WO2019085387A1 - 一种提高铝电解电容器用电极箔发孔密度的预处理方法 - Google Patents
一种提高铝电解电容器用电极箔发孔密度的预处理方法 Download PDFInfo
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- WO2019085387A1 WO2019085387A1 PCT/CN2018/081589 CN2018081589W WO2019085387A1 WO 2019085387 A1 WO2019085387 A1 WO 2019085387A1 CN 2018081589 W CN2018081589 W CN 2018081589W WO 2019085387 A1 WO2019085387 A1 WO 2019085387A1
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- aluminum foil
- minutes
- washing
- water
- washed
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- 239000011888 foil Substances 0.000 title claims abstract description 70
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 60
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 60
- 238000002203 pretreatment Methods 0.000 title claims abstract description 11
- 239000003990 capacitor Substances 0.000 title claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 238000004140 cleaning Methods 0.000 claims abstract description 44
- 238000005406 washing Methods 0.000 claims abstract description 40
- 238000011282 treatment Methods 0.000 claims abstract description 27
- 238000000034 method Methods 0.000 claims abstract description 16
- 238000001035 drying Methods 0.000 claims abstract description 13
- 239000000126 substance Substances 0.000 claims abstract description 11
- 239000011148 porous material Substances 0.000 claims abstract description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 27
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 24
- 229910017604 nitric acid Inorganic materials 0.000 claims description 24
- 239000008399 tap water Substances 0.000 claims description 23
- 235000020679 tap water Nutrition 0.000 claims description 23
- 238000005530 etching Methods 0.000 claims description 21
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 16
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 16
- 230000008569 process Effects 0.000 claims description 9
- ZNCPFRVNHGOPAG-UHFFFAOYSA-L sodium oxalate Chemical compound [Na+].[Na+].[O-]C(=O)C([O-])=O ZNCPFRVNHGOPAG-UHFFFAOYSA-L 0.000 claims description 9
- 229940039790 sodium oxalate Drugs 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 8
- 239000007921 spray Substances 0.000 claims description 7
- 238000009826 distribution Methods 0.000 abstract description 7
- 230000015572 biosynthetic process Effects 0.000 abstract description 2
- 239000012792 core layer Substances 0.000 abstract description 2
- 238000005260 corrosion Methods 0.000 description 9
- 230000007797 corrosion Effects 0.000 description 8
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000006056 electrooxidation reaction Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/048—Electrodes or formation of dielectric layers thereon characterised by their structure
- H01G9/055—Etched foil electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/042—Electrodes or formation of dielectric layers thereon characterised by the material
- H01G9/045—Electrodes or formation of dielectric layers thereon characterised by the material based on aluminium
Definitions
- the invention relates to an electrochemical corrosion method for a medium-high voltage anode foil for capacitors.
- the anode foil for medium and high voltage aluminum electrolytic capacitors generally generates a large number of tunnel holes on the surface of the aluminum foil by electrochemical etching to enlarge the effective surface area thereof to increase the specific capacitance of the capacitor.
- the electrode foil after corrosion has a certain tensile strength and bending performance.
- H 3 PO 4 is a medium-strong acid, which is highly susceptible to chemical corrosion reaction with aluminum foil.
- concentration or temperature of the treatment liquid is too low, the oxide film and oil stain on the surface of the aluminum foil cannot be completely removed.
- concentration or temperature is too high, the surface of the light foil will be Due to chemical corrosion, the thickness of the aluminum foil is reduced, which has a negative impact on the next step of electrochemical surface expansion corrosion, which is not conducive to the improvement of specific volume and the reduction of strength.
- Pretreatment using a 5 wt% phosphoric acid solution at a temperature of 40 ° C, the treatment time is controlled at 90 seconds;
- the etching solution is a mixture of 15 wt% sulfuric acid and 5 wt% hydrochloric acid, the temperature is 70 ° C, using direct current, the electric quantity is 35 C/cm 2 , and the current density is 0.5 A/cm 2 ;
- the etching solution is 5 wt% nitric acid, the temperature is 65 ° C, the direct current is used, the electric quantity is 45 C/cm 2 , and the current density is 0.1 A/cm 2 ;
- the cleaning solution is 8wt% nitric acid, the temperature is 65 ° C, and the cleaning time is 2 minutes;
- Pure water cleaning under normal temperature conditions, pure water spray water wash for 6 minutes;
- Drying Dry at 200 ° C for 2 minutes.
