CN109786113A - A kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technology - Google Patents

A kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technology Download PDF

Info

Publication number
CN109786113A
CN109786113A CN201711120018.5A CN201711120018A CN109786113A CN 109786113 A CN109786113 A CN 109786113A CN 201711120018 A CN201711120018 A CN 201711120018A CN 109786113 A CN109786113 A CN 109786113A
Authority
CN
China
Prior art keywords
waste acid
level
hua cheng
foil
cheng foil
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.)
Pending
Application number
CN201711120018.5A
Other languages
Chinese (zh)
Inventor
杨小兵
费新金
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TIANQUAN JUNLI ELECTRONIC MATERIAL CO Ltd
Original Assignee
TIANQUAN JUNLI ELECTRONIC MATERIAL CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by TIANQUAN JUNLI ELECTRONIC MATERIAL CO Ltd filed Critical TIANQUAN JUNLI ELECTRONIC MATERIAL CO Ltd
Priority to CN201711120018.5A priority Critical patent/CN109786113A/en
Publication of CN109786113A publication Critical patent/CN109786113A/en
Pending legal-status Critical Current

Links

Landscapes

  • Fixed Capacitors And Capacitor Manufacturing Machines (AREA)

Abstract

The present invention relates to a kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technologies, comprising the following steps: 1) carries out pre-treatment to electrolytic etching foil;2) liquid spray is carried out to aluminium foil with chemical solution and carries out level Four chemical conversion;3) it cleans;4) piece is burnt;5) Pyatyi, six grades of chemical conversions are carried out to level Four Waste Acid From Hua Cheng Foil, obtains six grades of Waste Acid From Hua Cheng Foils;6) it post-processes;7) reprocessed six grades of Waste Acid From Hua Cheng Foils carry out cleaning and are placed on drying in baking oven.The technique of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil of the present invention, the technology with chemical conversion tank liquid spray is increased in chemical synthesis technology, effectively remove impurity and dissolution surface fiber shape alpha-alumina crystals in etch pit, control the growth of outer layer hydrate, fine and close oxidation film is generated by six grades of chemical conversions, and then improves the specific volume and bending strength of Waste Acid From Hua Cheng Foil.

