JPH09178392A - Manufacture of heat exchanger made of aluminum and being excellent in corrosion resistance - Google Patents

Manufacture of heat exchanger made of aluminum and being excellent in corrosion resistance

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Publication number
JPH09178392A
JPH09178392A JP33534495A JP33534495A JPH09178392A JP H09178392 A JPH09178392 A JP H09178392A JP 33534495 A JP33534495 A JP 33534495A JP 33534495 A JP33534495 A JP 33534495A JP H09178392 A JPH09178392 A JP H09178392A
Authority
JP
Japan
Prior art keywords
heat exchanger
corrosion resistance
metal oxide
sol
aluminum
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.)
Pending
Application number
JP33534495A
Other languages
Japanese (ja)
Inventor
Kazunobu Shimakage
和宜 嶋影
Shinji Hirai
伸治 平井
Tomiyoshi Kanai
富義 金井
Isao Makita
功 牧田
Mikio Kondo
幹夫 近藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Showa Aluminum Can Corp
Original Assignee
Showa Aluminum Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Showa Aluminum Corp filed Critical Showa Aluminum Corp
Priority to JP33534495A priority Critical patent/JPH09178392A/en
Publication of JPH09178392A publication Critical patent/JPH09178392A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To manufacture a heat exchanger made of aluminum and being excellent in corrosion resistance without causing a problem of pollution due to release of sexivalent chromium and the like, by coating the surface with a metal oxide film by a sol-gel process. SOLUTION: A plurality of flat tube elements 1 each of which is formed by joining the peripheral end parts of paired core plates 3 by soldering and has a refrigerant passage inside and a plurality of corrugated fins 2 are stacked alternately and soldered, while side plates 4 are placed outside the outermost fins 2 and an inlet header 5 and an outlet header are provided. On the other hand, a sol solution of a metal oxide is prepared and made to stick on the stacked type heat exchanger by a dip coating method. Next, the heat exchanger whereon the sol solution sticks is subjected to a drying treatment by leaving it in the atmosphere at room temperature and then subjected to a heating treatment in the atmosphere of oxygen. These processes from sticking to heating are repeated. Herein the metal oxide is an oxide of Zr, Ti, Hf or Al.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、例えばカーエア
コン用蒸発器、凝縮器、産業用ラジエータ、オイルクー
ラー等として使用されるようなアルミニウム製熱交換器
の製造方法、特に耐食性に優れたアルミニウム製熱交換
器の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing an aluminum heat exchanger, which is used as an evaporator, a condenser, an industrial radiator, an oil cooler, etc. for a car air conditioner, and in particular, an aluminum heat exchanger excellent in corrosion resistance. The present invention relates to a method for manufacturing a heat exchanger.

【0002】なお、この明細書においてアルミニウムの
語はアルミニウム及びその合金を含む意味で用いられ
る。
In this specification, the term aluminum is used to mean aluminum and its alloys.

【0003】[0003]

【従来の技術】上記のようなアルミニウム製熱交換器
は、腐食環境下での使用に耐え得るものとするために、
耐食性を付与されたものに構成されることがある。
2. Description of the Related Art Aluminum heat exchangers such as those described above are designed to withstand use in corrosive environments.
It may be configured to have corrosion resistance.

【0004】このような耐食性付与のための方法の一つ
として、熱交換器を表面処理して耐食性を有する皮膜を
形成する方法がある。かかる表面処理法は、薄肉のアル
ミニウム材に対しても適用可能であることから、強度に
優れてはいるが耐食性にやや劣る超々ジュラルミン等の
アルミニウム材に適用することにより、薄肉軽量でかつ
強度、耐食性ともに優れた熱交換器を提供し得る利点が
ある。
As one of the methods for imparting such corrosion resistance, there is a method in which a heat exchanger is surface-treated to form a film having corrosion resistance. Since such a surface treatment method can be applied to a thin aluminum material, by applying it to an aluminum material such as ultra-super duralumin which is excellent in strength but slightly inferior in corrosion resistance, it is thin and lightweight, and strength, There is an advantage that a heat exchanger having excellent corrosion resistance can be provided.

