JPH034639B2 - - Google Patents

Info

Publication number
JPH034639B2
JPH034639B2 JP21727986A JP21727986A JPH034639B2 JP H034639 B2 JPH034639 B2 JP H034639B2 JP 21727986 A JP21727986 A JP 21727986A JP 21727986 A JP21727986 A JP 21727986A JP H034639 B2 JPH034639 B2 JP H034639B2
Authority
JP
Japan
Prior art keywords
current
current density
electrolytic
signal
electrolytic 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
JP21727986A
Other languages
Japanese (ja)
Other versions
JPS6372898A (en
Inventor
Takeo Oki
Aizaburo Yagishita
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP21727986A priority Critical patent/JPS6372898A/en
Publication of JPS6372898A publication Critical patent/JPS6372898A/en
Publication of JPH034639B2 publication Critical patent/JPH034639B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Control Of Voltage And Current In General (AREA)

Description

【発明の詳細な説明】 〔発明の目的〕 産業上の利用分野 本発明は、物品等の表面に電気メツキ等の電解
処理を施す方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] Industrial Application Field The present invention relates to a method of subjecting the surface of an article to electrolytic treatment such as electroplating.

従来の技術 物品等の表面に対して電気メツキや電解研磨等
の電解処理を行なうに当つて被処理面の電流密度
を適切な範囲内に調整することは、良好な電解処
理面を得るために欠くことができない。このよう
な電解処理において電流密度を知るために、被処
理面の面積と通電全電流値とから算出する方法が
あるが、被処理面の形状が一様でないときにはそ
の凸部や端部などに電流が集中し、また凹部や裏
面などには少ししか電流が廻らないという問題が
あり、前記のような平均電流密度を知るのみでは
良好な電解処理面は得られない。
Prior Art When performing electrolytic treatment such as electroplating or electropolishing on the surface of an article, it is necessary to adjust the current density of the surface to be treated within an appropriate range in order to obtain a good electrolytically treated surface. Indispensable. In order to know the current density in such electrolytic treatment, there is a method of calculating it from the area of the surface to be treated and the total current value. There is a problem in that the current is concentrated and only a small amount of current flows to the recesses or the back surface, so it is not possible to obtain a good electrolytically treated surface just by knowing the average current density as described above.

そこで、電解処理を行なうに当つて、被処理導
電体と電解浴との接触面におけるそれぞれ異つた
場所での局所的電流密度を知ることが重要となる
が、このような接液面の局所的電流密度を知る手
段としては、実験室的に測定する方法はあつたと
しても、工業的に操作現場で利用し得る測定方法
は未だに無いのが現実であつた。
Therefore, when performing electrolytic treatment, it is important to know the local current density at different locations on the contact surface between the conductor to be treated and the electrolytic bath. As a means of determining current density, even if there was a method to measure it in a laboratory, the reality is that there is still no measurement method that can be used in industrial operations.

これに対して、本発明者の1人は、対になつた
互に絶縁された導電体電極を所定距離を隔てて対
向配置したバイポーラ電極型センサーを電流密度
測定対象導電体の接液面に近接させて電解液中に
位置させ、電解液中を流れる電流によつて液中に
発生する液中電流密度に比例した電位傾度を前記
センサーの電極間の電位差として検出し、この電
位差信号をあらかじめ同じ電解液について測定し
た得た電位差−電流密度の関数に代入することに
よつて測定対象導電体の接液面付近の液中電流密
度を求め、これによつて該接液面の特定個所を通
過する電流の密度を近似的に測定する手段が、工
業的に実用可能であることを見出した。そして、
この原理に基づく電流密度測定装置を発明し、別
途特許出願している(特開昭62−27655号)。
In contrast, one of the inventors of the present invention proposed a bipolar electrode type sensor, in which a pair of mutually insulated conductor electrodes are arranged facing each other at a predetermined distance, on the liquid contact surface of the conductor to be measured for current density. The sensors are placed close to each other in an electrolytic solution, and a potential gradient proportional to the current density in the solution generated by the current flowing through the electrolytic solution is detected as a potential difference between the electrodes of the sensor, and this potential difference signal is detected in advance. By substituting the obtained potential difference-current density function measured for the same electrolytic solution, the current density in the liquid near the liquid contact surface of the conductor to be measured is determined, and from this, a specific point on the liquid contact surface can be determined. It has been found that a means for approximately measuring the density of passing current is industrially practical. and,
He invented a current density measuring device based on this principle and has filed a separate patent application (Japanese Patent Application Laid-open No. 27655/1983).

