JPS6295182A - Production of fin for heat exchanger having excellent wettability - Google Patents

Production of fin for heat exchanger having excellent wettability

Info

Publication number
JPS6295182A
JPS6295182A JP23101085A JP23101085A JPS6295182A JP S6295182 A JPS6295182 A JP S6295182A JP 23101085 A JP23101085 A JP 23101085A JP 23101085 A JP23101085 A JP 23101085A JP S6295182 A JPS6295182 A JP S6295182A
Authority
JP
Japan
Prior art keywords
film
heat exchanger
fin
aluminum material
inorg
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
JP23101085A
Other languages
Japanese (ja)
Inventor
Tetsuji Iwama
岩間 哲治
Tsuyoshi Katsumata
堅 勝又
Hajime Kudo
元 工藤
Isao Takeuchi
竹内 庸
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.)
MA Aluminum Corp
Original Assignee
Mitsubishi Aluminum Co Ltd
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 Mitsubishi Aluminum Co Ltd filed Critical Mitsubishi Aluminum Co Ltd
Priority to JP23101085A priority Critical patent/JPS6295182A/en
Publication of JPS6295182A publication Critical patent/JPS6295182A/en
Pending legal-status Critical Current

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  • Application Of Or Painting With Fluid Materials (AREA)

Abstract

PURPOSE:To obtain the titled fin having excellent wettability by forming an inorg. film on the surface of an Al material, treating the film with an aq. soln. contg. a phosphonic acid, etc., and then applying prescribed working. CONSTITUTION:An inorg. film such as a boehmite film having excellent wettability is formed on the surface of an Al or an Al alloy material. The inorg. film is treated with an aq. soln. contg. one or >=2 kinds of phosphonic acids and the phosphates. The amt. of the film to be deposited, expressed in terms of P, is regulated to 0.0001-0.15g/m<2>. Then prescribed forming is applied, and simple degreasing treatment is carried out. The fins for a heat exchanger thus produced are assembled into a heat exchanger. Since the wettability of the fin surface is not deteriorated due to the improvement of the hydrophilicity and resistance to oil contamination, the air permeability and defrosting property are improved, and the performance of the heat exchanger is also ameliorated.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、例えば、自動車等の熱交換器や家電用冷熱機
器に使用されるアルミニウム又はアルミニウム合金製熱
交換器用フィンの製造方法に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for manufacturing aluminum or aluminum alloy heat exchanger fins used, for example, in heat exchangers for automobiles, etc., and cooling and heating equipment for home appliances. be.

〔従来技術とその問題点〕[Prior art and its problems]

アルミニウム又はアルミニウム合金材(以下単にアルミ
ニウム材)調熱交換器用フィンは、例えば、アルミニウ
ム材表面に有機質、無機質、又は、これらの複合系の水
濡れ性(親水性)の良い皮膜を形成し、この親水性皮膜
の形成されたアルミニウム材をプレス成形して熱交換器
用フィンを形成し、その後プレス加工工程で表面に付着
したプレス油等の潤滑油を中性もしくは弱アルカリ性洗
剤水溶液又は、非水溶液(例えば、パークロルエチレン
、トリクロルエチレン等)で脱脂してから熱交換器用フ
ィンとして製造されている。
Fins for heat control exchangers made of aluminum or aluminum alloy material (hereinafter simply referred to as aluminum material), for example, are made by forming a film with good water wettability (hydrophilicity) of organic, inorganic, or a composite of these on the surface of the aluminum material. The heat exchanger fins are formed by press-molding the aluminum material with the hydrophilic film formed, and then the lubricating oil such as press oil that adhered to the surface during the pressing process is removed using a neutral or weakly alkaline aqueous detergent solution or a non-aqueous solution. For example, fins for heat exchangers are manufactured after degreasing with perchlorethylene, trichlorethylene, etc.).

