JPS6225756B2 - - Google Patents

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Publication number
JPS6225756B2
JPS6225756B2 JP4072380A JP4072380A JPS6225756B2 JP S6225756 B2 JPS6225756 B2 JP S6225756B2 JP 4072380 A JP4072380 A JP 4072380A JP 4072380 A JP4072380 A JP 4072380A JP S6225756 B2 JPS6225756 B2 JP S6225756B2
Authority
JP
Japan
Prior art keywords
anode
catholyte
cathode
etching
electrolytic regeneration
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
JP4072380A
Other languages
Japanese (ja)
Other versions
JPS56136827A (en
Inventor
Morinobu Kondo
Hiromitsu Hotsuta
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.)
Chuo Seisakusho KK
Original Assignee
Chuo Seisakusho 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 Chuo Seisakusho KK filed Critical Chuo Seisakusho KK
Priority to JP4072380A priority Critical patent/JPS56136827A/en
Publication of JPS56136827A publication Critical patent/JPS56136827A/en
Publication of JPS6225756B2 publication Critical patent/JPS6225756B2/ja
Granted legal-status Critical Current

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  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Electroplating Methods And Accessories (AREA)
  • ing And Chemical Polishing (AREA)

Description

【発明の詳細な説明】 <産業上の利用分野> 本発明はプラステイツク材に電気鍍金を施すに
あたつての前処理として、該プラステイツク材の
表面を粗面化するいわゆるエツチング工程の浴液
を常時電解再生する装置の改良に関する。
[Detailed Description of the Invention] <Industrial Application Field> The present invention uses a bath solution for a so-called etching process to roughen the surface of plastic materials as a pretreatment for electroplating plastic materials. This invention relates to improvement of a device for constant electrolytic regeneration.

<従来技術> プラステイツク材に電気鍍金を行なうには、鍍
金工程に先立つて、クロム酸と硫酸の混液で成る
エツチング浴に浸漬して、プラステイツク材の表
面を粗面化し、しかるのちに電析される電気鍍金
層とプラステイツク材との密着性の向上を図るの
が常法となつている。此のエツチング工程はクロ
ム酸の酸化作用によつて、プラステイツク材表面
を部分的に酸化溶解させるものであるから、クロ
ム酸が酸化作用を営めば、クロム酸自体は還元さ
れ、六価クロム状態から三価クロム状態に変化
し、エツチング浴としての酸化作用が弱められ、
ついにはエツチング作用を継続することが不可能
となる。そこで該エツチング浴液を電解再生槽に
循環し、常時直流電解を行つて三価クロムを六価
クロムに再酸化して、エツチング浴液中の六価ク
ロム濃度を一定に保ち、エツチング作用を長期間
に渡つて維持する装置が実用化されている。
<Prior art> In order to perform electroplating on plastic materials, prior to the plating process, the surface of the plastic material is roughened by immersing it in an etching bath consisting of a mixture of chromic acid and sulfuric acid, and then the surface of the plastic material is roughened. It is a common practice to improve the adhesion between the electroplated layer and the plastic material. This etching process partially oxidizes and dissolves the surface of the plastic material through the oxidizing action of chromic acid, so when the chromic acid performs its oxidizing action, the chromic acid itself is reduced, changing from the hexavalent chromium state. It changes to trivalent chromium state, weakening its oxidizing effect as an etching bath,
Eventually it becomes impossible to continue the etching action. Therefore, the etching bath solution is circulated to an electrolytic regeneration tank, and constant DC electrolysis is performed to reoxidize trivalent chromium to hexavalent chromium, keeping the concentration of hexavalent chromium in the etching bath constant and prolonging the etching action. Devices that maintain this over a period of time have been put into practical use.

ここで第1図は、前記エツチング浴液の電解再
生装置の一例であつて、1はクロム酸と硫酸を主
成分とするエツチング液2を収容するエツチング
槽を示し、該エツチング液2にはエツチング処理
を受けるプラステイツク材3が浸漬される。また
前記エツチング槽1には、エツチング液2を電解
再生槽5へ送液するポンプ4が接続され、さらに
該電解再生槽5で再生されたエツチング液2をエ
ツチング槽1へ返送する返送パイプ6が接続され
ている。
Here, FIG. 1 shows an example of the electrolytic regeneration device for the etching bath solution, in which 1 indicates an etching bath containing an etching solution 2 whose main components are chromic acid and sulfuric acid. The plastic material 3 to be treated is immersed. Further, a pump 4 is connected to the etching tank 1 to send the etching solution 2 to the electrolytic regeneration tank 5, and a return pipe 6 is connected to return the etching solution 2 regenerated in the electrolytic regeneration tank 5 to the etching tank 1. It is connected.