しかしながら、このような手段によつて接液面
における電流密度を知り得ても、電解処理対象物
品に対して最適の通電をするためには、電解技術
者の判断に基づいて通電電流の制御を行なつた上
電解処理時間を調整整することが必要とされてい
た。
However, even if the current density at the surface in contact with the liquid can be determined by such means, the current must be controlled based on the judgment of the electrolytic engineer in order to optimally apply the current to the object to be electrolytically treated. It was necessary to adjust the electrolytic treatment time carried out.

解決しようとする問題点 前述のように、従来技術による物品の電解処理
法にあつては、電流密度の正確な測定手段が知ら
れて居らずまた平均電流密度の推定精度も充分で
なかつたので、電解処理の完全を期すためにはど
うしても余裕をみて通電電流量が過大となるよう
な操業条件を設定しなければならなかつた。
Problems to be Solved As mentioned above, in the electrolytic treatment of articles according to the prior art, there was no known accurate means of measuring current density, and the accuracy of estimating the average current density was not sufficient. In order to ensure complete electrolytic treatment, it was necessary to set operating conditions such that the amount of current applied was excessive.

そのため、処理物品についてはたとえばメツキ
被膜が厚すぎるなどの過剰品質を与えることにな
り、また一方では原料やエネルギーの無駄と操業
効率の低迷とを招いていた。
As a result, the treated articles are given an excessive quality, for example, the plating film is too thick, and on the other hand, this results in waste of raw materials and energy and a decrease in operational efficiency.

そこで本発明は、さきに本発明者らが発明した
電流密度測定方法を利用して、処理対象物品に対
して良好かつ経済的な電解処理を実施できる信頼
性の高い電解処理法を提供しようとするものであ
る。
Therefore, the present invention aims to provide a highly reliable electrolytic treatment method that can perform good and economical electrolytic treatment on objects to be treated by using the current density measurement method previously invented by the present inventors. It is something to do.

〔発明の構成〕[Structure of the invention]

問題点を解決するための手段 かかる目的を達成できる本発明の電解処理法
は、互に絶縁された状態で所定距離を隔てて設け
られた2個の接液電極を有する電流密度測定用セ
ンサを電解処理対象物品の表面に近接させて設
け、該センサからの出力信号値を演算して電流密
度信号を発生する積分回路と、該電流密度信号を
予め入力・記憶された設定値と比較して制御信号
を発生する比較回路と、該制御信号をうけて電解
電流を制御する電流制御回路と、を少くとも備え
た制御装置を介して該電解処理対象物品に対して
電流を供給することを、特徴とするものである。
Means for Solving the Problems The electrolytic treatment method of the present invention that can achieve the above object uses a current density measuring sensor having two wetted electrodes that are insulated from each other and are spaced apart from each other by a predetermined distance. An integrating circuit is provided close to the surface of the article to be electrolytically treated, and calculates the output signal value from the sensor to generate a current density signal, and compares the current density signal with a set value input and stored in advance. supplying current to the article to be electrolytically treated through a control device comprising at least a comparison circuit that generates a control signal and a current control circuit that controls an electrolytic current in response to the control signal; This is a characteristic feature.

実施例 以下、本発明を第1図によつて更に説明する。Example The present invention will be further explained below with reference to FIG.

本発明において使用される電流密度測定用セン
サSは、たとえば絶縁性の筒状体1の先端部に、
互に絶縁された所定距離たとえば5mm程度を隔て
て2個の接液電極2を設けてなるものが用いられ
る。かかる接液電極2は、たとえば白金などの耐
食性金属か、または電解液中に含有されるイオン
と同種の金属などで構成されるのが望ましく、た
とえ溶出しても電解液を汚染しないような金属で
あることが好ましい。また、かかる接液電極に
は、検出した電圧信号を送出するための電線3が
接続され、電解処理槽Bの外部などへ導かれるよ
うに構成される。
The current density measurement sensor S used in the present invention includes, for example, a tip of an insulating cylindrical body 1;
Two electrodes 2 in contact with the liquid are provided at a predetermined distance, for example, about 5 mm, and are insulated from each other. The wetted electrode 2 is desirably made of a corrosion-resistant metal such as platinum, or a metal of the same type as the ions contained in the electrolyte, and is preferably made of a metal that will not contaminate the electrolyte even if eluted. It is preferable that Further, an electric wire 3 for transmitting a detected voltage signal is connected to the liquid contact electrode, and is configured to be guided to the outside of the electrolytic treatment tank B.