近年、熱交換効率の向上及び小型化のために、フィンピ
ッチを縮小する傾向にあり、このような場合エバポレー
ターにおいては、大気中の水分のフィンへの凝縮によっ
て通風抵抗の増大、騒音の発生、凝縮水の室内への吹き
出し等が生じ、また、冬期においては室外における除霜
エネルギーの増大等の問題が生ずるために、フィン表面
の水濡れ性及び耐油汚染性の良いことが極めて重要な因
子となっている。
In recent years, there has been a trend to reduce the fin pitch in order to improve heat exchange efficiency and downsize the fins. Good water wettability and oil contamination resistance on the fin surface are extremely important factors because problems such as condensed water blowing out indoors and increased defrosting energy outdoors occur in winter. It has become.

本発明者等は、上記のような点を満足する技術的手段を
開発し、先に提案した(特開昭 58−106396号
)のであるが、これらの技術的手段であっても種々のタ
イプの熱交換器に応用する段階で、必らずしも十分に満
足するものでないことが明らかとなった。すなわち、特
願昭 58−106396号公報提案のプレコートフィ
ン材を所定のプレス成形加工後に於いて、加工時に付与
した表面の潤滑油等をトリクロルエチレン等の有機溶剤
で脱脂洗浄し、エバポレーターとして組み立てたところ
、脱脂浴温度1.脱脂浴中の油濃度等の脱脂条件、陽極
酸化皮膜、ベーマイト系皮膜、水和酸化皮膜、MBV皮
膜等の酸化皮膜の表面形状及び性状等によっては、良好
な水濡れ性、耐油汚染性が得られにくいことが判った。
The present inventors have developed and previously proposed a technical means that satisfies the above points (Japanese Patent Application Laid-open No. 106396/1983), but even with these technical means, there are various types. At the stage of application to heat exchangers, it became clear that the results were not necessarily fully satisfactory. That is, after the pre-coated fin material proposed in Japanese Patent Application No. 58-106396 was subjected to a predetermined press molding process, the lubricating oil applied on the surface during the process was degreased and washed with an organic solvent such as trichlorethylene, and then assembled as an evaporator. However, the degreasing bath temperature is 1. Depending on the degreasing conditions such as the oil concentration in the degreasing bath, the surface shape and properties of the oxide film such as anodized oxide film, boehmite film, hydrated oxide film, MBV film, etc., good water wettability and oil stain resistance can be obtained. It turned out that it was difficult to do so.

〔発明の開示〕[Disclosure of the invention]

本発明者等は、これらの原因について追求する段階で、
アルミニウム材表面の水濡れ性に優れた無機質系多孔質
皮膜は、その多孔性のために成形加工等の加工工程に於
いて付着するプレス油等の油脂類を多孔質皮膜表面に吸
着し定着するので、成形加工終了後にトリクロルエチレ
ン等で脱脂洗浄する際に於いて、それらの油脂吸着物の
除去が不充分となり、その結果、無機質系皮膜自身の良
好なる親水性が阻害されるという知見を得たのである。
The present inventors, at the stage of pursuing these causes,
Due to its porosity, the inorganic porous film on the surface of aluminum materials, which has excellent water wettability, adsorbs and fixes oils and fats such as press oil that adhere to the surface of the porous film during processing processes such as molding. Therefore, when degreasing and cleaning with trichlorethylene etc. after the completion of the molding process, it was found that the removal of these fat and oil adsorbed substances was insufficient, and as a result, the good hydrophilicity of the inorganic film itself was inhibited. It was.

本発明は、これら上記知見に基づき為されたものであり
、その要旨とするところは、アルミニウム材表面に水濡
れ性に優れた無機質系皮膜を形成した後で、ホスホン酸
及びホスホン酸塩類のうちの1種又は2種以上を含有し
、さらに必要に応じて、非イオン界面活性剤を含有する
水溶液で処理し、乾燥後において、該アルミニウム材に
所定の脱脂洗浄条件等に全く影響されない水濡れ性の優
れた熱交換器フィンを得ることにある。
The present invention has been made based on the above findings, and its gist is that after forming an inorganic film with excellent water wettability on the surface of an aluminum material, The aluminum material is treated with an aqueous solution containing one or more of the following and, if necessary, a nonionic surfactant, and after drying, the aluminum material is completely unaffected by predetermined degreasing and cleaning conditions. The objective is to obtain heat exchanger fins with excellent properties.