- the prepared anode foil 560VF capacity is as follows:
- the object of the present invention is to overcome the above deficiencies and to provide a pretreatment method for a medium-high voltage anode foil for an aluminum electrolytic capacitor having uniform pores, uniform pore length and good strength.
- the object of the present invention is achieved by the following technical solution: a pretreatment method for increasing the pore density of an electrode foil for an aluminum electrolytic capacitor, and the specific process is as follows:
- the aluminum foil is pretreated with 0.1-10 g/L sodium hydroxide solution at a temperature of 20-60 ° C, and the treatment time is controlled at 20-90 seconds;
- the aluminum foil is further pretreated with 0.1-10 g/L sodium oxalate solution at a temperature of 30-70 ° C, and the treatment time is controlled at 20-120 seconds;
- One-time water washing the aluminum foil after two pre-treatments is washed once, that is, under normal temperature conditions, using pure water for 1-3 minutes;
- the aluminum foil is vented with an etching solution, which is a mixture of 8-40 wt% sulfuric acid and 1-10 wt% hydrochloric acid, the temperature is 60-90 ° C, and the direct current is used, and the electric quantity is 30-60 C/cm. 2 , the current density is 0.4-1.5A/cm 2 ;
- an etching solution which is a mixture of 8-40 wt% sulfuric acid and 1-10 wt% hydrochloric acid, the temperature is 60-90 ° C, and the direct current is used, and the electric quantity is 30-60 C/cm. 2 , the current density is 0.4-1.5A/cm 2 ;
- Medium treatment the aluminum foil after the hole is processed in the middle, using 1-10 wt% of nitric acid, the temperature is 30-70 ° C, and the cleaning time is controlled to 1-10 minutes;
- the water-washed aluminum foil is reamed using an etching solution, the etching solution is 1-10 wt% of nitric acid, the temperature is 30-80 ° C, and the direct current is used, the electric quantity is 30-60 C/cm 2 , and the current density is 0.05. -0.5 A/cm 2 ;
- Chemical cleaning the washed aluminum foil is chemically cleaned with a cleaning solution, the cleaning solution is 1-10 wt% nitric acid, the temperature is 30-70 ° C, and the cleaning time is 1-10 minutes;
- the washed aluminum foil is washed four times, that is, under normal temperature conditions, washing with tap water for 1-3 minutes;
- the cleaned aluminum foil is dried at 100-300 ° C for a drying time of 1-5 minutes.
- the present invention has the advantage over the prior art that the present invention employs a stepwise approach.
- the first step is impregnated with a NaOH solution and the second step is impregnated with a sodium oxalate solution.
- the reaction between the dilute NaOH solution and the surface of the aluminum foil is relatively mild, and it can effectively remove the uneven oxide film and the oil stain layer on the surface of the aluminum foil; and the sodium oxalate has strong oxidizing property, and can form a uniform porous oxide film on the surface of the new aluminum foil.
- the surface corrosion of the sample is prevented from occurring, and the porous oxide film plays a very important role in the corrosion of the pores.
- the stepwise pretreatment method of the acid after the alkali is used to make the surface distribution of the aluminum foil more uniform.
- a method for preparing aluminum sulfate from waste foil production of electrode foil the specific steps are as follows:
- the aluminum foil is pretreated with 0.1-10g/L sodium hydroxide solution at a temperature of 20-60 ° C, the treatment time is controlled at 20-90 seconds; the second pretreatment: 0.1-10 g / L is used again.
- the sodium oxalate solution is subjected to secondary pretreatment of the aluminum foil at a temperature of 30-70 ° C, and the treatment time is controlled at 20-120 seconds; once water washing: the aluminum foil after two pretreatments is washed once, that is, under normal temperature conditions.