【0005】従来、上記のような熱交換器に対する耐食
性皮膜形成のための表面処理方法としては、熱交換器を
クロメート処理したのち、要すればさらに樹脂塗装を施
すことが一般的に行われていた。
Conventionally, as a surface treatment method for forming a corrosion resistant film on a heat exchanger as described above, it has been generally practiced to subject the heat exchanger to chromate treatment and then, if necessary, further coat a resin. It was

【0006】[0006]

【発明が解決しようとする課題】ところが、クロメート
処理はCrO3 と鉱酸を処理液に用いることから、6価
クロムの大気中への放出が公害問題となっており、その
放出規制が年々厳しくなっているため、クロメート処理
に代わる新しいアルミニウム製熱交換器の耐食性向上の
ための表面処理法の開発が急務となっている。
However, since the chromate treatment uses CrO 3 and a mineral acid in the treatment liquid, the release of hexavalent chromium into the atmosphere has become a pollution problem, and its release regulations are becoming stricter year by year. Therefore, there is an urgent need to develop a surface treatment method to improve the corrosion resistance of a new aluminum heat exchanger that replaces the chromate treatment.

【0007】この発明は、上記問題に鑑み、6価クロム
の放出等に起因する公害問題を生じることなく、耐食性
に優れたアルミニウム製熱交換器を製造することのでき
る製造方法の提供を目的とするものである。
In view of the above problems, an object of the present invention is to provide a manufacturing method capable of manufacturing an aluminum heat exchanger having excellent corrosion resistance without causing pollution problems due to the release of hexavalent chromium. To do.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
に、この発明に係る耐食性に優れたアルミニウム製熱交
換器の製造方法は、ゾル−ゲル法によって表面に金属酸
化物皮膜を被覆することを特徴とするものである。
In order to achieve the above object, a method of manufacturing an aluminum heat exchanger having excellent corrosion resistance according to the present invention comprises coating a surface with a metal oxide film by a sol-gel method. It is characterized by.

【0009】ゾル−ゲル法は、一般的には金属の有機ま
たは無機化合物の溶液を加水分解、重縮合させてゾル溶
液を作成し、更に反応を進めることによってゲル化さ
せ、このゲルを加熱することによって金属酸化物の固体
を得る方法である。具体的には、該ゾル溶液を被処理物
に何等かの方法で付着せしめた後、乾燥することによっ
て被処理物表面のゾルをゲル化し、さらにこのゲルを加
熱することによって金属酸化物の皮膜を被処理物に被覆
形成するものである。本発明において、このようなゾル
−ゲル法を用いるのは、比較的簡易な工程で均一かつ緻
密な金属酸化物皮膜を確実に形成することができるから
である。
In the sol-gel method, a solution of a metal organic or inorganic compound is generally hydrolyzed and polycondensed to prepare a sol solution, which is further gelled by further reaction, and the gel is heated. This is a method of obtaining a solid of a metal oxide. Specifically, after the sol solution is attached to the object to be treated by some method, the sol on the surface of the object to be treated is gelated by drying, and the gel is further heated to form a metal oxide film. To form a coating on the object to be treated. In the present invention, such a sol-gel method is used because a uniform and dense metal oxide film can be reliably formed by a relatively simple process.

【0010】また、前記金属酸化物を構成する金属は、
特に限定されることはないが、硬質でより耐食性に優れ
た皮膜とするためには、Zr、Ti、Hf、Si、Al
のいずれの中から1種以上を用いることが好ましい。ま
た、前記ゾル−ゲル法の出発物質となる金属化合物とし
ては金属アルコキシドが好ましい。具体的にはジルコニ
ウムテトラノルマルブトキシド、チタンテトライソプロ
ポキシド、ハフニウムエトキシド、テトラエチルオルソ
シリケイト、アルミニウムセカンダリーブトキシド等が
挙げられる。
The metal constituting the metal oxide is
Although it is not particularly limited, Zr, Ti, Hf, Si and Al are required to form a hard and more excellent corrosion resistance film.
It is preferable to use one or more of the above. Further, a metal alkoxide is preferable as the metal compound which is the starting material of the sol-gel method. Specific examples thereof include zirconium tetranormal butoxide, titanium tetraisopropoxide, hafnium ethoxide, tetraethyl orthosilicate, aluminum secondary butoxide and the like.

