JP2014214342A - Method for forming oxidized film - Google Patents
Method for forming oxidized film Download PDFInfo
- Publication number
- JP2014214342A JP2014214342A JP2013092178A JP2013092178A JP2014214342A JP 2014214342 A JP2014214342 A JP 2014214342A JP 2013092178 A JP2013092178 A JP 2013092178A JP 2013092178 A JP2013092178 A JP 2013092178A JP 2014214342 A JP2014214342 A JP 2014214342A
- Authority
- JP
- Japan
- Prior art keywords
- voltage
- oxide film
- constant
- forming
- treatment
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 62
- 239000000463 material Substances 0.000 claims abstract description 17
- 230000003647 oxidation Effects 0.000 claims abstract description 12
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 12
- 229910000838 Al alloy Inorganic materials 0.000 claims abstract description 11
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 8
- 239000012670 alkaline solution Substances 0.000 claims description 5
- 238000007743 anodising Methods 0.000 claims description 4
- 230000003247 decreasing effect Effects 0.000 claims description 4
- 238000005260 corrosion Methods 0.000 abstract description 11
- 230000007797 corrosion Effects 0.000 abstract description 11
- 238000009413 insulation Methods 0.000 abstract description 4
- 238000005530 etching Methods 0.000 abstract description 3
- 239000002585 base Substances 0.000 abstract 2
- 239000003513 alkali Substances 0.000 abstract 1
- 230000000052 comparative effect Effects 0.000 description 13
- 239000010407 anodic oxide Substances 0.000 description 4
- 239000008151 electrolyte solution Substances 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000004888 barrier function Effects 0.000 description 3
- 229910052710 silicon Inorganic materials 0.000 description 3
- 239000010703 silicon Substances 0.000 description 3
- 239000004115 Sodium Silicate Substances 0.000 description 2
- 238000002048 anodisation reaction Methods 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 238000004512 die casting Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000001488 sodium phosphate Substances 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 229910052911 sodium silicate Inorganic materials 0.000 description 2
- 238000004381 surface treatment Methods 0.000 description 2
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 2
- 229910000406 trisodium phosphate Inorganic materials 0.000 description 2
- 235000019801 trisodium phosphate Nutrition 0.000 description 2
- 229910021364 Al-Si alloy Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 description 1
- -1 and the like Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910000403 monosodium phosphate Inorganic materials 0.000 description 1
- 235000019799 monosodium phosphate Nutrition 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 235000015424 sodium Nutrition 0.000 description 1
- 229910001388 sodium aluminate Inorganic materials 0.000 description 1
- AJPJDKMHJJGVTQ-UHFFFAOYSA-M sodium dihydrogen phosphate Chemical compound [Na+].OP(O)([O-])=O AJPJDKMHJJGVTQ-UHFFFAOYSA-M 0.000 description 1
- FQENQNTWSFEDLI-UHFFFAOYSA-J sodium diphosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])([O-])=O FQENQNTWSFEDLI-UHFFFAOYSA-J 0.000 description 1
- 235000019795 sodium metasilicate Nutrition 0.000 description 1
- 235000019832 sodium triphosphate Nutrition 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/02—Anodisation
- C25D11/04—Anodisation of aluminium or alloys based thereon
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/02—Anodisation
- C25D11/04—Anodisation of aluminium or alloys based thereon
- C25D11/06—Anodisation of aluminium or alloys based thereon characterised by the electrolytes used
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Other Surface Treatments For Metallic Materials (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
Abstract
Description
高い絶縁性と耐食性を必要とし、真空装置で使うアルミニウム又はアルミニウム合金の表面処理、アノード酸化処理による酸化皮膜の形成方法に関するものである。 The present invention relates to a method for forming an oxide film by surface treatment or anodic oxidation treatment of aluminum or aluminum alloy which requires high insulation and corrosion resistance and is used in a vacuum apparatus.
