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JPS6259198B2 - - Google Patents
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JPS6259198B2 - - Google Patents

Info

Publication number
JPS6259198B2
JPS6259198B2 JP9295980A JP9295980A JPS6259198B2 JP S6259198 B2 JPS6259198 B2 JP S6259198B2 JP 9295980 A JP9295980 A JP 9295980A JP 9295980 A JP9295980 A JP 9295980A JP S6259198 B2 JPS6259198 B2 JP S6259198B2
Authority
JP
Japan
Prior art keywords
heat transfer
transfer surface
aluminum material
aluminum
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
Application number
JP9295980A
Other languages
Japanese (ja)
Other versions
JPS5719396A (en
Inventor
Toshimitsu Uchama
Eizo Isoyama
Masayuki Tanji
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 JP9295980A priority Critical patent/JPS5719396A/en
Publication of JPS5719396A publication Critical patent/JPS5719396A/en
Publication of JPS6259198B2 publication Critical patent/JPS6259198B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Electrochemical Coating By Surface Reaction (AREA)

Description

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

この発明は、アルミニウム材に伝熱面を形成す
る方法に関する。 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、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。 一般に熱交換器の蒸発伝熱面においては、熱交
換は主に沸騰伝熱によりなされる。そのため熱交
換性能を高めるには、伝熱面の面積をできるだけ
拡大し、また、伝熱面における流体の蒸気泡の発
生核密度を高めてこれによつて流体を十分に撹拌
させることが重要になつてくる。他方、凝縮伝熱
面においては、熱交換性能を高めるには、上記の
ように伝熱面の面積を拡大することのほか、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。そのため伝熱
面はヌレ性の良好なものであることが要望せられ
る。このような観点から、従来より機械的ないし
化学的に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問題があるため、未だ
工業的に実用化されるに至つていない。 この発明は、上記のような実情から、蒸発伝熱
面および凝縮伝熱面の両方に適用可能なアルミニ
ウム製熱交換管の伝熱面の形成方法を提係するこ
とを目的とする。 すなわち、この発明は、通常の陽極酸化処理液
にケイ酸、ケイ酸塩またはシリカゾルを添加して
なる液を用いてアルミニウム材を陽極酸化処理す
ることを特徴とするアルミニウム材に伝熱面を形
成する方法である。 上記処理によつてアルミニウム材表面に形成さ
れた陽極酸化皮膜が伝熱面を構成する。 通常の陽極酸化処理液は、硫酸、シユウ酸、リ
ン酸等を所要量含有する水溶液である。 ケイ酸、ケイ酸塩およびシリカゾルは、形成さ
れた伝熱面の耐食性を増し、皮膜の安定性を向上
する作用をなす。 ケイ酸塩としては、ケイ酸ナトリウム、ケイ酸
カリウム、水ガラスなどがよく用いられる。 ケイ酸およびケイ酸塩の濃度は0.0005〜0.5モ
ル/の範囲にある。その理由は、濃度が0.0005
モル/未満では上記効果が十分に発揮されず、
0.5モル/を越えると処理液中で沈澱物が生じ
るからである。特に好ましい濃度は0.003〜0.3モ
ル/である。シリカゾルの濃度はSiO2として
0.0001〜5%の範囲にある。この理由も上記ケイ
酸およびその塩の場合と同じである。 処理液の調製に用いられる建浴水は、脱イオン
水、蒸留水のほか水動水、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。 陽極酸化の処理条件は常法による。処理時間
は、処理液の濃度とも関連するが、通常1〜120
分である。蒸発伝熱面を形成するには、高濃度の
処理液を用いて、比較的長時間処理を行う。他方
凝縮伝熱面を形成するには、低濃度の処理液を用
いて、比較的短時間処理を行う。処理後、好まし
くは、加圧蒸気または沸騰水によつて封孔処理を
施こす。 なお、この発明による伝熱面の形成方法は、エ
ツチング、プ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
ト化工、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。ま
た蒸発伝熱面を形成するには、蒸気泡の発生核と
なる比較的粗な多孔質の酸化物ないし水和酸化物
層を形成することができ、他方凝縮伝熱面を形成
するには、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を施すことが
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よい。しかも、処理は
1段階でなされるためこの点でも作業性が良い。 実施例 1〜6 アルミニウム材としてJISA1100―H24製のも
の(大きさ1mm×50mm×100mm)を用い、以下の
条件でこれを陽極酸化処理した。
The present invention relates to a method of forming a heat transfer surface on an aluminum material. 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, in the evaporative heat transfer side of a heat exchanger, heat exchange is mainly performed by boiling heat transfer. Therefore, in order to improve heat exchange performance, it is important to expand the area of the heat transfer surface as much as possible, and also to increase the density of the generation nuclei of fluid vapor bubbles on the heat transfer surface, thereby stirring the fluid sufficiently. I'm getting old. On the other hand, in order to improve heat exchange performance on the condensation heat transfer surface, in addition to expanding the area of the heat transfer surface as described above, it is also necessary to take energy from uncondensed vapor through a layer of liquid produced by condensation. For this reason, it is necessary to make the layer of the condensate as thin as possible. Therefore, the heat transfer surface is required to have good wettability. From this point of view, efforts have been made to mechanically or chemically roughen the 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 stability, and manufacturing cost, and also have problems in terms of corrosion, so they have not yet been put into practical use industrially. In view of the above-mentioned circumstances, it is an object of the present invention to provide a method for forming a heat transfer surface of an aluminum heat exchange tube, which is applicable to both the evaporative heat transfer surface and the condensation heat transfer surface. That is, the present invention provides a method for forming a heat transfer surface on an aluminum material by anodizing the aluminum material using a solution obtained by adding silicic acid, silicate, or silica sol to a normal anodizing solution. This is the way to do it. The anodic oxide film formed on the surface of the aluminum material by the above treatment constitutes a heat transfer surface. A typical anodizing solution is an aqueous solution containing a required amount of sulfuric acid, oxalic acid, phosphoric acid, etc. Silicic acid, silicates, and silica sol serve to increase the corrosion resistance of the formed heat transfer surface and improve the stability of the film. As silicates, sodium silicate, potassium silicate, water glass, etc. are often used. The concentration of silicic acid and silicates is in the range 0.0005-0.5 mol/. The reason is that the concentration is 0.0005
If the amount is less than mol/mol, the above effects will not be fully exhibited,
This is because if the amount exceeds 0.5 mol/min, a precipitate will form in the treatment solution. A particularly preferred concentration is 0.003 to 0.3 mol/. The concentration of silica sol is as SiO2
It is in the range of 0.0001 to 5%. The reason for this is also the same as in the case of the silicic acid and its salts. The prepared bath water used for preparing the treatment liquid may be water containing various ions such as deionized water, distilled water, hydrostatic water, and ground water. The treatment conditions for anodic oxidation are according to conventional methods. The processing time is related to the concentration of the processing solution, but is usually 1 to 120
It's a minute. To form the evaporative heat transfer surface, a highly concentrated treatment liquid is used and the treatment is performed for a relatively long time. On the other hand, in order to form a condensing heat transfer surface, a treatment is performed for a relatively short time using a treatment liquid of low concentration. After the treatment, a sealing treatment is preferably performed using pressurized steam or boiling water. The method for forming a heat transfer surface according to the present invention will be more effective if it is performed after roughening the aluminum surface by chemical or mechanical treatment such as etching or plasting, or after forming grooves 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 addition, to form an evaporative heat transfer surface, a relatively coarse porous oxide or hydrated oxide layer can be formed, which serves as a nucleus for generating vapor bubbles, and on the other hand, to form a condensation heat transfer surface, It is possible to form an oxide or hydrated oxide layer that is dense and has good wettability with liquid. Further, according to the present invention, it is possible to easily treat the inner surface of the tube, which has conventionally been difficult to treat, and therefore the inner and outer surfaces of the tube can be treated simultaneously, resulting in extremely high workability. Furthermore, since the processing is performed in one step, workability is also good in this respect. Examples 1 to 6 An aluminum material made of JISA1100-H24 (size: 1 mm x 50 mm x 100 mm) was anodized under the following conditions.