【0011】ゾル溶液は上記金属化合物の中から1種以
上をアルコール等の溶媒に溶解し、水や酸その他添加物
を加えることにより作成される。該ゾル溶液中の金属化
合物等の濃度は任意であるが、被処理物である熱交換器
のフィン等の微細な隙間がゾル溶液によって目詰まりを
起こす恐れがあるため、比較的粘性の小さいゾル溶液に
調整するのが好ましい。具体的には、粘度1〜10mP
a・sが望ましい。
The sol solution is prepared by dissolving one or more of the above metal compounds in a solvent such as alcohol and adding water, an acid and other additives. The concentration of the metal compound or the like in the sol solution is arbitrary, but a fine sol such as fins of a heat exchanger, which is an object to be processed, may be clogged with the sol solution, so that the sol having a relatively low viscosity is used. It is preferable to prepare a solution. Specifically, the viscosity is 1 to 10 mP
a · s is desirable.

【0012】前記ゾル溶液を被処理物に付着せしめる方
法としては、ディップコーティング法やスピンコート
法、ロールコート法等従来公知の方法を適宜採択すれば
良いが、複雑形状の被処理物も簡単に処理できることか
ら、ディップコーティング法を採用するのが簡易性の点
で好ましい。
As a method for adhering the sol solution to the object to be treated, a conventionally known method such as a dip coating method, a spin coating method, a roll coating method may be appropriately adopted, but an object having a complicated shape can be easily treated. It is preferable to use the dip coating method because it can be processed.

【0013】また、この発明では、結果的に熱交換器の
表面に金属酸化物の皮膜が形成されれば良く、必ずしも
熱交換器の完成後に皮膜形成処理を行わなければならな
いものではない。例えば、熱交換器に組み立てられる前
の構成部品の段階で処理しても良いし、あるいはフィン
等のようにコイルから成形されるものにあっては、成形
前のコイルフォームの状態で皮膜を形成しても良い。も
とより、熱交換器の完成後に処理しても良く、処理の時
期は限定されることはない。なお、金属酸化物皮膜を密
着性良く被覆するために、ゾル溶液付着前に被処理物を
十分に脱脂・洗浄・乾燥させるのが好ましい。
Further, according to the present invention, it is sufficient that a metal oxide film is formed on the surface of the heat exchanger as a result, and it is not always necessary to perform the film forming treatment after the heat exchanger is completed. For example, it may be processed at the stage of component parts before being assembled in a heat exchanger, or, in the case of a product formed from a coil such as fins, a film is formed in the state of coil form before forming. You may. Of course, the heat exchanger may be treated after completion, and the timing of the treatment is not limited. In order to coat the metal oxide film with good adhesion, it is preferable to sufficiently degrease, wash, and dry the object to be treated before attaching the sol solution.

【0014】ゾル溶液の付着後に乾燥、加熱工程を順次
的に実施する。この乾燥、加熱工程によって、被処理物
の表面に付着したゾル溶液がゲル化する。乾燥は、例え
ば大気中において、常温〜60℃で5〜10分間放置す
ることにより行えば良い。一方、乾燥後の加熱は含酸素
雰囲気中で行うのが、緻密で密着力が高くより優れた耐
食性皮膜を形成し得る点から好ましい。具体的には、大
気中または酸素気流中で温度150〜350℃、時間5
〜60分間の範囲で行うのが良い。かかる加熱工程によ
って金属酸化物の皮膜が被覆形成される。
After the deposition of the sol solution, the drying and heating steps are sequentially carried out. By this drying and heating process, the sol solution attached to the surface of the object to be treated is gelled. The drying may be carried out, for example, by leaving it in the air at room temperature to 60 ° C. for 5 to 10 minutes. On the other hand, it is preferable that the heating after drying is performed in an oxygen-containing atmosphere from the viewpoint that a dense and high adhesive force can form a more excellent corrosion resistant film. Specifically, the temperature is 150 to 350 ° C. for 5 hours in the atmosphere or oxygen stream.
It is good to do in the range of ~ 60 minutes. The metal oxide film is formed by the heating process.