尚、ここで水濡れ性良好な無機質系皮膜とは、例えば、
陽極酸化皮膜、ヘーマイト系皮膜、ヘーマイト処理又は
陽極酸化処理後ケイ酸塩処理しfコ皮膜、若しくは、ン
リカゾル処理した皮膜、クロメート処理後ケイ酸塩処理
した皮膜、ケイ酸塩塗布皮膜、ソリ力ゾル水溶液による
皮膜、あるいは特開昭58−106397号開示のよう
な酸化剤を添加した浴で生成した酸化皮膜等がある。こ
れらの無機質系皮膜は、例えば、陽極酸化皮膜の場合に
あっては約100〜200人の孔径を、ベーマイト系皮
膜の場合にあっては約500〜1000人の孔径を、ケ
イ酸塩処理した皮膜の場合にあっては約3000〜10
000人の孔径を何しているといったように微細孔を有
する多孔性のものであり、そして無機質系皮膜の厚みは
約0.2〜Ig/m2のものであることが特に望ましい
ものである。
In this case, the inorganic film with good water wettability is, for example,
Anodic oxidation film, hemite-based film, hemite treatment or anodic oxidation treatment followed by silicate treatment fco film, or rica sol treated film, chromate treatment followed by silicate treatment, silicate coated film, warping sol There are films formed by an aqueous solution, or oxide films formed in a bath containing an oxidizing agent as disclosed in JP-A-58-106397. These inorganic coatings are treated with silicate to have a pore size of about 100 to 200 pores in the case of anodized coatings and about 500 to 1000 pores in the case of boehmite coatings. Approximately 3000 to 10 in the case of a film
It is particularly desirable that the inorganic coating is porous with micropores having a pore diameter of about 1,000 people, and that the thickness of the inorganic coating is about 0.2 to Ig/m2.

また、上記無機質系皮膜表面に介在せられるホスホン酸
及びそれらの塩類は、例えば、それらのうちの1種又は
2種以上を含有する水溶液を用いて浸漬、塗布、シャワ
ー等の適宜手段を選んで実施することが出来、それらの
付着皮膜量はo、oooi〜0.15g/m2となるよ
うにその塗布条件が設定される。
In addition, the phosphonic acid and its salts interposed on the surface of the inorganic film can be prepared by, for example, dipping, coating, showering, or other suitable means using an aqueous solution containing one or more of them. The coating conditions are set so that the amount of the deposited film is from o,oooi to 0.15 g/m2.

上記水溶液は、蒸留水、脱イオン水、上水、工業用水等
に上記ホスホン酸及びホスホン酸の塩類のうちの1種又
は2種以上をその濃度か通常0.05%〜溶解度限、好
ましくは、2〜10%として溶解して調整され、処理条
件としては、温度20〜80°C1pH6〜8、時間5
〜20秒間が適正である。
The above aqueous solution is prepared by adding one or more of the above phosphonic acids and phosphonic acid salts to distilled water, deionized water, tap water, industrial water, etc. at a concentration of usually 0.05% to the solubility limit, preferably , 2 to 10%, and the processing conditions include temperature 20 to 80°C, pH 6 to 8, and time 5.
~20 seconds is appropriate.

尚、pHQ整には、上記酸等の水溶液の塩基仕度又は酸
性度を考慮して、ケイ酸、リン酸等の酸性化合物、K 
OHlCa(OHL、アンモニア、トリエタノールアミ
ン等の塩基性化合物のうちから適宜選んで行う。
In addition, for pH adjustment, acidic compounds such as silicic acid and phosphoric acid, K
OHlCa (OHL, ammonia, triethanolamine, and other basic compounds) are suitably selected.

またここで、ホスホン酸等による付着皮膜量かP換算で
0.0001〜0.15g/ m2の範囲と定められた
のは、その皮膜量が0.OQOLg/ m2未満ては、
良好なる親水性が得ずらく、また一方、0.15g/m
2を超えては、良好なるプレス成形性が得られないから
である。
Also, here, the amount of the film attached by phosphonic acid, etc., in terms of P, was determined to be in the range of 0.0001 to 0.15 g/m2, because the amount of the film was 0.0001 to 0.15 g/m2. Less than OQOLg/m2,
Good hydrophilicity is difficult to obtain, and on the other hand, 0.15 g/m
This is because if it exceeds 2, good press formability cannot be obtained.

