JPS6152901B2 - - Google Patents
Info
- Publication number
- JPS6152901B2 JPS6152901B2 JP55096681A JP9668180A JPS6152901B2 JP S6152901 B2 JPS6152901 B2 JP S6152901B2 JP 55096681 A JP55096681 A JP 55096681A JP 9668180 A JP9668180 A JP 9668180A JP S6152901 B2 JPS6152901 B2 JP S6152901B2
- Authority
- JP
- Japan
- Prior art keywords
- film
- aluminum plate
- selective absorption
- concentration
- 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.)
- 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
- Y02E10/44—Heat exchange systems
Landscapes
- Electrochemical Coating By Surface Reaction (AREA)
Description
【発明の詳細な説明】
この発明は、アルミニウム又はアルミニウム合
金を基体とする太陽熱集熱板材の連続的製造方法
に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for continuously manufacturing a solar heat collecting plate material having aluminum or an aluminum alloy as a base material.
アルミニウム材を基体とする太陽熱集熱板とし
ては、該アルミニウム材を先ず陽極酸化処理して
その表面に多孔性酸化皮膜を形成し、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皮膜
の微細孔に金属を析出充填せしめ、もつて表面に
黒色化された太陽熱エネルギーの選択吸収膜を生
成せしめたものが多く用いられている。かかる集
熱板の選択吸収膜は、性能的に太陽熱エネルギー
の吸収率(α)が可及的大であり、一方輻射エネ
ルギーとして放熱する放射率(ε)が可及的小な
るものであることが要求される。このような要求
から、上記選択吸収膜は、好ましくは厚さ1μ以
下の極薄膜に形成せられるものであり、しかもそ
れ自体強度的に弱いものであるところから、非常
に傷がつき易くかつ耐摩耗性にも乏しい。このた
め、選択吸収膜形成後の板材は、その取扱いに細
心の注意が必要であり、もとより選択吸収膜形成
後にこれを所要形状に成形加工するというような
ことは極めて困難であつた。従つて従来では、ア
ルミニウム板材に予め加工、成形を施したあと
で、前述の如き選択吸収膜の生成のための表面処
理を行つているのが普通であり、該表面処理工程
を連続的に実施できないために、その製造能率が
悪い欠点があつた。 For a solar heat collecting plate based on an aluminum material, the aluminum material is first anodized to form a porous oxide film on its surface, and then this is electrolytically treated in an aqueous solution containing a metal salt to form the film. Many are used in which metal is precipitated and filled into the fine pores of the solar cell, resulting in a blackened surface that selectively absorbs solar thermal energy. In terms of performance, the selective absorption film of such a heat collecting plate should have the highest possible solar thermal energy absorption rate (α), while the emissivity (ε) for dissipating heat as radiant energy should be as low as possible. is required. In view of these requirements, the selective absorption membrane is preferably formed into an extremely thin film with a thickness of 1 μm or less, and since it itself is weak in strength, it is extremely easily scratched and has poor durability. It also has poor abrasion resistance. For this reason, the plate material after the selective absorption membrane has been formed must be handled with great care, and it has been extremely difficult to mold it into a desired shape after the selective absorption membrane has been formed. Therefore, conventionally, the surface treatment for producing the selective absorption film as described above is usually performed after processing and forming the aluminum plate material in advance, and the surface treatment process is carried out continuously. As a result, the manufacturing efficiency was low.
この発明はかかる問題点の解決をはかることを
目的とするものであり、更に具体的には、選択吸
収膜の形成後において所要の加工、成形を行いう
るような、太陽熱集熱板材の能率的な製造方法を
提供しようとするものである。 The purpose of this invention is to solve these problems, and more specifically, to improve the efficiency of solar heat collecting plate materials, which can be processed and formed as required after forming a selective absorption film. The aim is to provide a manufacturing method that is easy to use.
而して、この発明は、コイル状に形成したアル
ミニウム板をその一端から引出して陽極酸化処理
を施し、次いで金属塩を含む水溶液中で電解処理
してアルミニウム板面に太陽熱エネルギーの選択
吸収膜を連続的に形成したのち、別途コイル状に
形成した合成樹脂保護フイルムをその一端から引
出して前記選択吸収膜面上に重ね、1対の弾性圧
着ロール間に導いて連続的にかつ剥離可能な状態
に貼合わせることを特徴とするものである。 Therefore, in this invention, an aluminum plate formed in a coil shape is pulled out from one end, subjected to anodizing treatment, and then electrolytically treated in an aqueous solution containing a metal salt to form a selective solar energy absorption film on the aluminum plate surface. After continuous formation, a synthetic resin protective film separately formed into a coil shape is pulled out from one end, overlaid on the selective absorption film surface, and guided between a pair of elastic pressure rolls in a state where it can be continuously and peeled off. It is characterized by being attached to.