【0015】金属酸化物の皮膜厚さは、0.1〜5.0
μmに設定するのが良い。0.1μm未満では耐食性の
防止効果に乏しく、逆に5.0μmを超えても該効果が
飽和する。皮膜の形成は、上記付着・乾燥・加熱の工程
を複数回繰り返すことにより行うのが望ましい。処理を
繰り返すことによって、皮膜が複数層に亘って形成さ
れ、より優れた密着性、平滑性、緻密性、耐食性を発揮
するからである。なお、皮膜厚さの制御は、付着・乾燥
・加熱工程の繰返し回数、ゾル溶液中の金属酸化物成分
の濃度、ゾル溶液の粘度、ディップコーティング法の場
合はゾル溶液からの引上げ速度等を調節することにより
行えば良い。
The film thickness of the metal oxide is 0.1 to 5.0.
It is better to set to μm. If it is less than 0.1 μm, the effect of preventing corrosion resistance is poor, and conversely if it exceeds 5.0 μm, the effect is saturated. It is desirable to form the film by repeating the above-mentioned steps of adhesion, drying and heating a plurality of times. By repeating the treatment, a film is formed over a plurality of layers, and more excellent adhesion, smoothness, denseness, and corrosion resistance are exhibited. The thickness of the film can be controlled by adjusting the number of times the adhesion, drying, and heating steps are repeated, the concentration of metal oxide components in the sol solution, the viscosity of the sol solution, and the pulling rate from the sol solution in the case of the dip coating method. You can do it by doing.

【0016】上記ゾル−ゲル法によれば、6価クロム等
の公害成分を大気に放出することなく、耐食性皮膜であ
る金属酸化物皮膜をアルミニウム製熱交換器に被覆する
ことができる。また、被覆された金属酸化物皮膜はそれ
自体緻密であるため、該皮膜が被覆された熱交換器の表
面は大気等と遮断され水等の浸透もなく、従ってクロメ
ート処理を施した熱交換器と同等ないしはそれ以上の優
れた耐食性を示す。さらに、金属酸化物皮膜は撥水性を
有するため、塩水等の腐食液が付着してもはじかれて該
腐食液との長時間の接触が回避され、このため益々耐食
性が向上する。かつまた、熱交換器を蒸発器として用い
た場合のように、熱交換器の動作によってフィンに水滴
が付着しても、該水滴がはじかれて転がり落ちるため、
水滴が溜まることによる通風空気の圧力損失が抑止さ
れ、熱交換器の熱交換効率を高く維持することができ
る。
According to the above-mentioned sol-gel method, the aluminum heat exchanger can be coated with the metal oxide film which is a corrosion resistant film without releasing pollutant components such as hexavalent chromium into the atmosphere. Further, since the coated metal oxide film is dense in itself, the surface of the heat exchanger coated with the film is shielded from the atmosphere and the like, and water and the like do not permeate. Therefore, the heat exchanger subjected to chromate treatment. Excellent corrosion resistance equivalent to or higher than. Further, since the metal oxide film has water repellency, even if a corrosive liquid such as salt water adheres, the metal oxide film is repelled and long-term contact with the corrosive liquid is avoided, so that the corrosion resistance is further improved. Also, even if water droplets adhere to the fins due to the operation of the heat exchanger as in the case where the heat exchanger is used as an evaporator, the water droplets are repelled and roll off,
The pressure loss of the ventilation air due to the accumulation of water droplets is suppressed, and the heat exchange efficiency of the heat exchanger can be maintained high.

【0017】[0017]

【実施例】次に、この発明にかかるアルミニウム製熱交
換器の製造方法の具体的一実施例について説明する。
EXAMPLE A specific example of a method for manufacturing an aluminum heat exchanger according to the present invention will be described below.

【0018】被処理物としては、図1および図2に示す
組立後のアルミニウム製積層型熱交換器を用いた。この
積層型熱交換器は、カークーラー用の蒸発器等に用いら
れるものであり、1対のコアプレート(3)(3)の周
端部をろう付接合することにより形成されかつ内部に冷
媒通路を有する複数枚の偏平チューブエレメント(1)
と、複数枚のコルゲートフィン(2)とが交互に積層さ
れろう付された形式のものである。なお、該熱交換器を
構成するアルミニウムとしてはJIS3003合金を使
用した。また、図1、図2において(4)(4)は最外
側のフィンの外側に配置されたサイドプレート、(5)
(6)は入口ヘッダーと出口ヘッダーである。
As the object to be treated, the laminated aluminum heat exchanger shown in FIGS. 1 and 2 was used. This laminated heat exchanger is used for an evaporator for car coolers, and is formed by brazing the peripheral ends of a pair of core plates (3) and (3) together with a refrigerant inside. Plural flat tube elements with passages (1)
And a plurality of corrugated fins (2) are alternately laminated and brazed. JIS3003 alloy was used as the aluminum forming the heat exchanger. Further, in FIGS. 1 and 2, (4) and (4) are side plates arranged outside the outermost fin, and (5)
(6) is an entrance header and an exit header.

