USRE31743E - AC Etching of aluminum capacitor foil - Google Patents
AC Etching of aluminum capacitor foil Download PDFInfo
- Publication number
- USRE31743E USRE31743E US06/294,251 US29425181A USRE31743E US RE31743 E USRE31743 E US RE31743E US 29425181 A US29425181 A US 29425181A US RE31743 E USRE31743 E US RE31743E
- Authority
- US
- United States
- Prior art keywords
- foil
- liter
- aluminum
- iaddend
- iadd
- 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.)
- Expired - Lifetime
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- 239000011888 foil Substances 0.000 title claims abstract description 31
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 15
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 14
- 239000003990 capacitor Substances 0.000 title claims abstract description 9
- 238000005530 etching Methods 0.000 title claims description 11
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 30
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims abstract description 17
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims abstract description 10
- 229940085991 phosphate ion Drugs 0.000 claims abstract description 9
- 238000000034 method Methods 0.000 claims description 19
- 239000000654 additive Substances 0.000 claims description 5
- 230000000996 additive effect Effects 0.000 claims 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical group OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims 2
- 238000007743 anodising Methods 0.000 claims 2
- 238000000866 electrolytic etching Methods 0.000 claims 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 claims 2
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 claims 2
- 239000000243 solution Substances 0.000 claims 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims 1
- 239000007864 aqueous solution Substances 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 150000007522 mineralic acids Chemical class 0.000 claims 1
- UEZVMMHDMIWARA-UHFFFAOYSA-N Metaphosphoric acid Chemical compound OP(=O)=O UEZVMMHDMIWARA-UHFFFAOYSA-N 0.000 description 5
- 239000011148 porous material Substances 0.000 description 3
- 240000000073 Achillea millefolium Species 0.000 description 2
- 235000007754 Achillea millefolium Nutrition 0.000 description 2
- 101000956368 Trittame loki CRISP/Allergen/PR-1 Proteins 0.000 description 2
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000004254 Ammonium phosphate Substances 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- OEWPJYGHIFSDET-UHFFFAOYSA-K [Cl-].P(O)(O)(O)=O.Cl.[Al+3].[Cl-].[Cl-] Chemical compound [Cl-].P(O)(O)(O)=O.Cl.[Al+3].[Cl-].[Cl-] OEWPJYGHIFSDET-UHFFFAOYSA-K 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- -1 aluminum ion Chemical class 0.000 description 1
- 229910000148 ammonium phosphate Inorganic materials 0.000 description 1
- 235000019289 ammonium phosphates Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
Images
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
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F3/00—Electrolytic etching or polishing
- C25F3/02—Etching
- C25F3/04—Etching of light metals
Definitions
- This invention relates to the etching of aluminum foil for electrolytic capacitors, and in particular to a process utilizing alternating current and a chloride electrolyte bath containing phosphate ions.
- AC etching has been used to produce aluminum articles such as lithographic plates and capacitor foil. It also has been used to electropolish aluminum articles prior to metal plating.
- the prior art has discussed the difficulties in obtaining an even or uniform etch structure and has overcome these difficulties in a variety of ways, e.g., interrupting the etch process to apply protective coatings, carrying out the etch process in stages of differing degrees of aggressiveness, and using additives in the electrolyte bath to control pit size or to increase mechanical strength of the foil.
- Another problem has been to prevent the precipitation of aluminum hydroxide, formed during etching, on or into the etched surfaces.
- a process of etching aluminum capacitor foil utilizes AC current to give a uniform etch structure while maintaining the strength of the foil.
- the process also provides a greater etch pit density than prior art processes.
- the above results are accomplished by using an etchant solution containing hydrochloric acid, hydrated aluminum trichloride, and a phosphate ion source at 35° to 55° C. and alternating current of 20 to 40 Hz frequency.
- the concentration of the hydrochloric acid in the etchant is 0.7 to 2.0 M to provide strongly acidic conditions that prevent the formation and precipitation of aluminum hydroxide on the foil.
- the concentration of the hydrated aluminum trichloride is 0.2 to 0.5 M to prevent wide variations of aluminum ion concentration, especially with fresh etchant solution.