さらにまた、」二記ホスホン酸等の水溶液に、必要に応
じて、非イオン系界面活性剤を0.1〜2%程度添加し
てしよい。このことにより、上記水溶液の表面張力を下
げたり、これらの皮膜がアルミニウム材表面の無機質系
皮膜の微細孔中への侵入を容易にするばかりでなく、成
形時に使用するプレス4(1等が加工後に於いてら該皮
膜より迅速に脱着しうろようになる等の顕粁な効果があ
る。
Furthermore, about 0.1 to 2% of a nonionic surfactant may be added to the aqueous solution of the phosphonic acid or the like, if necessary. This not only lowers the surface tension of the aqueous solution and makes it easier for these films to penetrate into the micropores of the inorganic film on the surface of the aluminum material, but also allows the press 4 (1 etc. Later on, there are obvious effects such as the film is more quickly desorbed and becomes loose.

尚、本発明に使用するポスホン酸としては、例えば、1
−ヒドロキノプロパン−1,I−ジホスホン酸、l−ヒ
ドロキン−■−フェニルメタンー1、l−ジホスホン酸
、l−ヒドロキシエタン−1、■−ンポスポン酸、■−
アミノエタンー1.1−ジホスホン酸、ツメチルアミノ
ブタン−111−ジホスホン酸、アミノトリメヂレンポ
スホン酸、エヂレンンアミンテトラメチレンポスポン酸
、ポスポン琥珀酸、1−ポスホン−1−メチル琥珀酸等
がある。また、ホスホン酸塩類としては、例えば、上記
ポスポン酸のナトリウム、カリウム、アンモニウム、及
びアルカノールアミン塩等を挙げることができる。
In addition, as the phosphonic acid used in the present invention, for example, 1
-Hydroquinopropane-1,I-diphosphonic acid, l-hydroquine-■-phenylmethane-1, l-diphosphonic acid, l-hydroxyethane-1, ■-polysponic acid, ■-
Aminoethane-1,1-diphosphonic acid, trimethylaminobutane-111-diphosphonic acid, aminotrimedylene phosphonic acid, ethyleneamine tetramethylene posphonic acid, posponsuccinic acid, 1-posphon-1-methylsuccinic acid, etc. There is. Examples of the phosphonates include sodium, potassium, ammonium, and alkanolamine salts of the above-mentioned posonic acids.

さらに又、本発明に使用する非イオン系界面活性剤とし
ては、例えば、ポリオキンエチレンアルギルアリルエー
テル型(例えば、ポリオキシエチレンノニルフェニルエ
ーテル、ポリオキシエチレンノニルフェニルエーテル等
がある。)、アルキルエーテル型(例えば、ポリオキン
エチレンラウリルエーテルがある。)、アルキルエステ
ル型(例えば、ポリオキシエチレンオレエートがある。
Furthermore, the nonionic surfactants used in the present invention include, for example, polyoxyethylene argyl allyl ether type (for example, polyoxyethylene nonylphenyl ether, polyoxyethylene nonylphenyl ether, etc.), alkyl Ether type (for example, polyoxyethylene lauryl ether), alkyl ester type (for example, polyoxyethylene oleate).

)、アルキルアミン型(例えば、ポリオキシエチレンラ
ウリルアミンがある。)、ソルビタン誘導エステル型(
例えば、ソルビタンラウレート、ソルビタンパルミテー
ト等がある。)、ソルヒタン誘導体複合型(例えば、ポ
リオキシエチレンソルビタンラウレート、ポリオキンエ
チレンソルビタンステアレート等がある。)等の中から
必要に応じて適宜選んで使用することができる。
), alkylamine type (for example, polyoxyethylene laurylamine), sorbitan-derived ester type (
Examples include sorbitan laurate, sorbitan palmitate, and the like. ), sorbitan derivative complex type (for example, polyoxyethylene sorbitan laurate, polyoxine ethylene sorbitan stearate, etc.), etc. can be appropriately selected and used as required.

そして、上記のような表面処理の終ったアルミニウム材
は十分に加熱乾燥することが、以後の成形加工又は表面
の皮膜の密着性にとって必須のらのである。
It is essential to sufficiently heat and dry the aluminum material after the surface treatment as described above for the subsequent molding process or the adhesion of the surface film.