- hair hole the aluminum foil is vented with an etching solution, which is a mixture of 8-40 wt% sulfuric acid and 1-10 wt% hydrochloric acid, at a temperature of 60-90 ° C, using direct current , the electric quantity is 30-60C/cm 2 , the current density is 0.4-1.5A/cm 2 ;
- the middle treatment the aluminum foil after the hole is processed in the middle, using 1-10wt% nitric acid, the temperature is 30-70 ° C, cleaning Time control in 1-10 minutes; secondary water washing: the treated aluminum foil is washed twice, that is, under normal temperature conditions, washing with tap water for 1-3 minutes; reaming: refining the washed aluminum foil with an etching solution
- the corrosive liquid is 1-10 wt% of nitric acid, the temperature is 30-80 ° C, using direct current, electricity Of 30-60C / cm 2, current density of 0.05-0.5A / cm 2; washed three times
- One pretreatment using 0.5g/L sodium hydroxide solution, the temperature is 60 ° C, the treatment time is controlled at 60 seconds;
- the etching solution is a mixture of 15 wt% sulfuric acid and 5 wt% hydrochloric acid, the temperature is 70 ° C, using direct current, the electric quantity is 35 C/cm 2 , and the current density is 0.5 A/cm 2 ;
- the etching solution is 5 wt% nitric acid, the temperature is 65 ° C, the direct current is used, the electric quantity is 45 C/cm 2 , and the current density is 0.1 A/cm 2 ;
- the cleaning solution is 8wt% nitric acid, the temperature is 65 ° C, and the cleaning time is 2 minutes;
- Pure water cleaning under normal temperature conditions, pure water spray water wash for 6 minutes;
- Drying Dry at 200 ° C for 2 minutes.
- One pretreatment using 1g/L sodium hydroxide solution, the temperature is 55 ° C, the treatment time is controlled at 60 seconds;
- the etching solution is a mixture of 15 wt% sulfuric acid and 5 wt% hydrochloric acid, the temperature is 70 ° C, using direct current, the electric quantity is 35 C/cm 2 , and the current density is 0.5 A/cm 2 ;
- the etching solution is 5 wt% nitric acid, the temperature is 65 ° C, the direct current is used, the electric quantity is 45 C/cm 2 , and the current density is 0.1 A/cm 2 ;
- the cleaning solution is 8wt% nitric acid, the temperature is 65 ° C, and the cleaning time is 2 minutes;
- Pure water cleaning under normal temperature conditions, pure water spray water wash for 6 minutes;
- Drying Dry at 200 ° C for 2 minutes.
- One pretreatment using 3g / L sodium hydroxide solution, the temperature is 50 ° C, the treatment time is controlled at 40 seconds;
- the etching solution is a mixture of 15 wt% sulfuric acid and 5 wt% hydrochloric acid, the temperature is 70 ° C, using direct current, the electric quantity is 35 C/cm 2 , and the current density is 0.5 A/cm 2 ;
- the etching solution is 5 wt% nitric acid, the temperature is 65 ° C, the direct current is used, the electric quantity is 45 C/cm 2 , and the current density is 0.1 A/cm 2 ;
- the cleaning solution is 8wt% nitric acid, the temperature is 65 ° C, and the cleaning time is 2 minutes;
- Pure water cleaning under normal temperature conditions, pure water spray water wash for 6 minutes;
- Drying Dry at 200 ° C for 2 minutes.
- One pretreatment using 5g / L sodium hydroxide solution, the temperature is 50 ° C, the treatment time is controlled at 30 seconds;
- the etching solution is a mixture of 15 wt% sulfuric acid and 5 wt% hydrochloric acid, the temperature is 70 ° C, using direct current, the electric quantity is 35 C/cm 2 , and the current density is 0.5 A/cm 2 ;
- the etching solution is 5 wt% nitric acid, the temperature is 65 ° C, the direct current is used, the electric quantity is 45 C/cm 2 , and the current density is 0.1 A/cm 2 ;
- the cleaning solution is 8wt% nitric acid, the temperature is 65 ° C, and the cleaning time is 2 minutes;
- Pure water cleaning under normal temperature conditions, pure water spray water wash for 6 minutes;
- Drying Dry at 200 ° C for 2 minutes.