また、本発明において使用される制御装置R
は、電解電流の大きさを制御するためのもので、
所定の電解処理効果を得るのに適切な電流密度を
維持するように、電流供給を自動的に調節するも
のである。かかる制御装置Rは、電流密度測定用
センサSで検出された出力電圧信号を受けてこれ
を演算し電流密度に対応する信号を発生する積分
回路4と、一方、所定の電解処理効果を得るのに
必要な電流密度の設定値を入力されてこれを記憶
する領域5′を有し、積分回路4で発生した電流
密度信号を受けて前記の設定値と比較し、設定値
よりも小さいか又大きいかによつて電解電流を増
すか又は減ずるための制御信号を発生する比較回
路5と、前記の制御信号を受けて電解電流を増減
するように作動する電流制御回路6とを備えてい
る。
Moreover, the control device R used in the present invention
is for controlling the magnitude of electrolytic current,
The current supply is automatically adjusted to maintain the appropriate current density to achieve the desired electrolytic treatment effect. The control device R includes an integrating circuit 4 that receives an output voltage signal detected by the current density measurement sensor S, calculates the output voltage signal, and generates a signal corresponding to the current density; It has an area 5' for inputting and storing the current density setting value required for the integration circuit 4, and receives the current density signal generated by the integrating circuit 4, compares it with the setting value, and determines whether the current density signal is smaller than the setting value or not. It comprises a comparator circuit 5 which generates a control signal for increasing or decreasing the electrolytic current depending on whether it is large, and a current control circuit 6 which operates to increase or decrease the electrolytic current in response to the control signal.

本発明の電解処理法を実施するに当つては、電
解槽B中に電極Aと対向させて電解処理対象物品
Cを浸漬するが、それに先立つて処理対象物品C
と同じ形状の試料について電解処理を受けるとき
その接液面の各部のの電流密度がどのように異る
かを予め調査して、代表的な電流密度たとえば平
均の電流密度を示す位置を選定しておく。そし
て、処理対象物品Cの代表的位置にセンサーSの
接液電極2を近接させて固定し、センサーSと制
御装置Rとを接続し、また電源Eから制御装置R
の電流制御回路6を経て処理対象物品Cへ電解電
流が流れるように結線して、電解処理を行なう。
In carrying out the electrolytic treatment method of the present invention, the article C to be electrolytically treated is immersed in the electrolytic bath B facing the electrode A.
When a sample of the same shape is subjected to electrolytic treatment, it is necessary to investigate in advance how the current density differs at each part of the surface in contact with the liquid, and select a position that shows a typical current density, for example, the average current density. I'll keep it. Then, the liquid contact electrode 2 of the sensor S is fixed in close proximity to a representative position of the article C to be processed, the sensor S and the control device R are connected, and the power source E is connected to the control device R.
The electrolytic treatment is performed by connecting so that an electrolytic current flows through the current control circuit 6 to the article C to be treated.

このようにして電解電流が流れると、処理対象
物品Cの接液面の近傍では電解液中にはその通電
抵抗と電流密度とに対応した電位傾度が生ずる
が、センサーSの先端部に所定距離を隔てて設け
られた2個の接液電極2には、上述の電位傾度に
対応する電位差が検出され、これが電線3を経て
電圧信号として積分回路4に入力される。
When the electrolytic current flows in this way, a potential gradient corresponding to the current carrying resistance and current density is generated in the electrolytic solution near the liquid contact surface of the article C to be processed, but the tip of the sensor S is placed at a predetermined distance. A potential difference corresponding to the above-mentioned potential gradient is detected between the two liquid contact electrodes 2 separated from each other, and this is inputted to the integrating circuit 4 as a voltage signal via the electric wire 3.

