JP5265181B2 - Protective film manufacturing method - Google Patents
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- JP5265181B2 JP5265181B2 JP2007315770A JP2007315770A JP5265181B2 JP 5265181 B2 JP5265181 B2 JP 5265181B2 JP 2007315770 A JP2007315770 A JP 2007315770A JP 2007315770 A JP2007315770 A JP 2007315770A JP 5265181 B2 JP5265181 B2 JP 5265181B2
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- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
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- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/02—Anodisation
- C25D11/04—Anodisation of aluminium or alloys based thereon
- C25D11/18—After-treatment, e.g. pore-sealing
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- C25D11/246—Chemical after-treatment for sealing layers
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Abstract
Description
本発明はアルミニウム材の保護膜製造方法に関し、特にアルミニウムのアノード酸化皮膜に緻密な層(保護膜)を形成する方法に関する。 The present invention relates to a method for producing a protective film of an aluminum material, and more particularly to a method for forming a dense layer (protective film) on an anodic oxide film of aluminum.
アルミニウムやアルミニウム合金は、ステンレス鋼等に比べて軽量で熱伝導性に優れる上に、クロム等の重金属汚染の影響が無いため、真空処理装置の真空槽の内壁部材として広く用いられている。
従来より、アルミニウムやアルミニウム合金の耐食処理は、アルマイト処理と呼ばれるアノード酸化処理が広く用いられている。
Aluminum and aluminum alloys are widely used as an inner wall member of a vacuum chamber of a vacuum processing apparatus because they are lighter and have better thermal conductivity than stainless steel and are not affected by heavy metal contamination such as chromium.
Conventionally, anodizing treatment called anodizing treatment has been widely used for corrosion treatment of aluminum or aluminum alloy.
しかし、真空処理装置でも特に反応性のガスや、そのプラズマやラジカルを用いる装置(CVD装置、エッチング装置等)では、高い耐食性が要求され、従来のアノード酸化処理では不十分であった。 However, even in a vacuum processing apparatus, particularly a reactive gas, or an apparatus (such as a CVD apparatus or an etching apparatus) that uses plasma or radical thereof requires high corrosion resistance, and the conventional anodic oxidation process is insufficient.
アノード酸化処理は、硫酸、シュウ酸等の水溶液を電解液とし、処理対象物を陽極として、電解液に浸漬する。同じ電解液に浸漬した陰極と、上記陽極との間で電気分解を起こし、処理対象物の表面にアルミニウムの酸化物、または水酸化物からなるアノード酸化皮膜を成長させる。 In the anodic oxidation treatment, an aqueous solution of sulfuric acid, oxalic acid or the like is used as an electrolytic solution, and the object to be treated is used as an anode, and is immersed in the electrolytic solution. Electrolysis is caused between the cathode immersed in the same electrolytic solution and the anode, and an anodic oxide film made of aluminum oxide or hydroxide is grown on the surface of the object to be treated.
このようにして形成されたアノード酸化皮膜は、厚さ数μmから数十μmであり、一般的に皮膜中には数10nmの無数の孔が表面から深さ方向に形成された多孔質構造になっている。穴底(孔の底壁)の酸化皮膜の厚さは数10nmであり、この薄い酸化皮膜がアノード酸化皮膜全体の耐食性を決めている。 The anodic oxide film thus formed has a thickness of several μm to several tens of μm. Generally, the film has a porous structure in which innumerable pores of several tens of nm are formed in the depth direction from the surface. It has become. The thickness of the oxide film on the bottom of the hole (bottom wall of the hole) is several tens of nm, and this thin oxide film determines the corrosion resistance of the entire anodic oxide film.
アノード酸化皮膜の耐食性を向上させるためには、孔を埋める封孔処理が必要である。封孔処理としては、アノード酸化皮膜が形成された処理対象物を沸騰水に浸漬する方法や、蒸気釜中で100℃以上の高温蒸気に曝す方法が知られている。 In order to improve the corrosion resistance of the anodic oxide film, a sealing treatment for filling the holes is necessary. As the sealing treatment, there are known a method in which an object to be treated on which an anodized film has been formed is immersed in boiling water, and a method in which the object to be exposed to high-temperature steam at 100 ° C. or higher in a steam kettle.
この方法によれば、アノード酸化皮膜の多孔質構造の上に、緻密な層が形成されることが知られている。この層は一般にベーマイト層と呼ばれ、緻密なベーマイト層が耐食性を向上させると言われていた。しかし、この方法で封孔処理を行っても、高い耐食性を示すベーマイト層が再現性よく形成されず、耐食性が不十分なことがあった。
本発明者等が、アノード酸化皮膜を、100℃以上の沸騰水に接触させる封孔処理を行ったところ、全く同一条件でアノード酸化処理と封孔処理を行っても、全く緻密層が形成されないものや、1μm以上の厚膜ができるものがあり、緻密層の膜厚にバラツキが生じることが分かった。
沸騰水に代え、100℃以上の水蒸気で封孔処理を行っても、同様にバラツキが生じた。
When the present inventors performed sealing treatment in which the anodic oxide film was brought into contact with boiling water at 100 ° C. or higher, no dense layer was formed even if anodic oxidation treatment and sealing treatment were performed under exactly the same conditions. Some have a thick film of 1 μm or more, and it has been found that the thickness of the dense layer varies.