- the prepared anode foil 560VF capacity is as follows:
- the invention improves the uniformity of the surface etch pit distribution of the aluminum foil by improving the pretreatment condition, reduces the thinning amount of the aluminum foil, and finally obtains the electrode foil for the medium and high voltage aluminum electrolytic capacitor with uniform pore distribution, uniform pore length and uniform thickness of the residual core layer. After the formation, the capacity and strength have been greatly improved.
Landscapes
- Engineering & Computer Science (AREA)
- Power Engineering (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
- Chemical Treatment Of Metals (AREA)
- ing And Chemical Polishing (AREA)
Abstract
本发明公开了一种提高铝电解电容器用电极箔发孔密度的预处理方法,包括以下步骤:预处理、一次水洗、发孔处理、中处理、二次水洗、扩孔处理、三次水洗、化学清洗、四次水洗、干燥。本发明通过改善预处理条件提高了铝箔表面蚀坑分布的均匀性,降低了铝箔的减薄量,最终得到孔洞均匀分布、孔长一致、残芯层厚度均匀的中高压铝电解电容器用电极箔,化成后容量与强度均有较大提升。
Description
本发明涉及一种电容器用中高压阳极箔的电化学腐蚀方法。
中高压铝电解电容器用阳极箔一般通过电化学腐蚀的方法在铝箔表面生成大量的隧道孔以扩大其有效表面积,以提高电容器比电容。为了保证电极箔具有必要的卷绕性能,腐蚀后的电极箔还要有一定的拉伸强度和折弯性能。此外,为了使电极箔综合性能更优化,在腐蚀过程中,需要提高铝箔表面蚀孔分布的均匀性,减少铝箔表面的自腐蚀现象。
由于铝箔表面存在一层致密的氧化膜Al
2O
3,它的厚度及分布的均匀性,对下道工艺中铝箔腐蚀发孔中蚀孔的萌生有较大影响作用。传统的预处理方法是使用H
3PO
4。H
3PO
4属于中强酸,极易与铝箔发生化学腐蚀反应,当处理液浓度或温度过低时,不能完全除去铝箔表面的氧化膜和油污;而浓度或温度过高时,光箔表面会因化学腐蚀而发生销蚀,铝箔厚度减薄,给下步电化学扩面腐蚀带来负面影响,不利于比容的提升,也带来强度的降低。
预处理:使用5wt%的磷酸溶液,温度为40℃,处理时间控制在90秒;
一次水洗:常温条件下,纯水洗2分钟;
发孔:腐蚀液为15wt%的硫酸和5wt%的盐酸混合液,温度为70℃,采用直流电,电量为35C/cm
2,电流密度为0.5A/cm
2;
中处理:7wt%的硝酸,温度为55℃,清洗时间控制在2分钟;
二次水洗:常温条件下,自来水洗3分钟;
扩孔:腐蚀液为5wt%的硝酸,温度为65℃,采用直流电,电量为45C/cm
2,电流密度为0.1A/cm
2;
三次水洗:常温条件下,自来水洗3分钟;
化学清洗:清洗液为8wt%的硝酸,温度为65℃,清洗时间为2分钟;