- the concentration of phosphate ion is 0.02 to 0.4 M to give the desired uniformity and etch density (number of pits/unit area of foil). It is postulated that the phosphate ion serves to passivate sites that have already been started so that etching will proceed at different sites, giving the desired etch density, rather than concentrating at started sites. More than 0.4 M phosphate ion was found to be detrimental, as it appears to cause excessive inhibition of new etch sites.
- the current density is maintained at 1.6 to 4 A/in 2 to provide the desired number of sites. If the current density is too low, i.e., below 1.6 A/in 2 , there will not be the desired number of sites; if too high, i.e., above 4 A/in 2 , the etch structure becomes fragile leading to a smooth, polished surface rather than an etched one. Foil is also thinned in the latter case.
- the frequency of the alternating current is maintained at 20 to 40 Hz as this frequency gives etched foil with optimum capacitance.
- the voltage, a function of current density and etch cell design is ⁇ 7 V. With a different cell design, the voltage will differ also.
- the temperature of the etchant solution is maintained at 35° to 55° C. to provide pores of suitable size and density. Lower temperatures result in fewer, larger pores while higher temperatures give more pores but narrower pits and lower capacitance. Etching time is 2 to 6 min.
- the sole FIGURE shows foil being etched by the process of the present invention.
- Aluminum foil 10 is passed over roller 20 into tank 30 containing the hydrochloric acid-aluminum chloride-phosphate etchant solution of the present invention. Electrodes 31, 32, 33, 34, 35, 36 and 37 are connected to an AC source (not shown). Foil 10 passes between electrodes 31 and 32 and under roller 21, thence between electrodes 32 and 33 and out of the etchant over roll 22, back into the etchant between electrodes 33 and 34, under roller 23, between electrodes 34 and 35, over roller 24, between electrodes 35 and 36, under roller 25 and finally between electrodes 36 and 37 out of tank 30 and over roller 26.
- This particular arrangement provides for a minimum number of electrodes as electrodes 31 and 32 form a pair as do 32 and 33, 33 and 34, 34 and 35, 35 and 36, and 36 and 37.
- a complete pass is defined as the path between the adjacent rolls that are out of the tank, i.e. between 20 and 22, 22 and 24, and 24 and 26.
- there are three complete passes utilizing a total of seven electrodes. More electrodes may be used for a greater number of passes per tank or other arrangements may be used.
- the rolls 21-25 are preferably the same size as the distance between electrodes and so arranged that the foil passes vertically between electrodes.
- the etched foil obtained by the method of the present invention has a metallic core, that gives good mechanical properties and low-temperature capacitance retention.
- soft foil of 99.99% purity was used.
- Hard foil can be etched by this process, as can foil of different purity, but satisfactory capacitance is obtained without resorting to hard foil.
- Capacitance per unit area is given in microfarads per square inch, ⁇ F/in 2 , and etch time in minutes.
- Foil 2.9 mil thick was etched at 30° C., at 30 Hz and 3 A/in 2 current density for 2.5 min in an etchant solution of 2.2 M hydrochloric acid, 0.6 M aluminum trichloride, and 0.4 M phosphoric acid. Higher hydrochloric acid and aluminum chloride concentrations gave less reproducible results. Average results are presented below.
- etching was carried out at 4 A/in 2 current density, 30 Hz, and 45° C. for 1.9 min using an etchant solution of 1.3 M hydrochloric acid, 0.36 M aluminum trichloride, and 0.2 M phosphoric acid. Average results on 2.9 mil foil are given below.
- This run was carried out at 20 Hz frequency, 2.8 A/in 2 current density, and 45° C. using an etchant solution of 1.4 M hydrochloric acid, 0.39 M aluminum trichloride, and 0.22 M phosphoric acid. Foil 2.9 mil thick was etched at two different etch times.
- the range of etchant solution composition and process variables that give the desired etching, as reflected by capacitance, is 0.7 to 2 M hydrochloric acid, 0.2 to 0.5 M aluminum trichloride, 0.02 to 0.4 M phosphate ion, 35° to 55° C., 20 to 40 Hz frequency and 1.6 to 4 amps/in 2 current density.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Power Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Microelectronics & Electronic Packaging (AREA)
- ing And Chemical Polishing (AREA)
Abstract
Aluminum electrolytic capacitor foil is etched in a bath containing 0.7 to 2.0 M hydrochloric acid, 0.2 to 0.5 M hydrated aluminum trichloride, and 0.02 to 0.4 M phosphate ion while subjected to the action of alternating current at 35° to 55° C.