電解再生槽5は素焼等の隔膜7で陽極室8と陰
極室9とに仕切られた槽10と、前記陽極室8に
浸漬された鉛若くは鉛合金の陽極11と、陰極室
9に浸漬された陰極12とで構成され、前記送液
ポンプ4から送られたエツチング液2は陽極室8
に導かれ、再び返送パイプ6を経てエツチング槽
1へ返送される。また13は整流器であつてその
正極出力端子14は前記陽極11に、負極出力端
子15は陰極12に接続されている。
The electrolytic regeneration tank 5 includes a tank 10 partitioned into an anode chamber 8 and a cathode chamber 9 by a bisque diaphragm 7, an anode 11 of lead or lead alloy immersed in the anode chamber 8, and an anode 11 of lead or lead alloy immersed in the cathode chamber 9. The etching liquid 2 sent from the liquid pump 4 is sent to the anode chamber 8.
and is returned to the etching bath 1 via the return pipe 6. Reference numeral 13 denotes a rectifier, the positive output terminal 14 of which is connected to the anode 11 and the negative output terminal 15 connected to the cathode 12.

第1図の電解再生装置において、エツチング液
2中に含まれている三価クロムイオンは、陽極室
8内で陽極酸化されて再び六価クロムイオンに変
換される。また同時にエツチング工程で、被処理
プラステイツク材3が部分溶解して、エツチング
液2中に存在している溶解生成物も、陽極11に
より酸化されてガス状となり、液面から放散され
る。このため、エツチング液2は絶えず再生され
る事になり、長期間に亘つてエツチング機能が維
持される。
In the electrolytic regeneration apparatus shown in FIG. 1, trivalent chromium ions contained in the etching solution 2 are anodized in the anode chamber 8 and converted back into hexavalent chromium ions. At the same time, during the etching process, the plastic material 3 to be treated is partially dissolved, and the dissolved products present in the etching solution 2 are also oxidized by the anode 11, becoming gaseous, and dissipated from the surface of the solution. Therefore, the etching liquid 2 is constantly regenerated, and the etching function is maintained for a long period of time.

また、陰極室9には隔膜7を通じて直流電流を
通電させるために陰極液16が収容されるが、陰
極液16中のイオンが、隔膜7を通じて陽極室8
へ移動し、エツチング液2の組成に変化を与え
て、そのエツチング機能を阻害してはならないの
で、陰極液16としてはエツチング液2の成分で
あるクロム酸若くは硫酸又は両者の混合液が用い
られる。
Further, the catholyte chamber 9 accommodates a catholyte 16 in order to pass a direct current through the diaphragm 7, but the ions in the catholyte 16 pass through the diaphragm 7 to the anode chamber 8.
Chromic acid, sulfuric acid, or a mixture of the two, which are components of the etching solution 2, is used as the catholyte 16 because the composition of the etching solution 2 must not be changed and its etching function should not be inhibited. It will be done.

<発明が解決しようとする問題点> ところで電解再生運転に際しては、陽極室液で
あるエツチング槽1の溶液中の三価クロムイオン
の中の若干は、隔膜7を通じて陰極室9中に流入
し、さらに陰極液16中の陰イオン即ちクロム酸
イオン若くは硫酸イオンは隔膜7を通じて陽極室
8へ移動するので、運転時間の経過と共に陰極液
16の水素イオン濃度は低下し、(PH値が上昇
し、)遂には三価クロムイオンがイオン状態で存
在する事ができなくなり、水酸化クロムとして沈
澱するに至る。又、陰イオンも前記の如く陽極室
8へ移動する結果、陰極液16中のイオンが少な
くなり、その電導度が低下し電解電流を通電する
事が不可能となる。このため、適時に陰極液16
を更新する必要がある。
<Problems to be Solved by the Invention> By the way, during electrolytic regeneration operation, some of the trivalent chromium ions in the solution in the etching tank 1, which is the anode chamber solution, flow into the cathode chamber 9 through the diaphragm 7. Furthermore, anions, ie, chromate ions or sulfate ions, in the catholyte 16 move to the anode chamber 8 through the diaphragm 7, so as the operating time passes, the hydrogen ion concentration in the catholyte 16 decreases (the PH value increases). ) Eventually, trivalent chromium ions can no longer exist in an ionic state and precipitate as chromium hydroxide. Further, as the anions also move to the anode chamber 8 as described above, the number of ions in the catholyte 16 decreases, and its conductivity decreases, making it impossible to pass an electrolytic current. For this reason, the catholyte 16
needs to be updated.