このようにして得られるアルミニウム材より熱交換器用
フィンを作るには、ドローレス加工、ドロープレス加工
等の適宜な加工手段が行イつれる。
To make heat exchanger fins from the aluminum material thus obtained, appropriate processing means such as drawless processing and draw press processing are performed.

成形中にアルミニウム材の表面に付着するプレス油等の
潤滑油は、中性又は弱アルカリ性の洗浄剤水溶液又はト
リクロルエチレン等の打機溶剤等で洗浄除去する。
Lubricating oil such as press oil that adheres to the surface of the aluminum material during molding is removed by cleaning with a neutral or weakly alkaline aqueous detergent solution or a punching machine solvent such as trichlorethylene.

AIr汚染性の向上によりフィン表面の水濡れ性(親水
性)が劣化しないので、通風性、除霜性らよく、従って
熱交換器性能の優れた乙のである。又、プレス油等の除
去のための煩雑な工程も要しないことより、製造能率ら
に<低コストで熱交換器を提供しうろようになる。
Since the water wettability (hydrophilicity) of the fin surface does not deteriorate due to the improvement in AIr contamination, ventilation and defrosting properties are good, and therefore the heat exchanger performance is excellent. Further, since no complicated process for removing press oil or the like is required, it becomes possible to provide a heat exchanger at a lower cost with improved manufacturing efficiency.

〔実施例〕〔Example〕

次に、本発明の内容につき各実施例に従い説明する。 Next, the content of the present invention will be explained according to each embodiment.

実施例1 J I S 1200、l−I26アルミニウム材 (
中800mm。
Example 1 JIS 1200, l-I26 aluminum material (
Medium 800mm.

長さ8000m、厚さ0.115mm)を脱脂処理した
後、次亜塩素酸すトリウム水溶液(NaOC,5濃度・
200ppm、 +1111:10.5)中に約85℃
の温度下で浸漬し、約0.6g/m2の水和酸化皮膜を
形成した。ついで、15%1号水ガラ→初液中(pH1
1,4)に約60°Cの温度下で浸漬した後シャワー水
洗工程を経て、アルミニウム材表面にケイ素換算で約0
.025g/m”のケイ酸化合物を形成した。ついで、
温度約30℃、濃度2%に調整した1%ヒドロキシエタ
ン−1,1−ジホスホン酸三ナトリウム塩(三菱モンサ
ンド化成(株)製品:商品名は、デイクエスト2015
DNという。)の水溶液を塗布し、150℃で10秒間
そして上記アルミニウム材にしごき加工を主体としたド
ローレスプレス加工を施して熱交換器用フィンを製造し
た。このように製造したフィンを約80℃に加熱したト
リクロルエチレンに1分間浸漬して脱脂処理を行った。
After degreasing the length of 8000 m and thickness of 0.115 mm, a sodium hypochlorite aqueous solution (NaOC, 5 concentration,
200ppm, +1111:10.5) at about 85℃
A hydrated oxide film of about 0.6 g/m2 was formed by immersion at a temperature of about 0.6 g/m2. Next, 15% No. 1 water glass → initial solution (pH 1
1, 4) at a temperature of about 60°C, and then a shower washing process, which results in approximately 0 silicon equivalent on the surface of the aluminum material.
.. 025 g/m" of silicic acid compound was formed. Then,
1% hydroxyethane-1,1-diphosphonic acid trisodium salt adjusted to a temperature of about 30°C and a concentration of 2% (product of Mitsubishi Monsando Chemical Co., Ltd.: trade name is Dayquest 2015)
It's called DN. ) was applied to the aluminum material for 10 seconds at 150° C., and then the aluminum material was subjected to drawless pressing mainly consisting of ironing to produce fins for heat exchangers. The thus produced fins were immersed in trichlorethylene heated to about 80° C. for 1 minute to perform a degreasing treatment.