アルミニウム又はアルミニウム合金から構成された母材をアルカリ溶液中に浸漬して、火花放電を伴うアノード酸化処理を行うことにより、母材表面に酸化皮膜を形成するために、一定の電流密度の電流を流しながら母材の表面のアノード酸化皮膜を成長させ、その後、目標とする電圧（第１の電圧）まで到達したら処理を終了することが一般的に行われている。
この方法で形成される皮膜構造は粗であり、耐電圧性、耐食性に問題があった。これを改善する方法として、第１の電圧に到達した後、第１の電圧よりも低い第２の電圧まで電圧を下降させ、電圧を維持した状態で処理を継続する方法を、出願人は先に提案している（特許文献１）。
しかしながら、同文献に開示される方法においては、電流密度を監視して所定の値となるまで定電圧処理を行うものであるが、実際には、形成された膜が絶縁破壊される場合もある。このため、膜質自体が安定したものとならず、高温雰囲気で使用されるＣＶＤ装置や、強腐食性ガスを使うエッチング装置等の部材として使用される部材の表面処理としては、絶縁性や耐腐食性という観点からすれば劣るものであった。また、上記定電圧処理は、電力量が嵩むという問題もあった。
In order to form an oxide film on the surface of the base material by immersing a base material composed of aluminum or an aluminum alloy in an alkaline solution and performing an anodic oxidation treatment with spark discharge, a current having a constant current density is applied. In general, the anodic oxide film on the surface of the base material is grown while flowing, and then the processing is terminated when the target voltage (first voltage) is reached.
The film structure formed by this method was rough, and there were problems with voltage resistance and corrosion resistance. As a method for improving this, after the first voltage is reached, the applicant decreases the voltage to a second voltage lower than the first voltage and continues the processing while maintaining the voltage. (Patent Document 1).
However, in the method disclosed in this document, the current density is monitored and constant voltage processing is performed until a predetermined value is reached. However, actually, the formed film may be broken down. . For this reason, the film quality itself does not become stable, and as a surface treatment of a member used as a member of a CVD apparatus used in a high temperature atmosphere or an etching apparatus using a strong corrosive gas, insulation or corrosion resistance is used. It was inferior from the viewpoint of sex. In addition, the constant voltage process has a problem that the amount of electric power increases.
本発明は、高温雰囲気で使用されるＣＶＤ装置や、強腐食性ガスを使用するエッチング装置を構成するアルミニウム又はアルミニウム合金に、絶縁性及び耐腐食性に優れたアノード酸化皮膜を形成する方法を提供する。 The present invention provides a method for forming an anodic oxide film excellent in insulation and corrosion resistance on aluminum or aluminum alloy constituting a CVD apparatus used in a high temperature atmosphere or an etching apparatus using a strong corrosive gas. To do.
本発明のアノード酸化皮膜の形成方法は、請求項１記載の通り、アルミニウム又はアルミニウム合金から構成された母材をアルカリ溶液中に浸漬して、火花放電を伴うアノード酸化処理を行うことにより、前記母材表面に酸化皮膜を形成する方法であって、２００Ｖ以上の第１の電圧まで定電流密度でアノード酸化処理する工程Ａと、工程Ａの第１の電圧による定電圧処理を行わずに、第１の電圧から、第１の電圧よりも低い電圧の第２の電圧まで、所定の時間で線形又は段階的に電圧を下降させて、前記アノード酸化処理を行う工程Ｂと、第２の電圧で、定電圧処理を行う工程Ｃと、を行うことを特徴とする。
請求項２記載の発明は、請求項１において、工程Ｂと工程Ｃとの間に、第２の電圧から第１の電圧まで電圧を上げる工程Ｂ’を行い、工程Ｂ及び工程Ｂ’を１組の工程とし、この１組の工程を、工程Ａの後に複数回繰り返し行うことを特徴とする。
請求項３記載の発明は、請求項１において、前記段階的に電圧を下降させる場合に、下降した電圧は、少なくとも３０秒以上保持されることを特徴とする。
請求項４記載の発明は、請求項１乃至３の何れか１項において、第２の電圧は、第１の電圧の０．７０倍〜０．９９倍であることを特徴とする。
The method for forming an anodic oxide film according to the present invention includes the step of immersing a base material composed of aluminum or an aluminum alloy in an alkaline solution and performing an anodic oxidation treatment with spark discharge as described in
The invention described in
According to a third aspect of the present invention, in the first aspect, when the voltage is lowered stepwise, the lowered voltage is held for at least 30 seconds.
According to a fourth aspect of the present invention, in any one of the first to third aspects, the second voltage is 0.70 to 0.99 times the first voltage.