Description
This invention relates to the etching of aluminum foil for electrolytic capacitors, and in particular to a process utilizing alternating current and a chloride electrolyte bath containing phosphate ions.
AC etching has been used to produce aluminum articles such as lithographic plates and capacitor foil. It also has been used to electropolish aluminum articles prior to metal plating.
The prior art has discussed the difficulties in obtaining an even or uniform etch structure and has overcome these difficulties in a variety of ways, e.g., interrupting the etch process to apply protective coatings, carrying out the etch process in stages of differing degrees of aggressiveness, and using additives in the electrolyte bath to control pit size or to increase mechanical strength of the foil. Another problem has been to prevent the precipitation of aluminum hydroxide, formed during etching, on or into the etched surfaces.
The resolution of these problems has led to processes in which the etch conditions are carefully controlled to provide the desired increase in surface area and, particularly for capacitor foil, little change in mechanical strength.
A process of etching aluminum capacitor foil utilizes AC current to give a uniform etch structure while maintaining the strength of the foil. The process also provides a greater etch pit density than prior art processes. The above results are accomplished by using an etchant solution containing hydrochloric acid, hydrated aluminum trichloride, and a phosphate ion source at 35° to 55° C. and alternating current of 20 to 40 Hz frequency.
The concentration of the hydrochloric acid in the etchant is 0.7 to 2.0 M to provide strongly acidic conditions that prevent the formation and precipitation of aluminum hydroxide on the foil. The concentration of the hydrated aluminum trichloride is 0.2 to 0.5 M to prevent wide variations of aluminum ion concentration, especially with fresh etchant solution. The concentration of phosphate ion is 0.02 to 0.4 M to give the desired uniformity and etch density (number of pits/unit area of foil). It is postulated that the phosphate ion serves to passivate sites that have already been started so that etching will proceed at different sites, giving the desired etch density, rather than concentrating at started sites. More than 0.4 M phosphate ion was found to be detrimental, as it appears to cause excessive inhibition of new etch sites.
The current density is maintained at 1.6 to 4 A/in2 to provide the desired number of sites. If the current density is too low, i.e., below 1.6 A/in2, there will not be the desired number of sites; if too high, i.e., above 4 A/in2, the etch structure becomes fragile leading to a smooth, polished surface rather than an etched one. Foil is also thinned in the latter case. The frequency of the alternating current is maintained at 20 to 40 Hz as this frequency gives etched foil with optimum capacitance. The voltage, a function of current density and etch cell design, is ±7 V. With a different cell design, the voltage will differ also.
The temperature of the etchant solution is maintained at 35° to 55° C. to provide pores of suitable size and density. Lower temperatures result in fewer, larger pores while higher temperatures give more pores but narrower pits and lower capacitance. Etching time is 2 to 6 min.
The sole FIGURE shows foil being etched by the process of the present invention.
This particular arrangement provides for a minimum number of electrodes as electrodes 31 and 32 form a pair as do 32 and 33, 33 and 34, 34 and 35, 35 and 36, and 36 and 37. A complete pass is defined as the path between the adjacent rolls that are out of the tank, i.e. between 20 and 22, 22 and 24, and 24 and 26. Hence, in the arrangement shown, there are three complete passes utilizing a total of seven electrodes. More electrodes may be used for a greater number of passes per tank or other arrangements may be used. The rolls 21-25 are preferably the same size as the distance between electrodes and so arranged that the foil passes vertically between electrodes.
The etched foil obtained by the method of the present invention has a metallic core, that gives good mechanical properties and low-temperature capacitance retention.
In the examples below, soft foil of 99.99% purity was used. Hard foil can be etched by this process, as can foil of different purity, but satisfactory capacitance is obtained without resorting to hard foil.