Description

A kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technology
Technical field
The present invention relates to a kind of Waste Acid From Hua Cheng Foil and its production technology, more particularly to a kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and Its production technology.
Background technique
The basic structure of general aluminium electrolutic capacitor is foil winding type structure, is by anode aluminium foil, electrolytic paper, cathode 4 layers of overlapping such as aluminium foil, electrolytic paper are wound.Its working media is to generate one layer in aluminium foil surface by way of anodic oxidation The anode of oxidation film, this oxide film dielectric layer and capacitor is combined into a rounded system.The anode foils and Cathode Foil of selection Waste Acid From Hua Cheng Foil usually after corrosion treatment, the reason is that corrosion can make the surface area of aluminium foil be far longer than its apparent surface Product, so that the available big static capacity after chemical conversion (energizing), more effectively utilizes its practical electrode area.
In recent years, in field of electronic device, the volume of aluminium electrolutic capacitor is being gradually reduced.In order to adapt to this feelings Condition, it is desirable that the Waste Acid From Hua Cheng Foil unit static capacity that aluminium electrolutic capacitor is selected is big.While Waste Acid From Hua Cheng Foil unit static capacity increases, The consumption that other auxiliary materials in aluminium electrolutic capacitor manufacture can also be reduced, also further conducive to the small-sized of aluminium electrolutic capacitor Change.The bending strength of Waste Acid From Hua Cheng Foil is bigger, and the volume occupied after the coiling is smaller, also has to the miniaturization of capacitor particularly significant Effect.Therefore unit static capacity (hereinafter referred to as specific volume) and the bending resistance for further increasing aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil are strong Degree is still the major subjects of current Waste Acid From Hua Cheng Foil production technology research and development.
It can be derived according to the electrostatic fundamental formular of physics, when the timing of voltage one of application, Yao Tigao Waste Acid From Hua Cheng Foil There are three types of approach for specific volume: 1) expanding the surface area of Waste Acid From Hua Cheng Foil;2) dielectric relative dielectric constant is improved;3) oxidation film is reduced Pressure-resistant thickness.
The production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil is generally specially following process: excessive erosion of learning from else's experience in the prior art , purity be 99.99% aluminium foil, in water soak after take out, in electrolytic bath carry out level Four chemical conversion;Change after level Four is melted into It is taken out at foil and carries out high-temperature heat treatment, then carry out Pyatyi chemical conversion;It takes out, is put into phosphoric acid solution and is handled;Washing is taken out, and It is put into aqueous solution, carries out six grades of chemical conversions;Aluminium foil after six grades of chemical conversions is taken out into again post-treated, washing, drying.
However this production technology is used, oxidation film obtained is thicker in formation process and is easy corrosion treatment The micropore in aluminium foil crossed blocks, and reduces the surface area of oxidation film, and obtained coating mass is lower, is melted into because prepared by Foil haves the defects that mechanical strength is low, specific volume is relatively low in actual operation, is not able to satisfy the demand of production aluminium electrolutic capacitor.Cause This, previous chemical conversion production control method can either be broken through, improve technique by needing to seek one kind, reach Condenser Factory to Waste Acid From Hua Cheng Foil The requirement of the performance indexess such as high intensity, Fabrication of High Specific Capacitance, resistance to hydrability.
Summary of the invention
The object of the present invention is to provide a kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technology, produce it Waste Acid From Hua Cheng Foil has the advantages that Fabrication of High Specific Capacitance and high-flexural strength.
A kind of production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil, comprising the following steps:
1) electrolytic etching treated aluminium foil is subjected to pre-treatment;
2) liquid spray is carried out to the aluminium foil after pre-treatment with level-one chemical solution and carries out level-one chemical conversion, obtain level-one At foil;Liquid spray is carried out to level-one Waste Acid From Hua Cheng Foil with second level chemical solution and carries out second level chemical conversion, obtains second level Waste Acid From Hua Cheng Foil;With three Grade chemical solution carries out liquid spray to second level Waste Acid From Hua Cheng Foil and carries out three-level chemical conversion, obtains three-level Waste Acid From Hua Cheng Foil;It is melted into level Four molten Liquid carries out liquid spray to three-level Waste Acid From Hua Cheng Foil and carries out level Four chemical conversion, obtains level Four Waste Acid From Hua Cheng Foil;
