JPS5844158B2 - Renzokuyoukiyokusankashiyorisouchi - Google Patents

Renzokuyoukiyokusankashiyorisouchi

Info

Publication number
JPS5844158B2
JPS5844158B2 JP13473975A JP13473975A JPS5844158B2 JP S5844158 B2 JPS5844158 B2 JP S5844158B2 JP 13473975 A JP13473975 A JP 13473975A JP 13473975 A JP13473975 A JP 13473975A JP S5844158 B2 JPS5844158 B2 JP S5844158B2
Authority
JP
Japan
Prior art keywords
chamber
cathode chamber
treated
anode chamber
anode
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
JP13473975A
Other languages
Japanese (ja)
Other versions
JPS5259036A (en
Inventor
芳雄 安藤
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.)
Toyo Giken Kogyo KK
Original Assignee
Toyo Giken Kogyo KK
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 Toyo Giken Kogyo KK filed Critical Toyo Giken Kogyo KK
Priority to JP13473975A priority Critical patent/JPS5844158B2/en
Publication of JPS5259036A publication Critical patent/JPS5259036A/en
Publication of JPS5844158B2 publication Critical patent/JPS5844158B2/en
Expired legal-status Critical Current

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  • Electrochemical Coating By Surface Reaction (AREA)

Description

【発明の詳細な説明】 本発明は、陽極室と陰極室とを交互に組合せてなる陽極
酸化処理槽に、アルミニウムまたはその合金の被処理物
をとおし、連続的に陽極酸化処理を行なう装置に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for continuously carrying out anodic oxidation treatment by passing a workpiece of aluminum or its alloy through an anodization treatment tank consisting of an alternating combination of anode chambers and cathode chambers. It is something.

従来、処理液槽を配置し、その始端から終端まで被処理
物を弔事した搬送杆を順次核種に移槽し、各種において
所定の表面処理を行なわせるようにしたバッチ式の表面
処理方法においては、被処理物を搬送杆へ吊付け、吊離
しするための作業時間、いわゆるラッキングとアンラッ
キングの時間、およびその労力が膨大であり、かつ、非
能率的であった。
Conventionally, in a batch-type surface treatment method, a treatment liquid tank is arranged, and a transport rod carrying the object to be treated is sequentially transferred to the nuclide tank from the start end to the end, and a predetermined surface treatment is performed for each type. However, the working time required to hang and unrack the objects to be processed, that is, so-called racking and unracking time, and the labor involved are enormous and inefficient.

とくに、陽極酸化処理条件よりも、ラッキング治具は、
電気的にも機械的にも制約が多く、高価なものとなり、
その治具の消耗は経済的観点からも損失が太き(、治具
レス方式の開発が望まれていた。
In particular, compared to the anodizing treatment conditions, the racking jig is
There are many restrictions both electrically and mechanically, making it expensive.
The wear and tear of the jig is also a big loss from an economic point of view (the development of a jig-less method has been desired).

一方、ラッキング時間、労力の膨大化、ラッキング治具
の損失等バッチ式の欠点を改良するため、被処理物を連
続して陽極酸化処理する連続式が提案されている。
On the other hand, in order to improve the disadvantages of the batch method, such as increased racking time, increased labor, and loss of racking jigs, a continuous method has been proposed in which the object to be anodized is continuously anodized.

しかるに従来の連続式陽極酸化処理方法においては、各
処理槽に渡り、つまり、被処理物の巻出側から巻取側ま
で、被処理物は連続しており、かつ、通電体であること
が条件であるため、帯板状、コイル状、線状の処理物に
はよいが、押出型材、折板、パイプ、角材などのように
、長さが比較的短< (10メートル以下)、曲げるこ
とができなく、製品そのままの形状で陽極酸化処理をし
なげればならないものについては、被処理物の搬送方法
と給電方法の点から連続処理ができなかった。
However, in the conventional continuous anodizing method, the workpiece is continuous across each treatment tank, from the unwinding side of the workpiece to the winding side, and the workpiece must be a current-carrying body. However, it is suitable for processing products in the form of strips, coils, and wires, but it is suitable for processing products that are relatively short (10 meters or less) or bent, such as extruded materials, folded plates, pipes, and square materials. For products that cannot be anodized and must be anodized in their original shape, continuous processing is not possible due to the method of transporting the objects to be processed and the method of power supply.