本発明によれば、火花放電を伴うアノード酸化処理において、２００Ｖ以上の第１の電圧まで定電流密度で処理を行った後に、第１の電圧による定電圧処理を行わずに、第１電圧から第２の電圧に時間をかけて、線形又は段階的に電圧を下降させるので、第２の電圧では絶縁破壊されないが、第２の電圧よりも高く第１の電圧では絶縁破壊されるような、弱い部分を十分に修復し、より高い耐電圧、耐食性の酸化皮膜を得ることが可能になる。
第１の電圧と第２の電圧の間の電圧変化を複数回繰り返すことで、膜の修復をより確実に行えるのでより高い耐電圧、耐食性の酸化皮膜を得ることが可能になる。
According to the present invention, in the anodic oxidation process with spark discharge, after performing the process at a constant current density up to a first voltage of 200 V or more, the first voltage is changed without performing the constant voltage process with the first voltage. Since the voltage is lowered linearly or stepwise over time with the second voltage, it is not broken down at the second voltage, but is broken down at the first voltage higher than the second voltage, It is possible to sufficiently repair the weak part and obtain an oxide film with higher withstand voltage and corrosion resistance.
By repeating the voltage change between the first voltage and the second voltage a plurality of times, the film can be repaired more reliably, so that an oxide film with higher withstand voltage and corrosion resistance can be obtained.
本発明において使用するアルカリ溶液の電解液の例としては、りん酸水素二ナトリウム、トリポリりん酸ナトリウム、りん酸二水素ナトリウム、ウルトラポリりん酸ナトリウム、ケイ酸ナトリウム、水酸化カリウム、二リン酸ナトリウム、リン酸三ナトリウム、アルミン酸ナトリウム、メタケイ酸ナトリウム及び水酸化ナトリウム等の中の１種類又はこれらの中の混合物を、水に溶解させたものを用いることができる。 Examples of the alkaline solution electrolyte used in the present invention include disodium hydrogen phosphate, sodium tripolyphosphate, sodium dihydrogen phosphate, sodium ultrapolyphosphate, sodium silicate, potassium hydroxide, sodium diphosphate. , Trisodium phosphate, sodium aluminate, sodium metasilicate, sodium hydroxide, and the like, or a mixture thereof can be used.
また、母材としては、アルミニウム又はアルミニウム合金を使用する。アルミニウム合金の鋳物材料、ダイキャスト材料はシリコンを代表として、一般的に含有されている元素が多く、ポーラス型アノード酸化皮膜が形成し難いといわれている。
本発明によれば、このようなシリコンが多い鋳物、ダイキャストでも耐食性良好な皮膜を形成することができる。また、展伸材の中でもＡｌ−Ｓｉ合金の４０００番系の処理も同様な理由でポーラス型アノード酸化処理の耐食性は悪いが、本発明によれば、良好な酸化皮膜が形成できる。シリコンが析出していないような展伸材、１０００番〜３０００番、５０００番から７０００番台のアルミニウム合金についても複雑形状の場合や１００℃以上の高温になる場合には効果がある。
Further, aluminum or an aluminum alloy is used as the base material. Aluminum alloy casting materials and die-casting materials, typically silicon, contain many elements in general, and it is said that it is difficult to form a porous anodic oxide film.
According to the present invention, it is possible to form a coating film with good corrosion resistance even in such a casting or die-casting with a lot of silicon. Further, among the wrought materials, the No. 4000 series treatment of the Al—Si alloy has a poor corrosion resistance due to the same reason, but according to the present invention, a good oxide film can be formed. The wrought material, in which silicon is not precipitated, and aluminum alloys in the 1000th to 3000th, 5000th to 7000th range, are also effective in the case of a complicated shape or a high temperature of 100 ° C. or higher.
本発明では、上記した母材を、アルカリ溶液中に浸漬して、火花放電を伴うアノード酸化処理を行うが、その際、２００Ｖ以上の第１の電圧まで定電流密度で行う工程Ａと、工程Ａの第１の電圧による定電圧処理を行わずに、第１の電圧から、第１の電圧よりも低い電圧の第２の電圧まで、所定の時間で線形又は段階的に電圧を下降させて、前記アノード酸化処理を行う工程Ｂと、第２の電圧で、定電圧処理を行う工程Ｃと、を行うことを含む。
工程Ａでは、第１の電圧による処理時間は、２００Ｖ以上の第１の電圧となるまで継続する。
第１の電圧の処理開始時の電流密度としては、１Ａ／ｄｍ２〜２０Ａ／ｄｍ２の範囲とすることが好ましい。１Ａ／ｄｍ２未満であると、電圧が上がらず放電しないことがあり、２０Ａ／ｄｍ２を超えると電圧が高くなり形成された膜が放電により破壊され皮膜構造が粗くなり耐食性が悪化するからである。
In the present invention, the above-described base material is immersed in an alkaline solution and anodizing with spark discharge is performed. At this time, the step A and the step A are performed at a constant current density up to a first voltage of 200 V or higher. A voltage is decreased linearly or stepwise in a predetermined time from the first voltage to the second voltage lower than the first voltage without performing the constant voltage processing with the first voltage of A. , Performing the anodizing process B and the second voltage performing the constant voltage process C.