これを更に図示実施例について説明すれば、1
はコイル状に形成してアルミニウム板であり、こ
れを該コイルから連続的に引出して先ず前処理部
2に導き、所定の脱脂等の前処理を施す。次いで
これを次位の陽極酸化処理部3に導き、硫酸、シ
ユウ酸、リン酸等の水容液を電解液として陽極酸
化処理を施し、アルミニウム板の表面に多孔性陽
極酸化皮膜を形成する。続いてこの酸化皮膜を形
成したアルミニウム板を次位の電解着色処理部4
に導き、ここで、ニツケル塩、銅塩、錫塩、コバ
ルト塩、鉄塩等の一種以上の金属塩を含む水溶液
を電解液として電解処理を施し、前記酸化皮膜の
微細孔中に金属を析出充填せしめてアルミニウム
板表面に黒色化された所期する太陽熱エネルギー
の選択吸収膜を形成する。次にこれをある程度乾
燥せしめたのち、アルミニウム板を更に次位に配
置した1対のゴム製圧着ロール5,5間に連続的
に導くと共に別途コイル状に形成された合成樹脂
保護フイルム6を該コイルから連続的に引出して
同時に圧着ロール5,5間に導き、該保護フイル
ム6を前記選択吸収膜面上に重ねてロールの加圧
力で圧着し、両者を貼合わせる。保護フイルム6
は、アルミニウム板に対して剥離可能な態様にて
貼合わせるものであり、その材料としては例えば
ポリエチレン、ポリプロピレン等が好適に用いら
れる。保護フイルム6を貼り合わせたアルミニウ
ム板1は、これをコイル7に巻取つて太陽熱集熱
板材として提供されるものである。 To further explain this with reference to the illustrated embodiments, 1
is an aluminum plate formed into a coil shape, which is continuously drawn out from the coil and first led to the pretreatment section 2, where it is subjected to a predetermined pretreatment such as degreasing. This is then led to the next anodizing section 3, where it is anodized using an aqueous solution of sulfuric acid, oxalic acid, phosphoric acid, etc. as an electrolyte to form a porous anodic oxide film on the surface of the aluminum plate. Subsequently, the aluminum plate with this oxide film formed thereon is sent to the next electrolytic coloring treatment section 4.
Here, an electrolytic treatment is performed using an aqueous solution containing one or more metal salts such as nickel salts, copper salts, tin salts, cobalt salts, and iron salts as an electrolyte to precipitate metals into the micropores of the oxide film. By filling the aluminum plate, a blackened film selectively absorbing solar energy is formed on the surface of the aluminum plate. Next, after drying this to some extent, it is continuously guided between a pair of rubber pressure bonding rolls 5, 5, which are placed next to the aluminum plate, and a synthetic resin protective film 6, which is separately formed into a coil shape, is applied to the film. The protective film 6 is continuously drawn out from the coil and simultaneously introduced between the pressure bonding rolls 5, 5, and the protective film 6 is superimposed on the surface of the selective absorption membrane and crimped by the pressing force of the rolls to bond the two together. Protective film 6
is attached to an aluminum plate in a peelable manner, and the material thereof is preferably polyethylene, polypropylene, etc. The aluminum plate 1 to which the protective film 6 is bonded is wound around a coil 7 and provided as a solar heat collecting plate material.
このようにして製造された太陽熱集熱板材は、
これに所要の加工、成形を施し所定寸法に切断し
たのち、保護フイルム6を剥離して最終製品たる
太陽熱集熱板に製作される。上記の加工、成形工
程は、たとえば集熱板材に吸熱管を嵌合するため
の凹溝を形成する工程、この凹溝に銅パイプ等か
らなる吸熱管を嵌合固定する工程、その後これを
コイルに巻取つて運搬等の取扱いに供する工程等
からなるものである。 The solar heat collecting plate material manufactured in this way is
After this is subjected to necessary processing and molding and cut to a predetermined size, the protective film 6 is peeled off to produce a final product, a solar heat collecting plate. The above-mentioned processing and forming steps include, for example, forming grooves in the heat collecting plate material for fitting heat absorption tubes, fitting and fixing heat absorption tubes made of copper pipes etc. into the grooves, and then coiling them into coils. It consists of the process of winding up and handling such as transportation.