3) level Four Waste Acid From Hua Cheng Foil is placed in cleaning solution and is cleaned;
4) the level Four Waste Acid From Hua Cheng Foil after cleaning is placed in burning piece furnace and carries out burning piece;
5) Pyatyi chemical conversion is carried out to the level Four Waste Acid From Hua Cheng Foil after burning piece with Pyatyi chemical solution, obtains Pyatyi Waste Acid From Hua Cheng Foil;With six Grade chemical solution carries out six grades of chemical conversions to Pyatyi Waste Acid From Hua Cheng Foil, obtains six grades of Waste Acid From Hua Cheng Foils;
6) six grades of Waste Acid From Hua Cheng Foils are post-processed;
7) it after to six grades of Waste Acid From Hua Cheng Foils cleaning after post treatment, places it in dry in baking oven.
The technique of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil of the present invention, the step of increasing with chemical conversion tank liquid spray, Using the acidity of chemical solution, impurity in the aluminium foil corrosion hole after corrosion treatment is effectively removed in spray avoids Waste Acid From Hua Cheng Foil from existing Corrosive degradation occurs in Working electrolyte and loses dielectric properties;The fibrous oxygen of chemical solution dissolution aluminium foil surface is utilized simultaneously Change aluminium crystal, control the growth of outer layer aqua oxidation film, so that the oxidation film obtained in chemical synthesis technology is finer and close, pressure resistance is thick Spend specific volume and bending strength smaller, and then that improve Waste Acid From Hua Cheng Foil.
Further, pretreatment process described in step 1) are as follows: treated that aluminium foil is placed in temperature is by electrolytic etching It is soaked 5~20 minutes in 90 DEG C or more of pure water.The process of pre-treatment is that aluminium foil surface and hot water reaction is made to generate one layer of hydration oxygen Change film, structure is the outer layer of the fine and close and even equal internal layer aluminium hydroxide of thickness and loose threadiness.The aqua oxidation film exists Current efficiency is higher when chemical conversion, and forms electricity reduction, thus saves electric energy when chemical conversion, to reduce in formation process Energy consumption.
Further, the spray flow of the spray of liquid described in step 2) is 20~100L/h, and spray time is 1~5 point Clock.It is intended that sufficiently being dissolved impurity by the parameter of control spray process, the thickness of outer layer aqua oxidation film is controlled, is kept away The aqua oxidation film for exempting to be formed in pretreatment process is blocked up, and the micropore in the aluminium foil after corrosion treatment is blocked to reduce corrosion The surface area of aluminium foil after processing;And keep the oxidation film formed in subsequent formation process finer and close, to increase Waste Acid From Hua Cheng Foil Specific volume.
Further, the chemical conversion of level-one described in step 2), second level chemical conversion, three-level chemical conversion, level Four chemical conversion be respectively adopted 60~ The current density of the formation voltage of 300V, 50~200mA/cm2, chemical conversion time are 1~20 clock, the level-one chemical solution, two Grade chemical solution, three-level chemical solution, level Four chemical solution are respectively the boric acid for 2wt%~8wt% that temperature is 80~95 DEG C Solution.
Further, the pure water solution that cleaning solution described in step 3) is 40~90 DEG C.
Further, the temperature of burning piece described in step 4) is 100~400 DEG C.Use the burning piece temperature, it is therefore intended that It opens the cracking hole of oxidation film at lower temperature, the hole that is cracked is enable when continuously forming oxidation film in subsequent formation process It preferably repairs, improves the defect of oxidation film, improve the specific volume of Waste Acid From Hua Cheng Foil, meanwhile, keep the oxidation film of Waste Acid From Hua Cheng Foil more soft, in turn Improve the bending strength of Waste Acid From Hua Cheng Foil.
Further, the chemical conversion of Pyatyi described in step 5) and six grades, which are melted into, is respectively adopted the formation voltage of 300~600V, and 50 ~200mA/cm2 current density, chemical conversion time are 1~30 minute, and the Pyatyi chemical solution, six grades of chemical solutions are respectively temperature Degree is 80~95 DEG C of 2wt%~8wt% boric acid solution and the mixed solution of 0.2wt%~3wt% ammonium hydroxide.
Further, last handling process described in step 6) are as follows: six grades of Waste Acid From Hua Cheng Foils will be passed through in the phosphorus of 3wt%~8wt% In acid solution, impregnated 3~12 minutes under conditions of 45~70 DEG C.The purpose is to make oxidation film adsorption phosphate anion, Make oxidation film that there is better resistance to hydration performance.
Further, the drying temperature of baking oven described in step 7) is 80~200 DEG C.It is intended that drying Waste Acid From Hua Cheng Foil Moisture inside surface area avoids oxidation film and water to react during the storage of product and generates unbodied aqua oxidation Object makes the dielectric properties of Waste Acid From Hua Cheng Foil that deterioration occur and reduce specific volume.