A series of runs were made using as etchant a solution of 1.5 M hydrochloric acid, 0.2 M aluminum chloride, and 0.02 M ammonium phosphate. The frequency of the alternating current was 45 Hz. Soft 2.9 mil aluminum foil was used; thickness refers to final thickness in mils. Capacitance per unit area (Cap) is given in microfarads per square inch, μF/in2, and etch time in minutes.
TABLE 1 ______________________________________ Temp. Wt-loss Thick- 30 V Sample Amps/in.sup.2 Time °C. % ness Cap ______________________________________ 1 2.03 2.5 62.5 29.9 2.6 36.8 2 2.03 3.0 62.5 36.7 2.6 46.0 3 3.05 1.8 63.0 29.3 2.5 32.7 4 3.05 2.0 63.0 33.1 2.5 39.6 5 1.02 6.0 60.0 31.7 2.1 20.0 ______________________________________
Another series of runs were made at a frequency of 30 Hz and a current density of 2.8 A/in2. The etchant solution was 1.4 M hydrochloric acid, 0.4 M aluminum trichloride, and 0.2 M phosphoric acid. Soft 3.3 mil foil was used, and thickness given is the final thickness. The other units are as given in Example 1.
TABLE 2 ______________________________________ Temp. Wt-loss Sample Time °C. % Thickness 30 V Cap ______________________________________ 1 2.7 44.5 29.2 3.15 71.2 2 3.0 44.5 31.7 3.10 64.8 3 3.3 44.0 37.5 3.05 81.5 ______________________________________
Foil 2.9 mil thick was etched at 30° C., at 30 Hz and 3 A/in2 current density for 2.5 min in an etchant solution of 2.2 M hydrochloric acid, 0.6 M aluminum trichloride, and 0.4 M phosphoric acid. Higher hydrochloric acid and aluminum chloride concentrations gave less reproducible results. Average results are presented below.
TABLE 3 ______________________________________ Thickness Wt-loss % 30 V Cap ______________________________________ 2.75 mil 27.1 68.7 ______________________________________
In this example, average results are presented for 2.9 mil thick foil etched at 70° C., 3.5 A/in2 current density, 30 Hz frequency for 2.2 min in an etchant solution of 0.75 M hydrochloric acid, 0.2 M aluminum trichloride, and 0.11 M phosphoric acid.
TABLE 4 ______________________________________ Thickness Wt-loss % 30 V Cap ______________________________________ 2.7 mil 30.5 53.7 ______________________________________
In this example, etching was carried out at 4 A/in2 current density, 30 Hz, and 45° C. for 1.9 min using an etchant solution of 1.3 M hydrochloric acid, 0.36 M aluminum trichloride, and 0.2 M phosphoric acid. Average results on 2.9 mil foil are given below.
TABLE 5 ______________________________________ Thickness Wt-loss % 30 V Cap ______________________________________ 2.7 mil 35.3 71.2 ______________________________________
This run was carried out at 20 Hz frequency, 2.8 A/in2 current density, and 45° C. using an etchant solution of 1.4 M hydrochloric acid, 0.39 M aluminum trichloride, and 0.22 M phosphoric acid. Foil 2.9 mil thick was etched at two different etch times.
TABLE 6 ______________________________________ Etch Time Thickness Wt-loss % 30 V Cap ______________________________________ 3 min 2.65 36.7 73.6 3.5 min 2.45 42.7 80.2 ______________________________________
The range of etchant solution composition and process variables that give the desired etching, as reflected by capacitance, is 0.7 to 2 M hydrochloric acid, 0.2 to 0.5 M aluminum trichloride, 0.02 to 0.4 M phosphate ion, 35° to 55° C., 20 to 40 Hz frequency and 1.6 to 4 amps/in2 current density.