ところで、アルミニウム板の前記陽極酸化処理
工程、および金属塩を含む水溶液中での電解着色
処理工程の各電解処理条件は、この発明において
特に限定されるものではない。しかし、この発明
はアルミニウム板をコイルにより連続処理するも
のであるから、上記各工程の処理時間は可及的短
時間であることが望ましいことはいうまでもな
い。このような要請に対処するため、種々実験と
研究の結果から見出したところによれば、選択吸
収膜生成のための上記各工程の電解条件として、
陽極酸化皮膜を生成せしめる第1工程の陽極酸化
処理は、これを特に、液濃度50g/以上のリン
酸水容液中で、かつ液温を35〜80℃に保持して行
うものとし、また皮膜黒色化のための第2工程の
金属塩処理は、電解液中の金属塩の濃度が従来の
常法の該電解処理に用いられる液濃度よりも相対
的に高濃度の、たとえばニツケル塩において50〜
200g/、コバルト塩において50〜200g/、
銅塩において15〜100g/、錫塩において5〜
50g/、鉄塩において5〜50g/の濃度の金
属塩水溶液中で、しかも液温を高温の35〜85℃に
保持して行うものとすることが好ましい。 By the way, the electrolytic treatment conditions of the anodic oxidation treatment step of the aluminum plate and the electrolytic coloring treatment step in an aqueous solution containing a metal salt are not particularly limited in the present invention. However, since the present invention involves continuously processing an aluminum plate using a coil, it goes without saying that it is desirable that the processing time of each of the above steps be as short as possible. In order to meet these demands, we have found out from the results of various experiments and research that the electrolytic conditions for each of the above steps for selective absorption membrane production are as follows:
The first step of anodizing treatment, which produces an anodic oxide film, is carried out in a phosphoric acid aqueous solution with a concentration of 50 g/min or more, and the temperature of the solution is maintained at 35 to 80°C, and The second step of metal salt treatment for blackening the film is performed using a method in which the concentration of metal salt in the electrolytic solution is relatively higher than that used in the conventional electrolytic treatment, such as nickel salt. 50~
200g/, 50-200g/ in cobalt salt,
15-100g/for copper salt, 5-100g/for tin salt
It is preferable to carry out the reaction in an aqueous metal salt solution having a concentration of 50 g/min and iron salt at a concentration of 5 to 50 g/min and keeping the liquid temperature at a high temperature of 35 to 85°C.
このような処理条件によれば、両工程の合計処
理時間を1〜5分程度で、しかも膜厚t=1μ以
下、吸収率α=0.9以上、放射率ε=0.1以下の優
れた選択吸収性能を有する太陽熱選択吸収膜を生
成せしめることができる。 According to these processing conditions, the total processing time for both steps is approximately 1 to 5 minutes, and excellent selective absorption performance is achieved with film thickness t = 1 μ or less, absorption rate α = 0.9 or more, and emissivity ε = 0.1 or less. It is possible to produce a solar heat selective absorption film having the following properties.