本発明は、帯板類、押出型材類などの被処理物の形状に
かかわらず、ラッキング作業およびラッキング治具を必
要としないで連続陽極酸化処理を可能とする装置を提供
することを目的とするものである。
An object of the present invention is to provide an apparatus that enables continuous anodizing treatment without the need for racking work or racking jigs, regardless of the shape of the object to be treated, such as strips or extruded materials. It is something.

すなわち、陽極酸化処理槽内を連続して流れる状態で一
体の通電体として扱うことのできない押出型材材料など
を連続して均一な皮膜を得るように、陽極室と陰極室を
交互に配置してなるものである。
In other words, the anode chamber and the cathode chamber are arranged alternately so that extruded mold material, etc., which cannot be treated as a single current-carrying body while flowing continuously in the anodizing treatment tank, can be coated continuously and uniformly. It is what it is.

以下、本発明の実施の態様について図面を参照しながら
説明する。
Embodiments of the present invention will be described below with reference to the drawings.

第1図ないし第3図は本発明の第1実施例を示したもの
で、同図において、1はアルミニウムまたはその合金か
らなる被処理物、2は変速可能なローラコンベアからな
る搬送装置、3は前記被処理物1の移行方向を示した矢
印、4は壁体が電気的絶縁性を有する陽極酸化処理槽で
ある。
1 to 3 show a first embodiment of the present invention, in which 1 is a workpiece made of aluminum or its alloy, 2 is a conveying device consisting of a variable-speed roller conveyor, and 3 is an arrow indicating the direction of movement of the object to be treated 1, and 4 is an anodizing tank whose wall has electrical insulation properties.

そしてこの処理槽4は被処理物1の移行方向3に対して
直角に設けられた電気的絶縁性の仕切壁5と6によって
順に陽極室I、陰極室8、陽極室9に分割されている。
The processing tank 4 is divided into an anode chamber I, a cathode chamber 8, and an anode chamber 9 by electrically insulating partition walls 5 and 6 provided perpendicularly to the transfer direction 3 of the object to be processed 1. .

また陽極室7には陽極としての鉛による給電材10、陰
極室8には陰極としてのカーボンによる給電材11.陽
極室9には陽極としての鉛による給電材12が設置され
、給電装置13によって各給電材に加電されるようにな
っている。
Further, the anode chamber 7 has a power supply material 10 made of lead as an anode, and the cathode chamber 8 has a power supply material 11 made of carbon as a cathode. Power supply materials 12 made of lead as anodes are installed in the anode chamber 9, and electricity is applied to each power supply material by a power supply device 13.

さらに該処理槽40入口に相当するところべは被処理材
1が通過し得る貫通部14を有し、出口に相当するとこ
ろにも被処理材1が通過し得る貫通部15を有し、かつ
、各仕切壁5と6にも同様な貫通部を有している。
Further, a portion corresponding to the inlet of the processing tank 40 has a penetration portion 14 through which the material to be treated 1 can pass, and a portion corresponding to the outlet also has a penetration portion 15 through which the material to be treated 1 can pass, and , each of the partition walls 5 and 6 also has similar penetrations.

すなわち、前記貫通部14と15からは処理液が該処理
槽4外に流出するので、溢流槽16と17が設けられ、
両槽16と17の処理液は循環ポンプ18によって吸引
されて戻し管19を介してそれぞれ陽極室7および陰極
室8ならびに陽極室9に戻されるようになっている。
That is, since the processing liquid flows out of the processing tank 4 from the penetration parts 14 and 15, overflow tanks 16 and 17 are provided.
The processing liquids in both tanks 16 and 17 are sucked by a circulation pump 18 and returned to the anode chamber 7, the cathode chamber 8, and the anode chamber 9 via a return pipe 19, respectively.

また矢印3の方向に対する前記各室7,8゜90幅は矢
印3の方向に対する被処理物1の幅より大きいとともに
、矢印3の方向に対する被処理物1の長さは矢印3の方
向に対する陰極室8の長さより長い。
Further, the width of each of the chambers 7, 8°90 in the direction of the arrow 3 is greater than the width of the object 1 to be treated in the direction of the arrow 3, and the length of the object 1 in the direction of the arrow 3 is the same as that of the cathode in the direction of the arrow 3. It is longer than the length of chamber 8.