四次水洗:常温条件下,自来水洗3分钟;
纯水清洗:常温条件下,纯水喷淋水洗6分钟;
干燥:200℃条件下,干燥2分钟。
制备得到的阳极箔560VF容量如下:
发明内容:
本发明的目的是为了克服以上的不足,提供一种孔洞均匀、孔长一致、强度良好的铝电解电容器用中高压阳极箔的预处理方法。
本发明的目的通过以下技术方案来实现:一种提高铝电解电容器用电极箔发孔密度的预处理方法,具体过程如下:
一次预处理:使用0.1-10g/L的氢氧化钠溶液对铝箔进行一次预处理,温度为20-60℃,处理时间控制在20-90秒;
二次预处理:再使用0.1-10g/L的草酸钠溶液对铝箔进行二次预处理,温度为30-70℃,处理时间控制在20-120秒;
一次水洗:将经过两次预处理后的铝箔进行一次水洗,即在常温条件下,使用纯水洗1-3分钟;
发孔:将铝箔使用腐蚀液进行发孔,所述腐蚀液为8-40wt%的硫酸和1-10wt%的盐酸混合液,温度为60-90℃,采用直流电,电量为30-60C/cm
2,电流密度为0.4-1.5A/cm
2;
中处理:将发孔之后的铝箔进行中处理,采用1-10wt%的硝酸,温度为30-70℃,清洗时间控制在1-10分钟;
二次水洗:将中处理后的铝箔进行二次水洗,即常温条件下,采用自来水洗1-3分钟;
扩孔:将水洗后的铝箔使用腐蚀液进行扩孔,所述腐蚀液为1-10wt%的硝酸,温度为30-80℃,采用直流电,电量为30-60C/cm
2,电流密度为0.05-0.5A/cm
2;
三次水洗:将扩孔后的铝箔进行三次水洗,即常温条件下,采用自来水洗1-3分钟;
化学清洗:将水洗后的铝箔采用清洗液进行化学清洗,所述清洗液为1-10wt%的硝酸,温度为30-70℃,清洗时间为1-10分钟;
四次水洗:将清洗后的铝箔进行四次水洗,即常温条件下,采用自来水洗1-3分钟;
纯水清洗:最后将铝箔进行纯水清洗,即常温条件下,采用纯水喷淋水洗5-10分钟;
干燥:将清洗过后的铝箔在100-300℃条件下进行干燥,干燥时间为1-5分钟。
本发明与现有技术相比具有以下优点:本发明采用分步法。第一步使用NaOH溶液浸渍,第二步使用草酸钠溶液浸渍。稀的NaOH溶液与铝箔表面反应比较柔和,它能有效去除铝箔表面不均匀的氧化膜和油污层;而草 酸钠具有较强的氧化性,能在新的铝箔表面形成均匀的多孔性氧化膜,防止了试样表面销蚀发生,同时这种多孔氧化膜在发孔腐蚀中又起着非常重要的作用。使用这种先碱后酸的分步预处理方法,使铝箔表面蚀坑分布更加均匀。
为使本发明实施例的目的、技术方案和优点更加清楚,下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。在本发明的一种实施方式中描述的元素和特征可以与一个或更多个其它实施方式中示出的元素和特征相结合。应当注意,为了清楚的目的,说明中省略了与本发明无关的、本领域普通技术人员已知的部件和处理的表示和描述。基于本发明中的实施例,本领域普通技术人员在没有付出创造性劳动的前提下所获得的所有其他实施例,都属于本发明保护的范围。
一种从电极箔生产废酸中制取硫酸铝的方法,具体步骤如下:
一次预处理:使用0.1-10g/L的氢氧化钠溶液对铝箔进行一次预处理,温度为20-60℃,处理时间控制在20-90秒;二次预处理:再使用0.1-10g/L的草酸钠溶液对铝箔进行二次预处理,温度为30-70℃,处理时间控制在20-120秒;一次水洗:将经过两次预处理后的铝箔进行一次水洗,即在常温条件下,使用纯水洗1-3分钟;发孔:将铝箔使用腐蚀液进行发孔,所述腐蚀液为8-40wt%的硫酸和1-10wt%的盐酸混合液,温度为60-90℃,采用直流电,电量为30-60C/cm
