CN101235527A - Chemical synthesis method for anodic foil oxide film acid resistance - Google Patents
Chemical synthesis method for anodic foil oxide film acid resistance Download PDFInfo
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- CN101235527A CN101235527A CNA2007101353265A CN200710135326A CN101235527A CN 101235527 A CN101235527 A CN 101235527A CN A2007101353265 A CNA2007101353265 A CN A2007101353265A CN 200710135326 A CN200710135326 A CN 200710135326A CN 101235527 A CN101235527 A CN 101235527A
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- oxide film
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- chemical synthesis
- acid resistance
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Abstract
The invention relates to technology method for forming acid-resistance of low pressure anode foil oxydic film, which comprises the following steps: forming corrosion foil, carrying out first stage compound plate in monoammonium phosphate solution with concentration 0.02-2wt% after being treated by phosphorus acid with concentration 0.5-15wt%, then carrying out high-temperature heating process, then carrying out second stage compounding plate in monoammonium phosphate solution with concentration 0.02-2wt%, drying after cleaning. The technology method solves the acid-resistance of the anode foil oxydic film based on a high capacity of electrostatic capacitance of anode foil oxydic unit area, thereby, the generated aluminum electrolytic capacitor with 85 DEG C high temperature load is guaranteed, and the storage life reaches 5000h.
Description
Technical field
The present invention relates to a kind of method for chemically synthesizing of anode foil for aluminum electrolytic capacitor.
Background technology
Anode foil for aluminum electrolytic capacitor in order to obtain the anode foils of the high electrostatic capacity of unit surface, generally forms in the ammonium adipate aqueous solution with 15wt%.The research of the high electrostatic capacity of units concerned's area anode foils has many reports, but the oxide film acid resistance of its formation is relatively poor, can not satisfy the aluminium electrolutic capacitor electricity consumption stick with paste in various acid additives oxide film compactness, corrosion stability requirement that the surface is formed, and 85 ℃ of high-temperature load of aluminium electrolutic capacitor of producing and only reach 1000h storage time.
Summary of the invention
The objective of the invention is to invent a kind of chemical synthesis method for anodic foil oxide film acid resistance, to improve the acid resistance and the life-span of product.
Technical solution of the present invention comprises that etched foil changes into, phosphoric acid is handled, sheet, cleaning, baking step are answered in sheet, pyroprocessing, the second stage to the first step again.
Adopt manufacturing of the present invention the densification of low-voltage anodic foil oxide film, have good acid resistance, can reach 5000h in 85 ℃ of high-temperature load and storage time.
Details are as follows for various processes:
1, etched foil changes into
Change into main purpose and form γ-AL on the etched foil surface
2O
3Concrete grammar is etched foil to be placed in the ammonium adipate aqueous solution of 50～90 ℃ of temperature, concentration 15wt% form oxide film, and the formation current density is 0.05A/cm
2, 20～40 minutes time.
Change into temperature and be lower than 50 ℃, the coating mass of formation is poor; Change into temperature and be higher than 90 ℃, be difficult to control on the industrial production.The best changes into 50～90 ℃ of temperature.
The time of changing into is less than 20 minutes, and the oxide film of formation is insufficient, and is withstand voltage low; If surpass 40 minutes, the oxide film water content of formation is high can to influence coating mass.The best changes into 20～40 minutes time.
2, phosphoric acid is handled
It is to clean to remove small part oxide film inferior and impurity in the formation process that phosphoric acid is handled main purpose.
40～90 ℃ of temperature, the phosphate aqueous solution of concentration 0.5～15wt%, 0.5～15 minute time that phosphoric acid is handled.
Treatment temp is lower than 40 ℃ or phosphoric acid concentration and is lower than 0.5wt%, can not reach to clean oxide film inferior and impurity effect; Temperature is higher than 90 ℃ or phosphoric acid concentration and is higher than 15wt%, can accelerated reaction, be difficult to control.Therefore 40～90 ℃ of optimum tempss, concentration 0.5～15wt%.
Phosphoric acid is less than 0.5 minute between handling, and can not remove oxide film inferior fully, if surpass 15 minutes, destroys the measured oxide film of matter on the contrary.0.5～15 minute optimum handling time.