実施例2 実施例1と同様にアルミニウム材表面に水濡れ性の良好
な無機質系酸化皮膜を形成した後、液温50°C,濃度
51%にそれぞれ調整したI−ヒドロキシ−1,l−ジ
ホスホン酸(三菱モンサンド化成(株)製品:商品名は
、デイクエスト2010という。)、アミノトリメチレ
ンポスホン酸の五ナトリウム塩(三菱モンサンド化成(
株)製品:商品名は、デイクエスト2006という。)
、及びポリオキシエチレンオレイルエーテル(14LB
価13)を濃度0.05%となるように調整した水溶液
に浸漬処理し、その後150面活性剤層とを該無機質系
皮膜表面に形成した。
Example 2 After forming an inorganic oxide film with good water wettability on the surface of an aluminum material in the same manner as in Example 1, I-hydroxy-1,l-diphosphophone was adjusted to a liquid temperature of 50°C and a concentration of 51%. acid (produced by Mitsubishi Monsando Kasei Co., Ltd.; the product name is DQuest 2010), pentasodium salt of aminotrimethylene phosphonic acid (produced by Mitsubishi Monsando Kasei Co., Ltd.),
Co., Ltd. product: The product name is Dayquest 2006. )
, and polyoxyethylene oleyl ether (14LB
13) was immersed in an aqueous solution adjusted to have a concentration of 0.05%, and then a 150 surfactant layer was formed on the surface of the inorganic film.

そして、該アルミニウム材にドロープレス加工を施して
熱交換器用フィンを製造した。その後、実施例Iと同様
な脱脂処理を行った。
Then, the aluminum material was subjected to draw press processing to produce fins for a heat exchanger. Thereafter, the same degreasing treatment as in Example I was performed.

実施例3 実施例1と同質のアルミニウム材を弱アルカリエツチン
グした後水洗乾燥し、ついで、トリエタノールアミン0
.5%を含む水溶液中に液温90℃で60秒間浸漬して
、ベーマイト処理を行い、該アルミニウム材表面に0.
4g/m2厚の水濡れ性の良好な無機質系皮膜を形成し
た。上記酸化皮膜の形成されたアルミニウム材表面に、
液温30℃、濃度2%に調整したl−ヒドロキシエタン
−11l−ジホスホン酸三ナトリウム塩(三菱モンサン
ト化成(株)製品:商品名は、デイクエスト2015D
 Nという。)水溶液を塗布して、150℃で10秒間
熱風乾燥することにより、P換算で0.05g/m2の
ホスホン酸化合物皮膜を該無機質系皮膜表面に形成した
。そして、上記アルミニウム材にドロープレス加工を施
して熱交換器用フィンを形成し、その後トリクロルエチ
レンにより脱脂処理(40℃−30°C−1−ペーパー
にて各1分間処理。)を行った。
Example 3 An aluminum material of the same quality as Example 1 was etched with a weak alkali, washed with water and dried, and then treated with triethanolamine 0
.. Boehmite treatment is performed by immersing the aluminum material in an aqueous solution containing 5% for 60 seconds at a temperature of 90°C, and the surface of the aluminum material is coated with 0.
An inorganic film with a thickness of 4 g/m2 and good water wettability was formed. On the surface of the aluminum material on which the oxide film is formed,
l-Hydroxyethane-11l-diphosphonic acid trisodium salt adjusted to a liquid temperature of 30°C and a concentration of 2% (Mitsubishi Monsanto Chemical Co., Ltd. product: trade name is Dayquest 2015D)
It's called N. ) A phosphonic acid compound film of 0.05 g/m 2 in terms of P was formed on the surface of the inorganic film by applying an aqueous solution and drying with hot air at 150° C. for 10 seconds. Then, the aluminum material was draw-pressed to form heat exchanger fins, and then degreased with trichlorethylene (40°C-30°C-1-paper treatment for 1 minute each).

比較例1〜3 実施例1〜3に於いて、ホスホン酸等を含査する水溶液
による処理工程を省いた工程で処理し熱交換器用フィン
を得た。
Comparative Examples 1 to 3 Fins for heat exchangers were obtained by carrying out the treatment in Examples 1 to 3, but omitting the treatment step with an aqueous solution containing phosphonic acid or the like.

比較例4 実施例1において、アルミニウム材表面への酸化皮膜形
成工程のみを省いた工程を経て熱交換器フィンを得た。
Comparative Example 4 A heat exchanger fin was obtained through a step similar to Example 1, except that only the step of forming an oxide film on the surface of the aluminum material was omitted.