かかる陰極液16の更新に際して、従来は経験
的に被処理プラステイツク材3のエツチング総
量、乃至は電解再生装置の電解時間の積算値が一
定値となると、該陰極液16を廃棄し、新液と交
換していた。然し乍ら廃棄される陰極液16とい
えども未だ使用に耐える場合があり不経済であつ
た。
When renewing the catholyte 16, conventionally, when the total etching amount of the plastic material 3 to be treated or the integrated value of the electrolysis time of the electrolytic regeneration device reaches a certain value, the catholyte 16 is discarded and replaced with a new solution. They were exchanging. However, even the catholyte 16 that is discarded may still be usable, which is uneconomical.

そこで、本発明者は、かかる陰極液の交換時期
を知得する手段として、電導度計により直接、液
の電導度を測定したり、PH計により陰極液のPHを
測定する方法を考えた。ところが、前者の方法は
電解電流により測定誤差を生ずるのを避けるため
に、電導度測定時には電解電流を中断させる必要
があり、電流制御が面倒となる。後者の方法はPH
の変化範囲が狭く、正確な検出が困難である。ま
たいずれも、陰極液中に測定器具を浸漬する必要
があつて、該器具の周囲に水酸化クロム等が付着
して、検出誤差を生じ易い。さらにまた、その演
算制御も複雑となる等の欠点があつた。
Therefore, as a means of knowing when to replace the catholyte, the present inventors devised a method of directly measuring the conductivity of the liquid using a conductivity meter or measuring the pH of the catholyte using a PH meter. However, in the former method, in order to avoid measurement errors caused by the electrolytic current, it is necessary to interrupt the electrolytic current when measuring conductivity, making current control troublesome. The latter method is PH
The range of change is narrow, making accurate detection difficult. Furthermore, in either case, it is necessary to immerse the measuring instrument in the catholyte, and chromium hydroxide or the like adheres to the periphery of the instrument, which tends to cause detection errors. Furthermore, there were other drawbacks such as the calculation and control being complicated.

本発明は、前記欠点を生ずることなく陰極液1
6の交換時期を検知することができ、該液を使用
可能限度迄有効に使用し得る電解再生装置の提供
を目的とするものである。
The present invention provides a solution to the catholyte 1 without causing the above-mentioned drawbacks.
The object of the present invention is to provide an electrolytic regeneration device that can detect when it is time to replace the liquid and can effectively use the liquid up to its usable limit.

<問題点を解決するための手段> 本発明は、電解再生槽5の陽極11と陰極12
との極間電圧を検出する電圧検出器と、 前記電圧検出器の検出値と、電流値との比を算
出し、その算出値が所定抵抗値以上となると出力
を発生する演算装置と、 前記演算装置の出力に起因して警報する警報器
とを設けたことを特徴とするものである。
<Means for solving the problems> The present invention provides an anode 11 and a cathode 12 of an electrolytic regeneration tank 5.
a voltage detector that detects a voltage between electrodes; an arithmetic device that calculates a ratio between a detected value of the voltage detector and a current value, and generates an output when the calculated value becomes a predetermined resistance value or more; The present invention is characterized by being provided with an alarm that issues an alarm based on the output of the arithmetic device.

<作用> 陰極液16の電導度が低下すると、電解再生槽
5の陽極11と陰極12間の電気抵抗が大とな
る。そこで、前記抵抗を測定するために、陽極1
1と陰極12との極間電圧を電圧検出器で検出
し、さらにその検出値と電流値から抵抗を算出
し、その抵抗値を陰極液を交換するに適当な所定
抵抗値と比較して、該算出値が前記所定抵抗値よ
りも大のときに警報器を駆動する。これにより、
最適な陰極液の交換時期を知得することができ
る。
<Function> When the conductivity of the catholyte 16 decreases, the electrical resistance between the anode 11 and the cathode 12 of the electrolytic regeneration tank 5 increases. Therefore, in order to measure the resistance, the anode 1
1 and the cathode 12 with a voltage detector, further calculate the resistance from the detected value and the current value, and compare the resistance value with a predetermined resistance value suitable for replacing the catholyte, An alarm is activated when the calculated value is greater than the predetermined resistance value. This results in
You can know the optimal time to replace the catholyte.