3, the multiple sheet of the first step
Multiple sheet purpose is the aluminum orthophoshpate structure (though owing to paper tinsel surface oxide film inferior after handling through phosphoric acid is removed, the defective and the crack of oxide film are more) that forms excellent property at the paper tinsel outside surface.
60～90 ℃ of multiple sheet temperature, concentration 0.02～2wt% ammonium dihydrogen phosphate aqueous solution, multiple sheet current density is 0.05A/cm
2, 6～20 minutes time;
Multiple sheet temperature is lower than 60 ℃, and the coating mass of formation is poor; Change into temperature and be higher than 90 ℃, be difficult to control in the production.The best changes into 60～90 ℃ of temperature.
The biphosphate ammonium concentration is lower than 0.02wt%, can not form the oxide film that contains the aluminum orthophoshpate structure; Concentration is higher than 2wt%, can destroy the oxide film of formation on the contrary, makes withstand voltage reduction.
The multiple sheet time is less than 6 minutes, and the oxide film of formation is insufficient, and is withstand voltage low; Surpass 20 minutes, the oxide film water content of formation is high can to influence coating mass.The best changes into 6～20 minutes time.
4, pyroprocessing
The pyroprocessing purpose is the aqua oxidation film that will form previously, at high temperature is converted into γ-AL
2O
3
350～600 ℃ of the temperature of pyroprocessing, 1～5 minute time.
The temperature of pyroprocessing is lower than 350 ℃, and the aqua oxidation film can not be converted into γ-AL
2O
3Temperature is higher than 600 ℃, and the aqua oxidation film then can be converted into the oxide film of other type, and aluminum substrate easily melts in the middle of the paper tinsel, and production can't move.
The pyroprocessing time is less than 1 minute, and the aqua oxidation film can not be converted into γ-AL fully
2O
3Surpass 5 minutes, the big and control difficulty of investment of production equipment cost.
5, the multiple sheet in the second stage
Multiple sheet purpose is that oxide film is repaired in defective and the crack that the oxide film surface produces when high temperature is made the transition.
60～90 ℃ of multiple sheet temperature, concentration 0.02～2wt% ammonium dihydrogen phosphate aqueous solution, multiple sheet current density is 0.05A/cm
2, 6～20 minutes time.
Multiple sheet temperature is lower than 60 ℃, and the coating mass of formation is poor; Change into temperature and be higher than 90 ℃, be difficult to control in the production.
The biphosphate ammonium concentration is lower than 0.02wt%, can not form the oxide film that contains the aluminum orthophoshpate structure; Concentration is higher than 2wt%, can destroy the oxide film of formation on the contrary, makes withstand voltage reduction.
The multiple sheet time is less than 6 minutes, and the oxide film of formation is insufficient, and is withstand voltage low; Surpass 20 minutes, the oxide film water content of formation is high can to influence coating mass.
6, clean
Clean and use room temperature pure water, 1～5 minute time.
Clean and use the room temperature pure water, the time is less than 1 minute, cleans unclean; Time is higher than 5 minutes, and the investment of production equipment cost is big.
7, oven dry
100～300 ℃ of bake out temperatures, 1～5 minute time.
Bake out temperature is lower than 100 ℃, can not dry fully; Temperature is higher than 300 ℃, can destroy the oxide film that multiple sheet forms.100～300 ℃ of best bake out temperatures.
Drying time is less than 1 minute, can not dry by the fire the part of anhydrating fully; Time was surpassed in 5 minutes, and equipment investment cost is big.
Embodiment
Below by further specifying the present invention with the actual technological process that changes into of 100um etched foil.
1, changes into
Ammonium adipate concentration of aqueous solution: 15wt%
Ammonium adipate aqueous temperature: 50～90 ℃, can be controlled in 85 ℃
Current density: 0.05A/cm
2
Etched foil is placed in the above-mentioned ammonium adipate aqueous solution 20～40 minutes, best 30 minutes, forms oxide film.
2, phosphoric acid is handled
Phosphate aqueous solution concentration: 0.5～15wt%, best 0.8wt%
The phosphate aqueous solution temperature: 40～90 ℃, best 70 ℃
Paper tinsel after etched foil changed into is placed on to be handled in the above-mentioned phosphate aqueous solution 0.5～15 minute, best 10 minutes.