In the process A, the processing time by the first voltage continues until the first voltage becomes 200 V or higher.
The current density at the start of the first voltage treatment is preferably in the range of 1 A / dm 2 to 20 A / dm 2 . If it is less than 1 A / dm 2 , the voltage may not increase and discharge may not occur. If it exceeds 20 A / dm 2 , the voltage increases and the formed film is destroyed by discharge, resulting in a rough film structure and poor corrosion resistance. is there.
工程Ｂでは、工程Ａで第１の電圧となった後に、第１の電圧による定電圧処理を行わずに、第１の電圧から、第１の電圧よりも低い電圧の第２の電圧まで、所定の時間で線形又は段階的に電圧を下降させて、アノード酸化処理を行うものである。これにより、第１の電圧による定電圧処理での酸化皮膜の絶縁破壊を避けることができ、更には、電力消費を抑えることができるからである。
第２の電圧は、２００Ｖ以上で、且つ、第１の電圧より低いものであれば良いが、第１の電圧の０．７０倍〜０．９９倍であることが好ましい。０．７０未満であると酸化皮膜と母材の界面に形成する緻密なバリア膜の膜厚を厚くすることができず、０．９９を超えると緻密なバリア膜が成長しないからである。
尚、工程Ｂと工程Ｃとの間に、第２の電圧から第１の電圧まで電圧を上げる工程Ｂ’を行い、工程Ｂ及び工程Ｂ’を１組の工程とし、この１組の工程を、工程Ａの後に複数回繰り返し行うことが好ましい。酸化皮膜の膜質を高めることができるからである。
また、「段階的」とは、第１の電圧と第２の電圧との間の電圧で少なくとも１つの定電圧処理を行うことを意味し、段階的に電圧を下降させる場合には、少なくとも１つの段階における電圧は、３０秒以上保持されることが好ましい。酸化皮膜が形成されにくい部分への酸化皮膜の形成に時間が必要だからである。尚、この時間の上限は最大でも１０時間とする。１０時間を超えるような場合には電解もしくは電解液により酸化皮膜が腐食するからである。
In the process B, after the first voltage is obtained in the process A, the constant voltage process using the first voltage is not performed, and the first voltage to the second voltage that is lower than the first voltage. The anodic oxidation treatment is performed by decreasing the voltage linearly or stepwise at a predetermined time. Thereby, dielectric breakdown of the oxide film in the constant voltage treatment with the first voltage can be avoided, and furthermore, power consumption can be suppressed.
The second voltage may be 200 V or higher and lower than the first voltage, but is preferably 0.70 to 0.99 times the first voltage. This is because if it is less than 0.70, the thickness of the dense barrier film formed at the interface between the oxide film and the base material cannot be increased, and if it exceeds 0.99, the dense barrier film does not grow.
In addition, between the process B and the process C, the process B ′ for increasing the voltage from the second voltage to the first voltage is performed, and the process B and the process B ′ are set as one set of processes. It is preferable that the step A is repeated a plurality of times. This is because the quality of the oxide film can be improved.
Further, “stepwise” means that at least one constant voltage process is performed with a voltage between the first voltage and the second voltage, and when the voltage is lowered stepwise, at least 1 The voltage at one stage is preferably maintained for 30 seconds or more. This is because it takes time to form the oxide film on the portion where the oxide film is difficult to be formed. The upper limit of this time is 10 hours at the maximum. This is because if the time exceeds 10 hours, the oxide film is corroded by electrolysis or an electrolytic solution.
また、印加する電圧及び電流の波形に関しては、交流、直流や交流と直流の重畳のいずれでもよく、交流の場合には、電流又は電圧は、正弦波でも、正弦波でなくてもよい。
上記のように、電圧を一定で処理することにより、電流の流れやすいところ、即ち、酸化皮膜が形成されていないところに順次酸化皮膜を形成させることができ、母材中の凹んだ部分や貫通孔内に電極を配置することなく孔の内部表面までも酸化皮膜を形成させることができる。
In addition, the voltage and current waveforms to be applied may be alternating current, direct current, or superposition of alternating current and direct current. In the case of alternating current, the current or voltage may be either a sine wave or not a sine wave.
As described above, by processing at a constant voltage, it is possible to form an oxide film sequentially where current flows easily, that is, where an oxide film is not formed. An oxide film can be formed even on the inner surface of the hole without disposing an electrode in the hole.