Even when the sealing treatment was carried out with water vapor of 100 ° C. or higher instead of boiling water, variation was similarly caused.
より封孔性を高めるために、封孔時間を通常30分のところ2時間に延長しても、緻密層の膜厚のバラツキの問題は解消されなかった。更に、封孔処理前の汚染の影響を考慮し、封孔処理前に十分に処理対象物を洗浄してから封孔処理を行っても、緻密層の膜厚のバラツキは改善されなかった。 In order to further improve the sealing performance, even if the sealing time is extended to 2 hours, usually 30 minutes, the problem of variation in the thickness of the dense layer has not been solved. Further, in consideration of the influence of contamination before the sealing treatment, even if the processing object is sufficiently cleaned before the sealing treatment and the sealing treatment is performed, the variation in the film thickness of the dense layer is not improved.
また、アノード酸化皮膜の膜構造の影響を考慮し、アノード酸化皮膜成膜中に印加電圧を変化させ、皮膜構造を変えて封孔処理を行ったが、緻密層の膜厚のバラツキは改善されなかった。 Also, considering the influence of the film structure of the anodic oxide film, the applied voltage was changed during film formation of the anodic oxide film, and the sealing process was performed by changing the film structure, but the variation in the thickness of the dense layer was improved. There wasn't.
上記課題を解決するために、本発明は、アルミニウムのアノード酸化皮膜が表面に形成された処理対象物の、前記アノード酸化皮膜を緻密化し、保護膜を製造する保護膜製造方法であって、前記アノード酸化皮膜の緻密化は、70℃以上90℃以下の第一の温度にされた純水の温水を前記アノード酸化皮膜に15分以上の時間接触させた後、前記第一の温度よりも高い100℃以上の第二の温度にされた熱水を前記アノード酸化被膜に接触させ、又は前記第一の温度よりも高い100℃以上の前記第二の温度にされた水蒸気を、常圧以上の圧力にした処理槽内で、前記アノード酸化皮膜に接触させ、前記アノード酸化被膜の表面を、膜厚1.0μm以上の緻密層にする保護膜製造方法である。
本発明は保護膜製造方法であって、前記温水には、前記純水に、アンモニアと、トリエタノールアミンと、ヒドラジンとからなる群より選択されるいずれか1種類のアルカリを添加したアルカリ性水溶液を用いる保護膜製造方法である。
In order to solve the above-mentioned problems, the present invention provides a method for producing a protective film, comprising densifying the anodic oxide film of a treatment target having an anodic oxide film formed on the surface thereof, and producing a protective film, Densification of the anodic oxide film is higher than the first temperature after contacting pure water having a first temperature of 70 ° C. or higher and 90 ° C. or lower with the anodic oxide film for 15 minutes or longer. The hot water brought to a second temperature of 100 ° C. or higher is brought into contact with the anodic oxide coating, or the water vapor made to the second temperature of 100 ° C. or higher, which is higher than the first temperature , In the method for producing a protective film , the surface of the anodic oxide film is brought into contact with the anodic oxide film in a pressure-treated treatment tank so that the surface of the anodic oxide film is a dense layer having a thickness of 1.0 μm or more .
The present invention is a method for producing a protective film, wherein the warm water is an alkaline aqueous solution obtained by adding any one alkali selected from the group consisting of ammonia, triethanolamine, and hydrazine to the pure water. It is a protective film manufacturing method to be used .
アノード酸化皮膜の緻密層(保護膜)を厚膜にし、しかもその膜厚が均一になるから、耐食性が向上する。 Since the dense layer (protective film) of the anodic oxide film is made thick and the film thickness becomes uniform, the corrosion resistance is improved.
図1の符号2は陽極酸化装置を示している。皮膜を形成するために、陽極酸化装置2の電解槽21の内部に電解液26として入れておく。
電源25のプラス端子に接続された取付器具23に処理対象物11を密着して取り付ける。その処理対象物11を取付器具23に取り付けた状態で電解液26に浸漬すると共に、電源25のマイナス端子に接続された陰極板22を電解液26に浸漬した。
Reference numeral 2 in FIG. 1 indicates an anodizing apparatus. In order to form a film, it is put as an electrolytic solution 26 in the electrolytic cell 21 of the anodizing device 2.
The object to be treated 11 is attached in close contact with the attachment 23 connected to the plus terminal of the power supply 25. The treatment object 11 was immersed in the electrolytic solution 26 while being attached to the attachment device 23, and the cathode plate 22 connected to the negative terminal of the power supply 25 was immersed in the electrolytic solution 26.
電解液26を所定の酸化温度に維持しながら、電源25を動作させ、処理対象物11と陰極板22の間に、所定の酸化電圧を印加し、所定の電流密度の直流電圧を、所定の酸化時間処理対象物11に流す。
処理対象物11の少なくとも表面部分にはアルミニウムとアルミニウム合金のいずれか一方又は両方からなるアルミニウム材料が露出しており、電流密度は、処理対象物11に流した電流を、処理対象物11のアルミニウム材料が露出する部分の面積で除した値である。
While maintaining the electrolytic solution 26 at a predetermined oxidation temperature, the power supply 25 is operated, a predetermined oxidation voltage is applied between the object to be processed 11 and the cathode plate 22, and a direct current voltage with a predetermined current density is applied to a predetermined voltage. Oxidation time treatment object 11
An aluminum material made of one or both of aluminum and an aluminum alloy is exposed on at least the surface portion of the processing object 11, and the current density is the current flowing through the processing object 11 by the aluminum of the processing object 11. It is a value divided by the area of the portion where the material is exposed.
処理対象物11に電流が流れると、表面部分からアルミニウムがイオンとなって溶け出す。該アルミニウムイオンは水の電気分解により発生した酸素や、水酸基と結合し、処理対象物11の表面に、酸化アルミニウム(Al2O3)と、水酸化アルミニウム(AlH3O3)のいずれか一方又は両方が生成され、アルミニウムのアノード酸化皮膜が形成される。 When a current flows through the object 11 to be processed, aluminum melts as ions from the surface portion. The aluminum ions are bonded to oxygen generated by electrolysis of water or hydroxyl groups, and either one of aluminum oxide (Al 2 O 3 ) and aluminum hydroxide (AlH 3 O 3 ) is formed on the surface of the object 11 to be processed. Or both are produced and an anodic oxide film of aluminum is formed.
電解液26は、シュウ酸や硫酸等の酸を含み、このような電解液26中では、アノード酸化皮膜は多孔質構造となる。
アノード酸化皮膜12が形成された処理対象物11を電解液26から引き上げ、取付器具23から取り外し、純水で洗浄する。
The electrolytic solution 26 includes an acid such as oxalic acid or sulfuric acid, and the anodic oxide film has a porous structure in the electrolytic solution 26.
The processing object 11 on which the anodic oxide film 12 is formed is pulled up from the electrolytic solution 26, removed from the fixture 23, and washed with pure water.
図2の符号4は第一の封孔処理装置を示している。第一の封孔処理装置4の第一の加熱処理槽41に第一の温度(70℃以上90℃以下)の温水46を配置しておく。温水46の温度を第一の温度に維持しながら、アノード酸化皮膜12が形成された処理対象物11を、その温水46に所定の第一の処理時間(5分以上60分以下)浸漬する。 The code | symbol 4 of FIG. 2 has shown the 1st sealing processing apparatus. Hot water 46 having a first temperature (70 ° C. or more and 90 ° C. or less) is placed in the first heat treatment tank 41 of the first sealing treatment device 4. While maintaining the temperature of the hot water 46 at the first temperature, the processing object 11 on which the anodic oxide film 12 is formed is immersed in the hot water 46 for a predetermined first processing time (5 minutes to 60 minutes).
アノード酸化皮膜12は第一の温度の温水46と接触すると、表面に不連続な面が形成され、アノード酸化皮膜12内の空隙が露出した状態になる(第一の熱処理工程)。
第一の熱処理工程後、第一の温度よりも高い第二の温度の熱水、又は第二の温度の水蒸気を、アノード酸化皮膜12に所定の第二の処理時間(5分以上60分以下)接触させる。
When the anodic oxide film 12 comes into contact with the hot water 46 at the first temperature, a discontinuous surface is formed on the surface and the voids in the anodic oxide film 12 are exposed (first heat treatment step).
After the first heat treatment step, hot water having a second temperature higher than the first temperature or water vapor having the second temperature is applied to the anodic oxide film 12 for a predetermined second treatment time (5 minutes to 60 minutes). ) Make contact.
上述したように、第一の熱処理工程によって、アノード酸化皮膜12内の空隙が露出しているから、熱水又は水蒸気は、アノード酸化皮膜12の表面に接触するだけでなく、空隙にも入り込む。 As described above, since the voids in the anodic oxide film 12 are exposed by the first heat treatment step, the hot water or water vapor not only contacts the surface of the anodic oxide film 12 but also enters the voids.
アノード酸化皮膜12の構成材料(酸化アルミニウムや水酸化アルミニウム)は熱水又は水蒸気と接触すると、水を吸収し、ベーマイト(Al2O3・H2O)やバイヤライト(Al2O3・3H2O)等の水和物となって、体積が膨張し、アノード酸化皮膜12の空隙が封孔され、アノード酸化皮膜12の表面部分に緻密な保護膜が形成される(第二の熱処理工程)。 When the constituent material (aluminum oxide or aluminum hydroxide) of the anodic oxide film 12 comes into contact with hot water or water vapor, it absorbs water and boehmite (Al 2 O 3 .H 2 O) or bayerite (Al 2 O 3 .3H). 2 O) and the like, and the volume expands, the voids of the anodic oxide film 12 are sealed, and a dense protective film is formed on the surface portion of the anodic oxide film 12 (second heat treatment step). ).
尚、第二の熱処理工程に熱水を用いる場合は、例えば、処理対象物11を第一の熱処理工程と同槽の温水46に漬けたまま該温水46を昇温させ、温水46が第二の温度の熱水になってから、その熱水に処理対象物11が浸漬された状態を第二の処理時間維持する。又は、処理対象物11を温水46から引き上げ、第一の熱処理工程とは別槽に配置した第二の温度の熱水に漬け、熱水を第二の温度に維持したまま、該熱水に処理対象物11を浸漬された状態を第二の処理時間維持する。 When hot water is used in the second heat treatment step, for example, the hot water 46 is heated while the processing object 11 is immersed in the hot water 46 in the same tank as the first heat treatment step. After the temperature of the hot water becomes, the state in which the processing object 11 is immersed in the hot water is maintained for the second processing time. Alternatively, the object to be treated 11 is pulled up from the hot water 46, soaked in hot water having a second temperature arranged in a separate tank from the first heat treatment step, and the hot water is maintained in the second temperature while being maintained at the second temperature. The state in which the processing object 11 is immersed is maintained for the second processing time.
第二の熱処理工程に水蒸気を用いる場合は、処理対象物11を温水46から引き上げた後、図3に示したような蒸気封孔装置(第二の封孔処理装置5)の釜(処理槽51)内に処理対象物11を配置する。水蒸気発生装置55により、該処理槽51内に第二の温度の水蒸気を充満させ、該水蒸気の温度を第二の温度に維持したまま、処理対象物11を該水蒸気に曝した状態を、第二の処理時間維持する。
第二の熱処理工程で水蒸気を用いる場合、処理槽51の内部圧力は常圧(1気圧)でもよいし、常圧を超えてもよい。
When water vapor is used in the second heat treatment step, after the processing object 11 is pulled up from the hot water 46, the pot (processing tank) of the steam sealing device (second sealing processing device 5) as shown in FIG. 51) Arrange the processing object 11 within. A state in which the treatment tank 11 is exposed to the steam while the treatment tank 51 is filled with the steam at the second temperature by the steam generator 55 and the temperature of the steam is maintained at the second temperature. Maintain the second processing time.
When using water vapor in the second heat treatment step, the internal pressure of the treatment tank 51 may be normal pressure (1 atm) or may exceed normal pressure.
幅30mm、長さ45mm、厚み2mmのアルミニウム合金板(A5052P、JIS H4000を参照)を基板とし、アノード酸化皮膜形成の前処理として、該基板を40℃の10%水酸化ナトリウム水溶液に1分浸漬し、脱脂した後、水洗し、室温で35%の硫酸水溶液に浸漬してスマット(黒色付着物)の除去を行った。 An aluminum alloy plate (A5052P, see JIS H4000) having a width of 30 mm, a length of 45 mm, and a thickness of 2 mm is used as a substrate, and the substrate is immersed in a 10% sodium hydroxide aqueous solution at 40 ° C. for 1 minute as a pretreatment for forming an anodic oxide film. After degreasing, it was washed with water and immersed in a 35% sulfuric acid aqueous solution at room temperature to remove smut (black deposit).
前処理後の基板を処理対象物とし、純水1リットルに対し、30gのシュウ酸を溶解した電解液を用い、酸化温度を15℃以上25℃以下、酸化電圧を60V以上100V以下とし、電流密度と酸化時間とアノード酸化皮膜12の膜厚は下記表1に示す条件でアノード酸化皮膜12を形成した。 The substrate after the pretreatment is treated, an electrolytic solution in which 30 g of oxalic acid is dissolved in 1 liter of pure water is used, the oxidation temperature is 15 ° C. or higher and 25 ° C. or lower, the oxidation voltage is 60 V or higher and 100 V or lower. The anodic oxide film 12 was formed under the conditions shown in Table 1 below for the density, oxidation time, and film thickness of the anodic oxide film 12.
アノード酸化皮膜12が形成された処理対象物11を用い、上記表1に示す条件で、第一の熱処理工程を行い、参考例1〜4の試料を5個ずつ作成した。
各試料の破断面を走査型電子顕微鏡(SEM)で観察したところ、第一の温度が60℃では、アノード酸化皮膜12(ポア層)の上には何も形成されず、第一の熱処理を行う前と後で表面状態が変らなかった。
Using the processing object 11 on which the anodic oxide film 12 was formed, the first heat treatment step was performed under the conditions shown in Table 1 above, and five samples of Reference Examples 1 to 4 were prepared.
When the fracture surface of each sample was observed with a scanning electron microscope (SEM), when the first temperature was 60 ° C., nothing was formed on the anodic oxide film 12 (pore layer), and the first heat treatment was performed. The surface condition did not change before and after the operation.
これに対し、第一の温度が70℃、80℃、90℃では、アノード酸化皮膜12の表面から1μmの深さまでの間に、不連続な面が現れ、アノード酸化皮膜12中の空隙が露出した。第一の温度が60℃、80℃、90℃の時のSEM写真を図4〜6にそれぞれ記載する。 On the other hand, when the first temperature is 70 ° C., 80 ° C., and 90 ° C., a discontinuous surface appears from the surface of the anodic oxide film 12 to a depth of 1 μm, and the voids in the anodic oxide film 12 are exposed. did. SEM photographs when the first temperature is 60 ° C., 80 ° C., and 90 ° C. are shown in FIGS.
次に、上記前処理後の基板を用い、下記表2に示す条件でアノード酸化皮膜12を形成した後、純水に浸漬して洗浄してから、下記表2に示す条件で第一、第二の熱処理を行い、実施例1〜5、比較例1〜3の試料を複数枚ずつ作成した。 Next, after forming the anodic oxide film 12 under the conditions shown in the following Table 2 using the substrate after the pretreatment, the substrate is dipped in pure water and washed, and then the first and second conditions under the conditions shown in the following Table 2 are used. Two heat treatments were performed to prepare a plurality of samples of Examples 1 to 5 and Comparative Examples 1 to 3.
尚、第二の熱処理工程の熱水(沸騰水、蒸気含む)は全て純水を用いた。実施例1〜4、比較例1、2については、アノード酸化皮膜12の成膜条件を上記参考例1〜4と同じにした。実施例5と比較例3については、参考例1〜4と同じ電解液を用いたが、最初の15分間は電流密度を5A/dm2、酸化電圧を60V以上70V以下、酸化温度を15℃以上17℃以下にし、次の15分間は電流密度を10A/dm2、酸化電圧を70V以上130V以下、酸化温度を17℃以上30℃以下にして、計30分間アノード酸化皮膜12の成膜を行った。 Note that pure water was used for all hot water (including boiling water and steam) in the second heat treatment step. In Examples 1 to 4 and Comparative Examples 1 and 2, the film formation conditions of the anodic oxide film 12 were the same as those in Reference Examples 1 to 4 described above. For Example 5 and Comparative Example 3, the same electrolyte solution as in Reference Examples 1 to 4 was used, but for the first 15 minutes, the current density was 5 A / dm 2 , the oxidation voltage was 60 V to 70 V, and the oxidation temperature was 15 ° C. The current density is 10 A / dm 2 for the next 15 minutes, the oxidation voltage is 70 to 130 V, the oxidation temperature is 17 to 30 ° C., and the anodic oxide film 12 is formed for a total of 30 minutes. went.
<SEM写真>
上記実施例1の試料10枚と、比較例1の試料6枚と、比較例2の試料6枚について、破断面のSEM写真を撮影した。実施例1のSEM写真を図7に、比較例1のSEM写真を図8に、比較例2のSEM写真を図9にそれぞれ示す。
<SEM photo>
SEM photographs of fracture surfaces were taken for 10 samples of Example 1, 6 samples of Comparative Example 1, and 6 samples of Comparative Example 2. FIG. 7 shows an SEM photograph of Example 1, FIG. 8 shows an SEM photograph of Comparative Example 1, and FIG. 9 shows an SEM photograph of Comparative Example 2.
図7を見ると、実施例1は10枚の試料全てに、膜厚1μm程度の緻密層が確認された。これに対し、図8、9を見ると、試料によっては緻密層が形成されたものもあるが、比較例1の試料1、2と、比較例2の試料1、2、6のように、緻密層が形成されているか否かが不明確なものもあった。 As shown in FIG. 7, in Example 1, a dense layer having a film thickness of about 1 μm was confirmed on all ten samples. On the other hand, when looking at FIGS. 8 and 9, some samples have a dense layer formed, but like Samples 1 and 2 in Comparative Example 1 and Samples 1, 2 and 6 in Comparative Example 2, In some cases, it was unclear whether a dense layer was formed.
以上のことから、アノード酸化皮膜12を熱水又は水蒸気に曝す前に、水蒸気でなく、温水46に接触させることで、確実に緻密層が形成されることがわかった。
実施例1、比較例1の各試料について、更に下記耐食性試験を行った。
From the above, it was found that a dense layer was reliably formed by contacting the anodic oxide film 12 with hot water 46 instead of water vapor before exposing it to hot water or water vapor.
The samples of Example 1 and Comparative Example 1 were further subjected to the following corrosion resistance test.
<耐食性試験>
各試料を室温で35%塩酸水溶液に浸漬してから、試料から目視で確認できる程大量の泡が出始めるまでの時間を測定した。その測定結果を、SEM写真から測定した緻密層の膜厚と共に下記表3に記載した。
<Corrosion resistance test>
After each sample was immersed in a 35% aqueous hydrochloric acid solution at room temperature, the time until a large amount of bubbles started to appear from the sample was measured. The measurement results are shown in Table 3 below together with the thickness of the dense layer measured from the SEM photograph.
上記表3から分かるように、緻密層の膜厚が増える程、泡が出始めるまでの時間が長くなる傾向がある。
緻密層の膜厚が1μm程度あれば、泡が大量に発生するまでの時間は350分から400分であるのに対し、緻密層が形成されていない試料は、200分前後であった。緻密層が形成されていれば、耐食性が高いことが分かる。
As can be seen from Table 3 above, as the thickness of the dense layer increases, the time until bubbles start to appear tends to increase.
When the film thickness of the dense layer was about 1 μm, the time until a large amount of bubbles was generated was 350 minutes to 400 minutes, whereas the sample without the dense layer was around 200 minutes. If the dense layer is formed, it can be seen that the corrosion resistance is high.
実施例1と比較例1とを比較すると、実施例1の各試料は比較例1に比べて緻密層が厚く、しかも、試料毎の厚さのばらつきも小さい。以上のことから、本発明により形成される保護膜(緻密層)は厚く、しかも、膜厚のばらつきが少ないことが分かる。 When Example 1 and Comparative Example 1 are compared, each sample of Example 1 has a thicker layer than Comparative Example 1, and the variation in thickness between samples is small. From the above, it can be seen that the protective film (dense layer) formed by the present invention is thick and has little variation in film thickness.
尚、実施例3について、実施例1と同様に保護膜の膜厚を測定したところ、膜厚と、そのばらつきは実施例1と同程度であった。以上のことから、第一の熱処理の時の温水46をそのままま加熱して第二の熱処理を行っても、別槽で行った場合と効果に違いのないことが確認された。
実施例2、4、5、比較例3の試料について、実施例1と同様に緻密層の膜厚を測定した。その測定結果を下記表4〜7に記載する。
In Example 3, the thickness of the protective film was measured in the same manner as in Example 1. As a result, the film thickness and variations thereof were similar to those in Example 1. From the above, it was confirmed that even when the second heat treatment was performed by heating the hot water 46 as it was during the first heat treatment, there was no difference in effect from the case where it was performed in a separate tank.
For the samples of Examples 2, 4, 5 and Comparative Example 3, the thickness of the dense layer was measured in the same manner as in Example 1. The measurement results are shown in Tables 4 to 7 below.
表4と上記表2の結果には大差が無く、第二の熱処理でアノード酸化被膜12に接触させるのが、熱水か、水蒸気かに関わらず、第二の温度であれば緻密層が厚く、その膜厚のばらつきも小さいことが分かる。 There is no significant difference between the results of Table 4 and Table 2 above, and the dense layer is thick at the second temperature regardless of whether it is hot water or water vapor that is contacted with the anodic oxide coating 12 in the second heat treatment. It can be seen that the variation in the film thickness is small.
実施例4で用いた弱アルカリ性水溶液(アンモニア水)は、封孔処理を促進するために一般に知られているものである。表5を見ると、実施例4は純水(中性)を用いた他の実施例に比べて緻密層が厚いから、本発明において、温水46をアルカリ性にすることは、緻密層の形成に悪影響を及ぼさず、むしろ、緻密層の形成を促進するものであることが分かる。 The weakly alkaline aqueous solution (ammonia water) used in Example 4 is generally known for promoting the sealing treatment. As seen from Table 5, since the dense layer is thicker in Example 4 than in other examples using pure water (neutral), in the present invention, making the warm water 46 alkaline is the formation of the dense layer. It can be seen that it does not adversely affect, but rather promotes the formation of a dense layer.
実施例5、比較例3は、上記表2に記載したように、アノード酸化被膜12を形成する際、前半を低電流密度にし、後半を高電流密度にすることで、アノード酸化皮膜12形成の後半で、アノード酸化被膜のポア(孔)サイズを大きくし、ポアで無い壁の部分の膜厚も厚くなるようにし、アノード酸化被膜の構造を膜厚方向に変化させた。 In Example 5 and Comparative Example 3, as described in Table 2 above, when the anodic oxide coating 12 was formed, the first half was set to a low current density, and the second half was set to a high current density. In the latter half, the pore (hole) size of the anodic oxide film was increased, the film thickness of the wall portion that was not a pore was also increased, and the structure of the anodic oxide film was changed in the film thickness direction.
しかし、表6、7と、上記表2を比較すると、アノード酸化被膜の構造を変化させても、第一、第二の熱処理後の緻密層の膜厚に大差が無い。従って、本発明は、アノード酸化被膜形成時の条件や、アノード酸化被膜の構造に関係無く、緻密層を形成可能なことが分かる。 However, comparing Tables 6 and 7 with Table 2 above, even if the structure of the anodic oxide film is changed, there is no significant difference in the thickness of the dense layer after the first and second heat treatments. Therefore, it can be seen that the present invention can form a dense layer regardless of the conditions during the formation of the anodic oxide coating and the structure of the anodic oxide coating.
尚、電解液をシュウ酸水溶液から硫酸水溶液に変えてアノード酸化皮膜12を形成したところ、シュウ酸水溶液を用いた場合と同様に多孔質のアノード酸化皮膜12が得られた。このアノード酸化皮膜12を用いて、上記実施例1〜5と同様の条件で第一、第二の熱処理工程を行ったところ、シュウ酸水溶液を用いた場合と同様に緻密な保護膜が形成された。以上のことから、本願発明は、電解液の種類を変えても、緻密な保護膜を形成可能なことが分かる。 When the anodic oxide film 12 was formed by changing the electrolytic solution from the oxalic acid aqueous solution to the sulfuric acid aqueous solution, the porous anodic oxide film 12 was obtained in the same manner as in the case of using the oxalic acid aqueous solution. When this anodic oxide film 12 was used and the first and second heat treatment steps were performed under the same conditions as in Examples 1 to 5, a dense protective film was formed as in the case of using an oxalic acid aqueous solution. It was. From the above, it can be seen that the present invention can form a dense protective film even if the type of the electrolytic solution is changed.
以上は、第一の熱処理工程で、処理対象物11を温水46に浸漬する場合について説明したが、本発明はこれに限定されるものではなく、処理対象物11と温水46とが接触するのであれば、温水46を処理対象物11の表面にかけ流してもよいし、温水46を処理対象物11表面に噴霧してもよい。 Although the above demonstrated the case where the process target object 11 was immersed in the warm water 46 at the 1st heat treatment process, this invention is not limited to this, Since the process target object 11 and the warm water 46 contact. If there is, the hot water 46 may flow over the surface of the processing object 11, or the hot water 46 may be sprayed on the surface of the processing object 11.
更に、第二の熱処理工程においても、熱水が処理対象物11と接触するのであれば、熱水を処理対象物11の表面にかけ流してもよいし、熱水を処理対象物11表面に噴霧してもよい。
第二の温度は第一の温度以上であればよいが、酸化アルミニウムと水酸化アルミニウムを十分に水和させるためには、100℃以上が望ましい。
Further, in the second heat treatment step, as long as the hot water comes into contact with the object to be treated 11, the hot water may flow over the surface of the object to be treated 11, or the hot water is sprayed on the surface of the object to be treated 11. May be.
The second temperature may be equal to or higher than the first temperature, but is preferably 100 ° C. or higher in order to sufficiently hydrate aluminum oxide and aluminum hydroxide.
電解液は、多孔質のアノード酸化皮膜12が形成されるのであれば特に限定されない。多孔質のアノード酸化皮膜12が形成される電解液としては、シュウ酸と、硫酸と、リンゴ酸と、マロン酸とからなる群より選択されるいずれか1種類以上の酸を、水に溶解させた水溶液がある。 The electrolytic solution is not particularly limited as long as the porous anodic oxide film 12 is formed. As an electrolytic solution in which the porous anodic oxide film 12 is formed, any one or more acids selected from the group consisting of oxalic acid, sulfuric acid, malic acid, and malonic acid are dissolved in water. There is an aqueous solution.
第一の熱処理に用いる温水46は、純水やアンモニア水に限定されない。例えば、純水に、アンモニアと、トリエタノールアミンと、ヒドラジンとからなる群より選択されるいずれか1種類のアルカリを添加したアルカリ性水溶液を用いることができる。 The hot water 46 used for the first heat treatment is not limited to pure water or ammonia water. For example, an alkaline aqueous solution in which any one kind of alkali selected from the group consisting of ammonia, triethanolamine, and hydrazine is added to pure water can be used.
また、第二の熱処理に用いる熱水と水蒸気も、純水に限定されない。例えば、純水に、アンモニアと、トリエタノールアミンと、ヒドラジンとからなる群より選択されるいずれか1種類のアルカリを添加したアルカリ性水溶液を用いることができる。
尚、上記温水46、熱水、水蒸気に添加するアルカリは特に限定されないが、第一、第二の熱処理工程後の洗浄工程を簡潔にするためには、揮発性のものが望ましい。
Also, hot water and water vapor used for the second heat treatment are not limited to pure water. For example, an alkaline aqueous solution in which any one kind of alkali selected from the group consisting of ammonia, triethanolamine, and hydrazine is added to pure water can be used.
The alkali added to the hot water 46, hot water, and water vapor is not particularly limited, but a volatile one is desirable in order to simplify the cleaning step after the first and second heat treatment steps.
本発明による封孔処理で形成される緻密層の厚さは0.5μm以上2μm以下である。
処理対象物は表面にアノード酸化被膜が形成されるのであれば、特に限定されない。例えば、全部がアルミニウム材料で構成されたものを用いてもよいし、アルミニウム材料以外の材料で構成された芯材の表面に、アルミニウム材料の薄膜が形成されたものを用いてもよい。
The thickness of the dense layer formed by the sealing treatment according to the present invention is 0.5 μm or more and 2 μm or less.
The object to be treated is not particularly limited as long as an anodic oxide film is formed on the surface. For example, an all-aluminum material may be used, or a core material made of a material other than an aluminum material may be used in which a thin film of an aluminum material is formed.
尚、アルミニウム材料はアルミニウムを主成分とするものであれば特に限定されない。この場合、主成分とはアルミニウムを50原子%以上含有するものであればよく、アルミニウムの形態はアルミニウム単体であってもよいし、合金であってもよい。 The aluminum material is not particularly limited as long as it is mainly composed of aluminum. In this case, the main component only needs to contain 50 atomic% or more of aluminum, and the form of aluminum may be an aluminum simple substance or an alloy.
