JPH0312150B2 - - Google Patents

Info

Publication number
JPH0312150B2
JPH0312150B2 JP1862581A JP1862581A JPH0312150B2 JP H0312150 B2 JPH0312150 B2 JP H0312150B2 JP 1862581 A JP1862581 A JP 1862581A JP 1862581 A JP1862581 A JP 1862581A JP H0312150 B2 JPH0312150 B2 JP H0312150B2
Authority
JP
Japan
Prior art keywords
heat transfer
transfer surface
treatment
aluminum
heat exchanger
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
JP1862581A
Other languages
Japanese (ja)
Other versions
JPS57134572A (en
Inventor
Eizo Isoyama
Masayuki Kaji
Hiroichi Takenaka
Masataka Sato
Susumu Inoe
Makoto Masubuchi
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 JP1862581A priority Critical patent/JPS57134572A/en
Publication of JPS57134572A publication Critical patent/JPS57134572A/en
Publication of JPH0312150B2 publication Critical patent/JPH0312150B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/18Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
    • 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
    • C23C22/06Chemical 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 aqueous acidic solutions with pH less than 6
    • C23C22/24Chemical 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 aqueous acidic solutions with pH less than 6 containing hexavalent chromium compounds

Landscapes

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

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は、アルミニウム製熱交換器の凝縮伝
熱面(この明細書で単に「伝熱面」とは凝縮伝熱
面をいう)における親水性付与方法に関する。 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、小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。 一般にアルミニウム製熱交換器の凝縮伝熱面、
たとえば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ー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。また他の凝縮伝熱面、すなわちカ
ー・クーラー、ルーム・クーラー等の空気調和機
の蒸発器として用いられる熱交換器のフイン表面
においては、フインの表面温度が大気の露天以下
となるためフイ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インピツチを狭
くした場合にとくに顕著に現われる。熱交換効率
はフインのヌレ性、すなわち親水性が大きく影響
するものであり、フイ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
いし化学的に凝縮伝熱面を粗面化したり、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、品質の安全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問題がある
上に、水との反応による水素ガスの発生のために
熱伝達性能が低下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伝
熱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。 すなわち、この発明の方法は、アルミナゾルま
たはシリカゾルを含有する酸系処理液を用いてア
ルミニウム製熱交換器の凝縮伝熱面を化成処理す
ることを特徴とする、アルミニウム製熱交換器の
凝縮伝熱面における親水性付与方法である。 上記処理によつてアルミニウム材表面に形成さ
れた皮膜が伝熱面を構成する。 酸系処理液による化成処理の代表例としては、
クロメート皮膜形成処理、ジルコニウム皮膜形成
処理、リン酸皮膜形成処理などが挙げられる。特
にクロメート皮膜形成処理、すなわちクロム酸、
クロム酸塩および/または重クロム酸塩を含む処
理液による処理が好ましい。 この酸系処理液による化成処理の結果、良好な
ヌレ性を有し、しかも耐食性にすぐれた伝熱面を
形成することができる。 クロメート処理において、クロム酸塩として
は、クロム酸ナトリウム、クロム酸カリウムがよ
く用いられ、また重クロム酸塩としては重クロム
酸ナトリウム、重クロム酸カリウムがよく用いら
れる。これらの塩の濃度は0.001〜1モル/の
範囲にあることが好ましい。その理由は、0.001
モル/未満では、上記効果が十分に発揮され
ず、1モル/を越えると、経済的に不利な上に
その後の水洗水の廃液処理負荷を大きくするから
である。特に好ましい濃度は0.01〜0.5モル/
である。 アルミナゾルの含有量はAl2O3として0.0001〜
4.0%、好ましくは0.01〜20%である。シリカゾ
ルの含有量はSiO2として0.0001〜40%、好ましく
は0.0001〜7%である。その理由は、アルミナゾ
ルおよびシリカゾルの含有量がそれぞれ0.0001%
未満では上記効果が十分に発揮されず、40%を越
えても上記効果はさしたる向上をみないからであ
る。 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、地下水のように種々の
イオンを含有する水であつてもよい。 処理液のPHは2〜7が望ましい。そのためアル
カリ金属の炭酸塩または水酸化物によつてPHを調
製することもある。処理温度は20℃以上が好まし
い。20℃未満で皮膜に吸着あるいは反応するクロ
メート量が少なく、上記効果が十分でない。好ま
しくは80℃以上である。また処理時間は、処理液
の濃度や温度とも関連するが、通常数秒〜1時間
である。 なお、この発明による伝熱面の形成方法は、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。 以上の次第で、この発明によれば、アルミニウ
ム材表面の粗面化により伝熱面積が大きくかつ耐
食性に優れた伝熱面を形成することができる。か
くして、ち密でかつ液体とのヌレ性の良好な酸化
物ないし水和酸化物層を形成することができる。
さらにこの発明によれば、従来処理の困難であつ
た管内面に対しても容易に処理に施すことがで
き、したがつて管の内外面を同時に処理すること
ができて、極めて作業性が良い。またこの発明に
よる方法は、一般にベーマイト皮膜の付着しにく
いブレージング製品にも適用でき、耐食性の良好
な伝熱面を形成することができる。またこの発明
の方法を熱交換器特に蒸発器の外面に適用するこ
とにより、そのヌレ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、流入空気によつてフインが振動して
騒音を生じるといつたトラブルを避けることがで
きる上に、フインピツチを挟めることができて、
熱交換器のコンパクト化を果すことができる。 実施例 熱交換器の凝縮伝熱面のアルミニウム材:
JISA1100−H24
The present invention relates to a method for imparting hydrophilicity to a condensing heat transfer surface (in this specification, the term "heat transfer surface" simply refers to a condensing heat transfer surface) of an aluminum heat exchanger. In this specification, the term "aluminum" is intended to include pure aluminum, commercially available aluminum with minor impurities, and aluminum alloys in which aluminum predominates. Generally the condensing heat transfer surface of aluminum heat exchangers,