工程Ｃは、工程Ｂの終了時の電圧、即ち、第２の電圧で所定の時間、定電圧処理を行うものである。処理時間としては、５分〜１０時間とすることが好ましい。短すぎるとバリア膜が成長しないからであり、１０時間を超えるような場合には電解もしくは電解液により酸化皮膜が腐食するからである。 In step C, constant voltage processing is performed for a predetermined time using the voltage at the end of step B, that is, the second voltage. The treatment time is preferably 5 minutes to 10 hours. This is because if it is too short, the barrier film does not grow, and if it exceeds 10 hours, the oxide film is corroded by electrolysis or an electrolytic solution.
上記酸化皮膜が形成された母材は、大気下において、１５０℃〜５００℃で加熱することが好ましい。形成された酸化皮膜をより緻密なものとして、耐食性を向上させることができるからである。尚、上記範囲とした理由は、１５０℃未満であると酸化が促進されず、５００℃を超えるとエネルギーを消費するだけで大きな効果は望めないためである。 The base material on which the oxide film is formed is preferably heated at 150 ° C. to 500 ° C. in the atmosphere. This is because the formed oxide film can be made denser to improve the corrosion resistance. The reason why the above range is adopted is that oxidation is not accelerated when the temperature is lower than 150 ° C., and energy is consumed only when the temperature exceeds 500 ° C., and a great effect cannot be expected.
以下に、本発明の実施例を比較例とともに説明する。尚、実施例１〜６、比較例１〜３において、共通の処理とした以下のことを行った。
［共通処理］
電解液として１０ｗｔ％りん酸三ナトリウムを用意した。アルミニウム合金Ａ６０６１の４０ｍｍx４０ｍｍx２ｍｍの板状試料を電解液に浸漬した。試料側をプラス極とし、対極のマイナス極にカーボン電極を取り付けた。
板状試料に、一定電流Ｉ１＝１．４４Ａ(電流密度４．１Ａ／ｄｍ２)で第１の電圧（Ｖ１＝４５０Ｖ）まで定電流で火花放電を伴うアノード酸化処理を行った。尚、４５０Ｖに達するまでの時間ｔ１は、１８００（秒）であった。
Examples of the present invention will be described below together with comparative examples. In Examples 1 to 6 and Comparative Examples 1 to 3, the following was performed as a common process.
[Common processing]
10 wt% trisodium phosphate was prepared as an electrolytic solution. A plate sample of 40 mm × 40 mm × 2 mm of aluminum alloy A6061 was immersed in the electrolytic solution. The sample side was a positive electrode, and a carbon electrode was attached to the negative electrode of the counter electrode.
The plate-like sample was subjected to anodic oxidation with spark discharge at a constant current up to a first voltage (V 1 = 450 V) at a constant current I 1 = 1.44 A (current density 4.1 A / dm 2 ). The time t 1 to reach 450V was 1800 seconds.
［比較例１］
共通処理のみを行うものとした。その工程を図７に示す。
[Comparative Example 1]
Only common processing was performed. The process is shown in FIG.
［比較例２］
共通処理後に、第２の電圧（Ｖ２＝４２０Ｖ）で、定電圧で火花放電を伴うアノード酸化処理を３０分間行った。その工程を図８に示す。
[Comparative Example 2]
After the common treatment, anodization with spark discharge was performed at a constant voltage at a second voltage (V 2 = 420 V) for 30 minutes. The process is shown in FIG.
［比較例３］
共通処理後に、所定の時間（ｔ２＝１５０秒）内で、第１の電圧（Ｖ１＝４５０Ｖ）から第２の電圧（Ｖ２＝３００Ｖ）まで電圧を、１（Ｖ／秒）の速度で線形に下降させ、その後、第２の電圧（Ｖ２＝３００Ｖ）で定電圧処理を所定の時間（ｔ３＝１６２０秒）行った。その工程を図９に示す。
[Comparative Example 3]
After the common processing, within a predetermined time (t 2 = 150 seconds), the voltage is changed from the first voltage (V 1 = 450 V) to the second voltage (V 2 = 300 V) at a speed of 1 (V / second). Then, the voltage was lowered linearly, and then a constant voltage process was performed for a predetermined time (t 3 = 1620 seconds) with the second voltage (V 2 = 300 V). The process is shown in FIG.
