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JPS5947032B2 - Method for imparting hydrophilicity to the condensing surface of an aluminum heat exchanger - Google Patents
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JPS5947032B2 - Method for imparting hydrophilicity to the condensing surface of an aluminum heat exchanger - Google Patents

Method for imparting hydrophilicity to the condensing surface of an aluminum heat exchanger

Info

Publication number
JPS5947032B2
JPS5947032B2 JP9296480A JP9296480A JPS5947032B2 JP S5947032 B2 JPS5947032 B2 JP S5947032B2 JP 9296480 A JP9296480 A JP 9296480A JP 9296480 A JP9296480 A JP 9296480A JP S5947032 B2 JPS5947032 B2 JP S5947032B2
Authority
JP
Japan
Prior art keywords
heat exchanger
condensing surface
aluminum
aluminum heat
imparting hydrophilicity
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
Application number
JP9296480A
Other languages
Japanese (ja)
Other versions
JPS5719383A (en
Inventor
利光 内山
永三 礒山
雅幸 鍜治
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.)
Altemira Co Ltd
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 JP9296480A priority Critical patent/JPS5947032B2/en
Publication of JPS5719383A publication Critical patent/JPS5719383A/en
Publication of JPS5947032B2 publication Critical patent/JPS5947032B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/82After-treatment
    • C23C22/83Chemical after-treatment
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/60Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using alkaline aqueous solutions with pH greater than 8
    • C23C22/66Treatment of aluminium or alloys based thereon

Landscapes

  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Treatment Of Metals (AREA)

Description

【発明の詳細な説明】 この発明は、アルミニクム製熱交換器の凝縮面における
親水性付与方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for imparting hydrophilicity to the condensing surface of an aluminum heat exchanger.

この明細書において、「アルミニウム」という用語は、
純アルミニウム、少量の不純物を含む市販のアルミニウ
ムおよびアルミニウムがその大部分を占めるアルミニウ
ム合金を含むものとする。
In this specification, the term "aluminum" means
It is intended to include pure aluminum, commercially available aluminum with small amounts of impurities, and aluminum alloys in which aluminum predominates.

一般にアルミニウム製熱交換器の凝縮面、たとえぱ凝縮
器として用いられる熱交換器の媒体流通管の内面におい
て、凝縮を伴なう熱交換性能を高めるには、凝縮により
生じた液の層を通して未凝縮蒸気のエネルギを奪う必要
があることから、上記凝縮液の層をできるだけ薄くする
必要がある。そのためこのような凝縮面は液との親水性
、すなわちヌレ性の良好なものであることが要望せられ
る。また他の凝縮面、すなわちカー ・クーラ−、ルー
ム・クーラ−等の空気調和機の蒸発器として用いられる
熱交換器のフィン表面においては、フィンの表面温度が
大気の露点以下となるためフィンの表面に水滴が付着し
、このような水滴の付着により通風抵抗が増大し、かつ
風量が減少して熱交換効率が低下する。これは蒸発器の
性能向上と小型化のためにフィンピッチを狭くした場合
にとくに顕著に現われる。熱交換効率はフィンのヌレ性
、すなわち親水性が大きく影響するものであり、フィン
表面のヌレ性が良いと付着した水が水滴となりにくく、
このため通風抵抗が小さくなり、風量も多くなつて熱交
換効率も向上する。このような観点から、従来より機械
的ないし化学的に凝縮面を粗面化したり、種々の形状に
加工したり、さらには焼結合金層を形成したりする工夫
がなされているが、これらはいずれも熱交換性能、品質
の安定性および製造コストの点に難点があり、さらに腐
食の点でも聞題がある上に、水との反応による水素ガス
の発生のために熱伝達性能が劣化するものであつたため
、未だ工業的に実用化されるに到つていない。この発明
は、アルミニウム製熱交換器の凝縮面に優れた親水性を
簡単に付与することのできる方法を提供することを目的
とする。
In general, on the condensing surface of an aluminum heat exchanger, for example on the inner surface of the medium flow pipe of a heat exchanger used as a condenser, in order to improve the heat exchange performance with condensation, it is necessary to pass through a layer of liquid produced by condensation. Since it is necessary to take away the energy of the condensed steam, it is necessary to make the layer of condensed liquid as thin as possible. Therefore, such a condensing surface is required to have good hydrophilicity with the liquid, that is, good wettability. In addition, on other condensing surfaces, that is, on the fin surfaces of heat exchangers used as evaporators in air conditioners such as car coolers and room coolers, the surface temperature of the fins is below the dew point of the atmosphere. Water droplets adhere to the surface, and the adhesion of such water droplets increases ventilation resistance and reduces the air volume, resulting in a decrease in heat exchange efficiency. This becomes especially noticeable when the fin pitch is narrowed to improve the performance and downsize the evaporator. Heat exchange efficiency is greatly influenced by the wettability of the fins, that is, their hydrophilicity.If the fin surface has good wettability, attached water will be less likely to form droplets.
This reduces ventilation resistance, increases the amount of air, and improves heat exchange efficiency. From this point of view, efforts have been made to mechanically or chemically roughen the condensation surface, process it into various shapes, and even form a sintered alloy layer. All of them have drawbacks in terms of heat exchange performance, quality stability, and manufacturing cost, and are also problematic in terms of corrosion, and heat transfer performance deteriorates due to the generation of hydrogen gas due to reaction with water. Because of this, it has not yet been put into practical use industrially. An object of the present invention is to provide a method that can easily impart excellent hydrophilicity to the condensing surface of an aluminum heat exchanger.