【0019】一方、ゾル溶液として、表1に示す各種の
ものを用意した。各ゾル溶液は、表1に示されるそれぞ
れ複数の成分を混合し十分に撹拌することにより作成し
た。また、ゾル溶液の粘度はいずれも1.3〜1.6m
Pa・sとした。
On the other hand, various sol solutions shown in Table 1 were prepared. Each sol solution was prepared by mixing a plurality of components shown in Table 1 and thoroughly stirring them. Moreover, the viscosity of the sol solution is 1.3 to 1.6 m in all cases.
Pa · s.

【0020】そして、ディップコーティング法により前
記積層型熱交換器に上記のゾル溶液を付着した。具体的
に説明すると、上記ゾル溶液を相対湿度50〜60%の
窒素雰囲気中に配置するとともに、ゾル溶液に前記熱交
換器を浸漬し、数回溶液中で揺動した後、3mm/秒の
速度で引上げた。なお、付着工程を窒素雰囲気中で行っ
たのは大気中の湿度がゾルの粘度変化に及ぼす影響を避
けるためであるが、特に窒素雰囲気に限定される必要は
ない。
Then, the sol solution was attached to the laminated heat exchanger by a dip coating method. More specifically, the sol solution is placed in a nitrogen atmosphere having a relative humidity of 50 to 60%, the heat exchanger is dipped in the sol solution, shaken in the solution for several times, and then at 3 mm / sec. Pulled up at speed. The adhesion step was performed in a nitrogen atmosphere in order to avoid the influence of atmospheric humidity on the viscosity change of the sol, but it is not particularly limited to the nitrogen atmosphere.

【0021】次に、ゾル溶液が付着した上記熱交換器を
大気中室温にて5分間放置して乾燥処理を行った後、純
酸素雰囲気中で300℃にて30分間加熱処理を行っ
た。
Next, the heat exchanger having the sol solution adhered thereto was left to stand in the air at room temperature for 5 minutes to be dried, and then heat-treated in a pure oxygen atmosphere at 300 ° C. for 30 minutes.

【0022】上記のような付着工程から加熱工程までを
表2に示されるように2〜6回繰り返し、耐食試験に供
する各種のサンプルを作成した。また比較例として、前
記実施例と同様の熱交換器を用いまったく表面処理を施
していないものと、クロメート処理したものの2種類の
サンプルを準備した。
The above-described adhesion process to heating process were repeated 2 to 6 times as shown in Table 2 to prepare various samples for the corrosion resistance test. Further, as comparative examples, two types of samples were prepared, one using the same heat exchanger as in the above-mentioned example, which was not subjected to any surface treatment, and the other which was chromate treated.

【0023】上記各サンプルにつき、JIS Z237
1に準じた塩水噴霧試験を行い、試験開始から144時
間後、500時間後、900時間後の時点で熱交換器の
表面を目視にて観察し発錆の状況を評価した。耐食性の
評価としては白錆の発生面積が全体の面積の50%以上
の場合をレイティングナンバー(以下R.N.)1と
し、ついで25%以上50%未満をR.N.2、10%
以上25%未満をR.N.3、10%未満をR.N.
4、まったく白錆が発生しない場合をR.N.5と評価
した。以上の結果を表2に示す。
For each of the above samples, JIS Z237
The salt spray test according to 1 was performed, and the surface of the heat exchanger was visually observed at 144 hours, 500 hours, and 900 hours after the start of the test to evaluate the rusting condition. For evaluation of corrosion resistance, a rating number (hereinafter, RN) of 1 is used when the area where white rust is generated is 50% or more of the entire area, and then 25% or more and less than 50% is R.N. N. 2, 10%
R.I. N. If less than 3, 10% is R. N.
4. If no white rust occurred, R. N. It was evaluated as 5. Table 2 shows the above results.