なお被処理物1は長さが10メートル以下というように
比較的短いもので、曲げられない性質のもので、製品そ
のままの形状で陽極酸化処理をしなげればならないもの
である。
Note that the object 1 to be treated is relatively short, such as 10 meters or less in length, and is unbendable, so that it must be anodized in its original shape.

このように構成された連続陽極酸化処理槽によって処理
を行なうには、被処理物1を搬送装置2に載せ、矢印3
の方向に移行せしめる。
In order to carry out the treatment using the continuous anodizing treatment tank configured in this way, the object to be treated 1 is placed on the transport device 2, and the object to be treated is placed in the direction indicated by the arrow 3.
move in the direction of

すると処理物1は貫通部14から陽極室7に入り、順に
陰極室8と陽極室9内を通過して貫通部15から槽外に
出ることになる。
Then, the processed material 1 enters the anode chamber 7 through the penetration portion 14, passes through the cathode chamber 8 and the anode chamber 9 in order, and exits from the tank through the penetration portion 15.

すなわち、まず、被処理物1は陽極室7内においてその
処理液に接触することによってプラスに帯電され、つぎ
に被処理物1は陽極室7と陰極室8とに渡って移行する
から、給電材10→陽極室7内の処理液→被処理物1→
陰極室8内の処理液→給電材11の順で通電され、被処
理物1の表面は陽極酸化処理される。
That is, first, the object to be treated 1 is positively charged by contacting the treatment liquid in the anode chamber 7, and then the object to be treated 1 moves between the anode chamber 7 and the cathode chamber 8. Material 10 → Processing liquid in anode chamber 7 → Workpiece 1 →
Electricity is applied in the order of the treatment liquid in the cathode chamber 8 and the power supply material 11, and the surface of the object to be treated 1 is anodized.

つづいて被処理物1の先端が陽極室9に達し、後端が陽
極室7内にあり、中央部が陰極室8内にあれば、前記通
電のほかに、給電材12→陽極室9内の処理液→被処理
物1→陰極室8内の処理液→給電材11の順でも通電さ
れ、同様に陽極酸化処理される。
Next, if the front end of the object to be processed 1 reaches the anode chamber 9, the rear end is in the anode chamber 7, and the center is in the cathode chamber 8, in addition to the above-mentioned energization, the power supply material 12 → the anode chamber 9. Electrification is also applied in the order of the treatment liquid → the object to be treated 1 → the treatment liquid in the cathode chamber 8 → the power supply material 11, and the anodic oxidation process is performed in the same manner.

最後に被処理物1が陰極室8と陽極室9に渡って移行す
る状態では、陽極室9がら被処理物1をとおって陰極室
8へと通電され、ここでも同様に陽極酸化処理がなされ
る。
Finally, when the object to be treated 1 is transferred to the cathode chamber 8 and the anode chamber 9, electricity is supplied from the anode chamber 9 through the object to be treated 1 to the cathode chamber 8, and the anodization treatment is similarly performed here. Ru.

すなわち、被処理物1の長さが陰極室8の長さより長く
、かつ、陰極室8の前部に陽極室7を有し、後部に陽極
室9を有するので、被処理物1の移行中に、被処理物1
の全長が陰極室8内に納まることなく、必ず、被処理物
1の前部か後部かのいずれかまたはその両方が陽極室7
または9にまたがっているため、被処理物の全長にわた
って表面処理が可能であり、したがって、被処理物1の
長さ方向には表面処理のされていない部分が全くなくな
る。
That is, since the length of the object to be processed 1 is longer than the length of the cathode chamber 8, and the anode chamber 7 is provided at the front of the cathode chamber 8, and the anode chamber 9 is provided at the rear thereof, the object to be processed 1 is moved. , the object to be treated 1
The entire length of the workpiece 1 does not fit in the cathode chamber 8, and either the front or rear part of the object 1, or both, is always in the anode chamber 7.
or 9, surface treatment can be performed over the entire length of the object to be treated, and therefore there is no unsurfaced portion in the length direction of the object to be treated 1.

なお貫通部14と15から溢流する処理液は、溢流槽1
6と11に回収され、処理液循環ポンプ18によって陽
極酸化処理槽4のそれぞれの室γおよび8ならび9に戻
される。
The processing liquid overflowing from the penetration parts 14 and 15 is stored in the overflow tank 1.
6 and 11, and returned to the respective chambers γ, 8, and 9 of the anodizing treatment tank 4 by the treatment liquid circulation pump 18.