2,电流密度为0.4-1.5A/cm
2;中处理:将发孔之后的铝箔进行中处理,采用1-10wt%的硝酸,温度为30-70℃,清洗时间控制在1-10分钟;二次水洗:将中处理后的铝箔进行二次 水洗,即常温条件下,采用自来水洗1-3分钟;扩孔:将水洗后的铝箔使用腐蚀液进行扩孔,所述腐蚀液为1-10wt%的硝酸,温度为30-80℃,采用直流电,电量为30-60C/cm
2,电流密度为0.05-0.5A/cm
2;三次水洗:将扩孔后的铝箔进行三次水洗,即常温条件下,采用自来水洗1-3分钟;化学清洗:将水洗后的铝箔采用清洗液进行化学清洗,所述清洗液为1-10wt%的硝酸,温度为30-70℃,清洗时间为1-10分钟;四次水洗:将清洗后的铝箔进行四次水洗,即常温条件下,采用自来水洗1-3分钟;纯水清洗:最后将铝箔进行纯水清洗,即常温条件下,采用纯水喷淋水洗5-10分钟;干燥:将清洗过后的铝箔在100-300℃条件下进行干燥,干燥时间为1-5分钟。
实施例1:
一次预处理:使用0.5g/L的氢氧化钠溶液,温度为60℃,处理时间控制在60秒;
二次预处理:使用1g/L的草酸钠溶液,温度为55℃,处理时间控制在60秒;
一次水洗:常温条件下,纯水洗2分钟;
发孔:腐蚀液为15wt%的硫酸和5wt%的盐酸混合液,温度为70℃,采用直流电,电量为35C/cm
2,电流密度为0.5A/cm
2;
中处理:7wt%的硝酸,温度为55℃,清洗时间控制在2分钟;
二次水洗:常温条件下,自来水洗3分钟;
扩孔:腐蚀液为5wt%的硝酸,温度为65℃,采用直流电,电量为45C/cm
2,电流密度为0.1A/cm
2;
三次水洗:常温条件下,自来水洗3分钟;
化学清洗:清洗液为8wt%的硝酸,温度为65℃,清洗时间为2分钟;
四次水洗:常温条件下,自来水洗3分钟;
纯水清洗:常温条件下,纯水喷淋水洗6分钟;
干燥:200℃条件下,干燥2分钟。
实施例2:
一次预处理:使用1g/L的氢氧化钠溶液,温度为55℃,处理时间控制在60秒;
二次预处理:使用4g/L的草酸钠溶液,温度为45℃,处理时间控制在40秒;
一次水洗:常温条件下,纯水洗2分钟;
发孔:腐蚀液为15wt%的硫酸和5wt%的盐酸混合液,温度为70℃,采用直流电,电量为35C/cm
2,电流密度为0.5A/cm
2;
中处理:7wt%的硝酸,温度为55℃,清洗时间控制在2分钟;
二次水洗:常温条件下,自来水洗3分钟;
扩孔:腐蚀液为5wt%的硝酸,温度为65℃,采用直流电,电量为45C/cm
2,电流密度为0.1A/cm
2;
三次水洗:常温条件下,自来水洗3分钟;
化学清洗:清洗液为8wt%的硝酸,温度为65℃,清洗时间为2分钟;
四次水洗:常温条件下,自来水洗3分钟;
纯水清洗:常温条件下,纯水喷淋水洗6分钟;
干燥:200℃条件下,干燥2分钟。
实施例3:
一次预处理:使用3g/L的氢氧化钠溶液,温度为50℃,处理时间控制 在40秒;
二次预处理:使用1g/L的草酸钠溶液,温度为60℃,处理时间控制在40秒;
一次水洗:常温条件下,纯水洗2分钟;
发孔:腐蚀液为15wt%的硫酸和5wt%的盐酸混合液,温度为70℃,采用直流电,电量为35C/cm
2,电流密度为0.5A/cm
2;
中处理:7wt%的硝酸,温度为55℃,清洗时间控制在2分钟;
二次水洗:常温条件下,自来水洗3分钟;
扩孔:腐蚀液为5wt%的硝酸,温度为65℃,采用直流电,电量为45C/cm
2,电流密度为0.1A/cm
2;
三次水洗:常温条件下,自来水洗3分钟;
化学清洗:清洗液为8wt%的硝酸,温度为65℃,清洗时间为2分钟;
四次水洗:常温条件下,自来水洗3分钟;
纯水清洗:常温条件下,纯水喷淋水洗6分钟;