すなわち、この発明の方法は、アルカリ金属もしくはア
ルカリ土類金属の塩を1または2種以上含有する40℃
以上の処理液でアルミニウム製熱交換器の凝縮面を処理
する第1工程と、シリカゾルを含む処理液で上記凝縮面
を処理する第2工程とからなることを特徴とするもので
ある。
That is, the method of the present invention involves the use of a 40° C.
This method is characterized by comprising a first step of treating the condensing surface of an aluminum heat exchanger with the above treatment liquid, and a second step of treating the condensing surface with a treatment liquid containing silica sol.

第1工程において、アルカリ金属またはアルカリ土類金
属による処理により、凝縮面に化成皮膜が形成される。
In the first step, a chemical conversion film is formed on the condensation surface by treatment with an alkali metal or alkaline earth metal.

アルカリ金属またはアルカリ土類金属は、周期律表中の
いずれの金属であつてもよい。特にリチウム、ナトリウ
ム、カリウム、マグネシウム、カルシウム、ストロンチ
ウムが好ましい。塩の形態も特に限定されないが、通常
は塩化物、ヨウ化物などの・・ロゲン化物、硫酸塩、硝
酸塩、炭酸塩、シユウ酸塩などがよく用いられる。上記
塩はアルミニウム表面に化成皮膜を形成するための必須
成分である。そしてこれは単独で、または数種類を併用
して用いられる。後者の場合には特に均一でかつ厚い皮
膜を形成することができる。処理液における塩の濃度は
0.005〜2モル/tの範囲にある。その理由は、濃
度が0.005モル/t未満の場合には、皮膜の形成が
十分に進まず、また2モル/tを越えても、皮膜形成能
はほぼ一定であつてそれ以上効果がなく、かえつて処理
液中に金属水酸化物が沈澱して液の安定性が悪くなるか
らである。凝縮面に処理を施す場合、皮膜は薄い方がよ
く、そのため濃度は0.01〜0.2モル/tが好まし
い。第1工程の処理液にはトリエタノールアミンのよう
なアミン類を添加することもある。アミン類は処理液の
安定性を向上して金属水酸化物の沈澱を防ぐ作用を示す
。第1工程の処理液の温度は40℃以上が好ましい。温
度が40℃未満では皮膜形成が十分になされない。処理
液のPHは6〜13が好ましい。PHが6未満では皮膜
の形成よりもアルミニウムの溶解の方がより進行してし
まい、皮膜が生成しにくくなる。第2工程において、シ
リカゾルは、第1工程で処理された凝縮面の耐食性を増
し、皮膜の安定性を向上する作用をなす。シリカゾルの
濃度は、SiO2として0.0001〜 40Cf6の
範囲内にあることが好ましい。
The alkali metal or alkaline earth metal can be any metal in the periodic table. Particularly preferred are lithium, sodium, potassium, magnesium, calcium, and strontium. The form of the salt is not particularly limited, but usually chlorides, iodides, etc., rogens, sulfates, nitrates, carbonates, oxalates, etc. are often used. The above salt is an essential component for forming a chemical conversion film on the aluminum surface. These can be used alone or in combination. In the latter case, a particularly uniform and thick film can be formed. The concentration of salt in the treatment liquid is in the range of 0.005 to 2 mol/t. The reason for this is that if the concentration is less than 0.005 mol/t, film formation will not proceed sufficiently, and even if the concentration exceeds 2 mol/t, the film-forming ability will remain almost constant and there will be no further effect. On the contrary, the metal hydroxide will precipitate in the treatment solution, which will worsen the stability of the solution. When treating a condensation surface, the thinner the film, the better, and therefore the concentration is preferably 0.01 to 0.2 mol/t. An amine such as triethanolamine may be added to the treatment solution in the first step. Amines have the effect of improving the stability of the treatment solution and preventing precipitation of metal hydroxides. The temperature of the treatment liquid in the first step is preferably 40° C. or higher. If the temperature is less than 40°C, sufficient film formation will not occur. The pH of the treatment liquid is preferably 6 to 13. When the pH is less than 6, the dissolution of aluminum progresses more than the formation of a film, making it difficult to form a film. In the second step, the silica sol serves to increase the corrosion resistance of the condensation surface treated in the first step and improve the stability of the film. The concentration of the silica sol is preferably within the range of 0.0001 to 40Cf6 as SiO2.