For example, in order to improve the heat exchange performance with condensation on the inner surface of the medium flow pipe of a heat exchanger used as a condenser, it is necessary to remove energy from uncondensed vapor through a layer of liquid produced by condensation. It is necessary to make the layer of condensate 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 condensation heat transfer surfaces, that is, on the surface of the fins of heat exchangers used as evaporators in air conditioners such as car coolers and room coolers, the surface temperature of the fins is lower than the atmospheric temperature. 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 fins have good wettability, attached water will be less likely to form droplets, which will reduce ventilation resistance and increase the amount of air, which will reduce heat transfer. Exchange efficiency is also improved. From this point of view, efforts have been made to mechanically or chemically roughen the condensation heat transfer surface, process it into various shapes, and even form a sintered alloy layer. All of these have drawbacks in terms of heat exchange performance, quality safety, and manufacturing cost.Furthermore, they have problems 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 heat transfer surface of an aluminum heat exchanger. That is, the method of the present invention is characterized in that a condensation heat transfer surface of an aluminum heat exchanger is subjected to a chemical conversion treatment using an acid-based treatment liquid containing alumina sol or silica sol. This is a method of imparting hydrophilicity to surfaces. The film formed on the surface of the aluminum material by the above treatment constitutes a heat transfer surface. Typical examples of chemical conversion treatment using acid-based treatment liquids include:
Examples include chromate film formation treatment, zirconium film formation treatment, phosphoric acid film formation treatment, and the like. In particular, chromate film formation treatment, i.e. chromic acid,
Treatment with a treatment solution containing chromate and/or dichromate is preferred. As a result of the chemical conversion treatment using this acid-based treatment liquid, a heat transfer surface having good wettability and excellent corrosion resistance can be formed. In the chromate treatment, sodium chromate and potassium chromate are often used as the chromate, and sodium dichromate and potassium dichromate are often used as the dichromate. The concentration of these salts is preferably in the range of 0.001 to 1 mol/mol. The reason is 0.001
If the amount is less than 1 mol/mol, the above effect will not be fully exhibited, and if it exceeds 1 mol/mol, it will be economically disadvantageous and the subsequent waste liquid treatment load of the washing water will be increased. A particularly preferable concentration is 0.01 to 0.5 mol/
It is. The content of alumina sol is 0.0001 ~ as Al2O3
4.0%, preferably 0.01-20%. The content of the silica sol is 0.0001 to 40%, preferably 0.0001 to 7% as SiO2 . The reason is that the content of alumina sol and silica sol is 0.0001% each.
This is because if it is less than 40%, the above effect will not be sufficiently exhibited, and if it exceeds 40%, the above effect will not be significantly improved. The prepared bath water used for preparing the treatment liquid may be water containing various ions such as deionized water, distilled water, tap water, and ground water. The pH of the treatment liquid is preferably 2 to 7. Therefore, pH may be adjusted using alkali metal carbonates or hydroxides. The treatment temperature is preferably 20°C or higher. At temperatures below 20°C, the amount of chromate adsorbed or reacted with the film is small, and the above effects are not sufficient. Preferably the temperature is 80°C or higher. Further, the processing time is related to the concentration and temperature of the processing liquid, but is usually from several seconds to one hour. Note that the method for forming a heat transfer surface according to the present invention is more effective when performed 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. It is true. As described above, according to the present invention, a heat transfer surface having a large heat transfer area and excellent corrosion resistance can be formed by roughening the surface of the aluminum material. In this way, an oxide or hydrated oxide layer that is dense and has good wettability with liquid can be formed.
Furthermore, according to the present invention, it is possible to easily treat the inner surface of the tube, which has traditionally been difficult to treat, and therefore the inner and outer surfaces of the tube can be treated simultaneously, resulting in extremely high workability. . Furthermore, the method according to the present invention can be applied to brazed products to which boehmite films are generally difficult to adhere, and can form a heat transfer surface with good corrosion resistance. Furthermore, by applying the method of the present invention to the outer surface of a heat exchanger, particularly an evaporator, its wettability can be improved and water droplets between the fins can be smoothly removed. Therefore,
It is possible to avoid troubles such as water droplets accumulating in a cross-linked manner between the fins, increasing air flow resistance, and noise caused by the fins vibrating due to inflowing air, and it is possible to sandwich the fin pitch. ,
The heat exchanger can be made more compact. Example: Aluminum material for condensation heat transfer surface of heat exchanger:
JISA1100−H24