In order to better understand and implement, the present invention will be described in detail combined with specific embodiments below.
Specific embodiment
Embodiment 1
With high-intensitive Fabrication of High Specific Capacitance Waste Acid From Hua Cheng Foil production technology in a kind of aluminium electrolutic capacitor, include the following steps:
It takes the purity after electrolytic etching to be placed in 97 DEG C of pure water for 99.99% aluminium foil to soak 12 minutes.
In level-one electrolytic bath, liquid spray is carried out simultaneously to the aluminium foil after pre-treatment with the boric acid solution of 85 DEG C of 2wt% Level-one chemical conversion is carried out, level-one Waste Acid From Hua Cheng Foil is obtained;Wherein, the flow of liquid spray is 20L/h, and spray time is 1 minute;Level-one At formation voltage be 80V, current density 60mA/cm2, chemical conversion the time be 5 minutes.
In second level electrolytic bath, liquid spray is carried out to level-one Waste Acid From Hua Cheng Foil with the boric acid solution of 85 DEG C of 2wt%, and carry out Second level chemical conversion, obtains second level Waste Acid From Hua Cheng Foil;Wherein, liquid spray flow is 20L/h, and spray time is 1 minute, the change of second level chemical conversion It is 150V, current density 60mA/cm2 at voltage, the chemical conversion time is 5 minutes.
In three-level electrolytic bath, liquid spray is carried out to second level Waste Acid From Hua Cheng Foil with the boric acid solution of 85 DEG C of 8wt%, and carry out Three-level chemical conversion, obtains three-level Waste Acid From Hua Cheng Foil;Wherein, liquid spray flow is 20L/h, and spray time is 1 minute, three-level formation voltage For 220V, current density 60mA/cm2, being melted into the time is 5 minutes.
In level Four electrolytic bath, liquid spray is carried out to three-level Waste Acid From Hua Cheng Foil with the boric acid solution of 85 DEG C of 8wt%, and carry out Level Four chemical conversion, obtains level Four Waste Acid From Hua Cheng Foil;Wherein, liquid spray flow is 20L/h, and spray time is 1 minute, and formation voltage is 300V, current density 60mA/cm2, chemical conversion time are 5 minutes.
Level Four Waste Acid From Hua Cheng Foil is placed in 40 DEG C of pure water solution and is cleaned 5 minutes.
Waste Acid From Hua Cheng Foil after cleaning is placed in 300 DEG C of burning piece furnace and is burnt piece 3 minutes.
In Pyatyi electrolytic bath, with 85 DEG C of 8wt% boric acid solutions and 1.5wt% ammonium hydroxide mixed solution to four after burning piece Grade Waste Acid From Hua Cheng Foil carries out Pyatyi chemical conversion, obtains Pyatyi Waste Acid From Hua Cheng Foil;Wherein, formation voltage 420V, current density 60mA/cm2 change It is 5 minutes at the time.
In six grades of electrolytic baths, Pyatyi is melted into the mixed solution of 85 DEG C of 8wt% boric acid solutions and 1.5wt% ammonium hydroxide Foil carries out six grades of chemical conversions, obtains six grades of Waste Acid From Hua Cheng Foils;Wherein, formation voltage 520V, current density 60mA/cm2 are melted into the time It is 5 minutes.
After impregnating 6 minutes in the phosphoric acid solution for the 8wt% that six grades of Waste Acid From Hua Cheng Foils are placed in 60 DEG C, it is placed in 40 DEG C of pure water solution Middle cleaning 5 minutes.
Six grades of Waste Acid From Hua Cheng Foils after cleaning are placed in baking oven, are dried 3 minutes at 150 DEG C.
Embodiment 2
With high-intensitive Fabrication of High Specific Capacitance Waste Acid From Hua Cheng Foil production technology in a kind of aluminium electrolutic capacitor, include the following steps:
It takes the purity after electrolytic etching to be placed in 97 DEG C of pure water for 99.99% aluminium foil to soak 12 minutes.
In level-one electrolytic bath, liquid spray is carried out simultaneously to the aluminium foil after pre-treatment with the boric acid solution of 85 DEG C of 2wt% Level-one chemical conversion is carried out, level-one Waste Acid From Hua Cheng Foil is obtained;Wherein, liquid spray flow is 40L/h, and spray time is 1 minute;Level-one chemical conversion Voltage is 80V, current density 60mA/cm2, and the chemical conversion time is 5 minutes.
In second level electrolytic bath, liquid spray is carried out to level-one Waste Acid From Hua Cheng Foil with the boric acid solution of 85 DEG C of 2wt%, and carry out Second level chemical conversion, obtains second level Waste Acid From Hua Cheng Foil;Wherein, liquid spray flow is 40L/h, and spray time is 1 minute, second level formation voltage It is 150, current density 60mA/cm2, the chemical conversion time is 5 minutes.
In three-level electrolytic bath, liquid spray is carried out to second level Waste Acid From Hua Cheng Foil with the boric acid solution of 85 DEG C of 8wt%, and carry out Three-level chemical conversion, obtains three-level Waste Acid From Hua Cheng Foil;Wherein, liquid spray flow is 40L/h, and spray time is 1 minute, three-level formation voltage For 220V, current density 60mA/cm2, being melted into the time is 5 minutes.