【0024】[0024]

【表1】 [Table 1]

【表2】 [Table 2]

【0025】上記の表2から明らかなように、この発明
によれば、クロメート処理した従来法による熱交換器の
耐食性と同等の耐食性を得ることができることを確認で
きた。
As is clear from Table 2 above, it has been confirmed that according to the present invention, corrosion resistance equivalent to that of the conventional chromate-treated heat exchanger can be obtained.

【0026】さらに、皮膜の水に対する濡れ性を接触角
測定法により測定したところ、サンプルNo1の本発明
実施品の表面は102゜であり、クロメート処理したサ
ンプルNo9の比較品の表面の70〜80゜に比べて撥
水性が高いものであった。
Further, the wettability of the film with water was measured by the contact angle measuring method, and the surface of the sample of the present invention of sample No. 1 was 102 °, which was 70 to 80 of the surface of the comparative sample of chromate-treated sample No9. The water repellency was higher than that of β.

【0027】[0027]

【発明の効果】以上説明したように、この発明はゾル−
ゲル法によってアルミニウム製熱交換器の表面処理を行
うため、6価クロム等の公害物質を大気中に放出するこ
となく、クロメート処理した場合と同等ないしはそれ以
上の耐食性を示す金属酸化物皮膜を被覆することができ
る。従って、公害問題等を生じることなく耐食性に優れ
た熱交換器を提供することが可能となる。
As described above, the present invention is a sol-
Since the surface treatment of the aluminum heat exchanger is performed by the gel method, it does not release pollutants such as hexavalent chromium into the atmosphere, and it is coated with a metal oxide film that exhibits corrosion resistance equivalent to or higher than that of chromate treatment. can do. Therefore, it is possible to provide a heat exchanger having excellent corrosion resistance without causing pollution problems and the like.

【0028】しかも、被覆された金属酸化物皮膜はクロ
メート処理した表面よりも撥水性が高いため、塩分等を
含んだ腐食液が付着してもすぐに転がり落ちるため、該
腐食液との長期接触を防止でき、益々熱交換器の耐食性
を向上できる。加えて、フィン等に水滴が付着してもフ
ィン表面を転がり落ちるため、該水滴がフィンに付着し
て起こる風圧損失を抑えることができ、熱交換効率を向
上させることができる。
Moreover, since the coated metal oxide film has higher water repellency than the chromate-treated surface, even if a corrosive liquid containing salt etc. adheres, the metal oxide film rolls off immediately, so that long-term contact with the corrosive liquid is caused. Can be prevented, and the corrosion resistance of the heat exchanger can be improved more and more. In addition, even if water drops adhere to the fins or the like, they roll down on the fin surface, so that it is possible to suppress wind pressure loss that occurs when the water drops adhere to the fins, and it is possible to improve heat exchange efficiency.

【0029】また、金属酸化物がZr,Ti,Hf,S
i,Alのいずれか1種または2種以上の金属の酸化物
からなるものである場合には、より耐食性に優れた皮膜
となしえ、さらに耐食性に優れた熱交換器を提供でき
る。
The metal oxide is Zr, Ti, Hf, S.
When it is made of any one of i and Al, or an oxide of two or more kinds of metals, it is possible to provide a heat exchanging film having a more excellent corrosion resistance.

【0030】また、ゾル−ゲル法において、加熱工程を
含酸素雰囲気中で行う場合には、緻密で密着力が高くよ
り優れた耐食性皮膜を形成することができ、益々耐食性
に優れた熱交換器を提供できる。
Further, in the sol-gel method, when the heating step is carried out in an oxygen-containing atmosphere, it is possible to form a dense, high-adhesion and excellent corrosion-resistant film, and a heat exchanger having even more excellent corrosion resistance. Can be provided.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 この発明の実施例におけるサンプルとして使
用したアルミニウム製積層型熱交換器の一部を分解して
示した斜視図である。
FIG. 1 is a perspective view showing a disassembled part of an aluminum laminated heat exchanger used as a sample in an embodiment of the present invention.

【図2】 同積層型熱交換器の正面図である。FIG. 2 is a front view of the laminated heat exchanger.