［実施例１］
共通処理後に、所定の時間（ｔ２＝１８０秒）内で、第１の電圧（Ｖ１＝４５０Ｖ）から第２の電圧（Ｖ２＝４２０Ｖ）まで電圧を、１／６（Ｖ／秒）の速度で線形に下降させ、その後、第２の電圧（Ｖ２＝４２０Ｖ）で定電圧処理を所定の時間（ｔ３＝１６２０秒）行った。その工程を図１に示す。
[Example 1]
After the common processing, within a predetermined time (t 2 = 180 seconds), the voltage from the first voltage (V 1 = 450 V) to the second voltage (V 2 = 420 V) is reduced to 1/6 (V / second). After that, the voltage was lowered linearly, and then the constant voltage process was performed for a predetermined time (t 3 = 1620 seconds) with the second voltage (V 2 = 420 V). The process is shown in FIG.
［実施例２］
共通処理後に、所定の時間（ｔ２＝９００秒）内で、第１の電圧（Ｖ１＝４５０Ｖ）から第２の電圧（Ｖ２＝４２０Ｖ）まで電圧を線形（１／６（Ｖ／秒）の速度）で下げるという工程を５回繰り返し、その後、定電圧処理（Ｖ２＝４２０Ｖ）を所定の時間（ｔ３＝９００秒）行った。その工程を図２に示す。
[Example 2]
After the common processing, within a predetermined time (t 2 = 900 seconds), the voltage is linear (1/6 (V / second) from the first voltage (V 1 = 450 V) to the second voltage (V 2 = 420 V). ) At a speed of 5) was repeated 5 times, and then a constant voltage process (V 2 = 420 V) was performed for a predetermined time (t 3 = 900 seconds). The process is shown in FIG.
［実施例３］
共通処理後に、所定の時間（ｔ２＝１４４０秒）内において、第２の電圧（Ｖ２＝４２０Ｖ）を所定の時間（１８０秒）保持する工程と、第１の電圧（Ｖ１＝４５０Ｖ）を所定の時間（１８０秒）保持する工程とを交互にそれぞれ４回ずつ繰り返し（合計ｔ２＝１４４０秒）、その後、定電圧処理（Ｖ２＝４２０Ｖ）を所定の時間（ｔ３＝３６０秒）行った。その工程を図３に示す。
[Example 3]
After the common processing, within a predetermined time (t 2 = 1440 seconds), a step of holding the second voltage (V 2 = 420 V) for a predetermined time (180 seconds), and a first voltage (V 1 = 450 V) And a step of holding for a predetermined time (180 seconds) alternately four times each (total t 2 = 1440 seconds), and then a constant voltage process (V 2 = 420 V) for a predetermined time (t 3 = 360 seconds) )went. The process is shown in FIG.
［実施例４］
共通処理後に、所定の時間（ｔ２＝６００秒）内において、第２の電圧（Ｖ２＝４２０Ｖ）まで線形（３０／６００（Ｖ／秒）の速度）に電圧を下げた後、定電圧処理（Ｖ２＝４２０Ｖ）を所定の時間（ｔ３＝１２００秒）行った。その工程を図４に示す。
[Example 4]
After the common processing, within a predetermined time (t 2 = 600 seconds), the voltage is reduced linearly (rate of 30/600 (V / second)) to the second voltage (V 2 = 420 V), and then the constant voltage The treatment (V 2 = 420 V) was performed for a predetermined time (t 3 = 1200 seconds). The process is shown in FIG.
［実施例５］
共通処理後に、所定の時間（ｔ２＝９０秒）内において、第１の電圧（Ｖ１＝４５０Ｖ）から第２の電圧（Ｖ２＝４２０Ｖ）までの間の電圧で、電圧下降幅（７．５Ｖ）で３段階に階段状に電圧を下げ（各段階の電圧で３０秒ずつ維持）、定電圧処理（Ｖ２＝４２０Ｖ）を所定の時間（ｔ３＝１７１０秒）行った。その工程を図５に示す。
[Example 5]
After the common processing, within a predetermined time (t 2 = 90 seconds), the voltage drop width (7) is a voltage between the first voltage (V 1 = 450 V) and the second voltage (V 2 = 420 V). 0.5 V), the voltage was lowered stepwise in three steps (maintained at each step voltage for 30 seconds), and constant voltage processing (V 2 = 420 V) was performed for a predetermined time (t 3 = 1710 seconds). The process is shown in FIG.