【表】 こうし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、30%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。これら結果を同図に示す。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。
[Table] Regarding the heat transfer surface thus formed, the relationship between the number of days elapsed and the contact angle was determined. The results are shown in the drawing. For comparison, the same material as the aluminum material above was used.
Chromate treated at 30℃ for 2 minutes (Comparative Example 1), same aluminum material treated with 5% NaOH solution at 50℃
The above relationship was also determined for the aluminum material treated for 3 minutes and degreased with 30% HNO 3 (Comparative Example 2), and the same aluminum material anodized and steam treated (Comparative Example 3). These results are shown in the figure. As can be seen from the figure, the heat transfer surface formed according to the example has a smaller contact angle than that formed according to the comparative example, and therefore has excellent wetting properties. Moreover, this wettability does not deteriorate over a long period of time.

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

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 通常の陽極酸化処理液にケイ酸、ケイ酸塩ま
たはシリカゾルを添加してなる液を用いてアルミ
ニウム材を陽極酸化処理することを特徴とするア
ルミニウム材に伝熱面を形成する方法。
1. A method for forming a heat transfer surface on an aluminum material, which comprises anodizing the aluminum material using a solution obtained by adding silicic acid, silicate, or silica sol to a normal anodizing solution.
JP9295980A 1980-07-07 1980-07-07 Formation of heating surface on aluminum material Granted JPS5719396A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9295980A JPS5719396A (en) 1980-07-07 1980-07-07 Formation of heating surface on aluminum material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9295980A JPS5719396A (en) 1980-07-07 1980-07-07 Formation of heating surface on aluminum material

Publications (2)

Publication Number Publication Date
JPS5719396A JPS5719396A (en) 1982-02-01
JPS6259198B2 true JPS6259198B2 (en) 1987-12-09

Family

ID=14068977

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9295980A Granted JPS5719396A (en) 1980-07-07 1980-07-07 Formation of heating surface on aluminum material

Country Status (1)

Country Link
JP (1) JPS5719396A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59136498A (en) * 1983-01-26 1984-08-06 Kobe Steel Ltd Surface treatment of al or al alloy
JPS60111843U (en) * 1983-12-30 1985-07-29 株式会社 桂精機製作所 Instant evaporation type vaporizer
US4894126A (en) * 1988-01-15 1990-01-16 Mahmoud Issa S Anodic coatings on aluminum for circuit packaging

Also Published As

Publication number Publication date
JPS5719396A (en) 1982-02-01

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