CN1585060A - Process for etching 63 WV-100WV anode foils with high-specific capacity - Google Patents
Process for etching 63 WV-100WV anode foils with high-specific capacity Download PDFInfo
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- CN1585060A CN1585060A CN 200410041286 CN200410041286A CN1585060A CN 1585060 A CN1585060 A CN 1585060A CN 200410041286 CN200410041286 CN 200410041286 CN 200410041286 A CN200410041286 A CN 200410041286A CN 1585060 A CN1585060 A CN 1585060A
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Abstract
The optical aluminum foil with preliminary treatment, in the mixed liquor of the concentration 0.1-1 wt%, sulfuric acid and 5-20 wt% muriatic acid, is pre-etched by the interflow current, then dip in the mixed liquor of the concentration 10-25 wt% muriatic acid, 0.1-1 wt% sulfuric acid and 0.01-10 ppm copper ion, again is pre-etched by the interflow current in the mixed liquor of the concentration 0.1-2 wt% sulfuric acid, 10-25 wt% muriatic acid, 0.01-1 wt% oxalic acid and 0.2-5 wt% aluminum trichloride, at the last dip in the water liquor of the concentration 1-10 wt% nitric acid. The technology solves the etching method of anode foil on the working voltage 63WV-100WV.
Description
Technical field
The present invention relates to a kind of etching process of anode foil for aluminum electrolytic capacitor.
Background technology
Anode foil for aluminum electrolytic capacitor in order to enlarge its effective surface area, increases the static capacity of unit are, generally handles aluminium foil with electrochemical corrosion.The research of relevant raising area expanding rate aspect has many reports, and the past etching process is hole pattern effective area maximum when 6.3WV～50WV behind the aluminium foil corrosion, and is then less when 63WV-100WV.Mainly be the thin and skewness in corrosion aperture, when forming the 63WV-100WV oxide-film, reduce the phenomenon of expansion face effect because of oxide-film is thicker.
Technical scheme
The objective of the invention is to invent a kind of etching process of 63WV-100WV high specific volume anode foil, have the making method for low-voltage anode foil of higher specific volume, better mechanical performance.
The present invention is through pre-treatment, prime communication pre-corrosion, intermediate treatment, final exchange corrosion, reprocessing, and this five steps facture is made the high specific volume low-voltage anode foil of 63WV-100WV.
Details are as follows for various processes:
1, pre-treatment
The pre-treatment main purpose is to remove the greasy dirt of aluminium foil surface, impurity, makes the paper tinsel surface evenly, forms equally distributed initial pit when helping pre-etching.Concrete grammar is aluminium foil to be placed in the phosphate aqueous solution of 20～50 ℃ of temperature, concentration 0.5～10wt% soaked 2～8 minutes.The concentration of phosphoric acid liquid is low excessively, does not reach cleaning performance, and height then can thickness thinning, and optimum efficiency is 1～6wt%.
The pre-treatment temperature is lower than 20 ℃, the weak effect that deoils, and surpassing 50 ℃ of comprehensive dissolvings of surface meeting and causing attenuate, optimum temperature is 25～40 ℃.
The pre-treatment time is less than 2 minutes, does not reach treatment effect, if surpass 8 minutes, understands attenuate equally, so 3～6 minutes optimization process time.
2, communication pre-corrosion
Pre-etching is the key of whole etching process, and its main purpose is to cause initial pit at aluminium foil surface, and make the pit aperture size reasonable, be evenly distributed.
The pre-etching method is the aluminium foil after the pre-treatment to be placed on carry out the alternating current electrolysis corrosion in concentration 0.1～1wt% sulfuric acid, the 5～20wt% hydrochloric acid mixed solution.Corrosion temperature is 30～60 ℃, and current density is 20～100A/dm
2, electric weight is 200～2000C/dm
2
Send out in the process of hole in pre-etching, concentration of hydrochloric acid is lower than 5wt%, and then a little less than the corrosiveness, it is few to send out hole point; Surpass 20wt%, it is thin and close that aluminium foil surface is sent out hole point, so optimum concentration range is at 10～15wt%.
Sulfuric acid concentration is lower than 0.1wt%, and aluminium foil surface is film forming not, and pit can not cause; Be higher than 1wt%, surface filming is too thick, and pit can not cause.Therefore optium concentration is at 0.1～1wt%.