［実施例６］
共通処理後に、所定の時間（ｔ２＝１２０秒）内で、第１の電圧（Ｖ１＝４５０Ｖ）から第２の電圧（Ｖ２＝３３０Ｖ）まで電圧を、１（Ｖ／秒）の速度で線形に下降させ、その後、第２の電圧（Ｖ２＝３３０Ｖ）で定電圧処理を所定の時間（ｔ３＝１６２０秒）行った。その工程を図６に示す。
[Example 6]
After the common processing, within a predetermined time (t 2 = 120 seconds), the voltage is changed from the first voltage (V 1 = 450 V) to the second voltage (V 2 = 330 V) at a speed of 1 (V / second). Then, constant voltage processing was performed for a predetermined time (t 3 = 1620 seconds) with the second voltage (V 2 = 330 V). The process is shown in FIG.
比較例１〜３及び実施例１〜６の処理条件、形成された酸化皮膜の抵抗値及び対応する図を表１に示す。
［評価］
表１に記載の通り、既定の処理後、４３０Ｖにした時の電流値Ｉ３は、実施例１〜６で０．０５〜０．１４Ａであり、比較例１が１．４４Ａ、比較例２が０．１８Ａ、比較例３が１．０１Ａであった。評価として各例とも処理を行った後、４３０Ｖにし、流れる電流値から酸化皮膜の抵抗値を算出した。この電流値I3が小さいということは、成膜した酸化皮膜の抵抗が大きく、酸化膜としてよいものになっていることを意味する。実施例１のように第２の電圧まで電圧を下降させるのに時間をかけたり、一度、第２の電圧に電圧を下降させてから再び電圧を上昇させ更に電圧を下降させるという、第１の電圧と第２の電圧との間で電圧の上下を繰り返すことで、比較例と比較して成長させた酸化皮膜の抵抗が上昇していることから、よりよい酸化皮膜が成長できていることが確認できた。
[Evaluation]
As described in Table 1, after the default treatment, the current value I 3 when formed into a 430V is 0.05~0.14A in Examples 1-6, Comparative Example 1 1.44A, Comparative Example 2 Was 0.18A, and Comparative Example 3 was 1.01A. As an evaluation, each example was treated and then set to 430 V, and the resistance value of the oxide film was calculated from the flowing current value. The small current value I 3 means that the resistance of the deposited oxide film is large and the oxide film is good. As in the first embodiment, it takes time to lower the voltage to the second voltage, or once the voltage is lowered to the second voltage, the voltage is raised again, and the voltage is further lowered. By repeating the voltage up and down between the voltage and the second voltage, the resistance of the oxide film grown compared to the comparative example is increased, so that a better oxide film can be grown. It could be confirmed.
Claims (4)
２００Ｖ以上の第１の電圧まで定電流密度でアノード酸化処理する工程Ａと、
工程Ａの第１の電圧による定電圧処理を行わずに、第１の電圧から、第１の電圧よりも低い電圧の第２の電圧まで、所定の時間で線形又は段階的に電圧を下降させて、前記アノード酸化処理を行う工程Ｂと、
第２の電圧で、定電圧処理を行う工程Ｃと、
を行うことを特徴とする酸化皮膜の形成方法。 A method of forming an oxide film on the surface of the base material by immersing a base material composed of aluminum or an aluminum alloy in an alkaline solution and performing an anodic oxidation treatment with spark discharge,
Step A for anodizing at a constant current density up to a first voltage of 200 V or higher;
The voltage is decreased linearly or stepwise in a predetermined time from the first voltage to the second voltage lower than the first voltage without performing the constant voltage process using the first voltage in step A. Step B for performing the anodizing treatment,
Step C for performing constant voltage processing with the second voltage;
A method for forming an oxide film, comprising:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2013092178A JP6108938B2 (en) | 2013-04-25 | 2013-04-25 | Formation method of oxide film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2013092178A JP6108938B2 (en) | 2013-04-25 | 2013-04-25 | Formation method of oxide film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2014214342A true JP2014214342A (en) | 2014-11-17 |
| JP6108938B2 JP6108938B2 (en) | 2017-04-05 |
Family
ID=51940404
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2013092178A Active JP6108938B2 (en) | 2013-04-25 | 2013-04-25 | Formation method of oxide film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP6108938B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109423674A (en) * | 2017-08-23 | 2019-03-05 | 株式会社爱发科 | Surface treatment method and surface processing device |
| CN114277419A (en) * | 2021-12-09 | 2022-04-05 | 广东工业大学 | Large-pore-spacing anodic aluminum oxide film based on parabolic equation boosting and preparation method and application thereof |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS506537A (en) * | 1973-05-22 | 1975-01-23 | ||
| JPS5339946A (en) * | 1976-09-25 | 1978-04-12 | Sankyo Aruminiumu Kougiyou Kk | Surface treatment of aluminum |
| JPH093693A (en) * | 1995-06-20 | 1997-01-07 | Nippon Oil & Fats Co Ltd | Method for coating aluminum blank |
| JP2011058611A (en) * | 2009-09-14 | 2011-03-24 | Ulvac Japan Ltd | Vacuum valve |