その理由は、0.0001%未満では上記効果が十分に
発揮されず、40%を越えると処理液中でSiO2の沈
澱物が生じるからであるが、特に0.0001〜10%
が好ましい。またシリカゾルを含む水溶液の温度は常温
以上、PHは2〜11が好ましい。各工程において、処
理液の調製に用いられる建浴水は、脱イオン水、蒸留水
のほか水道水のように種々のイオンを含有する水であつ
てもよい。また各工程の浸漬時間は、処理液の濃度とも
関連するが、それぞれ通常1〜60分である。凝縮面を
処理するには、低濃度の処理液を用いて、比較的短時間
浸漬を行う。この発明による方法は、エツチング、ブラ
ストなどの化学的ないし機械的処理によるアルミニウム
表面の粗面化や、ローレツト加工、切削加工などの溝形
成加工の後に行うと、一層効果的である。
The reason for this is that if it is less than 0.0001%, the above effect will not be fully exhibited, and if it exceeds 40%, SiO2 will precipitate in the treatment solution.
is preferred. Further, the temperature of the aqueous solution containing silica sol is preferably room temperature or higher, and the pH thereof is preferably 2 to 11. In each step, the bath water used to prepare the treatment liquid may be water containing various ions such as deionized water, distilled water, or tap water. The immersion time in each step is usually 1 to 60 minutes, although it is related to the concentration of the treatment liquid. To treat condensation surfaces, a relatively short immersion is performed using a low concentration treatment solution. The method according to the present invention is more effective when carried out after roughening the aluminum surface by chemical or mechanical treatment such as etching or blasting, or after groove forming processing such as knurling or cutting.

以上の次第で、この発明によれば凝縮器として用いられ
るアルミニウム製熱交換器の凝縮面にち密でかつ液体と
のヌレ性の良好な酸化物ないし水酸化物層を形成するこ
とができるため、優れた熱交換性能を有する熱交換器と
することができる。また、蒸発器のフインの表面のヌレ
性、すなわち親水性を改良してフイン間の水滴をスムー
ズに排除することができる。そのため、水滴がフイン間
に架橋状に溜まつて空気流通抵抗を増したり、流人空気
によつてフインが振動して騒音を生じるといつ一たトラ
ブルを避けることができて熱交換効率が向上する上に、
フインピツチを狭めることができて、熱交換器のコンパ
クト化を果すことができる。また、この発明は2工程か
らなつているために、処理液の濃度その他の条件の選択
が容易となり、最適条件で処理をなし得る。しかも、処
理液の安定性に優れ、処理液における沈澱も少なくなり
、処理液の寿命が長くなる。実施例 1および2 アルミニウム材としてJISAIIOO−H24を用い
、これを下表に示す条件で処理した。
As described above, according to the present invention, it is possible to form a dense oxide or hydroxide layer on the condensing surface of an aluminum heat exchanger used as a condenser and with good wettability with liquid. A heat exchanger having excellent heat exchange performance can be obtained. Furthermore, the wettability, ie, hydrophilicity, of the surface of the fins of the evaporator can be improved, allowing water droplets between the fins to be smoothly removed. Therefore, it is possible to avoid troubles such as when water droplets accumulate in a cross-linked manner between the fins and increase air flow resistance, or when the fins vibrate due to floating air and cause noise, and improve heat exchange efficiency. In addition,
The fin pitch can be narrowed and the heat exchanger can be made more compact. Further, since the present invention consists of two steps, it is easy to select the concentration of the treatment liquid and other conditions, and the treatment can be carried out under optimal conditions. Moreover, the stability of the processing liquid is excellent, the amount of precipitation in the processing liquid is reduced, and the life of the processing liquid is extended. Examples 1 and 2 JISAIIOO-H24 was used as the aluminum material and treated under the conditions shown in the table below.