Claims (4)
- frequency of the alternating current is 20 to 40 Hz..]. 3. A process according to claim .[.1.]. .Iadd.8 .Iaddend.wherein the concentration of said hydrochloric acid is 1.4 M, the concentration of said hydrated aluminum chloride is 0.4 M, the concentration of said phosphate ion is 0.2
- M, and said temperature is 45° C. 4. A process according to claim .[.1.]. .Iadd.8 .Iaddend.wherein the etching time is 2 to 6 minutes. .Iadd.5. In a method for producing electrodes for use in an aluminum electrolytic capacitor whose effective surface area is enlarged by electrochemically etching aluminum foil in an aqueous solution consisting essentially of hydrogen chloride and an additive capable of anodizing said aluminum foil with electric power supplied in alternating current, an improvement characterized in that the concentration of the hydrogen chloride in said solution is set at a range between 0.7N and 2N, the concentration of said additive is set at a range between 0.02 mole/liter and 0.4 mole/liter, the frequency of said alternating current power supply is ranging from 20 Hz to 40 Hz and its current density is ranging from 1.6 A/in2 to 4 A/in2, while the temperature of said solution is
- being maintained at 30° to 45° C. .Iaddend. .Iadd.6. A method as claimed in claim 5, further characterized in that said additive is selected from an inorganic acid capable of anodizing (forming an oxide protecting layer on the surface of) aluminum. .Iaddend. .Iadd.7. A method as claimed in claim 6, further characterized in that said additive is
- phosphoric acid. .Iaddend. .Iadd.8. A process for the electrolytic etching of aluminum electrolytic capacitor foil comprising passing the foil between electrodes supplied with alternating current in a bath consisting essentially of 0.7 to 2 moles/liter hydrochloric acid, 0.2 to 0.5 moles/liter hydrated aluminum trichloride, and 0.02 to 0.4 moles/liter phosphate ion at a temperature of 30° to 45° C. and an alternating current frequency of 20 to 40 Hz. .Iaddend. .Iadd.9. A process according to claim 1 wherein the anodic current density is 1.6 to 4 amps/in2. .Iaddend.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/294,251 USRE31743E (en) | 1980-09-15 | 1981-08-19 | AC Etching of aluminum capacitor foil |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/187,241 US4279714A (en) | 1980-09-15 | 1980-09-15 | AC Etching of aluminum capacitor |
US06/294,251 USRE31743E (en) | 1980-09-15 | 1981-08-19 | AC Etching of aluminum capacitor foil |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US06/187,241 Reissue US4279714A (en) | 1980-09-15 | 1980-09-15 | AC Etching of aluminum capacitor |
Publications (1)
Publication Number | Publication Date |
---|---|
USRE31743E true USRE31743E (en) | 1984-11-20 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US06/294,251 Expired - Lifetime USRE31743E (en) | 1980-09-15 | 1981-08-19 | AC Etching of aluminum capacitor foil |
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US (1) | USRE31743E (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
USRE32512E (en) | 1980-06-25 | 1987-09-29 | Matsushita Electric Industrial Co., Ltd. | Method for producing foil electrodes for electrolytic capacitor |
US20060098384A1 (en) * | 2002-11-08 | 2006-05-11 | Nippon Chemi-Con Corporation Tokyo Japan | Electrolytic capacitor |
US20060127566A1 (en) * | 2002-11-08 | 2006-06-15 | Nippon Chemi-Con Corporation | Electrolytic capacitor manufacturing method |
US20060152882A1 (en) * | 2002-11-08 | 2006-07-13 | Masayuki Takeda | Electrolytic capacitor |
US20060164791A1 (en) * | 2002-11-08 | 2006-07-27 | Masashi Ozawa | Electrolytic capacitor |
US20060250751A1 (en) * | 2002-11-08 | 2006-11-09 | Masashi Ozawa | Electrolyte for electrolytic capacitor and electrolytic capacitor containing the same |