陽極酸化処理工程の電解液として、特にリン酸
水溶液を用いるのが好ましい理由は、硫酸やシユ
ウ酸等の水溶液を用いる場合に較べて、生成しう
る皮膜厚さが薄く、しかもその微細孔の孔径の大
きいものが得られ、結果的に金属の析出量を大と
して一層良好な選択吸収膜を得ることができるこ
とに基づく。リン酸水溶液を用いる陽極酸化処理
の従来の一般的な処理条件は、液濃度20〜30g/
、液温20〜30℃、電流密度0.2〜0.4A/dm2
D・Cであり、その処理時間は概ね15分間程度で
あつた。このような従来の一般的な処理条件に較
べて、上記の液濃度および液温は、かなり高い値
に設定されるものである。当該液濃度の上限は、
経済性、および皮膜の良好な生成状態を考慮した
場合、一応800g/程度と考えられる。一方50
g/未満の濃度では、必要とする皮膜厚さを得
るのに長時間を要し、短時間では安定した皮膜が
得られない。かかる事項から、特に好適な濃度範
囲は80〜300g/である。また液温度は、液濃
度との相対関係で決められるものであるが、35℃
未満では必要とする酸化皮膜厚さを得るのに長時
間を要し、安定した皮膜が得られず、逆に80℃を
超える場合は、皮膜の溶解作用が大となるため、
必要な皮膜厚さを得ることが困難になり、又パウ
ダー状の乳白色皮膜となる不都合が派生する。液
濃度と温度との関係で相対的な好適範囲を示せ
ば、濃度70g/〜150g/に対し、液温45〜
55℃程度の範囲が好ましい。 The reason why it is especially preferable to use an aqueous phosphoric acid solution as the electrolyte in the anodizing process is that the thickness of the film that can be formed is thinner than when using an aqueous solution such as sulfuric acid or oxalic acid, and the pore size of the micropores is smaller. This is based on the fact that a large amount of metal can be obtained, and as a result, an even better selective absorption membrane can be obtained by increasing the amount of metal precipitated. Conventional general processing conditions for anodizing using a phosphoric acid aqueous solution are a solution concentration of 20 to 30 g/
, liquid temperature 20~30℃, current density 0.2~0.4A/ dm2
D.C., and the processing time was approximately 15 minutes. Compared to such conventional general processing conditions, the above-mentioned liquid concentration and liquid temperature are set to considerably higher values. The upper limit of the concentration of the liquid is
Considering economic efficiency and good film formation, the amount is considered to be about 800 g/approx. while 50
If the concentration is less than g/g, it takes a long time to obtain the required film thickness, and a stable film cannot be obtained in a short time. From this point of view, a particularly suitable concentration range is 80 to 300 g/g/. Also, the liquid temperature is determined by the relative relationship with the liquid concentration, but it is 35℃.
If the temperature is below 80°C, it will take a long time to obtain the required oxide film thickness and a stable film will not be obtained;
It becomes difficult to obtain the necessary film thickness, and the disadvantage is that the film becomes powdery and milky white. If we show the relative preferable range in relation to liquid concentration and temperature, the concentration is 70g/~150g/, and the liquid temperature is 45~150g/.
A range of about 55°C is preferable.
また、皮膜黒色化のための金属塩処理におい
て、金属塩を含む水溶液の濃度および液温を前記
範囲に設定するのは、いずれもそれらが下限未満
であると、良好な選択吸収膜を生成せしめるのに
長時間を要する欠点があり、また濃度が上限値を
超えるとコスト高になると共に、着色性が悪くな
つて良好な選択吸収膜の生成が困難になり、また
温度が上限値を超えると皮膜の溶解作用が大きく
なつてやはり良好な選択吸収膜が得られないこと
に基づくものである。特に好ましい濃度範囲は、
ニツケル塩において80〜130g/、コバルト塩
において80〜130g/、銅塩において30〜50
g/、錫塩にいて15〜30g/、鉄塩において
60〜100g/の範囲であり、また温度は特に40
〜60℃の範囲が好適である。 In addition, in the metal salt treatment for blackening the film, the concentration and temperature of the aqueous solution containing the metal salt are set within the above ranges.If both are below the lower limit, a good selective absorption film will be produced. However, if the concentration exceeds the upper limit, the cost will increase, the colorability will deteriorate, making it difficult to form a good selective absorption film, and if the temperature exceeds the upper limit, This is because the dissolving action of the film increases, making it impossible to obtain a good selective absorption film. A particularly preferable concentration range is
80-130g/ for nickel salt, 80-130g/ for cobalt salt, 30-50g/ for copper salt
g/, in tin salt 15-30 g/, in iron salt
The range is 60 to 100g/, and the temperature is especially 40g/
A range of ~60°C is preferred.