第4図は本発明の第2実施例を示したもので、前述の第
1実施例と大差はないが、この第2実施例では、陰極室
8′と陽極室グが付加されており、かつ、上部の給電材
10,11.’f2・・・・・・・・・のほかに、それ
ぞれに対応する給電材10′(プラス側)、11′(マ
イナス側)、121(プラス側)、・・・・・・・・・
が設げられている。
FIG. 4 shows a second embodiment of the present invention, which is not much different from the first embodiment described above, but in this second embodiment, a cathode chamber 8' and an anode chamber 8' are added. And the upper power supply materials 10, 11. In addition to 'f2......, the corresponding power supply materials 10' (plus side), 11' (minus side), 121 (plus side),...
is provided.

したがって、前記第1実施例に比較して、より陽極酸化
皮膜は均一となり、また被処理物の両面を同時に処理で
きる。
Therefore, compared to the first embodiment, the anodic oxide film is more uniform, and both sides of the object to be treated can be treated at the same time.

第5図は本発明の第3実施例を示したもので、ちょうど
前記第1実施例において、溢流槽16と11および搬送
装置2はそのままの位置で、陽極酸化処理槽4の上下関
係を逆にして、上半分を取去ったようなものに相当する
FIG. 5 shows a third embodiment of the present invention, in which the overflow tanks 16 and 11 and the conveying device 2 are in the same position as in the first embodiment, and the vertical relationship of the anodizing tank 4 is changed. It is equivalent to having the upper half removed.

すなわち、この第3実施例では、被処理物1はその下面
が主として表面処理されることになる。
That is, in this third embodiment, the lower surface of the object 1 to be treated is mainly subjected to surface treatment.

したがって本発明は、長さが比較的短く、曲げられない
アルミニウムまたはその合金からなる被処理物の移行方
向に対し、陽極酸化処理槽を、陽極室と陰極室が交互に
配列するよう、陽極室と陰極室とに分割し、かつ、すく
なくとも、2つの陽極室と1つの陰極室からなる構造と
し、これら陽極室と陰極室を連続して被処理物が通過し
て陽極酸化処理を行なうものであるから、被処理物に対
するラッキングが不用で、しかも被処理物の長さが陰極
室の長さより長く、がっ、陽極室と陰極室とが交互に配
置されていて、陽極室が陰極室よりも数の点で多くなっ
ているので、前記実施例でも述べたとおり、被処理物の
移行中に、被処理物の全長が陰極室内たけにあることな
く、必ず、被処理物の前部か後部かのいずれがまたはそ
の両方が陽極室にまたがっているため、被処理物の全長
にわたって陽極酸化処理が可能であり、表面に均一な陽
極酸化皮膜が得られるうえ、間接給電が可能なため、電
流制限を受けることがなく、かつ、設備の小型化をはか
れるなど、その奏する効果が犬である。
Therefore, in the present invention, the anodizing treatment tank is arranged such that the anode chamber and the cathode chamber are arranged alternately in the direction of movement of the object to be treated, which is relatively short and unbendable and made of aluminum or its alloy. and a cathode chamber, and has a structure consisting of at least two anode chambers and one cathode chamber, and the object to be treated passes through these anode chambers and cathode chambers in succession to carry out anodizing treatment. Because of this, there is no need for racking for the object to be processed, and the length of the object to be processed is longer than the length of the cathode chamber. As mentioned in the previous example, the entire length of the object is not inside the cathode chamber, and the front part of the object is always moved. Because one or both of the rear parts straddle the anode chamber, it is possible to anodize the entire length of the object to be treated, and a uniform anodic oxide film can be obtained on the surface. In addition, indirect power supply is possible. The benefits of this technology include not being subject to current limitations and allowing equipment to be made smaller.

なお陽極酸化処理後の処理液を回収する溢流槽と、この
溢流槽から陽極酸化処理槽へ処理液を戻すための戻し管
ならびに循環ポンプを備えたものは、処理液をすべて循
環させることができ、処理液の無1駄がない。
In addition, if the equipment is equipped with an overflow tank to collect the treatment liquid after anodizing treatment, a return pipe and a circulation pump to return the treatment liquid from the overflow tank to the anodization treatment tank, all the treatment liquid must be circulated. There is no waste of processing liquid.