3, the multiple sheet of the first step
NH
4H
2PO
4Concentration of aqueous solution: 0.02～2wt%, best 1.8wt%
NH
4H
2PO
4Aqueous temperature: 60～90 ℃, controlledly be made as 68 ℃
Will the paper tinsel after phosphoric acid is handled be immersed in the above-mentioned ammonium dihydrogen phosphate aqueous solution 6～20 minutes, best 12 minutes.
4, pyroprocessing
Oven temperature: 350～600 ℃, best 550 ℃
Paper tinsel behind the multiple sheet of the first step is placed baking oven,, take out after best 4 minutes through 1～5 minute time.
5, the multiple sheet in the second stage
NH
4H
2PO
4Concentration: 0.02～2wt%, best 1.8wt%
Temperature: 60～90 ℃, best 68 ℃
Current density: 0.05A/cm
2
The paper tinsel that will take out from baking oven is immersed in the above-mentioned ammonium dihydrogen phosphate aqueous solution, multiple 6～20 minutes sheet time, best 12 minutes.
6, clean
To clean 1～5 minute with the room temperature pure water through the paper tinsel behind the multiple sheet in the second stage.
7, oven dry
Oven temperature: 100～300 ℃, best 250 ℃
Time: 1～5 minute, best 4 minutes
The result is as follows: (stick with paste 85 ℃ and soaked print 2mA/5cm 5 minutes with moisture 〉=40% electricity
2Survey the time that it arrives the AV value)
| Operating voltage (WV) | 6.3 | 10 | 16 | 25 | 35 | 50 | 63 | 80 | 100 | ||
| Proof voltage (Vf) | 8.0 | 13 | 21 | 33 | 47 | 67 | 85 | 105 | 132 | ||
| Dipping back Tr pressure rising time (S) | Former technology | 60-90 | 82 | 76 | 68 | 86 | 77 | 69 | 80 | 73 | 76 |
| Existing technology | ≤40 | 30 | 35 | 28 | 32 | 38 | 22 | 36 | 39 | 35 | |
As seen from the above table: the invention solves the acid resistance of anode foils oxide film, 85 ℃ of high-temperature load of aluminium electrolutic capacitor of producing through evidence and reach 5000h storage time.
Claims (9)
1, chemical synthesis method for anodic foil oxide film acid resistance is characterized in that comprising successively that etched foil changes into, phosphoric acid is handled, sheet, cleaning, baking step are answered in sheet, pyroprocessing, the second stage to the first step again.
2, according to the described chemical synthesis method for anodic foil oxide film acid resistance of claim 1, it is characterized in that it is etched foil to be placed in the ammonium adipate aqueous solution of 50～90 ℃ of temperature, concentration 15wt% form oxide film that etched foil changes into, the formation current density is 0.05A/cm
2, 20～40 minutes time.
3,, it is characterized in that it is that paper tinsel after etched foil is changed into is placed in the phosphate aqueous solution of 40～90 ℃ of temperature, concentration 0.5～15wt% and handled 0.5～15 minute that phosphoric acid is handled according to the described chemical synthesis method for anodic foil oxide film acid resistance of claim 1.
4,, it is characterized in that the multiple sheet of the first step is that the paper tinsel after handling at phosphoric acid is carried out in 60～90 ℃ of temperature, concentration 0.02～2wt% ammonium dihydrogen phosphate aqueous solution according to the described chemical synthesis method for anodic foil oxide film acid resistance of claim 1.
5,, it is characterized in that multiple 6～20 minutes sheet time of the first step according to the described chemical synthesis method for anodic foil oxide film acid resistance of claim 1.
6,, it is characterized in that pyroprocessing is that the paper tinsel behind the multiple sheet of the first step is placed temperature is 1～5 minute 350～600 ℃ of baking oven treatment time according to the described chemical synthesis method for anodic foil oxide film acid resistance of claim 1.