干燥:200℃条件下,干燥2分钟。
实施例4:
一次预处理:使用5g/L的氢氧化钠溶液,温度为50℃,处理时间控制在30秒;
二次预处理:使用0.5g/L的草酸钠溶液,温度为60℃,处理时间控制在60秒;
一次水洗:常温条件下,纯水洗2分钟;
发孔:腐蚀液为15wt%的硫酸和5wt%的盐酸混合液,温度为70℃,采用直流电,电量为35C/cm
2,电流密度为0.5A/cm
2;
中处理:7wt%的硝酸,温度为55℃,清洗时间控制在2分钟;
二次水洗:常温条件下,自来水洗3分钟;
扩孔:腐蚀液为5wt%的硝酸,温度为65℃,采用直流电,电量为45C/cm
2,电流密度为0.1A/cm
2;
三次水洗:常温条件下,自来水洗3分钟;
化学清洗:清洗液为8wt%的硝酸,温度为65℃,清洗时间为2分钟;
四次水洗:常温条件下,自来水洗3分钟;
纯水清洗:常温条件下,纯水喷淋水洗6分钟;
干燥:200℃条件下,干燥2分钟。
制备得到的阳极箔560VF容量如下:
此结果与背景技术中的结果对比可以看出,采用本发明腐蚀工艺产出的腐蚀电极箔化成后容量与强度均有提升。
本发明通过改善预处理条件提高了铝箔表面蚀坑分布的均匀性,降低了铝箔的减薄量,最终得到孔洞均匀分布、孔长一致、残芯层厚度均匀的中高压铝电解电容器用电极箔,化成后容量与强度均有较大提升。
最后应说明的是:虽然以上已经详细说明了本发明及其优点,但是应当理解在不超出由所附的权利要求所限定的本发明的精神和范围的情况下可以进行各种改变、替代和变换。而且,本发明的范围不仅限于说明书所 描述的过程、设备、手段、方法和步骤的具体实施例。本领域内的普通技术人员从本发明的公开内容将容易理解,根据本发明可以使用执行与在此所述的相应实施例基本相同的功能或者获得与其基本相同的结果的、现有和将来要被开发的过程、设备、手段、方法或者步骤。因此,所附的权利要求旨在在它们的范围内包括这样的过程、设备、手段、方法或者步骤。
Claims (1)
- 一种提高铝电解电容器用电极箔发孔密度的预处理方法,其特征在于:具体过程如下:一次预处理:使用0.1-10g/L的氢氧化钠溶液对铝箔进行一次预处理,温度为20-60℃,处理时间控制在20-90秒;二次预处理:再使用0.1-10g/L的草酸钠溶液对铝箔进行二次预处理,温度为30-70℃,处理时间控制在20-120秒;一次水洗:将经过两次预处理后的铝箔进行一次水洗,即在常温条件下,使用纯水洗1-3分钟;发孔:将铝箔使用腐蚀液进行发孔,所述腐蚀液为8-40wt%的硫酸和1-10wt%的盐酸混合液,温度为60-90℃,采用直流电,电量为30-60C/cm 2,电流密度为0.4-1.5A/cm 2;中处理:将发孔之后的铝箔进行中处理,采用1-10wt%的硝酸,温度为30-70℃,清洗时间控制在1-10分钟;二次水洗:将中处理后的铝箔进行二次水洗,即常温条件下,采用自来水洗1-3分钟;扩孔:将水洗后的铝箔使用腐蚀液进行扩孔,所述腐蚀液为1-10wt%的硝酸,温度为30-80℃,采用直流电,电量为30-60C/cm 2,电流密度为0.05-0.5A/cm 2;三次水洗:将扩孔后的铝箔进行三次水洗,即常温条件下,采用自来水洗1-3分钟;化学清洗:将水洗后的铝箔采用清洗液进行化学清洗,所述清洗液为1-10wt%的硝酸,温度为30-70℃,清洗时间为1-10分钟;四次水洗:将清洗后的铝箔进行四次水洗,即常温条件下,采用自来水洗1-3分钟;纯水清洗:最后将铝箔进行纯水清洗,即常温条件下,采用纯水喷淋水洗5-10分钟;干燥:将清洗过后的铝箔在100-300℃条件下进行干燥,干燥时间为1-5分钟。
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