 claims description 6
- LFVGISIMTYGQHF-UHFFFAOYSA-N Ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 claims description 3
- 229910000387 ammonium dihydrogen phosphate Inorganic materials 0.000 claims description 3
- 235000019837 monoammonium phosphate Nutrition 0.000 claims description 3
- 230000002378 acidificating Effects 0.000 claims description 2
- ZRDXIILBYDTYOA-UHFFFAOYSA-N azane;phosphonous acid Chemical compound N.OPO ZRDXIILBYDTYOA-UHFFFAOYSA-N 0.000 claims description 2
- 238000005452 bending Methods 0.000 abstract description 14
- 238000003860 storage Methods 0.000 abstract description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-K [O-]P([O-])([O-])=O Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 abstract 4
- 239000010452 phosphate Substances 0.000 abstract 4
- 238000009835 boiling Methods 0.000 abstract 1
- 238000007598 dipping method Methods 0.000 abstract 1
- 230000036571 hydration Effects 0.000 abstract 1
- 238000006703 hydration reaction Methods 0.000 abstract 1
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 24
- 230000000630 rising Effects 0.000 description 20
- 239000007788 liquid Substances 0.000 description 16
- 150000002148 esters Chemical class 0.000 description 12
- 238000005516 engineering process Methods 0.000 description 9
- BDJRBEYXGGNYIS-UHFFFAOYSA-N Azelaic acid Chemical compound OC(=O)CCCCCCCC(O)=O BDJRBEYXGGNYIS-UHFFFAOYSA-N 0.000 description 5
- 238000003786 synthesis reaction Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- KGBXLFKZBHKPEV-UHFFFAOYSA-N Boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002194 synthesizing Effects 0.000 description 1
Abstract
The invention discloses a method for manufacturing an anodic foil of an aluminum electrolytic capacitor, which comprises the following steps of boiling treatment, three polarization, heat treatment, formation, phosphate treatment, formation, heat treatment, and reformation. Different from the prior art, the phosphate treatment is carried out before the second heat treatment, and an after-treatment is removed. The phosphate treatment is dipping treatment performed under the conditions of the concentration of a phosphate treating agent of between 1 and 5 v/v%, and the temperature of between 20 and 80 DEG C for 1 to 10 minutes. The method can ensure that after three months of storage, the anodic foil of the aluminum electrolytic capacitor has short boosting time, short hydration resistance boosting time, stable pressure resistance and good bending performance.
Description
Technical field
The invention belongs to electronic material manufacturing technology field, be specifically related to a kind of manufacture method of aluminum electrolysis capacitor anode foil.
Background technology
At present, the manufacture method of aluminium electrolytic capacitor high-voltage anode paper tinsel, comprise boil processing, then carry out three grades change into, heat treatment, change into, phosphoric acid is handled, change into, heat treatment, change into and postprocessing working procedures again.Product bending intensity difference, water-fast long, storage fast, poach rear oxidation film withstand voltage decline of rise pressure rising time after 3 months pressure rising time, the unstable product quality of closing of using this kind chemical synthesizing method to be produced.
Summary of the invention
The objective of the invention is to overcome the deficiencies in the prior art, provide a kind of and can improve aluminum electrolysis capacitor anode foil bending intensity, water-fast manufacture method of closing the aluminum electrolysis capacitor anode foil that pressure rising time is short, storage rise pressure rising time is slow, poach rear oxidation film withstand voltage is stable.
The present invention achieves the above object by the following technical programs: a kind of manufacture method of aluminum electrolysis capacitor anode foil, comprise boil that processing, three is polarized to, heat treatment, change into, phosphoric acid is handled, change into, heat treatment, formation process again, before second heat treatment step, carry out phosphatization and handle, remove postprocessing working procedures simultaneously; It is to be 1～5v/v% in phosphate inorganic agent concentration that described phosphatization is handled, and temperature is impregnation process 1～10min under 20～80 ℃ the condition.
The phosphorous acidic group inorganic agent that described phosphatization processing is adopted is one or more in phosphoric acid, ammonium dihydrogen phosphate, phosphorous acid, the ammonium hypophosphite.
Method step and controlled condition that the present invention is concrete are:
Employing purity is that the middle and high pressure etched foil more than 99.99% boils processing 5～15min in the pure water more than 95 ℃, then carrying out the one-level constant voltage in the liquid changing into of citric acid and its esters changes into 10～20min, then carrying out the secondary constant voltage in the liquid changing into of citric acid and its esters changes into 10～20min, and then carry out three grades of constant voltages in the liquid changing into of azelaic acid and its esters and change into 20～40min, under 400～550 ℃ of conditions, heat-treat 1～5min; Change into constant voltage 10～20min again; In phosphoric acid liquid concentration is that 1.0～10v/v%, temperature are to carry out phosphoric acid under 60～80 ℃ the condition to handle 5～15min; Be 1～5v/v% in phosphate inorganic agent concentration then, temperature is to carry out impregnation process 1～10min, 80～400 ℃ of heat treatments, time 1～5min under 20～80 ℃ the condition.
The present invention compared with prior art has following advantage:
Because carrying out phosphatization before second heat treatment step handles, anode foils water-fast closed pressure rising time Tr60 and shortened 10～20s, bending intensity has improved 15～50 times, store that variable quantity pressure rising time of anode foils oxide-film has shortened 5～85s after 3 months, the oxide-film withstand voltage does not descend before and after the aquation 1h, has effectively improved the product quality of aluminum electrolysis capacitor anode foil; Production procedure is simple.
Description of drawings
Fig. 1 is the chemical synthesis technology flow chart of the manufacture method of aluminum electrolysis capacitor anode foil of the present invention.
Embodiment
Below in conjunction with specific embodiment technical scheme of the present invention is described in further detail, but embodiments of the present invention are not limited thereto.
Embodiment 1
Employing purity is that the middle pressure etched foil more than 99.99% boils processing 5min in 96 ℃ pure water, and then carrying out one-level constant voltage 130V in the liquid changing into of citric acid and its esters changes into 10min; Then carrying out secondary constant voltage 280V in the liquid changing into of citric acid and its esters changes into 10min; And then carry out three grades of constant voltage 315V in the liquid changing into of azelaic acid and its esters and change into 20min; Under 400 ℃ of conditions, heat-treat 1min; Change into constant voltage 315V again and change into 10min; In 1v/v%, temperature are 80 ℃ phosphoric acid liquid, carry out phosphoric acid and handle 5min; It is to be 5v/v% in phosphate inorganic agent concentration that phosphatization is handled, and temperature is impregnation process 1min under 80 ℃ the condition, and described phosphate inorganic agent is a phosphoric acid.Heat treatment temperature is 400 ℃ for the second time, time 1min.
Variation delta Tr (Tr pressure rising time of test storage anode foils oxide-film after 3 months
(3 months)-Tr
(initially)), the withstand voltage variation delta TV (TV of oxide-film before and after the aquation 1h
(behind the 1h)-TV
(before the 1h)), water-fast Tr60 pressure rising time, the bending intensity of closing, compare with existing chemical synthesis technology, the result is as shown in table 1:
Table 1
| Technology | ??ΔTr(s) | ??ΔTV(v) | ??Tr60 | Bending intensity (returning) |
| Existing technological process A | ??30 | ??-2 | ??20 | ??120 |
| Existing process flow B | ??50 | ??-4 | ??20 | ??140 |
| Embodiment 1 | ??5 | ??+1 | ??10 | ??160 |
Table 1 shows: middle pressure 315Vf product, to store after 3 months, and rise pressure rising time value has reduced by 25～45s; The oxide-film withstand voltage does not descend before and after the aquation 1h; The water-fast pressure rising time Tr60 of closing has shortened 10s; The existing technological process of the bending strength ratio of embodiment has improved 20～40 times.
Embodiment 2
Employing purity is that the high pressure etched foil more than 99.99% boils processing 10min in 96 ℃ pure water, and then carrying out one-level constant voltage 200V in the liquid changing into of citric acid and its esters changes into 15min; Then carrying out secondary constant voltage 400 in the liquid changing into of citric acid and its esters changes into 15min; And then carry out three grades of constant voltage 530V in the liquid and change into 30min containing changing into of azelaic acid and its esters; Under 500 ℃ of conditions, heat-treat 3min; Change into constant voltage 530V again and change into 15min; In 6v/v%, temperature are 70 ℃ phosphoric acid liquid, carry out phosphoric acid and handle 10min; It is to be 2v/v% in phosphate inorganic agent concentration that phosphatization is handled, and temperature is impregnation process 5min under 60 ℃ the condition, and described phosphate inorganic agent is a phosphorous acid.Ammonium dihydrogen solution and 85% phosphorous acid.Heat treatment temperature is 300 ℃ for the second time, time 3min.
Variation delta Tr (Tr pressure rising time of test storage anode foils oxide-film after 3 months
(3 months)-Tr
(initially)), the withstand voltage variation delta TV (TV of oxide-film before and after the aquation 1h
(behind the 1h)-TV
(before the 1h)), water-fast Tr60 pressure rising time, the bending intensity of closing, compare with existing chemical synthesis technology, the result is as shown in table 2:
Table 2
| Technology | ??ΔTr(s) | ??ΔTV(v) | ??Tr60 | Bending intensity (returning) |
| Existing technological process A | ??20 | ??-2 | ??28 | ??100 |
| Existing process flow B | ??60 | ??-5 | ??25 | ??120 |
| Embodiment 2 | ??10 | ??+1 | ??12 | ??140 |
Table 2 is the result show: to high pressure 530Vf product, store after 3 months, rise pressure rising time value has reduced by 10～50s; The oxide-film withstand voltage does not descend before and after the aquation 1h; The water-fast pressure rising time Tr60 of closing has shortened 13～16s; The existing technological process of the bending strength ratio of embodiment has improved 20～40 times.
Embodiment 3
Employing purity is that the high pressure etched foil more than 99.99% boils processing 15min in 96 ℃ pure water, and then carrying out one-level constant voltage 250V in the liquid changing into of citric acid and its esters changes into 20min; Then carrying out secondary constant voltage 480 in the liquid changing into of citric acid and its esters changes into 20min; And then carry out three grades of constant voltage 590V in the liquid changing into of azelaic acid and its esters and change into 40min; Under 550 ℃ of conditions, heat-treat 5min; Change into constant voltage 590V again and change into 20min; In 10v/v%, temperature are 60 ℃ phosphoric acid liquid, carry out phosphoric acid and handle 15min; It is to be 1v/v% in phosphate inorganic agent concentration that phosphatization is handled, and temperature is impregnation process 10min under 20 ℃ the condition, and described phosphate inorganic agent is 50wt% ammonium dihydrogen phosphate and 50wt% ortho phosphorous acid ammonium salt solution.Heat treatment temperature is 80 ℃ for the second time, time 5min.
Variation delta Tr (Tr pressure rising time of test storage anode foils oxide-film after 3 months
(3 months)-Tr
(initially)), the withstand voltage variation delta TV (TV of oxide-film before and after the aquation 1h
(behind the 1h)-TV
(before the 1h)), water-fast Tr60 pressure rising time, the bending intensity of closing, compare with existing chemical synthesis technology, the result is as shown in table 3:
Table 3
| Technology | ??ΔTr(s) | ??ΔTV(v) | ??Tr60 | Bending intensity (returning) |
| Existing technological process A | ??20 | ??-2 | ??35 | ??80 |
| Existing process flow B | ??100 | ??-6 | ??25 | ??115 |
| Embodiment 3 | ??15 | ??+2 | ??15 | ??130 |
The result finds out from table 3: high pressure 590Vf product, to store after 3 months, and rise pressure rising time value has reduced by 5～85s; The oxide-film withstand voltage does not descend before and after the aquation 1h; The water-fast pressure rising time Tr60 of closing has shortened 10～20s; The existing technological process of the bending strength ratio of embodiment has improved 15～50 times.
From table 1,2,3 as can be seen, with existing boric acid system or azelaic acid is that treatment process is compared, after oxide-film of the present invention is handled through phosphatization, the bending intensity of anode foils has improved 15～50 times, store that variable quantity pressure rising time of anode foils oxide-film has shortened 5～85s after 3 months, the oxide-film withstand voltage does not descend before and after the aquation 1h, the water-fast pressure rising time Tr60 of closing has shortened 10～20s, shows that the anode foils performance that the manufacture method of aluminum electrolysis capacitor anode foil of the present invention is produced effectively improves.
Claims (2)
1. the manufacture method of an aluminum electrolysis capacitor anode foil, comprise boil that processing, three is polarized to, heat treatment, change into, phosphoric acid is handled, change into, heat treatment, formation process again, it is characterized in that, carrying out phosphatization before second heat treatment step handles, it is to be 1～5v/v% in phosphate inorganic agent concentration that described phosphatization is handled, and temperature is impregnation process 1～10min under 20～80 ℃ the condition.
2. the manufacture method of aluminum electrolysis capacitor anode foil according to claim 1 is characterized in that, the phosphorous acidic group inorganic agent that described phosphatization processing is adopted is one or more in phosphoric acid, phosphorous acid, ammonium dihydrogen phosphate, the ammonium hypophosphite.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910114537A CN101707141A (en) | 2009-11-09 | 2009-11-09 | Method for manufacturing anodic foil of aluminum electrolytic capacitor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910114537A CN101707141A (en) | 2009-11-09 | 2009-11-09 | Method for manufacturing anodic foil of aluminum electrolytic capacitor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101707141A true CN101707141A (en) | 2010-05-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200910114537A Pending CN101707141A (en) | 2009-11-09 | 2009-11-09 | Method for manufacturing anodic foil of aluminum electrolytic capacitor |
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| CN103160902A (en) * | 2012-12-13 | 2013-06-19 | 宝兴县剑锋制箔电子有限公司 | Middle-high voltage electrode foil five-section formation two-stage liquid feed production method |
| CN103741187A (en) * | 2014-01-06 | 2014-04-23 | 广西贺州市桂东电子科技有限责任公司 | Power supply solution for formation of electronic aluminum foil at middle-high voltage and application method thereof |
| CN103779098A (en) * | 2014-01-06 | 2014-05-07 | 广西贺州市桂东电子科技有限责任公司 | Formation method of energy storage material applied to alternating current motor start capacitor |
| CN106252081A (en) * | 2016-08-11 | 2016-12-21 | 四川立业电子有限公司 | A kind of anodizing composite dielectric film and preparation method thereof |
| CN107967996A (en) * | 2017-11-15 | 2018-04-27 | 广西贺州市桂东电子科技有限责任公司 | A kind of chemical synthesizing method of mash welder capacitor anode foils |
| CN107974701A (en) * | 2017-11-15 | 2018-05-01 | 广西贺州市桂东电子科技有限责任公司 | A kind of pre-treating method of anode aluminium foil chemical conversion |
| CN108376611A (en) * | 2017-12-29 | 2018-08-07 | 广西贺州市桂东电子科技有限责任公司 | A kind of production method of no foil ash medium-high pressure chemical foil |
| WO2020048045A1 (en) * | 2018-09-06 | 2020-03-12 | 南通海星电子股份有限公司 | Pretreatment process for preparing tio2 dielectric layer-containing electronic aluminum foil |
| CN113035596A (en) * | 2021-05-27 | 2021-06-25 | 南通海星电子股份有限公司 | Multi-effect cathode treatment aluminum anode foil formation method |
| CN113990667A (en) * | 2021-10-27 | 2022-01-28 | 宝兴县剑锋制箔电子有限公司 | Formation method of electrode foil |
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2009
- 2009-11-09 CN CN200910114537A patent/CN101707141A/en active Pending
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| CN103160902B (en) * | 2012-12-13 | 2015-12-23 | 宝兴县剑锋制箔电子有限公司 | Middle-high voltage electrode foil 5 sections changes into 2 grades of liquid feedback production methods |
| CN103160902A (en) * | 2012-12-13 | 2013-06-19 | 宝兴县剑锋制箔电子有限公司 | Middle-high voltage electrode foil five-section formation two-stage liquid feed production method |
| CN103779098B (en) * | 2014-01-06 | 2017-02-08 | 广西贺州市桂东电子科技有限责任公司 | Formation method of energy storage material applied to alternating current motor start capacitor |
| CN103779098A (en) * | 2014-01-06 | 2014-05-07 | 广西贺州市桂东电子科技有限责任公司 | Formation method of energy storage material applied to alternating current motor start capacitor |
| CN103741187B (en) * | 2014-01-06 | 2016-08-24 | 广西贺州市桂东电子科技有限责任公司 | A kind of mesohigh electric aluminum foil chemical conversion produces power supply solution and using method thereof |
| CN103741187A (en) * | 2014-01-06 | 2014-04-23 | 广西贺州市桂东电子科技有限责任公司 | Power supply solution for formation of electronic aluminum foil at middle-high voltage and application method thereof |
| CN106252081A (en) * | 2016-08-11 | 2016-12-21 | 四川立业电子有限公司 | A kind of anodizing composite dielectric film and preparation method thereof |
| CN107967996A (en) * | 2017-11-15 | 2018-04-27 | 广西贺州市桂东电子科技有限责任公司 | A kind of chemical synthesizing method of mash welder capacitor anode foils |
| CN107974701A (en) * | 2017-11-15 | 2018-05-01 | 广西贺州市桂东电子科技有限责任公司 | A kind of pre-treating method of anode aluminium foil chemical conversion |
| CN108376611A (en) * | 2017-12-29 | 2018-08-07 | 广西贺州市桂东电子科技有限责任公司 | A kind of production method of no foil ash medium-high pressure chemical foil |
| WO2020048045A1 (en) * | 2018-09-06 | 2020-03-12 | 南通海星电子股份有限公司 | Pretreatment process for preparing tio2 dielectric layer-containing electronic aluminum foil |
| CN113035596A (en) * | 2021-05-27 | 2021-06-25 | 南通海星电子股份有限公司 | Multi-effect cathode treatment aluminum anode foil formation method |
| CN113035596B (en) * | 2021-05-27 | 2021-08-13 | 南通海星电子股份有限公司 | Multi-effect cathode treatment aluminum anode foil formation method |
| CN113990667A (en) * | 2021-10-27 | 2022-01-28 | 宝兴县剑锋制箔电子有限公司 | Formation method of electrode foil |
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Open date: 20100512 |