In level Four electrolytic bath, liquid spray is carried out to three-level Waste Acid From Hua Cheng Foil with the boric acid solution of 85 DEG C of 8wt%, and carry out Level Four chemical conversion, obtains level Four Waste Acid From Hua Cheng Foil;Wherein, liquid spray flow is 40L/h, and spray time is 1 minute, and formation voltage is 300V, current density 60mA/cm2, chemical conversion time are 5 minutes.
Level Four Waste Acid From Hua Cheng Foil is placed in 90 DEG C of pure water solution and is cleaned 5 minutes.
Level Four Waste Acid From Hua Cheng Foil after cleaning is placed in 330 DEG C of burning piece furnace and is burnt piece 5 minutes.
In Pyatyi electrolytic bath, with the mixed solution of 85 DEG C of 8wt% boric acid solutions and 1.5wt% ammonium hydroxide to burn piece after Level Four Waste Acid From Hua Cheng Foil carries out Pyatyi chemical conversion, obtains Pyatyi Waste Acid From Hua Cheng Foil;Wherein, formation voltage 420V, current density 60mA/cm2, Being melted into the time is 5 minutes.
In six grades of electrolytic baths, Pyatyi is melted into the mixed solution of 85 DEG C of 8wt% boric acid solutions and 1.5wt% ammonium hydroxide Foil carries out six grades of chemical conversions, obtains six grades of Waste Acid From Hua Cheng Foils;Wherein, formation voltage 520V, current density 60mA/cm2 are melted into the time It is 5 minutes.
Six grades of Waste Acid From Hua Cheng Foils are placed in 60 DEG C of 8wt% phosphoric acid solution after impregnating 6 minutes, are placed in 40 DEG C of pure water solution Cleaning 5 minutes.
Six grades of Waste Acid From Hua Cheng Foils after cleaning are placed in baking oven, are dried 3 minutes at 150 DEG C.
Comparative example 1
It takes the purity after electrolytic etching to be placed in 97 DEG C of pure water for 99.99% aluminium foil to soak 12 minutes.
It is sprayed without liquid, level-one chemical conversion is carried out to the aluminium foil after pre-treatment with the boric acid solution of 85 DEG C of 2wt%, is obtained Level-one Waste Acid From Hua Cheng Foil;Wherein, level-one formation voltage is 80V, current density 60mA/cm2, and the chemical conversion time is 5 minutes.
It is sprayed without liquid, second level chemical conversion is carried out to level-one Waste Acid From Hua Cheng Foil with the boric acid solution of 85 DEG C of 2wt%, obtains second level Waste Acid From Hua Cheng Foil;Wherein, second level formation voltage is 150V, current density 60mA/cm2, and the chemical conversion time is 5 minutes.
It is sprayed without liquid, three-level chemical conversion is carried out to second level Waste Acid From Hua Cheng Foil with the boric acid solution of 85 DEG C of 8wt%, obtains three-level Waste Acid From Hua Cheng Foil;Wherein, three-level formation voltage is 220V, current density 60mA/cm2, and the chemical conversion time is 5 minutes.
It is sprayed without liquid, level Four chemical conversion is carried out to three-level Waste Acid From Hua Cheng Foil with the boric acid solution of 85 DEG C of 8wt%, obtains level Four Waste Acid From Hua Cheng Foil;Wherein, level Four formation voltage is 300V, current density 60mA/cm2, and the chemical conversion time is 5 minutes.
Level Four Waste Acid From Hua Cheng Foil is placed in 40 DEG C of pure water solution and is cleaned 5 minutes.
Level Four Waste Acid From Hua Cheng Foil after cleaning is placed in 200 DEG C of burning piece furnace and is burnt piece 3 minutes.
In Pyatyi electrolytic bath, with the mixed solution of the boric acid solution of 85 DEG C of 8wt% and 1.5wt% ammonium hydroxide to piece is burnt after Level Four Waste Acid From Hua Cheng Foil carry out Pyatyi chemical conversion, obtain Pyatyi Waste Acid From Hua Cheng Foil;Wherein, formation voltage 420V, current density 60mA/ Cm2, chemical conversion time are 5 minutes.
In six grades of electrolytic baths, with the boric acid solution of 85 DEG C of 8wt% and the mixed solution of 1.5wt% ammonium hydroxide to Pyatyi Six grades of chemical conversions are carried out at foil, obtain six grades of Waste Acid From Hua Cheng Foils;Wherein, formation voltage 520V, current density 60mA/cm2, when chemical conversion Between be 5 minutes.
Six grades of Waste Acid From Hua Cheng Foils are impregnated in 60 DEG C of 8wt% phosphoric acid solution and are placed within 6 minutes in 40 DEG C of pure water solution clearly It washes 5 minutes.
Six grades of Waste Acid From Hua Cheng Foils after cleaning are placed in baking oven, are dried 3 minutes at 150 DEG C.
Performance test
Example 1,2 and the chemical conversion foil sample obtained of comparative example 1, using MIT-DA-Foldding Endurance Tester bending strength-testing machine, to measure its bending intensity.Use the non-Waste Acid From Hua Cheng Foil of total 40000 μ F of static capacity or more as pair Pole, using specific volume test loop device to test specific volume, test result is shown in Table 1.
Table 1
As can be seen that compared with prior art, being had using Waste Acid From Hua Cheng Foil made from production technology of the invention higher anti- Curved intensity and specific volume.
The embodiments described above only express several embodiments of the present invention, and the description thereof is more specific and detailed, but simultaneously It cannot therefore be construed as limiting the scope of the patent.It should be pointed out that coming for those of ordinary skill in the art It says, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to protection of the invention Range.