7, according to the described chemical synthesis method for anodic foil oxide film acid resistance of claim 1, it is characterized in that it is to answer sheet in 60～90 ℃ of temperature, concentration 0.02～2wt% ammonium dihydrogen phosphate aqueous solution at the paper tinsel after the pyroprocessing that sheet is answered in the second stage, multiple sheet current density is 0.05A/cm
2, 6～20 minutes time.
8,, it is characterized in that adopting the room temperature pure water to clean 1～5 minute time according to the described chemical synthesis method for anodic foil oxide film acid resistance of claim 1.
9,, it is characterized in that under 100～300 ℃ of temperature condition, drying 1～5 minute time according to the described chemical synthesis method for anodic foil oxide film acid resistance of claim 1.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200710135326A CN100591808C (en) | 2007-11-05 | 2007-11-05 | Chemical synthesis method for anodic foil oxide film acid resistance |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200710135326A CN100591808C (en) | 2007-11-05 | 2007-11-05 | Chemical synthesis method for anodic foil oxide film acid resistance |
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| Publication Number | Publication Date |
|---|---|
| CN101235527A true CN101235527A (en) | 2008-08-06 |
| CN100591808C CN100591808C (en) | 2010-02-24 |
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|---|---|---|---|
| CN200710135326A Expired - Fee Related CN100591808C (en) | 2007-11-05 | 2007-11-05 | Chemical synthesis method for anodic foil oxide film acid resistance |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101383228B (en) * | 2008-10-24 | 2010-12-29 | 南通海一电子有限公司 | Formation method of electrode foil for low voltage low leakage aluminum electrolysis capacitor |
| CN102800483A (en) * | 2012-08-10 | 2012-11-28 | 南通海星电子有限公司 | Formation processing method for reducing leaking current of low-voltage formation foil |
| CN104599845A (en) * | 2014-12-31 | 2015-05-06 | 日丰（清远）电子有限公司 | Production method of low voltage aluminum anode foil for electrolytic condenser |
| CN113774456A (en) * | 2021-08-20 | 2021-12-10 | 扬州宏远电子股份有限公司 | Alternating-current corrosion foil formation process method for starting double-formation motor and aluminum foil |
| CN114411219A (en) * | 2021-12-30 | 2022-04-29 | 立敦电子科技（惠州）有限公司 | High-acid-resistance low-pressure formed foil, preparation method and application thereof |
-
2007
- 2007-11-05 CN CN200710135326A patent/CN100591808C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101383228B (en) * | 2008-10-24 | 2010-12-29 | 南通海一电子有限公司 | Formation method of electrode foil for low voltage low leakage aluminum electrolysis capacitor |
| CN102800483A (en) * | 2012-08-10 | 2012-11-28 | 南通海星电子有限公司 | Formation processing method for reducing leaking current of low-voltage formation foil |
| CN102800483B (en) * | 2012-08-10 | 2015-05-20 | 南通海星电子股份有限公司 | Formation processing method for reducing leaking current of low-voltage formation foil |
| CN104599845A (en) * | 2014-12-31 | 2015-05-06 | 日丰（清远）电子有限公司 | Production method of low voltage aluminum anode foil for electrolytic condenser |
| CN104599845B (en) * | 2014-12-31 | 2017-07-11 | 日丰（清远）电子有限公司 | A kind of production method of electrolytic capacitor low voltage anode aluminum foil |
| CN113774456A (en) * | 2021-08-20 | 2021-12-10 | 扬州宏远电子股份有限公司 | Alternating-current corrosion foil formation process method for starting double-formation motor and aluminum foil |
| CN114411219A (en) * | 2021-12-30 | 2022-04-29 | 立敦电子科技（惠州）有限公司 | High-acid-resistance low-pressure formed foil, preparation method and application thereof |
| CN114411219B (en) * | 2021-12-30 | 2023-10-27 | 立敦电子科技（惠州）有限公司 | High acid-resistant low-pressure formed foil, preparation method and application thereof |
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| Publication number | Publication date |
|---|---|
| CN100591808C (en) | 2010-02-24 |
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Owner name: XINJIANG WESTERN HONGYUAN ELECTRONIC CO., LTD. Free format text: FORMER OWNER: HONGYUAN ELECTRONIC CO LTD, YANGZHOU Effective date: 20110624 |
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