積分回路4に入力された電圧信号は、用いられ
たセンサーSの特性定数および用いられた電解液
の特性定数を含む関数によつて電流密度に変換さ
れ、電流密度信号として出力される。この電流密
度信号は比較回路5に入力されるが、その記憶領
域5′には、所定の電解処理効果たとえばメツキ
の場合には良好な表面状態を有するメツキ被膜を
得るに必要な電流密度値が設定されていて、この
設定値と比較される。そして、電流密度信号が設
定値よりも小であるときは、電解電流を増加させ
るような制御信号が出力され、また電流密度信号
が設定値よりも大であるときは、電解電流を減少
させるような制御信号が出力される。
The voltage signal input to the integrating circuit 4 is converted into a current density by a function including the characteristic constant of the sensor S used and the characteristic constant of the electrolytic solution used, and is output as a current density signal. This current density signal is input to the comparator circuit 5, and its storage area 5' stores the current density value necessary to obtain a predetermined electrolytic treatment effect, for example, in the case of plating, a plating film with a good surface condition. is set and compared with this setting value. When the current density signal is smaller than the set value, a control signal is output to increase the electrolytic current, and when the current density signal is larger than the set value, a control signal is outputted to decrease the electrolytic current. A control signal is output.

このような制御信号が電流制御回路6に入力さ
れると、電流制御回路6は制御信号に対応して電
流を増加させまたは減少させるように作動する。
この際の制御信号の形式は、設定電流密度値を中
心とした比例信号でもよく、また増−中立−減の
三減置信号であつてもよい。そして、電流制御回
路6の形式や構造に応じて、最も効果的に電解電
流の制御ができるような信号の形式を選択採用す
るのが望ましい。
When such a control signal is input to the current control circuit 6, the current control circuit 6 operates to increase or decrease the current in response to the control signal.
The format of the control signal at this time may be a proportional signal centered on the set current density value, or may be a three-point signal of increase-neutral-decrease. According to the type and structure of the current control circuit 6, it is desirable to select and adopt a signal format that allows the most effective control of the electrolytic current.

作 用 本発明の電解処理法によれば、電解処理対象物
品の代表的位置があらかじめ設定された電流密度
で電解処理をうけるように、電流の強さが自動的
に調節される。従つて、電解処理実施中に電源電
圧の変動や、同時に並行して処理を受ける処理対
象品の数などの変化があつても、それらによる変
動は自動的に補償され、一定の電解処理効果を期
待することができる。
Function According to the electrolytic treatment method of the present invention, the strength of the current is automatically adjusted so that representative positions of the article to be electrolytically treated are subjected to the electrolytic treatment at a preset current density. Therefore, even if there are fluctuations in the power supply voltage or changes in the number of items to be processed simultaneously during electrolytic treatment, these fluctuations are automatically compensated for and a certain level of electrolytic treatment effect can be maintained. You can expect it.

〔発明の効果〕〔Effect of the invention〕

本発明の電解処理法は、電解処理対象物品の接
液面における電流密度を検出して個々の物品、さ
1には各部分の表面の電流密度が夫々定常を維持
するように自動的に補償されるから、電源電圧の
変動や同時に並行して処理を受ける物品の数の変
動などの予期しない変動があつても電流密度は変
化しない。そのため、各物品について均一な電解
処理が保証されることになる。
The electrolytic treatment method of the present invention detects the current density on the liquid-contact surface of the article to be electrolytically treated and automatically compensates so that the current density on the surface of each article and each part remains steady. Therefore, the current density does not change even if there are unexpected fluctuations such as fluctuations in the power supply voltage or fluctuations in the number of articles being processed in parallel at the same time. Therefore, uniform electrolytic treatment is guaranteed for each article.

従つて、品質のバラツキが減ると共に過剰品質
も発生せず、高効率で経済的な電解処理ができ
る。
Therefore, variations in quality are reduced and excessive quality does not occur, making it possible to perform highly efficient and economical electrolytic treatment.