Claims (10)

1. a kind of production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil, comprising the following steps:
1) electrolytic etching treated aluminium foil is subjected to pre-treatment;
2) liquid spray is carried out to the aluminium foil after pre-treatment with level-one chemical solution and carries out level-one chemical conversion, obtain level-one chemical conversion Foil;Liquid spray is carried out to level-one Waste Acid From Hua Cheng Foil with second level chemical solution and carries out second level chemical conversion, obtains second level Waste Acid From Hua Cheng Foil;Use three-level Chemical solution carries out liquid spray to second level Waste Acid From Hua Cheng Foil and carries out three-level chemical conversion, obtains three-level Waste Acid From Hua Cheng Foil;With level Four chemical solution Liquid spray is carried out to three-level Waste Acid From Hua Cheng Foil and carries out level Four chemical conversion, obtains level Four Waste Acid From Hua Cheng Foil;
3) level Four Waste Acid From Hua Cheng Foil is placed in cleaning solution and is cleaned;
4) the level Four Waste Acid From Hua Cheng Foil after cleaning is placed in burning piece furnace and carries out burning piece;
5) Pyatyi chemical conversion is carried out to the level Four Waste Acid From Hua Cheng Foil after burning piece with Pyatyi chemical solution, obtains Pyatyi Waste Acid From Hua Cheng Foil;Changed with six grades Six grades of chemical conversions are carried out to Pyatyi Waste Acid From Hua Cheng Foil at solution, obtain six grades of Waste Acid From Hua Cheng Foils;
6) six grades of Waste Acid From Hua Cheng Foils are post-processed;
7) it after to six grades of Waste Acid From Hua Cheng Foils cleaning after post treatment, places it in dry in baking oven.
2. the production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil according to claim 1, it is characterised in that: institute in step 2) The spray flow for stating liquid spray is 20~100L/h, and spray time is 1~5 minute.
3. the production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil according to claim 2, it is characterised in that: step 2) is described Level-one chemical conversion, second level chemical conversion, three-level chemical conversion, level Four are melted into the formation voltage, 50~200mA/cm2 that 60~300V is respectively adopted Current density, chemical conversion time are 1~20 minute, the level-one chemical solution, second level chemical solution, three-level chemical solution, level Four Chemical solution is respectively the boric acid solution for 2wt%~8wt% that temperature is 80~95 DEG C.
4. the production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil according to claim 1, it is characterised in that: institute in step 4) The burning piece temperature stated is 100~400 DEG C.
5. the production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil according to claim 1, it is characterised in that: institute in step 5) It states Pyatyi chemical conversion and six grades is melted into the formation voltage of 300~600V is respectively adopted, 50~200mA/cm2 current density, when chemical conversion Between be 1~30 minute, the Pyatyi chemical solution, six grades of chemical solutions are respectively that temperature is 80~95 DEG C of 2wt%~8wt% Boric acid solution and 0.2wt%~3wt% ammonium hydroxide mixed solution.
6. the production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil according to claim 1, it is characterised in that: institute in step 1) The pretreatment process stated are as follows: soaked 5~20 minutes in the pure water for being 90 DEG C or more by electrolytic etching treated aluminium foil is placed in temperature.
7. the production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil according to claim 1, it is characterised in that: institute in step 3) State the pure water solution that cleaning solution is 40~90 DEG C.
8. the production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil according to claim 1, it is characterised in that: institute in step 6) State last handling process are as follows: six grades of Waste Acid From Hua Cheng Foils will be passed through in the phosphoric acid solution of 3wt%~8wt%, under conditions of 45~70 DEG C It impregnates 3~12 minutes.
9. the production technology of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil according to claim 1, it is characterised in that: step 7) is described Baking oven drying temperature be 80~200 DEG C.
10. using the aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil of the preparation of production technology described in any one claim of claim 1~9.
CN201711120018.5A 2017-11-14 2017-11-14 A kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technology Pending CN109786113A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711120018.5A CN109786113A (en) 2017-11-14 2017-11-14 A kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technology