<実施例> 第2図は本発明の実施例を示し、第1図の装置
と共通する部分には同一符号を付してある。
<Embodiment> FIG. 2 shows an embodiment of the present invention, in which parts common to the apparatus in FIG. 1 are given the same reference numerals.

ここで17は整流器13の直流出力側に設けら
れた分流器等の直流電流検出器を示し、また18
は電解再生槽の陽極11と陰極12との間の電圧
即ち極間電圧を検出する電圧検出器を示す。前記
電流検出器17と、電圧検出器18の出力側に
は、演算装置19が接続されている。前記演算装
置19は前記電圧検出器18の検出値と電流検出
器17の検出値との比、即ち電解再生槽の電気抵
抗を算出し、その算出値をあらかじめ設定した所
定抵抗値と比較し、該所定抵抗値以上となると継
電器20に出力を発生する機能を有する。前記出
力により継電器20の駆動を生じ、継電器20の
接点を介して図示されない電源に接続されたベ
ル、ブザー等の警報器21に鳴音を生ずる。
Here, 17 indicates a DC current detector such as a shunt provided on the DC output side of the rectifier 13, and 18
1 shows a voltage detector that detects the voltage between the anode 11 and the cathode 12 of the electrolytic regeneration tank, that is, the voltage between the electrodes. An arithmetic unit 19 is connected to the output sides of the current detector 17 and voltage detector 18. The arithmetic device 19 calculates the ratio of the detected value of the voltage detector 18 and the detected value of the current detector 17, that is, the electrical resistance of the electrolytic regeneration tank, and compares the calculated value with a predetermined resistance value set in advance, It has a function of generating an output to the relay 20 when the resistance value exceeds the predetermined resistance value. The output causes the relay 20 to be driven, causing an alarm 21 such as a bell or buzzer connected to a power source (not shown) to ring through the contacts of the relay 20.

演算装置19の設定値を適当に選べば電解再生
槽5の電気抵抗が所定抵抗値以下においては警報
器21は作動せず、所定抵抗値以上となると該警
報器21が作動する様にする事は容易に可能であ
る。電解再生槽の電気抵抗は陽極液の電導度と陰
極液16の電導度の両者に依存する事は当然であ
るが、陽極液はエツチング槽1の浴液自体であつ
て、本来一定の組成に保たれるべきであり、かつ
高濃度の電解液であるので、電導度も十分高く一
定しているから、前記電気抵抗は陰極液16の電
導度にのみ依存するとみなすことができる。従つ
て陰極液16の電気抵抗を監視する事によつて該
陰極液16の使用限界を知る事ができることとな
る。
If the set value of the calculation device 19 is appropriately selected, the alarm 21 will not operate when the electrical resistance of the electrolytic regeneration tank 5 is below a predetermined resistance value, and will operate when the electrical resistance exceeds the predetermined resistance value. is easily possible. It goes without saying that the electrical resistance of the electrolytic regeneration tank depends on both the conductivity of the anolyte and the conductivity of the catholyte 16, but the anolyte is the bath solution itself in the etching tank 1, and originally has a constant composition. Since it is a highly concentrated electrolyte, the electrical conductivity is also sufficiently high and constant, so it can be considered that the electrical resistance depends only on the electrical conductivity of the catholyte 16. Therefore, by monitoring the electrical resistance of the catholyte 16, the usage limit of the catholyte 16 can be known.

電解再生槽の電気抵抗を測定するために、必ず
しも前記の電流検出器17を用いる必要はなく、
例えば整流器13として定電流調整型の整流器を
用いて、電流を一定とするようにしてもよい。こ
の場合には、電圧と抵抗とは比例関係となるか
ら、陽極11、陰極12間の電圧を測定するだけ
で電解再生槽の電気抵抗が得られることとなる。
In order to measure the electrical resistance of the electrolytic regeneration tank, it is not always necessary to use the current detector 17,
For example, a constant current adjustment type rectifier may be used as the rectifier 13 to keep the current constant. In this case, since voltage and resistance are in a proportional relationship, the electrical resistance of the electrolytic regeneration tank can be obtained simply by measuring the voltage between the anode 11 and the cathode 12.