| US20120031765A1 (en) * | 2009-04-03 | 2012-02-09 | Keronite International Ltd | Process for the enhanced corrosion protection of valve metals |
-
2013
- 2013-04-25 JP JP2013092178A patent/JP6108938B2/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS506537A (en) * | 1973-05-22 | 1975-01-23 | ||
| JPS5339946A (en) * | 1976-09-25 | 1978-04-12 | Sankyo Aruminiumu Kougiyou Kk | Surface treatment of aluminum |
| JPH093693A (en) * | 1995-06-20 | 1997-01-07 | Nippon Oil & Fats Co Ltd | Method for coating aluminum blank |
| US20120031765A1 (en) * | 2009-04-03 | 2012-02-09 | Keronite International Ltd | Process for the enhanced corrosion protection of valve metals |
| JP2011058611A (en) * | 2009-09-14 | 2011-03-24 | Ulvac Japan Ltd | Vacuum valve |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109423674A (en) * | 2017-08-23 | 2019-03-05 | 株式会社爱发科 | Surface treatment method and surface processing device |
| JP2019039030A (en) * | 2017-08-23 | 2019-03-14 | 株式会社アルバック | Surface treatment method and surface treatment apparatus |
| CN114277419A (en) * | 2021-12-09 | 2022-04-05 | 广东工业大学 | Large-pore-spacing anodic aluminum oxide film based on parabolic equation boosting and preparation method and application thereof |
| CN114277419B (en) * | 2021-12-09 | 2023-05-23 | 广东工业大学 | Macroporous-spacing anodic aluminum oxide film based on parabolic equation boosting and preparation method and application thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP6108938B2 (en) | 2017-04-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR101195458B1 (en) | Method for treating the surface of metal | |
| WO2006134737A1 (en) | Metal oxide film, laminate, metal member and process for producing the same | |
| JP5152574B2 (en) | Method for anodizing aluminum member | |
| CN106065488B (en) | A method of preparing anode aluminium foil using positive negative pulse stuffing anodizing | |
| KR101356230B1 (en) | Method for formation of anode oxide film | |
| JP2006083467A (en) | Anodized film and anodizing method | |
| CN103088384A (en) | valve metal plasma electrolytic oxidation surface treatment method | |
| CN101880904A (en) | Method for cast aluminum alloy micro-arc oxidation pretreatment | |
| JP5700235B2 (en) | Method of forming alumite film | |
| JP4888948B2 (en) | Method for forming high speed anodized film of aluminum material | |
| JP6108938B2 (en) | Formation method of oxide film | |
| WO2020177223A1 (en) | Preparation method for calcium salt-based magnesium alloy surface corrosion-resistant self-repairing coating | |
| JPWO2014203919A1 (en) | Manufacturing method of magnesium alloy products | |
| JP2010236043A (en) | Anodic oxide coating film and anodizing oxidation method | |
| JP6212383B2 (en) | Method for anodizing aluminum-based members | |
| JP2007154300A (en) | Aluminum alloy anodic oxidation method and power source for aluminum alloy anodic oxidation | |
| JP5522117B2 (en) | Insulating coated aluminum conductor, insulating coating and method for forming the same | |
| CN109811385B (en) | Polyvinylidene fluoride/aluminum oxide composite film on surface of aluminum and aluminum alloy and preparation method thereof | |
| JP2004035930A (en) | Aluminum alloy material and anodization treatment method therefor | |
| CN105624757A (en) | Industrial-frequency alternating-current anodic oxidation method of anode aluminum foil for aluminum electrolytic capacitor | |
| JP5937937B2 (en) | Aluminum anodized film | |
| JP5371477B2 (en) | Formation method of oxide film | |
| JP5798900B2 (en) | Method for forming oxide film and oxide film | |
| EP1715083A1 (en) | Method for producing heavy highly adhesive protective coatings on valve-metal parts by micro-arc oxidation | |
| JP5452034B2 (en) | Surface treatment member for semiconductor manufacturing apparatus and method for manufacturing the same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20160301 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20161110 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20161122 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20161209 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20170221 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20170307 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 6108938 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |