JPS6323460B2 - - Google Patents
Info
- Publication number
- JPS6323460B2 JPS6323460B2 JP55143220A JP14322080A JPS6323460B2 JP S6323460 B2 JPS6323460 B2 JP S6323460B2 JP 55143220 A JP55143220 A JP 55143220A JP 14322080 A JP14322080 A JP 14322080A JP S6323460 B2 JPS6323460 B2 JP S6323460B2
- Authority
- JP
- Japan
- Prior art keywords
- film
- treatment
- metal salt
- current
- aqueous solution
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
Landscapes
- Electrochemical Coating By Surface Reaction (AREA)
Description
産業上の利用分野
この発明は、アルミニウムまたはアルミニウム
合金を基体とした太陽熱集熱板等の製造に於て、
アルミニウム材の表面に太陽熱エネルギーの選択
吸収膜を形成する方法に関する。
従来の技術
従来、アルミニウム材の表面に太陽熱エネルギ
ーの良好な選択吸収膜を形成するための一般的な
方法として、先ずアルミニウム材を陽極酸化処理
してその表面に多孔性の陽極酸化皮膜を生成せし
めたのち、次いでこれを金属塩を含む水溶液中で
電解処理して前記酸化皮膜の微細孔中に金属を折
出充填せしめ、もつて黒色化された所期する選択
吸収膜を得る方法が既知である。
ところで、一般的に太陽熱選択吸収膜の評価
は、太陽光に対する吸収率αを放射率εとの関係
で比較するのが普通であり、特に好ましい選択吸
収膜としては吸収率αが0.90以上、放射率εが
0.10以下であることが必要であるが、これを満足
するためには、先ず皮膜厚さを1μ以下の厚さで
生成せしめることが必要である。
これが1μを超えると、太陽熱エネルギーを吸
収してもその多くを輻射エネルギーとして放出し
てしまうので、放射率εが悪くなる。
そこで、前記陽極酸化処理は、皮膜形成を厚さ
1μ以下に制御して行うことを好適とするが、斯
る薄膜の陽極酸化皮膜に対して次段に行われる二
次電解処理は、皮膜破壊を生じさせることなく、
しかも充分に良好な着色効果が得られるような配
慮のもとに行われなければならない。而して、従
来、この二状電解処理は、金属の穏やかな析出効
果を得るために、一般的には交流を用いて電解す
ることによつて行われていた。
発明が解決しようとする問題点
ところが、従来の交流を用いて行う二次電解処
理によるときは、その処理時間を長く要し、良好
な黒色化のためには一般的に5〜10分以上の処理
時間を必要とするため、ひいては選択吸収膜の形
成作業能率に劣るという問題点があつた。
問題点を解決するための手段
この発明は、かゝる問題点に鑑み、特に第2工
程の金属塩処理における処理時間の短縮化をはか
ることを目的としたものであり、該工程の電解に
特定の波形電流を用いることによつて電解時間を
顕著に短縮しうることを見出し、これを完成した
ものである。
即ち、この発明は、アルミニウム材を陽極酸化
処理し、厚さ1μ以下の陽極酸化皮膜を形成した
のち、金属塩を含む水溶液中で電解処理して太陽
熱エネルギーの選択吸収膜を形成する方法におい
て、前記金属塩を含む水溶液中での電解処理を、
電流の正負が交番的に変換しかつ負の電圧が5〜
25Vで正の電圧より1.1〜1.5倍高いPR波形の電流
を用いて行うことを特徴とするアルミニウム材の
表面に太陽熱エネルギーの選択吸収膜を形成する
方法を特徴とするものである。
この発明に用いる前記PR波形(Periodic
reverse)の電流は、正と負が非対称に交番的に
変換するものであるが、こゝに正と負の各波高
値、即ち電圧条件が金属塩処理効果に大きく影響
する。負の電圧は殊に金属の析出(着色)速度と
皮膜性能に影響を与えるものであり、これを5〜
25Vの範囲に調整することが必要である。これが
5V未満の場合には、着色速度を早める効果に乏
しく、電解着色工程の短時間処理という所期する
効果を充分に満足せしめることができない。反対
に25Vを超える場合には、電解により水素ガスが
発生し、皮膜の破壊等の欠陥が生じる。
正の電圧は、上記負の電圧値に左右されるもの
であるが、好適には5〜15Vの範囲に設定され
る。
正負の両電圧値の相対関係では、正の電圧値を
1とした場合、負の電圧値は1.1〜1.5倍の範囲に
設定すべきであり、この範囲を逸脱すると、前記
電圧範囲が規定値から逸脱する場合と同様の欠点
が派生する。
正負の通電時間は、処理浴によつて変わるが、
負の通電時間を正より長くした方が着色時間の短
縮に効果がある。しかしあまり長くすると水素ガ
スが発生し、スポーリング現象が生ずる。
なお、この発明は上述のように、特に第2工程
としての金属塩処理の時間短縮をはかることを目
的として、それに用いる電解波形に特徴を有する
ものである。従つて、第1工程の陽極酸化処理条
件は何ら限定されるものではなく、従来の常法に
よつて処理しうる。しかしながら、この陽極酸化
処理も、従来の常法によるときはその処理に10〜
15分もの長時間を要するものであつたのに対し、
該処理を、濃度50g/l以上の高濃度のリン酸水
溶液中で、しかも液温を35〜80℃の高温度に設定
して行うものとすることにより、0.5〜3.0分の極
めて短時間で処理可能となり、しかも選択吸収性
の良好な厚さ1μ以下で安定した酸化皮膜を生成
せしめることが可能となる。従つて、かゝる陽極
酸化処理と組合わせてこの発明の金属塩処理を実
施することにより、選択吸収膜の形成のための全
体としての処理時間を大幅に短縮化することがで
き、しかも吸収率(α)および放射率(ε)の相
対評価において卓越した性能を有する良好な選択
吸収膜を形成せしめることが可能となる。
発明の効果
二次電解に上記のような特殊波形の電流を用い
て電解するこの発明の方法によれば、第1工程で
生成せしめた極薄の、即ち厚さ1μ以下の陽極酸
化皮膜の黒色化のための二次電解処理、即ち金属
塩処理に要する時間を1〜2分としてしかも良好
な選択吸収膜を得ることができるものであり、従
来の交流を用いる場合に5〜10分要していた処理
時間を顕著に短縮し得て生産性の大幅な向上をは
かることができるものである。
実施例
次に、この発明の実施例を、比較例との対比に
おいて示す。
JIS・A1050Pの純度を有する厚さ1mmのアルミ
ニウム板を用い、これを通常の前処理方法で脱脂
したのち、液温30℃の40g/リン酸水溶液中
で、対極にカーボンを用い、直流8Vで15分間陽
極酸化処理した。
次いで、第2工程として、上記第1工程により
得られたアルミニウム板を、下記A,Bの液組成
からなる25℃の電解液中で、交流及び各種PR波
形の直流を用い、かつ電解処理時間を変えて電解
処理した。
電解液組成
A:酢酸ニツケル 45g/
ホウ酸 45g/
PH 6.4
Industrial Application Field This invention is applicable to the production of solar heat collector plates etc. using aluminum or aluminum alloy as a base.
The present invention relates to a method for forming a selective solar energy absorption film on the surface of an aluminum material. Conventional technology Conventionally, as a general method for forming a film that selectively absorbs solar thermal energy on the surface of an aluminum material, the aluminum material is first anodized to form a porous anodic oxide film on its surface. There is a known method in which the oxide film is then electrolytically treated in an aqueous solution containing a metal salt to precipitate and fill the fine pores of the oxide film, thereby obtaining the desired blackened selective absorption film. be. By the way, in general, solar heat selective absorption films are evaluated by comparing the absorption rate α of sunlight in relation to the emissivity ε. Particularly preferable selective absorption films are those with an absorption rate α of 0.90 or more and a radiation The rate ε
It is necessary that the thickness be 0.10 or less, but in order to satisfy this, it is first necessary to form a film with a thickness of 1 μm or less. If this exceeds 1μ, even if solar thermal energy is absorbed, much of it will be emitted as radiant energy, resulting in poor emissivity ε. Therefore, the anodic oxidation treatment reduces the thickness of the film.
Although it is preferable to control the thickness to 1μ or less, the secondary electrolytic treatment performed on such a thin anodic oxide film in the next step can be carried out without causing film destruction.
Moreover, consideration must be given to obtaining a sufficiently good coloring effect. Conventionally, this two-state electrolytic treatment has generally been carried out by electrolyzing with alternating current in order to obtain a mild metal deposition effect. Problems to be Solved by the Invention However, when using the conventional secondary electrolytic treatment using alternating current, the treatment time is long, and it generally takes 5 to 10 minutes or more to achieve good blackening. Since this method requires a long processing time, there is a problem in that the efficiency of forming the selective absorption membrane is poor. Means for Solving the Problems In view of the above problems, the present invention aims to shorten the treatment time, particularly in the second step of metal salt treatment. They discovered that the electrolysis time could be significantly shortened by using a specific waveform current, and this was completed. That is, the present invention provides a method in which an aluminum material is anodized to form an anodic oxide film with a thickness of 1 μm or less, and then electrolytically treated in an aqueous solution containing a metal salt to form a selective solar energy absorption film. Electrolytic treatment in an aqueous solution containing the metal salt,
The positive and negative currents are changed alternately and the negative voltage is 5~
This method is characterized by using a PR waveform current of 25V, which is 1.1 to 1.5 times higher than the positive voltage, to form a selective absorption film for solar thermal energy on the surface of an aluminum material. The PR waveform (Periodic
The current (reverse) is one in which the positive and negative currents are asymmetrically and alternately converted, and the positive and negative peak values, that is, the voltage conditions, greatly affect the metal salt treatment effect. Negative voltage particularly affects the metal deposition (coloring) rate and film performance, and this can be
It is necessary to adjust to the 25V range. This is
If the voltage is less than 5 V, the effect of accelerating the coloring speed is poor, and the desired effect of shortening the electrolytic coloring process cannot be sufficiently achieved. On the other hand, if the voltage exceeds 25V, hydrogen gas is generated due to electrolysis, resulting in defects such as destruction of the film. The positive voltage depends on the negative voltage value, but is preferably set in the range of 5 to 15V. Regarding the relative relationship between both positive and negative voltage values, if the positive voltage value is 1, then the negative voltage value should be set in the range of 1.1 to 1.5 times, and if it deviates from this range, the voltage range will change to the specified value. The same disadvantages arise when deviating from The positive and negative current application times vary depending on the treatment bath, but
It is more effective to shorten the coloring time by making the negative energization time longer than the positive energization time. However, if it is too long, hydrogen gas will be generated and a spalling phenomenon will occur. As described above, the present invention is characterized by the electrolysis waveform used for the purpose of shortening the time required for the metal salt treatment as the second step. Therefore, the conditions for the anodizing treatment in the first step are not limited at all, and the treatment can be carried out by any conventional method. However, when this anodic oxidation treatment is performed using the conventional method,
Whereas it used to take a long time of 15 minutes,
By performing this treatment in a highly concentrated phosphoric acid aqueous solution with a concentration of 50 g/l or more and setting the liquid temperature at a high temperature of 35 to 80°C, the treatment can be carried out in an extremely short time of 0.5 to 3.0 minutes. It becomes possible to produce a stable oxide film with a thickness of 1 μm or less that has good selective absorption properties. Therefore, by carrying out the metal salt treatment of the present invention in combination with such anodic oxidation treatment, the overall processing time for forming a selective absorption film can be significantly shortened, and moreover, the absorption It becomes possible to form a good selective absorption film having excellent performance in relative evaluation of radiation rate (α) and emissivity (ε). Effects of the Invention According to the method of the present invention, which uses a current with a special waveform as described above for secondary electrolysis, the ultrathin anodic oxide film produced in the first step, that is, the thickness of 1 μm or less, becomes black. The secondary electrolytic treatment for oxidation, that is, the metal salt treatment, requires only 1 to 2 minutes, and a good selective absorption membrane can be obtained, compared to 5 to 10 minutes when conventional alternating current is used. This makes it possible to significantly shorten processing time and significantly improve productivity. Examples Next, examples of the present invention will be shown in comparison with comparative examples. Using a 1 mm thick aluminum plate with JIS/A1050P purity, it was degreased using the usual pretreatment method, and then heated at 8 V DC using carbon as a counter electrode in a 40 g/phosphoric acid aqueous solution at a temperature of 30°C. Anodized for 15 minutes. Next, as a second step, the aluminum plate obtained in the first step was electrolyzed in an electrolytic solution at 25°C having the following liquid compositions A and B using alternating current and direct current with various PR waveforms, and for an electrolytic treatment time. Electrolytic treatment was performed by changing the Electrolyte composition A: Nickel acetate 45g/boric acid 45g/PH 6.4
【表】【table】
【表】
上表より明らかなように、この発明によれば、
第2工程の金属塩処理を1〜2分の極めて短時間
で行い得てしかも選択吸収性能に優れた選択吸収
膜を得ることができる。[Table] As is clear from the above table, according to this invention,
The metal salt treatment in the second step can be carried out in an extremely short time of 1 to 2 minutes, and a selective absorption membrane having excellent selective absorption performance can be obtained.
Claims (1)
以下の陽極酸化皮膜を形成したのち、金属塩を含
む水溶液中で電解処理して太陽熱エネルギーの選
択吸収膜を形成する方法において、前記金属塩を
含む水溶液中での電解処理を、電流の正負が交番
的に変換しかつ負の電圧が5〜25Vで正の電圧よ
り1.1〜1.5倍高いPR波形の電流を用いて行うこと
を特徴とするアルミニウム材の表面に太陽熱エネ
ルギーの選択吸収膜を形成する方法。1 Aluminum material is anodized and has a thickness of 1μ
In the method of forming the following anodic oxide film and then electrolytically treating it in an aqueous solution containing a metal salt to form a film that selectively absorbs solar thermal energy, the electrolytic treatment in an aqueous solution containing the metal salt is performed depending on the polarity of the current. Forming a selective absorption film for solar thermal energy on the surface of an aluminum material, which is characterized by alternating conversion and using a current with a PR waveform in which the negative voltage is 5 to 25 V and is 1.1 to 1.5 times higher than the positive voltage. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14322080A JPS5767749A (en) | 1980-10-13 | 1980-10-13 | Formation of solar energy selective absorptive film on surface of aluminum material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14322080A JPS5767749A (en) | 1980-10-13 | 1980-10-13 | Formation of solar energy selective absorptive film on surface of aluminum material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5767749A JPS5767749A (en) | 1982-04-24 |
| JPS6323460B2 true JPS6323460B2 (en) | 1988-05-17 |
Family
ID=15333679
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14322080A Granted JPS5767749A (en) | 1980-10-13 | 1980-10-13 | Formation of solar energy selective absorptive film on surface of aluminum material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5767749A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5426014A (en) * | 1977-07-29 | 1979-02-27 | Fuji Giken Kogyo | Vacuum block |
-
1980
- 1980-10-13 JP JP14322080A patent/JPS5767749A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5767749A (en) | 1982-04-24 |
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