<発明の効果> 本発明は、上述のように、陰極液の抵抗値を自
動的に常時測定して、該抵抗値が、陰極液を交換
すべき所定抵抗値以上となると、警報を発生する
ようにしたから、陰極液に測定装置を浸漬する必
要はなく、該測定装置に水酸化クロム等が付着し
て測定誤差を生ぜず、安定した検出が可能とな
る。また単純な演算によつて制御できるから、制
御手段も簡易となる。従つて簡易な構成により、
陰極液に最適な交換タイミングを知得でき、無駄
のない交換が可能となる等の優れた効果がある。
<Effects of the Invention> As described above, the present invention automatically and constantly measures the resistance value of the catholyte, and when the resistance value exceeds a predetermined resistance value at which the catholyte should be replaced, an alarm is generated. Because of this, there is no need to immerse the measuring device in the catholyte, and stable detection is possible without chromium hydroxide or the like adhering to the measuring device and causing measurement errors. Furthermore, since the control can be performed by simple calculations, the control means can also be simplified. Therefore, with a simple configuration,
This has excellent effects such as knowing the optimal timing for replacing the catholyte and making it possible to replace the catholyte without waste.

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

第1図は従来より実用されている電解再生装置
の系統図、第2図は本発明の電解再生装置の系統
図である。 1;エツチング槽、3;プラステイツク材、
4;送液ポンプ、5;電解再生槽、6;返送パイ
プ、7;隔膜、8;陽極室、9;陰極室、11;
陽極、12;陰極、13;整流器、16;陰極
液、17;分流器、18;電圧検出器、19;演
算装置、20;継電器、21;警報器。
FIG. 1 is a system diagram of a conventional electrolytic regeneration device, and FIG. 2 is a system diagram of an electrolytic regeneration device of the present invention. 1; Etching tank, 3; Plastic material,
4; Liquid pump, 5; Electrolytic regeneration tank, 6; Return pipe, 7; Diaphragm, 8; Anode chamber, 9; Cathode chamber, 11;
Anode, 12; cathode, 13; rectifier, 16; catholyte, 17; shunt, 18; voltage detector, 19; arithmetic device, 20; relay, 21; alarm.

Claims (1)

【特許請求の範囲】 1 クロム酸と硫酸の混合液からなるプラステイ
ツク材のエツチング浴液を循環する陽極室と、隔
膜で仕切られ、硫酸若くはクロム酸又は両者の混
合液を収容する陰極室とを有する電解再生槽と、 前記陽極室内に浸漬された陽極と、陰極室内に
浸漬された陰極とに直流電流を供給する整流器 とを備えたものにおいて、 電解再生槽の陽極と陰極との極間電圧を検出す
る電圧検出器と、 前記電圧検出器の検出値と、電流値との比を算
出し、その算出値が所定抵抗値以上となると出力
を発生する演算装置と、 前記演算装置の出力に起因して警報する警報器
とを設けたことを特徴とするプラステイツク材の
エツチング浴液の電解再生装置。
[Claims] 1. An anode chamber in which a plastic material etching bath solution consisting of a mixture of chromic acid and sulfuric acid is circulated, and a cathode chamber separated by a diaphragm and containing sulfuric acid, chromic acid, or a mixture of both. and a rectifier for supplying direct current to the anode immersed in the anode chamber and the cathode immersed in the cathode chamber, wherein: between the anode and the cathode of the electrolytic regeneration tank a voltage detector that detects voltage; an arithmetic device that calculates a ratio between a detected value of the voltage detector and a current value and generates an output when the calculated value becomes a predetermined resistance value or more; and an output of the arithmetic device. 1. An electrolytic regeneration device for an etching bath solution for plastic materials, characterized in that it is equipped with an alarm device that gives an alarm due to the above.
JP4072380A 1980-03-29 1980-03-29 Regeneration device by electrolysis for etching bath solution for plastic material Granted JPS56136827A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4072380A JPS56136827A (en) 1980-03-29 1980-03-29 Regeneration device by electrolysis for etching bath solution for plastic material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4072380A JPS56136827A (en) 1980-03-29 1980-03-29 Regeneration device by electrolysis for etching bath solution for plastic material

Publications (2)

Publication Number Publication Date
JPS56136827A JPS56136827A (en) 1981-10-26
JPS6225756B2 true JPS6225756B2 (en) 1987-06-04

Family

ID=12588516

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4072380A Granted JPS56136827A (en) 1980-03-29 1980-03-29 Regeneration device by electrolysis for etching bath solution for plastic material

Country Status (1)

Country Link
JP (1) JPS56136827A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60236977A (en) * 1984-05-09 1985-11-25 Kitajima Jidosha Kk Wind-up device for wire such as aerial wire
CN102383159A (en) * 2011-08-09 2012-03-21 长春一汽富维高新汽车饰件有限公司 Coarsening production and trivalent chromium electrolysis process incorporating device and method

Also Published As

Publication number Publication date
JPS56136827A (en) 1981-10-26

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