US20140326595A1 (en) * | 2013-05-02 | 2014-11-06 | Chung Shan Institute of Science and Technology, Armaments Bureau, Ministry of National Defense | Roll-to-roll electrochemical polish apparatus |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3193485A (en) * | 1960-09-20 | 1965-07-06 | Plessey Co Ltd | Electrolytic treatment of aluminium for increasing the effective surface |
JPS4940537A (en) * | 1972-08-18 | 1974-04-16 | ||
US3887447A (en) * | 1971-07-09 | 1975-06-03 | Alcan Res & Dev | Process of electrograining aluminium |
JPS50159430A (en) * | 1974-06-14 | 1975-12-24 | ||
JPS5264659A (en) * | 1975-11-21 | 1977-05-28 | Nippon Chikudenki Kougiyou Kk | Method of etching aluminum foil for electrolytic capacitor |
JPS52133043A (en) * | 1976-04-30 | 1977-11-08 | Hitachi Denkaihaku Kenkyusho | Method of etching aluminum |
JPS52141444A (en) * | 1976-05-21 | 1977-11-25 | Hitachi Denkaihaku Kenkyusho | Method of etching aluminum |
US4276129A (en) * | 1980-06-25 | 1981-06-30 | Matsushita Electric Industrial Co., Ltd. | Method for producing foil electrodes for electrolytic capacitor |
US4297184A (en) * | 1980-02-19 | 1981-10-27 | United Chemi-Con, Inc. | Method of etching aluminum |
-
1981
- 1981-08-19 US US06/294,251 patent/USRE31743E/en not_active Expired - Lifetime
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3193485A (en) * | 1960-09-20 | 1965-07-06 | Plessey Co Ltd | Electrolytic treatment of aluminium for increasing the effective surface |
US3887447A (en) * | 1971-07-09 | 1975-06-03 | Alcan Res & Dev | Process of electrograining aluminium |
JPS4940537A (en) * | 1972-08-18 | 1974-04-16 | ||
JPS50159430A (en) * | 1974-06-14 | 1975-12-24 | ||
JPS5264659A (en) * | 1975-11-21 | 1977-05-28 | Nippon Chikudenki Kougiyou Kk | Method of etching aluminum foil for electrolytic capacitor |
JPS52133043A (en) * | 1976-04-30 | 1977-11-08 | Hitachi Denkaihaku Kenkyusho | Method of etching aluminum |
JPS52141444A (en) * | 1976-05-21 | 1977-11-25 | Hitachi Denkaihaku Kenkyusho | Method of etching aluminum |
US4297184A (en) * | 1980-02-19 | 1981-10-27 | United Chemi-Con, Inc. | Method of etching aluminum |
US4276129A (en) * | 1980-06-25 | 1981-06-30 | Matsushita Electric Industrial Co., Ltd. | Method for producing foil electrodes for electrolytic capacitor |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
USRE32512E (en) | 1980-06-25 | 1987-09-29 | Matsushita Electric Industrial Co., Ltd. | Method for producing foil electrodes for electrolytic capacitor |
US20060098384A1 (en) * | 2002-11-08 | 2006-05-11 | Nippon Chemi-Con Corporation Tokyo Japan | Electrolytic capacitor |
US20060127566A1 (en) * | 2002-11-08 | 2006-06-15 | Nippon Chemi-Con Corporation | Electrolytic capacitor manufacturing method |
US20060152882A1 (en) * | 2002-11-08 | 2006-07-13 | Masayuki Takeda | Electrolytic capacitor |
US20060164791A1 (en) * | 2002-11-08 | 2006-07-27 | Masashi Ozawa | Electrolytic capacitor |
US20060250751A1 (en) * | 2002-11-08 | 2006-11-09 | Masashi Ozawa | Electrolyte for electrolytic capacitor and electrolytic capacitor containing the same |
US7256983B2 (en) | 2002-11-08 | 2007-08-14 | Nippon Chemi-Con Corporation | Electrolytic capacitor |
US7262953B2 (en) * | 2002-11-08 | 2007-08-28 | Nippon Chemi-Con Corporation | Electrolytic capacitor |
US20080030926A1 (en) * | 2002-11-08 | 2008-02-07 | Masashi Ozawa | Electrolytic capacitor |
US7430108B2 (en) | 2002-11-08 | 2008-09-30 | Nippon Chemi-Con Corporation | Electrolyte for electrolytic capacitor and electrolytic capacitor containing the same |
US7492572B2 (en) | 2002-11-08 | 2009-02-17 | Nippon Chemi-Con Corporation | Electrolytic capacitor manufacturing method |
US20140326595A1 (en) * | 2013-05-02 | 2014-11-06 | Chung Shan Institute of Science and Technology, Armaments Bureau, Ministry of National Defense | Roll-to-roll electrochemical polish apparatus |
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Owner name: UNITED CHEMI-CON MANUFACTURING, INC., NORTH CAROLI Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:SPRAGUE ELECTRIC COMPANY;REEL/FRAME:006483/0442 Effective date: 19920903 |