この発明は上述の次第で、コイル状のアルミニ
ウム板に、陽極酸化処理、および金属塩を含む水
溶液中での電解処理を順次施して選択吸収膜を連
続的に形成したのち、該選択吸収膜面上にコイル
状の合成樹脂保護フイルムを連続的にしかも弾性
ロールによる圧着により剥離可能な状態に貼合わ
せるものであるから、得られた太陽熱集熱板材
は、選択吸収膜面がフイルムによつて保護された
ものとなり、これに吸熱管の取付け等のための加
工、成形等を行つても選択吸収膜に有害な傷を発
生するおそれのないものとなしうる。かつその他
の取扱い中の傷発生をも防止しうるので、取扱い
が容易で作業性の良好なものとなしうる。このよ
うに加工、成形工程の前に、アルミニウム板をコ
イルで連続処理して選択吸収膜の形成を行うこと
を可能にするものであるから、従来のように加
工、成形後にそれを行う場合に較べて大幅に選択
吸収膜形成工程の高能率化をはかることができ、
ひいては太陽熱集熱板の製造能率を顕著に向上し
て、その製造コストを大幅に低減せしめることが
可能になる。 As described above, the present invention involves sequentially forming a selective absorption membrane on a coiled aluminum plate by sequentially subjecting it to anodizing treatment and electrolytic treatment in an aqueous solution containing a metal salt. A coiled synthetic resin protective film is continuously pasted onto the top in a peelable state by pressure bonding with an elastic roll, so the obtained solar heat collecting plate material has a selective absorption film surface protected by the film. Even if processing, molding, etc. for attaching a heat absorption tube to the selective absorption membrane are carried out, there is no risk of damaging the selective absorption membrane. In addition, it is possible to prevent other scratches from occurring during handling, resulting in easy handling and good workability. In this way, before the processing and forming process, it is possible to continuously process the aluminum plate with a coil to form a selective absorption film, so when doing it after processing and forming as in the past, The efficiency of the selective absorption film formation process can be greatly improved compared to the previous method.
As a result, it becomes possible to significantly improve the manufacturing efficiency of solar heat collecting plates and significantly reduce the manufacturing cost.
図面はこの発明の実施例態様を示すブロツク図
である。
1……アルミニウム板のコイル、2……前処理
部、3……陽極酸化処理部、4……電解着色処理
部、5……圧着ロール。
The drawing is a block diagram showing an embodiment of the invention. DESCRIPTION OF SYMBOLS 1... Aluminum plate coil, 2... Pretreatment section, 3... Anodizing section, 4... Electrolytic coloring section, 5... Pressing roll.
Claims (1)
一端から引出して陽極酸化処理を施し、次いで金
属塩を含む水溶液中で電解処理してアルミニウム
板面に太陽熱エネルギーの選択吸収膜を連続的に
形成したのち、別途コイル状に形成した合成樹脂
保護フイルムをその一端から引出して前記選択吸
収膜面上に重ね、1対の弾性圧着ロール間に導い
て連続的にかつ剥離可能な状態に貼合わせること
を特徴とする太陽熱集熱板材の連続的製造方法。1. An aluminum plate formed in a coil shape is pulled out from one end and subjected to anodizing treatment, and then subjected to electrolytic treatment in an aqueous solution containing a metal salt to continuously form a selective solar energy absorption film on the aluminum plate surface. , a synthetic resin protective film separately formed into a coil shape is pulled out from one end thereof, overlaid on the surface of the selective absorption film, and guided between a pair of elastic pressure rolls to be laminated continuously and in a releasable state. A continuous manufacturing method for solar heat collecting plate material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9668180A JPS5723093A (en) | 1980-07-14 | 1980-07-14 | Continuous preparation of heat collecting plate material for solar heat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9668180A JPS5723093A (en) | 1980-07-14 | 1980-07-14 | Continuous preparation of heat collecting plate material for solar heat |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5723093A JPS5723093A (en) | 1982-02-06 |
| JPS6152901B2 true JPS6152901B2 (en) | 1986-11-15 |
Family
ID=14171527
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9668180A Granted JPS5723093A (en) | 1980-07-14 | 1980-07-14 | Continuous preparation of heat collecting plate material for solar heat |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5723093A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58153049A (en) * | 1982-03-08 | 1983-09-10 | Sharp Corp | Manufacture of heat collecting element used in solar heat collector |
| JPS61130754A (en) * | 1984-11-30 | 1986-06-18 | Sanou Kogyo Kk | Manufacture of heat collecting fin |
| CN102485967A (en) * | 2010-12-06 | 2012-06-06 | 深圳市鹏桑普太阳能股份有限公司 | Process for preparing continuous anodic oxide film light-absorbing coating |
| JP6535098B2 (en) * | 2015-09-29 | 2019-06-26 | 富士フイルム株式会社 | Method of manufacturing metal-filled microstructure |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS513333A (en) * | 1974-06-27 | 1976-01-12 | Showa Aluminium Co Ltd | |
| JPS54103487A (en) * | 1978-01-31 | 1979-08-14 | Matsushita Electric Works Ltd | Preparation of decorative laminate |
-
1980
- 1980-07-14 JP JP9668180A patent/JPS5723093A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5723093A (en) | 1982-02-06 |
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