【符号の説明】 1…チューブエレメント 2…フィン 3…サイドプレート[Explanation of symbols] 1 ... Tube element 2 ... Fin 3 ... Side plate

フロントページの続き (72)発明者 牧田 功 堺市海山町6丁224番地 昭和アルミニウ ム株式会社内 (72)発明者 近藤 幹夫 堺市海山町6丁224番地 昭和アルミニウ ム株式会社内Front page continuation (72) Inventor Isao Makita 6224, Kaiyamacho, Sakai City, Showa Aluminum Co., Ltd. (72) Inventor, Mikio Kondo, 6224, Kaiyamacho, Sakai City, Showa Aluminum Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 ゾル−ゲル法によって表面に金属酸化物
皮膜を被覆することを特徴とする耐食性に優れたアルミ
ニウム製熱交換器の製造方法。
1. A method of manufacturing an aluminum heat exchanger having excellent corrosion resistance, which comprises coating a surface with a metal oxide film by a sol-gel method.
【請求項2】 金属酸化物がZr,Ti,Hf,Si,
Alのいずれの中から1種以上の金属の酸化物からなる
ことを特徴とする請求項1に記載の耐食性に優れたアル
ミニウム製熱交換器の製造方法。
2. The metal oxide is Zr, Ti, Hf, Si,
The method for manufacturing an aluminum heat exchanger having excellent corrosion resistance according to claim 1, wherein the method comprises an oxide of at least one metal selected from any of Al.
【請求項3】 ゾル−ゲル法において、加熱工程を含酸
素雰囲気中で行うことを特徴とする請求項1または2に
記載の耐食性に優れたアルミニウム製熱交換器の製造方
法。
3. The method for producing an aluminum heat exchanger having excellent corrosion resistance according to claim 1, wherein the heating step in the sol-gel method is performed in an oxygen-containing atmosphere.
JP33534495A 1995-12-22 1995-12-22 Manufacture of heat exchanger made of aluminum and being excellent in corrosion resistance Pending JPH09178392A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33534495A JPH09178392A (en) 1995-12-22 1995-12-22 Manufacture of heat exchanger made of aluminum and being excellent in corrosion resistance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33534495A JPH09178392A (en) 1995-12-22 1995-12-22 Manufacture of heat exchanger made of aluminum and being excellent in corrosion resistance

Publications (1)

Publication Number Publication Date
JPH09178392A true JPH09178392A (en) 1997-07-11

Family

ID=18287478

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33534495A Pending JPH09178392A (en) 1995-12-22 1995-12-22 Manufacture of heat exchanger made of aluminum and being excellent in corrosion resistance

Country Status (1)

Country Link
JP (1) JPH09178392A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000075397A1 (en) * 1999-06-04 2000-12-14 Calsonickansei Corp. Heat exchanger made of aluminum alloy
CN102906527A (en) * 2010-05-26 2013-01-30 阿尔法拉瓦尔股份有限公司 Heat exchanger plates with anti-fouling properties
CN103958998A (en) * 2011-11-28 2014-07-30 阿尔法拉瓦尔股份有限公司 Block-type plate heat exchanger with anti-fouling properties

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000075397A1 (en) * 1999-06-04 2000-12-14 Calsonickansei Corp. Heat exchanger made of aluminum alloy
US6869677B1 (en) 1999-06-04 2005-03-22 Calsonickansei Corporation Heat exchanger made of aluminum alloy
KR100706972B1 (en) * 1999-06-04 2007-04-13 칼소닉 칸세이 코포레이숀 Heat exchanger made of aluminum alloy
CN102906527A (en) * 2010-05-26 2013-01-30 阿尔法拉瓦尔股份有限公司 Heat exchanger plates with anti-fouling properties
CN102906527B (en) * 2010-05-26 2016-07-06 阿尔法拉瓦尔股份有限公司 There is the heat exchanger plate of ant-scaling character
EP2577209B1 (en) * 2010-05-26 2017-10-04 Alfa Laval Corporate AB Heat exchanger plates with anti-fouling properties
CN103958998A (en) * 2011-11-28 2014-07-30 阿尔法拉瓦尔股份有限公司 Block-type plate heat exchanger with anti-fouling properties
CN103958998B (en) * 2011-11-28 2016-11-09 阿尔法拉瓦尔股份有限公司 There is the block-type heat-exchangers of the plate type of the dirty character of anti-caking

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