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711120018.5A CN109786113A (en) 2017-11-14 2017-11-14 A kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technology

Publications (1)

Publication Number Publication Date
CN109786113A true CN109786113A (en) 2019-05-21

Family

ID=66493357

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711120018.5A Pending CN109786113A (en) 2017-11-14 2017-11-14 A kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technology

Country Status (1)

Country Link
CN (1) CN109786113A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110578163A (en) * 2019-10-21 2019-12-17 佛山科学技术学院 Manufacturing method of medium-pressure corrosion foil
CN110783108A (en) * 2019-10-18 2020-02-11 佛山科学技术学院 Method for manufacturing corrosion foil
CN113611539A (en) * 2021-07-13 2021-11-05 乳源县立东电子科技有限公司 Low-voltage soft-state corrosion anode aluminum foil and preparation method and application thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110783108A (en) * 2019-10-18 2020-02-11 佛山科学技术学院 Method for manufacturing corrosion foil
CN110578163A (en) * 2019-10-21 2019-12-17 佛山科学技术学院 Manufacturing method of medium-pressure corrosion foil
CN110578163B (en) * 2019-10-21 2021-08-24 佛山科学技术学院 Manufacturing method of medium-pressure corrosion foil
CN113611539A (en) * 2021-07-13 2021-11-05 乳源县立东电子科技有限公司 Low-voltage soft-state corrosion anode aluminum foil and preparation method and application thereof
CN113611539B (en) * 2021-07-13 2022-04-22 乳源县立东电子科技有限公司 Low-voltage soft-state corrosion anode aluminum foil and preparation method and application thereof

Similar Documents

Publication Publication Date Title
CN106653373B (en) A kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technology
CN109609991B (en) Formed foil, preparation method and application thereof
CN102709059B (en) Formation method for anode foil of intermediate-voltage aluminum electrolytic capacitor
CN105405658B (en) A kind of purely inorganic sour chemical synthesis technology of high-pressure bolt formula anode foil for aluminum electrolytic capacitor
CN105551805B (en) The middle processing method of medium-high voltage aluminum electrolytic capacitor electrode foil
KR102132004B1 (en) Pretreatment method to improve the pore generation density of electrode foil for aluminum electrolytic capacitors
CN101030487A (en) Production of electrolytic capacitor anode aluminum foil
CN109786113A (en) A kind of aluminium electrolutic capacitor Waste Acid From Hua Cheng Foil and its production technology
CN104078240B (en) Method for manufacturing anode foil of alternating current motor capacitor
KR102317276B1 (en) Method for manufacturing electrode foil for surface mount aluminum electrolytic capacitors
WO2022247364A1 (en) Method for preparing nano microporous structure aluminum electrode foil for automotive electronics
JP6768088B2 (en) Etching method of electrode foil for low-voltage aluminum electrolytic capacitors with low contact resistance
CN107488871B (en) The hair engaging aperture caustic solution of aluminium foil and the manufacturing method of etched foil
KR20140001991A (en) Manufacturing method for anode foil of aluminum electrolytic capacitor
WO2023056725A1 (en) Method for preparing corroded aluminum foil having high hole length consistency
CN101345137A (en) Anode foil corrosion technology of electrolytic capacitor
CN112080787B (en) Corrosion foil for aluminum electrolytic capacitor and preparation method thereof
CN104357886B (en) The method that mesohigh anode deposits disperse tin, zinc nucleus with high-purity aluminum foil surface chemistry
CN109554746B (en) Method for manufacturing high-pressure high-specific-volume corrosion foil
CN109859949A (en) A method of reducing medium-high pressure chemical foil leakage current
CN108335925A (en) A method of promoting mesohigh electric aluminum foil leakage current characteristic
CN104103428B (en) A kind of manufacture method of aluminium electrolutic capacitor high pressure high-dielectric formed foil
CN103590085A (en) Surface treatment method of aluminum spool for bonding wire production
CN105742067A (en) Aluminum foil production method capable of improving capacitance extraction rate of solid-state capacitor and decreasing leakage current of solid-state capacitor
CN108754594B (en) Method for power-on protection of semi-V cathode after medium-high voltage electronic aluminum foil hole corrosion

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20190521

WD01 Invention patent application deemed withdrawn after publication