アルミニウム材料で構成された部材の耐食性を上げるための表面処理に用いられる。CVD装置や、エッチング装置等の真空槽の内壁を構成する内壁部材や、アンテナ部材等、真空槽の内部に露出して、反応ガスや、反応ガスのプラズマやラジカルと接触する虞のある部材に特に適している。 Used for surface treatment to increase the corrosion resistance of members made of aluminum materials. For members that are exposed to the inside of the vacuum chamber, such as the inner wall member constituting the inner wall of the vacuum chamber, such as a CVD device or an etching device, or an antenna member, and that may come into contact with the reaction gas, plasma of the reactive gas, or radicals Especially suitable.
11……処理対象物 12……アノード酸化皮膜 46……温水 11 …… Treatment object 12 …… Anodic oxide film 46 …… Warm water
Claims (2)
前記アノード酸化皮膜の緻密化は、70℃以上90℃以下の第一の温度にされた純水の温水を前記アノード酸化皮膜に15分以上の時間接触させた後、
前記第一の温度よりも高い100℃以上の第二の温度にされた熱水を前記アノード酸化被膜に接触させ、又は前記第一の温度よりも高い100℃以上の前記第二の温度にされた水蒸気を、常圧以上の圧力にした処理槽内で、前記アノード酸化皮膜に接触させ、前記アノード酸化被膜の表面を、膜厚1.0μm以上の緻密層にする保護膜製造方法。 A method for producing a protective film, comprising densifying the anodic oxide film of a treatment target having an anodic oxide film of aluminum formed on a surface thereof, and producing a protective film,
The densification of the anodic oxide film is performed by bringing warm water of pure water brought to a first temperature of 70 ° C. or higher and 90 ° C. or lower into contact with the anodic oxide film for 15 minutes or more ,
Said first hot water that is high in 100 ° C. over a second temperature higher than the temperature in contact with the anode oxide film, or the first temperature the second temperature of 100 ° C. or higher have higher than A method for producing a protective film, wherein the water vapor is brought into contact with the anodic oxide film in a treatment tank having a pressure equal to or higher than normal pressure, and the surface of the anodic oxide film is formed into a dense layer having a thickness of 1.0 μm or more.
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| JP2007315770A JP5265181B2 (en) | 2007-12-06 | 2007-12-06 | Protective film manufacturing method |
| PCT/JP2008/072024 WO2009072546A1 (en) | 2007-12-06 | 2008-12-04 | Method for forming protective film |
| CN2008801191634A CN101889108B (en) | 2007-12-06 | 2008-12-04 | Protective film manufacturing method |
| KR1020107010913A KR101222921B1 (en) | 2007-12-06 | 2008-12-04 | Method for forming protective film |
| TW097147427A TWI481748B (en) | 2007-12-06 | 2008-12-05 | Method for producing a protective film |
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| KR20110131136A (en) * | 2010-05-28 | 2011-12-06 | 성균관대학교산학협력단 | Flexible organic / inorganic composite protective film for preventing moisture and / or oxygen permeation, preparation method thereof, and electronic device comprising the flexible organic / inorganic composite protective film |
| DE102012204636A1 (en) * | 2012-03-22 | 2013-09-26 | Nanogate Ag | Treatment of anodized surface |
| CN102660763B (en) * | 2012-05-07 | 2014-09-03 | 复旦大学 | Preparation method and application of a high catalytic property TiO2 nanotube array film |
| US9702053B2 (en) * | 2012-06-29 | 2017-07-11 | Apple Inc. | Elimination of crazing in anodized layers |
| JP6562500B2 (en) * | 2015-03-31 | 2019-08-21 | 地方独立行政法人山口県産業技術センター | Surface-treated aluminum material and manufacturing method thereof |
| JPWO2017018462A1 (en) * | 2015-07-30 | 2018-06-28 | 富士フイルム株式会社 | Aluminum plate |
| US11312107B2 (en) * | 2018-09-27 | 2022-04-26 | Apple Inc. | Plugging anodic oxides for increased corrosion resistance |
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| GB965837A (en) * | 1962-06-19 | 1964-08-06 | Charles Calvin Cohn | Treatment of aluminum oxide coatings |
| JPS5273140A (en) * | 1975-12-15 | 1977-06-18 | Matsushita Electric Industrial Co Ltd | Production process for alumite products |
| ATE138T1 (en) * | 1978-05-22 | 1981-08-15 | Alcan Res & Dev | PROCESS FOR DIGESTING ANODISED ALUMINUM AND THE PRODUCT THUS OBTAINED. |
| CN1003656B (en) * | 1986-07-09 | 1989-03-22 | 国家海洋局海洋技术研究所 | Sealing method of anodic aluminum oxide |
| JP2614133B2 (en) * | 1990-04-20 | 1997-05-28 | 富士写真フイルム株式会社 | Surface treatment device for printing plate support |
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