The pre-etching temperature is lower than 30 ℃, and then corrosion rate is too slow, and corrosive effect is poor; Surpass 60 ℃, passivation can take place, be difficult to corrosion, so temperature preferably is controlled at 30～60 ℃.
The pre-etching current density also is one of the factor in an influence hole, and current density is too small, excessive, can cause pit inhomogeneous tiny with the aperture, thereby current density should be 20～100A/dm
2
The pre-etching electric weight is less than 200C/dm
2, send out the hole weak effect; Electric weight is greater than 2000C/dm
2, aluminium foil surface is dissolving comprehensively, so electric weight preferably is controlled at 200～2000C/dm
2
3, intermediate treatment
The intermediate treatment purpose is the deposited film that is unfavorable for reaming that produces in the pre-etching process by the chemical method flush away.
Content of copper ion is lower than 0.01PPM in the treatment fluid, and aluminium foil surface can not activate, and surpasses 10PPM, then forms primary cell at aluminium foil surface, the reaction speed aggravation, and corrosive effect is poor.Therefore the optimum content scope is 0.01～10PPM.
Middle treatment temperature is lower than 40 ℃, does not have and washes membrane interaction; Optimum temperature is higher than 80 ℃, can destroys initial pit, so should be 40～80 ℃.
Processing time is less than 1 minute, does not have equally to wash membrane interaction; Surpass 6 minutes and can destroy initial pit.Therefore the processing time preferably was controlled at 1～6 minute.
4, final exchange corrosion
Be called main corrosion again, its objective is on initial pit basis and carry out reaming, make the aperture of etch pit satisfy the requirement that 63WV-100WV changes into.
Level corroding method in back is the aluminium foil after the intermediate treatment to be placed in the mixed solution of sulfuric acid, 10～25wt% hydrochloric acid, 0.01～1wt% thiocarbamide, 0.01～1wt% oxalic acid and 0.2～5wt% alchlor of concentration 0.1～1wt% carry out the alternating current electrolysis corrosion.25～45 ℃ of temperature, current density are 10～40A/dm
2, electric weight is 5000～30000C/dm
2
When corrosion back level, concentration of hydrochloric acid is lower than 10wt%, then a little less than the corrosiveness, and can not deep etch; Surpass 25wt%, aluminium foil surface is dissolving comprehensively, so optimum concentration range is at 15～23wt%.
Sulfuric acid concentration is lower than 0.1wt%, can not form pitting or spot corrosion, and corrosive effect is poor; Be higher than 1wt%, surface filming is too thick, and reaming is difficult to deeply.Therefore optium concentration is at 0.1～0.8wt%.
Thiocarbamide, oxalic acid play surperficial corrosion inhibiter effect, and content is lower than 0.01wt%, does not have corrosion mitigating effect; Be higher than 1wt%, rust inhibition is too strong, and aluminium foil surface produces passivation, so the optimum content scope is 0.01～1wt%.
When alchlor content was low in the corrosive liquid, corrosivity was strong, and it is big to lose the aluminium amount; Alchlor content is in high 5wt%, and then corrosiveness weakens, and specific volume descends.So alchlor content the best is at 0.2～4wt%.
The temperature of back level corrosion is lower than 25 ℃, and corrosive effect is poor; Be higher than 45 ℃, can make the corrosion aggravation, be difficult to control.Optimum temperature is at 25～45 ℃.
The current density of corrosion is less than 10A/dm
2, reaming hole DeGrain; Current density is greater than 40A/dm
2, the dissolving comprehensively of paper tinsel surface.The optimum current density range is 10～40A/dm
2
The electric weight of corrosion is less than 5000C/dm
2, the reaming effect is also not obvious; Electric weight is greater than 30000C/dm
2, the aluminium foil surface meltage is big, intensity difference.Best electric weight is 5000～28000C/dm
2
5, reprocessing
The reprocessing purpose is to remove residual chloride ion of aluminium foil surface and metal impurities.
The method of reprocessing of the present invention is with the aqueous solution of nitric acid of the aluminium foil after the corrosion with concentration 1～10wt%, soaks 2～4 minutes down for 20～50 ℃ in temperature.Handle back aluminium foil surface chloride ion residual quantity≤1mg/m
2
Specific embodiment:
Below further specify the present invention by many paper tinsel actual process process in 85um (95um) Xinjiang.
1, pre-treatment:
With aluminium foil be placed on soak 4 minutes in the phosphate aqueous solution that 40 ℃, concentration are 3wt% after, take out.
2, prime pre-etching:
It is that 45 ℃, concentration are to carry out the alternating current electrolysis corrosion in the sulfuric acid, 15wt% hydrochloric acid mixed solution of 0.8wt% that aluminium foil after the pre-treatment is placed on temperature, and wherein, the mixed liquor current density is 31A/dm
2, electric weight is: 800C/dm
2
3, intermediate treatment:
At the sulfuric acid of concentration 22wt% hydrochloric acid, 0.8wt% and contain soak 5 minutes in the mixed solution of 3PPM copper ion after, take out.
4, final exchange corrosion:
Carry out the alternating current electrolysis corrosion in the mixed solution of the sulfuric acid of concentration 0.7wt%, 21wt% hydrochloric acid, 0.02wt% thiocarbamide, 0.05wt% oxalic acid, 0.4wt% alchlor, the parameters of mixed solution is:
Temperature: 31 ℃
Current density: 22A/dm
2
Electric weight: 12000C/dm
2(85um), 13800C/dm
2(95um)
5, reprocessing:
In temperature is that 44 ℃, concentration are to soak 3 minutes in the aqueous solution of nitric acid of 5wt%.
The condition of changing into is:
85 ℃ of 0.05A/cm of 5% ammonium adipate
2Vfe=80V, 130V
The result is as follows:
1, is respectively through the 85um Xinjiang crowd of above explained hereafter and every performance that paper tinsel reaches: C
85Vf=9.1～10uf/cm
2C
135Vf=4.1～4.4uf/cm
2F=21.5N/cm.
2, be respectively through the 95um Xinjiang crowd of above explained hereafter and every performance that paper tinsel reaches: C
85Vf=10～11uf/cm
2C
135Vf=4.5～4.8uf/cm
2F=22.5N/cm.
Claims (6)
1, the etching process of 63WV-100WV high specific volume anode foil is characterized in that may further comprise the steps:
A, pre-treatment: aluminium foil is placed in the phosphate aqueous solution of 20～80 ℃ of concentration 0.5～10wt% and soaked 2～8 minutes;
B, prime communication pre-corrosion: the aluminium foil after the pre-treatment is placed in the sulfuric acid, 5～20wt% hydrochloric acid mixed solution of concentration 0.1～1wt% and carries out the alternating current electrolysis corrosion;
C, intermediate treatment: at the sulfuric acid of concentration 10～25wt% hydrochloric acid, 0.1-1wt% and contain in the mixed solution of 0.01～10PPM copper ion and carry out intermediate treatment;
D, final exchange corrosion: in the mixed solution of the sulfuric acid of concentration 0.1～1wt%, 10-25wt% hydrochloric acid, 0.01～1wt% thiocarbamide, 0.01～1wt% oxalic acid, 0.1～5wt% alchlor, carry out the alternating current electrolysis corrosion;
E, reprocessing: in the aqueous solution of nitric acid of 20～50 ℃ of concentration 1～10wt% of temperature, soaked 1～5 minute.
2, according to the etching process of the described 63WV-100WV high specific volume anode foil of claim 1, it is characterized in that: in pre-treatment, optical aluminum foil soaked in phosphate aqueous solution 3～6 minutes.
3,, it is characterized in that in the prime communication pre-corrosion current density is 20～100A/dm according to the etching process of the described 63WV-100WV high specific volume anode foil of claim 1
2, electric weight is 200～2000C/dm
2
4, according to the etching process of the described 63WV-100WV high specific volume anode foil of claim 1, it is characterized in that when intermediate treatment the temperature of mixed solution is 40～80 ℃, soak time is 1～6 minute.
5,, it is characterized in that when final exchange corrosion the temperature of mixed solution is 25～45 ℃ and carries out the alternating current electrolysis corrosion that its current density is 10～40A/dm according to the etching process of the described 63WV-100WV high specific volume anode foil of claim 1
2, electric weight is 5000～30000C/dm
2
6,, it is characterized in that when reprocessing soak time is 2～4 minutes according to the etching process of the described 63WV-100WV high specific volume anode foil of claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410041286 CN1253900C (en) | 2004-06-14 | 2004-06-14 | Process for etching 63 WV-100WV anode foils with high-specific capacity |
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|---|---|---|---|
| CN 200410041286 CN1253900C (en) | 2004-06-14 | 2004-06-14 | Process for etching 63 WV-100WV anode foils with high-specific capacity |
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| CN1585060A true CN1585060A (en) | 2005-02-23 |
| CN1253900C CN1253900C (en) | 2006-04-26 |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100511517C (en) * | 2005-06-06 | 2009-07-08 | 肇庆华锋电子铝箔有限公司 | Variable frequency corrosion method of low-voltage anode foil for electrolytic capacitor |
| CN100524558C (en) * | 2006-11-06 | 2009-08-05 | 乳源瑶族自治县东阳光化成箔有限公司 | A low-voltage anode foil used for aluminium electrolytic capacitor and its manufacturing method |
| CN102279139A (en) * | 2011-07-25 | 2011-12-14 | 新疆众和股份有限公司 | Method for detecting surface solubility of anode electronic aluminum foil for aluminum electrolytic capacitor and test aqueous solution thereof |
| CN103187176A (en) * | 2013-03-22 | 2013-07-03 | 常州大学 | Corrosion technology of anode aluminum foil of electrolysis capacitor |
| CN103779577A (en) * | 2014-01-16 | 2014-05-07 | 新疆众和股份有限公司 | Three-dimensional porous lithium battery current collector and preparation method thereof |
| CN103779578A (en) * | 2014-01-16 | 2014-05-07 | 新疆众和股份有限公司 | Secondary-corrosion three-dimensional porous lithium battery current collector and preparation method thereof |
| CN112080787A (en) * | 2020-08-14 | 2020-12-15 | 东莞东阳光科研发有限公司 | Corrosion foil for aluminum electrolytic capacitor and preparation method thereof |
| CN116446027A (en) * | 2023-04-19 | 2023-07-18 | 恒扬（韶关）工业有限公司 | Preparation process of low-voltage anode foil |
-
2004
- 2004-06-14 CN CN 200410041286 patent/CN1253900C/en not_active Expired - Fee Related
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100511517C (en) * | 2005-06-06 | 2009-07-08 | 肇庆华锋电子铝箔有限公司 | Variable frequency corrosion method of low-voltage anode foil for electrolytic capacitor |
| CN100524558C (en) * | 2006-11-06 | 2009-08-05 | 乳源瑶族自治县东阳光化成箔有限公司 | A low-voltage anode foil used for aluminium electrolytic capacitor and its manufacturing method |
| CN102279139A (en) * | 2011-07-25 | 2011-12-14 | 新疆众和股份有限公司 | Method for detecting surface solubility of anode electronic aluminum foil for aluminum electrolytic capacitor and test aqueous solution thereof |
| CN103187176A (en) * | 2013-03-22 | 2013-07-03 | 常州大学 | Corrosion technology of anode aluminum foil of electrolysis capacitor |
| CN103187176B (en) * | 2013-03-22 | 2015-12-02 | 常州大学 | A kind of etching process of anode aluminum foil of electrolytic capacitor |
| CN103779577A (en) * | 2014-01-16 | 2014-05-07 | 新疆众和股份有限公司 | Three-dimensional porous lithium battery current collector and preparation method thereof |
| CN103779578A (en) * | 2014-01-16 | 2014-05-07 | 新疆众和股份有限公司 | Secondary-corrosion three-dimensional porous lithium battery current collector and preparation method thereof |
| CN103779578B (en) * | 2014-01-16 | 2016-06-29 | 新疆众和股份有限公司 | Two grades corrode three-dimensional porous lithium battery collector and preparation method thereof |
| CN103779577B (en) * | 2014-01-16 | 2016-09-14 | 新疆众和股份有限公司 | Three-dimensional porous lithium battery collector and preparation method thereof |
| CN112080787A (en) * | 2020-08-14 | 2020-12-15 | 东莞东阳光科研发有限公司 | Corrosion foil for aluminum electrolytic capacitor and preparation method thereof |
| CN116446027A (en) * | 2023-04-19 | 2023-07-18 | 恒扬（韶关）工业有限公司 | Preparation process of low-voltage anode foil |
| CN116446027B (en) * | 2023-04-19 | 2023-12-29 | 恒扬（韶关）工业有限公司 | Preparation process of low-voltage anode foil |
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