【表】 実施例および比較例において形成した伝熱面に
ついて、経過日数と接触角の関係を求めた。結果
を添付図面に示す。同図からわかるように、実施
例により形成した伝熱面は、比較例のものに比べ
て接触角が小さく、換言すれば優れたヌレ性を有
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。 また各伝熱面について耐食性およびヌレ性の試
験を行つた。結果を下記表1に示す。なお耐食性
の試験は塩水噴霧試験(JIS、Z2371)により行
つた。
[Table] The relationship between the number of days elapsed and the contact angle was determined for the heat transfer surfaces formed in Examples and Comparative Examples. The results are shown in the attached drawings. As can be seen from the figure, the heat transfer surface formed according to the example has a smaller contact angle than that of the comparative example, in other words, it has excellent wetting properties. Moreover, this wettability does not deteriorate over a long period of time. Corrosion resistance and wettability tests were also conducted on each heat transfer surface. The results are shown in Table 1 below. The corrosion resistance test was conducted using a salt spray test (JIS, Z2371).

【表】【table】

【表】 × 不良
同表からわかるように、実施例により形成した
伝熱面は耐食性、ヌレ性共に良好である。
[Table] × Poor As can be seen from the table, the heat transfer surface formed according to the example has good corrosion resistance and wettability.

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

図面は経過日数と接触角の関係を示すグラフで
ある。
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 アルミナゾルまたはシリカゾルを含有する酸
系処理液を用いてアルミニウム製熱交換器の凝縮
伝熱面を化成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伝熱面における親水性付
与方法。
1. A method for imparting hydrophilicity to a condensing heat transfer surface of an aluminum heat exchanger, the method comprising chemically treating the condensing heat transfer surface of the aluminum heat exchanger using an acid-based treatment liquid containing alumina sol or silica sol.
JP1862581A 1981-02-10 1981-02-10 Formation of heat transfer surface on surface of aluminum material Granted JPS57134572A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1862581A JPS57134572A (en) 1981-02-10 1981-02-10 Formation of heat transfer surface on surface of aluminum material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1862581A JPS57134572A (en) 1981-02-10 1981-02-10 Formation of heat transfer surface on surface of aluminum material

Publications (2)

Publication Number Publication Date
JPS57134572A JPS57134572A (en) 1982-08-19
JPH0312150B2 true JPH0312150B2 (en) 1991-02-19

Family

ID=11976796

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1862581A Granted JPS57134572A (en) 1981-02-10 1981-02-10 Formation of heat transfer surface on surface of aluminum material

Country Status (1)

Country Link
JP (1) JPS57134572A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5022571B2 (en) * 2005-03-25 2012-09-12 ニチアス株式会社 Method for manufacturing gasket and washer

Also Published As

Publication number Publication date
JPS57134572A (en) 1982-08-19

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