つぎに実施例1および2により形成した親水面について
、経過日数ど接触角の関係を求めた。結果を図面に示す
。また比較のために、上記アルミニウム材と同じ材料を
30℃にて2分間クロメート処理したもの(比較例1)
、同アルミニウム材を5%NaOH溶液で50℃にて3
分間処理し、3001)HNO3で脱脂したもの(比較
例2)、同アルミニウム材を陽極酸化処理し蒸気処理し
たもの(比較例3)についても上記関係を求めた。これ
ら結果を同図面に示す。図かられかるように、実施例に
より形成した親水面は、比較例により形成したものに比
べて接触角が小さく、したがつて優わたヌレ性を有する
。しかもこのヌレ性は長期にわたつて劣化することがな
い。また、JISAllOO−H24材の表面を上記実
施例1および2における第2工程の条件と同じ条件で処
理したところ、得られた親水面におけるヌレ性は上記実
施例1}よび2とほとんど変わるところがなかつたが、
皮膜の安定性に問題があつた。
Next, for the hydrophilic surfaces formed in Examples 1 and 2, the relationship between the contact angle and the number of days elapsed was determined. The results are shown in the drawing. For comparison, the same material as the aluminum material above was treated with chromate at 30°C for 2 minutes (Comparative Example 1)
, the same aluminum material was treated with 5% NaOH solution at 50°C.
The above relationship was also determined for the aluminum material treated for 3001 minutes and degreased with 3001) HNO3 (Comparative Example 2), and the same aluminum material anodized and steam treated (Comparative Example 3). These results are shown in the same drawing. As can be seen from the figure, the hydrophilic surface formed according to the example has a smaller contact angle than that formed according to the comparative example, and therefore has superior wettability. Moreover, this wettability does not deteriorate over a long period of time. Furthermore, when the surface of the JISA AllOO-H24 material was treated under the same conditions as the second step conditions in Examples 1 and 2 above, the wettability of the obtained hydrophilic surface was almost the same as in Examples 1 and 2 above. However,
There was a problem with the stability of the film.

【図面の簡単な説明】 図面は経過日数と接触角の関係を示すグラフである。[Brief explanation of the drawing] The drawing is a graph showing the relationship between elapsed days and contact angle.

Claims (1)

【特許請求の範囲】[Claims] 1 アルカリ金属もしくはアルカリ土類金属の塩を1種
または2種以上含有する40℃以上の処理液でアルミニ
ウム製熱交換器の凝縮面を処理し、ついでシリカゾルを
含む処理液で上記凝縮面を処理することを特徴とするア
ルミニウム製熱交換器の凝縮面における親水性付与方法
1 Treat the condensing surface of an aluminum heat exchanger with a treatment liquid at 40°C or higher containing one or more salts of alkali metals or alkaline earth metals, and then treat the condensation surface with a treatment liquid containing silica sol. A method for imparting hydrophilicity to a condensing surface of an aluminum heat exchanger.
JP9296480A 1980-07-07 1980-07-07 Method for imparting hydrophilicity to the condensing surface of an aluminum heat exchanger Expired JPS5947032B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9296480A JPS5947032B2 (en) 1980-07-07 1980-07-07 Method for imparting hydrophilicity to the condensing surface of an aluminum heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9296480A JPS5947032B2 (en) 1980-07-07 1980-07-07 Method for imparting hydrophilicity to the condensing surface of an aluminum heat exchanger

Publications (2)

Publication Number Publication Date
JPS5719383A JPS5719383A (en) 1982-02-01
JPS5947032B2 true JPS5947032B2 (en) 1984-11-16

Family

ID=14069107

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9296480A Expired JPS5947032B2 (en) 1980-07-07 1980-07-07 Method for imparting hydrophilicity to the condensing surface of an aluminum heat exchanger

Country Status (1)

Country Link
JP (1) JPS5947032B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60111843U (en) * 1983-12-30 1985-07-29 株式会社 桂精機製作所 Instant evaporation type vaporizer

Also Published As

Publication number Publication date
JPS5719383A (en) 1982-02-01

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