〔特 性〕〔Characteristic〕

上記の様にして製造するアルミニウム製熱交換器用フィ
ンについて、水濡れ性及びその耐久性について示すと表
の通りとなる。
The water wettability and durability of the aluminum heat exchanger fins manufactured as described above are shown in the table below.

この表から解るように、本発明実施例による熱交換器用
フィンは水濡れ性の良好なものであり、特にプレス加工
後において、トリクロルエチレン等で脱脂処理が行われ
ても、フィン表面の水濡れ性は劣化せず、脱脂処理後に
行う流水洗浄500時間後の親水性試験値からも解るよ
うに、優れた水濡れ性と耐久性のあるものである。これ
に対して、比較例1〜4のいずれの場合にも、トリクロ
ルエチレン等で脱脂を行った後では、水濡れ性の劣化が
起こり、耐久性ら好ましいものではない。
As can be seen from this table, the heat exchanger fins according to the examples of the present invention have good water wettability, and even after degreasing with trichlorethylene or the like, especially after press working, the fin surfaces do not get wet with water. It has excellent water wettability and durability, as can be seen from the hydrophilicity test value after 500 hours of washing under running water after degreasing. On the other hand, in any of Comparative Examples 1 to 4, after degreasing with trichlorethylene or the like, the water wettability deteriorates, and the durability is not desirable.

〔親水性評価試験〕[Hydrophilicity evaluation test]

り親水性及び耐久性:熱交換器用フィンの親水性につい
ては、フィン表面に滴下した水滴の(A):表面処理直
後、(B):脱脂処理直後、(C):流水洗浄500時
間後、3時点における接触角を測定して比較し、その耐
久性を調べた。
Hydrophilicity and durability: Regarding the hydrophilicity of heat exchanger fins, water droplets dropped on the fin surface (A): Immediately after surface treatment, (B): Immediately after degreasing treatment, (C): After 500 hours of washing under running water. The contact angles at three points in time were measured and compared to examine their durability.

(以下余白)(Margin below)

Claims (1)

【特許請求の範囲】[Claims] アルミニウム又はアルミニウム合金材表面に無機質系皮
膜を形成した後、該無機質系皮膜をホスホン酸、ホスホ
ン酸塩のうちの1種又は2種以上を含有する水溶液で処
理し、その後、所定の成形加工を施すことを特徴とする
熱交換器用フィンの製造方法。
After forming an inorganic film on the surface of an aluminum or aluminum alloy material, the inorganic film is treated with an aqueous solution containing one or more of phosphonic acid and phosphonate, and then subjected to a prescribed forming process. A method of manufacturing a fin for a heat exchanger, the method comprising:
JP23101085A 1985-10-18 1985-10-18 Production of fin for heat exchanger having excellent wettability Pending JPS6295182A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23101085A JPS6295182A (en) 1985-10-18 1985-10-18 Production of fin for heat exchanger having excellent wettability

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23101085A JPS6295182A (en) 1985-10-18 1985-10-18 Production of fin for heat exchanger having excellent wettability

Publications (1)

Publication Number Publication Date
JPS6295182A true JPS6295182A (en) 1987-05-01

Family

ID=16916830

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23101085A Pending JPS6295182A (en) 1985-10-18 1985-10-18 Production of fin for heat exchanger having excellent wettability

Country Status (1)

Country Link
JP (1) JPS6295182A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007167754A (en) * 2005-12-21 2007-07-05 Paint Staff:Kk Object having inorganic coating film and its manufacturing method
JP2012172061A (en) * 2011-02-22 2012-09-10 Nihon Univ Hydrophilic thin film, and method for producing the same

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5817868A (en) * 1981-07-17 1983-02-02 Daido Kagaku Kogyo Kk Production of aluminum fin for heat exchanger

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5817868A (en) * 1981-07-17 1983-02-02 Daido Kagaku Kogyo Kk Production of aluminum fin for heat exchanger

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007167754A (en) * 2005-12-21 2007-07-05 Paint Staff:Kk Object having inorganic coating film and its manufacturing method
JP2012172061A (en) * 2011-02-22 2012-09-10 Nihon Univ Hydrophilic thin film, and method for producing the same

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