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

第1図は本発明の第1実施例の縦断側面図、第2図は第
1図の切断線■−■に?i5横断平面図、第3図は第1
図の矢視線■−■からみた正面図、第4図は本発明の第
2実施例の縦断側面図、第5図は本発明の第3実施例の
縦断側面図である。 1・・・・・・被処理物、2・・・・・・搬送装置、3
・・・・・・移行方向の矢印、4・・・・・・陽極酸化
処理槽、5,6・・・・・・仕切壁、1・・・・・・陽
極室、8,8′・・・・・・陰極室、9゜91・・・・
・・陽極室、10,10’、11,11’、12゜12
1・・・・・・給電材、13・・・・・・給電装置、1
4,15・・・・・・貫通部、16,17・・・・・・
溢流槽、18・・・・・・処理循環ポンプ、19・・・
・・・処理液戻し管。
Fig. 1 is a longitudinal cross-sectional side view of the first embodiment of the present invention, and Fig. 2 is along the cutting line ■-■ in Fig. 1? i5 cross-sectional plan view, Figure 3 is the 1st
FIG. 4 is a longitudinal sectional side view of the second embodiment of the present invention, and FIG. 5 is a longitudinal sectional side view of the third embodiment of the present invention. 1... Workpiece, 2... Conveyance device, 3
...Arrow in the direction of transition, 4...Anodizing treatment tank, 5,6...Partition wall, 1...Anode chamber, 8,8'. ...Cathode chamber, 9゜91...
...Anode chamber, 10, 10', 11, 11', 12゜12
1...Power supply material, 13...Power supply device, 1
4, 15... Penetration part, 16, 17...
Overflow tank, 18... Processing circulation pump, 19...
...Processing liquid return pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 長さが比較的短く、曲げられないアルミニウムまた
はその合金からなる被処理物の移行方向に対し、陽極室
と陰極室とが交互に配置1ルでいるように陽極室と陰極
室とに分割された陽極酸化処理槽を備え、かつ、それら
の配列が、すくなくとも、2つの陽極室と1つの陰極室
からなり、しかも、前記陽極室および陰極室を連続して
陽極酸化を行ない得るように、該被処理物を該被処理物
の前記移行方向に移送する搬送装置および給電装置を備
え、さらに、前記移行方向に対する該陽極室および陰極
室の幅が前記移行方向に対する被処理物の幅より大きい
とともに、前記移行方向に対する該被処理物の長さが前
記移行方向に対する該陰極室の長さより長いことを特徴
とする、連続陽極酸化処理装置。
1 Divided into an anode chamber and a cathode chamber so that the anode chamber and cathode chamber are arranged alternately in the direction of movement of the workpiece made of aluminum or its alloy, which is relatively short and unbendable. anodizing treatment tank, and the arrangement thereof consists of at least two anode chambers and one cathode chamber, and furthermore, the anode chamber and the cathode chamber can be continuously anodized, A transport device and a power supply device are provided for transporting the object to be processed in the direction of movement of the object to be processed, and further, the width of the anode chamber and the cathode chamber in the direction of movement is larger than the width of the object to be processed in the direction of movement. Also, a continuous anodizing treatment apparatus, characterized in that the length of the object to be treated in the transition direction is longer than the length of the cathode chamber in the transition direction.
JP13473975A 1975-11-11 1975-11-11 Renzokuyoukiyokusankashiyorisouchi Expired JPS5844158B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13473975A JPS5844158B2 (en) 1975-11-11 1975-11-11 Renzokuyoukiyokusankashiyorisouchi

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13473975A JPS5844158B2 (en) 1975-11-11 1975-11-11 Renzokuyoukiyokusankashiyorisouchi

Publications (2)

Publication Number Publication Date
JPS5259036A JPS5259036A (en) 1977-05-16
JPS5844158B2 true JPS5844158B2 (en) 1983-10-01

Family

ID=15135444

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13473975A Expired JPS5844158B2 (en) 1975-11-11 1975-11-11 Renzokuyoukiyokusankashiyorisouchi

Country Status (1)

Country Link
JP (1) JPS5844158B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0387563U (en) * 1989-12-18 1991-09-05

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0387563U (en) * 1989-12-18 1991-09-05

Also Published As

Publication number Publication date
JPS5259036A (en) 1977-05-16

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