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

第1図は本発明の電解処理法の構成を説明する
ためのブロツク図である。 A……電極、B……電解槽、C……電解処理対
象物品、E……電源、S……電流密度測定用セン
サ、R……制御装置、1……筒状体、2……接液
電極、3……電線、4……積分回路。5……比較
回路、6……電流制御回路。
FIG. 1 is a block diagram for explaining the structure of the electrolytic treatment method of the present invention. A...electrode, B...electrolytic cell, C...article to be electrolytically treated, E...power source, S...sensor for current density measurement, R...control device, 1...cylindrical body, 2...connection Liquid electrode, 3... electric wire, 4... integral circuit. 5... Comparison circuit, 6... Current control circuit.

Claims (1)

【特許請求の範囲】[Claims] 1 互に絶縁された状態で所定距離を隔てて設け
られた2個の接液電極を有する電流密度測定用セ
ンサを電解処理対象物品の表面に近接させて設
け、該センサからの出力信号値を演算して電流密
度信号を発生する積分回路と、該電流密度信号を
予め入力・記憶された設定値と比較して制御信号
を発生する比較回路と、該制御信号をうけて電解
電流を制御する電流制御回路と、を少くとも備え
た制御装置を介して該電解処理対象物品に対して
電流を供給すること、を特徴とする電解処理法。
1. A current density measuring sensor having two electrodes in contact with liquid that are insulated from each other and separated by a predetermined distance is provided close to the surface of the article to be electrolytically treated, and the output signal value from the sensor is An integrating circuit that calculates and generates a current density signal, a comparison circuit that compares the current density signal with a pre-input/stored setting value and generates a control signal, and controls the electrolytic current in response to the control signal. An electrolytic treatment method characterized by supplying current to the article to be electrolytically treated via a control device comprising at least a current control circuit.
JP21727986A 1986-09-17 1986-09-17 Electrolytic treatment Granted JPS6372898A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21727986A JPS6372898A (en) 1986-09-17 1986-09-17 Electrolytic treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21727986A JPS6372898A (en) 1986-09-17 1986-09-17 Electrolytic treatment

Publications (2)

Publication Number Publication Date
JPS6372898A JPS6372898A (en) 1988-04-02
JPH034639B2 true JPH034639B2 (en) 1991-01-23

Family

ID=16701646

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21727986A Granted JPS6372898A (en) 1986-09-17 1986-09-17 Electrolytic treatment

Country Status (1)

Country Link
JP (1) JPS6372898A (en)

Also Published As

Publication number Publication date
JPS6372898A (en) 1988-04-02

Similar Documents

Publication Publication Date Title
EP0140460A1 (en) ISFET-based measuring device and method for fabricating the ISFET used therein
DE69534714D1 (en) METHOD AND DEVICE FOR CONTROLLING THE SUPPLY OF WATER TREATMENT SCHEMICALS USING A VOLTAMETRIC SENSOR
KR880009386A (en) Water quality management method, conductivity measuring method and apparatus used therein
JPH075002A (en) Method and device for measuring electrolyte flow
US4129480A (en) Method and apparatus for determining the immersed surface area of one of the electrodes of an electro-chemical bath
JPH034639B2 (en)
JPH034640B2 (en)
EP0625592A1 (en) Method and device for the electrolytic recovery of silver in two film processing machines
US4935107A (en) Process for electrochemical measurement of the concentration of oxide ions in a bath based on molten halides
GB1579110A (en) Device for the determination ofthe concentration of sodium in a flowing mercury-sodium amalgam
JP2020003264A (en) Nitrous oxide concentration detector
JP2006010413A (en) Polarographic densitometer
JP2001174431A (en) Apparatus and method for measuring residual chlorine concentration in acidic liquid
SU1048989A3 (en) Unit for electric slag refining
EP0401257B1 (en) Method and system for measuring the corrosion properties of specimens
SU1585399A1 (en) Apparatus for automatic control of mean current density in electroplating bath
JPH0619089Y2 (en) Residual chlorine meter with automatic calibration function
JPS6020762B2 (en) How to adjust cathode current density in electroplating equipment
SU605872A1 (en) Apparatus for automatic measurement and control of current density in electrolytic bath
SU339596A1 (en) DEVICE FOR MONITORING AND REGULATING TEMPERATURE DENSITY
JPS6097247A (en) Continuous liquid-concentration measuring device
JPS6313486Y2 (en)
JPH0360058B2 (en)
US3481838A (en) Method of weighing
SU883197A2 (en) Method of measuring area of parts at galvanic process